blacktip annual environmental performance report …€¦ · - the quarterly discharge sample for...
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REVISION HISTORY
Rev. Date Nr. of
sheets
Description
00 07/02/17 125 Issued for Comments
01 14/02/17 128 Re-Issued for Comments
02 27/02/17 99 Final Issue
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TABLE OF CONTENTS
1. EXECUTIVE SUMMARY ........................................................................................ 7
2. INTRODUCTION .................................................................................................. 8
2.1 Project background ...................................................................................... 8
2.2 Purpose of the report ................................................................................... 9
3. OVERVIEW OF YELCHERR GAS PLANT ............................................................... 11
3.1 General overview ........................................................................................ 11
3.2 Plant configuration ...................................................................................... 11
3.3 Other facilities ............................................................................................ 14
4. PRODUCTION .................................................................................................... 16
4.1 Overview ................................................................................................... 16
4.2 Condensate ................................................................................................ 16
4.3 Gas production ........................................................................................... 17
4.4 Gas composition ......................................................................................... 18
5. ATMOSPHERIC EMISSIONS ............................................................................... 20
5.1 Overview of atmospheric emissions ............................................................... 20
5.2 Fuel gas consumption .................................................................................. 20
5.3 Flaring ....................................................................................................... 23
5.4 Diesel usage .............................................................................................. 26
5.5 Stack emission monitoring ........................................................................... 27
5.6 Air Emissions Assessment Report .................................................................. 28
5.7 Pollutant inventory ...................................................................................... 28
5.8 Fugitive emissions assessment ..................................................................... 29
6. LIQUID WASTE DISCHARGES ............................................................................ 30
6.1 Produced water .......................................................................................... 30
6.1.1 Overview ........................................................................................... 30
6.1.2 Discharge and routine monitoring .......................................................... 30
6.1.3 Quarterly chemical characterisation ....................................................... 31
6.1.4 Produced Formation Water Plan............................................................. 32
6.1.5 Annual Marine Monitoring ..................................................................... 32
6.2 Treated Wastewater Effluent ........................................................................ 32
6.3 Stormwater ................................................................................................ 33
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7. SOLID WASTE ................................................................................................... 34
8. GROUND WATER ............................................................................................... 35
8.1 Ground water use ....................................................................................... 35
8.2 Ground water monitoring ............................................................................. 35
9. INCIDENTS AND NON-CONFORMANCES ............................................................ 37
9.1 Incidents and non-compliances ..................................................................... 37
9.2 Complaints ................................................................................................ 40
9.3 Audits and inspections ................................................................................. 40
9.4 Continuous improvement and other activities ................................................. 40
10. COMMUNITY INITIATIVES ................................................................................ 41
11. ACRONYMS ....................................................................................................... 42
12. REFERENCES ..................................................................................................... 44
TABLES
Table 3.1: YGP Coordinates ......................................................................................... 11
Table 3.2: YGP process area functionality ...................................................................... 13
Table 4.1: Overview of production ................................................................................ 16
Table 4.2: Blacktip reservoir fluid properties .................................................................. 18
Table 4.3: Contaminants in Blacktip Gas ....................................................................... 18
Table 5.1: Gas flow meters ......................................................................................... 20
Table 5.2: Gas consumption at YGP .............................................................................. 20
Table 5.3: Gas flared at YGP ........................................................................................ 23
Table 5.4: Annual diesel consumption and GHG emissions .............................................. 26
Table 5.5: Air emissions improvement plan ................................................................... 28
Table 6.1: Produced water discharge annually ............................................................... 31
Table 6.2: Treated wastewater effluent reuse ................................................................ 32
Table 7.1: Waste disposal ........................................................................................... 34
Table 8.1: Total annual volume of groundwater abstracted .............................................. 35
Table 9.1 : Environmental non-compliances ................................................................... 37
Table 9.2 : Environmental notifications to NTEPA ............................................................ 39
Table G.1: Quarterly groundwater monitoring data 2016 ................................................. 88
Table G.2: Results of further groundwater investigations ................................................. 95
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FIGURES
Figure 2.1: Blacktip Field location ................................................................................... 8
Figure 2.2: Yelcherr Gas Plant and Offshore Pipeline Facilities ............................................ 9
Figure 3.1: Blacktip YGP layout ..................................................................................... 12
Figure 3.2: YGP Process Block Diagram .......................................................................... 14
Figure 4.1: Overview of production ................................................................................ 16
Figure 4.2: Gas production in 2015 ............................................................................... 17
Figure 4.3: Gas production in 2016 ............................................................................... 17
Figure 5.1: Gas consumed for compressors and power generation in 2015 ......................... 21
Figure 5.2: Gas consumed for compressors and power generation in 2016 ......................... 21
Figure 5.3: GHG emissions from gas consumed by compressors and power generation in
2015 ......................................................................................................... 23
Figure 5.4: GHG emissions from gas consumed by compressors and power generation in
2016 ......................................................................................................... 23
Figure 5.5: Volume of gas flared from Blacktip YGP in 2015 .............................................. 24
Figure 5.6: Volume of gas flared from Blacktip YGP in 2016 .............................................. 24
Figure 5.7: GHG emissions from flaring in 2015 .............................................................. 25
Figure 5.8: GHG emissions from flaring in 2016 .............................................................. 26
Figure 6.1: Volume of produced formation water discharged from Blacktip YGP ................... 31
Figure 8.1: Groundwater abstraction and monitoring bores .............................................. 35
Figure G.1: Groundwater trends – pH............................................................................. 90
Figure G.2: Groundwater trends – EC ............................................................................. 90
Figure G.3: Groundwater trends – TDS ........................................................................... 91
Figure G.4: Groundwater trends – turbidity ..................................................................... 91
Figure G.5: Groundwater trends – total suspended solids ................................................. 91
Figure G.6: Groundwater trends – biochemical oxygen demand ......................................... 92
Figure G.7: Groundwater trends – dissolved oxygen ........................................................ 92
Figure G.8: Groundwater trends – oil in water ................................................................. 92
Figure G.9: Groundwater trends – NOx .......................................................................... 93
Figure G.10: Groundwater trends – Total P ....................................................................... 93
Figure G.11: Groundwater trends – Total N ...................................................................... 93
Figure G.12: Groundwater trends – Ammonia ................................................................... 94
Figure G.13: Groundwater trends – E.Coli ........................................................................ 94
Figure G.14: Twice-weekly groundwater level ................................................................... 98
Figure G.15: Twice-weekly groundwater conductivity trends ............................................... 98
Figure G.16: Twice-weekly groundwater pH trends ............................................................ 99
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APPENDICES 46
Appendix A: Annual Return 47
Appendix B: Pollutant Mass Inventory 65
Appendix C: Emissions Sampling Results 71
Appendix D: Produced Water Monitoring Results 76
Appendix E: WWTP Sampling Results 81
Appendix F: Stormwater Monitoring Results 84
Appendix G: Groundwater Monitoring Data 87
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1. EXECUTIVE SUMMARY
The Blacktip Annual Environmental Performance Report 2016 summarises the
environmental performance of the Yelcherr Gas Plant for the reporting period 10
February 2016 to 9 February 2017 as required by condition 40 of the Environment
Protection Licence EPL57-02, which is currently in force. EPL57-02 was issued to Eni
on 10 February 2015 as an amendment to the previous licence, EPL57-01. The
Report includes the Annual Return in Appendix A, which provides an overview of
compliance against the Licence as required by condition 38.
The findings of the compliance assessment against the Licence are as follows:
65 conditions were compliant;
18 conditions were non-compliant; and
10 conditions deemed not applicable to current activities.
Key findings are summarised below:
Produced water:
- One exceedance of the oil in water and total suspended solids limits was
reported in December 2016.
- The quarterly discharge sample for Q3 was not tested.
- Due to the unavailability of site water analyzers, a number of parameters
could not be measured on site until the second half of 2016.
Treated sewage wastewater:
- One exceedance of the E Coli licence limit was reported, however this was
later attributed to elevated temperatures during transport.
Stormwater:
- All discharge test results were within the EPL limit for OIW.
- Although testing has been undertaken on a regular basis, data for some
parameters was not available.
Groundwater:
- E.Coli was below detection in all samples taken during the reporting
period.
Air emissions monitoring:
- CO from the generators ranged from 980 to 1,500 mg/m3 and exceeded
the EPL limit of 100 mg/m3, however this is in line with manufacturer
specifications and revision of the limit is under discussion with NTEPA.
- All other emissions concentrations were within licence limits.
- The total CO emissions (by mass) exceeded the EPL limits for the power
generators and emergency diesel generator. Revision of this limit is under
discussion with NTEPA.
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2. INTRODUCTION
2.1 Project background
Eni Australia B.V. (Eni) is operator of the Blacktip Gas Project. The development
consists of a small unmanned offshore wellhead platform, a subsea pipeline
bringing whole well stream fluid, (i.e. gas, condensate and produced water) to
Yelcherr Beach and the Yelcherr Gas Plant (YGP) near Wadeye in the Northern
Territory (Figure 2.1 and Figure 2.2). The processed gas is exported via an onshore
export pipeline, by Australian Pipeline Trust, to the customer, Power and Water
Corporation.
Production commenced on 26 August 2009. The operation of the YGP is licensed
under the Environmental Protection Licence (EPL), EPL57, issued by the former
Department of Natural Resources, Environment, The Arts and Sport (NRETAS) (now
Northern Territory Environment Protection Authority (NT EPA)) on 11 August 2009.
EPL57-01 was issued to Eni on 16 December 2010 as an amendment to EPL57.
EPL57-02 (the current licence) was issued to Eni on 10 February 2015 as an
amendment to EPL57-01.
Figure 2.1: Blacktip Field location
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Figure 2.2: Yelcherr Gas Plant and Offshore Pipeline Facilities
2.2 Purpose of the report
This report summarises the environmental performance of the YGP for the reporting
period 10 February 2016 to 9 February 2017, as required by condition 40 of the
EPL.
This report has been prepared in accordance with requirements under condition 41
of the EPL, outlined below.
Clause EPL condition Section in
this report
41.1 include a description of gas plant infrastructure and
processes
3.1
41.2 report on total condensate produced and total gas processed
by the gas plant
4
41.3 report on quality of gas received by the plant; 4.4
41.4 include a tabulation of all monitoring data required as a
condition of this Licence, including:
discharge,
groundwater and
air emissions monitoring;
6
8
5
41.5 include a trend analysis and interpretation of all monitoring
data required as a condition of this Licence;
Various
41.6 include long term trend analysis of monitoring data to
demonstrate any environmental impact associated with the
Various
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Activity over a minimum period of three years;
41.7 identify the number of exceedances of
discharge/concentration trigger values that have occurred
during the reporting period;
9
41.8 report on the following associated with discharges:
total annual discharges (ML/year);
frequency and volume of Produced Formation Water
discharges;
6
41.9 report the total annual emissions of the following
parameters, for each emission point, as well as for
condensate tanks and fugitive emissions:
NOx;
SO2;
VOC;
PM10;
5
41.10 report in accordance with the requirements for a Monitoring
Report identified in Guidelines for Consultants Reporting on
Environmental Issues (as amended from time to time),
available from:
http://www.ntepa.nt.gov.au/__data/assets/pdf_file/0005/13
6481/guidelines_consultants_reporting_environmental_issue
s.pdf
n/a
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3. OVERVIEW OF YELCHERR GAS PLANT
3.1 General overview
In accordance with condition 41.1 of the EPL, this section provides a description of
the gas plant infrastructure and processes.
Infrastructure at the YGP includes:
a gas processing plant consisting of a slug catcher and pig receiver, separation,
gas dehydration, compression, condensate storage and produced water
treatment facilities
the onshore portion of an 18“ carbon steel, multi-phase pipeline bringing
produced fluids from the offshore gas field to the YGP, starting from the shore
crossing
the onshore portion of a condensate export pipeline from the condensate storage
facilities at the YGP to the shore crossing
a portion of the onshore gas export pipeline that runs from the gas processing
plant to a custody transfer meter at the boundary of the YGP site.
3.2 Plant configuration
After processing, un-odorised natural gas at agreed specifications is delivered to the
customer via an onshore export pipeline to a custody transfer meter at the
boundary of the YGP.
Stabilised condensate is stored on site at the YGP before being exported to the SPM
for offload via tankers.
The production life of the field is planned to be 25 years based on initial gas sales
contract. The design life of the Blacktip YGP is 30 years.
The entire YGP site occupies an area of 750 m by 750 m, with the main process
facility located to the south of the site (occupying an area of approximately 250 m
by 380 m) and the accommodation, warehouse, offices and control room to the
north (see Figure 3.1). The coordinates of the YGP are shown in Table 3.1.
Table 3.1: YGP Coordinates
Corner
GDA 1994 GDA 1994 MGA Zone 52
East North mE mN
W 129°25'52.09" 14°14'33.60" 546 510 8 425 393
N 129°26'05.87" 14°14'13.22" 546 924 8 426 018
E 129°26'26.77" 14°14'26.66" 547 549 8 425 604
S 129°26'12.99" 14°14'47.04" 547 135 8 424 979
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Figure 3.1: Blacktip YGP layout
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The YGP process facility is divided into four main areas, namely:
Inlet Separation;
Gas Processing and Treatment;
Condensate Processing; and
Produced Formation Water Treatment.
The YGP is also self-sufficient in all utilities required to allow continuous manned
operation for the hydrocarbon processing. The functionality for the process areas in
the YGP is summarised in Table 3.2 and illustrated in Figure 3.2.
Table 3.2: YGP process area functionality
Process Area
Inlet Facilities Gas Processing
Condensate
Processing PFW Treatment
Fu
ncti
on
ali
ty
Pig Receiver Inlet Separation Dewatering PFW Degasser /de-
oiler
Slug catcher and
bulk gas liquid
separation
Gas Dehydration
and Conditioning Stabilisation
Dispersed oil
removal - Air
Induced Floatation
Units
Sales Gas
Compression and
Export
Storage and Export
Pumping PFW Discharge Point
Gas Sales and
Fiscal Metering
The YGP includes a slug catcher facility for the receipt of the multiphase production
fluids from the offshore gas field. The process is essentially divided into two streams:
a gas processing stream and produced liquids processing stream.
The gas processing route uses a Triethylene Glycol (TEG) absorption process system
to extract condensed water from the gas stream. Further treatment of the gas stream
via the Joule-Thompson pressure-temperature reduction process for additional liquids
separation process downstream of the TEG-glycol system is applied to the gas stream
to meet the export gas dewpoint specifications. Thereafter, the gas is compressed
before it is exported via a custody transfer meter.
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Liquids stream removed from the slug catcher are further separated in two stages:
medium pressure (MP) followed by a low pressure (LP) separation system. The
stream entering the LP separator is heated to flash off lighter components in the liquid
stream in order to meet the condensate vapour pressure (RVP) specification prior to
being rundown to condensate storage tank, and subsequently load-out to tanker at
the SPM.
Produced water separated from the liquids stream is further processed in the PFW
system to remove free oil prior to disposal at sea.
Figure 3.2: YGP Process Block Diagram
The YGP is designed to export at up to 128 MMscfd of sales gas under steady state
conditions on a continuous basis. This capacity exceeds the contractual maximum
daily quantity of 103 MMscfd, to provide daily operating flexibility to meet changing
gas nominations.
3.3 Other facilities
Other key facilities on site include:
Utilities system – including:
- Power generation;
- Compressed air system;
- Potable water system;
- Chemical injection;
- Stormwater drainage;
- Sewage treatment plant and effluent reuse;
Inlet
Separation
Gas
Dehydration
Package
(Glycol
Gas/Gas
Exchanger
Gas
Compressors
Dewpointing
Package
J-T valves/LT
MP
Separator Condensate
LP
Separator
PW
Treatment
System
Bonaparte
Gas
PW
Pipeline
Ocean
Condensate
Export Pipeline
to SPM
HP Fuel
Gas
Fuel
Gas
LP Fuel
Gas
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- Firewater.
Ancillary buildings – including:
- Accommodation;
- Laboratory, workshop and stores;
Hazardous chemicals storage; and
Lighting and security.
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4. PRODUCTION
4.1 Overview
The annual production is provided in Table 4.1 and Figure 4.1.
The total gas and condensate production for the reporting period was approximately
487,900 t and 8,550 t, respectively. Blacktip is licensed for a maximum scale of
1,055,300 tonnes of gas and 50,930 tonnes of condensate per annum.
Table 4.1: Overview of production
20141 20151 20161
Annual gas production (KSCM) 678,866 615,305 636,533
Annual gas production (t) 514,200 467,200 487,900
Condensate production (t) 9,400 8,500 8,550
Total production (t) 523,600 475,700 496,450
Notes: 1 Reporting period is from 1 January – 31 December
Figure 4.1: Overview of production
4.2 Condensate
Two offtakes occurred in April and October 2016, amounting to a total volume of
70,380 bbl (8,554 t) of condensate offloaded.
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4.3 Gas production
Figure 4.2 shows the rate of gas produced from Blacktip for the reporting period. Daily
gas production typically ranged between 1.0 and 2.5 MSCM, with a total of 637 MSCM
being produced in 2016.
Figure 4.2: Gas production in 2015
Figure 4.3: Gas production in 2016
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4.4 Gas composition
The reservoir fluid properties and contaminants are shown in Table 4.2 and Table 4.3.
Table 4.2: Blacktip reservoir fluid properties
Component Percentage
CO2 0.62 mol%
N2 5.88 mol%
Methane 89.06 mol%
Ethane 2.82 mol%
Propane 1.00 mol%
Ibutane 0.12 mol%
Butane 0.23 mol%
Ipentane 0.06 mol%
Pentane 0.05 mol%
Hexanes 0.02 mol%
Heptanes 0.01 mol%
Octanes 0.02 mol%
Nonanes 0.03 mol%
Decanes 0.04 mol%
Undecanes 0.02 mol%
C12+ 0.01 mol%
Source: Ref. [19], [24]
Table 4.3: Contaminants in Blacktip Gas
Component Maximum measured
H2S 3.0 ppmv
Mercaptan <0.5 ppmv
Mercury 0.2 µg/m³
Radon 222 Bq/m³
Argon 0.01 mol%
Oxygen <0.01 mol%
Helium 0.06 mol%
Hydrogen 0.01 mol%
Benzene 0.002 mol%
Toluene 0.002 mol%
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Component Maximum measured
Ethyl Benzene <0.001 mol%
Xylenes 0.001 mol%
Source: Ref. [23], [24]
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5. ATMOSPHERIC EMISSIONS
5.1 Overview of atmospheric emissions
Major sources of atmospheric emissions from the Blacktip YGP are:
Export gas turbine compressors;
Gas engine power generators;
Flaring; and
Diesel usage.
Fuel usage for the compressors and gas engines is monitored continuously, as are gas
quantities flared. Table 5.1 lists the flow meters used for measuring the various gas
streams.
Table 5.1: Gas flow meters
Emission Source Gas Flow Meter Reference Number
Turbine Compressor Compressor A
Compressor B
Compressor C
420.1 FIT 161
420.1 FIT 261
420.1 FIT 361
Engine Generators LP Fuel Gas 420.1 FIT 004
Flare HP Flare 230.1 FQI 008
LP Flare 230.1 FQI 002
Fuel Gas
Distribution
420.1 FQI 007
5.2 Fuel gas consumption
The two main consumers of high pressure (HP) and low pressure (LP) fuel gas are the
gas turbine compressors and power generators. The volume of gas consumed as fuel
during the reporting period is summarised in Table 5.2 and shown in Figure 5.2 and
Figure 5.3.
The average daily and total consumption for the year were approximately 49
KSCM/day and 18 MSCM, respectively.
Table 5.2: Gas consumption at YGP
2014 2015 2016
Daily fuel gas consumption (KSCM) 50.2 47.3 49.2
Total annual fuel gas consumption
(MSCM) 18.3 17.3 18.0
Emissions (t CO2-e) 37,100 34,900 36,500
Notes:
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1 Reporting period is from 1 January – 31 December
Figure 5.1: Gas consumed for compressors and power generation in 2015
Figure 5.2: Gas consumed for compressors and power generation in 2016
0
2
4
6
8
10
12
14
16
18
20
0
10
20
30
40
50
60
70
80
90
Jan-15 Feb-15 Mar-15 Apr-15 May-15 Jun-15 Jul-15 Aug-15 Sep-15 Oct-15 Nov-15 Dec-15
Cu
mala
tive
Co
nsu
mp
tio
n (
MS
CM
)
Dail
y C
on
su
mp
tio
n (
KS
CM
/da
y)
Time
Gas Consumed for Compressor and Power Generation 2015
Daily Cumulative
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Total equivalent greenhouse gas (GHG) emissions for gas consumption is shown in
Figure 5.3. These were calculated using equations provided by the National
Greenhouse Accounts Factors for Stationary Energy Emissions (Ref. [3]), as follows:
1000
ijoxecii
ij
EFECQE
Where:
Eij is the emissions of gas type (j), (carbon dioxide, methane or nitrous oxide),
from the fuel type (i), i.e. unprocessed natural gas;
Qi is the quantity of fuel type (i) (m3);
ECi is the energy factor of the fuel type (i), which is given as 39.3 x 10-3 GJ/m3 for
natural gas;
EFijoxecis the emission factor for each gas type (j), measured in kilograms CO2-e
per gigajoule of fuel type (i).
Gas type Emission factor (Kg CO2-e/GJ)
CO2 51.4
CH4 0.1
N2O 0.03
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Figure 5.3: GHG emissions from gas consumed by compressors and power
generation in 2015
Figure 5.4: GHG emissions from gas consumed by compressors and power
generation in 2016
5.3 Flaring
The annual volume of gas flared from 2014-2016 is summarised in Table 5.3.
The volume of gas flared and the equivalent GHG emissions during the 2015 and 2016
reporting periods are presented in Figure 5.5, Figure 5.6, Figure 5.7 and Figure 5.8.
Daily and total consumption for 2016 were approximately 8.2 KSCM/day and 2.98
MSCM, respectively, representing a 20% reduction in flaring the previous year despite
an increase in production. This is attributed to fewer plant trips and depressure events
due to increased plant reliability and better coordination of plant maintenance.
Table 5.3: Gas flared at YGP
2014 2015 2016
Daily volume of gas flared (KSCM) 10.3 10.4 8.2
Total volume of gas flared (KSCM) 3,770 3,812 2,983
Estimated emissions (t CO2-e)2 8,200 8,300 6,500
Notes: 1 Reporting period is from 1 January – 31 December 2 Estimate to nearest 100 tonnes.
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Figure 5.5: Volume of gas flared from Blacktip YGP in 2015
Figure 5.6: Volume of gas flared from Blacktip YGP in 2016
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Total equivalent greenhouse gas (GHG) emissions for flaring is shown in Figure 5.7.
These were calculated using equations provided by the National Greenhouse Accounts
Factors for Stationary Energy Emissions (Ref. [3]), as follows:
ijiij EFQE
Where:
Eij is the emissions of gas type (j), (carbon dioxide, methane or nitrous oxide)
flared (CO2-e tonnes);
Qi is the quantity of fuel type (i) flared (tonnes);
EFij is the emission factor for each gas type (i) flared.
Gas type Emission factor
(tonnes CO2-e/tonnes of fuel flared)
CO2 2.8
CH4 0.8
N2O 0.03
Figure 5.7: GHG emissions from flaring in 2015
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Figure 5.8: GHG emissions from flaring in 2016
5.4 Diesel usage
Diesel usage over the reporting period was 39.9 m3, 10.0 m3 of which was used for
transport purposes and 29.9 m3 of which was used for stationary energy purposes.
This equates to GHG emissions of approximately 110 tonnes CO2-e.
Table 5.4: Annual diesel consumption and GHG emissions
2014 2015 2016
Diesel consumption (m3) 58.6 49.5 39.9
Emissions (t CO2-e) 159 134 108
Notes:
Reporting period is from 1 January – 31 December
Total equivalent greenhouse gas (GHG) emissions for diesel consumption was
calculated using equations provided by the National Greenhouse Accounts Factors for
Stationary Energy Emissions (Ref. [3]), as follows:
1000
ijoxecii
ij
EFECQE
Where:
Eij is the emissions of gas type (j), (carbon dioxide, methane or nitrous oxide) from
fuel type (i) (CO2-e tonnes);
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Qi is the quantity of fuel type (i) (kilolitres);
ECi is the energy content factor of fuel type (i) (GJ/kL)
EFijoxec is the emission factor for each gas type (j) for fuel type (i).
Gas type
Emission factor
(kg CO2-e/GJ)
Diesel fuel combusted for
transport energy purposes
Diesel fuel combusted for
stationary energy purposes
CO2 69.9 69.9
CH4 0.1 0.1
N2O 0.5 0.2
Energy content factor for diesel 38.6 GJ/kL
5.5 Stack emission monitoring
Emissions from the export gas turbine compressors and gas engine power generators
are sampled and analysed for
nitrogen oxides (NOx);
sulphur oxides (SOx);
carbon monoxide (CO);
volatile organic compounds (VOCs);
methane (CH4).
Stack emission monitoring was undertaken on 9 December 2015 and 18 August 2016,
with the most recent monitoring survey undertaken on 15 February 2017, the results
for which will be presented in next years’ report.
A summary of the results is provided in Appendix C. Key results during the reporting
period are as follows:
Carbon monoxide (CO) emission concentrations measured from the generators in
August 2016 ranged from 980 to 1,500 mg/m3 and exceeded the limit of 100
mg/m3 specified in Table 5 under EPL57-02 condition 21. The CO emissions are in
line with the manufacturer specifications and an amendment request has been
submitted to NTEPA to revise this limit.
All other generator pollutant emissions from the generators were within the EPL
limits. In particular, VOCs and methane emissions were very low and particulate
matter were below detection limit.
Nitrogen oxide (NOx) emission concentrations from the generators in August 2016
were within the EPL limits and ranged from 1,500 to 1,700 mg/m3.
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All pollutant emissions measured from the compressors were within the EPL limits.
Particulate matter emissions were also below detection limit.
Compressor A was out of service and therefore not included in the emissions
monitoring.
No visible smoke was reported during the last 12 months.
5.6 Air Emissions Assessment Report
The Air Emissions Assessment Report 000036_DV_PR.HSE.1057.000 was submitted to
NTEPA in 2015 in accordance with Condition 47 of EPL57-02. The report:
Reviews the trends in NOx emissions from the generators; and
Outlines an improvement plan for NOx emissions from the generators.
The improvement plan and current status are outlined below.
Table 5.5: Air emissions improvement plan
Improvement and corrective action Planned
completion Status
Install sampling ports on all three
generator stacks.
1 October
2015
Ports are compliant.
Undertake air dispersion modelling to
characterize the NOx downwind
concentrations.*
31 January
2016
Complete.
Undertake a detailed
engineering/feasibility assessment of
NOx control technology proposed by
selected vendors.
31
December
2016
Complete, final report pending.
*Revised action agreed to by NT EPA on 8 February 2016 (D Spelchan 2016, pers. comm., 8 February).
5.7 Pollutant inventory
Eni reports emissions to atmosphere and the environment via the National Pollutant
Inventory (NPI) and the National Greenhouse and Energy Reporting Scheme (NGERS).
Appendix B provides a comparison against the pollutant mass limits stipulated in the
EPL Appendix 2, Table B.
Key results during the reporting period are as follows:
The annual carbon monoxide (CO) emissions were reported above the EPL limits
(specified in Table B under Appendix 2 of the EPL) for the power generators and
emergency diesel generator. An amendment request has been submitted to NTEPA
to revise the CO limits to reflect normal operation of the equipment.
All other emissions were within the mass limits.
Eni submitted the annual NPI reporting figures via the NPI Online Reporting System on
29 September 2016.
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The annual NGERS reporting figures were submitted to the Department of Climate
Change on 24 October 2016.
5.8 Fugitive emissions assessment
A fugitive emissions campaign was undertaken at the Blacktip Yelcherr Gas Plant and
Well Head Platform in line with US EPA Method 21 for the estimation of fugitive
emissions of methane, using advanced techniques for the screening of potentially
leaking items of equipment.
The results from this campaign are still being finalised, however only a few minor
leaks were identified, and preliminary calculations show a significant reduction in
fugitive emissions compared to the previously estimated values. Further details may
be made available to the NTEPA upon completion of the assessment.
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6. LIQUID WASTE DISCHARGES
6.1 Produced water
6.1.1 Overview
Produced water discharge in this reporting period was 6.2 ML. Annual marine
monitoring was conducted in May 2016 and continues to provide no indication of
adverse impact from produced water discharge.
Three non-compliances were identified:
one exceedance of the oil in water and total suspended solids limits was reported in
December 2016;
the quarterly discharge sample for Q3 was not tested; and
due to the unavailability of site water analyzers, a number of parameters could not
be measured on site until the second half of 2016.
All incidents and non-compliances are listed in Section 9.
6.1.2 Discharge and routine monitoring
Table 6.1 and Figure 6.1 present the annual produced water discharges for the past
three years. Produced water is sampled and tested on site prior to discharge to ensure
the following parameters are within the limits stipulated in Table 6 of EPL57-02:
pH;
Electrical conductivity (EC);
Dissolved oxygen (DO);
Temperature;
Turbidity; and
Oil in water (OIW).
Samples are then taken hourly to ensure water quality remains within the licence
limits. The results are presented in Appendix E.
Key issues identified include:
Due to unavailability of site water analyzers, a number of parameters could not be
measured on site until the second half of 2016, including EC, DO, Temperature,
Turbidity.
There have been issues with the supply of reagent for analysis of dissolved oxygen
using the site multi-parameter unit.
There have been instances of either elevated EC (~600 µs/cm) or turbidity (~800
NTU). This will be investigated further as part of the PFW Plan (see Section 6.1.4).
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Table 6.1: Produced water discharge annually
2014 2015 2016
Volume of produced water
discharged (m3)
1,754 6,179 6,206
Number of discharge days 7 22 22
Notes:
Reporting period is from 1 January – 31 December
Figure 6.1: Volume of produced formation water discharged from Blacktip YGP
6.1.3 Quarterly chemical characterisation
Table A in EPL57-02 stipulates the requirements for characterisation of PW on a
quarterly basis. Sampling was undertaken in March 2016, September 2016, December
2016 and February 2017. The September 2016 sample was collected from the MP
separator and therefore not associated with a discharge. Laboratory results have not
yet been received for monitoring conducted on 6 February 2017. The results are
presented in Appendix E.
Key results are as follows:
Oil in water (OIW) in the quarterly sample taken on 25 May 2016 was measured at
106.9 mg/L. The analysis was undertaken using a TD3100 benchtop fluorometer.
Prior to discharge, site monitoring using a Horiba water analyser measured OIW at
13.5 mg/L. Furthermore, a combination of Gas Chromatography Mass Spectrometry
(GC-MS) and Gas Chromatography Flame Ionisation Detection (GC-FID) measured
TRH and TPH in the same sample at ~9 mg/L and below limits of detection,
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Jan-14 Apr-14 Jul-14 Oct-14 Jan-15 Apr-15 Jul-15 Oct-15 Jan-16 Apr-16 Jul-16 Oct-16
Oil
in w
ate
r (m
g/L)
Vo
lum
e (
m3
/d)
Produced Formation Water Discharge Volumes 2014-2016
Discharge volume Oil in water content Oil in water limit (25 mg/L)
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respectively. Therefore, the high OIW reading is unlikely to reflect oil contamination
from produced formation water. Anecdotal evidence suggests the presence of
corrosion inhibitor influences OIW measurements by fluorometry.
OIW and total suspended solids (TSS) in the quarterly sample taken on 12
December 2016 were measured at 57.4 mg/L and 84 mg/L, respectively, exceeding
the EPL limits. NTEPA was notified and an incident investigation was subsequently
undertaken to identify the cause, environmental risk and corrective actions. The
receiving environment is known to be well mixed, and the produced water plume
would have rapidly dispersed and mixed into the receiving waters upon discharge,
resulting in rapid dilution and degradation of any hydrocarbons. Therefore the risk
of environmental harm was determined to be low.
Copper was within the EPL limit in all samples.
Zinc was above the trigger value in the sample collected on 25 May 2016, and close
to the limit in the sample collected in 12 December 2016.
Total petroleum hydrocarbons measured by GC-FID (i.e. TPH>C16-C35 aliphatics,
TPH>C35 aliphatics and TPH C16-C35 aromatics) were below the limits of detection
in all samples, suggesting that a proportion of the hydrocarbon content is of
biological origin. A potential source of organic matter is the hazardous open drains
pit, which is connected to the PFW system. The pit is open and collects debris from
the environment.
6.1.4 Produced Formation Water Plan
The Produced Formation Water Plan 000036_DV_PR.HSE.1056.000 was submitted to
NTEPA in accordance with condition 43 of the EPL. NTEPA have requested the Plan to
be modified and resubmitted by 1 April 2017.
6.1.5 Annual Marine Monitoring
Eni has an annual commitment, set out in Produced Water Management Plan
000036_DV_EX.HSE.0381.000_A02, to undertake sediment and shellfish sampling in
the vicinity of the produced water pipeline to monitor any impacts on sediment and
biota. Overall, the results were consistent across the sampling sites, with little
variation between the control and monitoring sites, providing confidence that there are
no adverse impacts from produced water discharge.
6.2 Treated Wastewater Effluent
Wastewater generated at Blacktip YGP is treated in an ABCO Water System 150 EP.
Effluent is reused through an irrigation system to land and a total of 3.0 ML was
discharged over the reporting period.
Table 6.2: Treated wastewater effluent reuse
2014 2015 2016
Effluent reuse (ML) 3.8 3.7 3.0
Notes:
Reporting period is from 1 January to 31 December.
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In accordance with Table A of the EPL, treated discharged wastewater is sampled and
analysed for constituents on a monthly basis by an external laboratory to verify
compliance against the contaminant limits. The results are presented in Appendix F.
Key results are as follows:
One exceedances of the E Coli licence limit in September 2016, which was reported
to NTEPA.
Oil in water, as determined using fluorometry, ranged between 14 mg/L to 24.4
mg/L, above the trigger value of 10 mg/L. However, analysis by gas
chromatography mass spectrometry detected no hydrocarbons.
Consistently no positive readings of hydrocarbons or BTEX. The WWTP is an open
system and uses aeration, hence any BTEX would rapidly volatilise.
BOD levels were slightly above the trigger value of 20 mg/L a few times in the first
half of the year, with the BOD ranging from 15 mg/L to 25 mg/L.
TSS concentrations were above the trigger value of 30 mg/L a few times during the
year, ranging from 26 mg/L to 51 mg/L.
6.3 Stormwater
Stormwater from the utilities and process skids are discharged to grade at SW-02 and
SW-03, respectively. Fire pump test water is sampled each time the pumps are tested,
i.e. typically weekly. Prior to July 2016, the utilities stormwater was fed into the
produced water treatment system and therefore not discharged to grade.
Stormwater from the Open Drains Sump (ODS) is discharged manually to grade. Prior
to discharge, the contents of the sump are sampled and tested for pH, EC and OIW on
site, and samples continue to be taken daily while discharging. In 2016, the ODS
remained closed for the majority of the year and was only opened to grade in late
November during the wet season.
The results are presented in Appendix G. Key findings are as follows:
All discharge test results were within the EPL limit for OIW.
Testing has been undertaken on a regular basis, however gaps have been identified
where data is not available. See Appendix G.
Results of stormwater from utilities (SW-02) are as follows:
- pH ranged between 5.6-7.3;
- electrical conductivity ranged between 102-122 µs/cm; and
- oil in water ranged between 0-3.4 mg/L.
Results of stormwater from the open drains sump (SW-03) are as follows:
- pH ranged between 5.4-6.9;
- electrical conductivity ranged between 51-194 µs/cm; and
- oil in water ranged between 0.9-5.6 mg/L.
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7. SOLID WASTE
Solid waste is managed onsite according the Blacktip Waste Management Plan
(000036_DV_PR.HSE.0832.000_02). Domestic waste from the accommodation village
and crib room is taken to the local West Daly Regional Shire Council Landfill. General
industrial waste and hazardous waste from the plant is transported by a licensed
contractor to Darwin for disposal, treatment, recycling or destruction.
Table 7.1: Waste disposal
2014 2015 2016
Domestic waste to local landfill (t)
Kitchen waste
Accommodation waste
Office waste
5 4 6
Darwin recycling (t) 1 24 13
Darwin disposal – non-hazardous (t) 31 35 14
Darwin disposal – hazardous (t) 3.6 109 90
Notes:
Reporting period is from 1 January to 31 December.
Local Landfill Disposal
This waste comprises predominately kitchen, accommodation and office waste and has
been estimated as approximately 6 tonnes for the reporting period.
Darwin Recycling
Metal is recycled / reused where practicable, and has been estimated as approximately
13 tonnes for the reporting period, comprising of mixed paper, wood and plastic, and
scrap metal.
Darwin Disposal – Non Hazardous
General waste sent back to Darwin for disposal has been estimated at approximately
14 tonnes for the reporting period, comprising of spent non-hazardous chemicals, and
spent cooking oil.
Darwin Disposal – Hazardous
Hazardous waste is managed onsite in accordance with legislation, and generally
consists of waste oil, oily rags, chemical drums and filters. Hazardous and listed
wastes are transported by licensed handlers to facilities approved to handle such
waste in Darwin, Adelaide and Perth. The estimated amount of hazardous waste
removed from site is 90 tonnes for the reporting period, comprising of 40kL of oily
wastewater and other oily wastes.
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8. GROUND WATER
8.1 Ground water use
Groundwater is abstracted for potable water use and ancillary equipment at Yelcherr
Gas Plant. The annual groundwater abstraction volumes are summarised in Table 8.1.
There are also two monitoring bores, BH5 and BH7, located at YGP. The location of the
abstraction and monitoring bores are shown in Figure 8.1.
The increase in groundwater consumption in 2016 is related to an increase in the
frequency of fire pump testing, from monthly to weekly.
Table 8.1: Total annual volume of groundwater abstracted
20141 2015 2016
Groundwater use (ML) 24.5 25.5 46.3
Notes:
Reporting period is from 1 January to 31 December.
Figure 8.1: Groundwater abstraction and monitoring bores
8.2 Ground water monitoring
Condition 28 and Table A in Appendix 3 of EPL57-02 stipulates the requirements
relating to groundwater monitoring.
Groundwater monitoring was conducted on 8 March 2016, 24 May 2016, 7 September
2016 and 7 December 2016. The results and trend analysis are presented in Appendix
H.
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Weekly field measurements are also recorded at each groundwater monitoring bore by
the Thamarrurr Ranger local indigenous group. The Rangers measure the pH, water
level, and electrical conductivity.
The key results are as follows:
Oil in water (OIW) was detected at 73.41 mg/L in BH5 and 18.61 mg/L in March
2016. Additional samples were subsequently taken in April 2016 and analysed for
hydrocarbons by GC-MS. This analysis returned a nil result (see Appendix H). In
subsequent groundwater samples, OIW measurements remained below 9 mg/L.
E.Coli was below detection in all samples taken during the reporting period.
Heterotrophic colony bacteria were detected at both bores. Many types of bacteria
can occur naturally in water and coliform bacteria are common in soils and water.
The World Health Organisation (WHO) advises that HCC alone is not a reliable
indicator of health risk and other tests, such as for E. coli and other fecal coliforms,
are a better indication of whether health risk exists (Ref. [25]). Therefore, the
heterotrophic colony count (HCC) is not of concern.
Low BOD, COD and nutrient levels measured at both sites, although BOD levels
were typically higher in BH5.
Quarterly monitoring, which measured pH at both bores between 5.2 and 6.
The water level ranged between 9 and 13 m at both bores, with the lower readings
measured in Q4 of 2016.
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9. INCIDENTS AND NON-CONFORMANCES
The Waste Management and Pollution Control Act (NT) and EPL require all non-
compliances with the EPL and any potential or actual environmental harm or pollution
event to be recorded and reported to NT EPA.
Pollution is defined in the Waste Management and Pollution Control Act (NT) as:
a) A contaminant or waste that is emitted, discharged, deposited or disturbed or
that escapes; or
b) A contaminant or waste, effect or phenomenon, that is present in the
environment as a consequence of an emission, discharge, deposition or escape
or disturbance of a contaminant or waste.
9.1 Incidents and non-compliances
The Annual Return (Appendix A) details the compliance assessment against the
Environment Licence EPL57-02. The findings are as follows:
65 conditions were compliant;
18 conditions were non-compliant; and
10 conditions deemed not applicable to current activities.
Table 9.1 lists the environmental non-compliances recorded between 10 February
2016 and 9 February 2017. All non-compliances summarised below have been
reported to NTEPA, except the non-compliance against Condition 22. Notifications to
NTEPA are listed in Table 9.2.
Table 9.1 : Environmental non-compliances
Condition Non-compliance
9.1, 9.2, 9.3
Licence
documents
The Blacktip Operations Emergency Response Plan was amended on 10 Feb 2016.
During the NTEPA audit on 28 July 2016, it was identified that the amendment
had not been communicated to NTEPA in accordance with Condition 9.
Subsequently on 14 November 2016, Eni submitted to NTEPA the complete
documentation, including a tabulated summary of the amendments with
document references, reasons for the amendments, and assessment of the
environmental risk associated with the amendments in accordance with Condition
9.
19
Wastewater
discharge limits
Eni has an ongoing water monitoring program to, where possible, verify prior to
discharge that wastewater is within the limits specified in Table 3 under Condition
19.
However, some exceedances were identified:
- 19 July 2016 – E.Coli in treated wastewater
- 6 December 2016 – OIW and TSS in produced water
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Condition Non-compliance
21
Air emission
concentration
limits
Carbon monoxide (CO) emission concentrations measured from the generators in
August 2016 ranged from 980 to 1,500 mg/m3 and exceeded the limit of 100
mg/m3 specified in Table 5 under EPL57-02 condition 21. The CO emissions are
in line with the manufacturer specifications.
Revision of the CO limit is under discussion with NTEPA.
22
Annual air
pollutant mass
limits
The annual carbon monoxide (CO) emissions were reported above the EPL limits
(specified in Table B under Appendix 2 of the EPL) for the power generators and
emergency diesel generator. Revision of the CO limits are under discussion with
NTEPA.
24.1
Signage for
terrestrial
monitoring points
Signage has been installed at terrestrial monitoring points.
However, power generators are labelled A, B and C whereas in the EPL57-02 they
are distinguished by numbers no 1, 2, 3. Revision of the EPL is under discussion
with NTEPA, including the generator labels.
26
Discharge
monitoring
Discharge monitoring has been undertaken. However, the monitoring undertaken
was not fully compliant.
The quarterly produced water sample collected on 7 Sept 2016 was not
representative of discharge.
On site monitoring of produced water did not include EC, DO,
Temperature or Turbidity until September 2016, when the equipment was
available on site and operators received training.
DO analysis is still pending further training on the procedure.
On site monitoring of stormwater discharge from the open drains sump
(ODS) and utilities discharge has been conducted on a regular basis,
however gaps have been identified where data is not available:
o 24 July 2016 (utilities)
o 14 Aug 2016 (utilities)
o 4 Dec 2016 (utilities)
o 11 Dec 2016 (utilities)
o 25 Dec 2016 (utilities)
o 1 Jan 2017 (utilities)
o 10 Jan 2017 (utilities)
o 15 Jan 2017 (utilities)
o 22 Dec 2016 (ODS)
o 26 Dec 2016 (ODS)
o 27 Dec 2016 (ODS)
o 28 Dec 2016 (ODS)
o 1 Jan 2017 (ODS)
o 2 Jan 2017 (ODS)
o 3 Jan 2017 (ODS)
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Condition Non-compliance
o 23 Jan 2017 (ODS)
o 24 Jan 2017 (ODS)
o 25 Jan 2017 (ODS)
o 3 Feb 2017 (ODS)
o 5 Feb 2017 (ODS)
o 6 Feb 2017 (ODS)
Refer to Section 6 and Appendices E and G of the Blacktip Annual Environmental
Performance Report 2016 (000036_DV_PR.HSE.1120.000).
34
Notification of
non-compliances
Non-compliance with Condition 22 was identified during the preparation of this
report, and not reported within 24 hours.
43, 44.1, 44.2,
44.5, 44.6, 44.7,
44.8, 44.9, 44.10
The Produced Formation Water Plan For EPL57-02 Condition 43
000036_DV_PR.HSE.1056.000_03 was submitted on 14 July 2016 as agreed with
NT EPA.
NTEPA provided feedback on 22 December 2016 and found it did not comply with
all requirements under Condition 44.
Table 9.2 : Environmental notifications to NTEPA
Date Description
19 July 2016 Oil in water was measured in produced water discharge waters 106.9 mg/L in a
sample collected on 25 May 2016, above the EPL limit of 25 mg/L. However, a
combination of GC-MS and GC-FID measured TRH and TPH in the same sample
at ~9 mg/L and below limits of detection, respectively.
19 July 2016 E.Coli was measured in treated effluent at 2046 MPN E.Coli/100ml in a sample
collected on 11 May 2016, above the EPL limit of 1000 MPN/100 mL.
Investigation with the testing laboratory identified that the May sample was
received at 25°C, whereas the June sample was received at 21°C (see specific
analysis reports attached). March and April results were also <10 MPN/100ml
(results attached) and the respective receiving temperatures were 18°C and
22°C. Therefore, it is believed that temperature during transport was the cause
of the elevated levels in May.
18 August 2016 Air emissions from Compressor A not tested during biannual monitoring due to
the Compressor being out of service. Biannual monitoring will recommence
when Compressor A is brought back online.
18 August 2016 Carbon monoxide (CO) measured in August 2016 from the generators ranged
from 980 to 1,500 mg/m3 and exceeded the limit of 100 mg/m3 specified in
Table 5 under EPL57-02 condition 21. The CO emissions are in line with the
manufacturer specifications and revision of this limit is under discussion with
NTEPA.
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Date Description
30 August 2016 Firewater pump test water discharge not tested for oil in water due to
insufficient solvent. Solvent stocks have been replenished.
30 August 2016 Produced formation water not tested in Q3 2016.
30 August 2016 Wastewater effluent not tested for enterococci between from February to July
2016. This matter was raised with the laboratory services provider and
enterococci testing has recommenced.
6 September 2016 Produced formation water not tested for dissolved oxygen due to the
unavailability of laboratory reagent. Reagent stocks have since been
replenished.
15 November 2016 Leak to ground observed in the base of the waste water irrigation tank. Tank
has since been repaired.
6 December 2016 PFW discharge exceeded TSS and OIW limits. On site laboratory equipment
have been recalibrated.
4 January 2017 A container used for collecting flush water during PFW sampling overflowed to
grade, releasing an estimated 2 m3 PFW to grade. The system was subsequently
reconfigured to eliminate the use of the container for collecting flush water.
9.2 Complaints
No complaints were received during the reporting period.
9.3 Audits and inspections
NTEPA conducted an inspection of YGP on 28 July 2016, which identified a number of
non-compliances. Eni has since implemented corrective actions for the non-
compliances identified.
The Commonwealth Department of the Environment also conducted an inspection of
YGP in October 2016, with a particular focus on the recently completed wharf
decommissioning project, a positive review was received.
Eni underwent a surveillance audit in October 2016 as part of maintaining its
ISO14001 certification.
9.4 Continuous improvement and other activities
During the reporting period, Eni engaged in the following continuous improvement
activities
Implement the improvement plans set out in the Air Emissions Assessment Report
000036_DV_PR.HSE.1057.000 (see Section 5.6);
Re-submission of the Produced Formation Water Plan
000036_DV_PR.HSE.1056.000 (see Section 6.1.4);
Demolition of the barge landing at Yelcherr Beach in September 2016; and
Fugitive emissions monitoring at the YGP and the WHP (see Section 5.8).
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10. COMMUNITY INITIATIVES
Eni continues to maintain a positive and engaging relationship with the Thamarrurr
Rangers, who deliver local environmental monitoring services including
offshore monitoring of the Single Point Mooring SPM);
turtle monitoring
marine monitoring;
controlled burning;
groundwater sampling, and
weed monitoring and spraying.
The SPM monitoring conducted by the Rangers includes inspection of the SPM
equipment as well as inspection of the surrounding waters for surface sheen and
possible spills. This provides a valuable contribution to the safe offtake of condensate
and is an important part of Eni’s scheduled maintenance.
During turtle nesting season, Eni engage the Rangers to monitor Yelcherr Beach for
turtle tracks and nests on a weekly basis. The Rangers identified a couple of sets of
Olive Ridley and Flatback nests in June and July 2016; in general, observations by the
Rangers suggest significantly less turtles coming ashore to rest this year. During the
demolition of the barge landing, the Rangers continued their weekly monitoring and
confirmed no turtle tracks were present during demolition activities.
The Rangers continued to support the YGP groundwater monitoring, marine
monitoring and weed management programs.
The regular monitoring by the rangers allows our site-based personnel to engage with
local indigenous community members, providing a greater appreciation of the region
and the importance of caring for country. Eni and the Thamarrurr Rangers continue to
work closely to identify opportunities for local engagement and achieve positive
environmental outcomes.
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11. ACRONYMS
ACRONYM Definition
BOD Biochemical oxygen demand
cfu Colony-forming unit
CH4 Methane
CO2 Carbon dioxide
COD Chemical oxygen demand
CPI Corrugated plate interceptor
DO Dissolved oxygen
E. coli Escherichia coli
EC Electrical conductivity
EMP Environmental management plan
Eni Eni Australia B.V.
EPL Environmental Protection Licence
g grams
GC-FID Gas Chromatography Flame Ionisation Detection
GC-MS Gas chromatography mass spectrometry
GHG Greenhouse gas
HCC Heterotrophic colony count
HP High pressure
IBC 1000L intermediate bulk container
k Kilo
KSCM Kilo standard cubic metres
LP Low pressure
µS/cm microSiemens per centimetre
m Metres
m3 Metres cubed
mbgl Metres below ground level
mg Milligrams
mL Millilitres
ML Megalitre
MPN Most probable number
MSCM Million standard cubic metres
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ACRONYM Definition
N2O Nitrogen dioxide
NM Not measured
NOx Nitrogen oxides
NRETAS Department of Natural Resources, Environment, The Arts and Sport (NT) (now
Northern Territory Environment Protection Authority (NT EPA))
NT Northern Territory
NT EPA Northern Territory Environment Protection Authority (formerly Department of
Natural Resources, Environment, The Arts and Sport (NRETAS))
NTP Normal temperature and pressure
OGP Onshore Gas Plant
OIW Oil in water
pH Measure of acidity or basicity
PM Particulate matter, solid particles
ppm Parts per million
PW Produced water
SOx Sulphur oxides
t CO2-e Tonnes of carbon dioxide equivalent
TDS Total dissolved solids
TJ Terra joules
TN Total nitrogen
TP Total phosphorous
TSS Total suspended solids
VOC Volatile organic compounds
WWTP Waste Water Treatment Plant
YGP Yelcherr Gas Plant (formerly named Onshore Gas Plant (OGP))
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12. REFERENCES
[1] AUSTRALIAN AND NEW ZEALAND ENVIRONMENT AND CONSERVATION COUNCIL
(ANZECC), 2000. AUSTRALIAN AND NEW ZEALAND GUIDELINES FOR FRESH AND
MARINE WATER QUALITY. VOLUME 1, THE GUIDELINES / AUSTRALIAN AND NEW
ZEALAND ENVIRONMENT AND CONSERVATION COUNCIL, AGRICULTURE AND
RESOURCE MANAGEMENT COUNCIL OF AUSTRALIA AND NEW ZEALAND. CANBERRA,
ACT.
[2] BARRON J., ASHTON C. & GEARY L. 2006. THE EFFECTS OF TEMPERATURE ON PH
MEASUREMENT. 57TH ANNUAL MEETING OF THE INTERNATIONAL SOCIETY OF
ELECTROCHEMISTRY, EDINBURGH, SEPTEMBER 2006. AVAILBLE ONLINE AT:
<HTTP://REAGECON.COM/PDF/TECHNICALPAPERS/EFFECTS_OF_TEMPERATURE_ON_P
H_V4-_TSP-01-2.PDF>.
[3] COMMONWEALTH OF AUSTRALIA (DEPARTMENT OF THE ENVIRONMENT) (2016).
NATIONAL GREENHOUSE ACCOUNTS FACTORS. AUGUST 2016.
[4] ENI AUSTRALIA BV (2010A). BLACKTIP PROJECT ONSHORE GAS PLANT
ENVIROINMENTAL MANAGEMENT PLAN 000036_DV_EX.HSE.0684.000 REV A03.
NOVEMBER 2010. PERTH, WA.
[5] ENI AUSTRALIA BV (2010B). PRODUCED FORMATION WATER MANAGEMENT.
DOCUMENT NUMBER 000036_DV_EX.HSE.0381.000 REV A03. PERTH, WA.
[6] ENI AUSTRALIA BV (2011). BLACKTIP OPERATIONS MARINE SURVEY 2011.
000036_DV_PR.HSE.0825.000_01. NOVEMBER 2011.
[7] ENI AUSTRALIA BV (2012A). BLACKTIP OPERATIONS MARINE SURVEY 2012.
000036_DV_PR.HSE.0826.000_01. NOVEMBER 2012.
[8] ENI AUSTRALIA BV (2012B). ANNUAL ENVIRONMENTAL PERFORMANCE REPORT 2011–
2012 (000036_DV_PR.HSE.0827.000_01). NOVEMBER 2012.
[9] ENI AUSTRALIA BV (2013A). ANNUAL ENVIRONMENTAL PERFORMANCE REPORT 2012–
2013 (000036_DV_PR.HSE.1023.000_01). OCTOBER 2013.
[10] ENI AUSTRALIA BV (2014). BLACKTIP OPERATIONS MARINE SURVEY 2014
(000036_DV_PR.HSE.1035.000_01). DECEMBER 2014.
[11] ENI AUSTRALIA BV (2015A). ANNUAL ENVIRONMENTAL PERFORMANCE REPORT 2013–
2014 (000036_DV_PR.HSE.1043.000_02). JANUARY 2015.
[12] ENI AUSTRALIA BV (2015B). PRODUCED FORMATION WATER PLAN FOR EPL57-02
CONDITION 43 (000036_DV_PR.HSE.1056.000_01). MAY 2015.
[13] ENI AUSTRALIA BV (2015C). AIR EMISSIONS ASSESSMENT REPORT FOR EPL57-02
CONDITION 47 (000036_DV_PR.HSE.1057.000_01). MAY 2015.
[14] ENI AUSTRALIA BV (2015D). ENVIRONMENTAL PROTECTION LICENCE COMPLIANCE
REPORT 2014–2015 (000036_DV_PR.HSE.1062.000_01). AUGUST 2015.
[15] ENI AUSTRALIA BV (2015E). ENVIRONMENT MANAGEMENT PLAN COMPLIANCE REPORT
2014–2015 (000036_DV_PR.HSE.1063.000_01). AUGUST 2015.
[16] ENI AUSTRALIA BV (2015F). EPBC 2003/1180 COMPLIANCE REPORT 2015
(000036_DV_PR.HSE.1064.000_01). JULY 2015.
[17] ENI AUSTRALIA BV (2015G). OFFSHORE ENVIRONMENT PLAN COMPLIANCE REPORT
2014–2015 (000036_DV_PR.HSE.1065.000_00). NOVEMBER 2015.
[18] ENI AUSTRALIA BV (2015H). NATIONAL GREENHOUSE AND ENERGY REPORTING
SECTION 19 – ENERGY AND EMISSIONS REPORT FOR THE REPORTING YEAR 2014-
2015. 26 OCTOBER 2015.
[19] ENI AUSTRALIA BV (2015I). NPI REPORT FOR 14/15 BLACKTIP ONSHORE GAS PLANT
NT502 FINANCIAL YEAR. 25 SEPTEMBER 2015.
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[20] ENI AUSTRALIA BV (2015J). BLACKTIP OPERATIONS MARINE SURVEY 2015
(000036_DV_PR.HSE.1066.000_01). SEPTEMBER 2015.
[21] USEPA 2000. EMISSIONS FACTOR DOCUMENTATION FOR AP-42 SECTION 3.2
NATURAL GAS-FIRED RECIPROCATING ENGINES, AVAILABLE ONLINE AT:
<HTTPS://WWW3.EPA.GOV/TTN/CHIEF/AP42/>.
[22] USEPA 2015. UNITED STATES ENVIRONMENTAL PROTECTION AGENCY. AVAILABLE
ONLINE AT: <HTTP://WWW3.EPA.GOV/>.
[23] WEATHERFORD LABORATORIES (AUSTRALIA) PTY LTD (2009A). PVT ANALYSIS –
FINAL REPORT 1288-06 FOR BLACKTIP-P2. DOCUMENT NUMBER BT-P2_A2.
UNPUBLISHED REPORT PREPARED FOR ENI AUSTRALIA LTD.
[24] WEATHERFORD LABORATORIES (AUSTRALIA) PTY LTD (2009B). COMPOSITIONAL
ANALYSIS – FINAL REPORT 1300-06 BLACKTIP-P1 (3RD BATCH). DOCUMENT NUMBER
BT-P1_A4. UNPUBLISHED REPORT PREPARED FOR ENI AUSTRALIA LTD.
[25] WORLD HEALTH ORGANISATION (2003). HETEROTROPHIC PLATE COUNTS AND
DRINKING-WATER SAFETY: THE SIGNIFICANCE OF HPCS FOR WATER QUALITY AND
HUMAN HEALTH. AVAILABLE ONLINE AT:
<HTTP://WWW.WHO.INT/WATER_SANITATION_HEALTH/DWQ/HPCFULL.PDF>.
PUBLISHED ON BEHALF OF THE WORLD HEALTH ORGANISATION BY IWA
PUBLISHING, ALLIANCE HOUSE, UK.
[26] WORLEY PARSONS (2011). GREENHOUSE GAS EMISSIONS: STUDY OF AUSTRALIAN
CSG TO LNG. PREPARED BY WORLEY PARSONS FOR APPEA.
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APPENDICES
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APPENDIX A:
ANNUAL RETURN
LICENCE NO. EPL57-02
REPORTING PERIOD 10 February 2016 – 9 February 2017
Please email a copy of your completed Annual Return to [email protected].
1. Licence Details ALL Licensees must check their Licence Details are correct. If there are changes to any of these details you must advise the NT EPA by submitting a Change of Contact Details Form.
Licensee Details
Legal Entity Name: Eni Australia B.V.
ACN: 18 092 812 023
Registered Business Address:
226 Adelaide Terrace
PERTH WA 6000
Postal Address: PO Box 6862
EAST PERTH WA 6892
Contact Person: Keith Cook
Position Title: HSE & CSR Manager
Contact Details: b/h: 08 9320 1184
mobile: 0437 254 166
email: [email protected]
Location of Premises
Name: Blacktip Onshore Gas Plant
Address: NT Portion 1637, WADEYE NT
24 hour emergency response
Contact Person(s): Eni IMT Duty Officer
Telephone Numbers: 0419 943 584
ANNUAL RETURN ENVIRONMENT PROTECTION LICENCE
Page 2 of 18
2. Compliance with Licence Conditions
LICENCE CONDITIONS How/ Evidence When (Date)
ADMINISTRATIVE - -
1. The Licensee must notify the NT EPA within 24 hours if there are changes to the details of the 24-hour emergency contact as provided on page one of this Licence.
No change Reviewed 16 Jan 2017
2. The Licensee must notify the NT EPA within 14 days if there are changes to the Licensee details shown on page one of this Licence.
Contact person has changed. NTEPA advised via Application to Amend Licence.
Reviewed 16 Jan 2017
3. The Licensee must pay an annual fee in accordance with the WMPC Act within 30 Business Days of the anniversary of the commencement date for each year that this Licence is in force.
The annual fee is not payable for this EPL
Reviewed 16 Jan 2017
4. The Licensee must notify the NT EPA prior to making any operational change that will cause, or is likely to cause, an increase in the potential for environmental harm.
No change Reviewed 16 Jan 2017
5. The Licensee must cause clear and legible signage to be displayed in a prominent location at the entrance to the Location including the following details:
Signage is present 13 Nov 2015
5.1. Environment Protection Licence number; and Included in signage Sighted 28 July 2016
5.2. 24 hour emergency contact details as provided on page one of this Licence. Included in signage. Sighted 28 July 2016
6. The Licensee must cause a copy of this Licence to be available at all times:
6.1. on the Licensee's Australian website; and Eni does not have an Australian website.
n/a
6.2. at the Location. A copy of the Licence is available in the YGP Central Control Room
Sighted 28 July 2016
7. Where this Licence requires the provision of any notice, document or other correspondence to the NT EPA, the relevant contact is:
- -
Pollution Control - -
Physical Address: Level 2 Darwin Plaza, 41 Smith Street Mall, Darwin NT 0800 - -
Postal Address: GPO Box 3675, Darwin NT 0801 - -
Email: [email protected] - -
Page 3 of 18
8. All notices, documents or other correspondence required to be provided pursuant to this Licence must be provided in electronic form unless otherwise specified as a condition of this Licence.
All notices, documents or other correspondence is provided in electronic form.
Reviewed 16 Jan 2017
9. Within 10 Business Days of any amendment being made to a document listed in Table 1 the Licensee must provide the amended document to the NT EPA, along with:
Non-compliant The Blacktip Operations Emergency Response Plan was amended on 10 Feb 2016. During the NTEPA audit on 28 July 2016, it was identified that the amendment had not been communicated to NTEPA. Subsequently on 14 November 2016, Eni submitted to NTEPA the complete documentation, including a tabulated summary of the amendments with document references, reasons for the amendments, and assessment of the environmental risk associated with the amendments.
28 July 2016
9.1. a tabulated summary of the amendment(s) with document references;
9.2. reasons for the amendment(s); and
9.3. an assessment of environmental risk associated with the amendment(s)
Table 1: Licence documents
Document title
Eni Australia Blacktip Project - Produced Water Management Plan (000036_DV_EX.HSE.0381.000_A03 – November 2010)
Eni Australia Blacktip – Flaring Management Plan (000036_DV_EX.HSE.679.000_A01 – April 2009)
Eni Australia Blacktip Operations Oil Spill Contingency Plan (000036_DV_PR.HSE.0388.000_07 – January 2014)
Eni Australia Blacktip Project Onshore Gas Plant Environmental Management Plan (000036_DV_EX.HSE.0684.000_A03 – November 2010)
Blacktip Offshore Environment Plan [as it applies to activities within NT waters] (0036_DV_PR.HSE.0677.000, Rev 06 – February 2014).
Blacktip Operations Emergency Response Plan (000036_DV_PR.HSE.0675.000 Rev 04, July 2012)
10. The NT EPA may require the licensee to revise or amend and resubmit any amended document. - -
OPERATIONAL - -
11. The Licensee must maintain and implement a Communication Plan which includes a strategy for communicating with Blacktip Project Operations Updated
Page 4 of 18
members of the public who are likely to have a real interest in or be affected by the Activity. Communication Plan 000036_DV_PR.DPM.0759.000_04 was updated 1 December 2015.
1 Dec 2015
12. The Licensee must maintain a log of each complaint made in relation to the Activity. The log must include details of the following:
No complaints have been received to date.
Reviewed 16 Jan 2017
12.1. the date and time of the complaint; - -
12.2. the contact details of the complainant if known, or where no details are provided a note to that effect; - -
12.3. the nature of the complaint; - -
12.4. the nature of events giving rise to the complaint; - -
12.5. prevailing weather conditions at the time of the complaint; - -
12.6. the action taken in relation to the complaint, including any follow-up contact with the complainant; and - -
12.7. if no action was taken, why no action was taken. - -
13. The Licensee must maintain and implement an Emergency Response Plan which documents the procedures to deal with emergencies associated with the Licensed Activity.
Blacktip Operations Emergency Response Plan 000036_DV_PR.HSE.0675.000_05 dated 10 Feb 2016
Sighted 30 Jan 2017
14. The Licensee must ensure that all relevant personnel have received training in the implementation of the Emergency Response Plan.
Inductions, muster drills and emergency exercises are conducted monthly at YGP. Records of emergency exercises are stored in J drive: <J:\EMERGENCY RESPONSE\EMERGENCY RESPONSE DRILLS>
Most recent exercises conducted on 18 Dec 2016, 8 Jan 2017 and 15 Jan 2017.
15. The Licensee must ensure any plant and equipment used for the Licensed Activity: Equipment maintained in accordance with maintenance procedures and engineering documentation, and
Sighted 28 July 2016
15.1. is fit for purpose;
15.2. is maintained; and
15.3. is operated by a person trained to use the plant or equipment.
Page 5 of 18
SAP work orders. Records are maintained in SAP.
16. The Licensee must segregate waste for recycling, re-use and disposal.
Waste is segregated on site, e.g. scrap steel, wooden pallets for reuse, general waste, hazardous waste.
Inspected 26 Jan 2017
DISCHARGES AND EMISSIONS - -
17. This Licence authorises wastewater to be discharged from the discharge points identified in Table 2, as shown in Figure 1 and Figure 2 in Appendix 1.
- -
Table 2: Authorised Wastewater Discharge Points
Authorised Discharge Point
Description Location UTM coordinates (MGA94)
PW-01 Produced Formation Water discharged via diffuser to ocean
Latitude: -14.241506 Longitude: 129.385128
542277 mE 8425557 mN
WW-01 Treated wastewater effluent to irrigation field
Latitude: -14.241548 Longitude: 129.438568
547311 mE 8425514 mN
SW-01 Treated stormwater effluent to ground
Latitude: -14.242255 Longitude: 129.436347
547072 mE 8425437 mN
SW-03 Stormwater overflow to ground
Latitude: -14.242255 Longitude: 129.436347
547033 mE 8425293 mN
- -
18. Wastewater discharged from the authorised discharge points specified in Table 2 must not: None reported or detected.
Reviewed 16 Jan 2017
18.1. contain any visible matter, petroleum hydrocarbon sheen or scum, litter or other objectionable matter; - -
18.2. cause or generate odours which would adversely affect the use of surrounding waters; - -
18.3. cause algal blooms in receiving waters; - -
18.4. cause visible change in the behaviour of fish or other aquatic organisms in receiving waters; - -
18.5. cause mortality of fish or other aquatic organisms in receiving waters; or - -
Page 6 of 18
18.6. cause adverse impacts on plants. - -
19.
Wastewater discharged from the authorised discharge points in Table 2 must not exceed the discharge limits specified in Table 3, when measured at the monitoring site codes specified in Table 3. Table 3: Wastewater discharge limits and trigger values
Monitoring site code
SW-02 & SW-03 WW-02 PW-02
Parameter Abbr Unit
Trigger value
Limit Trigger value
Limit Trigger value
Limit
pH pH pH - - 6.5-8.51 - - 6.5-8.5
Biological oxygen demand
BOD mg/L - - 20 - -
Total Suspended Solids
TSS mg/L - - 301 - 10 50
Escherichia coli E.coli cfu/ 100mL
- - 1001 10002 - -
Copper Cu µg/L - - - - - 10
Zinc Zn µg/L - - - - 433 -
Benzene µg/L - - - - 13003 -
Oil in Water4 OIW mg/L 1 6 10 - 6 25
1 Wastewater Treatment Plant Approval, Department of Health and Community Services (DF2008/15, DD2008/02134) 2 Guidelines for Management of Recycled Water Systems, Northern Territory Department of Health 2014 3 80% species protection trigger levels, Australian and New Zealand Guidelines for Fresh and Marine Water Quality (ANZECC 2000) 4 Analysis method: Hand held meter using florescence with hexane extraction
Non-compliant Eni has an ongoing water monitoring program to, where possible, verify wastewater is within the specified limits prior to discharge. However, some exceedances were identified: - 19 July 2016 – E.Coli in treated wastewater - 6 December 2016 – OIW and TSS in produced water
Dates of exceedances: 19 July 2016 6 Dec 2016
Page 7 of 18
20.
This Licence authorises air emissions to be discharged from the authorised emission points identified in Table 4, as shown in Figure 1 in Appendix 2.
Table 4: Authorised Atmospheric Emission Points
Authorised Emission Point
Description Location Emission Point Height (m)
A01 High Pressure Flare 01.230.1.A.002
Latitude: -14.244668 Longitude: 129.436305
-
A02 Low Pressure Flare 01.230.1.A.003
Latitude: -14.244668 Longitude: 129.436305
-
A03 Gas Turbine Compressor A 01.360.1.A.001A
Latitude: -14.242052 Longitude: 129.435811
15
A04 Gas Turbine Compressor B 01.360.1.A.001B
Latitude: -14.242328 Longitude: 129.435709
15
A05 Gas Turbine Compressor C 01.360.1.A.001C
Latitude: -14.242557 Longitude: 129.43557
15
A06 Gas Engine Generator No. 1 01.470.1.A.001A
Latitude: -14.241621 Longitude: 129.435146
8
A07 Gas Engine Generator No. 2 01.470.1.A.001B
Latitude: -14.241621 Longitude: 129.435146
8
A08 Gas Engine Generator No. 3 01.470.1.A.001C
Latitude: -14.241621 Longitude: 129.435146
8
A09 Emergency Diesel Generator Package 01.480.1.A.001
Latitude: -14.240997 Longitude: 129.43558
-
- -
21.
Air emissions at the authorised emission points identified in Table 4 must not exceed the concentration limits specified in Table 5. Table 5: Air emission concentration limits and trigger values
Atmospheric Emission Points Concentration limits Trigger values
Emission point code Description
SO2* NOx* CO* Solid Particles VOC Smoke NOx* Smoke
mg/m3 mg/m3 mg/m3 mg/m3 mg/m3 mg/m3
Non-compliant Carbon monoxide (CO) emission concentrations measured from the generators in August 2016 ranged from 980 to 1,500 mg/m3 and exceeded the limit of 100 mg/m3 specified in
Dates of exceedance: 18 August 2016
Page 8 of 18
A01 High Pressure Flare
‐ ‐ ‐ ‐ 402
No visible emission other than for a total period of no more than 5 minutes in any 2 hours
‐ Ringelmann 1 or 20% opacity
A02 Low Pressure Flare
A03 Gas Turbine Compressor A
100 3502 1001 502 402 ‐ ‐ ‐ A04 Gas Turbine Compressor B
A05 Gas Turbine Compressor C
A06 Gas Engine Generator No. 1
1002 5000 1001 502 402 ‐ 3502 ‐ A07 Gas Engine Generator No. 2
A08 Gas Engine Generator No. 3
A09 Emergency Diesel Generator ‐ ‐ ‐ ‐ ‐ ‐ ‐ ‐
*Dry, 273K, 101.3 kPa, 15% O2 or at manufacturer's specified level 1 Integrated Pollution Prevention and Control Reference Document on Best Available Techniques for Large Combustion Plants, European Commission 2006 2 Protection of the Environment Operations (Clean Air) Regulation 2010, New South Wales
Table 5 under EPL57-02 condition 21. The CO emissions are in line with the manufacturer specifications. Revision of the CO limit is under discussion with NTEPA. All other emissions were within the concentration limits.
22. Air emissions from the authorised emission points identified in Table 4 must not exceed the annual pollutant mass limits specified in Table B in Appendix 2.
Non-compliant The annual carbon monoxide (CO) emissions were reported above the EPL limits (specified in Table B under Appendix 2 of the EPL) for the power
Identified 7 Feb 2017
Page 9 of 18
generators and emergency diesel generator. Revision of the CO limits are under discussion with NTEPA. All other emissions were within the mass limits.
23. The Licensee must ensure that stormwater does not come into contact with a contaminant or waste, which causes or is likely to cause environmental harm.
Clean stormwater, that is allowed to run off site, is kept segregated from contaminated stormwater or other polluting substances.
Inspected 26 Jan 2017
MONITORING - -
24. The Licensee must for all terrestrial monitoring points: - -
24.1. install, maintain and provide appropriate identification signage so that they are easily identifiable at all times;
and
Non-compliant Signage has been installed at terrestrial monitoring points. However, power generators are labelled A, B and C whereas in the EPL57-02 they are distinguished by numbers no 1, 2, 3. Revision of the EPL is under discussion with NTEPA, including the generator labels.
Inspected 28 July 2016
24.2. maintain safe access and egress, as is reasonably practicable. Access and egress is maintained.
Inspected 26 Jan 2017
25. For each sample required to be collected by this Licence the following information must be recorded and retained: For each sample, a Chain of Custody form
Sighted
Page 10 of 18
25.1. the date on which the sample was taken; is available with the required information. Samples are also recorded in the lab sampling register.
26 Jan 2017
25.2. the time at which the sample was collected;
25.3. the point at which the sample was taken;
25.4. the name of the person who collected the sample;
25.5. the chain of custody forms relating to the sample;
Chain of custody forms are available for each sample sent for external laboratory analysis.
Sighted 26 Jan 2017
25.6. the field measurements and/or analytical results for the sample; and
External laboratory results are maintained on file. Field measurements are recorded in the lab sampling register.
Sighted 26 Jan 2017
25.7. laboratory QA/QC documentation.
Laboratory QA/QC documentation is maintained by the laboratory.
Reviewed 28 July 2016
26. Discharge monitoring must be conducted in accordance with Table A in Appendix 1.
Non-compliant Discharge monitoring has been undertaken. However, the monitoring undertaken was not fully compliant. The quarterly produced water sample collected on 7 Sept 2016 was not representative of discharge. On site monitoring of produced water did not include EC, DO,
Reviewed 26 Jan 2017
Page 11 of 18
Temperature or Turbidity until Sept 2016, when the equipment was available on site and operators received training. DO analysis is still pending further training on the procedure. On site monitoring of stormwater discharge from the open drains sump (ODS) and utilities discharge has been conducted on a regular basis, however gaps have been identified where data is not available: 24 July 2016 (utilities) 14 Aug 2016 (utilities) 4 Dec 2016 (utilities) 11 Dec 2016 (utilities) 25 Dec 2016 (utilities) 1 Jan 2017 (utilities) 10 Jan 2017 (utilities) 15 Jan 2017 (utilities) 22 Dec 2016 (ODS) 26 Dec 2016 (ODS) 27 Dec 2016 (ODS) 28 Dec 2016 (ODS) 1 Jan 2017 (ODS) 2 Jan 2017 (ODS)
Page 12 of 18
3 Jan 2017 (ODS) 23 Jan 2017 (ODS) 24 Jan 2017 (ODS) 25 Jan 2017 (ODS) 3 Feb 2017 (ODS) 5 Feb 2017 (ODS) 6 Feb 2017 (ODS) Refer to Section 6 and Appendices E and G of the Blacktip Annual Environmental Performance Report 2016 (000036_DV_PR.HSE.1120.000).
27. Air emission monitoring must be conducted in accordance with Table A in Appendix 2.
Air emission monitoring has been conducted in accordance with the EPL.
Conducted: 10 Dec 2015, 17 Aug 2016, 15 Feb 2017
28. Groundwater monitoring must be conducted in accordance with Table A in Appendix 3.
Groundwater monitoring was conducted in accordance with the EPL
Conducted: 8 March 2016, 24 May 2016, 7 Sep 2016, 7 Dec 2016
29. The Licensee must measure and record fuel/gas flow from the flow meters listed in Table 6.
Flowmeters operational
Reviewed 16 Jan 2017
Table 6: Flow Meters
Gas Flow Meter Description Location
230.1 FIT.008 High pressure flare meter Latitude: -14.243973 Longitude: 129.435191
230.1 FIT.002 Low pressure flare meter
420.1 FIT 007 Fuel gas to flare purge distribution
420.1 FIT 161 Gas Turbine Compressor A 01.360.1.A.001A
Latitude: -14.242052 Longitude: 129.435811
420.1 FIT 261 Gas Turbine Compressor B Latitude: -14.242328
Page 13 of 18
01.360.1.A.001B Longitude: 129.435709
420.1 FIT 361 Gas Turbine Compressor C 01.360.1.A.001C
Latitude: -14.242557 Longitude: 129.43557
420.1 FIT 004 Low pressure fuel gas to generators
Latitude: -14.243071 Longitude: 129.435511
30. The Licensee must ensure that all water samples: - -
30.1. are collected in accordance with AS/NZS 5567; and
All water sampling is carried out in accordance with Water Sampling Procedure 000036_DV_PR.HSE.1013.000_01 dated 9 October 2014
Checked 26 Jan 2017
30.2. are submitted to a laboratory with current NATA accreditation or equivalent, for the parameters to be
measured.
The external laboratory services provider is Intertek, which is NATA accredited. Refer to <http://www.nata.com.au/nata/scopeinfo/?key=14671>
Reviewed 16 Jan 2017
RECORDING AND REPORTING - -
31. All records required to be kept by this Licence must be in a legible format. All sighted records are legible.
-
32. The Licensee must maintain records of the nature, quantities and disposal method of all waste streams generated at the premises, including Listed Waste.
Waste volume and type removed from site is recorded in a monthly report.
Reviewed 26 Jan 2017
33. The Licensee must keep records of all non-compliances with this Licence. All non-compliances are recorded in a non-compliances register.
Reviewed 26 Jan 2017
34. The Licensee must as soon as practicable, and in any case within 24 hours, notify the NT EPA of non-compliances with this Licence.
Non-compliant Non-compliance with Condition 22 was identified during the preparation of this
Reviewed 26 Jan 2017
Page 14 of 18
report, and not reported within 24 hours.
35. Non-compliance notifications required under condition 34 must identify:
Non-conformance notifications include the information specified.
Reviewed 26 Jan 2017
35.1. the date and time of the non-compliance;
35.2. when the non-compliance was detected and by whom;
35.3. the actual and potential causes and contributing factors to the non-compliance;
35.4. the risk of environmental harm arising from the non-compliance;
35.5. action(s) that have or will be undertaken to mitigate any environmental harm arising from the non-compliance;
and
35.6. corrective actions that have or will be undertaken to ensure the non-compliance does not reoccur.
36. The Licensee must immediately, and in any case within 24 hours, notify the NT EPA of any potential or actual environmental harm or pollution, by contacting the Pollution Hotline on telephone number 1800 064 567 and emailing [email protected].
Incidents causing potential or actual environmental harm or pollution have been reported – see Section 3 Summaries.
Reviewed 16 Jan 2017
37. The Licensee must notify the NT EPA of material or serious environmental harm in accordance with section 14 of the WMPC Act.
There have been no events resulting in material or serious environmental harm.
-
38. The Licensee must complete the attached Annual Return, Appendix 4, which report relates to the preceding 12 month period, and provide to the NT EPA within 10 Business Days after the anniversary of the commencement date of this Licence.
This report will be provided to NT EPA in accordance with the EPL
February 2017
39. The NT EPA may require the Licensee to revise or amend and resubmit the Annual Return. - -
40. The Licensee must provide an Annual Performance Report, which report relates to the preceding 12 month period, to the NT EPA within 10 Business Days after the anniversary of the commencement date of this Licence.
This report will be provided to NT EPA in accordance with the EPL
February 2017
41. The Annual Performance Report required under condition 40 must:
Refer to the following sections of the Blacktip Annual Environmental Performance Report 2016
-
Page 15 of 18
41.1. include description of gas plant infrastructure and processes; Section 3
February 2017
41.2. report on total condensate produced and total gas processed by the gas plant; Section 4
41.3. report on the quality of gas received by the plant; Section 4
41.4. include a tabulation of all monitoring data required as a condition of this Licence, including discharge,
groundwater and air emissions monitoring; Section 5-6, 8
41.5. include a trend analysis and interpretation of all monitoring data required as a condition of this Licence; Section 5-6, 8
41.6. include long term trend analysis of monitoring data to demonstrate any environmental impact associated with
the Activity over a minimum period of three years; Section 5-6, 8
41.7. identify the number of exceedances of discharge/concentration trigger values that have occurred during the
reporting period; Section 9
41.8. report on the following associated with discharges:
total annual discharges (ML/year);
frequency and volume of Produced Formation Water discharges;
Section 6, 7
41.9. report the total annual emissions of the following parameters, for each emission point, as well as for condensate tanks and fugitive emissions:
NOx;
SO2;
VOC;
PM10;
Refer to Eni NGER and NPI submissions for 2015-2016.
41.10. report in accordance with the requirements for a Monitoring Report identified in: Guidelines for Consultants Reporting on Environmental Issues (as amended from time to time), available from http://www.ntepa.nt.gov.au/__data/assets/pdf_file/0005/136481/guidelines_consultants_reporting_environmental_issues.pdf:
Section 2.2
42. The NT EPA may require the Licensee to revise or amend and resubmit the Annual Performance Report. - -
PERFORMANCE IMPROVEMENT - -
43. The Licensee must provide a Produced Formation Water Plan to the NT EPA by 1 May 2015. Non-compliant The Produced Formation Water Plan For EPL57-02 Condition 43 000036_DV_PR.HSE.1056.000_03 was submitted on 14 July
14 July 2016
44. The Produced Formation Water Plan required under condition 43 must:
44.1. propose a mixing zone in accordance with the NT EPA Guidelines on Mixing Zones, Version 1.2, available
from: http://www.ntepa.nt.gov.au/__data/assets/pdf_file/0017/160631/guidelines_mixing_zones.pdf;
44.2. assess whether the risks posed by management of Produced Formation Water are as low as reasonably
practicable (ALARP);
44.3. include a proposed dilution factor (including methodology used to derive the dilution factor) based on results from produced water chemical characterisation, ecotoxicity and biodegradation studies undertaken in
Page 16 of 18
accordance with EPL 57-01; 2016 as agreed with NT EPA. NTEPA provided feedback on 22 December 2016 and found it did not comply with all requirements under Condition 44. The following conditions have not been satisfied: 44.1, 44.2, 44.5, 44.6, 44.7, 44.8, 44.9, 44.10.
44.4. include summary and interpretation of the results for all historical studies, including:
chemical composition of Produced Formation Water;
biodegradation and bioaccumulation potential of Produced Formation Water contaminants;
toxicity testing of Produced Formation Water; and
marine surveys;
44.5. identify surface water monitoring points where the 99% level of species protection trigger values specified in
Table 3.4.1 of the Australian and New Zealand Guidelines for Fresh and Marine Water Quality (ANZECC 2000) will be applied;
44.6. identify a schedule for monitoring of the surface water monitoring points identified as part of condition 44.5;
44.7. identify a methodology for validating the near and far field Produced Formation Water dispersion modelling
predictions that have been included in the document Eni Blacktip Project Produced Water Management Plan (document number 00036_DV_EX.HSE.0381.000_A03);
44.8. identify a schedule for implementation and completion of validation activities.
44.9. identify actions that will be completed to ensure that wastewater discharged from authorised discharge point
PW-01 achieves the trigger value specified in Table 3, when measured at monitoring site code PW-02; and
44.10. identify a schedule for completion of actions identified as part of condition 44.9.
45. The NT EPA may require the Licensee to revise or amend and resubmit the Produced Formation Water Plan. NTEPA requested resubmission of the Plan.
Received 22 Dec 2016
46. The Licensee must comply with the schedules prepared in accordance with conditions 44.6, 44.8 and 44.10. The activities are tracked in Sharepoint.
Checked 16 Jan 2017
47. The Licensee must provide an Air Emissions Assessment Report to the NT EPA by 1 May 2015.
Air Emissions Assessment Report For EPL57-02 Condition 47 000036_DV_PR.HSE.1057.000_01 dated 29 May 2015 Submitted 29 May 2015 as per extension agreed with NT EPA
29 May 2015
48. The Air Emissions Assessment Report required under condition 47 must:
48.1. identify whether emissions stack maintenance, discharge ducting and sampling ports for authorised
emissions points A03, A04, A05, A06, A07 and A08 comply with the Australian Standard for Stationary Source Emissions (AS4323.1), as amended from time to time;
48.2. identify whether stack sampling complies with the Environment Protection Authority, Victoria document A
Guide to the Sampling and Analysis of Air Emissions and Air Quality, as amended from time to time;
48.3. identify a schedule for achieving compliance with the two abovementioned documents;
48.4. identify the cause and contributing factors to ongoing NOx exceedance(s) of the trigger value specified in
Table 5 of this Licence;
Page 17 of 18
48.5. identify the risk to the environment associated with continued NOx exceedances;
48.6. assess whether the risks posed by management of NOx emissions are ALARP;
48.7. identify actions that will be completed to reduce NOx air emissions from authorised emissions points A06,
A07 and A08 to achieve the trigger value specified in Table 5 of this Licence; and
48.8. identify a schedule for completion of actions identified as part of condition 48.7.
49. The NT EPA may require the Licensee to revise or amend and resubmit the Air Emissions Assessment Report. The report has been accepted by NTEPA.
-
50. The Licensee must comply with the schedules prepared in accordance with conditions 48.3 and 48.8. The activities are tracked in Sharepoint.
Checked 16 Jan 2017
Page 18 of 18
3. Summaries Complaints Recording
Number of complaints recorded by the licensee during the reporting period (as required by condition 12 of the licence)
None
Summary of complaints n/a Summary of outcomes n/a
Notifications of potential or actual environmental harm or pollution Number of events recorded by the licensee during the reporting period (as required by condition 35 of the licence)
2
Summary of events Summary of outcomes 6 December 2016 – PFW discharge exceeded TSS and OIW limits.
On site laboratory equipment have been re-verified and calibrated.
2 January 2017 – PFW overflow to grade System has been reconfigured and the valve, which is not normally used, has been isolated.
Signature and Certification
This declaration must only be signed by a person(s) with the legal authority to sign it. The ways in which the application may be signed, and the people who may sign the application, are set out in the categories below.
If the licence holder is: Tick The application must be signed and certified by one of the following:
An individual The individual.
A partnership A partner.
A company
The common seal being affixed in accordance with the Corporations Act, or
Two directors, or
A director and a company secretary, or
If a proprietary company that has a sole director who is also the sole company secretary – by that director.
A public authority
The Chief Executive Officer (CEO) of the public authority, or
By a person delegated to sign on the public authority’s behalf in accordance with its legislation (Please note: a copy of the relevant instrument of delegation must be attached to this application).
I/We hereby declare that the information provided in this Annual Audit and Compliance Report and accompanying documents is to the best of my/our knowledge, true and correct.
Signature Signature
Name (printed) Name (printed)
Position Position
Date Date
Seal (if signing under seal):
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APPENDIX B:
POLLUTANT MASS INVENTORY
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Appendix B: Air emissions annual pollutant mass inventory and comparison against EPL limits
Atmospheric Emission Points Annual Pollutant Mass (t)
Point ID Description SO2 NOx CO CO2 CH4 N2O CO2-e
A01 High Pressure Flare limits 0.1 6 9 4,239 7 0.1 4,443
Annual pollutant load 2013-2014 <0.1 2 11 3,281 6 <0.1 3,438
2014-2015 <0.1 2 14 3,350 6 <0.1 3,512
2015-2016 0.02 1.4 8 2,520 4 <0.1 2,641
A02 Low Pressure Flare limits 0.1 8 13 5,909 10 0.1 6,193
Annual pollutant load 2013-2014 <0.1 3 15 4,531 8 <0.1 4,749
2014-2015 <0.1 2 11 4,626 8 <0.1 4,849
2015-2016 0.03 1.9 11 3,382 5 0.1 3,545
- Flare Fuel Gas limits - - - - - - -
Annual pollutant load 2013-2014 -3 -3 -3 305 1 <0.1 320
2014-2015 -3 -3 -3 305 1 <0.1 320
2015-2016 0.002 0.2 1 295 0.4 0.01 310
A03 Gas Turbine Compressor A limits
0.3 266 44 77,494 7 0.1 77,690 A04 Gas Turbine Compressor B limits
A05 Gas Turbine Compressor C limits
Annual pollutant load 2013-2014 0.2 117 29 25,620 2 <0.1 25,685
2014-2015 0.2 93 30 25,875 2 <0.1 25,941
2015-2016 0.2 100 28 24,885 2 0.05 24,948
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Atmospheric Emission Points Annual Pollutant Mass (t)
Point ID Description SO2 NOx CO CO2 CH4 N2O CO2-e
A06 Gas Engine Generator No. 1 limits
0.1 234 7 4,061 0.4 0.1 4,072 A07 Gas Engine Generator No. 2 limits
A08 Gas Engine Generator No. 3 limits
Annual pollutant load 2013-2014 <0.1 117 12 2,911 <0.1 <0.01 2,918
2014-2015 <0.1 168 12 3,027 <0.1 <0.01 3,035
2015-2016 0.02 155 16 3,111 0.24 0.006 3,119
A09 Emergency Diesel Generator limits 0.1 1 0.1 100 0.1 0.1 100
Annual pollutant load 2013-2014 <0.1 <1 0.4 -6 -6 -6 -6
2014-2015 <0.1 <1 0.4 88 0.13 0.25 88
2015-2016 <0.001 0.7 0.18 34 0.002 <0.001 34
- Condensate Tank vents limits - - - - 39 - 809
Annual pollutant load 2013-2014 -3 -3 -3 0 <1 0 11
2014-2015 -3 -3 -3 0 <1 0 11
2015-2016 -3 -3 -3 0 <1 0 10
- Fugitive limits - - - - 58 - 1213
Annual pollutant load 2013-2014 <0.1 0.9 0.4 0 29 0 617
2014-2015 <0.1 0.7 0.3 0 29 0 611
2015-2016 -3 -3 -3 0 23 0 563
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1 Sox, NOx and CO figures are as per the NPI reports, and CH4, N2O and CO2 are as per NGER reports.
2 Pollutants above the EPL mass limit are indicated in red text.
3 Not available or below threshold (i.e. for NPI substances, SO2, NOx, CO).
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APPENDIX C:
EMISSIONS SAMPLING RESULTS
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Appendix C.1: Summary of stack emission monitoring results from the compressors
CO CO2 CH4 NOx1 Sox Solid particles VOCs
EPL57-02 limit 100 mg/m3 - - 350 mg/m3 100 mg/m3 50 mg/m3 40 mg/m3
27 March 2014
Compressor A NM NM NM 280 32 NM <0.035
Compressor B NM NM NM 310 21 NM <0.048
Compressor C NM NM NM NM NM NM NM
18 June 2014
Compressor A NM NM NM 260 24 NM <0.045
Compressor B NM NM NM 260 48 NM <0.047
Compressor C NM NM NM NM NM NM NM
17 December 2014
Compressor A NM NM NM 250 15 NM 0.83
Compressor B NM NM NM 160 <6.1 NM 1.3
Compressor C NM NM NM 240 14 NM 5.6
24 June 2015
Compressor A NM NM NM NM NM NM NM
Compressor B <3.2 2.6% <0.19 310 NM NM <0.19
Compressor C NM NM NM NM NM NM NM
9 December 2015
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CO CO2 CH4 NOx1 Sox Solid particles VOCs
EPL57-02 limit 100 mg/m3 - - 350 mg/m3 100 mg/m3 50 mg/m3 40 mg/m3
Compressor A NM NM NM NM NM NM NM
Compressor B <3.1 2.6% NM 180 <2.8 NM <0.19
Compressor C <3.1 2.6% NM 200 <2.8 NM <0.234
18 August 2016
Compressor A NM NM NM NM NM NM NM
Compressor B 3.6 2.3 <1.9 190 <6.5 <1.9 2.3
Compressor C 3.3 2.3 <2.0 210 <6.0 <2.0 1.4
15 February 2017
Compressor A tba tba tba tba tba tba tba
Compressor B tba tba tba tba tba tba tba
Compressor C tba tba tba tba tba tba tba
Notes: 1 NOx presented as NO2 equivalent. 2 Sox presented as the cumulative concentration of SO2 and SO3. 3 All measurements reported on a dry basis at NTP and corrected to 15% O2 in accordance with the EPL. 4 Measurements above the EPL limit are indicated in red. 5 NM = Not measured.
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Appendix C.2: Summary of stack emission monitoring results from the generators
CO CO2 CH4 NOx1 Sox PM VOCs
EPL57-02 limit 100 mg/m3 5000 mg/m3 100 mg/m3 50 mg/m3 40 mg/m3
EPL57-02 trigger value 350 mg/m3
27 March 2014
Generator A NM NM NM NM NM NM NM
Generator B NM NM NM 1810 NM NM NM
Generator C NM NM NM 1450 NM NM NM
18 June 2014
Generator A NM NM NM 2120 NM NM NM
Generator B NM NM NM 1570 NM NM NM
Generator C NM NM NM 1890 NM NM NM
17 December 2014
Generator A NM NM NM 1220 NM NM NM
Generator B NM NM NM 1570 NM NM NM
Generator C NM NM NM 1770 NM NM NM
24 June 2015
Generator A 944 7.8% NM 1730 NM NM 0.2
Generator B 1023 7.9% NM 1610 NM NM 1.7
Generator C 787 6.7% NM 1500 NM NM 0.7
9 December 2015
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CO CO2 CH4 NOx1 Sox PM VOCs
EPL57-02 limit 100 mg/m3 5000 mg/m3 100 mg/m3 50 mg/m3 40 mg/m3
EPL57-02 trigger value 350 mg/m3
Generator A 900 11.6% NM 1500 <2.8 NM 0.7
Generator B 800 6.6% NM 1700 <2.8 NM 0.7
Generator C 710 11.5% NM 1600 <2.8 NM 0.5
18 August 2016
Generator A 1300 11.5 0.0041 1700 45 <2.8 3.9
Generator B 1500 11.3 0.0041 1500 50 <2.8 2.8
Generator C 980 11.5 <0.002 1700 56 <2.8 2.9
15 February 2017
Generator A tba tba tba tba tba tba tba
Generator B tba tba tba tba tba tba tba
Generator C tba tba tba tba tba tba tba
Notes: 1 NOx presented as NO2 equivalent. 2 Sox presented as the cumulative concentration of SO2 and SO3. 3 All measurements reported on a dry basis at NTP and corrected to 15% O2 in accordance with the EPL. 4 Measurements above the EPL limit are indicated in red.
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APPENDIX D:
PRODUCED WATER MONITORING RESULTS
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Routine produced water discharge sampling and analysis under Table A of EPL57-02
Date Volume pH EC DO Temp Turbidity OIW
m3 pH µs/cm mg/L °C NTU mg/L
17 January 2016 71 19 -2 -2 -2 -2 19
24 January 2016 139 6.83 -2 -2 -2 -2 7.7
1 February 2016 562 6.63 -2 -2 -2 -2 18.5
13 February 2016 481 6.59 -2 -2 -2 -2 3.9
24 February 2016 361 8.01 -2 -2 -2 -2 3.6
2 March 2016 300 6.89 -2 -2 -2 -2 9.2
12 March 2016 62 6.52 -2 -2 -2 -2 22
28 March 2016 464 7.1 -2 -2 -2 -2 9.6
10 April 2016 75 6.6 -2 -2 -2 -2 10.2
4 May 2016 233 6.75 -2 -2 -2 -2 19
5 May 2016 394 8.09 -2 -2 -2 -2 24.6
24 May 2016 274 6.95 -2 -2 -2 -2 10.4
25 May 2016 257 6.98 -2 -2 -2 -2 11.7
8 June 2016 212 6.58 -2 -2 -2 -2 9.7
22 July 2016 405 7.37 -2 -2 -2 -2 12.8
6 September 2016 473 6.78 646.2 -3 24 67.1 20.6
23 September 2016 446 8.4 594.2 -3 23.6 4.8 13.6
13 October 2016 395 7.7 1.25 -3 20.6 800 8.8
15 October 2016 171 6.7 1.05 -3 25.8 596 2.8
25 November 2016 88 6.6 - -3 - - 7.8
28 November 2016 189 6.5 1.06 -3 28.2 75 7.6
6 December 2016 155 6.5 819 -3 28 34 1.6
Notes: 1 This table summarises the discharges between 1 January 2016 – 31 December 2016. 2 Some site laboratory equipment not yet available and required training still in progress. Note: these
parameters are included in the quarterly monitoring. 3 Reagent not available on site. Note: these parameters are included in the quarterly monitoring.
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Quarterly produced water sampling and analysis under Table A of EPL57-02
Unit EPL
limit
Trigger
value
25 May
2016
7 Sep
20161
12 Dec
2016
6 Feb
20172
ENVIRONMENTAL PARAMETERS
pH - 6.8-8.5 - 7.12 - 7.59 tba
EC µs/cm - - 416 - 805 tba
Turbidity NTU - - 28 - 9.5 tba
DO mg/L - - 11.2 - 8.4 tba
OIW mg/L 25 6 106.93 - 57.44 tba
TSS mg/L 50 10 48 - 844 tba
TDS mg/L 201 - 259 tba
BOD mg/L - - NM - 18.1 tba
TOC mg/L - - 130 - 940 tba
COD mg/L - - 550 - 3000 tba
NUTRIENTS
Nox-N µg/L - - <5 - 7 tba
NO3-N µg/L - - <5 - 6 tba
NO2-N µg/L - - <5 - <5 tba
Ammoniacal N µg/L - - 650 - 10 tba
TP µg/L - - 630 - 800 tba
TN µg/L - - 1200 - 200 tba
HYDROCARBONS
TRH C6-C9 µg/L - - 4400 - 5500 tba
TRH C6-C10 µg/L - - 5500 - 6300 tba
TRH C6-C10 less BTEX µg/L - - 3000 - 3800 tba
TPH >C16-C35 Ali µg/L - - <100 - <100 tba
TPH >C35 Ali µg/L - - <100 - <100 tba
TPH C16-C35 Aro µg/L - - <50 - <50 tba
Benzene µg/L - 1300 420 - 460 tba
Toluene µg/L - - 1000 - 1000 tba
Ethylbenzene µg/L - - 140 - 140 tba
m+p-xylene µg/L - - 670 - 690 tba
o-xylene µg/L - - 230 - 230 tba
napththalene µg/L - - 43 - 68 tba
TRH C10-C14 µg/L - - 3100 - 27000 tba
TRH C15-C28 µg/L - - 1200 - 620 tba
TRH C29-C36 µg/L - - <100 - <100 tba
TRH >C10-C16 µg/L - - 3100 - 12000 tba
TRH >C10-C16 less Napth µg/L - - 3100 - 12000 tba
TRH >C16-C34 µg/L - - 580 - 360 tba
TRH >C34-C40 µg/L - - <100 - <100 tba
Ali/Ar µg/L - - NM - NM tba
Naphthalene µg/L - - 47 - 14 tba
Acenaphthylene µg/L - - <1 - <1 tba
Acenaphthene µg/L - - <1 - <1 tba
Fluorene µg/L - - 3 - 3 tba
Phenanthrene µg/L - - 3 - 2 tba
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Unit EPL
limit
Trigger
value
25 May
2016
7 Sep
20161
12 Dec
2016
6 Feb
20172
Anthracene µg/L - - <1 - <1 tba
Fluoranthene µg/L - - <1 - <1 tba
Pyrene µg/L - - <1 - <1 tba
Benzo(a)anthracene µg/L - - <1 - <1 tba
Chrysene µg/L - - <1 - <1 tba
Benzo(b,j+k)fluoranthene µg/L - - <2 - <2 tba
Benzo(a)pyrene) µg/L - - <1 - <1 tba
Indeno(1,2,3-c,d)pyrene µg/L - - <1 - <1 tba
Dibenzo(a,h)anthracene µg/L - - <1 - <1 tba
Benzo(g,h,i)perylene µg/L - - <1 - <1 tba
Benzo(a)pyrene TEQ µg/L - - <5 - <5 tba
Total +ve PAHs µg/L - - 53 - 19 tba
PHENOLS
Phenol mg/L - - 0.089 - 0.25 tba
2-Chlorophenol mg/L - - <0.001 - <0.01 tba
4-Chloro-3-Methylophenol mg/L - - <0.005 - <0.05 tba
2-Methylphenol (O-Cresol) mg/L - - 0.14 - 0.54 tba
3/4-Methylphenol(m/p-
Cresol)
mg/L - -
0.14
-
0.43
tba
2-Nitrophenol mg/L - - <0.001 - <0.01 tba
2,4-Dimethylphenol mg/L - - 0.15 - 0.33 tba
2,4-Dichlorophenol mg/L - - <0.001 - <0.01 tba
2,6-Dichlorophenol mg/L - - <0.001 - <0.01 tba
2,4,5-Trichlorophenol mg/L - - <0.001 - <0.01 tba
2,4,6-Trichlorophenol mg/L - - <0.001 - <0.01 tba
2,4-Dinitrophenol mg/L - - <0.02 - <0.01 tba
4-Nitrophenol mg/L - - <0.02 - <0.2 tba
2,3,4,6-Tetrachlorophenol mg/L - - <0.001 - <0.2 tba
2-methyl-4,6-Dinitrophenol mg/L - - <0.01 - <0.01 tba
Pentachlorophenol mg/L - - <0.005 - 0.1 tba
MBA mg/L - - <0.1 - <0.05 tba
METALS
Al µg/L - - 490 - 20 tba
Ar µg/L - - <1 - <1 tba
Ba µg/L - - 260 - 580 tba
Be µg/L - - <0.5 - <0.5 tba
B µg/L - - 86 - 100 tba
Cd µg/L - - 0.4 - 0.4 tba
Co µg/L - - <1 - 1 tba
Cu µg/L 10 - <1 - <1 tba
Cr µg/L - - <1 - 9 tba
Fe µg/L - - 2500 - 4000 tba
Hg µg/L - - 0.6 - 0.6 tba
Mg µg/L - - <5005 9006 34007 tba
Mn µg/L - - 67 - 150 tba
Mo µg/L - - 1 - 3 tba
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Unit EPL
limit
Trigger
value
25 May
2016
7 Sep
20161
12 Dec
2016
6 Feb
20172
Pb µg/L - - <1 - <1 tba
Ni µg/L - - <1 - 81 tba
Se µg/L - - <1 - <1 tba
Sn µg/L - - <1 - <1 tba
Sr µg/L - - 110 - 540 tba
Zn µg/L - 43 2006 - 42 tba
RADIUM
Ra-226 mBq/L - - - - - -
Ra-228 mBq/L - - - - - -
1 A discharge sample was collected on 7 September 2016, however it was sent to the wrong laboratory and therefore
not tested for the quarterly parameters. 2 Results of samples collected on 6 February 2017 are yet to be received. 3 This exceedance was reported to NTEPA See Section 9.1. The analysis was undertaken using a TD3100 benchtop
fluorometer. Prior to discharge, site monitoring using a Horiba water analyser measured OIW at 13.5 mg/L. A
combination of Gas Chromatography Mass Spectrometry (GC-MS) and Gas Chromatography Flame Ionisation
Detection (GC-FID) measured TRH and TPH at ~9 mg/L and below limits of detection, respectively, in the same
sample.
4 Exceedances reported to NTEPA. See Section 9.1.
5 Sampled 11 May 2016 6 Sampled 13 July 2016. 7 Sampled 9 November 2016.
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APPENDIX E:
WWTP SAMPLING RESULTS
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Treated wastewater effluent monitoring results
Date
sampled
Unit EPL
limit
Trigger
value
8 Jan
2016
10 Feb
2016
9 Mar
2016
13 Apr
2016
11 May
2016
8 June
2016
13 July
2016
10Aug
2016
14 Sep
2016
7 Oct
2016
16 Nov
2016
4 Dec
2016
4 Jan
2017
BACTERIOLOGICAL
E Coli /100mL
MPN
1000 100 <10 <10 NM 441 <10 <10 <10 323 <10 203 20 161 tba
Enterococci /100mL
MPN
- - NM NM NM <10 NM NM NM NM 213 NM 50 373 tba
ENVIRONMENTAL
PARAMETERS
pH - - 6.8-8.5 5.02 5.2 NM 6.02 4.59 5.83 5.85 7.18 7.11 7.15 7.26 6.81 tba
EC µs/cm - - 712 836 NM 1560 955 1139 912 1056 808 884 915 773 tba
Turbidity NTU - - NM NM NM 33 NM NM 11 3.2 28 8.5 4.5 4.9 tba
DO mg/L - - NM NM NM 2.7 9.5 7.7 8.2 7.4 4.2 6.1 6.5 6.5 tba
OIW mg/L - - 21.99 18.83 NM 20.48 24.38 84.61 19.42 19.5 29.78 20.12 25.3 43.31 tba
TSS mg/L - 30 25.5 29 14 92 73 26 28 5 56.5 32 35 29 tba
TDS mg/L - - 369 415 81.3 440 515 568 465 531 404 432 401 384 tba
BOD mg/L - 20 18.6 15.8 8.3 23 12 4.9 17 3.8 21.3 19.4 20.1 21.4 tba
TOC mg/L - - NM NM NM 10 15 14 8 10 10 27 7 11 tba
COD mg/L - - NM NM NM <50 70 65 55 50 200 550 <50 65 tba
NUTRIENTS
Nox-N mg/L - - NM NM NM 29 39 28.8 32.3 1.8 5.8 0.3 3.1 0.01 tba
NO3-N mg/L - - NM NM NM 28.8 38.9 28.7 32.2 1.7 5.7 0.15 3.1 <0.005 tba
NO2-N mg/L - - NM NM NM 0.15 <0.05 0.8 0.025 0.11 0.046 0.13 0.014 0.006 tba
Ammoniacal N mg/L - - NM NM NM 5.75 3.27 22.2 13.1 29 14 11 1.87 8.3 tba
TP mg/L - - 2.46 1.91 NM 3.01 2.52 NM 2.4 2.14 2.76 2.34 11.5 2.12 tba
TN mg/L - - 28 32.6 NM 37.6 45.8 NM 46.1 34.8 30.1 25.3 9.4 9.61 tba
HYDROCARBONS
vTRH(C6-
10)/BTEX
mg/L - - NM NM NM NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
tba
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Date
sampled
Unit EPL
limit
Trigger
value
8 Jan
2016
10 Feb
2016
9 Mar
2016
13 Apr
2016
11 May
2016
8 June
2016
13 July
2016
10Aug
2016
14 Sep
2016
7 Oct
2016
16 Nov
2016
4 Dec
2016
4 Jan
2017
METALS
Al mg/L - - NM NM NM 14100 NM NM NM NM NM NM NM NM NM
Ar mg/L - - NM NM NM 1.45 NM NM NM NM NM NM NM NM NM
Ba mg/L - - NM NM NM 23 NM NM NM NM NM NM NM NM NM
Be mg/L - - NM NM NM 0.05 NM NM NM NM NM NM NM NM NM
B mg/L - - NM NM NM 64 NM NM NM NM NM NM NM NM NM
Cd mg/L - - NM NM NM 0.24 NM NM NM NM NM NM NM NM NM
Co mg/L - - NM NM NM 0.23 NM NM NM NM NM NM NM NM NM
Cu mg/L - - NM NM NM 27.7 NM NM NM NM NM NM NM NM NM
Cr mg/L - - NM NM NM 1.7 NM NM NM NM NM NM NM NM NM
Cr III mg/L - - NM NM NM <0.05 NM NM NM NM NM NM NM NM NM
Cr IV mg/L - - NM NM NM <0.05 NM NM NM NM NM NM NM NM NM
Fe mg/L - - NM NM NM 552 NM NM NM NM NM NM NM NM NM
Hg mg/L - - NM NM NM 0.04 NM NM NM NM NM NM NM NM NM
Mg mg/L - - NM NM NM 2.4 NM NM NM NM NM NM NM NM NM
Mn mg/L - - NM NM NM 25.9 NM NM NM NM NM NM NM NM NM
Mo mg/L - - NM NM NM 0.6 NM NM NM NM NM NM NM NM NM
Pb mg/L - - NM NM NM 1.36 NM NM NM NM NM NM NM NM NM
Ni mg/L - - NM NM NM 24.5 NM NM NM NM NM NM NM NM NM
Se mg/L - - NM NM NM 0.4 NM NM NM NM NM NM NM NM NM
Sn mg/L - - NM NM NM 2.6 NM NM NM NM NM NM NM NM NM
Zn mg/L - - NM NM NM 121 NM NM NM NM NM NM NM NM NM
* Values above the trigger value are shown in orange text. There were no exceedances of the E Coli limit specified in EPL57-02.
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APPENDIX F:
STORMWATER MONITORING RESULTS
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Utilities stormwater discharge monitoring (SW-02)
Date
Utilities Stormwater (SW-02)
pH EC OIW
pH µs/cm mg/L
24 July 2016 -3 -3 3.8
14 August 2016 -3 -3 4.1
21 August 2016 6.2 108.6 0
29 August 2016 6.12 104.1 0
4 September 2016 5.79 105.2 0
19 September 2016 6.62 105.9 0
25 September 2016 6.55 106.2 0
16 October 2016 7.05 118.3 0.3
23 October 2016 7.01 118.3 0.2
30 October 2016 5.98 107.1 0.3
13 November 2016 6.38 106.2 0
20 November 2016 5.92 114.4 0
27 November 2016 6.1 117.6 0
4 December 2016 6.0 -3 0
11 December 2016 6.56 -3 0
25 December 2016 -3 113.2 0
1 January 2017 7.3 -3 0.3
10 January 2017 6.19 -3 0
15 January 2017 6.58 -3 2.4
22 January 2017 6.7 111.9 1.6
29 January 2017 6.37 108.9 3.4
Notes: 1 This table summarises the discharge monitoring between 1 January 2016 – 31 December 2016. 2 Prior to July 2016, the utilities stormwater was fed into the produced water treatment system and
part of the produced water stream discharged offshore. 3 Data not available.
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Open drains sump stormwater discharge monitoring (SW-03)
Date
Open Drains Sump (SW-03)
pH EC OIW
pH µs/cm mg/L
22 December 2016 6.86 193.6 -2
26 December 2016 -2 75.4 5.2
27 December 2016 -2 58.8 5.6
28 December 2016 -2 65.6 5.3
1 January 2017 -2 69.9 2.9
2 January 2017 -2 77.6 5.2
3 January 2017 -2 58.6 3.5
4 January 2017 6.34 50.75 3.1
23 January 2017 -2 -2 2.6
24 January 2017 5.45 -2 4.3
25 January 2017 5.93 -2 4.8
3 February 2017 6.62 -2 2.2
5 February 2017 6.43 -2 1.2
6 February 2017 6.05 -2 0.9
Notes: 1 This table summarises the discharge monitoring between 1 January 2016 – 31 December 2016. 2 Data not available.
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APPENDIX G:
GROUNDWATER MONITORING DATA
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Table G.1: Quarterly groundwater monitoring data 2016
Date sampled 8 March 2016 24 May 2016 7 Sep 2016 7 Dec 2016
Parameter Test method Units ADWG61 ANZECC2 BH5 BH5 BH7 BH7 BH5 BH7 BH5 BH7
pH ASTM D1287 - 6.5-8.5 6-8.5 5.47 5.29 5.56 5.78 5.62 5.87 5.71 5.36
EC APHA 2510 mS/cm - 900 221 176.2 184.1 61.3 197.2 77 206.1 183.4
Turbidity Turb1 NTU 5 - 480 150 186 87 210 250 150 400
DO HACH mg/L 85% 80-110% 7.1 7.1 7.3 5.8 8.1 5.8 8.4 7.2
OIW Turner TD3100 mg/L - - 73.41 18.61 8.6 3 7.1 4.3 6.2 8.4
TSS APHA 2540 D mg/L - - 221 278 354 2751 681 2620 704 1413
TDS APHA 2540 C mg/L 600 - 86.7 84.4 90.2 30.3 81 26 78 39
BOD APHA 5210 mg/L - - 12.3 12.2 16.1 12.4 15.3 17.3 17.6 16.8
TOC APHA 5310 B mg/L - - 3 3 4 2 6 3 3 3
COD WCL_13 mg/L - - <50 <50 <50 <50 <50 <50 <50 <50
NOx APHA No2B mg/L - - 1.5 1.1 1.7 0.74 2 1.3 1.9 1.3
Nitrate APHA No2B mg/L 503 - 1.5 1.1 1.7 0.75 2 1.3 1.9 1.3
Nitrite APHA No2B mg/L 34 17 <0.005 <0.005 <0.005 <.005 <0.005 <0.005 <0.005 <0.005
Ammonia APHA 4500 mg/L 0.5 - 0.03 0.02 0.12 0.014 0.008 <0.005 0.017 0.015
Total P ICP-AES mg/L - 320 2.41 1.62 2.1 1.1 1.4 1.8 1.4 1.8
Total N APHA no2B mg/L - - 3.11 2.43 3.5 1.5 4.7 3.4 4.6 3.1
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Date sampled 8 March 2016 24 May 2016 7 Sep 2016 7 Dec 2016
Parameter Test method Units ADWG61 ANZECC2 BH5 BH5 BH7 BH7 BH5 BH7 BH5 BH7
Tot. Coliform AS4276.21-2005 /100ml MPN - - 2 1 387 84 <1 <1 8 15
E. coli AS4276.21-2005 /100ml MPN 05 - <1 <1 <1 <1 <1 <1 <1 <1
HCC AS4276.3.1-2007 CFU/mL - - >3000 >3000 >3000 >3000 >3000 470 >3000 >3000
1 Aesthetic water quality criteria from the Australian Drinking Water Guidelines 6 (2011) version 3.2 (ADWG6). 2 Trigger value for 99% species protection from the Australian and New Zealand Guidelines for Fresh and Marine Water Quality, Volume 1. 3 Health water quality criteria (infant) from ADWG6, as there is no aesthetic criteria. 4 Health water quality criteria (adult) from ADWG6, as there is no aesthetic criteria. 5 Health water quality criteria (adult) from ADWG6, as there is no aesthetic criteria.
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Trends of key quarterly groundwater monitoring parameters
Figure G.1: Groundwater trends – pH
Figure G.2: Groundwater trends – EC
4.8
5
5.2
5.4
5.6
5.8
6
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
pH
Groundwater trends - pH
BH5 BH7
0
50
100
150
200
250
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Ele
ctri
cal c
on
du
ctiv
ity
(mS/
cm)
Groundwater trends - EC
BH5 BH7
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Figure G.3: Groundwater trends – TDS
Figure G.4: Groundwater trends – turbidity
Figure G.5: Groundwater trends – total suspended solids
0
10
20
30
40
50
60
70
80
90
100
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Tota
l dis
solv
ed
so
lids
(mg/
L)
Groundwater trends - TDS
BH5 BH7
0
200
400
600
800
1000
1200
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Turb
idit
y (N
TU)
Groundwater trends - turbidity
BH5 BH7
0
500
1000
1500
2000
2500
3000
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Turb
idit
y (N
TU)
Groundwater trends - TSS
BH5 BH7
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Figure G.6: Groundwater trends – biochemical oxygen demand
Figure G.7: Groundwater trends – dissolved oxygen
Figure G.8: Groundwater trends – oil in water
0
5
10
15
20
25
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
BO
D, T
OC
, CO
D (
mg/
L)
Groundwater trends - BOD
BH5 BH7
0
1
2
3
4
5
6
7
8
9
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Dis
solv
ed
oxy
gen
(m
g/L)
Groundwater trends - DO
BH5 BH7
0
20
40
60
80
100
120
140
160
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Oil
in w
ate
r (m
g/L)
Groundwater trends - oil in water
BH5 BH7
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Figure G.9: Groundwater trends – NOx
Figure G.10: Groundwater trends – Total P
Figure G.11: Groundwater trends – Total N
0
0.5
1
1.5
2
2.5
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
NO
x (m
g/L)
Groundwater trends - NOx
BH5 BH7
0
0.5
1
1.5
2
2.5
3
3.5
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Tota
l P (
mg/
L)
Groundwater trends - Total P
BH5 BH7
0
1
2
3
4
5
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Tota
l N (
mg/
L)
Groundwater trends - Total N
BH5 BH7
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Figure G.12: Groundwater trends – Ammonia
Figure G.13: Groundwater trends – E.Coli
0
0.5
1
1.5
2
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
Am
mo
nia
(m
g/L)
Groundwater trends - Ammonia
BH5 BH7
0
500
1000
1500
2000
2500
Aug 2015 Dec 2015 Apr 2016 Aug 2016 Dec 2016
E.C
oli
(pe
r 1
00
ml M
PN
)
Groundwater trends - E.Coli
BH5 BH7
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Table G.2: Results of further groundwater investigations
Report No. AU115-3286 AU115-3337
Date sampled 1 April 2016 24 May 2016
Parameter Test method Units BH5 BH5 BH7 BH7
Al ICP-MS μg/L 220 970 1100 2300
Ar ICP-MS μg/L <1 1 1 3
Ba ICP-MS μg/L 68 26 130 79
Be ICP-MS μg/L <0.5 <0.5 <0.5 <0.5
B ICP-MS μg/L 43 32 43 32
Cd ICP-MS μg/L 0.2 <0.1 0.1 <0.1
Co ICP-MS μg/L <1 <1 1 1
Cu ICP-MS μg/L 2 1 6 3
Cr ICP-MS μg/L <1 1 2 7
Fe ICP-MS μg/L 99 890 1500 4900
Hg ICP-MS μg/L <0.05 <0.05 <0.05 <0.05
Mn ICP-MS μg/L 48 16 120 71
Mo ICP-MS μg/L <1 <1 <1 <1
Pb ICP-MS μg/L <1 <1 3 6
Ni ICP-MS μg/L 2 <1 3 2
Se ICP-MS μg/L <1 <1 <1 <1
Sn ICP-MS μg/L <1 <1 <1 <1
Sr ICP-MS μg/L 5.2 1.7 14 9
Zn ICP-MS μg/L 26 19 9 3.7
TRH C6-C9 GC-MS μg/L <10 <10 <10 <10
TRH C6-C10 GC-MS μg/L <10 <10 <10 <10
TRH C6-C10 less BTEX GC-MS μg/L <10 <10 <10 <10
Benzene GC-MS μg/L <1 <1 <1 <1
Toluene GC-MS μg/L <1 <1 <1 <1
Ethylbenzene GC-MS μg/L <1 <1 <1 <1
m+p-xylene GC-MS μg/L <2 <2 <2 <2
o-xylene GC-MS μg/L <1 <1 <1 <1
napththalene GC-MS μg/L <1 <1 <1 <1
TRH C10-C14 GD-FID μg/L <50 <50 <50 <50
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Report No. AU115-3286 AU115-3337
Date sampled 1 April 2016 24 May 2016
Parameter Test method Units BH5 BH5 BH7 BH7
TRH C15-C28 GD-FID μg/L <100 <100 <100 <100
TRH C29-C36 GD-FID μg/L <100 <100 <100 <100
TRH >C10-C16 GD-FID μg/L <50 <50 <50 <50
TRH >C10-C16 less Napth GD-FID μg/L <50 <50 <50 <50
TRH >C16-C34 GD-FID μg/L <100 <100 <100 <100
TRH >C34-C40 GD-FID μg/L <100 <100 <100 <100
TPH >C16-C35 Ali GD-FID μg/L <100 <100 <100 <100
TPH >C35 Ali GD-FID μg/L <100 <100 <100 <100
TPH C16-C35 Aro GD-FID μg/L <100 <100 <100 <100
Naphthalene GC-MS μg/L <1 <1 <1 <1
Acenaphthylene GC-MS μg/L <1 <1 <1 <1
Acenaphthene GC-MS μg/L <1 <1 <1 <1
Fluorene GC-MS μg/L <1 <1 <1 <1
Phenanthrene GC-MS μg/L <1 <1 <1 <1
Anthracene GC-MS μg/L <1 <1 <1 <1
Fluoranthene GC-MS μg/L <1 <1 <1 <1
Pyrene GC-MS μg/L <1 <1 <1 <1
Benzo(a)anthracene GC-MS μg/L <1 <1 <1 <1
Chrysene GC-MS μg/L <1 <1 <1 <1
Benzo(b,j+k)fluoranthene GC-MS μg/L <2 <2 <2 <2
Benzo(a)pyrene) GC-MS μg/L <1 <1 <1 <1
Indeno(1,2,3-c,d)pyrene GC-MS μg/L <1 <1 <1 <1
Dibenzo(a,h)anthracene GC-MS μg/L <1 <1 <1 <1
Benzo(g,h,i)perylene GC-MS μg/L <1 <1 <1 <1
Indeno*1,2,3-c,d)pyrene GC-MS μg/L <1 <1 <1 <1
Dibenzo(a,h)anthracene GC-MS μg/L <1 <1 <1 <1
Benzo(g,h,i)perylene GC-MS μg/L <1 <1 <1 <1
Benzo(a)pyrene TEQ GC-MS μg/L <5 <5 <5 <5
Total +ve PAHs GC-MS μg/L NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
NIL
(+)VE
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Report No. AU115-3286 AU115-3337
Date sampled 1 April 2016 24 May 2016
Parameter Test method Units BH5 BH5 BH7 BH7
Phenol GC-MS μg/L <1 <1 - -
2-Chlorophenol GC-MS μg/L <1 <1 - -
4-Chloro-3-Methylophenol GC-MS μg/L <5 <5 - -
2-Methylphenol (O-Cresol) GC-MS μg/L <1 <1 - -
3/4-Methylphenol(m/p-
Cresol) GC-MS μg/L <2 <2 - -
2-Nitrophenol GC-MS μg/L <1 <1 - -
2,4-Dimethylphenol GC-MS μg/L <1 <1 - -
2,4-Dichlorophenol GC-MS μg/L <1 <1 - -
2,6-Dichlorophenol GC-MS μg/L <1 <1 - -
2,4,5-Trichlorophenol GC-MS μg/L <1 <1 - -
2,4,6-Trichlorophenol GC-MS μg/L <1 <1 - -
2,4-Dinitrophenol GC-MS μg/L <20 <20 - -
4-Nitrophenol GC-MS μg/L <20 <20 - -
2,3,4,6-Tetrachlorophenol GC-MS μg/L <1 <1 - -
2-methyl-4,6-
Dinitrophenol GC-MS μg/L <10 <10 - -
Pentachlorophenol GC-MS μg/L <5 <5 - -
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Twice-weekly groundwater monitoring trends
Figure G.14: Twice-weekly groundwater level
Figure G.15: Twice-weekly groundwater conductivity trends
0
2
4
6
8
10
12
14
16
14/01/2008 9/04/2009 9/07/2010 5/03/2012 9/08/2013 14/11/14 16/12/15 28/12/16
Leve
l bel
ow
gro
un
d (
m)
Time
Water table level
BH5 BH7 Benchmark level below ground
0
50
100
150
200
250
14/01/2008 9/04/2009 9/07/2010 5/03/2012 9/08/2013 14/11/14 16/12/15 28/12/16
Elec
tric
al C
on
du
ctiv
ity
(mic
roSi
emen
s/cm
)
Time
Twice-weekly groundwater conductivity
BH5 BH7 EC max limit
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Figure G.16: Twice-weekly groundwater pH trends
Note: During twice-weekly monitoring, pH is determined using litmus paper.
0
2
4
6
8
10
12
14/01/2008 9/04/2009 9/07/2010 5/03/2012 9/08/2013 14/11/14 16/12/15 28/12/16
pH
leve
l
Time
Twice-weekly groundwater pH
BH5 BH7 pH min limit pH max limit