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[File Name or Event] Emerson Confidential 27-Jun-01, Slide 1

Title: Challenges in Characterizing Flowmeter Dynamic Response

Mass Flow is directly proportional to

Delta T (Pickoff Signal Phase Shift)

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1 7 13 19 25 31 37 43 49 55 61 67 73 79 85Mass Flow

6 7

Coriolis Mass Flow Metering

In this Presentation I will

Discuss Industrial Applications

for High Speed Flow Metering

Chuck Gray, Micro Motion

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 2

Chuck Gray Application & Test Engineer - Micro Motion Inc

Micro Motion Technology • Product support

• EMC

• Flow Measurement Test

• “High End” Customer Support

• 23 Years Experience

Retired Naval Flight Officer

• Patrol Aviation & Naval Air Test

BSEE – University of Colorado

• Electrical Power & Control Systems

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 3

High Speed Applications

Pipeline Provers

High Speed Filling

Numerous Other Specialized Applications

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 4

Response to Flow Change

Response Time is the Time between a Physical Change & a Corresponding Change in an Output Signal

Coriolis meters exhibit a two-part response curve for changes in measured flow

– a fixed processing delay - Latency

• a function of the system architecture

– second part of the response curve approximates an RC delay - Damping

• Typically adjustable by the user

• Rise Time

• Settling Time

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 5

Definitions

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1.40

23.500 24.500 25.500 26.500 27.500 28.500

No

rmali

zed

Flo

w

Time (Seconds)

Response Time; Old vs Improved Technology Rise Time

Latency

Settling Time

Actual Flow

Improved Response Flow

Signal

Flow Signal

95%

63 %

Other Considerations Update Rate

Reference Conditions

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 6

Coriolis Meter Geometry These are dual tube meters

Common Coriolis Geometries

MMI CMF100 1”

MMI CMF400 4”

E&H F83 1”

Straight Tube Meter

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 7

Theory of Operations – Mass Flow

Mass Flow is directly proportional to Delta

T (Pickoff Signal Phase Shift)

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 8

MMI DSP – No Lost Flow data

-1.5

-1

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0

0.5

1

1.5

123

45

67

89

11

113

315

517

719

922

124

326

528

730

933

135

337

539

741

944

146

348

550

752

955

1

Shifted

Reference

T

Frequency (Hz) = 1/T (sec)

2π radians

MMI DSP Transmitters Convert the Pickoff

Signal at a 48 Khz Rate

~80 to 250 samples

per ½ cycle

In Analog

Transmitters Flow

is Computed every

½ cycle (only)

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 9

Measured Meter Response to Valve Closure

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1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30

Mass F

low

Lb

s./M

in.

Time in 10's of Milliseconds

63

44 MSec 40 MSec

85 MSec

95

Latency

63% (1 Tc) Response

An Older, Production Meter

set for 0.04 Damping

Analog Flow Signal

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 10

Use Appropriate Flow Damping (filtering)

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15

523

230

938

646

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061

769

477

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892

510

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10

79

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56

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33

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10

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41

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49

19

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Steady Flow - 700/2700- Special mode 0.04 Damping

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7

Steady Flow 700/2700 - Special mode 0.64 damping

This Flow Signal Would be

Severely Aliased with a Slow

Sampling Control System

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 11

Meter Zero & Calibration S

ca

le

Meter

Zero Error Changes the Offset

Flow Calibration Changes the Slope

Fill Target

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 12

Micro Motion MVD Technology

Multi- Stage DSP

– “immediate “ conversion to digital data for stability

– Versatile

• Very fast response with moderate filtering

– OR

• Slower response with extensive filtering

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 13

Why are Response Characteristics Important? Matching the Meter to the Application

Pipelines

– Small Volume Provers

Chemical Plants & Refineries – Fast Control Loops

Special Applications

– Automotive RDT&E

Food & Beverage

– Filling

• Short Fills

• Dosing

• Specialty

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 14

Filling Machines

Bag in Box

Rotary – PSA w/1500F

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 15

Heavily Aerated Liquid Laundry Detergent at the

product feed supply to Filling Pressure Tank.

H 050 Sensor with Precision Filling Valve

Sample from

Pressure Tap

Accuracy

995

996

997

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1000

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1003

1004

1005

1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39

-0.2

-0.1

0

0.1

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0.5

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0.7

Fill_Value

Scale

% Accuracy

% Fill accuracy

H 50 Performance on

Aerated Detergent

Fill = 1000 Grams; Fill Time ~ 3.78 Sec Flow ~ 264 G/Sec.

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 16

FMT Performance – Better Std Dev!

Meter Rate

G/Sec.

Fill

Target

Grams

Fill Time

Sec.

Average Fill

Grams

Fill

Standard

Deviation*

.5” 250 1250 4.87 1249.94 0.06%

.5” 125 250 1.99 250.37 0.15%

.5” 62.5 47 0.74 47.02 0.18%

.15” 100 50 0.52 50.02 0.12%

.15” 50 37.5 0.69 37.55 0.18%

.15”

10 5 0.49 5.01 0.33%

* Fill Standard Deviation was calculated using 30 points. Test

data demonstrates performance of the complete fill system.

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 17

Filler OEM: Results with Micro Motion Coriolis

Higher Efficiency and Reliability – 10,000 cases per shift vs. 8,000 with older, less reliable filling technology

Greater Accuracy = Less Giveaway: Product savings alone can pay for a machine in 2 to 5 years.

Faster changeover/cleaning = More flexibility and shorter runs. Less inventory and greater uptime!

Additional measurables provide new features such as density & temperature tracking for quality control.

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 18

3950

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3990

4000

4010

4020

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4040

4050

Avg

. W

eig

ht

(gra

ms

)

Old Filling Technology Machine

Filled Container

Samples New Filling Machine with MMI

Coriolis Filling Technology

Target Fill 3990 Grams

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 19

Flow Meter Fill Standard Deviation vs Flow Rate – Several Fill Times

10:1 Turndown 2:1 Turndown

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 20

Pipeline Proving

Volumetric Flow Meter References

– Useful when Flow Can’t be Interupted

Large Volume – “Ball” Provers

– Long Run Times

• Measurement Phase Difference Generally not Problematic

Small Volume – “Piston” Provers

– Short Run Times

• Measurement Phase Difference may Cause Significant Error

• Well Documented by others.

– Takashi Shimada, et all (National Metrology Institute of Japan)

– Micro Motion Proving Manual, (Cathy Apple)

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 21

Daniel Ball Prover

The time is measured as the ball traverses the pipe between two detectors

The ball is launched & recovered here

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 22

Daniels Compact Prover

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 23

Daniel Small Volume Prover

Outlet

Inlet

Valve Actuation Cause flow

rate change

Pre-Run Time Run Time

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 24

Flow Change with Prover “Launch”

Analog RFT 9739 Data

Micro Motion

Proving Manual

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 25

Erratic Product Delivery

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7

Mass Flow_4

Mass Flow_4

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 26

THANK YOU !

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