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ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279 Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24 T: +353 86 853 8247 E: [email protected] Your Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247) Waterford Cork Road Industrial Park Honeywell International Technologies Ltd Ireland Honeywell International Technologies Ltd A2-1 Abrasive Extraction DELETE & COVER ME Dates of the Monitoring Campaign Version Team Leader Team Leader TE1 TE2 TE3 TE4 MM 08 922 MCERTS Level 2 Patrick O'Brien Report Approved by Stack Emissions Testing Report Commissioned by 8th December 2015 Job Reference Number CDU-0559 Installation Name & Address Report Written by Patrick O'Brien 5th January 2016 Report Date TE1 TE2 TE3 TE4 Stack Reference Irish EPA IPPC Licence: P0698-01 Signature of Report Approver Version 1 MM 08 922 MCERTS Level 2 CAT-RT (Version BJ) CDU-0559 Honeywell Int Technology A2-1 (POST) For inspection purposes only. Consent of copyright owner required for any other use. EPA Export 14-04-2016:01:16:51

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Page 1: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279

Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24T: +353 86 853 8247

E: [email protected] Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

WaterfordCork Road Industrial Park

Honeywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-1 Abrasive Extraction

DELETE & COVER ME

Dates of the Monitoring Campaign

Version

Team Leader

Team Leader

TE1 TE2 TE3 TE4MM 08 922

MCERTS Level 2

Patrick O'Brien

Report Approved by

Stack Emissions Testing Report Commissioned by

8th December 2015

Job Reference Number

CDU-0559

Installation Name & Address

Report Written by

Patrick O'Brien

5th January 2016Report Date

TE1 TE2 TE3 TE4

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Version 1

MM 08 922MCERTS Level 2

CAT-RT (Version BJ)

CDU-0559 Honeywell Int Technology A2-1 (POST)

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EPA Export 14-04-2016:01:16:51

Page 2: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

The testing performed fully meets the technical requirements in Irish EPA

Guidance Note, AG2.

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the written

approval of Exova Catalyst Ireland.

2

9

3

5

6

8

7

CONTENTS

4

7

CAT-RT (Version BJ)

Page 2 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 3: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd

to carry out stack emissions testing on the A2-1 Abrasive Extraction at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

Antimony, Lead, Total VOCs (as Carbon)

MONITORING OBJECTIVES

Executive Summary(Page 1 of 7)

Honeywell International Technologies Ltd, Unit 328

A2-1 Abrasive Extraction

8th December 2015

CAT-RT (Version BJ)

Page 3 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

For

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ectio

n pur

pose

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EPA Export 14-04-2016:01:16:51

Page 4: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

where MU = Measurement Uncertainty associated with the Result

Parameter

Antimony ¹ < <

Lead ¹ < <

Total VOCs (as Carbon) ¹ - -

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

-

-

-

0.0004

0.00046 0.000 - g/hr

Honeywell International Technologies Ltd, Unit 328

8th December 2015

+/-

Units Result

Concentration

MULimit

+/-

0.0003

0.0013

0.0012

Units

mg/m³

-

Result LimitMU

A2-1 Abrasive Extraction

0.00048mg/m³ g/hr

-

0.000

Executive Summary

Mass Emission

-

MONITORING RESULTS

- g/hr

2.9

1.07

m³/hr

0.46

1.3

2692 239

% v/v

m/s

0.1

24.0

mg/m³

263

1.24

0.22

2967

m³/hrVolumetric Flow Rate (REF)

°C

Volumetric Flow Rate (ACTUAL)

0.40

(Page 2 of 7)

CAT-RT (Version BJ)

Page 4 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 5: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Parameter

R1 < <

R1 < <

R1 - -

R1

All results are expressed at the respective reference conditions.

Date(s)

Mass Emission

Antimony

g/hrLead

08/12/2015 12:50 - 12:55Velocity & Volumetric Flow Rate

mg/m³

0.0013

14:05 - 15:0508/12/2015

mg/m³ 14:05 - 15:05

0.0012

g/hr

Honeywell International Technologies Ltd, Unit 328

Duration

Executive Summary

Sampling

Times

Units

(Page 3 of 7)

MONITORING DATE(S) & TIMES

A2-1 Abrasive Extraction

8th December 2015

Units Concentration Sampling

g/hr

60

60

mg/m³ 0.00046

mins

08/12/20150.00048

Total VOCs (as Carbon) 0.4 08/12/2015 3014:05 - 14:351.07

CAT-RT (Version BJ)

Page 5 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 6: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Standard Operating Conditions

Process Status

Honeywell International Technologies Ltd, Unit 328

Value

Continuous or Batch Process

Plume Appearance

Bag Filter

A2-1 Abrasive Extraction

8th December 2015

(Page 4 of 7)

Executive Summary

PROCESS DETAILS

Parameter

On

Continuous

Not Visible

Normal Operation

Abatement System

Abatement System Running Status

CAT-RT (Version BJ)

Page 6 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 7: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

M31

M31

17025 Analysis

0.1 % v/vGravimetricCAT-TP-05

Yes

CAT

Yes

Pitot Tube and Thermocouple

YesCAT

All

CAT-TP-06

Yes 1.2 m/s

ISO 17025 Accreditation Number: 0605

CAT

EN 12619:2013

Yes

ICP-MSCAT Yes Yes

Procedure

LOD

0.16 mg/m³CAT-TP-20

CAT YesWater Vapour

ISOParameter

0 mg/m³

Antimony

EN 16911-1 (MID)

EN 14385 CAT-TP-06 Yes

Lab

Monitoring Analysis

0 mg/m³

Procedure

Analytical

Technique

AnalyticalTechnical

CAT-TP-05 YesEN 14790

(Average)

ISO

Flame Ionisation Detection by Sick 3006 FID

A2-1 Abrasive Extraction

Standard

Lab

Yes

MCERTS

17025

Testing

EN 14385

ICP-MS

Run

SUMMARY OF SAMPLING DEVIATIONS

Parameter

Yes RPS

CAT Yes RPS

Total VOCs (as Carbon)

Testing

(Page 5 of 7)

Testing Analysis

Lead

(with short name reference as appears in the table above)

RPS Laboratories Ltd (RPS)

ANALYSIS LABORATORIES

All There are no deviations associated with the sampling employed.

Velocity & Vol. Flow Rate

Deviation

CAT-TP-41

MONITORING & ANALYTICAL METHODS

Executive Summary

Honeywell International Technologies Ltd, Unit 328

8th December 2015

CAT-RT (Version BJ)

Page 7 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 8: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

6.9

Safe Access Available

-

-

-

-

There is no requirement to perform a BS EN 15259 Homogeneity Test on this Stack.

-

--m/s

Maximum Angle of Swirl

Executive Summary

cm

Yes

General Platform Information

Units

-

On Roof

-

-

Mean Velocity

Outside

Criteria in EN 15259 -

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

0.60

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

Yes

-

-

-

m

All platforms should be designed in accordance with the requirements in the Environment Agency's Technical Guidance Note M1

and EN 15259.

Permanent / Temporary Platform

Inside / Outside

Yes

Units

1.02

°

-

--

(Page 6 of 7)

Width

Compliant

0

SUITABILITY OF SAMPLING LOCATION

Vertical

Yes

Parameter

There are no obstructions present which hamper insertion of sampling equipment

Sample Port Size

Circular

Value

> 5 Pa Yes

-

Yes

Yes

m

Lowest Gas Velocity

m/s

Yes

-

2.89

-

-

Required

-

0.28

-

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

-

Port Depth

-

Yes

Traverse 1

m/s

Easy Access Available

-

-2.91

Value

Depth

2.95Highest Gas Velocity

Area

0.00 0.00

Hole

-

Lowest Differential Pressure

Value

-

No Local Negative Flow

Platform has vertical base boards (approx. 0.25m high)

-

-

Yes

< 15°

Yes

-

-

< 3 : 1

-

5

0.00Ratio of Above : 1

-

-

0.00

-

CAT-RT (Version BJ)

Page 8 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 9: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Photo 4

PLANT PHOTOS

(Page 7 of 7)

Photo 1

SAMPLE POINTS

Executive Summary

Photo 2

Photo 3

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

Line A

Line B

A1

A2

B1

B2

CAT-RT (Version BJ)

Page 9 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 10: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDICES

APPENDIX CONTENTS

CAT-RT (Version BJ)

Page 10 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 11: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Bioaerosols Temperature Logger -

Electronic Refrigerator -

Velocity & Vol. Flow Rate

Eco Physics CLD 822Mh

MM 08 922 TE1 TE2 TE3 TE4

Heated Probe (2)

-

-

CAT 3.59

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

Extractive Sampling

LIST OF EQUIPMENT

MCERTS Accreditation

Gasmet Sampling System-

MCERTS Number

Equipment Type Equipment I.D.

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

-

-

SELECT Gas Conditioning

CAT 13.27

Equipment Type

Technical Endorsements

Team Leader Patrick O'Brien MCERTS Level 2

Technician James Magann MCERTS Level 1 MM 15 1330 None

1m Heated Line (1)

-

Technical ProcedureStandard

Heated Probe (1)

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

CAT 11.61

SELECT Logger 2 -

Dual Channel Heater Controller CAT 3.81Kg Check Weight CAT 17.24

Last Impinger Arm CAT 4.404

Callipers

- 20m Heated Line (1)

-

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

5m Heated Line (1)

Bernath 3006 FID CAT 8.15

Water Vapour

Total VOCs (as Carbon)

CAT 5.52 1m Heated Line (2)

EN 14790

-

EN 14385

EN 14385

Mass Flow Controller (1)

Single Channel Heater Controller

S-Pitot (2) -

Heated Probe (3) -

CAT 6.44

-

SELECT Logger 1

CAT 20.62

500g Check Weight

SELECT Heated Head 1m Heated Line (3)

CAT 21.S42

EN 16911-1 (MID) CAT-TP-41

Mass Flow Controller (2) CAT 6.45

Mass View (1) -

20m Heated Line (2)

Parameter

Tape Measure CAT 16.35

-

-

Umbilical (2) Servomex 5200MP

Oven Box (1)

-

CAT 4.467

Mass View (2)

-

Laboratory Balance CAT 1.18 / 1.18a

Stack Thermocouple (3)

Stack Thermocouple (2)

-

-

CAT 12.53

CAT 3.59

-

Control Box DGM (1)

CAT 3.73-

-

Stack Thermocouple (1)

CAT 23.26

Instrumental Analysers

Stopwatch

CAT-TP-06

CAT-TP-06

CAT-TP-20

CAT-TP-05

EN 12619:2013

CAT 20.71

15m Heated Line (1)

CAT 17.24

CAT 7.23

Equipment I.D.

-

Position

Equipment I.D.

Digital Manometer (1)SELECT Horiba Model (1)

Oven Box (2)

-

CAT 14.53

Name

Control Box DGM (2)

-

ABB AO2020-URAS26

-

S-Pitot (1)

L-Pitot

-

CAT 3.73

Equipment Type

-

Antimony

Lead

Miscellaneous Items

CAT-RT (Version BJ)

Page 11 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 12: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

Stack Diameter / Depth, D

Gas Volumetric Flowrate (from Traverse)

Gas Volumetric Flowrate (STP, Dry)

°C

Average Stack Static Pressure, Pstatic

-

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

Volume

7.0

Molar Conc

0.28Stack Area, A

APPENDIX 2

mStack Width, W

24.0

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

kPa

kPa

0.84

Value

0.60

100.0

Average Stack Gas Temperature, Ta

0.005

-

Units

Average Pitot Tube Calibration Coefficient, Cp

ppm kg/m³

Average Stack Gas Pressure

Conc

1.31

Conc

M

Wet

r% v/v

kg/m³

m³/hr

Total Pressure

Average Wet Density (Actual), P ActualW

1.31

79.14

Fraction

Density

Dry

0.011

20.80 32.00

Actual

kg/m³

kPa

0.0131

20.53

Wet Density (STP), P STW

-

101.3

Temperature

N₂

0.06

Mass

Component

m³/hr

Result

°C

kg/m³

0.7914 28.01

1.31

kg/m³ 1.28

Duct gas flow conditions

2692

2967

1.17

0.989

1.29

kg/m³

Gas Volumetric Flowrate (STP, Wet)

Moisture

Conc

0.001

Pa

0.06

24.0

100.0

% v/v

Units

-

1.25

44.01

2657

Gas Volumetric Flowrate REF ¹

%

0.80

p pi

78.10

Dry Density (STP), P STD

18.02

Determinand

0.0006

2692

Result

1.96

-

-

0.2080

m³/hr

REF ¹

1.16

Dry Density (Actual), P Actual

m³/hr

-

1.43 0.297-

Units

Gas Volumetric Flowrate (Actual)

0.0

CAT-RT (Version BJ)

Page 12 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:51

Page 13: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

Wet Density

Pa 0.84

S-Type Pitot with KIMO MP 200 (500Pa)

Units

5 -

Pass

-

-

-

4.02.91

2.91

-

12:50 - 12:55

Sampling Line A

STATIC (Units: Pa)

Value

∆P -

-

-

100.0

2

0.56

Temp

-

-Swirl

No

kPa

-

-

-

-

Vertical

Pass

1

08/12/2015

Value

-

Depth

-

Velocity

Units

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

-

(1 of 1)

1

-

4

-

24.0

7.0

5.0

1.162

m/sPa

Traverse

m

0.041

1.162

24.00.45

--

4.0

°

6.9

-°C

5.0

7.2

3

2.95

kg/m³Point

1.162

Pass

- - --

-

- -

-

2.91

- -

24.0

- -

24.0

7.0

7.0 -

1.162

-Mean

-

-

0.15

-

-

-

-

4.0

-

-

-

-

-

-

-

- -

-

-

-

-

-

- - -

-

--

-

-

-

-

-

-

-

- -

-

-

1.162

2.89

24.0

-

-

---

-

-

-

-

-

-

--

-

-

-

-

-

-

-

-

-

-

-

-

-

CAT-RT (Version BJ)

Page 13 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 14: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

- u(qV,w)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

-

u(φO₂,d)

u(φCO₂,w)

- u²(a)/a²

- u²(qV,w)/q²V,w

-

u(res)

- u²(qV,w)

20.527

0.059

0.637

0.002

263.5 m³/hr

Pa

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

u(φCO₂,d) 0.002

u(cal) 0.005

u(drift) 0.083

u(fit) 0.047

u(Cf) 0.137

u(M) 0.00003

1.066

0.00087

K

u(pc) 175.695 Pa

u(patm) 175.692

- φCO₂,w

- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

1.066

u(ρ) 0.00627 -

u(vi) 0.223 Pa

u(v) 0.114 m/s

Uc(v) 0.223 m/s

Uc,rel(v) 7.64

u(φH₂O) 0.067

u(φO₂,w) 0.629

u(Tc) 1.515

Standard uncertainty associated with the mean velocity (95% Confidence)

Standard uncertainty associated with the mean velocity (95% Confidence), relative

Standard uncertainty associated with the volume flow rate (95% Confidence)

%

Uc(qV,w)

0.00205

- 18072

- 134.4

UnitsValueUncertainty

0.00053

-

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

- Resolution

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

Standard uncertainty associated with the molar mass of the gas

- φO₂,w

u(pstat)

Uc,rel(qV,w) 8.88 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

Performance characteristics (Uncertainty Components)

CAT-RT (Version BJ)

Page 14 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 15: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

0.0001Uncertainty ±mg/m³

MaximumUnits Blank 1

A1, A2, A3 & A4

Parameter

Number of Sampling Lines Used 1 / 1

Number of Sampling Points Used 4 / 4

A2-1 Abrasive Extraction

Parameter

0.0001

Sample Point I.D.'s

ANTIMONY: RESULTS SUMMARY

Units Run 1 Mean

Concentration mg/m³ 0.0005 0.0005

Titanium

Filter Housing Material Borosilicate Glass

0.0

Uncertainty ±g/hr 0.0

APPENDIX 2

Impinger Material

Mass Emission g/hr 0.0

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter

1.31

Uncertainty ±% v/v 0.07

Date of Sample Analysis 17/12/2015

Out Stack

0.0005

Parameter Value

Probe Material

0.0

NOTE: Where the maximum Blank concentration is higher than the Sample concentration, the Blank concentration has been reported.

Parameter Units Run 1 Mean

Water Vapour % v/v 1.31

Honeywell International Technologies Ltd, Unit 328

0.07

Concentration mg/m³ 0.0005

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure M31

ISO 17025 Accredited Analysis?

Filter Size and Material 47mm Quartz Fibre

Yes

Standard EN 14385

Technical Procedure CAT-TP-06

CAT-RT (Version BJ)

Page 15 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 16: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

Nozzle diameter, Dn mm 6.99

Nozzle area, An mm² 38.38

Total sampling time, q min 60

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 113.2

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Average square root of velocity heads, √∆P √mmH₂O 2.81

Average stack gas temperature, Ts °C 24.0

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 9.68

Conversion factor (K/mm.Hg), Cf - 0.3592

Area of stack, As m² 0.28

Qa = (60)(As)(Vs) m³/min 164.3

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw) m³/min N/A

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273) m³/min 149.0

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 147.1

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol 28.70

Pitot tube velocity constant, Kp - 34.97

Average of velocity heads, ∆Pavg mmH₂O 7.88

Total mass of liquid collected, Vlc

Vwstd = (0.001246)(Vlc)

% v/v 1.31

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

m³ 1.4430

Gas meter correction factor, Yd

28.84

Average pressure drop across orifice, ∆H mmH₂O

Average dry gas meter temperature, Tm °C 20.5

Total mass collected in impingers (silica trap)

APPENDIX 2

ANTIMONY: ISOKINETIC SAMPLING CALCULATIONS

N/A

% dry oxygen measured in gas stream, ACT%O₂d % v/v N/A

% v/v 0.06

% v/v 20.80

1.3736

g 14.5

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) - No

% wet oxygen measured in gas stream, ACT%O₂w % v/v

- N/A

53.4

% oxygen reference condition, REF%O₂ % v/v

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0131

m³ 0.0180

Volume of gas sample through gas meter, Vm

Ps = (Pb + (Pstatic / 13.6) mmHg 750.0

- 1.0180

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

Stack static pressure, Pstatic mmH₂O 0.5

N/A

1.3556

Total % v/v 20.86

Vmstw = (Vmstd)(100/(100 - Rwv))

21.8

Test

750.0

% v/v 1.31

Units Run 1

g

Barometric pressure, Pb mmHg

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) - N/A

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

Total mass collected in impingers (liquid trap) g -7.3

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂) g/gmol

Velocity pressure coefficient, Cp - 0.84

N₂ % v/v 79.14

CAT-RT (Version BJ)

Page 16 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 17: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<

µg 0.02

Calculated Concentration mg/m³ 0.0005

Calculated Concentration mg/m³ 0.0005

Total Mass Collected µg 0.66

Reported Concentration mg/m³ 0.0005

Mass on Filter / in Rinse µg 0.60

Mass in Front Impingers µg 0.04

Parameter Units Blank 1

Blank Dates - 08/12/2015

Average Volume Sampled (REF) m³ 1.3736

Total Mass Collected µg 0.66

Mass in Front Impingers µg 0.04

µg 0.02

Sampling Times - 14:05 - 15:05

Sampling Dates - 08/12/2015

Sampling Device - ISO

Volume Sampled (REF) m³ 1.3736

Mass on Filter / in Rinse µg 0.60

APPENDIX 2

ANTIMONY: SAMPLING DETAILS

Parameter Units Run 1

Reported Concentration mg/m³ 0.0005

CAT-RT (Version BJ)

Page 17 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 18: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

Maximum Temperature Recorded °C 10

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable - Yes

Test Conditions Units Run 1

Ambient Temperature Recorded? - Yes

Allowable Isokinetic Range % 95 - 115

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Maximum Filter Temperature °C 160

Impingers Exit Temperature Units Run 1

MU Acceptable % Yes

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded % Yes

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 113.2

Water Droplets Units Run 1

Are Water Droplets Present - No

MU (Concurrent Water Vapour) Units Run 1

Measurement Uncertainty (MU) % 5.2

Allowable MU % 20

Allowable Leak Rate l/min 0.49

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Detection Limit µg/m³ 0.5

Leak Test Acceptable - Yes

Absorption Efficiency Units Run 1

Absorption Efficiency % 100.0

Allowable Absorption Efficiency % 90

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Mean Sampling Rate l/min 24.48

Pre-Sampling Leak Rate l/min 0.11

Post-Sampling Leak Rate l/min 0.12

Detection Limit Acceptable

Allowable Detection Limit

- Yes

µg/m³ 5

CAT-RT (Version BJ)

Page 18 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 19: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

Expected Sampling Rate l/min 20.00

Validity of Blank vs ELV Units Blank 1

Allowable Blank mg/m³ N/A

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

Pre-Sampling Leak Rate l/min 0.15

Post-Sampling Leak Rate l/min 0.05

Allowable Leak Rate l/min 0.40

Leak Test Acceptable - Yes

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 2 OF 2)

Leak Test Results Units Blank 1

CAT-RT (Version BJ)

Page 19 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 20: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

N/A

0.49

ANTIMONY: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

Vm 1.4430

0.0001

L

Hm 0.0

Vm m³ 1.3556

% 0.68

Symbol

Lr 14.00

1.00

L 0.49 uL % -

≤2%

uLr %

0.0000 1.00

No Requirement

uHm % v/v 1.0

0.00

-

Symbol

- N/A

Uncertainty in Result

Lr mg/m³

Units Run 1

Uncertainty as a Percentage

Sensitivity Coefficient

Measured Quantities

Measured Quantities Units Run 1 Requirement of Standard

≤1%

% 2.00

Tm 293.5 uTm

Run 1

Oxygen Correction Part of MU Budget

mg/m³ 0.0000

≤2%

%

%

Uncertainty in Measurement Units

% v/v

uVm m³ 0.0289

N/A

mg/m³

0.0001

%

% N/A

Units Run 1

mg/m³ 0.0000

mg/m³

% 0.50

% 14.00

≤1%

Overall MU For O₂ Measurement

1.00

Run 1

Measured Quantities

ρm 100.0

Run 1

Measured Quantities Units

≤1%

Parameter Units Run 1

mg/m³ 0.0001

% 27.9

% 27.9

% 27.9

% N/A

mg/m³ 0.0001

mg/m³ N/A

mg/m³ 0.0001

mg/m³ 0.0001

uρm kPa 0.5

Units

APPENDIX 2

K 2.0

CAT-RT (Version BJ)

Page 20 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 21: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Parameter Value

Titanium

Filter Housing Material Borosilicate Glass

Impinger Material

1.31

Uncertainty ±% v/v 0.07 0.07

Parameter Units Blank 1 Maximum

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Number of Sampling Lines Used 1 / 1

Number of Sampling Points Used 4 / 4

Sample Point I.D.'s A1, A2, A3 & A4

Uncertainty ±mg/m³ 0.0001 0.0001

Mass Emission g/hr 0.0 0.0

Uncertainty ±g/hr 0.0 0.0

Parameter Units Run 1 Mean

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis? Yes

Water Vapour % v/v 1.31

Concentration mg/m³ 0.0004 0.0004

Date of Sample Analysis 17/12/2015

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure

Probe Material

APPENDIX 2

LEAD: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-1 Abrasive Extraction

Parameter Units Run 1 Mean

Concentration mg/m³ 0.0005 0.0005

CAT-RT (Version BJ)

Page 21 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 22: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

N/Am³/min

m³/min N/A

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

147.1

mm²

N₂ % v/v 79.14

Nozzle diameter, Dn mm 6.99

2.81

28.70

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

% v/v

% oxygen reference condition, REF%O₂ % v/v N/A

m³/min 149.0

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

Nozzle area, An

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

Average stack gas temperature, Ts

Area of stack, As m²

38.38

Conversion factor (K/mm.Hg), Cf

N/A

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 113.2

Average square root of velocity heads, √∆P √mmH₂O

0.28

N/A

N/A

0.06

Qa = (60)(As)(Vs) m³/min

Total sampling time, q min 60

164.3

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) -

% dry oxygen measured in gas stream, ACT%O₂d

g/gmol 28.84

- 0.3592

Vmstw@X%oxygen = (Vmstw) / (O₂REFw)

0.5

750.0

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0131

mmH₂O 53.4

Total mass collected in impingers (silica trap) g 21.8

Test Units Run 1

% v/v

Stack static pressure, Pstatic mmH₂O

Barometric pressure, Pb mmHg

1.31

750.0

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (liquid trap) g -7.3

7.88

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 9.68

24.0

Velocity pressure coefficient, Cp -

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

N/A

14.5

Vwstd = (0.001246)(Vlc)

% wet oxygen measured in gas stream, ACT%O₂w % v/v

1.4430

Gas meter correction factor, Yd - 1.0180

Average dry gas meter temperature, Tm °C

% v/v

0.84

No-

m³ N/A

Average of velocity heads, ∆Pavg mmH₂O

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d) -

Vmstw = (Vmstd)(100/(100 - Rwv))

APPENDIX 2

LEAD: ISOKINETIC SAMPLING CALCULATIONS

% v/v

Total mass of liquid collected, Vlc g

m³ 0.0180

Volume of gas sample through gas meter, Vm m³

20.5

Average pressure drop across orifice, ∆H

20.80

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³ 1.3556

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³

N/A

1.3736

m³/min

Total % v/v 20.86

Pitot tube velocity constant, Kp - 34.97

% v/v 1.31

°C

CAT-RT (Version BJ)

Page 22 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 23: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<

µg

µg

Sampling Device -

- 08/12/2015

Reported Concentration mg/m³

Mass in Front Impingers

0.0004

0.56

Parameter

Sampling Dates

ISO

Sampling Times

0.500

Volume Sampled (REF) m³

Total Mass Collected

1.3736

APPENDIX 2

Run 1

µg

Calculated Concentration mg/m³ 0.0005

0.02

0.627

Average Volume Sampled (REF)

0.029µg

- 14:05 - 15:05

Mass on Filter / in Rinse µg

Blank 1

Total Mass Collected µg

08/12/2015

µg 0.04

m³ 1.3736

LEAD: SAMPLING DETAILS

Parameter Units

Calculated Concentration mg/m³ 0.0004

Mass in Front Impingers µg 0.097

Mass on Filter / in Rinse

-

0.50

Blank Dates

Units

mg/m³ 0.0005Reported Concentration

CAT-RT (Version BJ)

Page 23 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 24: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

30

113.2

10°C

°C

Maximum Filter Temperature

Maximum Temperature Recorded

90

Post-Sampling Leak Rate l/min

% 100.0

Allowable Isokinetic Range %

Ambient Temperature Recorded?

Yes

Units

°C

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Absorption Efficiency Units Run 1

Absorption Efficiency

APPENDIX 2

Impingers Exit Temperature

Isokinetic Criterion Compliance

MU (Concurrent Water Vapour) Units

Yes

Units Run 1

Isokineticity Acceptable

%

Are Water Droplets Present

Units Run 1

-

-

Isokinetic Variation

-

LEAD: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Allowable Leak Rate l/min

MU Acceptable

Detection Limit Acceptable

µg/m³

Run 1

Yes

Silica Gel (Concurrent Water Vapour) Units

Units Run 1

Exit Temperature Acceptable - Yes

Test Conditions Run 1

160

- Yes

Run 1

Detection Limit 0.4

%

Pre-Sampling Leak Rate

l/min 24.48

Filter Temperatures

Less than 50% Faded

Run 1

Mean Sampling Rate

0.49

µg/m³

Allowable MU

Maximum Allowable Temperature

Water Droplets Units

Leak Test Acceptable

Yes

%

No

Allowable Absorption Efficiency %

l/min 0.11

95 - 115

0.12

Measurement Uncertainty (MU) % 5.2

Allowable Detection Limit

%

20

5

- Yes

CAT-RT (Version BJ)

Page 24 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 25: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

Yes

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Allowable Blank

Leak Test Acceptable -

Units Blank 1

Pre-Sampling Leak Rate

Post-Sampling Leak Rate l/min 0.05

mg/m³ N/A

Blank 1

(PAGE 2 OF 2)

Leak Test Results

0.15

There are no deviations associated with the sampling employed.

Allowable Leak Rate l/min 0.40

Expected Sampling Rate l/min

Units

APPENDIX 2

Validity of Blank vs ELV

20.00

LEAD: QUALITY ASSURANCE

l/min

CAT-RT (Version BJ)

Page 25 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Page 26: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

≤2%%

Run 1

13.00

%

mg/m³ 0.0001

1.00Lr mg/m³ 0.0001

Symbol

Uncertainty in Measurement Units

mg/m³

Run 1

K

Units

≤1%

26.0

uTm

Measured Quantities

Vm

mg/m³

Requirement of Standard

mg/m³ 0.0001

0.0001

293.5

% 0.50

N/A

Run 1

UnitsMeasured Quantities

Uncertainty in Result

0.0000

Units

Oxygen Correction Part of MU Budget

Measured Quantities Units

uLr % -

L 0.49

uHm % v/v

Standard uncertainty

APPENDIX 2

1.00

Measured Quantities Symbol Run 1

1.0

ρm 100.0

-

Hm 0.0

Units

Vm

0.49

Lr

m³1.4430 uVm

uL %

%

0.0000

uρm

0.00

Units Run 1

Tm

0.0001

%

% 13.00

≤1%

0.0000

≤1%

Run 1

-

% N/A

Overall MU For O₂ Measurement

0.0289

Value

26.0

mg/m³

% 26.0

%

Measured Quantities

0.68

1.3556

Run 1

No Requirement

Parameter

Uncertainty as a Percentage

0.0001

mg/m³

Symbol

≤2%% 2.00

kPa 0.5

2.0

LEAD: MEASUREMENT UNCERTAINTY CALCULATIONS

Sensitivity Coefficient

% v/v N/A

mg/m³

L mg/m³

Run 1

1.00%

N/A

mg/m³ N/A

% N/A

CAT-RT (Version BJ)

Page 26 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 27: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Span Gas Type Propane In Synthetic Air (5 Grade)

EN 12619:2013

Technical Procedure

Heated Head Filter Used

Probe Material Stainless Steel

Filtration Type / Size 0.1µm Glass Fibre

A2-1 Abrasive Extraction

Parameter Units Run 1

Span Gas Expiry Date

1.2

Parameter

0.40

Number of Sampling Lines Used

A1

Number of Sampling Points Used 1 / 1

Uncertainty ±mg/m³ 0.46

N/A

Yes

Synthetic Air (5 Grade)

Mean

Standard

15/07/2020

Uncertainty

Value

Span Gas Reference Number

Sample Point I.D.'s

mg/m³

0.46

Span Gas Uncertainty (%)

Honeywell International Technologies Ltd, Unit 328

80.2

1.1 1.1

Heated Line Temperature

1.0187

Span Gas Start Pressure (bar) 100

Gas Cylinder Concentration (ppm)

g/hr

TOTAL VOCs (as CARBON): RESULTS SUMMARY

0.40

CAT-TP-20

APPENDIX 2

Mass Emission

Concentration

180°C

Span Gas Set Point (ppm) 80.20

1 / 1

1.2±g/hr

Zero Gas Type

CAT-RT (Version BJ)

Page 27 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 28: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Graphical Trend of Data

APPENDIX 2

TOTAL VOCs (as CARBON): DATA TREND

COVER ME WITH CHART/S

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

14

:05

14

:06

14

:07

14

:08

14

:09

14

:10

14

:11

14

:12

14

:13

14

:14

14

:15

14

:16

14

:17

14

:18

14

:19

14

:20

14

:21

14

:22

14

:23

14

:24

14

:25

14

:26

14

:27

14

:28

14

:29

14

:30

14

:31

14

:32

14

:33

14

:34

14

:35

Co

nce

ntr

atio

n (

mg/

m³)

Total VOCs At Reference Conditions

- Run 1

CAT-RT (Version BJ)

Page 28 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 29: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampling Details

Quality Assurance

Zero Drift 0 0 0

Zero Drift 0 0 0

Zero Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Method Deviations

1

x

- - -

- - -

- - -

- - -

- - -

ppm

CA

L 2

CA

L 1

- Yes

-

There are no deviations associated with the sampling employed.

Run Ambient Temperature Range 10 - 15

Units Run 1

Zero Down Sampling Line (Pre)

APPENDIX 2C

AL

3

± ppm

Run 1

CA

L 3

Units

4.01Allowable Zero Drift

ppm

Span Down Sampling Line (Post) ppm

ppm

ppm

CA

L 1

08/12/2015

ppm

ppm 79.80

Nature of Deviation

(x = deviation applies to the associated run)

ppm

Test Conditions

-

ppm

Units

ppm

Sampling Times -

ppm

Zero Down Sampling Line (Post) ppm

ppm 0.10

0.10

Allowable Span Drift

Sampling Dates

Units Run 1

Parameter

°C

Run Number

± ppm 4.01

Yes

ppm

Zero Drift

Zero Down Sampling Line (Pre)

Instrument Range ppm 100

0.00

Zero Down Sampling Line (Post)

Span Down Sampling Line (Pre)

Span Down Sampling Line (Pre)

Span Down Sampling Line (Post)

Span Drift Acceptable

ppm 79.90

Zero Down Sampling Line (Post) ppm

80.2

Zero Down Sampling Line (Pre)

Run 1

TOTAL VOCs (as CARBON): SAMPLING DETAILS & QUALITY ASSURANCE

Span Gas Value

CA

L 2

0.10ppm

ppm

Span Drift

14:05 - 14:35

Zero Drift Acceptable

Span Down Sampling Line (Post)

Span Down Sampling Line (Pre) ppm

CAT-RT (Version BJ)

Page 29 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 30: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

k =

ppm to mg/m³

MCERTS Range [B] 15.0

mg/m³

Combined interference

mg/m³

Volume or pressure flow dependence 0.00 mg/m³

% at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A

Ambient temperature dependence

mg/m³

Cal gas conc. 80.2 ppm

use rep at span

Performance characteristic

RUN 1 Units

Response time 45

15.0 mg/m³

Cal gas conc. 128.8

%

0.40 mg/m³ (STP, dry)

Expanded uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A -

Lack of fit 0.01

RUN 1 Units

% of Value

Expanded uncertainty (no O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (no O₂) - at 95% Confidence N/A

160.6

RUN 1 Units

Standard deviation of repeatability at zero

mg/m³

Lower of [A] or [B]

ppm

Range Used [A]

TOTAL VOCs (as CARBON): MEASUREMENT UNCERTAINTY CALCULATIONS

Units

- mg/m³ (REF)

15.0

mg/m³

Performance characteristics

mg/m³

Uncertainty of calibration gas 0.00

Atmospheric pressure dependence 0.01 mg/m³

APPENDIX 2

0.45

% of Value

mg/m³

mg/m³

Losses in the line (leak) 0.00

RUN 1 Units

Measurement uncertainty

0.20

mg/m³

Expanded uncertainty (with O₂) - at 95% Confidence

Result 0.40 mg/m³

Combined uncertainty 0.24

-

Repeatability at zero 2.00

Range Used 100.0

Performance characteristics RUN 1

% of value

Repeatability at span level 0.00 % full scale

Deviation from linearity 0.17 % of value

Zero drift 0.13 % full scale

Span drift

Requirement for SRM is that Uncertainty should be <15% of the value at the ELV, on a dry gas basis, or if O₂ correction is applied less than 15% + the uncertainty

associated with the O₂ correction (using sqrt of sum squares to add uncertainty components). Ref EA TGN M2.

Measured concentration

TGN M2 Allowable MU

Limit value

Expanded uncertainty 1.96 0.47 mg/m³

Uncertainty corrected to std conds. (O₂) 0.47 mg/m³ (REF)

RUN 1 Units

Expanded uncertainty (no O₂) - at 95% Confidence 115.13

% range

Dependence on voltage 0.50 % full scale/10V

Losses in the line (leak) 0.50

mg/m³

Combined interference (from MCERTS Certificate) 0.04

-

N/A

% full scale

Conversion 1.61

mg/m³

Standard deviation of repeatability at span level 0.00

mg/m³

Drift 0.09

30

% of value/kPa

Ambient temperature dependence 1.40

mg/m³

Dependence on voltage 0.06

seconds

Number of readings in measurement

% full scale

Volume or pressure flow dependence 1.60

0.13

% of full scale

Atmospheric pressure dependence 0.30

% full scale/10K

% of value

Uncertainty of calibration gas 2.00

CAT-RT (Version BJ)

Page 30 of 30

Honeywell International Technologies Ltd

Unit 328

A2-1 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 31: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279

Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Stack Emissions Testing Report Commissioned by

8th December 2015

Job Reference Number

CDU-0559

Installation Name & Address

Report Written by

Patrick O'Brien

5th January 2016Report Date

TE1 TE2 TE3 TE4

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Version 1

MM 08 922MCERTS Level 2

Team Leader

Team Leader

TE1 TE2 TE3 TE4MM 08 922

MCERTS Level 2

Patrick O'Brien

Report Approved by

Dates of the Monitoring Campaign

Version

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24T: +353 86 853 8247

E: [email protected] Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

WaterfordCork Road Industrial Park

Honeywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-2 Abrasive Extraction

DELETE & COVER ME

CAT-RT (Version BJ)

CDU-0559 Honeywell Int Technology A2-2 (POST)

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Page 32: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

4

7

7

CONTENTS

2

9

3

5

6

8

The testing performed fully meets the technical requirements in Irish EPA

Guidance Note, AG2.

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the written

approval of Exova Catalyst Ireland.

CAT-RT (Version BJ)

Page 2 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 33: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

Honeywell International Technologies Ltd, Unit 328

A2-2 Abrasive Extraction

8th December 2015

(Page 1 of 7)

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd

to carry out stack emissions testing on the A2-2 Abrasive Extraction at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

Antimony, Lead, Total VOCs (as Carbon)

MONITORING OBJECTIVES

Executive Summary

CAT-RT (Version BJ)

Page 3 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 34: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

where MU = Measurement Uncertainty associated with the Result

Parameter

Antimony ¹ < <

Lead ¹ - -

Total VOCs (as Carbon) ¹ - -

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

0.43

(Page 2 of 7)

°C

Volumetric Flow Rate (ACTUAL)

0.41

372

m³/hrVolumetric Flow Rate (REF)

A2-2 Abrasive Extraction

0.0010mg/m³ g/hr

-

0.00027

Executive Summary

Mass Emission

-

MONITORING RESULTS

- g/hr

3.3

0.15

m³/hr

0.46

1.03% v/v

m/s

0.06

23.0

mg/m³

50

0.16

Honeywell International Technologies Ltd, Unit 328

8th December 2015

+/-

Units Result

Concentration

MULimit

+/-

UnitsResult LimitMU

-

0.00010

0.0010 0.00026 - g/hr 0.00010

0.00033

0.00034mg/m³

-

339 45 -

-

CAT-RT (Version BJ)

Page 4 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 35: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Parameter

R1 < <

R1 - -

R1 - -

R1

All results are expressed at the respective reference conditions.

Total VOCs (as Carbon) 0.43 08/12/2015 3012:40 - 13:100.15

08/12/20150.0010

30

30

mg/m³ 0.0010

mins

Executive Summary

Sampling

Times

Units

(Page 3 of 7)

MONITORING DATE(S) & TIMES

A2-2 Abrasive Extraction

8th December 2015

Units Concentration Sampling

g/hrmg/m³

08/12/2015 11:40 - 11:45

Date(s)

Mass Emission

Antimony

g/hrLead

Velocity & Volumetric Flow Rate

0.00033

12:40 - 13:1008/12/2015

mg/m³ 12:40 - 13:10

0.00034

g/hr

Honeywell International Technologies Ltd, Unit 328

Duration

CAT-RT (Version BJ)

Page 5 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 36: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Standard Operating Conditions

Normal Operation

Abatement System

Abatement System Running Status

(Page 4 of 7)

Executive Summary

PROCESS DETAILS

On

ContinuousContinuous or Batch Process

Plume Appearance

Bag Filter

Not Visible

ValueParameter

Process Status

Honeywell International Technologies Ltd, Unit 328

A2-2 Abrasive Extraction

8th December 2015

CAT-RT (Version BJ)

Page 6 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Honeywell International Technologies Ltd, Unit 328

MONITORING & ANALYTICAL METHODS

Executive Summary

(with short name reference as appears in the table above)

RPS Laboratories Ltd (RPS)

ANALYSIS LABORATORIES

All There are no deviations associated with the sampling employed.

Yes RPS

CAT Yes RPS

Total VOCs (as Carbon)

EN 16911-1 (MID) CAT-TP-41

Run

SUMMARY OF SAMPLING DEVIATIONS

Parameter

Velocity & Vol. Flow Rate

Deviation

8th December 2015

(Page 5 of 7)

Testing Analysis

Lead

(Average)

ISO

Flame Ionisation Detection by Sick 3006 FID

A2-2 Abrasive Extraction

Standard

Lab

Yes

MCERTS

17025

Testing

EN 14385

ICP-MS

Testing

CAT-TP-06

EN 14385 CAT-TP-06 Yes

Lab

Monitoring Analysis

0.001 mg/m³

Procedure

Analytical

Technique

AnalyticalTechnical ISOParameter

ICP-MSCAT Yes Yes

Procedure

LOD

0.16 mg/m³CAT-TP-20

CAT YesWater Vapour

0.001 mg/m³

Antimony

Yes 1.2 m/s

ISO 17025 Accreditation Number: 0605

CAT

All

EN 12619:2013

YesCAT-TP-05 YesEN 14790

Pitot Tube and Thermocouple

YesCAT

GravimetricCAT-TP-05

Yes

0.1 % v/vCAT

Yes

M31

M31

17025 Analysis

CAT-RT (Version BJ)

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Sample Date/s: 8th December 2015

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Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

Value

0.00 0.00

-

-

0.00

Hole

-

Area

Yes

Lowest Differential Pressure

-3.29

Value

Depth

3.29

-

5

0.00Ratio of Above : 1 Yes

< 15°

< 3 : 1

-

Yes

-

Highest Gas Velocity

Yes

m

Lowest Gas Velocity

m/s

Yes

-

3.29

-

-

Required

-

0.03

-

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

-

-

-

Yes

Traverse 1

m/s

Easy Access Available

-

Width

Compliant

Vertical

Yes

Parameter

There are no obstructions present which hamper insertion of sampling equipment

Sample Port Size

Circular

Value

Yes

(Page 6 of 7)

Port Depth

-

There is no requirement to perform a BS EN 15259 Homogeneity Test on this Stack.

9.0

1.00

°

-

--

0

Yes

Units

-

-

m

All platforms should be designed in accordance with the requirements in the Environment Agency's Technical Guidance Note M1

and EN 15259.

Permanent / Temporary Platform

Inside / Outside

SUITABILITY OF SAMPLING LOCATION

General Platform Information

Units

-

On Roof

-

-

Mean Velocity

Outside

-

-

-

-

--m/s

Maximum Angle of Swirl

Executive Summary

cm

Yes

- -

No Local Negative Flow

Criteria in EN 15259 -

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

0.20

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

Yes

-

-

-

Platform has vertical base boards (approx. 0.25m high)

> 5 Pa

Safe Access Available

CAT-RT (Version BJ)

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Photo 3

SAMPLE POINTS

Executive Summary

Photo 2

PLANT PHOTOS

(Page 7 of 7)

Photo 1

Photo 4

Line A

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

CAT-RT (Version BJ)

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Page 40: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDIX CONTENTS

APPENDICES

CAT-RT (Version BJ)

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Name

CAT-TP-06

CAT-TP-06

-

Heated Probe (3) -

CAT 6.44

Control Box DGM (2)

-

ABB AO2020-URAS26

-

S-Pitot (1)

L-Pitot

-

Equipment I.D.

-

Position

Digital Manometer (1)SELECT Horiba Model (1)

Oven Box (2)

Technical Endorsements

Team Leader Patrick O'Brien MCERTS Level 2

Extractive Sampling

LIST OF EQUIPMENT

MCERTS Accreditation

Single Channel Heater Controller

S-Pitot (2)

CAT-TP-20

CAT-TP-05

EN 12619:2013

CAT 20.71

15m Heated Line (1)

CAT 17.24

-

CAT 14.53

Equipment I.D.

Stack Thermocouple (3)

Stack Thermocouple (2)

-

-

CAT 12.53

CAT 3.59

-

Miscellaneous Items

MM 08 922 TE1 TE2 TE3 TE4

Technician James Magann MCERTS Level 1 MM 15 1330 None

-

-

Umbilical (2) Servomex 5200MP

Oven Box (1)

-

CAT 4.467

Mass View (2)

-

Laboratory Balance CAT 1.18 / 1.18a

Equipment Type

Tape Measure CAT 16.35

EN 16911-1 (MID) CAT-TP-41

Mass Flow Controller (2) CAT 6.45

Mass View (1) -

20m Heated Line (2)

Parameter

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

Water Vapour

Total VOCs (as Carbon)

CAT 5.52 1m Heated Line (2)

EN 14790

-

EN 14385

EN 14385

Mass Flow Controller (1)

CAT 23.26

-

Antimony

Lead

CAT 11.61

SELECT Logger 2 -

Dual Channel Heater Controller CAT 3.81Kg Check Weight CAT 17.24

Last Impinger Arm CAT 4.404

Callipers

- 20m Heated Line (1)

-

Equipment Type

SELECT Logger 1

1m Heated Line (1)

-

Technical ProcedureStandard

Heated Probe (1)

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

Equipment I.D.

-

-

SELECT Gas Conditioning

CAT 13.27

Instrumental Analysers

Stopwatch

CAT 3.73

Equipment Type

-

Heated Probe (2)

-

-

CAT 3.59

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

5m Heated Line (1) CAT 20.62

500g Check Weight

SELECT Heated Head 1m Heated Line (3)

Control Box DGM (1)

CAT 3.73-

-

CAT 21.S42

Stack Thermocouple (1)

Gasmet Sampling System-

CAT 7.23

Bernath 3006 FID CAT 8.15

MCERTS Number

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

Eco Physics CLD 822Mh

Velocity & Vol. Flow Rate

Bioaerosols Temperature Logger -

Electronic Refrigerator -

CAT-RT (Version BJ)

Page 11 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 42: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

0.0

1.43 0.30-

Units

Gas Volumetric Flowrate (Actual)

-

0.2080

m³/hr

REF ¹

1.17

Dry Density (Actual), P Actual

m³/hr

-

336

Gas Volumetric Flowrate REF ¹

%

0.80

p pi

78.32

Dry Density (STP), P STD

18.02

Determinand

0.0006

339

Result

1.96

-

kg/m³

Gas Volumetric Flowrate (STP, Wet)

Moisture

Conc

0.0012

Pa

0.06

23.0

100.2

% v/v

Units

Component

m³/hr

Result

°C

kg/m³

0.7914 28.01

1.03

kg/m³ 1.28

Duct gas flow conditions

339

372

1.17

0.99

1.29kg/m³

kPa

0.0103

20.59

Wet Density (STP), P STW

-

101.3

Temperature

N₂

0.06

Gas Volumetric Flowrate (from Traverse)

Gas Volumetric Flowrate (STP, Dry)

Mass

-

1.25

44.01

-

Units

Average Pitot Tube Calibration Coefficient, Cp

ppm kg/m³

Average Stack Gas Pressure

Conc

1.03

Conc

M

Wet

r% v/v

kg/m³

m³/hr

Total Pressure

Average Wet Density (Actual), P ActualW

1.03

79.14

Fraction

Density

Dry

0.01

20.80 32.00

Actual

Volume

9.0

Molar Conc

0.03Stack Area, A

APPENDIX 2

mStack Width, W

23.0

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

kPa

0.84

Value

0.20

100.2

Average Stack Gas Temperature, Ta

0.005Average Stack Static Pressure, Pstatic

-

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

kPa

°C

Stack Diameter / Depth, D

CAT-RT (Version BJ)

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Job Number: CDU-0559, Version 1

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Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

--

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

---

-

23.0

-

-

- -

-

--

-

-

-

-

-

-

-

-

-

-

-

-

- - -

-

-

-

-

-

-

- -

-

- -

-

Mean

-

-

-

-

9.0 -

1.170

-

- - - -

- --

-

- -

-

kg/m³Point

Pass

-

m/sPa

Traverse

m

0.101

--° -°C

4.5

9.0 3.29

1

-

-

23.0

5.0

1.170

Units

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

-

(1 of 1)

kPa

-

-

-

-

Vertical

Pass

1

08/12/2015

Value

-

Depth

-

Velocity

STATIC (Units: Pa)

Value

∆P -

-

-

100.2

Temp

-

-

3.29

-

11:40 - 11:45

Sampling Line A

Units

5 -

Pass

-

-

-Swirl

No

Wet Density

Pa 0.84

S-Type Pitot with KIMO MP 200 (500Pa)

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 44: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Uc,rel(qV,w) 13.39 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

Performance characteristics (Uncertainty Components)

Standard uncertainty associated with the volume flow rate (95% Confidence)

%

Uc(qV,w)

0.00467

- 645

- 25.4

UnitsValueUncertainty

0.00053

-

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

- Resolution

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

Standard uncertainty associated with the molar mass of the gas

- φO₂,w

u(pstat) 1.061

u(ρ) 0.00631 -

u(vi) 0.211 Pa

u(v) 0.211 m/s

Uc(v) 0.414 m/s

Uc,rel(v) 12.60

u(φH₂O) 0.053

u(φO₂,w) 0.630

Standard uncertainty associated with the mean velocity (95% Confidence)

Standard uncertainty associated with the mean velocity (95% Confidence), relative

K

u(pc) 175.695 Pa

u(patm) 175.692

- φCO₂,w

- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

u(φCO₂,d) 0.002

u(cal) 0.008

u(drift) 0.083

u(fit) 0.033

u(Cf)

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

0.126

u(M) 0.00003

u(Tc) 1.510

1.061

- u²(qV,w)

- u(qV,w)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

20.585

- 0.059

u(φO₂,d) 0.637

u(φCO₂,w) 0.002

- u²(a)/a²

- u²(qV,w)/q²V,w

-

49.8 m³/hr

Pa

u(res) 0.00087

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Yes

Standard EN 14385

Technical Procedure CAT-TP-06

Filter Size and Material 47mm Quartz Fibre

Honeywell International Technologies Ltd, Unit 328

0.06

0.0

NOTE: Where the maximum Blank concentration is higher than the Sample concentration, the Blank concentration has been reported.

Parameter Units Run 1 Mean

Water Vapour % v/v 1.03

Sample Point I.D.'s

Concentration mg/m³ 0.0010

Name of Analytical Laboratory

APPENDIX 2

Impinger Material

Mass Emission g/hr 0.0

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter

1.03

Uncertainty ±% v/v 0.06

Date of Sample Analysis 17/12/2015

Out Stack

0.0010

Parameter Value

Probe Material

Units Run 1 Mean

Concentration mg/m³ 0.0010 0.0010

Titanium

Filter Housing Material Borosilicate Glass

0.0

Uncertainty ±g/hr 0.0

ANTIMONY: RESULTS SUMMARY

A2-2 Abrasive Extraction

Parameter

0.00030.0003Uncertainty ±mg/m³

MaximumUnits Blank 1

A1

Parameter

Number of Sampling Lines Used 1 / 1

Number of Sampling Points Used 1 / 1

RPS

Analytical Laboratory's Procedure M31

ISO 17025 Accredited Analysis?

CAT-RT (Version BJ)

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

g

Barometric pressure, Pb mmHg

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) - N/A

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

Total mass collected in impingers (liquid trap) g -3.5

N₂ % v/v 79.14

% v/v 1.03

Units Run 1

g/gmol

9.1

Test

750.0

0.6687

Total % v/v 20.86

No

Vmstw = (Vmstd)(100/(100 - Rwv))

Stack static pressure, Pstatic mmH₂O 0.5

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0103

m³ 0.0070

Volume of gas sample through gas meter, Vm

Ps = (Pb + (Pstatic / 13.6) mmHg 750.0

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) -

% wet oxygen measured in gas stream, ACT%O₂w % v/v

- N/A

61.0

% oxygen reference condition, REF%O₂ % v/v N/A

% dry oxygen measured in gas stream, ACT%O₂d % v/v N/A

N/A

% v/v 0.06

% v/v 20.80

0.6757

g 5.6

- 1.0180

Average pressure drop across orifice, ∆H mmH₂O

Average dry gas meter temperature, Tm °C 17.9

Total mass collected in impingers (silica trap)

APPENDIX 2

ANTIMONY: ISOKINETIC SAMPLING CALCULATIONS

Velocity pressure coefficient, Cp - 0.84

Average of velocity heads, ∆Pavg mmH₂O 9.00

Total mass of liquid collected, Vlc

Vwstd = (0.001246)(Vlc)

% v/v 1.03

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

m³ 0.7051

Gas meter correction factor, Yd

28.84

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol 28.73

Pitot tube velocity constant, Kp - 34.97

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

Area of stack, As m² 0.03

Qa = (60)(As)(Vs) m³/min 19.5

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw) m³/min N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Average square root of velocity heads, √∆P √mmH₂O 3.00

Average stack gas temperature, Ts °C 23.0

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 10.33

Conversion factor (K/mm.Hg), Cf - 0.3592

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273) m³/min 17.7

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 17.5

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 103.7

Nozzle diameter, Dn mm 7.00

Nozzle area, An mm² 38.49

Total sampling time, q min 30

CAT-RT (Version BJ)

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Page 47: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<mg/m³ 0.0010

APPENDIX 2

ANTIMONY: SAMPLING DETAILS

Parameter Units Run 1

Volume Sampled (REF) m³ 0.6757

Mass on Filter / in Rinse µg 0.60

Sampling Times - 12:40 - 13:10

Sampling Dates - 08/12/2015

Sampling Device - ISO

Total Mass Collected µg 0.66

Mass in Front Impingers µg 0.04

µg 0.02

Parameter Units Blank 1

Blank Dates - 08/12/2015

Average Volume Sampled (REF) m³ 0.6757

Calculated Concentration mg/m³ 0.0010

Total Mass Collected µg 0.66

Reported Concentration mg/m³ 0.0010

Mass on Filter / in Rinse µg 0.60

Mass in Front Impingers µg 0.04

µg 0.02

Calculated Concentration mg/m³ 0.0010

Reported Concentration

CAT-RT (Version BJ)

Page 17 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:52

Page 48: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

Yes

µg/m³

Detection Limit Acceptable

Allowable Detection Limit

-

5

Pre-Sampling Leak Rate l/min 0.11

Post-Sampling Leak Rate l/min 0.08

Allowable Absorption Efficiency % 90

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Mean Sampling Rate l/min 23.93

Detection Limit µg/m³ 1.0

Leak Test Acceptable - Yes

Absorption Efficiency Units Run 1

Absorption Efficiency % 100.0

Measurement Uncertainty (MU) % 6.1

Allowable MU % 20

Allowable Leak Rate l/min 0.48

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Water Droplets Units Run 1

Are Water Droplets Present - No

MU (Concurrent Water Vapour) Units Run 1

Yes

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 103.7

Maximum Filter Temperature °C 160

Impingers Exit Temperature Units Run 1

MU Acceptable % Yes

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded %

Allowable Isokinetic Range % 95 - 115

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Test Conditions Units Run 1

Ambient Temperature Recorded? - Yes

Maximum Temperature Recorded °C 10

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable - Yes

CAT-RT (Version BJ)

Page 18 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 49: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 2 OF 2)

Leak Test Results Units Blank 1

l/min 0.40

Leak Test Acceptable - Yes

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

Pre-Sampling Leak Rate l/min 0.15

Post-Sampling Leak Rate l/min 0.05

Allowable Leak Rate

Validity of Blank vs ELV Units Blank 1

Allowable Blank mg/m³ N/A

Blank Acceptable - N/A

Nature of Deviation Run Number

Expected Sampling Rate l/min 20.00

CAT-RT (Version BJ)

Page 19 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 50: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

APPENDIX 2

K 2.0

uρm kPa 0.5

Units

mg/m³ 0.0003

mg/m³ N/A

mg/m³ 0.0003

mg/m³ 0.0003

% 27.9

% 27.9

% 27.9

% N/A

Parameter Units Run 1

mg/m³ 0.0001

≤1%

Measured Quantities Units

Measured Quantities

ρm 100.0

Run 1

Run 1

N/A

% 14.00

≤1%

Overall MU For O₂ Measurement

Units

% 0.50

1.000.0001

%

% N/A

% v/v

uVm m³ 0.0141

N/A

Requirement of Standard

≤1%

0.00

Tm 290.9 uTm

Run 1

Oxygen Correction Part of MU Budget

mg/m³ 0.0000

Uncertainty as a Percentage

Sensitivity Coefficient

Measured Quantities

Measured Quantities Units Run 1

Symbol

- N/A

Uncertainty in Result

Lr mg/m³

Units Run 1

% 2.00 ≤2%

%

mg/m³ 0.0000 1.00

No Requirement

uHm % v/v 1.0

1.00

L 0.33 uL % -

≤2%

Lr 14.00

L

Hm 0.0

Vm m³ 0.6687

% 0.69

Symbol

Run 1

%

Uncertainty in Measurement Units

uLr % -

ANTIMONY: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

Vm 0.7051

mg/m³ 0.0000

mg/m³ 0.0001

0.33

CAT-RT (Version BJ)

Page 20 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 51: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

APPENDIX 2

LEAD: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-2 Abrasive Extraction

Parameter Units Run 1 Mean

Concentration mg/m³ 0.0010 0.0010

Date of Sample Analysis 17/12/2015

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure

Probe Material

NOTE: Where the maximum Blank concentration is higher than the Sample concentration, the Blank concentration has been reported.

Parameter Units Run 1 Mean

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis? Yes

Water Vapour % v/v 1.03

Concentration mg/m³ 0.0010 0.0010

Uncertainty ±mg/m³ 0.0003 0.0003

Mass Emission g/hr 0.0 0.0

Uncertainty ±g/hr 0.0 0.0

1 / 1

Number of Sampling Points Used 1 / 1

Sample Point I.D.'s A1

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Number of Sampling Lines Used

Titanium

Filter Housing Material Borosilicate Glass

Impinger Material

1.03

Uncertainty ±% v/v 0.06 0.06

Parameter Units Blank 1 Maximum

Parameter Value

CAT-RT (Version BJ)

Page 21 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 52: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

Total % v/v 20.86

Pitot tube velocity constant, Kp - 34.97

% v/v 1.03

°C

m³/min

N/A

0.6757

17.9

Average pressure drop across orifice, ∆H

20.80

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³ 0.6687

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³

Average of velocity heads, ∆Pavg mmH₂O

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d) -

Vmstw = (Vmstd)(100/(100 - Rwv))

APPENDIX 2

LEAD: ISOKINETIC SAMPLING CALCULATIONS

% v/v

% wet oxygen measured in gas stream, ACT%O₂w % v/v

0.7051

Gas meter correction factor, Yd - 1.0180

Average dry gas meter temperature, Tm °C

% v/v

0.84

No-

m³ N/A

Velocity pressure coefficient, Cp -

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

N/A

5.6

Vwstd = (0.001246)(Vlc)

9.00

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 10.33

23.0

Test Units Run 1

% v/v

Stack static pressure, Pstatic mmH₂O

Barometric pressure, Pb mmHg

1.03

750.0

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (liquid trap) g -3.5

mmH₂O 61.0

Total mass collected in impingers (silica trap) g 9.1

Total mass of liquid collected, Vlc

Vmstw@X%oxygen = (Vmstw) / (O₂REFw)

0.5

750.0

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0103

g

m³ 0.0070

Volume of gas sample through gas meter, Vm

19.5

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) -

% dry oxygen measured in gas stream, ACT%O₂d

g/gmol 28.84

Total sampling time, q min 30

Average square root of velocity heads, √∆P √mmH₂O

0.03

N/A

N/A

0.06

Qa = (60)(As)(Vs)

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) %

N/A

38.49

Conversion factor (K/mm.Hg), Cf

103.7

m³/min

- 0.3592

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

Nozzle area, An

% v/v

% oxygen reference condition, REF%O₂ % v/v N/A

m³/min 17.7

N₂ % v/v 79.14

Nozzle diameter, Dn mm 7.00

3.00

28.73

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

Average stack gas temperature, Ts

Area of stack, As m²

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

17.5

mm²

m³/min

m³/min N/A

N/A

CAT-RT (Version BJ)

Page 22 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:52

Page 53: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

-

Mass in Back Impinger <

-

-

-

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

-

<

Mass in Back Impinger -

-

-

-

Reported Concentration mg/m³ 0.0010

Units

-

Calculated Concentration mg/m³ 0.0010

Mass in Front Impingers µg 0.061

LEAD: SAMPLING DETAILS

Parameter Units

m³ 0.6757

08/12/2015

µg 0.04

Mass on Filter / in Rinse µg

Blank 1

Total Mass Collected µg 0.580

Average Volume Sampled (REF)

0.019µg

- 12:40 - 13:10

Mass on Filter / in Rinse

Run 1

µg

Calculated Concentration mg/m³

Volume Sampled (REF) m³

Total Mass Collected

0.6757

APPENDIX 2

Sampling Times

0.500

0.0009

0.03

Parameter

Sampling Dates

ISO

0.67

- 08/12/2015

Reported Concentration mg/m³

Mass in Front Impingers

0.0010

0.60

Blank Dates

µg

Sampling Device -

µg

CAT-RT (Version BJ)

Page 23 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 54: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

Yes-

5

Measurement Uncertainty (MU) % 6.1

Allowable Detection Limit

%

20

0.08

95 - 115

Allowable Absorption Efficiency %

l/min 0.11

Water Droplets Units

Leak Test Acceptable

Yes

%

No

Run 1

Detection Limit 0.8

%

Pre-Sampling Leak Rate

l/min 23.93

Filter Temperatures

Less than 50% Faded

Run 1

Mean Sampling Rate

0.48

µg/m³

Allowable MU

Maximum Allowable Temperature

Units Run 1

Exit Temperature Acceptable - Yes

Test Conditions Run 1

160

- Yes

Allowable Leak Rate l/min

MU Acceptable

Detection Limit Acceptable

µg/m³

Run 1

Yes

Silica Gel (Concurrent Water Vapour) Units

Isokineticity Acceptable

%

Are Water Droplets Present

Units Run 1

-

-

Isokinetic Variation

-

LEAD: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Isokinetic Criterion Compliance

MU (Concurrent Water Vapour) Units

Yes

Units Run 1

Absorption Efficiency

APPENDIX 2

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Absorption Efficiency Units Run 1

% 100.0

Allowable Isokinetic Range %

Ambient Temperature Recorded?

Yes

Units

°C

Impingers Exit Temperature

90

Post-Sampling Leak Rate l/min

Maximum Filter Temperature

Maximum Temperature Recorded

°C

103.7

10°C

30

CAT-RT (Version BJ)

Page 24 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 55: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

l/min

LEAD: QUALITY ASSURANCE

20.00

APPENDIX 2

Validity of Blank vs ELV

Expected Sampling Rate l/min

Units

There are no deviations associated with the sampling employed.

(PAGE 2 OF 2)

Leak Test Results

0.15

mg/m³ N/A

Pre-Sampling Leak Rate

Post-Sampling Leak Rate l/min 0.05

Blank 1

Allowable Leak Rate l/min 0.40

Units Blank 1

Leak Test Acceptable - Yes

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Allowable Blank

CAT-RT (Version BJ)

Page 25 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:52

Page 56: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

N/A

Run 1

mg/m³ N/A

% N/A

1.00%

L mg/m³

Sensitivity Coefficient

% v/v N/A

mg/m³

2.0

LEAD: MEASUREMENT UNCERTAINTY CALCULATIONS

Uncertainty as a Percentage

0.0001

mg/m³

25.9

mg/m³

% 25.9

%

Measured Quantities

0.69

0.6687

Run 1

No Requirement

Parameter

0.0003

%

% 13.00

≤1%

0.0000

≤1%

Run 1

-

% N/A

Overall MU For O₂ Measurement

Run 1

Tm

uρm

0.00

Units

0.0141

Value

Symbol

uL %

%

0.0000

≤2%% 2.00

kPa 0.5

0.33

Lr

m³0.7051 uVm

Standard uncertainty

APPENDIX 2

Measured Quantities Symbol Run 1

1.0

ρm 100.0

L 0.33

uHm % v/v

-

Hm 0.0

Vm

290.9

% 0.50

N/A

Run 1

UnitsMeasured Quantities

Uncertainty in Result

0.0000

Oxygen Correction Part of MU Budget

Measured Quantities Units

uLr % -

1.00

Units

Units

≤1%

Requirement of Standard

mg/m³ 0.0003

0.0001

Units

25.9

uTm

Measured Quantities

Vm

mg/m³

1.00Lr mg/m³ 0.0001

%

mg/m³ 0.0003

Symbol

≤2%%

Run 1

13.00

Uncertainty in Measurement Units

mg/m³

Run 1

K

CAT-RT (Version BJ)

Page 26 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 57: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Zero Gas Type

APPENDIX 2

Mass Emission

Concentration

180°C

Span Gas Set Point (ppm) 80.20

1 / 1

0.2±g/hr

TOTAL VOCs (as CARBON): RESULTS SUMMARY

0.43

CAT-TP-20

Mean

Standard

15/07/2020

Uncertainty

Value

Span Gas Reference Number

Sample Point I.D.'s

mg/m³

0.46

Span Gas Uncertainty (%)

Honeywell International Technologies Ltd, Unit 328

80.2

0.1 0.1

Heated Line Temperature

1.0187

Span Gas Start Pressure (bar) 100

Gas Cylinder Concentration (ppm)

g/hr

A1

Number of Sampling Points Used 1 / 1

Uncertainty ±mg/m³ 0.46

N/A

Yes

Synthetic Air (5 Grade)

Number of Sampling Lines Used

0.2

Parameter

0.43

Units Run 1

Span Gas Expiry Date

A2-2 Abrasive Extraction

Parameter

Probe Material Stainless Steel

Filtration Type / Size 0.1µm Glass Fibre

Heated Head Filter Used

EN 12619:2013

Technical Procedure

Span Gas Type Propane In Synthetic Air (5 Grade)

CAT-RT (Version BJ)

Page 27 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 58: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Graphical Trend of Data

COVER ME WITH CHART/S

APPENDIX 2

TOTAL VOCs (as CARBON): DATA TREND

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

12

:40

12

:41

12

:42

12

:43

12

:44

12

:45

12

:46

12

:47

12

:48

12

:49

12

:50

12

:51

12

:52

12

:53

12

:54

12

:55

12

:56

12

:57

12

:58

12

:59

13

:00

13

:01

13

:02

13

:03

13

:04

13

:05

13

:06

13

:07

13

:08

13

:09

13

:10

Co

nce

ntr

atio

n (

mg/

m³)

Total VOCs At Reference Conditions

- Run 1

CAT-RT (Version BJ)

Page 28 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sampling Details

Quality Assurance

Zero Drift 0 0 0

Zero Drift 0 0 0

Zero Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Method Deviations

1

x

- - -

- - -

- - -

- - -

- - -

Span Down Sampling Line (Pre) ppm

Zero Drift Acceptable

Span Down Sampling Line (Post)

12:40 - 13:10

Zero Down Sampling Line (Pre)

Run 1

TOTAL VOCs (as CARBON): SAMPLING DETAILS & QUALITY ASSURANCE

Span Gas Value

CA

L 2

0.10ppm

ppm

Span Drift

ppm 79.90

Zero Down Sampling Line (Post) ppm

ppm

Zero Drift

Zero Down Sampling Line (Pre)

Instrument Range ppm 100

0.00

Zero Down Sampling Line (Post)

Span Down Sampling Line (Pre)

80.2

Sampling Dates

Units Run 1

Parameter

°C

Run Number

± ppm 4.01

Yes-

ppm

Units

ppm

Sampling Times -

ppm

Zero Down Sampling Line (Post) ppm

ppm 0.10

0.10

Allowable Span Drift

CA

L 1

08/12/2015

ppm

ppm 79.80

Nature of Deviation

(x = deviation applies to the associated run)

ppm

Test Conditions

Allowable Zero Drift

ppm

Span Down Sampling Line (Post) ppm

ppm

ppm

Span Down Sampling Line (Pre)

Span Down Sampling Line (Post)

Span Drift Acceptable

APPENDIX 2C

AL

3

± ppm

Run 1

There are no deviations associated with the sampling employed.

Run Ambient Temperature Range 10 - 15

Units Run 1

Zero Down Sampling Line (Pre)

CA

L 3

Units

4.01

CA

L 2

CA

L 1

- Yes

-

ppm

CAT-RT (Version BJ)

Page 29 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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k =

% full scale

Volume or pressure flow dependence 1.60

0.13

% of full scale

Atmospheric pressure dependence 0.30

% full scale/10K

% of value

Uncertainty of calibration gas 2.00

% full scale

Conversion 1.61

mg/m³

Standard deviation of repeatability at span level 0.00

mg/m³

Drift 0.09

30

% of value/kPa

Ambient temperature dependence 1.40

mg/m³

Dependence on voltage 0.06

seconds

Number of readings in measurement

0.50

mg/m³

Combined interference (from MCERTS Certificate) 0.04

-

N/A

% full scale

Span drift

Requirement for SRM is that Uncertainty should be <15% of the value at the ELV, on a dry gas basis, or if O₂ correction is applied less than 15% + the uncertainty

associated with the O₂ correction (using sqrt of sum squares to add uncertainty components). Ref EA TGN M2.

Measured concentration

TGN M2 Allowable MU

Limit value

Expanded uncertainty 1.96 0.47 mg/m³

Uncertainty corrected to std conds. (O₂) 0.47 mg/m³ (REF)

RUN 1 Units

Expanded uncertainty (no O₂) - at 95% Confidence 105.92

% range

Dependence on voltage 0.50 % full scale/10V

Losses in the line (leak)

-

Repeatability at zero 2.00

Range Used 100.0

Performance characteristics RUN 1

0.45

% of Value

mg/m³

mg/m³

Losses in the line (leak) 0.00

RUN 1 Units

Measurement uncertainty

0.20

mg/m³

Expanded uncertainty (with O₂) - at 95% Confidence

Result 0.44 mg/m³

Combined uncertainty 0.24

mg/m³

Performance characteristics

mg/m³

Uncertainty of calibration gas 0.01

Atmospheric pressure dependence 0.01 mg/m³

% of value

Repeatability at span level 0.00 % full scale

Deviation from linearity 0.17 % of value

Zero drift 0.13

Units

-

ppm

Range Used [A]

TOTAL VOCs (as CARBON): MEASUREMENT UNCERTAINTY CALCULATIONS

160.6

RUN 1 Units

Standard deviation of repeatability at zero

mg/m³

Lower of [A] or [B]

Expanded uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A -

Lack of fit 0.01

RUN 1 Units

% of Value

Expanded uncertainty (no O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (no O₂) - at 95% Confidence N/A

0.44 mg/m³ (STP, dry)

mg/m³ (REF)

15.0

APPENDIX 2

% at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A

Ambient temperature dependence

mg/m³

Cal gas conc. 80.2 ppm

use rep at span

Performance characteristic

RUN 1 Units

Response time 45

mg/m³

Combined interference

mg/m³

Volume or pressure flow dependence 0.00 mg/m³

15.0 mg/m³

Cal gas conc. 128.8

%

ppm to mg/m³

MCERTS Range [B] 15.0

CAT-RT (Version BJ)

Page 30 of 30

Honeywell International Technologies Ltd

Unit 328

A2-2 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 61: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279

Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Stack Emissions Testing Report Commissioned by

8th December 2015

Job Reference Number

CDU-0559

Installation Name & Address

Report Written by

Patrick O'Brien

5th January 2016Report Date

TE1 TE2 TE3 TE4

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Version 1

MM 08 922MCERTS Level 2

Team Leader

Team Leader

TE1 TE2 TE3 TE4MM 08 922

MCERTS Level 2

Patrick O'Brien

Report Approved by

Dates of the Monitoring Campaign

Version

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24T: +353 86 853 8247

E: [email protected] Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

WaterfordCork Road Industrial Park

Honeywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-3 Abrasive Extraction

DELETE & COVER ME

CAT-RT (Version BJ)

CDU-0559 Honeywell Int Technology A2-3 (POST)

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TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

4

7

7

CONTENTS

2

9

3

5

6

8

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the written

approval of Exova Catalyst Ireland.

The testing performed fully meets the technical requirements in Irish EPA

Guidance Note, AG2.

CAT-RT (Version BJ)

Page 2 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 63: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

Honeywell International Technologies Ltd, Unit 328

A2-3 Abrasive Extraction

8th December 2015

(Page 1 of 7)

MONITORING OBJECTIVES

Executive Summary

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd

to carry out stack emissions testing on the A2-3 Abrasive Extraction at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

Antimony, Lead, Total VOCs (as Carbon)

CAT-RT (Version BJ)

Page 3 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 64: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

where MU = Measurement Uncertainty associated with the Result

Parameter

Antimony ¹ < <

Lead ¹ - -

Total VOCs (as Carbon) ¹ - -

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

0.46

(Page 2 of 7)

°C

Volumetric Flow Rate (ACTUAL)

0.27

0.76

464

m³/hrVolumetric Flow Rate (REF)

- g/hr

0.81

0.20

m³/hr

0.46

1.68

424 400

% v/v

m/s

0.09

22.0

mg/m³

0.0007

Units

mg/m³

-

Result LimitMU

A2-3 Abrasive Extraction

0.0010mg/m³ g/hr

-

0.00028

Executive Summary

Mass Emission

-

MONITORING RESULTS

438

-

0.0004

0.0016 0.00042 - g/hr

Honeywell International Technologies Ltd, Unit 328

8th December 2015

+/-

Units Result

Concentration

MULimit

+/-

0.0007

0.0004

-

-

CAT-RT (Version BJ)

Page 4 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Parameter

R1 < <

R1 - -

R1 - -

R1

All results are expressed at the respective reference conditions.

Total VOCs (as Carbon) 0.46 08/12/2015 3012:00 - 12:300.20

08/12/20150.0010

32

32

mg/m³ 0.0016

mins

0.0004

12:00 - 12:3008/12/2015

mg/m³ 12:00 - 12:30

0.0007

g/hr

Honeywell International Technologies Ltd, Unit 328

Duration

Executive Summary

Sampling

Times

Units

(Page 3 of 7)

MONITORING DATE(S) & TIMES

A2-3 Abrasive Extraction

8th December 2015

Units Concentration Sampling

Velocity & Volumetric Flow Rate

g/hrmg/m³

08/12/2015 11:50 - 11:55

Date(s)

Mass Emission

Antimony

g/hrLead

CAT-RT (Version BJ)

Page 5 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Standard Operating Conditions

Normal Operation

Abatement System

Abatement System Running Status

A2-3 Abrasive Extraction

8th December 2015

(Page 4 of 7)

Executive Summary

PROCESS DETAILS

Parameter

On

ContinuousContinuous or Batch Process

Plume Appearance

Bag Filter

Not Visible

Value

Process Status

Honeywell International Technologies Ltd, Unit 328

CAT-RT (Version BJ)

Page 6 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 67: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

8th December 2015

Honeywell International Technologies Ltd, Unit 328

MONITORING & ANALYTICAL METHODS

Executive Summary

(with short name reference as appears in the table above)

RPS Laboratories Ltd (RPS)

ANALYSIS LABORATORIES

All There are no deviations associated with the sampling employed.

Yes RPS

CAT Yes RPS

Total VOCs (as Carbon)

EN 16911-1 (MID) CAT-TP-41

Run

SUMMARY OF SAMPLING DEVIATIONS

Parameter

Velocity & Vol. Flow Rate

Deviation

(Page 5 of 7)

Testing Analysis

Lead

(Average)

ISO

Flame Ionisation Detection by Sick 3006 FID

A2-3 Abrasive Extraction

Standard

Lab

Yes

MCERTS

17025

Testing

EN 14385

ICP-MS

Testing

EN 14385 CAT-TP-06 Yes

Lab

Monitoring Analysis

0.001 mg/m³

Procedure

Analytical

Technique

AnalyticalTechnical ISOParameter

ICP-MSCAT Yes Yes

Procedure

LOD

0.16 mg/m³CAT-TP-20

CAT YesWater Vapour

0.001 mg/m³

Antimony

CAT-TP-06

Yes 1.2 m/s

ISO 17025 Accreditation Number: 0605

CAT

All

EN 12619:2013

YesCAT-TP-05 YesEN 14790

Pitot Tube and Thermocouple

YesCAT

GravimetricCAT-TP-05

Yes

CAT

Yes

0.1 % v/v

M31

M31

17025 Analysis

CAT-RT (Version BJ)

Page 7 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 68: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

Hole

-

Lowest Differential Pressure

Value

Highest Gas Velocity

Area

Yes

0.00 0.00

-

-

0.00

-0.81

Value

Depth

0.92

-

2

0.00Ratio of Above : 1 Yes

< 15°

< 3 : 1

-

No

-

Yes

Yes

m

Lowest Gas Velocity

m/s

Yes

-

0.78

-

-

Required

-

0.16

-

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

-

-

-

Yes

Traverse 1

m/s

Easy Access Available

-

Vertical

Yes

Parameter

There are no obstructions present which hamper insertion of sampling equipment

Sample Port Size

Circular

Value

(Page 6 of 7)

Port Depth

-

There is no requirement to perform a BS EN 15259 Homogeneity Test on this Stack.

0.5

1.18

°

-

--

Width

Compliant

0

Units

-

-

m

All platforms should be designed in accordance with the requirements in the Environment Agency's Technical Guidance Note M1

and EN 15259.

Permanent / Temporary Platform

Inside / Outside

Yes

SUITABILITY OF SAMPLING LOCATION

General Platform Information

Units

-

On Roof

-

-

Mean Velocity

Outside

Criteria in EN 15259 -

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

0.45

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

Yes

-

-

-

-

-

--m/s

Maximum Angle of Swirl

Executive Summary

cm

Yes

Safe Access Available

-

-

- -

No Local Negative Flow

Platform has vertical base boards (approx. 0.25m high)

> 5 Pa

CAT-RT (Version BJ)

Page 8 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Photo 2

Photo 3

SAMPLE POINTS

Executive Summary

PLANT PHOTOS

(Page 7 of 7)

Photo 1

Photo 4

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

Line A

A1

A4

A3

A2

CAT-RT (Version BJ)

Page 9 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDIX CONTENTS

APPENDICES

CAT-RT (Version BJ)

Page 10 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Page 71: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

-

S-Pitot (1)

L-Pitot

-

Equipment I.D.

-

Position

Equipment I.D.

Digital Manometer (1)SELECT Horiba Model (1)

Oven Box (2)

-

CAT 14.53

Name

CAT-TP-06

CAT-TP-06

CAT-TP-20

CAT-TP-05

EN 12619:2013

CAT 20.71

15m Heated Line (1)

CAT 17.24

Equipment Type

Technical Endorsements

Team Leader Patrick O'Brien MCERTS Level 2

Extractive Sampling

LIST OF EQUIPMENT

MCERTS Accreditation

Single Channel Heater Controller

S-Pitot (2) -

Heated Probe (3) -

CAT 6.44

Control Box DGM (2)

-

ABB AO2020-URAS26

Stack Thermocouple (3)

Stack Thermocouple (2)

-

-

CAT 12.53

CAT 3.59

-

-

-

Umbilical (2) Servomex 5200MP

Oven Box (1)

-

CAT 4.467

Mass View (2)

-

Laboratory Balance CAT 1.18 / 1.18a

Tape Measure CAT 16.35

EN 16911-1 (MID) CAT-TP-41

Mass Flow Controller (2) CAT 6.45

Mass View (1) -

20m Heated Line (2)

Parameter

Bernath 3006 FID CAT 8.15

Water Vapour

Total VOCs (as Carbon)

CAT 5.52 1m Heated Line (2)

EN 14790

-

EN 14385

EN 14385

Mass Flow Controller (1)

CAT 23.26

-

Antimony

Lead

CAT 11.61

SELECT Logger 2 -

Dual Channel Heater Controller CAT 3.81Kg Check Weight CAT 17.24

Last Impinger Arm CAT 4.404

Callipers

- 20m Heated Line (1)

-

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

Equipment Type

SELECT Logger 1

1m Heated Line (1)

-

Technical ProcedureStandard

Heated Probe (1)

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

Equipment I.D.

-

-

SELECT Gas Conditioning

CAT 13.27

Instrumental Analysers

Stopwatch

CAT 3.73

Equipment Type

-

Miscellaneous Items

Heated Probe (2)

-

-

CAT 3.59

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

5m Heated Line (1) CAT 20.62

500g Check Weight

SELECT Heated Head 1m Heated Line (3)

Control Box DGM (1)

CAT 3.73-

-

CAT 21.S42

Stack Thermocouple (1)

Gasmet Sampling System-

CAT 7.23

MM 08 922 TE1 TE2 TE3 TE4

Technician James Magann MCERTS Level 1 MM 15 1330 None

MCERTS Number

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

Eco Physics CLD 822Mh

Velocity & Vol. Flow Rate

Bioaerosols Temperature Logger -

Electronic Refrigerator -

CAT-RT (Version BJ)

Page 11 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

0.0

Gas Volumetric Flowrate (Actual)

Result

1.96

-

-

0.2080

m³/hr

REF ¹

1.17

Dry Density (Actual), P Actual

m³/hr

-

1.43 0.297-

Units

-

1.25

44.01

417

Gas Volumetric Flowrate REF ¹

%

0.80

kg/m³

Gas Volumetric Flowrate (STP, Wet)

Moisture

Conc

0.0012

Pa

0.06

22.0

100.0

% v/v

Units

p pi

Mass

Component

m³/hr

Result

°C

kg/m³

0.7914 28.01

1.68

kg/m³ 1.28

Duct gas flow conditions

424

464

1.18

0.989

1.29

77.81

Dry Density (STP), P STD

18.02

Determinand

0.0006

424

kg/m³

kPa

0.0168

20.45

Wet Density (STP), P STW

-

101.3

Temperature

N₂

-

Units

Average Pitot Tube Calibration Coefficient, Cp

ppm kg/m³

Average Stack Gas Pressure

Conc

1.68

Conc

M

Wet

r% v/v

kg/m³

m³/hr

Total Pressure

Average Wet Density (Actual), P ActualW

1.68

79.14

Fraction

Density

Dry

0.014

20.80 32.00

Actual

0.06

Volume

0.6

Molar Conc

0.16Stack Area, A

APPENDIX 2

mStack Width, W

22.0

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

kPa

0.84

Value

0.45

100.0

Average Stack Gas Temperature, Ta

0.000

-

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

Average Stack Static Pressure, Pstatic kPa

°C

Stack Diameter / Depth, D

Gas Volumetric Flowrate (from Traverse)

Gas Volumetric Flowrate (STP, Dry)

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

--

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

---

-

-

- -

-

1.169

0.92

22.0

-

- -

-

--

-

-

-

-

-

-

-

-

-

-

-

- - -

-

-

-

-

-

-

- -

-

-

2.0

-

-Mean

-

-

0.11

-

-

22.0

0.5

0.6 -

0.78

- -

22.0

- -

- --

-

- -

-

Pass

-

1.169

m

0.031

1.169

22.00.34

--

2.0

°

0.7

-°C

0.3

0.5

3

0.78

kg/m³Point -

4

-

22.0

0.5

2.0

1.169

m/sPa

Traverse Depth

-

Velocity

Units

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

-

(1 of 1)

1

-Swirl

No

kPa

-

-

-

-

Vertical

Pass

STATIC (Units: Pa)

Value

∆P -

-

-

100.0

2

0.42

Temp

-

-

2.00.78

0.81

-

11:50 - 11:55

Sampling Line A

1

08/12/2015

Value

-

Units

0 -

Pass

-

-

Wet Density

Pa 0.84

S-Type Pitot with KIMO MP 200 (500Pa)

1.169

CAT-RT (Version BJ)

Page 13 of 30

Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Uc,rel(qV,w) 94.25 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

Performance characteristics (Uncertainty Components)

Standard uncertainty associated with the mean velocity (95% Confidence)

Standard uncertainty associated with the mean velocity (95% Confidence), relative

Standard uncertainty associated with the volume flow rate (95% Confidence)

%

Uc(qV,w)

0.23125

- 49878

- 223.3

UnitsValueUncertainty

0.00053

-

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

- Resolution

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

Standard uncertainty associated with the molar mass of the gas

- φO₂,w

u(pstat) 1.042

u(ρ) 0.00631 -

u(vi) 0.777 Pa

u(v) 0.390 m/s

Uc(v) 0.764 m/s

Uc,rel(v) 94.14

u(φH₂O) 0.086

u(φO₂,w) 0.626

K

u(pc) 175.695 Pa

u(patm) 175.692

- φCO₂,w

- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

u(φCO₂,d) 0.002

u(cal) 0.000

u(drift) 0.083

u(fit) 0.002

u(Cf)

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

0.086

u(M) 0.00003

u(Tc) 1.505

1.042

- u²(qV,w)

- u(qV,w)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

20.450

- 0.059

u(φO₂,d) 0.637

u(φCO₂,w) 0.002

- u²(a)/a²

- u²(qV,w)/q²V,w

-

437.7 m³/hr

Pa

u(res) 0.00087

CAT-RT (Version BJ)

Page 14 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Yes

Standard EN 14385

Technical Procedure CAT-TP-06

Filter Size and Material 47mm Quartz Fibre

Concentration mg/m³ 0.0010

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure M31

ISO 17025 Accredited Analysis?

Honeywell International Technologies Ltd, Unit 328

0.09

0.0

NOTE: Where the maximum Blank concentration is higher than the Sample concentration, the Blank concentration has been reported.

Parameter Units Run 1 Mean

Water Vapour % v/v 1.68

APPENDIX 2

Impinger Material

Mass Emission g/hr 0.0

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter

1.68

Uncertainty ±% v/v 0.09

Date of Sample Analysis 17/12/2015

Out Stack

0.0010

Parameter Value

Probe Material

Units Run 1 Mean

Concentration mg/m³ 0.0010 0.0010

Titanium

Filter Housing Material Borosilicate Glass

0.0

Uncertainty ±g/hr 0.0

ANTIMONY: RESULTS SUMMARY

A2-3 Abrasive Extraction

Parameter

0.0003

Sample Point I.D.'s

0.0003Uncertainty ±mg/m³

MaximumUnits Blank 1

A1, A2, A3 & A4

Parameter

Number of Sampling Lines Used 1 / 1

Number of Sampling Points Used 4 / 4

CAT-RT (Version BJ)

Page 15 of 30

Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 76: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

N₂ % v/v 79.14

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂) g/gmol

Units Run 1

g

Barometric pressure, Pb mmHg

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) - N/A

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

Total mass collected in impingers (liquid trap) g -1.7

% v/v 1.68

Vmstw = (Vmstd)(100/(100 - Rwv))

10.4

Test

750.0

N/A

0.6334

Total % v/v 20.86

Stack static pressure, Pstatic mmH₂O 0.0

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0168

m³ 0.0108

Volume of gas sample through gas meter, Vm

Ps = (Pb + (Pstatic / 13.6) mmHg 750.0

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) - No

% wet oxygen measured in gas stream, ACT%O₂w % v/v

- N/A

54.0

% oxygen reference condition, REF%O₂ % v/v N/A

% dry oxygen measured in gas stream, ACT%O₂d % v/v N/A

% v/v 0.06

% v/v 20.80

0.6442

g 8.7

- 1.0180

Average pressure drop across orifice, ∆H mmH₂O

Average dry gas meter temperature, Tm °C 15.7

Total mass collected in impingers (silica trap)

APPENDIX 2

ANTIMONY: ISOKINETIC SAMPLING CALCULATIONS

Velocity pressure coefficient, Cp - 0.84

Average of velocity heads, ∆Pavg mmH₂O 0.50

Total mass of liquid collected, Vlc

Vwstd = (0.001246)(Vlc)

% v/v 1.68

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

m³ 0.6632

Gas meter correction factor, Yd

28.84

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol 28.66

Pitot tube velocity constant, Kp - 34.97

Area of stack, As m² 0.16

Qa = (60)(As)(Vs) m³/min 23.2

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw) m³/min N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Average square root of velocity heads, √∆P √mmH₂O 0.71

Average stack gas temperature, Ts °C 22.0

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 2.43

Conversion factor (K/mm.Hg), Cf - 0.3592

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273) m³/min 21.2

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 20.9

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 98.1

Nozzle diameter, Dn mm 14.00

Nozzle area, An mm² 153.96

Total sampling time, q min 32

CAT-RT (Version BJ)

Page 16 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 77: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<Reported Concentration mg/m³ 0.0010

APPENDIX 2

ANTIMONY: SAMPLING DETAILS

Parameter Units Run 1

Volume Sampled (REF) m³ 0.6442

Mass on Filter / in Rinse µg 0.60

Sampling Times - 12:00 - 12:30

Sampling Dates - 08/12/2015

Sampling Device - ISO

Total Mass Collected µg 0.66

Mass in Front Impingers µg 0.04

µg 0.02

Parameter Units Blank 1

Blank Dates - 08/12/2015

Average Volume Sampled (REF) m³ 0.6442

Calculated Concentration mg/m³ 0.0010

Total Mass Collected µg 0.66

Reported Concentration mg/m³ 0.0010

Mass on Filter / in Rinse µg 0.60

Mass in Front Impingers µg 0.04

µg 0.02

Calculated Concentration mg/m³ 0.0010

CAT-RT (Version BJ)

Page 17 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

YesDetection Limit Acceptable

Allowable Detection Limit

-

µg/m³ 5

Pre-Sampling Leak Rate l/min 0.11

Post-Sampling Leak Rate l/min 0.05

Allowable Absorption Efficiency % 90

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Mean Sampling Rate l/min 21.10

Detection Limit µg/m³ 1.0

Leak Test Acceptable - Yes

Absorption Efficiency Units Run 1

Absorption Efficiency % 100.0

Measurement Uncertainty (MU) % 5.4

Allowable MU % 20

Allowable Leak Rate l/min 0.42

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Water Droplets Units Run 1

Are Water Droplets Present - No

MU (Concurrent Water Vapour) Units Run 1

Yes

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 98.1

Maximum Filter Temperature °C 160

Impingers Exit Temperature Units Run 1

MU Acceptable % Yes

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded %

Allowable Isokinetic Range % 95 - 115

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Test Conditions Units Run 1

Ambient Temperature Recorded? - Yes

Maximum Temperature Recorded °C 10

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable - Yes

CAT-RT (Version BJ)

Page 18 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

APPENDIX 2

ANTIMONY: QUALITY ASSURANCE(PAGE 2 OF 2)

Leak Test Results Units Blank 1

l/min 0.40

Leak Test Acceptable - Yes

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

Pre-Sampling Leak Rate l/min 0.15

Post-Sampling Leak Rate l/min 0.05

Allowable Leak Rate

Validity of Blank vs ELV Units Blank 1

Allowable Blank mg/m³ N/A

Blank Acceptable - N/A

Nature of Deviation Run Number

Expected Sampling Rate l/min 20.00

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Page 80: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

APPENDIX 2

K 2.0

uρm kPa 0.5

Units

mg/m³ 0.0003

mg/m³ N/A

% 27.9

% 27.9

% 27.9

% N/A

Parameter Units Run 1

mg/m³ 0.0001

mg/m³ 0.0003

mg/m³ 0.0003

≤1%

Measured Quantities Units

Measured Quantities

ρm 100.0

Run 1

Run 1

% 0.50

% 14.00

≤1%

Overall MU For O₂ Measurement

1.000.0001

%

% N/A

Units Run 1

%

Uncertainty in Measurement Units

% v/v

uVm m³ 0.0133

Tm 288.7 uTm

Run 1

Oxygen Correction Part of MU Budget

N/A

mg/m³ 0.0000

Symbol

- N/A

Uncertainty in Result

Lr mg/m³

Units Run 1

Uncertainty as a Percentage

Sensitivity Coefficient

Measured Quantities

Measured Quantities Units Run 1 Requirement of Standard

≤1%

% 2.00 ≤2%

%

mg/m³ 0.0000 1.00

No Requirement

uHm % v/v 1.0

0.00

1.00

L 0.24 uL % -

mg/m³ 0.0000

mg/m³ 0.0001

L

Hm 0.0

Vm m³ 0.6334

% 0.69

Symbol

≤2%

Lr 14.00 uLr % -

ANTIMONY: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

Vm 0.6632

N/A

0.24

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

APPENDIX 2

LEAD: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-3 Abrasive Extraction

Parameter Units Run 1 Mean

Concentration mg/m³ 0.0016 0.0016

Date of Sample Analysis 17/12/2015

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure

Probe Material

Parameter Units Run 1 Mean

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis? Yes

Uncertainty ±mg/m³ 0.0004 0.0004

Mass Emission g/hr 0.0 0.0

Uncertainty ±g/hr 0.0 0.0

1 / 1

Number of Sampling Points Used 4 / 4

Sample Point I.D.'s A1, A2, A3 & A4

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Number of Sampling Lines Used

Water Vapour % v/v 1.68

Concentration mg/m³ 0.0011 0.0011

Titanium

Filter Housing Material Borosilicate Glass

Impinger Material

1.68

Uncertainty ±% v/v 0.09 0.09

Parameter Units Blank 1 Maximum

Parameter Value

CAT-RT (Version BJ)

Page 21 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

For

insp

ectio

n pur

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Page 82: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

Total % v/v 20.86

Pitot tube velocity constant, Kp - 34.97

% v/v 1.68

m³/min

N/A

0.6442

°C

% v/v

Total mass of liquid collected, Vlc g

m³ 0.0108

Volume of gas sample through gas meter, Vm m³

15.7

Average pressure drop across orifice, ∆H

20.80

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³ 0.6334

Average of velocity heads, ∆Pavg mmH₂O

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d) -

Vmstw = (Vmstd)(100/(100 - Rwv))

% wet oxygen measured in gas stream, ACT%O₂w % v/v

0.6632

Gas meter correction factor, Yd - 1.0180

Average dry gas meter temperature, Tm °C

% v/v

Velocity pressure coefficient, Cp -

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

N/A

8.7

Vwstd = (0.001246)(Vlc)

0.50

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 2.43

22.0

0.84

Test Units Run 1

% v/v

Stack static pressure, Pstatic mmH₂O

Barometric pressure, Pb mmHg

1.68

750.0

APPENDIX 2

LEAD: ISOKINETIC SAMPLING CALCULATIONS

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (liquid trap) g -1.7

mmH₂O 54.0

Total mass collected in impingers (silica trap) g 10.4

No

0.0

750.0

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0168

-

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) -

% dry oxygen measured in gas stream, ACT%O₂d

g/gmol 28.84

m³/min

Total sampling time, q min 32

23.2

- 0.3592

Average square root of velocity heads, √∆P √mmH₂O

0.16

N/A

N/A

0.06

Qa = (60)(As)(Vs)

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 98.1

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

Average stack gas temperature, Ts

Area of stack, As m²

153.96

Conversion factor (K/mm.Hg), Cf

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

Nozzle area, An

% oxygen reference condition, REF%O₂ % v/v N/A

m³/min 21.2

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

N₂ % v/v 79.14

Nozzle diameter, Dn mm 14.00

0.71

28.66

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

% v/v

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

m³/min

m³/min N/A

20.9

mm²

N/A

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Sample Runs

-

-

Mass in Back Impinger <

-

-

-

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

-

Mass in Back Impinger <

-

-

-

Reported Concentration mg/m³ 0.0016

Units

0.50

Blank Dates -

Mass in Front Impingers µg

LEAD: SAMPLING DETAILS

Parameter Units

Calculated Concentration mg/m³ 0.0011

0.128

Mass on Filter / in Rinse

m³ 0.6442

08/12/2015

µg 0.19

Mass on Filter / in Rinse µg

Blank 1

Total Mass Collected µg

0.02

1.047

Average Volume Sampled (REF)

0.019µg

- 12:00 - 12:30

Run 1

µg

Calculated Concentration mg/m³ 0.0016

0.6442

APPENDIX 2

Sampling Times

0.900

Volume Sampled (REF) m³

Total Mass Collected

Parameter

Sampling Dates

0.71

ISO

- 08/12/2015

Reported Concentration mg/m³

Mass in Front Impingers

0.0011

µg

Sampling Device -

µg

CAT-RT (Version BJ)

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

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Sample Runs

Yes-

5

Measurement Uncertainty (MU) % 5.4

Allowable Detection Limit

%

20

0.05

95 - 115

Allowable Absorption Efficiency %

l/min 0.11

Yes

%

No

Leak Test Acceptable

µg/m³

Allowable MU

Maximum Allowable Temperature

- Yes

Run 1

Detection Limit 0.9

%

Pre-Sampling Leak Rate

l/min 21.10

Filter Temperatures Units Run 1

Exit Temperature Acceptable - Yes

Test Conditions Run 1

Allowable Leak Rate l/min

MU Acceptable

Detection Limit Acceptable

µg/m³

Run 1

Yes

Silica Gel (Concurrent Water Vapour) Units

Less than 50% Faded

Run 1

Mean Sampling Rate

0.42

Water Droplets Units

Isokineticity Acceptable

%

Are Water Droplets Present

Units Run 1

-

MU (Concurrent Water Vapour) Units

Yes

Units Run 1

-

Impingers Exit Temperature

Isokinetic Criterion Compliance

Isokinetic Variation

-

Absorption Efficiency

APPENDIX 2

LEAD: QUALITY ASSURANCE(PAGE 1 OF 2)

Leak Test Results Units Run 1

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Absorption Efficiency Units Run 1

160

Post-Sampling Leak Rate l/min

% 100.0

Allowable Isokinetic Range %

Ambient Temperature Recorded?

Yes

Units

°C

90

°C

Maximum Filter Temperature

Maximum Temperature Recorded

98.1

10°C

30

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

wx

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

l/min

LEAD: QUALITY ASSURANCE

20.00

APPENDIX 2

Validity of Blank vs ELV

Allowable Leak Rate l/min 0.40

Expected Sampling Rate l/min

Units

There are no deviations associated with the sampling employed.

Blank 1

(PAGE 2 OF 2)

Leak Test Results

0.15

mg/m³ N/A

Pre-Sampling Leak Rate

Post-Sampling Leak Rate l/min 0.05

Units Blank 1

Leak Test Acceptable - Yes

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Allowable Blank

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

mg/m³ N/A

% N/A

N/A

Run 1

1.00%

L mg/m³

Sensitivity Coefficient

% v/v N/A

mg/m³

2.0

LEAD: MEASUREMENT UNCERTAINTY CALCULATIONS

Symbol

≤2%% 2.00

kPa 0.5

Uncertainty as a Percentage

0.0002

mg/m³

25.9

mg/m³

% 25.9

%

Measured Quantities

0.69

0.6334

Run 1

No Requirement

Parameter

0.0133

Value

0.0004

%

% 13.00

≤1%

0.0000

≤1%

Run 1

Tm

Run 1

-

% N/A

Overall MU For O₂ Measurement %

0.0000

uρm

0.00

Units

0.24

Lr

1.00

Measured Quantities Symbol Run 1

1.0

ρm 100.0

-

Hm 0.0

Units

Vm 0.6632 uVm

uL %

uHm % v/v

Standard uncertainty

APPENDIX 2

uLr % -

L 0.24

Requirement of Standard

mg/m³ 0.0004

0.0002

288.7

% 0.50

N/A

Run 1

UnitsMeasured Quantities

Uncertainty in Result

0.0000

Units

Oxygen Correction Part of MU Budget

Measured Quantities Units

Uncertainty in Measurement Units

mg/m³

Run 1

K

Units

≤1%

25.9

uTm

Measured Quantities

Vm

mg/m³

1.00Lr mg/m³ 0.0002

%

mg/m³ 0.0004

Symbol

≤2%%

Run 1

13.00

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

- -

- -

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Zero Gas Type

APPENDIX 2

Mass Emission

Concentration

180°C

Span Gas Set Point (ppm) 80.20

1 / 1

0.3±g/hr

TOTAL VOCs (as CARBON): RESULTS SUMMARY

0.46

CAT-TP-20

Mean

Standard

15/07/2020

Uncertainty

Value

Span Gas Reference Number

Sample Point I.D.'s

mg/m³

0.46

Span Gas Uncertainty (%)

Honeywell International Technologies Ltd, Unit 328

80.2

0.2 0.2

Heated Line Temperature

1.0187

Span Gas Start Pressure (bar) 100

Gas Cylinder Concentration (ppm)

A1

Number of Sampling Points Used 1 / 1

Uncertainty ±mg/m³ 0.46

N/A

Yes

Synthetic Air (5 Grade)

g/hr

Number of Sampling Lines Used

0.3

Parameter

0.46

Units Run 1

Span Gas Expiry Date

A2-3 Abrasive Extraction

Parameter

Heated Head Filter Used

Probe Material Stainless Steel

Filtration Type / Size 0.1µm Glass Fibre

EN 12619:2013

Technical Procedure

Span Gas Type Propane In Synthetic Air (5 Grade)

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Graphical Trend of Data

COVER ME WITH CHART/S

APPENDIX 2

TOTAL VOCs (as CARBON): DATA TREND

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

12

:00

12

:01

12

:02

12

:03

12

:04

12

:05

12

:06

12

:07

12

:08

12

:09

12

:10

12

:11

12

:12

12

:13

12

:14

12

:15

12

:16

12

:17

12

:18

12

:19

12

:20

12

:21

12

:22

12

:23

12

:24

12

:25

12

:26

12

:27

12

:28

12

:29

12

:30

Co

nce

ntr

atio

n (

mg/

m³)

Total VOCs At Reference Conditions

- Run 1

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Sampling Details

Quality Assurance

Zero Drift 0 0 0

Zero Drift 0 0 0

Zero Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Span Drift 0 0 0

Method Deviations

1

x

- - -

- - -

- - -

- - -

- - -

Span Down Sampling Line (Pre) ppm

Zero Drift Acceptable

Span Down Sampling Line (Post)

12:00 - 12:30

80.2

Zero Down Sampling Line (Pre)

Run 1

TOTAL VOCs (as CARBON): SAMPLING DETAILS & QUALITY ASSURANCE

Span Gas Value

CA

L 2

ppm 79.90

Zero Down Sampling Line (Post) ppm

0.10ppm

Span Down Sampling Line (Pre)

Span Down Sampling Line (Pre)

ppm

Span Drift

Span Down Sampling Line (Post)

ppm

Zero Drift

Zero Down Sampling Line (Pre)

Instrument Range ppm 100

0.00

Span Drift Acceptable

Allowable Span Drift

Sampling Dates

Units Run 1

Parameter

°C

Run Number

± ppm 4.01

Yes-

ppm

Units

ppm

Sampling Times -

ppm

Zero Down Sampling Line (Post) ppm

ppm 0.10

0.10

CA

L 1

08/12/2015

ppm

ppm 79.80

Nature of Deviation

(x = deviation applies to the associated run)

ppm

Test Conditions

CA

L 3

Units

4.01Allowable Zero Drift

ppm

Span Down Sampling Line (Post) ppm

Zero Down Sampling Line (Post)

ppm

ppm

Run 1

There are no deviations associated with the sampling employed.

Run Ambient Temperature Range 10 - 15

Units Run 1

Zero Down Sampling Line (Pre)

APPENDIX 2C

AL

3

± ppm

CA

L 2

CA

L 1

- Yes

-

ppm

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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k =

% of value/kPa

Ambient temperature dependence 1.40

mg/m³

Dependence on voltage 0.06

seconds

Number of readings in measurement

% full scale

Volume or pressure flow dependence 1.60

mg/m³

Combined interference (from MCERTS Certificate) 0.04

-

N/A

% full scale

Conversion 1.61

mg/m³

Standard deviation of repeatability at span level 0.00

mg/m³

Drift 0.09

30

0.13

% of full scale

Atmospheric pressure dependence 0.30

% full scale/10K

Requirement for SRM is that Uncertainty should be <15% of the value at the ELV, on a dry gas basis, or if O₂ correction is applied less than 15% + the uncertainty

associated with the O₂ correction (using sqrt of sum squares to add uncertainty components). Ref EA TGN M2.

Measured concentration

TGN M2 Allowable MU

Limit value

Expanded uncertainty 1.96 0.47 mg/m³

Uncertainty corrected to std conds. (O₂) 0.47 mg/m³ (REF)

RUN 1 Units

Expanded uncertainty (no O₂) - at 95% Confidence 99.28

% range

Dependence on voltage 0.50 % full scale/10V

Losses in the line (leak) 0.50 % of value

Uncertainty of calibration gas 2.00 % of value

Repeatability at span level 0.00 % full scale

Deviation from linearity 0.17 % of value

Zero drift 0.13 % full scale

Span drift

-

Repeatability at zero 2.00

Range Used 100.0

Performance characteristics RUN 1

0.45

% of Value

mg/m³

mg/m³

Losses in the line (leak) 0.00

RUN 1 Units

Measurement uncertainty

0.20

mg/m³

Expanded uncertainty (with O₂) - at 95% Confidence

Result 0.47 mg/m³

Combined uncertainty 0.24

mg/m³ (REF)

15.0

mg/m³

Performance characteristics

mg/m³

Uncertainty of calibration gas 0.01

Atmospheric pressure dependence 0.01 mg/m³

APPENDIX 2

Units

-

ppm

Range Used [A]

TOTAL VOCs (as CARBON): MEASUREMENT UNCERTAINTY CALCULATIONS

160.6

RUN 1 Units

Standard deviation of repeatability at zero

mg/m³

Lower of [A] or [B]

Expanded uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (with O₂) - at 95% Confidence N/A % at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A -

Lack of fit 0.01

RUN 1 Units

% of Value

Expanded uncertainty (no O₂) - at 95% Confidence N/A % at ELV

Overall Allowable uncertainty (no O₂) - at 95% Confidence N/A

%

0.47 mg/m³ (STP, dry)

% at ELV

Result of Compliance with Uncertainty Requirement in M2 N/A

Ambient temperature dependence

mg/m³

Cal gas conc. 80.2 ppm

use rep at span

Performance characteristic

RUN 1 Units

Response time 45

15.0 mg/m³

Cal gas conc. 128.8

mg/m³

Combined interference

mg/m³

Volume or pressure flow dependence 0.00 mg/m³

ppm to mg/m³

MCERTS Range [B] 15.0

CAT-RT (Version BJ)

Page 30 of 30

Honeywell International Technologies Ltd

Unit 328

A2-3 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 8th December 2015

Irish EPA IPPC Licence: P0698-01

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Page 91: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279

Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Report Written by

Piotr Nadany

23rd November 2015

Report Date

TE1 TE2 TE3 TE4

TE1 TE2 TE3 TE4

MM 07 881

MCERTS Level 2

Piotr Nadany

Report Approved by

Stack Emissions Testing Report Commissioned by

29th 30th October 2015

Job Reference Number

CDU-0559

Installation Name & Address

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Version 1

MM 07 881

MCERTS Level 2

Team Leader

Team Leader

Dates of the Monitoring Campaign

Version

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24

T: +353 86 853 8247

E: [email protected]

Your Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

Waterford

Cork Road Industrial Park

Honeywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-4 Abrasive Extraction

CAT-RT (Version BJ)

CDU-0559 A2-4 Abrasive Extraction Honeywell International Technlogies (Report)

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Page 92: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

4

7

7

CONTENTS

2

9

3

5

6

8

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the

written approval of Exova Catalyst Ireland.

The testing performed fully meets the technical requirements in Irish EPA

Guidance Note, AG2.

CAT-RT (Version BJ)

Page 2 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 93: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

A2-4 Abrasive Extraction

29th 30th October 2015

Honeywell International Technologies Ltd, Unit 328

(Page 1 of 7)

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd to carry out stack emissions testing on the

A2-4 Abrasive Extraction at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

Total Particulate Matter, Iron, Titanium

MONITORING OBJECTIVES

Executive Summary

CAT-RT (Version BJ)

Page 3 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 94: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

where MU = Measurement Uncertainty associated with the Result

Parameter

Total Particulate Matter ¹

Iron ¹ - -

Titanium ¹ < <

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

°C

Volumetric Flow Rate (ACTUAL)

(Page 2 of 7)

Volumetric Flow Rate (REF)

0.47

9904

m³/hr

m/s

% v/v

9.55

m³/hr

Executive Summary

Mass Emission

-

30.47

MONITORING RESULTS

A2-4 Abrasive Extraction

0.05mg/m³ g/hr

-

31

0.010

Units

mg/m³

mg/m³

-

5.77

Result

0.02 0.004 - g/hr

Honeywell International Technologies Ltd, Unit 328

29th 30th October 2015

g/hr 4.60.59

+/-

Units Result

Concentration

MULimit

+/-

Limit

0.1

660

0.46

0.19

0.1

21.1

1.40

9797 653 15000

0.0

MU

-

CAT-RT (Version BJ)

Page 4 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 95: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Parameter

R1 - -

R1 - -

R1 < <

R1

All results are expressed at the respective reference conditions.

0.05 29/10/2015

mg/m³

mins

0.02 30

30

mg/m³

10:10 - 11:13

g/hr

09:00 - 10:0229/10/2015

mg/m³ 09:00 - 10:02

0.19

0.46

Units Concentration

29/10/2015

Sampling

5.77

MONITORING DATE(S) & TIMES

A2-4 Abrasive Extraction

29th 30th October 2015

(Page 3 of 7)

0.59Total Particulate Matter

Units

Honeywell International Technologies Ltd, Unit 328

60

Duration

Executive Summary

Sampling

Times

29/10/2015 09:05 - 09:15

Date(s)

Mass Emission

g/hr

g/hrTitanium

Iron

Velocity & Volumetric Flow Rate

CAT-RT (Version BJ)

Page 5 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 96: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Standard Operating Conditions

Capacity (of 100%) and Tonnes / Hour

Continuous or Batch Process

N/A

A2-4 Abrasive Extraction

29th 30th October 2015

Normal Operation

Abatement System

Abatement System Running Status

(Page 4 of 7)

PROCESS DETAILS

Parameter

Process Status

Honeywell International Technologies Ltd, Unit 328

N/A

Fuel

Plume Appearance

Bag Filter

Executive Summary

Not Visible

Value

Feedstock (if applicable)

N/A

On

Batch

CAT-RT (Version BJ)

Page 6 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 97: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

29th 30th October 2015

MONITORING & ANALYTICAL METHODS

Velocity & Vol. Flow Rate

Deviation

1 There are no deviations associated with the sampling employed.

Run

SUMMARY OF SAMPLING DEVIATIONS

Parameter

ANALYSIS LABORATORIES(with short name reference as appears in the table above)

Exova Catalyst (CAT)

Technique

Analytical

Yes

Gravimetric

MCERTS

17025

Testing

0.1 mg/m³

EN 14385

ICP-MS

Yes YesTotal Particulate Matter

Honeywell International Technologies Ltd, Unit 328

CAT

(Average)17025 Analysis

EN 16911-1 (MID) CAT-TP-41

CAT Yes RPS

Yes

Executive Summary

TestingProcedure

LOD

CAT-TP-05 YesEN 14790

Yes

GravimetricCAT-TP-05

RPS

EN 13284-1

(Page 5 of 7)

Testing AnalysisISO

A2-4 Abrasive Extraction

EN 14385 CAT-TP-06 Yes

CAT-TP-01 Yes

Lab

YesCAT YesICP-MSTitanium

0.004 mg/m³

Procedure

AnalyticalStandard

Lab

Yes

CAT-TP-06

Yes 1.2 m/s

ISO 17025 Accreditation Number: 4279

ISO 17025 Accreditation Number: 0605

All

Pitot Tube and Thermocouple

CAT 0.1 % v/v

M31

M31

RPS Laboratories Ltd (RPS)

CAT-TP-03

Technical ISOParameter

0.008 mg/m³

Iron

Water Vapour

Monitoring

CAT

Analysis

CAT Yes

CAT

CAT-RT (Version BJ)

Page 7 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 98: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

Lowest Differential Pressure

Value

Hole

-

Highest Gas Velocity

Area

0.00 0.00

-

-

0.00

-Yes

< 3 : 1

-

Platform has chains / self closing gates at top of ladders

-9.55

Value

Depth

10.12

-

15

0.00Ratio of Above : 1 Yes

< 15°

No Local Negative Flow

Platform has vertical base boards (approx. 0.25m high)

> 5 Pa Yes

-

N/A

No

m

Lowest Gas Velocity

m/s

Yes

-

8.83

-

-

Required

-

0.29

-

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

-

-

-

Yes

Traverse 1

m/s

Easy Access Available

-

- -

-

Sample Port Size

There is no requirement to perform a EN 15259 Homogeneity Test on this Stack.

68.6

Rectangular

Value

Safe Access Available

-

Vertical

Yes

Parameter

There are no obstructions present which hamper insertion of sampling equipment

(Page 6 of 7)

Port Depth

On Roof

--

1.15

°

- Yes

0

Permanent / Temporary Platform

Inside / Outside

Width

Compliant

-

-

m

All platforms should be designed in accordance with the requirements in the Environment Agency's Technical Guidance Note M1

and EN 15259.

Units

No

SUITABILITY OF SAMPLING LOCATION

-

Mean Velocity

Outside

General Platform Information

Units

-

No

0.36

-

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

0.80

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

-

-

-

-

--m/s

Maximum Angle of Swirl

Executive Summary

cm

Yes

Criteria in EN 15259

-

CAT-RT (Version BJ)

Page 8 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 99: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Photo 3

Photo 2

SAMPLE POINTS

Executive Summary

PLANT PHOTOS

(Page 7 of 7)

Photo 1

Photo 4

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

Line A Line B

A1

A2

B1

B2

B3 A3

CAT-RT (Version BJ)

Page 9 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 100: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDIX CONTENTS

APPENDICES

CAT-RT (Version BJ)

Page 10 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 101: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

-

S-Pitot (1)

L-Pitot

-

-

CAT 14.53

Name

CAT 25.37

CAT 3.73

Equipment Type

SELECT Horiba Model (1)

Oven Box (2)

ABB AO2020-URAS26

-

-

Laboratory Balance CAT 1.18 / 1.18a

Tape Measure CAT 16.35

Equipment I.D.

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

Stopwatch

Control Box DGM (2)

-

-

Iron

Miscellaneous Items

CAT 7.23

Equipment I.D.

-

Position

Equipment I.D.

CAT 20.71

15m Heated Line (1)

CAT 17.24

CAT-TP-06

CAT-TP-06

Heated Probe (3)

Digital Manometer (1)

-

-

EN 14385

EN 14385

-

JCT JCC P1 Cooler

-

Oven Box (1)

-

CAT 4.467

Mass View (1)

CAT 23.26

Instrumental Analysers

Equipment Type

Technical Endorsements

Team Leader Piotr Nadany MCERTS Level 2

Extractive Sampling

LIST OF EQUIPMENT

MCERTS Accreditation

Single Channel Heater Controller

S-Pitot (2) CAT 21P59

-

-

Umbilical (2) Servomex 5200MP

CAT 25.36

20m Heated Line (2)

Bernath 3006 FID -

CAT-TP-05

CAT 13.27

Mass Flow Controller (1)

Mass View (2)

Stack Thermocouple (3)

Stack Thermocouple (2)

-

-

-

-

CAT 3.62

Parameter

Total Particulate Matter

EN 14790

Titanium

Water Vapour

CAT 5.52 1m Heated Line (2)

-

Easylogger EN-EL-12 Bit -

Dual Channel Heater Controller CAT 3.81Kg Check Weight CAT 17.24

Last Impinger Arm CAT 4.404

Callipers

- 20m Heated Line (1)

-

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

1m Heated Line (3)

EN 16911-1 (MID) CAT-TP-41

Mass Flow Controller (2) -

Velocity & Vol. Flow Rate

Control Box DGM (1)

CAT 3.73-

-

-

Stack Thermocouple (1)

Gasmet Sampling System-

MCERTS Number

Equipment Type

Hioki 5043 (V)

1m Heated Line (1)

-

EN 13284-1

Technical ProcedureStandard

Heated Probe (1)

CAT-TP-01

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

Heated Probe (2)

-

-

CAT 3.59

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

5m Heated Line (1) CAT 20.62

500g Check Weight

M&C PSS

MM07 881 TE1 TE2 TE3 TE4

Technician Donal O Faogain MCERTS Level 1 MM 13 1259 TE1

Eco Physics CLD 822Mh

-

-

-

-

CAT-RT (Version BJ)

Page 11 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 102: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

Moisture

-

1.2498

44.01

9659

Gas Volumetric Flowrate REF ¹

%

0.8037

0.0

m³/hr

101.3

Temperature

N₂

kPa

-

- 0.0140

kg/m³

kg/m³

Gas Volumetric Flowrate (Actual)

Gas Volumetric Flowrate (STP, Wet)

Units

1.40

kg/m³ 1.280

Duct gas flow conditions

9797

9904

1.273

Wet Density (STP), P STW

-

1.40

Total Pressure

Average Wet Density (Actual), P ActualW

1.40

79.14

Determinand

0.0006

9797

1.4277 0.29696

Mass

-

0.2080

m³/hr

REF ¹

1.267

Dry Density (Actual), P Actual

m³/hr

Result

°C

20.51

pi

kg/m³

1.9635

0.7914 28.01

Fraction

% v/v p

-

Units

Result

Dry

0.01129

20.80 32.00

Actual

0.06

Volume

Units

ppm kg/m³

Conc Conc

M

Wet

r% v/v

kg/m³

m³/hr

0.98913

1.287

78.03

Dry Density (STP), P STD

18.02

Conc

0.001180.06

21.1

107.9

Molar Conc

0.29Stack Area, A

APPENDIX 2

mStack Width, W

21.1

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

kPa

kPa

0.85

Value

0.80

107.7

Average Stack Gas Temperature, Ta

0.238

-Average Pitot Tube Calibration Coefficient, Cp

Average Stack Gas Pressure mmH₂O

Component

Stack Diameter / Depth, D

0.36

Density

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

°C

Average Stack Static Pressure, Pstatic

8.2

Gas Volumetric Flowrate (from Traverse)

Gas Volumetric Flowrate (STP, Dry)

CAT-RT (Version BJ)

Page 12 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 103: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

- -

-

---

- -

-

-

-

-

-

-

-

-

-

-

-

-

9.52

1.266

9.02

21.0

21.1

1.267

15.0

-

12.0

12.0

8.2

-

-

-

-

12.09.2

15.0

-

-

-

--

-

-

-

-

-

--

-

-

-

-

- -

-

-

-

- -

-

- - -

-

--

--

-

-

-

-

-

-

-

0.73

-

1.2678.3

-

9.79

1.267

-

12.0

- -

8.83

8.210.12

-

7.5

-

-

- -

21.1

21.0

7.0

8.2

1.266

21.1

9.0

9.68

Mean

9.56

8.4

0.60

-

8.6

1.26621.11.266

21.0 21.0

1.266

12.0

21.10.47

9.96

9.14

9.56

1.267

21.0

0.20

4

kPa

-

Wet Density

-

Swirl

Vertical

Pass

238.0

∆P

-

Value

-

Units

2

238 -

S-Type Pitot with KIMO MP 200 (500Pa)

kg/m³

238.0

14.0

Pass

VelocitySwirl

No

21.1

8.83

1.267

3

6

∆P Temp

Sampling Line B

mmH₂O

-

(1 of 1)

2

m

0.07

Pass

5

21.1

10.12

1

1.266

21.10.33

kg/m³

12.0

°C

14.0

°

8.9

7.3

m/s°C

Depth

-

Velocity

107.7

mmH₂O

Traverse

2

1.267

Temp

-

0.85Pa

1.266

Point °

21.07.0

12.0

1.267

m/s

STATIC (Units: Pa)

--

09:05 - 09:15

Sampling Line A

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

12.0

9.2

10.01

9.59

Wet Density

29/10/2015

Units

APPENDIX 2

Value

CAT-RT (Version BJ)

Page 13 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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0.628

Standard uncertainty associated with the mean velocity (95% Confidence)

Standard uncertainty associated with the mean velocity (95% Confidence), relative

Standard uncertainty associated with the volume flow rate (95% Confidence)

%

Uc(qV,w)

0.00116

u(φO₂,w)

- φCO₂,w

- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

- Resolution

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

Standard uncertainty associated with the molar mass of the gas

- φO₂,w

K

u(pc) 175.695 Pa

u(patm) 175.692

u(pstat) 0.959

u(ρ) 0.00678

- 113497

- 336.9

m/s

Uc(v) 0.468 m/s

Uc,rel(v) 4.90

0.00053

-

660.3 m³/hr

Uc,rel(qV,w) 6.67 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

u(φH₂O) 0.072

-

u(vi) 0.796 Pa

u(v) 0.239

Performance characteristics (Uncertainty Components) UnitsValueUncertainty

u(φCO₂,d) 0.002

u(cal) 0.675

u(drift) 0.083

u(fit) 0.082

u(Cf)

1.357 Pa

u(res) 0.00087

0.840

u(M) 0.00003

u(Tc) 1.500

20.508

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

- u(qV,w)

- 0.059

u(φO₂,d) 0.637

u(φCO₂,w) 0.002

- u²(qV,w)

- u²(a)/a²

- u²(qV,w)/q²V,w

-

CAT-RT (Version BJ)

Page 14 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 105: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Number of Sampling Points Used 6/6

Uncertainty ±mg/m³ 0.47 0.47

Titanium

Filter Housing Material Titanium

Probe Material

Parameter Units

Positioning of Filter

Filter Size and Material

In Stack

Mass Emission

Technical Procedure CAT-TP-01

Number of Sampling Lines Used 2/2

Run 1

Water Vapour

Concentration

Parameter Units

Uncertainty ±g/hr

Honeywell International Technologies Ltd, Unit 328

Mean

1.35

A2-4 Abrasive Extraction

Parameter

Concentration

0.07

Units

0.59

Blank 1

±% v/v

Standard

47mm Glass Fibre

0.37

Parameter

EN 13284-1

Sample Point I.D.'s

1.35

g/hr 5.8

0.07

4.6

Uncertainty

A1, A2, A3, B1, B2 & B3

% v/v

Value

Maximum

mg/m³ 0.37

TOTAL PARTICULATE MATTER: RESULTS SUMMARY

Mean

4.6

APPENDIX 2

5.8

mg/m³ 0.59

Run 1

CAT-RT (Version BJ)

Page 15 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 106: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

g

5.6

APPENDIX 2

Average dry gas meter temperature, Tm °C

Nozzle area, An

1.2457

Velocity pressure coefficient, Cp

% v/v

Average square root of velocity heads, √∆P

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

% v/v 1.35

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100))

Nozzle diameter, Dn

mmH₂O

0.0171

Volume of gas sample through gas meter, Vm m³

Gas meter correction factor, Yd

11.6

79.14

% oxygen reference condition, REF%O₂ % v/v N/A

√mmH₂O

13.7

Vmstw = (Vmstd)(100/(100 - Rwv))

% v/v

18.5

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Total mass of liquid collected, Vlc g

TOTAL PARTICULATE MATTER: ISOKINETIC SAMPLING CALCULATIONS

Test Units

Total mass collected in impingers (liquid trap)

Barometric pressure, Pb

mmH₂O

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w)

0.9450

1.35

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

% v/v

1.2628

g 2.1

-

0.84

m³/min N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min

Stack static pressure, Pstatic

Run 1

m³/min

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps))

Total sampling time, q

98.7

m/s

-

m³/min

0.29

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 153.6

Average of velocity heads, ∆Pavg

-

min 60

% v/v

°C

155.7

%

N/A

Average stack gas temperature, Ts

g/gmol 28.84

mm

39.45

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

Conversion factor (K/mm.Hg), Cf

Bwo = Vwstd / (Vmstd + Vwstd) 0.0135

Total mass collected in impingers (silica trap)

0.3592

Area of stack, As

21.0

8.06

mm²

N₂

- N/A

Average pressure drop across orifice, ∆H

763.2Ps = (Pb + (Pstatic / 13.6) mmHg

-

% wet oxygen measured in gas stream, ACT%O₂w

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100)

N/A

% v/v 20.86

20.80

% v/v

Total

% dry oxygen measured in gas stream, ACT%O₂d

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

1.3950

2.84

mmH₂O

7.09

N/A

Qa = (60)(As)(Vs)

34.97

No

Pitot tube velocity constant, Kp

762.8

0.06

-

g/gmol 28.70

167.0

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

9.66

Vwstd = (0.001246)(Vlc)

mmHg

Vmstd@X%oxygen = (Vmstd) / (O₂REFd)

Velocity of stack gas, Vs

N/A

N/A

-

57.3

% v/v

CAT-RT (Version BJ)

Page 16 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 107: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

Filter I.D. Number

Probe Rinse I.D. Number

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

Filter I.D. Number

Probe Rinse I.D. Number

g

mg

g

29/10/2015

Balance Uncertainty / LOD

0.00009

3.22563

Total Mass Collected

Volume Sampled (REF) m³

Sampling Times

APPENDIX 2

-

Total Mass in Probe Rinse

10:10 - 11:13

3.04691

0.74

Average Volume Sampled (REF)

0.00038

g

Total Mass in Probe Rinse g

-Sampling Dates

End Filter Mass

-

Parameter

End Probe Rinse Mass

Blank 1

Start Filter Mass

Parameter Units

47-28131

1.2628

g

0.00023

-

Balance Uncertainty / LOD

Calculated Concentration

Units

TOTAL PARTICULATE MATTER: SAMPLING DETAILS

g

0.13982

0.14005

g

g

3.22572

-

-

Total Mass Collected

0.37

Start Probe Rinse Mass

0.00051

Sampling Device

PR-47-28131

Start Filter Mass

0.59

mg/m³

Run 1

g

Total Mass on Filter

29/10/2015

Start Probe Rinse Mass

g

47-28136

-

0.14030

Total Mass on Filter

-

Blank Dates

End Filter Mass

End Probe Rinse Mass

mg/m³

g

0.10

mg/m³

mg 0.47

0.10

Calculated Concentration

1.2628

ISO

3.04742

g

0.13992

PR-47-28136

mg/m³

CAT-RT (Version BJ)

Page 17 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:53

Page 108: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

MU (Concurrent Water Vapour)

-

Units Run 1

Leak Test Acceptable

Run 1

Units

Pre-Conditioning Temperature °C

°C

mg/m³ 0.15

Water Droplets

Units Run 1

Test Conditions Units

95 - 115

180

Run 1

Overall Weighing Uncertainty ± mg

20

%

98.7

Weighing Uncertainty Acceptable

Ambient Temperature Recorded? -

Overall Weighing Uncertainty

Less than 50% Faded

Run 1

%

No

Allowable Weighing Uncertainty

Run 1

0.19

°C

Isokinetic Variation

Yes

Isokineticity Acceptable - Yes

TOTAL PARTICULATE MATTER: QUALITY ASSURANCE

21

No

%

Isokinetic Criterion Compliance

Leak Test Results

Yes

Pre-Sampling Leak Rate l/min 0.00

%

Run 1

Yes

APPENDIX 2

MU Acceptable

Allowable Leak Rate

l/min 0.10

Allowable MU

(PAGE 1 OF 2)

5.4

Units

-

Silica Gel (Concurrent Water Vapour) Units

Maximum Filter Temperature

Run 1

Post-Sampling Leak Rate

Are Water Droplets Present

l/min

Post-Conditioning Temperature

Units

Filter Temperatures

0.44

Units

Measurement Uncertainty (MU)

Allowable Isokinetic Range %

%

Mean Sampling Rate

0.24

l/min 21.97

-

Yes

± mg/m³

Weighing Uncertainty Criteria

160

ELV [Daily ELV for IED] mg/m³ 3.00

CAT-RT (Version BJ)

Page 18 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 109: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

Expected Sampling Rate

Validity of Blank vs ELV

-

Run Number

Units Blank 1

-

Yes

Nature of Deviation

Blank Acceptable

Blank Acceptable

Allowable Blank

mg/l

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

l/min

2.7

Blank 1

mg/m³

Units

0.6

10

l/min

20.00

0.00

Post-Sampling Leak Rate l/min 0.00

Allowable Leak Rate

l/min

Pre-Sampling Leak Rate

Acetone / Water Rinse Value

0.40

mg/l

(PAGE 2 OF 2)

YesLeak Test Acceptable

There are no deviations associated with the sampling employed.

Acetone / Water Rinse Blank Units Blank

Allowable Blank

Leak Test Results

APPENDIX 2

TOTAL PARTICULATE MATTER: QUALITY ASSURANCE

- Yes

CAT-RT (Version BJ)

Page 19 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 110: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (STP)

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (STP)

Leak

Mass of Particulate

Uncollected Mass

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Vm

uHm

0.0279

ρm 101.8

≤2%

291.5

% 79.5

-

Units

≤1%

%

% v/v0.0Hm

0.5

1.3950

Tm uTm K 2.0

0.0015

<5% of ELV

% 79.5

Uncertainty in Result

0.47

Measured Quantities

mg

% 3.43

≤1%

≤2%

Uncertainty as a Percentage

uVm m³

uρm

1.2457

≤1%

mg/m³ 0.47

% 0.46

mg/m³ 0.2149

1.00

N/A

Run 1

2.00

1.00

0.13

Measured Quantities

uUCM mg -

-

Run 1 Requirement of Standard

Overall MU For O₂ Measurement

mg/m³ N/A

Symbol Units

UCM

%

Parameter

0.79

mg/m³ 0.47

Lr mg

-

Units Run 1

0.74

mg/m³ 0.015

mg/m³

%

0.24

Units

0.47

Symbol

0.69

mg/m³

%

Uncertainty in Measurement Units Sensitivity Coefficient

%

Units Run 1

% N/A

%

% v/v N/A

kPa

L 0.46

m mg

APPENDIX 2

TOTAL PARTICULATE MATTER: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

Vm

-uL %

1.0

um

Run 1

UCM

L

Run 1

79.5

mg/m³

N/A

mg/m³

N/A

%

0.47

0.743

0.79

Units

0.27

-

0.49

0.1029

0.002

Oxygen Correction Part of MU Budget

Measured Quantities

Run 1

mg/m³

Measured Quantities

CAT-RT (Version BJ)

Page 20 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 111: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Yes

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis?

0.46

Uncertainty ±g/hr 0.11

Filter Size and Material 47mm Quartz Fibre

Probe Material Titanium

Filter Housing Material Titanium

Sample Point I.D.'s A1, A2, A3, B1, B2 & B3

Concentration mg/m³ 0.0123

Name of Analytical Laboratory RPS

Number of Sampling Lines Used 2/2

Number of Sampling Points Used 6/6

Analytical Laboratory's Procedure

1.43

Uncertainty ±% v/v 0.08

Parameter

0.0104

Mean

Honeywell International Technologies Ltd, Unit 328

0.0470

0.11

Parameter Units Run 1 Mean

Water Vapour % v/v 1.43

APPENDIX 2

Impinger Material

Mass Emission g/hr 0.46

Borosilicate Glass

Absorption Solution Nitric Peroxide

0.08

Parameter MaximumUnits Blank 1

Uncertainty ±mg/m³

Date of Sample Analysis 11/11/2015

Out Stack

0.0123

Parameter Value

Positioning of Filter

0.0104

Units Run 1

Concentration mg/m³ 0.0470

IRON: RESULTS SUMMARY

A2-4 Abrasive Extraction

CAT-RT (Version BJ)

Page 21 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 112: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

0.4

Test Units Run 1

g

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) - N/A

Barometric pressure, Pb mmHg

g/gmol

762.8

% oxygen reference condition, REF%O₂ % v/v N/A

Total % v/v 20.86

% v/v

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

N₂ % v/v 79.14

20.80

Total mass of liquid collected, Vlc

Vwstd = (0.001246)(Vlc)

g 8.0

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Total mass collected in impingers (silica trap)

APPENDIX 2

IRON: ISOKINETIC SAMPLING CALCULATIONS

60.0

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0143

m³ 0.0100

Volume of gas sample through gas meter, Vm

Ps = (Pb + (Pstatic / 13.6) mmHg 763.2

Stack static pressure, Pstatic mmH₂O 5.6

% v/v

-

1.43

Total mass collected in impingers (liquid trap) g 7.6

N/A

m³ N/A

N/A

N/A

m³ 0.7880

1.43

% v/v 0.06

Vmstd@X%oxygen = (Vmstd) / (O₂REFd)

Vmstw = (Vmstd)(100/(100 - Rwv))

0.6867

% dry oxygen measured in gas stream, ACT%O₂d % v/v N/A

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³

Gas meter correction factor, Yd - 0.9450

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) - No

% wet oxygen measured in gas stream, ACT%O₂w % v/v

0.6967

Average pressure drop across orifice, ∆H mmH₂O

Average dry gas meter temperature, Tm °C 25.8

% v/v

28.84

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol 28.69

Pitot tube velocity constant, Kp - 34.97

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

Velocity pressure coefficient, Cp - 0.84

Average of velocity heads, ∆Pavg mmH₂O 8.41

Average square root of velocity heads, √∆P √mmH₂O 2.90

Average stack gas temperature, Ts °C 23.0

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 9.90

Area of stack, As m² 0.29

Qa = (60)(As)(Vs) m³/min 171.1

Conversion factor (K/mm.Hg), Cf - 0.3592

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273) m³/min 158.5

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 156.2

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw) m³/min N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Nozzle diameter, Dn mm 7.06

Nozzle area, An mm² 39.18

Total sampling time, q min 30

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 107.7

CAT-RT (Version BJ)

Page 22 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 113: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

-

<

Mass in Back Impinger <

-

-

-

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

-

<

Mass in Back Impinger <

-

-

-Reported Concentration mg/m³ 0.0123

APPENDIX 2

IRON: SAMPLING DETAILS

Parameter Units Run 1

Total Mass Collected µg 32.77

Mass in Front Impingers µg 0.52

µg 0.24

Sampling Times - 09:00 - 10:02

Sampling Dates - 29/10/2015

Sampling Device - ISO

Volume Sampled (REF) m³ 0.6967

Mass on Filter / in Rinse µg 32.00

Calculated Concentration mg/m³ 0.0470

Total Mass Collected µg 8.54

Reported Concentration mg/m³ 0.0470

Mass on Filter / in Rinse µg 8.00

Mass in Front Impingers µg 0.41

Parameter Units Blank 1

Blank Dates - 29/10/2015

Average Volume Sampled (REF) m³ 0.6967

µg 0.13

Calculated Concentration mg/m³ 0.0123

CAT-RT (Version BJ)

Page 23 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:53

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Sample Runs

YesDetection Limit Acceptable

Allowable Detection Limit

-

µg/m³ 5

APPENDIX 2

IRON: QUALITY ASSURANCE

(PAGE 1 OF 2)

Leak Test Results Units Run 1

Mean Sampling Rate l/min 24.82

Pre-Sampling Leak Rate l/min 0.10

Post-Sampling Leak Rate l/min 0.10

Allowable Leak Rate l/min 0.50

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

90

Detection Limit µg/m³ 4.0

Leak Test Acceptable - Yes

Absorption Efficiency Units Run 1

Absorption Efficiency % 100.0

Allowable Absorption Efficiency %

Water Droplets Units Run 1

Are Water Droplets Present - No

MU (Concurrent Water Vapour) Units Run 1

Measurement Uncertainty (MU) % 5.9

Allowable MU % 20

MU Acceptable % Yes

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded % Yes

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 107.7

Ambient Temperature Recorded? - Yes

Allowable Isokinetic Range % 95 - 115

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Maximum Filter Temperature °C 180

Impingers Exit Temperature Units Run 1

Maximum Temperature Recorded °C 15

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable - Yes

Test Conditions Units Run 1

CAT-RT (Version BJ)

Page 24 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

Leak Test Acceptable - Yes

Post-Sampling Leak Rate l/min 0.00

APPENDIX 2

IRON: QUALITY ASSURANCE(PAGE 2 OF 2)

Leak Test Results Units Blank 1

Allowable Leak Rate l/min 0.30

Validity of Blank vs ELV Units Blank 1

Allowable Blank mg/m³ N/A

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

l/min 15.00Expected Sampling Rate

Pre-Sampling Leak Rate l/min 0.00

CAT-RT (Version BJ)

Page 25 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

0.0104

≤1%

Run 1

Sensitivity Coefficient

Units

mg/m³ 0.0104

mg/m³

uρm kPa 0.5

mg/m³ 0.0104

mg/m³ N/A

APPENDIX 2

K 2.0

% 22.2

Overall MU For O₂ Measurement %

Run 1 Requirement of Standard

≤1%

% 0.49

% N/A

% 22.2

% 22.2

Parameter Units Run 1

mg/m³ 0.0053

Measured Quantities Units

% v/v

Measured Quantities

ρm 101.8

1.00

Measured Quantities Units

≤1%

% 11.00

Run 1

% N/A

Units Run 1

Uncertainty as a Percentage

Uncertainty in Measurement Units

Measured Quantities

Oxygen Correction Part of MU Budget

N/A

mg/m³ 0.0001

N/A

No Requirement

%

Symbol Units Run 1

uHm % v/v 1.0

% 2.00 ≤2%

% 0.67

L 0.40

- N/A

Uncertainty in Result

Lr mg/m³ 0.0052

Symbol

mg/m³ 0.0012

uVm m³ 0.0158

Tm 298.8 uTm

IRON: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

uL

Vm m³ 0.6867 0.07

1.00

% -

uLr % -

L

Hm 0.0

Vm 0.7880

Run 1

0.40 ≤2%

Lr 11.00

mg/m³ 0.0001

mg/m³ 0.0052

1.00

%

CAT-RT (Version BJ)

Page 26 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

APPENDIX 2

TITANIUM: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-4 Abrasive Extraction

Parameter Units Run 1 Mean

Run 1 Mean

Concentration mg/m³ 0.0199 0.0199

Probe Material

Water Vapour % v/v 1.43

Concentration mg/m³ 0.0182 0.0182

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Titanium

Filter Housing Material Titanium

Impinger Material

Uncertainty ±mg/m³ 0.0044

Parameter Units Blank 1

0.0044

Mass Emission g/hr 0.2

Uncertainty ±% v/v 0.08 0.08

Maximum

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis? Yes

Date of Sample Analysis 11/11/2015

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure

Filter Size and Material 47mm Quartz Fibre

Number of Sampling Lines Used 2/2

Number of Sampling Points Used 6/6

Sample Point I.D.'s A1, A2, A3, B1, B2 & B3

Parameter Value

1.43

0.2

Uncertainty ±g/hr 0.0 0.0

Parameter Units

CAT-RT (Version BJ)

Page 27 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

- 0.9450

Total mass of liquid collected, Vlc

% v/v 1.43

°C

g 7.6

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) -

% v/v 1.43

m³/min

g

N/A

0.6967

m³ 0.0100

Total % v/v

g/gmol 28.84

%

Volume of gas sample through gas meter, Vm m³

25.8

% wet oxygen measured in gas stream, ACT%O₂w % v/v

0.7880

Gas meter correction factor, Yd

Vmstw = (Vmstd)(100/(100 - Rwv))

Total mass collected in impingers (silica trap) g 0.4

8.0

No

763.2

Average dry gas meter temperature, Tm °C

% dry oxygen measured in gas stream, ACT%O₂d % v/v

% v/v N/A

% v/v

20.86

Pitot tube velocity constant, Kp - 34.97

0.84

9.90

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

N/A

8.41

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s

23.0

Velocity pressure coefficient, Cp -

Vwstd = (0.001246)(Vlc)

mmH₂O

Barometric pressure, Pb mmHg

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (liquid trap)

762.8

APPENDIX 2

TITANIUM: ISOKINETIC SAMPLING CALCULATIONS

Test Units

5.6

Run 1

Stack static pressure, Pstatic

20.80

m³/min

Total sampling time, q min

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0143

-

mmH₂O 60.0Average pressure drop across orifice, ∆H

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³ 0.6867

Average of velocity heads, ∆Pavg mmH₂O

N/A

N/A

0.06

Qa = (60)(As)(Vs) 171.1

- 0.3592

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d) -

Average square root of velocity heads, √∆P √mmH₂O

0.29

30

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) 107.7

39.18

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

% v/v 79.14

% v/v

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

Nozzle area, An

Conversion factor (K/mm.Hg), Cf

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

Average stack gas temperature, Ts

Area of stack, As m²

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

Nozzle diameter, Dn mm 7.06

2.90

28.69

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

m³/min 158.5

N₂

m³/min

% oxygen reference condition, REF%O₂

mm²

156.2

N/A

m³/min N/AQstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

CAT-RT (Version BJ)

Page 28 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<

Reported Concentration mg/m³ 0.0199

Blank Dates

Units

Calculated Concentration mg/m³

-

0.0182

TITANIUM: SAMPLING DETAILS

Parameter Units

10.00

2.613

29/10/2015

Total Mass Collected µg

Mass on Filter / in Rinse

µg 2.06

12.71

Run 1

µg

Calculated Concentration mg/m³ 0.0199

- 09:00 - 10:02

Blank 1

Total Mass Collected

0.65

Sampling Times

10.000

Sampling Dates

0.6967

APPENDIX 2

1.224µg

Volume Sampled (REF) m³

- 29/10/2015

µg

Sampling Device - ISO

µg

Reported Concentration mg/m³

Mass in Front Impingers

0.0182

Parameter

Average Volume Sampled (REF)

µg

Mass in Front Impingers µg

Mass on Filter / in Rinse

13.837

0.6967

CAT-RT (Version BJ)

Page 29 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

No

Measurement Uncertainty (MU) % 5.9

Allowable Detection Limit

%

0.10

95 - 115

Allowable Absorption Efficiency %

Run 1Test Conditions

20

24.82

-

Run 1

MU Acceptable

Detection Limit Acceptable

Units Run 1

Isokineticity Acceptable

Pre-Sampling Leak Rate

Yes

%

No

l/min

UnitsAbsorption Efficiency

5

MU (Concurrent Water Vapour) Units

Yes

Run 1

Detection Limit 8.4

Units

Yes

µg/m³

Maximum Allowable Temperature

Run 1

Leak Test Results

Yes

Run 1

Allowable Leak Rate l/min

µg/m³

Silica Gel (Concurrent Water Vapour) Units

Leak Test Acceptable

Allowable MU

Run 1

l/min

Water Droplets Units

Mean Sampling Rate

0.50

%

%

Are Water Droplets Present

Less than 50% Faded

Isokinetic Variation

Detection Limit Units Run 1

-

Isokinetic Criterion Compliance Units Run 1

-

Absorption Efficiency

APPENDIX 2

TITANIUM: QUALITY ASSURANCE

(PAGE 1 OF 2)

-

Absorption Efficiency Acceptable - Yes

% 100.0

Allowable Isokinetic Range %

180

Post-Sampling Leak Rate l/min

Units Run 1

Impingers Exit Temperature

Units

°C

Yes

90

Filter Temperatures

°C

0.10

Maximum Filter Temperature

Maximum Temperature Recorded

Ambient Temperature Recorded?

Exit Temperature Acceptable - Yes

-

107.7

15°C

30

CAT-RT (Version BJ)

Page 30 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

- - - - -

- - - - -

15.00

APPENDIX 2

Validity of Blank vs ELV

l/min

TITANIUM: QUALITY ASSURANCE

Allowable Leak Rate l/min 0.30

Expected Sampling Rate l/min

(PAGE 2 OF 2)

Leak Test Results

mg/m³ N/A

Post-Sampling Leak Rate l/min 0.00

N/A

Blank 1

-

Allowable Blank

0.00

Leak Test Acceptable -

Units

There are no deviations associated with the sampling employed.

Pre-Sampling Leak Rate

Units

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Blank 1

Yes

Blank Acceptable

CAT-RT (Version BJ)

Page 31 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

mg/m³ N/A

% N/A

N/A

TITANIUM: MEASUREMENT UNCERTAINTY CALCULATIONS

mg/m³

Run 1

0.0000

Sensitivity Coefficient

% v/v N/A

Uncertainty as a Percentage

0.0022

≤2%% 2.00

kPa 0.5

1.00%

mg/m³

mg/m³

% 22.2

%

Measured Quantities

0.67

22.2

No Requirement

0.6867

Run 1

Tm

Units

0.7880

Hm 0.0

Units

0.40

Lr

L 0.40

%

2.0

-

0.0000

%

≤1%

≤1%

Run 1

mg/m³

uρm

0.03

1.00

ρm 101.8

Units

Oxygen Correction Part of MU Budget

Measured Quantities Units Run 1

-

% N/A

Overall MU For O₂ Measurement %

Parameter

N/A

0.0158

Value

Vm

0.0044

%

% 11.00

Run 1

UnitsMeasured Quantities

Uncertainty in Result

0.0005

Standard uncertainty

Measured Quantities Symbol Run 1

1.0

uL

Run 1

11.00

Symbol

mg/m³ 0.0044

0.0022

298.8

% 0.49

Measured Quantities

Vm

≤2%

mg/m³

uLr % -

Uncertainty in Measurement Units

L

Units

uHm % v/v

Run 1

K

1.00Lr mg/m³ 0.0022

Requirement of Standard

Symbol

uVm

≤1%

%

mg/m³ 0.0044

22.2

uTm

mg/m³

APPENDIX 2

CAT-RT (Version BJ)

Page 32 of 32

Honeywell International Technologies Ltd

Unit 328

A2-4 Abrasive Extraction

Job Number: CDU-0559, Version 1

Sample Date/s: 29th 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 123: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Report Written by

Piotr Nadany

23rd November 2015

Stack Emissions Testing Report Commissioned by

29th - 30th October 2015

Job Reference Number

CDU-0559

Installation Name & Address

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Version 1

MM 07 881

MCERTS Level 2

Team Leader

Team Leader

TE1 TE2 TE3 TE4MM 07 881

MCERTS Level 2

Piotr Nadany

Report Approved by

Dates of the Monitoring Campaign

Version

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24

T: +353 86 853 8247

E: [email protected]

Your Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

Waterford

Cork Road Industrial ParkHoneywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-9 Wet Scrubber

Report Date

TE1 TE2 TE3 TE4

CAT-RT (Version BJ)CDU-0559 A2-9 Wet Scrubber Honeywell International Technlogies (Report)

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TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

4

7

7

CONTENTS

2

9

3

5

6

8

The testing performed fully meets the technical requirements in Irish

EPA Guidance Note, AG2.

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the

written approval of Exova Catalyst Ireland.

CAT-RT (Version BJ)Page 2 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

Job Number: CDU-0559, Version 1Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 125: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

Honeywell International Technologies Ltd, Unit 328

(Page 1 of 7)

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd to carry out stack emissions testing on

the A2-9 Wet Scrubber at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

Hydrogen Fluoride, Nitric acid, Sulphuric acid

MONITORING OBJECTIVES

Executive Summary

A2-9 Wet Scrubber

29th - 30th October 2015

CAT-RT (Version BJ)Page 3 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

Job Number: CDU-0559, Version 1Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 126: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

where MU = Measurement Uncertainty associated with the Result

Parameter

Hydrogen Fluoride ¹ - -

Nitric acid ¹ - -

Sulphuric acid ¹ - -

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

Volumetric Flow Rate (REF)

0.74

24771

m³/hr

m/s

0.1

22.4

1.8

22991 2993

(Page 2 of 7)

mg/m³

592.6

Honeywell International Technologies Ltd, Unit 328

29th - 30th October 2015

+/-

% v/v

6.1

m³/hr

4.4 0.620

3225

°C

Mass Emission

MONITORING RESULTS

g/hr

mg/m³

592.60.00 1.1200.05 0.2

A2-9 Wet Scrubber

mg/m³ 1.03

g/hr0.01

UnitsResult Limit

0.2

MU

0.067 g/hr 5.903.523.73

Units Result

Concentration

MULimit

+/-

Executive Summary

0.19

-

Volumetric Flow Rate (ACTUAL)

30000

CAT-RT (Version BJ)Page 4 of 26

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Parameter

R1 - -

R1 - -

R1 - -

R1

All results are expressed at the respective reference conditions.

0.05

4.4Nitric acid

mg/m³

0.19

g/hrHydrogen Fluoride

30

23.73

140

14029/10/2015

g/hr

Velocity & Volumetric Flow Rate

1.1

29/10/2015

Sulphuric acid

g/hr

mins

09:00 - 09:30mg/m³ 29/10/2015

Units Concentration Sampling

MONITORING DATE(S) & TIMES

A2-9 Wet Scrubber

29th - 30th October 2015

(Page 3 of 7)

Units

10:00 - 12:20

09:00 - 09:30

Honeywell International Technologies Ltd, Unit 328

Duration

Executive Summary

Sampling

Times

29/10/2015 11:00 - 11:20

Date(s)

Mass Emission

mg/m³

1.03

CAT-RT (Version BJ)Page 5 of 26

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Standard Operating Conditions

Normal Operation

Abatement System

Abatement System Running Status

N/A

Fuel

Plume Appearance

Bag Filter

N/A

On

Continuous

Parameter

Not Visible

Value

(Page 4 of 7)

Executive Summary

PROCESS DETAILS

Capacity (of 100%) and Tonnes / Hour

Continuous or Batch Process

N/A

A2-9 Wet Scrubber

29th - 30th October 2015

Feedstock (if applicable)

Process Status

Honeywell International Technologies Ltd, Unit 328

CAT-RT (Version BJ)Page 6 of 26

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29th - 30th October 2015

Standard

Lab

Honeywell International Technologies Ltd, Unit 328

Yes

Executive Summary

Testing

MONITORING & ANALYTICAL METHODS

(with short name reference as appears in the table above)

Exova Catalyst (CAT)

DeviationRun

SUMMARY OF SAMPLING DEVIATIONS

Parameter

All

CAT-TP-10

Yes

(Average)

ISO

Velocity & Vol. Flow Rate

ANALYSIS LABORATORIES

Lab

CAT IC Yes

(Page 5 of 7)

Testing Analysis

Sulphuric acid

Nitric acid 0.049 mg/m³

Procedure

Analytical

Technique

Analytical

CAT-AP-01

CAT-AP-01

CAT-AP-01

Technical ISO

Yes

Parameter

CAT-TP-31 0.049 mg/m³

EN 1911 CAT-TP-31 Yes

CAT

CAT

Yes Yes

A2-9 Wet Scrubber

Water Vapour

Monitoring Analysis

CAT Yes

IC

Procedure

LOD

Yes CAT

Yes

EN 16911-1 (MID) CAT-TP-41

CAT

MCERTS

17025

Testing

Hydrogen Fluoride ISO 15713

EN 14791

CAT

Yes

Pitot Tube and Thermocouple

CAT-TP-05 YesEN 14790 Gravimetric

Yes

1 There are no deviations associated with the sampling employed.

CAT 0.1 % v/v

17025 Analysis

IC

0.019 mg/m³CAT

CAT-TP-05

1.2 m/s

ISO 17025 Accreditation Number: 4279

Yes

CAT-RT (Version BJ)Page 7 of 26

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Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

Where NM = Not Measured as no Isokinetic sampling was performed.

Lowest Differential Pressure

Value

4" BSP

-

Yes

0.00

-

NM

0.00

-

Highest Gas Velocity

Area

< 3 : 1

-

Platform has chains / self closing gates at top of ladders

-6.08

Value

Depth

6.17

-

NM

0.00Ratio of Above : 1

> 5 Pa Yes

-

Yes

Yes

m

Lowest Gas Velocity

m/s

Yes

-

5.87

-

-

Required

-

1.13

NM

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

0.00

28.4

Circular

Value

Safe Access Available

-

Vertical

No

Parameter

There are no obstructions present which hamper insertion of sampling equipment

(Page 6 of 7)

The sampling location meets all the requirements specified in Irish EPA Guidance Note AG1 and EN 15259, and therefore there

are no improvement recommendations.

Yes

Traverse 1

Easy Access Available

Permanent / Temporary Platform

Inside / Outside

Width

Compliant

Port Depth

--

-

NM

-

m/s

- -

-

Sample Port Size

There is no requirement to perform a EN 15259 Homogeneity Test on this Stack.

1.05

°

-

Yes

25

Yes

NM

No Local Negative Flow

-

Criteria in EN 15259

-

-

Yes

SUITABILITY OF SAMPLING LOCATION

-

Mean Velocity

Outside

General Platform Information

Units

-

Permanent

Platform has vertical base boards (approx. 0.25m high)

m

No

-

-

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

1.20

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

NM

-

-

-

--m/s

Maximum Angle of Swirl

Executive Summary

cm

NM

-

Units

CAT-RT (Version BJ)Page 8 of 26

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Photo 3

Photo 2

SAMPLE POINTS

Executive Summary

PLANT PHOTOS

(Page 7 of 7)

Photo 1

Photo 4

Line A

Line B

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

A2

CAT-RT (Version BJ)Page 9 of 26

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APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDIX CONTENTS

APPENDICES

CAT-RT (Version BJ)Page 10 of 26

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-

-

S-Pitot (1)

L-Pitot

-

-

CAT 14.53

Name

-

CAT 3.73

Equipment Type

-

Miscellaneous Items

-

Equipment I.D.

Position

Equipment I.D.

Digital Manometer (1)SELECT Horiba Model (1)

Oven Box (2)

Piotr Nadany MCERTS Level 2

Extractive Sampling

LIST OF EQUIPMENT

MCERTS Accreditation

15m Heated Line (1)

CAT 17.24

Control Box DGM (2)

Instrumental Analysers

Equipment Type

Technical Endorsements

Team Leader

CAT-TP-31

CAT-TP-10

CAT-TP-05

Stopwatch

Sulphuric acid

-

ABB AO2020-URAS26

-

Single Channel Heater Controller

S-Pitot (2) -

EN 1911

Heated Probe (3) -

-

-

Laboratory Balance CAT 1.18 / 1.18a

Tape Measure CAT 16.35

Equipment I.D.

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

-

-

-

JCT JCC P1 Cooler

CAT 13.27

Mass Flow Controller (1)

-

-

Umbilical (2) Servomex 5200MP

Oven Box (1)

-

CAT 4.467

ISO 15713Hydrogen Fluoride

Stack Thermocouple (3)

Stack Thermocouple (2)

-

-

CAT 12.53

-

-

Mass View (2)

Mass Flow Controller (2) -

Mass View (1) CAT 25.36

20m Heated Line (2)

EN 14791

Parameter

EN 14790

CAT 20.71

Bernath 3006 FID -

CAT-TP-31

Water Vapour

- 1m Heated Line (2)

-

Easylogger EN-EL-12 Bit -

Dual Channel Heater Controller CAT 3.81Kg Check Weight CAT 17.24

Last Impinger Arm CAT 4.404

Callipers

- 20m Heated Line (1)

-

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

1m Heated Line (3)

Nitric acid

EN 16911-1 (MID) CAT-TP-41

Control Box DGM (1)

CAT 3.73-

-

CAT 21.S42

Stack Thermocouple (1)

Gasmet Sampling System-

MCERTS Number

Equipment Type

Hioki 5043 (V)

1m Heated Line (1)

CAT 5.53

Technical ProcedureStandard

Heated Probe (1)

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

Heated Probe (2)

-

-

-

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

5m Heated Line (1) CAT 20.62

500g Check Weight

M&C PSS

MM07 881 TE1 TE2 TE3 TE4

Technician Donal O Faogain MCERTS Level 1 MM 13 1259 TE1

Eco Physics CLD 822Mh

Velocity & Vol. Flow Rate

- -

- -

CAT-RT (Version BJ)Page 11 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

Gas Volumetric Flowrate (Actual)

0.0

kg/m³

-

1.2498

44.01

22586

Gas Volumetric Flowrate REF ¹

%

0.8037

-

101.3

Temperature

kg/m³

Gas Volumetric Flowrate (STP, Wet)

Moisture

1.4277 0.29696-

Units

Result

1.9635

-

% v/v

Units

1.76

kg/m³ 1.279

Duct gas flow conditions

22991

24771

1.195

Wet Density (STP), P STW

-

79.14 0.98913

1.287

77.75

Dry Density (STP), P STD

18.02

Determinand

0.0006

22991

Conc

0.001180.06

22.4

101.7

-

kg/m³

0.7914 28.01N₂

kPa

Density

Dry

0.01416

20.80 32.00

Actual

0.06

Volume

-

Units

Average Pitot Tube Calibration Coefficient, Cp

ppm kg/m³

Conc

1.76

0.2080

m³/hr

REF ¹

1.187

Dry Density (Actual), P Actual

m³/hr

Conc

M

Wet

r% v/v

Gas Volumetric Flowrate (from Traverse)

Gas Volumetric Flowrate (STP, Dry)

3.1

Molar Conc

1.13Stack Area, A

APPENDIX 2

mStack Width, W

22.4

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

kPa

kPa

0.85

Value

1.20

101.7

Average Stack Gas Temperature, Ta

0.023

Component

Average Stack Gas Pressure mmH₂O

-

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

°C

Average Stack Static Pressure, Pstatic

Stack Diameter / Depth, D

Total Pressure

m³/hr

Average Wet Density (Actual), P ActualW

1.76 0.0176

20.43

p pi

Mass

m³/hr

Result

°C

Fraction

kg/m³

CAT-RT (Version BJ)Page 12 of 26

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Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

--

--

-

-

-

-

-

-

-

-

-

- -

-

-

-

-

- -

-

-

6.10

-

-

-

- - -

-

-

3.1

-

--

1.187

6.17

22.3

-

-

-

-

-

--

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

- - -

-

--

1.187

1.188

-

-

-

-

-

- -

1.187

22.4

22.4

3.2

3.1 22.3Mean

6.17

- -

1.187

-

22.4

6.07

0.30

22.4

-

- -

3.1

-

-

3

6.17

3.1

S-Type Pitot with KIMO MP 200 (500Pa)

kg/m³Point °

22.4

4

-

22.4

6.07

6.072.9

3.1

-

1.187

1.187

m/smmH₂O

-

Units

22.2

Pass

VelocitySwirl

No

kPa

-

Wet Density

-

Swirl

Vertical

Pass

Traverse

23.0

0.90

kg/m³

-

°C

-

°

3.2

3.2

m/s°C

22.0

Wet Density

2

-

m

0.08

6.07

1

1.187

22.4

Pass

∆P

-

STATIC (Units: Pa)

Value

∆P Temp

Sampling Line B

mmH₂O

-

(1 of 1)

2

Depth

-

Velocity

2

1.187

1.12

Temp

--

11:00 - 11:20

Sampling Line A

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

-

3.1

5.87

6.07

29/10/2015

101.7

Value

0.85

Units

APPENDIX 2

1.187

23 -Pa

CAT-RT (Version BJ)Page 13 of 26

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- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

Performance characteristics (Uncertainty Components) UnitsValueUncertainty

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

- Resolution

Standard uncertainty associated with the mean velocity (95% Confidence), relative

Standard uncertainty associated with the volume flow rate (95% Confidence)

%

Uc(qV,w)

0.00441

u(φO₂,w) 0.626

K

u(pc) 175.694 Pa

u(patm) 175.692

u(pstat) 0.772

u(ρ) 0.00639

0.00053

-

- 1645.2

Uc,rel(qV,w) 13.02 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

u(φH₂O) 0.090

- 2706705

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

Standard uncertainty associated with the molar mass of the gas

- φO₂,w

- φCO₂,w

Standard uncertainty associated with the mean velocity (95% Confidence)

-

u(vi) 1.068 Pa

u(v) 0.379 m/s

Uc(v) 0.742 m/s

Uc,rel(v) 12.21

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

u(φCO₂,d) 0.002

u(cal) 0.097

u(drift) 0.083

u(fit) 0.012

u(Cf)

1.092 Pa

u(res) 0.00087

0.193

u(M) 0.00003

u(Tc) 1.507

- u(qV,w)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

3224.6 m³/hr

- u²(qV,w)

20.433

- 0.059

u(φO₂,d) 0.637

u(φCO₂,w) 0.002

- u²(a)/a²

- u²(qV,w)/q²V,w

-

CAT-RT (Version BJ)Page 14 of 26

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Analytical Laboratory's Procedure

Name of Analytical Laboratory CAT

CAT-AP-01

Parameter Value

Probe Material Monel

Filter Housing Material Monel

±g/hr

0.11

Run 1

2.57Water Vapour % v/v

Impinger Material Polyethylene

Absorption Solution 0.1 mol/l Sodium Hydroxide

Positioning of Filter Out Stack

Filter Size and Material

Yes

Date of Sample Analysis 09/11/2015

ISO 17025 Accredited Analysis?

Number of Sampling Lines Used

A1

47mm Quartz Fibre

1/1

Uncertainty ±mg/m³

2.57

0.11

1.03Concentration mg/m³

APPENDIX 2

Mean

Mean

HYDROGEN FLUORIDE: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

Parameter Units

A2-9 Wet Scrubber

Run 1

0.07

1.03

Number of Sampling Points Used

Parameter Units

Mass Emission

0.01

Blank 1

0.07

CAT-TP-10

Sample Point I.D.'s

Concentration mg/m³

1/1

ISO 15713

Technical Procedure

Parameter Units Maximum

3.5 3.5

23.7

±% v/v

g/hr 23.7

Standard

Uncertainty

Uncertainty

0.01

CAT-RT (Version BJ)Page 15 of 26

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Sample Runs

-

-

-

-

-

-

-

-

Where: MFC stands for Mass Flow Controller, MV stands for Mass View Flowmeter

Blank Runs

<

-

<

<Calculated Concentration mg/m³ 0.01

Blank Dates - 29/10/2015

Average Volume Sampled (REF) m³ 1.2253

Total Mass Collected µg 15.6

Liquid Trap Start Mass g 2521.8

Liquid Trap End Mass g 2546.6

Calculated Concentration mg/m³ 1.03

Silica Trap End Mass g 806.9

Total Mass Of Water Vapour g 25.3

Calculated Water Vapour % v/v 2.57

Parameter Units Blank 1

Laboratory Result for Impingers µg/ml 0.05

Volume in Impingers ml 311.7

Silica Trap Start Mass g 806.4

-

Mass in Back Impinger µg 7.8

Total Mass Collected µg 1264.8

Laboratory Result for Front Impingers

Laboratory Result for Back Impinger

Volume in Front Impingers

Volume in Back Impinger

µg/ml

µg/ml

ml

ml

4.12

-

0.05

305.1

155.9

Sampling Device MFC / MV

Sample Flow Rate l/min 8.52

mins 140

Sampling Dates

Mass in Front Impingers µg 1257.0

Sampling Times - 10:00 - 12:20

Volume Sampled (STP, Dry) m³ 1.1937

1.2253

Volume Sampled (REF) m³ 1.2253

29/10/2015

APPENDIX 2

HYDROGEN FLUORIDE: SAMPLING DETAILS

Parameter Units Run 1

Volume Sampled (STP, Wet)

Duration

CAT-RT (Version BJ)Page 16 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sample Runs

1 0 0 1

Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

Blank 1

Post-Sampling Leak Rate l/min 0.00

Blank Acceptable

mg/m³

Yes

Yes

Mean Sampling Rate

Yes

0.00

Units

Allowable Blank

Post-Sampling Leak Rate l/min

Validity of Blank vs ELV

Are Water Droplets Present

0.0

-

l/min 8.52

Pre-Sampling Leak Rate l/min 0.00

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

-

Units Run 1

Allowable Leak Rate l/min 0.20

- No

MU (Concurrent Water Vapour) Units Run 1

Measurement Uncertainty (MU) % 4.1

Leak Test Acceptable - Yes

APPENDIX 2

HYDROGEN FLUORIDE: QUALITY ASSURANCE

Leak Test Results Units Run 1

Units Run 1

Allowable Leak Rate l/min 0.17

Allowable MU % 20

MU Acceptable % Yes

Ambient Temperature Recorded? -

Pre-Sampling Leak Rate l/min 0.00

Test Conditions

Leak Test Acceptable

Nature of Deviation Run Number

Units Run 1

Less than 50% Faded % Yes

Leak Test Results Units Blank 1

Expected Sampling Rate l/min 10.00

Silica Gel (Concurrent Water Vapour)

Absorption Efficiency Units Run 1

Absorption Efficiency % 99.4

Allowable Absorption Efficiency % 95

Absorption Efficiency Acceptable - Yes

Water Droplets

CAT-RT (Version BJ)Page 17 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

- N/A

mg/m³ 0.000

mg/m³

Measured Quantities

Oxygen Correction Part of MU Budget

1.00

L

Units

1.00

Measured Quantities

APPENDIX 2

% 6.5

0.86

Run 1

6.5

Overall MU For O₂ Measurement

Uncertainty as a Percentage

Lr

1.1937

Units Run 1

mg/m³ 0.0000

% 0.00 ≤2%

% 2.65

N/A

% 6.5

Value Standard uncertainty

Symbol Run 1

mg/m³

mg/m³

Measured Quantities Units Run 1

0.027

Uncertainty in Measurement Units Sensitivity Coefficient

%

mg/m³ 0.07

- N/A

% v/v

% N/A

0.07

mg/m³

Vm

uVm

Uncertainty in Result

Measured Quantities Units Run 1

Parameter

mg/m³ 0.0206

No Requirement

0.0274

Lr

uLr2.65

2.00 ≤2%%

Run 1 Requirement of Standard

HYDROGEN FLUORIDE: MEASUREMENT UNCERTAINTY CALCULATIONS

Symbol Units Run 1

0.03

mg/m³ N/A

% N/A

Measured Quantities Symbol Units Run 1

Vm 1.1937 m³ 0.0239

uL %

mg/m³ 0.07

L 0.00

% -

-

CAT-RT (Version BJ)Page 18 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Analytical Laboratory's Procedure

Number of Sampling Lines Used

Sample Point I.D.'s A1

Filter Housing Material Monel

Impinger Material Polyethylene

Absorption Solution 1.0 mol/l Sodium Hydroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Parameter Value

Probe Material Monel

Standard

Date of Sample Analysis 19/11/2015

CAT-AP-01

ISO 17025 Accredited Analysis? Yes

0.09 0.09

Maximum

Concentration mg/m³ 0.04 0.04

Water Vapour % v/v 1.36 1.36

Uncertainty ±% v/v

Name of Analytical Laboratory

1/1

Number of Sampling Points Used 1/1

Parameter Units Blank 1

4.4

Parameter Units Run 1 Mean

CAT

Uncertainty ±mg/m³ 0.01 0.01

EN 1911

Technical Procedure CAT-TP-31

Uncertainty ±g/hr 0.6 0.6

APPENDIX 2

NITRIC ACID: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-9 Wet Scrubber

Parameter Units Run 1

0.19

Mass Emission g/hr 4.4

Concentration mg/m³ 0.19

Mean

CAT-RT (Version BJ)Page 19 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sample Runs

-

-

-

-

-

<

-

-

Where: MFC stands for Mass Flow Controller, MV stands for Mass View Flowmeter

Blank Runs

<

-

<

<

Volume Sampled (STP, Dry) m³ 0.3804

Blank Dates - 29/10/2015

Silica Trap Start Mass g 834.1

15.7

Mass in Back Impinger µg 6.2

Total Mass Collected

Calculated Concentration

g 4.2

Liquid Trap Start Mass g 1201.7

0.05

834.2

Total Mass Of Water Vapour

Total Mass Collected µg

Silica Trap End Mass

g 1205.8

Calculated Concentration mg/m³

1.36

Parameter Units Blank 1

Average Volume Sampled (REF) m³ 0.3857

Calculated Water Vapour % v/v

Duration 140

Volume in Front Impingers ml 252.4

g

Sample Flow Rate l/min 2.72

Volume Sampled (REF) m³

mg/m³ 0.19

Laboratory Result for Front Impingers µg/ml 0.27

Laboratory Result for Back Impinger

µg 74.3

0.3857

Units Run 1

Liquid Trap End Mass

Sampling Device

Sampling Dates

Volume in Back Impinger ml 123.9

0.3857

µg/ml 0.05

Mass in Front Impingers µg 68.1

Sampling Times - 09:00 - 09:30

Volume Sampled (STP, Wet) m³

- 29/10/2015

- MFC / MV

mins

APPENDIX 2

NITRIC ACID: SAMPLING DETAILS

Parameter

µg/ml

Volume in Impingers ml

0.04

Laboratory Result for Impingers

314.9

CAT-RT (Version BJ)Page 20 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

Job Number: CDU-0559, Version 1Sample Date/s: 29th - 30th October 2015

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Sample Runs

¹ The concentration in the last absorber was less than 5 times the analytical detection limit. 1 7 11 19

Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

0.00

MU Acceptable % Yes

Leak Test Results

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

There are no deviations associated with the sampling employed.

l/min 10.00

Blank Acceptable

% 6.5

Less than 50% Faded

l/min 0.20

Expected Sampling Rate

Water Droplets Units Run 1

Mean Sampling Rate

Nature of Deviation Run Number

Run 1

-

Validity of Blank vs ELV Units

Yes

Allowable Leak Rate

Test Conditions Units Run 1

Ambient Temperature Recorded?

l/min

Blank 1

Post-Sampling Leak Rate

Allowable MU % 20

Leak Test Acceptable

%

Silica Gel (Concurrent Water Vapour) Units

Absorption Efficiency Units Run 1

2.72

Allowable Absorption Efficiency

Pre-Sampling Leak Rate l/min 0.00

- Yes

- Yes

N/A ¹

Absorption Efficiency Acceptable - N/A ¹

Are Water Droplets Present - No

APPENDIX 2

NITRIC ACID: QUALITY ASSURANCE

Leak Test Results

Absorption Efficiency % 100.0

l/min

Pre-Sampling Leak Rate l/min 0.00

Post-Sampling Leak Rate l/min 0.00

MU (Concurrent Water Vapour) Units Run 1

%

Leak Test Acceptable - Yes

Allowable Leak Rate l/min 0.05

Units Blank 1

Yes

Measurement Uncertainty (MU)

Units Run 1

Allowable Blank mg/m³ 2.0

CAT-RT (Version BJ)Page 21 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

-

%

% v/v N/A

No Requirement

% 6.5

- N/A

N/A

Uncertainty as a Percentage

Measured Quantities

≤2%

%

Run 1

2.65

Units Run 1

%

≤2%

Measured Quantities Symbol

0.0000

1.00L

Uncertainty in Result

Measured Quantities

%

0.01

1.00

Value Standard uncertainty

0.3804

mg/m³

mg/m³ 0.01

%

Lr 2.65

0.0076

L 0.00

Run 1

Vm

mg/m³

Units Run 1

Symbol

mg/m³

mg/m³

0.01

Symbol

uVm m³

Parameter

Oxygen Correction Part of MU Budget

Measured Quantities Units Run 1

mg/m³

Overall MU For O₂ Measurement N/A

6.5

- N/A

% N/A

mg/m³

Units

0.01

% 6.5

Units

mg/m³

0.000

Requirement of Standard

Measured Quantities

mg/m³

0.3804

0.00

%uLr

Vm

0.0051

0.0039

APPENDIX 2

NITRIC ACID: MEASUREMENT UNCERTAINTY CALCULATIONS

uL % -

mg/m³

Units

0.51

2.00

Uncertainty in Measurement Units Sensitivity Coefficient

0.005

Run 1

Run 1

Lr

Run 1

CAT-RT (Version BJ)Page 22 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

Job Number: CDU-0559, Version 1Sample Date/s: 29th - 30th October 2015

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

CAT

ISO 17025 Accredited Analysis? Yes

19/11/2015

1.36

APPENDIX 2

Absorption Solution

Mean

mg/m³ 0.05

Polypropylene

1.1

Uncertainty ±g/hr

Parameter

0.2

Number of Sampling Lines Used

Value

Water Vapour

Parameter

Concentration

Date of Sample Analysis

CAT-AP-01Analytical Laboratory's Procedure

Parameter

±% v/v

Borosilicate Glass

Impinger Material

Name of Analytical Laboratory

Uncertainty ±mg/m³ 0.00

47mm Quartz Fibre

% v/v 1.36

Out Stack

Filter Housing Material

Maximum

1 / 1

SULPHURIC ACID: RESULTS SUMMARY

0.00

Honeywell International Technologies Ltd, Unit 328

A2-9 Wet Scrubber

Units

g/hr 1.1

A1

Probe Material

Number of Sampling Points Used

0.04

Mean

Concentration

Run 1

EN 14791

mg/m³ 0.04

Titanium

Parameter

Mass Emission

0.2

0.09Uncertainty

HPLC Grade Water

Units Blank 1

Technical Procedure CAT-TP-31

0.09

Filter Size and Material

Standard

Positioning of Filter

Units Run 1

0.05

1 / 1

Sample Point I.D.'s

CAT-RT (Version BJ)Page 23 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sample Runs

-

-

-

-

-

<

-

-

Where: MFC stands for Mass Flow Controller, MV stands for Mass View Flowmeter

Blank Runs

<

-

<

<

µg

mg/m³

SULPHURIC ACID: SAMPLING DETAILS

834.2

Mass in Back Impinger µg 6.2

Calculated Concentration

Total Mass Collected

1.36

Parameter

Calculated Water Vapour

Silica Trap Start Mass g

Laboratory Result for Back Impinger µg/ml

Liquid Trap End Mass

18.8

Calculated Concentration mg/m³ 0.05

% v/v

Blank 1

µg/ml 0.05

MFC / MV

APPENDIX 2

Laboratory Result for Impingers

Units

Silica Trap End Mass g

Sampling Times -

Duration

Volume Sampled (REF) m³

30

µg/ml 0.05

Sample Flow Rate l/min 12.68

0.3857

Volume in Front Impingers ml 252.4

0.05

Blank Dates -

g 4.2

834.1

Volume in Back Impinger

29/10/2015

0.04

314.9

0.3857

Liquid Trap Start Mass g 1201.7

Mass in Front Impingers µg 12.6

ml 123.9

Total Mass Collected µg

g

Volume in Impingers ml

15.7

1205.8

Total Mass Of Water Vapour

Average Volume Sampled (REF)

Volume Sampled (STP, Wet) m³ 0.3857

Laboratory Result for Front Impingers

Sampling Dates -

Parameter

Volume Sampled (STP, Dry) m³ 0.3804

09:00 - 09:30

Sampling Device

mins

-

29/10/2015

Units Run 1

CAT-RT (Version BJ)Page 24 of 26

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Sample Runs

² The concentration is less than 30% of the ELV, therefore no assessment against an allowable efficiency is required. 1 7 0 8

Blank Runs

Method Deviations

1

x

- - - - -

- - - - -

- - - - -

l/min 0.00

0.00

Pre-Sampling Leak Rate

Blank Acceptable

- Yes

N/A ²

Silica Gel (Concurrent Water Vapour) Units Run 1

Run 1

Absorption Efficiency Units Run 1

Water Droplets

Less than 50% Faded

Allowable Leak Rate

-

mg/m³

0.20

Units

Leak Test Acceptable - Yes

0.25

Post-Sampling Leak Rate

10.00

Leak Test Acceptable

- Yes

Test Conditions

Allowable Leak Rate l/min

0.00

Validity of Blank vs ELV Units

Yes

l/min

Blank 1

Pre-Sampling Leak Rate l/min

2.0

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Leak Test Results

Units Run 1

There are no deviations associated with the sampling employed.

Blank 1

l/min

Expected Sampling Rate l/min

Allowable Blank

Measurement Uncertainty (MU) % 6.5

Allowable MU %

% 100.0

Allowable Absorption Efficiency % N/A ²

MU (Concurrent Water Vapour)

Units Run 1

Are Water Droplets Present - No

Absorption Efficiency

MU Acceptable

SULPHURIC ACID: QUALITY ASSURANCE

Leak Test Results Units

Units Run 1

Mean Sampling Rate

APPENDIX 2

20

Ambient Temperature Recorded? - Yes

Post-Sampling Leak Rate l/min 0.00

Absorption Efficiency Acceptable

%

% Yes

l/min 12.68

CAT-RT (Version BJ)Page 25 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

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Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Run 1

Oxygen Correction Part of MU Budget

Measured Quantities Units

Measured Quantities Symbol Run 1

Requirement of Standard

Sensitivity Coefficient

Measured Quantities Symbol

0.0076

Overall MU For O₂ Measurement % N/A

0.13

- N/A

mg/m³ 0.0013

0.00

0.00

Units Run 1

Uncertainty in Measurement Units

No Requirement

Units Run 1

0.3804

≤2%

% N/A

Symbol Units Run 1

% 2.00

-

≤2%

Uncertainty as a Percentage

Measured Quantities

Lr mg/m³ 0.001

0.0010

mg/m³

Uncertainty in Result

Measured Quantities Units

% 2.70

%

APPENDIX 2

SULPHURIC ACID: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

1.00

0.3804 uVm

uL % -

Lr 2.70

Run 1

0.00

uLr %

Vm

Run 1

Units Run 1

mg/m³

% 6.6

0.0000

- N/A

% v/v

Parameter

L mg/m³ 0.000

mg/m³ 0.00

mg/m³

% 6.6

1.00

% 6.6

mg/m³

Vm

L

mg/m³ N/A

0.00

mg/m³

0.00

N/A

CAT-RT (Version BJ)Page 26 of 26

Honeywell International Technologies LtdUnit 328A2-9 Wet Scrubber

Job Number: CDU-0559, Version 1Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 149: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

ISO/IEC 17025 Accredited Legal Entity, UKAS Accredited Testing Laboratory No. 4279

Exova (UK) Ltd trading as Exova Catalyst & Exova Catalyst Ireland

Unit C5, Emery Court, The Embankment Business Park, Stockport, SK4 3GL

Stack Emissions Testing Report Commissioned by

29th - 30th October 2015

Job Reference Number

CDU-0559

Installation Name & Address

Report Written by

Piotr Nadany

23rd November 2015

Report Date

TE1 TE2 TE3 TE4

Stack Reference

Irish EPA IPPC Licence: P0698-01

Signature of Report Approver

Piotr Nadany

Report Approved by

Exova Catalyst Ireland, Unit 18 Tallaght Business Centre, Whitestown Business Park, Tallaght, Dublin 24

T: +353 86 853 8247

E: [email protected]

Your Exova Catalyst Ireland Contact: Nick Kenny (+353 86 853 8247)

Waterford

Cork Road Industrial Park

Honeywell International Technologies Ltd

Ireland

Honeywell International Technologies Ltd

A2-11 Chemical storage

Dates of the Monitoring Campaign

Version

Version 1

MM 07 881

MCERTS Level 2

Team Leader

Team Leader

TE1 TE2 TE3 TE4

MM 07 881

MCERTS Level 2

CAT-RT (Version BJ)

CDU-0559 A2-11 Chemical Store Honeywell International Technlogies (POST)

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TITLE PAGE

CONTENTS

EXECUTIVE SUMMARY

Monitoring Objectives

Monitoring Results

Monitoring Dates & Times

Process Details

Monitoring & Analytical Methods

Summary of Method Deviations

Sampling Location

Plant Photos / Sample Points

APPENDIX 1 - Monitoring Personnel & List of Equipment

APPENDIX 2 - Raw Data, Sampling Equations & Charts

8

9

3

5

6

Opinions and interpretations expressed herein are outside the scope of

Exova Catalyst Ireland's ISO 17025 accreditation.

This test report shall not be reproduced, except in full, without the

written approval of Exova Catalyst Ireland.

2

7

CONTENTS

4

7

The testing performed fully meets the technical requirements in Irish EPA

Guidance Note, AG2.

CAT-RT (Version BJ)

Page 2 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Overall Aim of the Monitoring Campaign

Special Requirements

Target Parameters

Honeywell International Technologies Ltd, Unit 328

A2-11 Chemical storage

29th - 30th October 2015

Total Particulate Matter, Nickel, Iron, Titanium

MONITORING OBJECTIVES

Executive Summary(Page 1 of 7)

Exova Catalyst Ireland were commissioned by Honeywell International Technologies Ltd to carry out stack emissions testing on the

A2-11 Chemical storage at Unit 328.

The aim of the monitoring campaign was to demonstrate compliance with a set of emission limit values (ELVs) as specified in the

Site's Licence.

There were no special requirements.

CAT-RT (Version BJ)

Page 3 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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where MU = Measurement Uncertainty associated with the Result

Parameter

Total Particulate Matter ¹

Nickel ¹ - -

Iron ¹ - -

Titanium ¹ < <

Water Vapour

Stack Gas Temperature

Stack Gas Velocity

¹

- -

NOTE: VOLUMETRIC FLOW RATE DATA TAKEN FROM THE PRELIMINARY VELOCITY TRAVERSE.

¹ Reference Conditions (REF) are: 273K, 101.3kPa, without correction for water vapour content.

°C

Volumetric Flow Rate (ACTUAL)

Executive Summary

mg/m³

Mass Emission

-

51.34

MONITORING RESULTS

0.02 0.21

Limit

+/-

m/s

0.2

23.1

0.43

12180

m³/hrVolumetric Flow Rate (REF)

18.7

m³/hr

1.4

11948 606

% v/v

618

0.97

0.09

1.01

Units

g/hr

mg/m³

0.20

mg/m³

-

6.21

Result LimitMU

A2-11 Chemical storage

0.01mg/m³ g/hr

-

96.5

0.007

g/hr 16.10.52

(Page 2 of 7)

+/-

Units Result

Concentration

MU

21000

-

0.08

0.017 -

0.08

-

0.081 - g/hr

Honeywell International Technologies Ltd, Unit 328

29th - 30th October 2015

CAT-RT (Version BJ)

Page 4 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Parameter

R1 - -

R1 - -

R1 - -

R1 < <

R1

All results are expressed at the respective reference conditions.

g/hr

30/10/20150.01

300.02

30

30

mg/m³

30/10/2015

0.08

mins

mg/m³

Sampling

0.1

08:50 - 09:2030/10/2015

mg/m³ 08:50 - 09:20

1.0

g/hr

Honeywell International Technologies Ltd, Unit 328

60

Duration

Executive Summary

Sampling

Times

09:30 - 10:35Total Particulate Matter

Units

(Page 3 of 7)

0.52

MONITORING DATE(S) & TIMES

A2-11 Chemical storage

29th - 30th October 2015

Units Concentration

30/10/20156.2

0.2

Velocity & Volumetric Flow Rate 30/10/2015 09:00 - 09:10

Date(s)

Mass Emission

g/hr

Nickel

Titanium mg/m³

g/hr

08:50 - 09:20

Iron

CAT-RT (Version BJ)

Page 5 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Standard Operating Conditions

Normal Operation

Abatement System

Abatement System Running Status

A2-11 Chemical storage

29th - 30th October 2015

N/A

(Page 4 of 7)

Executive Summary

PROCESS DETAILS

Parameter

Capacity (of 100%) and Tonnes / Hour

Continuous or Batch Process

N/A

Plume Appearance

Bag Filter

Not Visible

Value

On

Batch

Process Status

Honeywell International Technologies Ltd, Unit 328

N/A

Fuel

Feedstock (if applicable)

CAT-RT (Version BJ)

Page 6 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 155: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

MONITORING & ANALYTICAL METHODS

Executive Summary

Velocity & Vol. Flow Rate

Deviation

All

ANALYSIS LABORATORIES

1 Lowest differential pressure < 5 Pa.

Velocity & Volumetric Flow Rate

Run

SUMMARY OF SAMPLING DEVIATIONS

Parameter

The sample points where negative flow was measured during the preliminary traverse were omitted from the sampling

exercise.

Honeywell International Technologies Ltd, Unit 328

CAT

Testing

ICP-MS

ICP-MS

0.005 mg/m³YesYes CATCAT-TP-06

Yes RPS

CAT Yes RPS

RPS

Nickel

(Page 5 of 7)

Testing

29th - 30th October 2015

Lab

Monitoring

CAT

Analysis

0.001 mg/m³

Procedure

Analytical

ICP-MSCAT Yes

0.11 mg/m³

EN 14385

EN 14385 CAT-TP-06 Yes

CAT-TP-01 Yes

Lab

Total Particulate Matter

Analysis

(Average)

ISO

A2-11 Chemical storage

Yes YesEN 13284-1

Yes

EN 14385

Procedure

LOD

Titanium

CAT YesWater Vapour

Technique

Analytical

CAT-TP-03

Technical ISOParameter

0.007 mg/m³

Yes

Yes

Gravimetric

MCERTS

17025

Testing

Iron

Standard

RPS Laboratories Ltd (RPS)

Following the agreement between the client and Environmental Agency the velocity/volumetric flow rate were

measured

upstream of the abetment system as the sampling location didn’t meet the requirements of BS EN 13284.

All 1 The sample points where the angle of swirl was > 15° were omitted from the sampling exercise.

Yes

All

CAT-TP-06

1 Ratio highest to lowest velocities > 5 : 1.

Yes 1.2 m/s

ISO 17025 Accreditation Number: 4279

ISO 17025 Accreditation Number: 0605

CAT

CAT-TP-05 YesEN 14790

Pitot Tube and ThermocoupleYes

1

GravimetricCAT-TP-05

EN 16911-1 (MID) CAT-TP-41

(with short name reference as appears in the table above)

Exova Catalyst (CAT)

1

0.1 % v/v

All

M31

M31

M31

17025 Analysis

CAT

CAT-RT (Version BJ)

Page 7 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 156: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Duct Characteristics Location of Sampling Platform

Platform Details

Sampling Location / Platform Improvement Recommendations

EN 15259 Homogeneity Test Requirements

Sampling Plane Validation Criteria (from EN 15259

-

-

0.00

--

9

0.00Ratio of Above : 1 Yes

< 15°

< 3 : 1

Yes

0.00 0.00

-No Local Negative Flow

-18.69

Value

18.85Highest Gas Velocity

Area

4" BSP

-

Lowest Differential Pressure

-

Yes

°

--

-

Platform has vertical base boards (approx. 0.25m high)

-

-

> 5 Pa Yes

-

N/A

No

m

Lowest Gas Velocity

m/s

Yes

-

18.51

-

Vertical

-

Required

-

0.18

-

-

Orientation of Duct

Irish EPA Technical Guidance Note AG1 / EN 15259 Platform Requirements

Pa

Sample Port Size

There is no requirement to perform a EN 15259 Homogeneity Test on this Stack.

-

299.0

Circular

Value

Safe Access Available

-

-

Depth

Value

Yes

Traverse 1

Easy Access Available

Platform has chains / self closing gates at top of ladders

Parameter

1.02

No

10

Permanent / Temporary Platform

Inside / Outside

Yes

-

Units

SUITABILITY OF SAMPLING LOCATION

General Platform Information

Units

-

Permanent

-

-

Mean Velocity

Outside

-

m

All platforms should be designed in accordance with the requirements in EPA Guidance Note AG1 and BS EN 15259.

Width

Compliant

Port Depth

There are no obstructions present which hamper insertion of sampling equipment

-

-

-

-

Criteria in EN 15259 -

-

Sufficient working area to manipulate probe and operate the measuring instruments

Type

-

-m/s

Maximum Angle of Swirl

Executive Summary

cm

Yes

(Page 6 of 7)

0.48

Platform has 2 levels of handrails (approx. 0.5m & 1.0m high)

No

-

-

-

m/s

-

CAT-RT (Version BJ)

Page 8 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Photo 2

SAMPLE POINTS

Photo 3

Executive Summary

PLANT PHOTOS

(Page 7 of 7)

Photo 1

Photo 4

where = isokinetic point sampled at

= isokinetic point not sampled at

= combustion gases sample point

= non-isokinetic sample point

Line A Line B Line C

A1

A3

A2

B1

B3

B2

C1

C3

C2 B4

B5

B6

CAT-RT (Version BJ)

Page 9 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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APPENDIX 1 - Stack Emissions Monitoring Personnel, List of Equipment & Methods and Technical Procedures Used

APPENDIX 2 - Summaries, Calculations, Raw Data and Charts

APPENDICES

APPENDIX CONTENTS

CAT-RT (Version BJ)

Page 10 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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CAT-TP-06

CAT-TP-06

CAT-TP-06

CAT-TP-05

-

15m Heated Line (1)

CAT 17.24

Equipment I.D.

Digital Manometer (1)SELECT Horiba Model (1)

-

CAT 14.53

CAT 23.26

Equipment I.D.

-

Position

CAT 3.73

Equipment Type

-

Nickel

Iron

Miscellaneous Items

CAT 13.27

Equipment Type

Extractive Sampling

LIST OF EQUIPMENT

Control Box DGM (2)

MM07 881 TE1 TE2 TE3 TE4

Technician Donal O Faogain MCERTS Level 1

-Oven Box (2)

Instrumental Analysers

Stopwatch

-

-

Umbilical (2) Servomex 5200MP

Oven Box (1)

-

CAT 4.467

Mass View (2)

-

Laboratory Balance CAT 1.18 / 1.18a

Stack Thermocouple (3)

Stack Thermocouple (2)

-

Tape Measure CAT 16.35

-

Dual Channel Heater Controller CAT 3.8

-

Heated Probe (3)

EN 16911-1 (MID) CAT-TP-41

Mass Flow Controller (2) -

Mass View (1) -

20m Heated Line (2)

Parameter

Total Particulate Matter

-

Easylogger EN-EL-12 Bit -

Equipment I.D.

1Kg Check Weight CAT 17.24

Last Impinger Arm

Bernath 3006 FID -

Water Vapour

CAT 5.52 1m Heated Line (2)

EN 14790

-

EN 14385

EN 14385

EN 14385

Mass Flow Controller (1)

Single Channel Heater Controller

S-Pitot (2)

M&C PSS 1m Heated Line (3) -

-

-

CAT 4.404

Callipers

- 20m Heated Line (1)

-

METHODS & TECHNICAL PROCEDURES USED

Tubes Kit Thermocouple CAT 4.439

Equipment Type

Hioki 5043 (V)

Titanium

1m Heated Line (1)

-

EN 13284-1

Technical ProcedureStandard

Heated Probe (1)

CAT-TP-01

Barometer

Digital Manometer (2)

Umbilical (1)

Box Thermocouples (2)

Box Thermocouples (1)

Control Box DGM (1)

CAT 3.73-

-

CAT 21.S42

Stack Thermocouple (1)

Gasmet Sampling System-

-

ABB AO2020-URAS26

CAT 12.53

CAT 3.59

-

CAT 7.23

S-Pitot (1)

L-Pitot

-

-

-

JCT JCC P1 Cooler

Heated Probe (2)

-

-

CAT 3.59

SELECT FTIR

SELECT Horiba Model (2)

Digital Temperature MeterServomex 4900

-

5m Heated Line (1) -

500g Check Weight

MM 13 1259 TE1

MCERTS Number

STACK EMISSIONS MONITORING PERSONNEL

APPENDIX 1

Technical Endorsements

Team Leader Piotr Nadany MCERTS Level 2

MCERTS AccreditationName

Velocity & Vol. Flow Rate

- -

- -

Eco Physics CLD 822Mh

CAT-RT (Version BJ)

Page 11 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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General Stack Details

Stack Gas Composition & Molecular Weights

CO₂ (Estimated)

O₂ (Estimated)

Moisture (H₂O)

Where: p = M / 22.41

pi = r x p

Calculation of Stack Gas Densities

Where: P STD = sum of component concentrations, kg/m³ (not including water vapour)

P STW = sum of all wet concentrations / 100 x density, kg/m³ (including water vapour)

P Actual = P STD x (TSTP / (PSTP)) x ((Pstatic + Pb) / Ta)

P ActualW (at each sampling point) = P STW x (Ts / Ps) x (Pa / Ta)

Calculation of Stack Gas Volumetric Flowrate, Q

Gas Volumetric Flowrate (Actual)

0.0

kg/m³

1.256

Dry Density (Actual), P Actual

m³/hr

-

11777

Units

Conc

0.00118

Pa

0.06

23.1

107.8

% v/v

Units

Mass

Component

m³/hr

Result

°C

-

1.2498

44.01

1.4277 0.29696-

kg/m³

kPa

0.0144

kg/m³

Gas Volumetric Flowrate (STP, Wet)

Moisture

Gas Volumetric Flowrate REF ¹

%

0.8037

p

Gas Volumetric Flowrate (STP, Dry)

0.7914

18.02

Determinand

pi

Dry Density (STP), P STD

1.44

kg/m³ 1.280

Duct gas flow conditions

11948

12180

1.263

11948

20.50

Wet Density (STP), P STW

-

101.3

Temperature

N₂

Result

1.9635

-

-

0.2080

m³/hr

REF ¹

0.0006

20.80 32.00

78.00 28.01

1.287

-

Units

Average Pitot Tube Calibration Coefficient, Cp

ppm kg/m³

Average Stack Gas Pressure

Conc

1.44

Conc

M

Wet

r% v/v

kg/m³

m³/hr

Total Pressure

Average Wet Density (Actual), P ActualW

1.44

79.14 0.98913

Dry

0.01154

Actual

0.06

Volume

305.0

Molar Conc

0.18Stack Area, A

APPENDIX 2

mStack Width, W

23.1

Average Barometric Pressure, Pb

m

Stack Details (from Traverse)

°C

Average Stack Static Pressure, Pstatic

kPa

0.85

Value

0.48

107.7

Average Stack Gas Temperature, Ta

0.096

-

Units

PRELIMINARY STACK SURVEY: CALCULATIONS

Fraction

Density

kPa

Stack Diameter / Depth, D

Gas Volumetric Flowrate (from Traverse)

CAT-RT (Version BJ)

Page 12 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Parameter Parameter

Date of Survey Initial Pitot Leak Check

Time of Survey Final Pitot Leak Check

Atmospheric Pressure Orientation of Duct

Average Stack Static Pressure Pitot Tube, Cp

Result of Pitot Stagnation Test Number of Lines Available

Are Water Droplets Present? Number of Lines Used

Device Used

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

- -

-

--

-

-

--

-

--

-

-

-

-

1.256

18.85

23.1

-

- -

-

-

-

-

-

-

-

-

-

-

-

-

-

-

-

- -

-

-

- -

--- -

-

0.36

-

4.0

-

-

--

1.256

1.256

23.2

0.12

-

-

- -

301.0

305.0

18.57

23.1

-

- -- -

0.031

23.1

310.0

3

18.85

kg/m³Point

4

m/s

23.1

Pass

-

2

0.45 299.0

7.0

1.256

-

Traverse

-°C

96.0

8.0

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID)

-

(1 of 1)

1

Mean

-

310.0

Units

107.7

Temp

-

-Swirl

No

kPa

-

-

96 -

STATIC (Units: Pa)

Value

∆P -

-

-

-

Vertical

Pass

9.018.51

18.69

-

09:00 - 09:10

Sampling Line A

1

30/10/2015

Value

-

Pa °m --

Pass

-

-

Depth

-

Velocity

Units

-

Wet Density

Pa 0.85

S-Type Pitot with KIMO MP 200 (500Pa)

1.256

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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0.00053

-

Standard Uncertainty on the coefficient of the Pitot Tube

Standard Uncertainty associated with the mean local dynamic pressures

0.00067

-

%

u(v) 0.219 m/s

Uc(v) 0.429 m/s

Uc,rel(v)

-

u(vi)

Uc,rel(qV,w) 5.08 %

u(k) 0.005 -

u(∆pi)

Standard uncertainty associated with the stack temperature

Standard uncertainty associated with the absolute pressure in the duct

- Atmospheric Pressure

- Static Pressure

Standard uncertainty associated with the density in the duct

Standard uncertainty associated with the local velocities

Standard uncertainty associated with the mean velocity

Performance characteristics (Uncertainty Components) UnitsValueUncertainty

Standard uncertainty associated with the volume flow rate (95% Confidence) Uc(qV,w)

- φO₂,w

- φCO₂,w

- Oxygen, dry

- Carbon Dioxide, dry

- Water Vapour

- Oxygen, wet

- Carbon Dioxide, wet

-

-

u(pstat) 5.044

u(ρ) 0.00673

Standard uncertainty associated with the mean velocity (95% Confidence)

Standard uncertainty associated with the mean velocity (95% Confidence), relative

175.764 Pa

u(patm) 175.692

5.044

u(φO₂,w) 0.628

- 315.4

99475

0.073

2.30

u(φH₂O)

K

0.257 Pa

- Resolution

- Calibration

- Drift

- Lack of Fit

- Overall corrections to dynamic measurements

u(pc)

Standard uncertainty associated with the molar mass of the gas

u(φCO₂,d) 0.002

u(cal) 9.686

u(drift) 0.083

u(fit) 14.669

u(Cf)

u(Tc) 1.511

APPENDIX 2

PRELIMINARY STACK SURVEY: VELOCITY TRAVERSE TO EN 16911-1 (MID) - MEASUREMENT UNCERTAINTY(1 of 1)

- u²(qV,w)

- u(qV,w)

Standard uncertainty associated with the volume flow rate (95% Confidence), relative

u(φO₂,d) 0.637

u(φCO₂,w) 0.002

20.501

- 0.059

- u²(a)/a²

- u²(qV,w)/q²V,w

-

24.439

u(M) 0.00003

618.2 m³/hr

Pa

u(res) 0.00087

CAT-RT (Version BJ)

Page 14 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

CAT-TP-01

Uncertainty ±mg/m³ 1.34 1.34

Units

0.52

Number of Sampling Lines Used 1/3

Number of Sampling Points Used 6/6

B1, B2, B3, B4, B5 & B6

% v/v

Value

Standard

47mm Glass Fibre

0.22

Parameter

EN 13284-1

Sample Point I.D.'s

A2-11 Chemical storage

Parameter

Concentration

0.16 0.16

16.1

±% v/v

Blank 1

Uncertainty

Filter Size and Material

In Stack

Mass Emission g/hr 6.2

Titanium

Filter Housing Material Titanium

Probe Material

Parameter Units

Water Vapour

Parameter Units

Uncertainty ±g/hr

1.68

Technical Procedure

APPENDIX 2

6.2

mg/m³ 0.52

Run 1

Positioning of Filter

TOTAL PARTICULATE MATTER: RESULTS SUMMARY

Mean

16.1

1.68

Run 1

Concentration

Honeywell International Technologies Ltd, Unit 328

Mean

Maximum

mg/m³ 0.22

CAT-RT (Version BJ)

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

Velocity pressure coefficient, Cp

Nozzle area, An

Average square root of velocity heads, √∆P

% v/v

11.3

1.1920

√mmH₂O

16.3

mmH₂O

Vwstd = (0.001246)(Vlc)

0.84

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100)

N/A

No

Pitot tube velocity constant, Kp

44.3

0.06

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

-

Total mass of liquid collected, Vlc g

mmH₂O

0.0203

Volume of gas sample through gas meter, Vm m³

Gas meter correction factor, Yd

15.2

TOTAL PARTICULATE MATTER: ISOKINETIC SAMPLING CALCULATIONS

1.1

Barometric pressure, Pb

g

Test Units

mmH₂O

Run 1

2.7780

762.8

m³/min

Total mass collected in impingers (liquid trap)

Vmstw = (Vmstd)(100/(100 - Rwv))

APPENDIX 2

% v/v

Nozzle diameter, Dn

Average dry gas meter temperature, Tm °C 21.3

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100))

79.14

1.68

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

% v/v

1.2123

Stack static pressure, Pstatic

763.6Ps = (Pb + (Pstatic / 13.6) mmHg

g

Average stack gas temperature, Ts

min

-

Total sampling time, q

0.18

% 108.7

m/s

m³/min

N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

Conversion factor (K/mm.Hg), Cf

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 65.8

6.60Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps))

66.9

m³/min

mm

Bwo = Vwstd / (Vmstd + Vwstd) 0.0168

% wet oxygen measured in gas stream, ACT%O₂w

Average pressure drop across orifice, ∆H

% v/v

-

% oxygen reference condition, REF%O₂ % v/v N/A

% dry oxygen measured in gas stream, ACT%O₂d

-

°C

Total

20.8

3.76

1.94

20.86

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

% v/v 1.68

50.27

N₂

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w)

Average of velocity heads, ∆Pavg

Area of stack, As m²

mm²

- N/A

0.4590

Total mass collected in impingers (silica trap)

0.3592

g/gmol 28.84

% v/v

% v/v

20.80

-

g/gmol 28.66

N/A

Qa = (60)(As)(Vs)

34.97

71.6

8.00

60

mmHg

Vmstd@X%oxygen = (Vmstd) / (O₂REFd)

Velocity of stack gas, Vs

N/A

N/A

-

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

% v/v

CAT-RT (Version BJ)

Page 16 of 38

Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

Filter I.D. Number

Probe Rinse I.D. Number

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

Filter I.D. Number

Probe Rinse I.D. Number

30/10/2015

Balance Uncertainty / LOD

0.00003

mg

gEnd Probe Rinse Mass

g

3.04264

g

g

Total Mass Collected

Volume Sampled (REF) m³

g

0.13921

0.13961

Sampling Times

APPENDIX 2

-

Total Mass in Probe Rinse

09:30 - 10:35

Sampling Dates

End Probe Rinse Mass

-

Parameter Units

g

g

47-27863

Start Filter Mass

Blank 1

End Filter Mass

-

Parameter

Balance Uncertainty / LOD

Calculated Concentration

g

Total Mass Collected

0.00040

-

m³ 1.2123

mg/m³

g

0.11

30/10/2015

-

Calculated Concentration

1.2123

-

Units

TOTAL PARTICULATE MATTER: SAMPLING DETAILS

0.22

Start Filter Mass

0.52

g

Sampling Device

PR-47-27863

mg

Start Probe Rinse Mass

0.00023

3.04267

Total Mass on Filter

Run 1

3.04864

0.63

Average Volume Sampled (REF)

0.00024

mg/m³

Total Mass in Probe Rinse

0.14000

Total Mass on Filter

Start Probe Rinse Mass

g

47-28183

-

0.27

0.11

-

End Filter Mass

mg/m³

3.04887

g

0.13976

PR-47-28183

mg/m³

Blank Dates

ISO

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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Sample Runs

MU (Concurrent Water Vapour)

-

°C

(PAGE 1 OF 2)

Leak Test Acceptable

Run 1

°C

mg/m³ 0.25

Run 1

Overall Weighing Uncertainty ± mg

± mg/m³

Weighing Uncertainty Criteria

Isokineticity Acceptable -

Run 1

Water Droplets

95 - 115

180

Ambient Temperature Recorded? -

Overall Weighing Uncertainty

Units

160

Yes

21

Isokinetic Variation

Yes%

108.7

20

°C

Allowable MU

0.24

-

Yes

APPENDIX 2

Run 1

Allowable Leak Rate

0.10

Isokinetic Criterion Compliance

No

%

0.20

Units Run 1

Test Conditions Units

Allowable Weighing Uncertainty

Pre-Conditioning Temperature

%

Units

Run 1

Leak Test Results

Yes

Pre-Sampling Leak Rate l/min 0.00

l/min

Filter Temperatures

l/min

Post-Conditioning Temperature

Yes

Units

Measurement Uncertainty (MU)

Allowable Isokinetic Range %

Weighing Uncertainty Acceptable

%

ELV [Daily ELV for IED] mg/m³ 5.00

Less than 50% Faded

%

Yes

Units Run 1

Mean Sampling Rate l/min 21.25

Units

TOTAL PARTICULATE MATTER: QUALITY ASSURANCE

MU Acceptable

0.43

-

Silica Gel (Concurrent Water Vapour) Units

Maximum Filter Temperature

Run 1

Post-Sampling Leak Rate

Are Water Droplets Present

9.6

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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Blank Runs

Method Deviations

1

x

x

x

x

- - - - -

- - - - -

Expected Sampling Rate

-

20.00

Validity of Blank vs ELV

l/min

Nature of Deviation

Blank 1

l/min

YesBlank Acceptable

Post-Sampling Leak Rate

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Blank Acceptable

Allowable Blank

mg/l

Acetone / Water Rinse Blank Units Blank

Pre-Sampling Leak Rate

2.7mg/l

10

mg/m³

Units Blank 1

-

l/min

Run Number

0.00

Allowable Leak Rate

1.0

Allowable Blank

0.40

APPENDIX 2

TOTAL PARTICULATE MATTER: QUALITY ASSURANCE

Units

0.00

Acetone / Water Rinse Value

l/min

(PAGE 2 OF 2)

Lowest differential pressure < 5 Pa.

The sample points where the angle of swirl was > 15° were omitted from the sampling exercise.

Ratio highest to lowest velocities > 5 : 1.

The sample points where negative flow was measured during the preliminary traverse were omitted from the sampling exercise.

YesLeak Test Acceptable

Leak Test Results

Yes-

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

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Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

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Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (STP)

Leak

Mass of Particulate

Uncollected Mass

Sampled Volume (STP)

Leak

Mass of Particulate

Uncollected Mass

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

mg/m³

mg

% 2.14

%

1.1920

1.34

Measured Quantities

mg/m³

294.3Tm

uHm

0.0556

% v/v

uρm 0.5ρm 101.8

Uncertainty in Result

0.27

0.0014

<5% of ELV

Measured Quantities

1.00

0.13

≤1%

≤1%

uUCM mg -

0.82Lr mg

Units

Vm

≤2%

Vm

-L 0.47

1.0

≤2%

%

mg/m³ 0.33

%

%

0.17

N/A

% 258.6

2.00

% 0.47

2.7780

-

Run 1 Requirement of Standard

0.63

0.0

uVm m³

mg/m³

N/A

Uncertainty as a Percentage

UCM

258.6

%

mg/m³

% v/v N/A

Symbol Units Run 1

kPa

uL %

m mg

APPENDIX 2

TOTAL PARTICULATE MATTER: MEASUREMENT UNCERTAINTY CALCULATIONS

Value Standard uncertainty

Measured Quantities Symbol Run 1

um

Hm

uTm K 2.0

63.9

0.630

0.82

%

Measured Quantities

Units

0.16

-

0.49

mg/m³

Run 1

N/A

Parameter

0.025

mg/m³

0.1286

0.68

%

0.44

- N/A

0.001

Run 1

Run 1

UCM

L

Run 1

≤1%

mg/m³ 1.34

1.00

mg/m³

Sensitivity Coefficient

Units

Overall MU For O₂ Measurement

mg/m³

Symbol Units

-

% N/A

Units

%

Uncertainty in Measurement Units

Oxygen Correction Part of MU Budget

Measured Quantities Run 1

0.1072

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

- -

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Number of Sampling Points Used

Number of Sampling Lines Used

Yes

Standard EN 14385

Technical Procedure CAT-TP-06

ISO 17025 Accredited Analysis?

Filter Size and Material 47mm Quartz Fibre

0.15

Mass Emission g/hr 0.1

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter

1.36

Uncertainty ±% v/v 0.15

Date of Sample Analysis 11/11/2015

Out Stack

0.0017

Parameter Value

Probe Material

Water Vapour % v/v

0.0017

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure M31

APPENDIX 2

Honeywell International Technologies Ltd, Unit 328

Parameter Units Run 1 Mean

MaximumUnits Blank 1

0.0078

Uncertainty ±mg/m³

Parameter

0.1

1.36

0.0069

Units Run 1 Mean

Concentration mg/m³ 0.0078

Titanium

6/6

Sample Point I.D.'s

Filter Housing Material Titanium

Impinger Material

1/3

Uncertainty ±g/hr 0.1

0.0069

Concentration mg/m³

B1, B2, B3, B4, B5 & B6

NICKEL: RESULTS SUMMARY

A2-11 Chemical storage

Parameter

0.1

CAT-RT (Version BJ)

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Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol 28.69

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

Total mass collected in impingers (liquid trap) g 4.3

% dry oxygen measured in gas stream, ACT%O₂d % v/v N/A

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂) g/gmol

Velocity pressure coefficient, Cp - 0.84

Average of velocity heads, ∆Pavg mmH₂O 1.19

g

Barometric pressure, Pb mmHg

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) - N/A

% v/v 1.36

Vmstw = (Vmstd)(100/(100 - Rwv))

Test Units Run 1

- 0.4590

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) - No

20.80

N₂ % v/v 79.14

N/A

% oxygen reference condition, REF%O₂ % v/v N/A

Total

0.0

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

NICKEL: ISOKINETIC SAMPLING CALCULATIONS

22.9

11.3

0.0054

Volume of gas sample through gas meter, Vm

Ps = (Pb + (Pstatic / 13.6) mmHg 763.6

762.8

Average pressure drop across orifice, ∆H mmH₂O

Average dry gas meter temperature, Tm °C 27.0

APPENDIX 2

Stack static pressure, Pstatic

20.86

% wet oxygen measured in gas stream, ACT%O₂w % v/v

- N/A

g 4.3

Total mass collected in impingers (silica trap)

% v/v 0.06

% v/v

Bwo = Vwstd / (Vmstd + Vwstd)

mmH₂O

0.3953

m³ 0.0136

0.3899Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273) m³

Total mass of liquid collected, Vlc

Vwstd = (0.001246)(Vlc)

% v/v 1.36

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

m³ 0.9280

Gas meter correction factor, Yd

28.84

Pitot tube velocity constant, Kp - 34.97

% v/v

Area of stack, As m² 0.18

Average square root of velocity heads, √∆P √mmH₂O 1.09

Average stack gas temperature, Ts °C 21.0

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 3.71

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw) m³/min N/A

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd) m³/min N/A

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) m³/min 37.1

Conversion factor (K/mm.Hg), Cf - 0.3592

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273) m³/min 37.6

Qa = (60)(As)(Vs) m³/min 40.3

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 99.6

Nozzle diameter, Dn mm 9.00

Nozzle area, An mm² 63.63

Total sampling time, q min 30

CAT-RT (Version BJ)

Page 22 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

-

<

Mass in Back Impinger <

-

-

-

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

-

<

Mass in Back Impinger <

-

-

-Reported Concentration 0.0017

APPENDIX 2

NICKEL: SAMPLING DETAILS

Parameter Units Run 1

Volume Sampled (REF) m³ 0.3953

Mass on Filter / in Rinse µg 3.00

Sampling Times - 08:50 - 09:20

Sampling Dates - 30/10/2015

Sampling Device - ISO

Total Mass Collected µg 3.08

Mass in Front Impingers µg 0.05

µg 0.02

Parameter Units Blank 1

Blank Dates - 30/10/2015

Average Volume Sampled (REF) m³ 0.3953

Calculated Concentration mg/m³ 0.0078

Total Mass Collected µg 0.66

Reported Concentration mg/m³ 0.0078

Mass on Filter / in Rinse µg 0.60

Mass in Front Impingers µg 0.05

µg 0.02

Calculated Concentration mg/m³ 0.0017

mg/m³

CAT-RT (Version BJ)

Page 23 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

µg/m³ 5Allowable Detection Limit

- YesDetection Limit Acceptable

Pre-Sampling Leak Rate l/min 0.10

Post-Sampling Leak Rate l/min 0.10

Allowable Absorption Efficiency % 90

APPENDIX 2

NICKEL: QUALITY ASSURANCE

(PAGE 1 OF 2)

Leak Test Results Units Run 1

Mean Sampling Rate l/min 14.20

Detection Limit µg/m³ 1.1

Leak Test Acceptable - Yes

Absorption Efficiency Units Run 1

Absorption Efficiency % 100.0

Measurement Uncertainty (MU) % 11.0

Allowable MU % 20

Allowable Leak Rate l/min 0.28

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Water Droplets Units Run 1

Are Water Droplets Present - No

MU (Concurrent Water Vapour) Units Run 1

Yes

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 99.6

Maximum Filter Temperature °C 180

Impingers Exit Temperature Units Run 1

MU Acceptable % Yes

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded %

Allowable Isokinetic Range % 95 - 115

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Test Conditions Units Run 1

Ambient Temperature Recorded? - Yes

Maximum Temperature Recorded °C 14

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable - Yes

CAT-RT (Version BJ)

Page 24 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

x

x

x

x

- - - - -

- - - - -

APPENDIX 2

NICKEL: QUALITY ASSURANCE(PAGE 2 OF 2)

Leak Test Results Units Blank 1

Allowable Leak Rate l/min 0.30

Leak Test Acceptable - Yes

Pre-Sampling Leak Rate l/min 0.00

Post-Sampling Leak Rate l/min 0.00

N/A

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Lowest differential pressure < 5 Pa.

The sample points where the angle of swirl was > 15° were omitted from the sampling exercise.

Ratio highest to lowest velocities > 5 : 1.

The sample points where negative flow was measured during the preliminary traverse were omitted from the sampling exercise.

Validity of Blank vs ELV Units Blank 1

Allowable Blank mg/m³

Expected Sampling Rate l/min 15.00

CAT-RT (Version BJ)

Page 25 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 174: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Units

% v/v

Measured Quantities

APPENDIX 2

K 2.0

mg/m³ 0.0069

mg/m³ N/A

Run 1

mg/m³

% N/A

mg/m³ 0.0069

Parameter Units

0.0009

mg/m³ 0.0017

% 21.9

% 88.6

% 88.6

≤1%

- N/A

Measured Quantities Units

Run 1

Run 1

Overall MU For O₂ Measurement

1.00

Uncertainty as a Percentage

Uncertainty in Measurement Units Sensitivity Coefficient

%

% N/A

Units Run 1

Oxygen Correction Part of MU Budget

Symbol Units Run 1

1.00

Uncertainty in Result

Lr mg/m³ 0.0008

N/A

mg/m³ 0.0004

Symbol

uVm m³ 0.0186

Tm 300.0

Units Run 1 Requirement of Standard

≤1%

% 0.49

Run 1

%

ρm 101.8 uρm kPa

% 10.00

≤1%

2.00 ≤2%

uTm

0.5

NICKEL: MEASUREMENT UNCERTAINTY CALCULATIONS

uL % -

uLr % -

Value Standard uncertainty

Measured Quantities Symbol Run 1

Hm 0.0

Vm m³ 0.3899

1.00

Lr 10.00

No Requirement

uHm % v/v 1.0

L 0.70

%

N/A

0.70

Vm 0.9280

Measured Quantities

Measured Quantities

≤2%

mg/m³ 0.0008

0.02

% 0.67

%

mg/m³ 0.0000

mg/m³ 0.0000

L

CAT-RT (Version BJ)

Page 26 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:54

Page 175: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

- -

- -

- -

- -

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

Mean

Concentration mg/m³ 0.0849 0.0849

Probe Material

Mean

Standard EN 14385

Technical Procedure CAT-TP-06

M31

ISO 17025 Accredited Analysis? Yes

Date of Sample Analysis 11/11/2015

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure

Uncertainty ±g/hr 1.0 1.0

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Number of Sampling Lines Used 1/3

Number of Sampling Points Used 6/6

Sample Point I.D.'s B1, B2, B3, B4, B5 & B6

Borosilicate Glass

Uncertainty ±mg/m³ 0.0813 0.0813

Mass Emission g/hr

Parameter Units Run 1

Water Vapour % v/v 1.36

1.0 1.0

APPENDIX 2

IRON: RESULTS SUMMARY

Honeywell International Technologies Ltd, Unit 328

A2-11 Chemical storage

Parameter Units Run 1

Concentration mg/m³ 0.0192 0.0192

1.36

Uncertainty ±% v/v 0.15 0.15

Parameter Units Blank 1 Maximum

Titanium

Parameter Value

Filter Housing Material Titanium

Impinger Material

CAT-RT (Version BJ)

Page 27 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 176: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

% v/v 1.36

Gas meter correction factor, Yd - 0.4590

N/A

0.3953

Total mass of liquid collected, Vlc g

m³ 0.0054

m³/min

Average of velocity heads, ∆Pavg mmH₂O

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d) -

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w) -

Total % v/v 20.86

Pitot tube velocity constant, Kp

Volume of gas sample through gas meter, Vm

°C

27.0

Average pressure drop across orifice, ∆H

20.80

Average dry gas meter temperature, Tm °C

% v/v

% v/v

% wet oxygen measured in gas stream, ACT%O₂w % v/v

0.84

1.19

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps)) m/s 3.71

0.3899

Stack static pressure, Pstatic mmH₂O

No

11.3

0.9280

% v/v 1.36

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273)

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction)

N/A

21.0

4.3

Test Units Run 1

Barometric pressure, Pb mmHg 762.8

APPENDIX 2

IRON: ISOKINETIC SAMPLING CALCULATIONS

763.6

Bwo = Vwstd / (Vmstd + Vwstd) m³ 0.0136

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (liquid trap) g 4.3

-

Vwstd = (0.001246)(Vlc)

mmH₂O 22.9

Total mass collected in impingers (silica trap) g 0.0

Vmstw = (Vmstd)(100/(100 - Rwv))

% dry oxygen measured in gas stream, ACT%O₂d

g/gmol 28.84

- 0.3592

N/A

N/A

- 34.97

% v/v 79.14

Nozzle diameter, Dn

m³/min

Total sampling time, q min 30

Velocity pressure coefficient, Cp -

mm 9.00

mm²

Average square root of velocity heads, √∆P √mmH₂O

0.18

63.63

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100)) % 99.6

Conversion factor (K/mm.Hg), Cf

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

Nozzle area, An

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

% v/v

m³/min 37.6

Qstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

1.09

28.69

Vmstw@X%oxygen = (Vmstw) / (O₂REFw) m³ N/A

Vmstd@X%oxygen = (Vmstd) / (O₂REFd) m³ N/A

N₂

% oxygen reference condition, REF%O₂ % v/v N/A

Average stack gas temperature, Ts

Area of stack, As m²

0.06

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

Qa = (60)(As)(Vs) 40.3

37.1

m³/min

m³/min N/A

N/A

CAT-RT (Version BJ)

Page 28 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

-

-

Mass in Back Impinger -

-

-

-

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<

Blank Dates

7.00

mg/m³ 0.0849Reported Concentration

-

Mass in Front Impingers µg

Calculated Concentration mg/m³ 0.0192

30/10/2015

µg 0.45

Units

Units

Average Volume Sampled (REF)

Volume Sampled (REF) m³

Total Mass Collected

- 08:50 - 09:20

Mass on Filter / in Rinse

-

IRON: SAMPLING DETAILS

Parameter

4.430

33.545

Mass on Filter / in Rinse µg

Blank 1

Sampling Dates

1.115µg

Total Mass Collected µg

APPENDIX 2

0.15

Run 1

µg

Sampling Times

28.000

0.3953

Calculated Concentration mg/m³ 0.0849

Parameter

ISO

m³ 0.3953

7.60

Sampling Device

- 30/10/2015

Reported Concentration mg/m³

Mass in Front Impingers

0.0192

µg

µg

CAT-RT (Version BJ)

Page 29 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Sample Runs

No

Test Conditions Run 1

%

0.10

%

No

20

5Allowable Detection Limit

-

Measurement Uncertainty (MU) % 11.0

14.20

%

l/min 0.10

APPENDIX 2

Yes

95 - 115

Mean Sampling Rate

%Allowable MU

Run 1

Yes

Pre-Sampling Leak Rate

Allowable Absorption Efficiency

l/min

µg/m³

Leak Test Acceptable

Filter Temperatures Units Run 1

- Yes

0.28

Maximum Allowable Temperature

Exit Temperature Acceptable - Yes

Run 1

Allowable Leak Rate l/min

MU Acceptable

Detection Limit Acceptable

Run 1

Detection Limit 7.0

Isokineticity Acceptable

%

µg/m³

Impingers Exit Temperature

Isokinetic Criterion Compliance Units Run 1

-

Are Water Droplets Present

IRON: QUALITY ASSURANCE

(PAGE 1 OF 2)

Less than 50% Faded

Silica Gel (Concurrent Water Vapour) Units

Units Run 1

Water Droplets Units

-

Absorption Efficiency

-

Isokinetic Variation

MU (Concurrent Water Vapour) Units

Yes

Absorption Efficiency Acceptable - Yes

Detection Limit Units Run 1

Absorption Efficiency Units Run 1

Leak Test Results Units Run 1

180

Post-Sampling Leak Rate l/min

% 96.7

Allowable Isokinetic Range %

Ambient Temperature Recorded?

Yes

Units

°C

90

°C

°C

Maximum Filter Temperature

Maximum Temperature Recorded

99.6

14

30

CAT-RT (Version BJ)

Page 30 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Blank Runs

Method Deviations

1

x

x

x

x

- - - - -

- - - - -

l/min

Units

The sample points where negative flow was measured during the preliminary traverse were omitted from the sampling exercise.

15.00

APPENDIX 2

Validity of Blank vs ELV

Allowable Leak Rate l/min 0.30

Expected Sampling Rate l/min

IRON: QUALITY ASSURANCE

Lowest differential pressure < 5 Pa.

Blank 1

The sample points where the angle of swirl was > 15° were omitted from the sampling exercise.

Ratio highest to lowest velocities > 5 : 1.

(PAGE 2 OF 2)

Leak Test Results

0.00

Post-Sampling Leak Rate l/min 0.00

mg/m³ N/A

Pre-Sampling Leak Rate

Units Blank 1

Leak Test Acceptable - Yes

Blank Acceptable - N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Allowable Blank

CAT-RT (Version BJ)

Page 31 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 180: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

N/A

Run 1

Sensitivity Coefficient

mg/m³

Parameter

mg/m³ N/A

% N/A

IRON: MEASUREMENT UNCERTAINTY CALCULATIONS

2.0

% v/v N/A

95.8

% 95.8

%

0.0186

Value

Run 1

uVm

APPENDIX 2

Run 1

Tm

Units

0.0003

≤1%

0.0813

Run 1

0.0093

1.00%

L mg/m³

Uncertainty in Result

0.0042mg/m³

0.0003

uρm

0.22

Units

Oxygen Correction Part of MU Budget

Measured Quantities

Overall MU For O₂ Measurement %

Uncertainty as a Percentage

Symbol

≤2%%

Measured Quantities Symbol

1.00

-

% 0.67

0.3899

% 11.00

≤1%

Requirement of StandardMeasured Quantities

2.00

kPa 0.5

Vm 0.9280

0.70

uLr %Lr

Units

uL %

uHm % v/v

Standard uncertainty

1.0

L 0.70

ρm 101.8

-

mg/m³ 0.0201

0.0102

300.0

% 0.49

N/A

Run 1

UnitsMeasured Quantities

Hm 0.0

Units

mg/m³

Run 1

≤2%%

Run 1

11.00

Uncertainty in Measurement Units

mg/m³

Run 1

No Requirement

uTm

Measured Quantities

Vm

mg/m³

1.00Lr mg/m³ 0.0093

K

mg/m³ 0.0813

23.6

Symbol

≤1%

%

-

% N/A

Units

CAT-RT (Version BJ)

Page 32 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

For

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Sample Runs

- -

< <

- -

< <

- -

- -

- -

- -

Blank Runs

- -

< <

General Sampling Information

FORMAT: Number Used / Number Required

FORMAT: Number Used / Number Required

Reference Conditions

Reference Conditions are: 273K, 101.3kPa, without correction for water vapour content.

1.36

Uncertainty ±% v/v

Concentration mg/m³

APPENDIX 2

TITANIUM: RESULTS SUMMARY

0.0166

0.15

Probe Material Titanium

Filter Housing Material Titanium

Impinger Material

Value

0.0152

Honeywell International Technologies Ltd, Unit 328

A2-11 Chemical storage

0.15

0.0166

Technical Procedure CAT-TP-06

Name of Analytical Laboratory RPS

Analytical Laboratory's Procedure M31

ISO 17025 Accredited Analysis? Yes

Date of Sample Analysis 11/11/2015

Sample Point I.D.'s B1, B2, B3, B4, B5 & B6

0.0173

0.2

0.0152

Parameter

Borosilicate Glass

Absorption Solution Nitric Peroxide

Positioning of Filter Out Stack

Filter Size and Material 47mm Quartz Fibre

Standard EN 14385

Units

0.2

Number of Sampling Points Used 6/6

Mean

Water Vapour % v/v 1.36

Number of Sampling Lines Used 1/3

Mean

Mass Emission g/hr

Maximum

Run 1

Parameter Units

0.2

0.0173

±g/hr

Uncertainty ±mg/m³

Uncertainty 0.2

Parameter Run 1

Concentration mg/m³

Parameter

Units

Blank 1

CAT-RT (Version BJ)

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Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:54

Page 182: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Absolute pressure of stack gas, Ps

Volume of water vapour collected, Vwstd

Volume of gas metered dry, Vmstd

Moisture content, Bwo & Rwv

Bwo as a percentage

Reported Water Vapour, checked with Tables in EN 14790, Rwv

Volume of gas metered wet, Vmstw

Volume of gas metered at Oxygen Reference Conditions, Vmstd@X%O₂ & Vmstw@X%O₂

Molecular weight of dry gas stream, Md

CO₂ (Estimated)

O₂ (Estimated)

Molecular weight of stack gas (wet), Ms

Velocity of stack gas, Vs

Total flow of stack gas: Actual (Qa), Wet (Qstw), Dry (Qstd), Wet@O₂REF (QstwO₂), Dry@O₂REF (QstdO₂)

Percent isokinetic, %I

m³ 0.0136

Volume of gas sample through gas meter, Vm m³

% wet oxygen measured in gas stream, ACT%O₂w % v/v

N/A

0.3899

Vmstw = (Vmstd)(100/(100 - Rwv))

1.36

g 0.0

Average dry gas meter temperature, Tm °C 27.0

1.19

Pitot tube velocity constant, Kp

Md = 0.44(%CO₂)+0.32(%O₂)+0.28(%N₂)

-

m³ 0.3953

O₂ Reference Factor dry (O₂REFd) = (21 - REF%O₂) / (21 - ACT%O₂d)

-

% oxygen reference condition, REF%O₂

% v/v

Gas meter correction factor, Yd - 0.4590

% v/v

0.0054

O₂ Reference Factor wet (O₂REFw) = (21 - REF%O₂) / (21 - ACT%O₂w)

Vmstw@X%oxygen = (Vmstw) / (O₂REFw)

28.69Ms = Md(1 - (Rwv/100)) + 18(Rwv/100) g/gmol

- N/A

Vmstd = ((0.3592)(Vm)(Pb + (∆H/13.6))(Yd)) / (Tm + 273)

mmH₂O

Average pressure drop across orifice, ∆H

% v/v

Total mass of liquid collected, Vlc g

Bwo = Vwstd / (Vmstd + Vwstd)

% v/v 79.14

11.3

Vwstd = (0.001246)(Vlc) m³

Vs = ((Kp)(Cp)(√∆P)(√Ts + 273)) / (√(Ms)(Ps))

% v/v

%I = (4.6398E⁶)(Ts+273)(Vmstd) / (Ps)(Vs)(An)(q)(1 - (Rwv/100))

QstdO₂ = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273) / (O₂REFd)

99.6

1.09√mmH₂OAverage square root of velocity heads, √∆P

m³/min N/A

40.3

min

QstwO₂ = ((Qa)(Ps)(Cf)) / ((Ts) + 273) / (O₂REFw)

37.6

Conversion factor (K/mm.Hg), Cf

0.18

30

Nozzle area, An

m³/min

m³/min

N/A

%

Qa = (60)(As)(Vs)

Total sampling time, q

N/A

N/A

Average stack gas temperature, Ts °C 21.0

m/s

m³/min

m³/minQstd = ((Qa)(Ps)(Cf)(1 - (Rwv/100))) / ((Ts) + 273)

Qstw = ((Qa)(Ps)(Cf)) / ((Ts) + 273)

Area of stack, As

0.3592

9.00

1.36

% v/v N/A

0.9280

% dry oxygen measured in gas stream, ACT%O₂d

IED & Incinerates Hazardous Material? (Yes = no positive O₂ correction) -

3.71

Stack static pressure, Pstatic

762.8

Ps = (Pb + (Pstatic / 13.6) mmHg

Total mass collected in impingers (silica trap)

Units Run 1

4.3

APPENDIX 2

TITANIUM: ISOKINETIC SAMPLING CALCULATIONS

Test

N₂

% v/v 0.06

Total mass collected in impingers (liquid trap)

Average of velocity heads, ∆Pavg mmH₂O

Nozzle diameter, Dn mm

763.6

mm² 63.63

mmH₂O 22.9

g

0.84

Total % v/v

N/A

20.86

4.3

No

Vmstd@X%oxygen = (Vmstd) / (O₂REFd)

- 34.97

Velocity pressure coefficient, Cp -

N/A

20.80

g/gmol 28.84

37.1

Barometric pressure, Pb mmHg

CAT-RT (Version BJ)

Page 34 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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EPA Export 14-04-2016:01:16:54

Page 183: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

<

<

Mass in Back Impinger <

<

<

<

Where: ISO stands for Manual Isokinetic Sampling Train

Blank Runs

<

<

Mass in Back Impinger <

<

<

<

0.3953

APPENDIX 2

3.000µg

2.606Mass in Front Impingers

Parameter

- 30/10/2015

0.3953m³

Blank Dates

Units

Reported Concentration mg/m³ 0.0152

Calculated Concentration

Total Mass Collected µg 6.019

Calculated Concentration mg/m³ 0.0152

mg/m³

Mass in Front Impingers µg 2.257

µg 0.762

Sampling Times

- 30/10/2015

Total Mass Collected

µg

µg 6.845

Volume Sampled (REF)

1.239

0.0173

Sampling Dates

- ISOSampling Device

- 08:50 - 09:20

Blank 1

Reported Concentration mg/m³ 0.0173

Average Volume Sampled (REF)

µg 3.000

TITANIUM: SAMPLING DETAILS

Parameter

µg

Mass on Filter / in Rinse

Mass on Filter / in Rinse

Units Run 1

CAT-RT (Version BJ)

Page 35 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 184: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sample Runs

Yes

Impingers Exit Temperature

Maximum Filter Temperature °C 180

Test Conditions Units Run 1

Ambient Temperature Recorded? -

Units Run 1

Isokinetic Criterion Compliance Units Run 1

Isokinetic Variation % 99.6

Isokineticity Acceptable - Yes

Filter Temperatures Units Run 1

Silica Gel (Concurrent Water Vapour) Units Run 1

Less than 50% Faded % Yes

Detection Limit Acceptable - No

Yes

-

14

Maximum Allowable Temperature °C 30

Exit Temperature Acceptable

Allowable MU %

Run 1

Detection Limit µg/m³ 5.1

Allowable Detection Limit µg/m³ 5

Allowable Isokinetic Range % 95 - 115

Maximum Temperature Recorded °C

Measurement Uncertainty (MU) % 11.0

20

MU Acceptable % Yes

Units Run 1

Are Water Droplets Present - No

Mean Sampling Rate l/min 14.20

Pre-Sampling Leak Rate l/min 0.10

Allowable Absorption Efficiency % 90

Absorption Efficiency Acceptable - Yes

Detection Limit Units

MU (Concurrent Water Vapour) Units Run 1

Post-Sampling Leak Rate l/min 0.10

Allowable Leak Rate l/min 0.28

Leak Test Acceptable

Absorption Efficiency % 100.0

Water Droplets

Absorption Efficiency Units Run 1

APPENDIX 2

TITANIUM: QUALITY ASSURANCE

- Yes

(PAGE 1 OF 2)

Leak Test Results Units Run 1

CAT-RT (Version BJ)

Page 36 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 185: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Blank Runs

Method Deviations

1

x

x

x

x

- - - - -

- - - - -

Expected Sampling Rate l/min 15.00

TITANIUM: QUALITY ASSURANCE

The sample points where the angle of swirl was > 15° were omitted from the sampling exercise.

The sample points where negative flow was measured during the preliminary traverse were omitted from the sampling exercise.

mg/m³ N/A

N/A

Nature of Deviation Run Number

(x = deviation applies to the associated run, wx = deviation also applies to the concurrent water vapour run)

Lowest differential pressure < 5 Pa.

Ratio highest to lowest velocities > 5 : 1.

Blank Acceptable -

Allowable Leak Rate l/min 0.30

Leak Test Acceptable - Yes

l/min 0.00Post-Sampling Leak Rate

0.00

Validity of Blank vs ELV Units Blank 1

Allowable Blank

Units Blank 1

(PAGE 2 OF 2)

Leak Test Results

APPENDIX 2

Pre-Sampling Leak Rate l/min

CAT-RT (Version BJ)

Page 37 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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Page 186: Environmental Protection Agency · Absolute pressure of stack gas, P s Volume of water vapour collected, V wstd Volume of gas metered dry, V mstd Moisture content, B wo & R wv B wo

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (Actual)

Sampled Gas Temperature

Sampled Gas Pressure

Sampled Gas Humidity

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

Sampled Volume (STP)

Leak

Laboratory Result

O₂ Correction Factor

Stack Gas O₂ Content

MU for O₂ Correction

Combined uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Expanded uncertainty (95% confidence), without Oxygen Correction

Expanded uncertainty (95% confidence), with Oxygen Correction

Expanded uncertainty (95% confidence), estimated with Method Deviations

Reported Uncertainty

Units

-

0.0

% v/v N/A

% N/A

Units

%

Vm

Uncertainty in Measurement Units

Measured Quantities

0.0001

%

mg/m³

Oxygen Correction Part of MU Budget

Uncertainty as a Percentage

mg/m³

-

Value

≤2%

N/A

Lr mg/m³

0.0021

Uncertainty in Result

mg/m³

% 1.00

11.00

1.00

1.00

Sensitivity Coefficient

Symbol

0.49

uρm kPa

TITANIUM: MEASUREMENT UNCERTAINTY CALCULATIONS

Tm 300.0

Run 1

1.0

101.8

L

≤1%

Run 1

Hm

Overall MU For O₂ Measurement

uTm K

0.5

Symbol

uLr

Measured Quantities Units Run 1

mg/m³

0.70

% N/A

Units

Parameter

mg/m³ 0.0041

≤1%

%

Units Run 1

% N/A

0.0009

Measured Quantities

% 2.00

mg/m³

2.0

L

Measured Quantities

APPENDIX 2

Lr 11.00

Standard uncertainty

ρm

m³ 0.0186

Run 1Measured Quantities Symbol Run 1

uVm

uHm % v/v

0.0019

%

≤2%

% 0.67

Run 1 Run 1

0.0001

Vm 0.9280

95.8

mg/m³ 0.0166

mg/m³ 0.0166

95.8

% 23.6

%

mg/m³ N/A

uL %

No Requirement

Requirement of Standard

% -

Units

0.3899

≤1%

0.0019

0.04

0.70

CAT-RT (Version BJ)

Page 38 of 38

Honeywell International Technologies Ltd

Unit 328

A2-11 Chemical storage

Job Number: CDU-0559, Version 1

Sample Date/s: 29th - 30th October 2015

Irish EPA IPPC Licence: P0698-01

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