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Liquid Meter Provers 2015 RMMS Dave Seiler Daniel Measurement & Control

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Page 1: Liquid Meter Proving

Liquid Meter Provers 2015 RMMS Dave Seiler

Daniel Measurement & Control

Page 2: Liquid Meter Proving

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

RMMS 2015

Page 2

What is Petroleum Fiscal Flow Measurement?

When ownership of petroleum is transferred from one company to another, a financial transaction occurs.

Accurate measurement of the transferred petroleum is critical to ensure an equitable exchange of money for petroleum.

Flow measurement equipment serves as the “cash register” for this exchange.

Q = $ For custody transfer

flow measurement

equals dollars

Page 3: Liquid Meter Proving

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

RMMS 2015

Page 3

Custody Transfer - Accuracy Requirements

% of Maximum Flow Rate

Maximum flow Rate = 11,400 Bbl/hr

275.5

275.0

274.5

274.0

273.5

273.0

272.5

272.0

271.5

271.0

270.5

0 20 40 60 80 100

} } }

Calibration data

Manufacturer’s specification

Legal limit

Customer’s desired accuracy

Government

W & M requirements

Page 4: Liquid Meter Proving

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

RMMS 2015

Page 4

Flow Meter Types

Variable Area

- Rotameter

Thermal

- Hot Wire Anemometer

Other

- Electromagnetic

- Vortex Shedding

- Ultrasonic- Doppler

- Ultrasonic – Transit Time

- Laser

Differential Pressure

- Orifice

- Pitot-staticTube

- Venturi

- Nozzle

- Elbow

- Wedge

- V-cone

Force

- Target

Momentum

- Turbine

- Positive Displacement

- Coriolis

- Swirl

Most commonly used

in Custody Transfer

Measurement

Page 5: Liquid Meter Proving

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

RMMS 2015

Page 5

Custody Transfer Measurement

All custody transfer measurement are contractual and usually cover…..

– measurement performance/accuracies

– frequency for measurement validation

– dispute resolution

Validation of measurement usually involves agreement into the proving method which are tied to known industry standards

– API, ISO, NIST …etc

Field (in-situ) proving most common

– establishes meter factor at working conditions

Page 6: Liquid Meter Proving

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

RMMS 2015

Page 6

Legal Approval and Standards

Organisation Internationale de Metrologie Legale (OIML) – Organization of individual country weights and measures. Issues recommendation for

legal trade worldwide. Countries follow recommendations when establishing specific regulations.

National Conference on Weights and Measures (NCWM) – Organization of individual state weights and measures officials and National Institute of

Standards and Technology (NIST) technical advisors

– National Type Evaluation Program (NTEP)

– NIST Handbook 44

International Standards Organization (ISO) – Publishes technology specific standards

American Petroleum Institute (API) – Publishes technology specific standards for Oil and Gas Industry

Page 7: Liquid Meter Proving

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

RMMS 2015

Page 7

API – Industry Standards Chapter 1 Vocabulary

Chapter 4 Proving System

Chapter 5 Sect 5 Fidelity and Security of flow measurement pulsed-data

transmission systems

Chapter 7 Temperature Determination

Chapter 8 Sect 1 Manual Sampling of Petroleum and Petroleum Products

Chapter 8 Sect 2 Automatic Sampling of Petroleum and Petroleum Products

Chapter 8 Sect 3 Mixing and Handling of Liquid samples of Petroleum and

Petroleum Products

Chapter 9 Density Determination

Chapter 11 Physical Properties Data

Chapter 12 Sect 2 Calculation of Petroleum Quantities using dynamic

measurement methods and Volume correction factors

Chapter 13 Statistical Aspects of Measurement and Samplings

Chapter 14 Sect 6 Continuous Density Measurement

Chapter 20 Sect 1 Allocation Measurement

Chapter 21 Sect 2 Electronic Liquid Volume Measurement Using PD and

Turbine Meters

Page 8: Liquid Meter Proving

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

RMMS 2015

Page 8

Meter Proving What is a Meter Proving

– Meter proving is the physical test used to determine the accuracy and performance of a liquid meter

Why is Proving performed

– The need for proving arises because operating

conditions differ significantly from the conditions under

which the meter is calibrated

Why Prove

– Establish reference point under operating conditions (initial installation)

– Accounts for changes in meter accuracy

– Verify repeatability / linearity of meter

– Contractual requirement for custody transfer

Page 9: Liquid Meter Proving

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

RMMS 2015

Page 9

Why Prove: Uncertainty versus Yearly Product Losses

Improvement in measurement accuracy of 0.10% on a 12,000 BPH (2,735 m3/h)

flow stream will result in product savings of $10,512,000 per year

Page 10: Liquid Meter Proving

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

RMMS 2015

Page 10

Meter Proving

How to Prove

– By placing a liquid meter in series with a meter prover, which has a known or base volume in such a way that all the liquid measured by the meter is also measured by the prover

Meter Prover

Page 11: Liquid Meter Proving

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

RMMS 2015

Page 11

Known Volume _______________

Indicated Volume = Meter Factor

Basic Proving Principle

Regardless of the prover or meter type, the same basic proving principle applies

Page 12: Liquid Meter Proving

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

RMMS 2015

Page 12

Operating

Conditions

When Proving. . . .

Flow Rate

Temperature

Pressure

Liquid Characteristics

– API Gravity

– Viscosity

Proving Conditions Should Match the

Operating Conditions

Proving

Conditions

Page 13: Liquid Meter Proving

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

RMMS 2015

Page 13

Measurement and Proving

F

Flowmeter

S

P DPT

PD Meter

Coriolis Meter

Turbine Meter

Liquid Ultrasonic Meter

Small Volume Prover

Standards exist that outlines best practices for the

measurement technology as well as prover type

used

API Chpt 5

covers Metering

API Chpt 4

covers Proving

Page 14: Liquid Meter Proving

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

RMMS 2015

Page 14

Earliest of Provers

Page 15: Liquid Meter Proving

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

RMMS 2015

Page 15

• Open Tank Prover • Pipe Prover (Uni or Bi-Di)

• Small Volume Prover • Master Meter Prover

Types of Provers Today

Page 16: Liquid Meter Proving

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

RMMS 2015

Page 16

Types of Proving Systems

Pipe Provers

– Bi-directional

– Uni-directional

– Piston

– Reduced volume

Small Volume Provers

Master Meter Provers

Volumetric Provers

– Volume

– Mass

Page 17: Liquid Meter Proving

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

RMMS 2015

Page 17

Gravimetric Prover

Micro

Motion

Page 18: Liquid Meter Proving

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

RMMS 2015

Page 18

(1) Prove under normal conditions

The meter must be proved under the same conditions as it

is normally expected to operate.

(2) Adequate prover capacity

The meter prover must have a capacity large enough to

provide proving runs of adequate duration.

(3) Sufficient number of runs

A sufficient number of runs must be made to establish a

valid proving.

(4) Traceable results to National Institute of Standards and

Technology

Calibration of the meter prover must be traceable to

(NIST) calibrated test measures.

Four Basic Requirements

Page 19: Liquid Meter Proving

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

RMMS 2015

Page 19

Displacement Provers

Small Volume Provers

Ball or Pipe Provers

Page 20: Liquid Meter Proving

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

RMMS 2015

Page 20

Flow from Meter

Displacer

Detectors

Calibrated length

Calibrated Volume

Pulses from Meter

START

STOP

Prover

Computer

Meter Proving by Displacement

Page 21: Liquid Meter Proving

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

RMMS 2015

Page 21

Pressure Gage and

Vent Connections

Bi-Directional Prover

Page 22: Liquid Meter Proving

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

RMMS 2015

Page 22

Bi-Directional Prover

Page 23: Liquid Meter Proving

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

RMMS 2015

Page 23

Double Folded

Skid Package

Single U-bend

Page 24: Liquid Meter Proving

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

RMMS 2015

Page 24

Proving Provisions

Take-off / Block

Valves

Double Block &

Bleed Valve

Page 25: Liquid Meter Proving

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

RMMS 2015

Page 25

Conventional Pulse Counting Discrimination

Start count Stop Count

1 2 3 4 5 6 7 8

1 2 3 4 5 6 7

1 2 3 4 5 6 7 8

Actual 7.255 Pulses

A

B

C

Page 26: Liquid Meter Proving

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

RMMS 2015

Page 26

Length Between Detectors For Uncertainty ± 0.01%, at Least 10,000 Pulse

Should Be Collected During the Proving Pass

For Repeatability 0.02%, Calibrated Length Is Dependent on Detector Switch Resolution (rd)

Max. Possible Difference in Length for Round Trip is 4rd

( ) For 0.02% Repeatability L = 4rd 0.0002

= 20,000rd

If rd = 1/32” Then L = 4 x 0.031 = 52 Ft.

.0002 x 12

L + 2rd ( ) L + 2rd - = 4rd

L + 2rd

L - 2rd rd rd rd rd

L DT DT

Page 27: Liquid Meter Proving

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

RMMS 2015

Page 27

Mechanical Detectors

Page 28: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 28

RMMS 2015

Page 28

Tc-c 1

2 2 RP = + sec x Sphere Speed ( )

Example:

Motor Operator Tc-c = 5.4 second

Sphere Speed = 4.97 fps

RP = + x 4.97 = 15.9 ft. 5.4 1

2 2 ( )

Length of Pre-Run (RP)

Page 29: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 29

RMMS 2015

Page 29

Prover Volume (30 ft)

Prover Volume Pre-Run

Calibrated Volume to allow 10,000 Pulses

Distance Between

Detectors

Page 30: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 30

RMMS 2015

Page 30

Max. V = 5 fps for Bi-Di

10 fps for Uni-Di BPH x 0.286

(I.D.(in))2

Min. Velocity 0.5 fps

Example:

Max. Flow Rate = 2,500 BPH

Pipe Diameter = 12” (12” Sched. 40)

Max. V = = 4.97 fps 2,500 x 0.286

(12)2

Displacer Velocity

Page 31: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 31

RMMS 2015

Page 31

Uni-Directional Prover

Page 32: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 32

RMMS 2015

Page 32

Small Volume Provers API Definition:

Old definition: A Small Volume Prover (SVP); is a prover that will collect less than 10,000 meter pulses in a prover pass.

Page 33: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 33

RMMS 2015

Page 33 Small Volume Prover??

Page 34: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 34

RMMS 2015

Page 34

Small Volume Provers API Definition:

Old definition: A Small Volume Prover (SVP); is a prover that will collect less than 10,000 meter pulses in a prover pass.

The new API Chapter 4.2 refers to a SVP as “unidirectional piston pipe provers with external optical switches.”

Reason: 10,000 pulse per pass is to generate the mathematical precision necessary to calculate a four decimal place meter factor accurately

Page 35: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 35

RMMS 2015

Page 35

Compact Prover

Better than 1,000 : 1 Turndown

Small size / Light weight

Utilizes precision optical detectors

Pulse interpolation reduces pulse collection

Volumetric and/or Mass proving

Page 36: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 36

RMMS 2015

Page 36

Size Comparison – ball vs. compact

Page 37: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 37

RMMS 2015

Page 37

Small Volume Prover or Compact Prover

Pneumatic

Page 38: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 38

RMMS 2015

Page 38

What Made Small volume provers possible?

Precision optical volume detection switches

The double chronometry pulse interpolation

technique

The advent of modern computers and precision

timing techniques

Modern computers ability to average multiple

pass prover runs to statistically attain meter

pulses per run

Page 39: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 39

RMMS 2015

Page 39

Mechanical vs. Optical Detectors

Page 40: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 40

RMMS 2015

Page 40

Compact Prover Detector Switches

•A “flag” attached to a detector shaft actuates switches by interrupting a thin beam of light

•Switches are positioned by two Invar rods which have an extremely low coefficient of thermal expansion

•Greatly Reduces effects of temperature changes on the volume

Page 41: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 41

RMMS 2015

Page 41

Flow Tube

– 17-4 ph stainless steel

– 304 stainless steel

– Carbon steel

Teflon Seals

Materials of Construction

Piston / Poppet Valve

300 series sst

Viton, Kalrez, or

Nitrile poppet valve

O ring

Rulon Rider Rings

Compatible with most hydrocarbon applications

Page 42: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 42

RMMS 2015

Page 42

– Internal poppet - designed so that flow is never stopped

– soft o-ring seated to prevent product leakage and ensure accurate calibration

– Note dual piston rings with dual Rulon Ryders which wipe fhe

flow tube clean during piston retraction

Main Piston Assembly

Page 43: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 43

RMMS 2015

Page 43

Proving Mode: Start Position

Page 44: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 44

RMMS 2015

Page 44

Proving Mode: Start Pulse Collection

Page 45: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 45

RMMS 2015

Page 45

Proving Mode: End of Pass (Stop Pulse Collection)

Page 46: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 46

RMMS 2015

Page 46

Conventional Pulse Counting Discrimination

Start count Stop Count

1 2 3 4 5 6 7 8

1 2 3 4 5 6 7

1 2 3 4 5 6 7 8

Actual 7.255 Pulses

A

B

C

Page 47: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 47

RMMS 2015

Page 47

Pulse Interpolation

Definition

– Process of determining some value between two known values through the use of a procedure or algorithm.

Uncertainty requirement

– +/- 0.01% or 1 part in 10,000

• must be able to distinguish time to at least 0.00001 of a second

Methodology

– Double Chronometry

Page 48: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 48

RMMS 2015

Page 48

K=Meter Factor

A=Time required to displace Volume D

B=Time required to accumulate whole flowmeter pulses, Count C

C=Whole flowmeter pulses counted during Time B

D=Calibrated volume of the prover flow tube between detectors

)(

)(

)(

)(

sesTimeforPulB

PulsesC

VolumeD

TimeAK

Double Chronometry

A

Interpolated meter pulses = C X B

Page 49: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 49

RMMS 2015

Page 49

Double Chronometry Example

K= A (TIME) C (PULSES)

D (VOLUME) B (TIME FOR PULSES) X

A = Time for known displaced volume

in seconds

B = Time for whole meter pulses

C = Accumulated whole meter pulses

D = Known displace volume (by water

draw certificate)

0 0 0 .5 8 3 7 7

0 0 0 .5 8 3 2 9

0 0 0 0 0 3 6 4

14.99988 Gal (.35714 Bbl)

Time Counter 5 Mhz

Time Counter 5 Mhz

Pulse Counter (from meter)

K = 0.58377 364

X 0.35714 BBL 0.58329

1020.0468 pulses / bbl

Interpolated Meter Pulses = 364 X 0.58377

0.58329

Interpolated Meter Pulses = 364.2995

Page 50: Liquid Meter Proving
Page 51: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 51

RMMS 2015

Page 51

Setup Configuration for Calibration

Page 52: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 52

RMMS 2015

Page 52

Waterdraw Diverter Valve System

Page 53: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 53

RMMS 2015

Page 53

Calibration of Coriolis Meters

Compact

Prover

Test

Meter

Prover

Computer

Flow Direction Block and Bleed Valve

Connection Valves

Prove like any volumetric flowmeter

Page 54: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 54

RMMS 2015

Page 54

Prover Volume Conversion to Mass Prover

Flow Direction

P

T

Density determined from

densitometer

Page 55: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 55

RMMS 2015

Page 55

Master Meter Proving

Flow Direction

Page 56: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 56

RMMS 2015

Page 56

Transit Time Liquid USM – How it works?

Transducer locations placed for optimum measurement accuracy

Transducers act alternately as transmitter and receiver

Downstream pulses traverse stream more quickly than upstream pulses

AVQ average

where

averageV = mean velocity of the fluid in the pipe

Q = flow rate

A = area of the pipe

n

iiaverage vwV1

For multipath Liquid USM

Multipath Liquid USM

Page 57: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 57

RMMS 2015

Page 57

How do we Prove Liquid Ultrasonic

Meters

Page 58: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 58

RMMS 2015

Page 58

Earliest of Provers

Page 59: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 59

RMMS 2015

Page 59

Proving Liquid Ultrasonic Meters

Turbine Meter – Sees all of the flow

– Local turbulence is averaged by the rotor

– The rotor can turn at only one rate

– Little data scatter due to inherent inertia of the measurement element

– Uniform pulse train

Ultrasonic Meter – Samples the flow at mutiple

chord locations

– Local turbulence is averaged by many samples

– Short term repeatability is a function of turbulence

– Data scatter due to ability to measure minute variations in velocity ie: turbulence

– Non-uniform pulse train

Differences exist in flow dynamics between

Turbine and Ultrasonic technology

Page 60: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 60

RMMS 2015

Page 60

Proving Liquid Ultrasonic Meters Coriolis and Liquid Ultrasonic Meters are

“manufactured pulse” type meters

There are two factors which can affect proving results.

– Proving accuracy can be affected by any delay in

pulses due to processing speed of the transmitter

– Ultrasonic meters produce a non-uniform pulse

output and has a varying frequency. This can cause

difficulty in obtaining acceptable repeatability while

proving

Proving run repeatability is used as an indication of

whether the proving results are valid

Proving run repeatability may not fall within the typical

5 run, 0.05% span of repeatability, however proving

runs shall repeat within the API Ch 4.8 guideline

Uniform pulse output – Turbine meter

Frequency normally very constant

Non-uniform pulse output – Ultrasonic meter

Frequency variation due to ability to measure

minute variations in velocity

Page 61: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 61

RMMS 2015

Page 61

API Guideline to Proving Runs

API Chapter 5.8, Table

B-1 recognizes that an

increase in proving runs

may be needed in order

to achieve a ±0.027%

uncertainty of meter

factor

Table B-1 – Proving an Ultrasonic Flow Meter

+/- 0.027% 0.22% 20

+/- 0.027% 0.21% 19

+/- 0.027% 0.20% 18

+/- 0.027% 0.19% 17

+/- 0.027% 0.18% 16

+/- 0.027% 0.17% 15

+/- 0.027% 0.16% 14

+/- 0.027% 0.15% 13

+/- 0.027% 0.14% 12

+/- 0.027% 0.13% 11

+/- 0.027% 0.12% 10

+/- 0.027% 0.10% 9

+/- 0.027% 0.09% 8

+/- 0.027% 0.08% 7

+/- 0.027% 0.06% 6

+/- 0.027% 0.05% 5

+/- 0.027% 0.03% 4

+/- 0.027% 0.02% 3

Uncertainty Repeatability * Runs

Low Counts) X 100 Counts – Low Counts) /

Repeatability = ((High

* per API MPMS Ch. 5.8, Table A-1 to achieve +/- 0.027%

uncertainty of meter factor.

Page 62: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 62

RMMS 2015

Page 62

Proving Volume is Important

The number of pulses

generated during a prove is

not the issue

The proving volume is

important in order to achieve

a successful prove on a LUSM

The critical issue is the

volume, not the prover

Use Master Meter – Prover

combination or a prover with

sufficient volume

5 Runs

0.05%

8 Runs

0.09%

10 Runs

0.12%

Meter Size (in.)

4 33 15 10

6 73 34 22

8 130 60 40

10 203 94 62

12 293 135 89

14 399 184 121

16 521 241 158

Prover Volume vs. Meter Size

Prover Size (bbl)

Table B-2 – Suggested Prover Volume to obtain

+/- 0.027% Uncertainty of Meter Factor

From API Chapter 5.8 2005 edition

Removed from 2011 edition

Page 63: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 63

RMMS 2015

Page 63 48” 600# Meter Prover for Crude Oil Service

Page 64: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 64

RMMS 2015

Page 64

Proving Manufactured Pulse Meters Master Meter – Prover Method

In-situ prover – master meter combination is accepted and recognized as a valid method to prove Liquid Ultrasonic Meters

– Small volume Prover or Ball Prover used in combination with a master meter

– Master Meter is calibrated against prover in-situ under

actual operating conditions

Master Meter proving is recognized by API and described in

the standard API MPMS Chapter 4.5

This methodology allows for longer proving cycle to improve meter repeatability

Eliminates uncertainties due to laboratory calibration of

master meter on different fluids at different operating

conditions

Page 65: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 65

RMMS 2015

Page 65

Small Volume Prover Configured to prove Coriolis or Ultrasonic Meters Densitometer and Master

Turbine Meter incorporated to prove Ultrasonic and Coriolis meters

Prover proves the master meter which proves the pipeline meters

Page 66: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 66

RMMS 2015

Page 66

Master Meter Proving Using Small Volume Prover

24” high temperature Small Volume Prover configured to prove Liquid Ultrasonic Meters (6” to 10”) on crude oil pipeline in Canada

10” Multi-Viscosity Turbine Meter as master meter

Page 67: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 67

RMMS 2015

Page 67

34” SVP w/master meter proving liquid USM

Page 68: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 68

RMMS 2015

Page 68

Small Volume Provers

Do not require 10,000 meter pulses per prover pass

Great fluid compatibility

Low pressure drop

Faster meter proving

Less product loss during proving operation, flush from one product to another

Requires less space ( less real estate )

Lower transportation cost for portable provers

Field Replaceable volume switches

High accuracy waterdraw calibration

Page 69: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 69

RMMS 2015

Page 69

In Situ Proving – Cryogenic Prover

Concepts evolved from bi-directional piston provers

Free floating piston

Honed prover barrel

Piston prover well established and commonly used on liquids operating at -45 DC

Meet API repeatability criteria

Special design details applied for LNG for operation at approximately -260⁰F (-162 ⁰C)

Page 70: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 70

RMMS 2015

Page 70

Fully insulated for LNG Service

Page 71: Liquid Meter Proving

[File Name or Event] Emerson Confidential 27-Jun-01, Slide 71

RMMS 2015

Page 71

Although Displacement Provers operate on the same basic concept, a prover is a complex piece of equipment and may have widely differing arrangement and operating features.

Each application for a prover should be studied carefully so that optimum choices can be made for equipment, installation and operation

Proving methodolgy must be carefully considered and agreed upon by all parties when using Manufactured Pulse type meters.

Summary

Page 72: Liquid Meter Proving

Liquid Meter Provers 2015 RMMS Dave Seiler

Daniel Measurement & Control