Micro Motion Manual: Oil and Gas Production Applications-PVR, TBR, TMR | Micro Motion Manuals & Guides

Supplement
MMI-20026578, Rev AD
January 2022
Micro Motion™ Multiphase Applications
Production Volume Reconciliation (PVR) | Transient Bubble Remediation (TBR) | Transient Mist Remediation (TMR)
Safety messages are provided throughout this manual to protect personnel and equipment. Read each safety message carefully before proceeding to the next step.
Safety and approval information
This Micro Motion product complies with all applicable European directives when properly installed in accordance with the instructions in this manual. Refer to the EU declaration of conformity for directives that apply to this product. The following are available: the EU declaration of conformity, with all applicable European directives, and the complete ATEX Installation Drawings and Instructions. In addition the IECEx Installation Instructions for installations outside of the European Union and the CSA Installation Instructions for installations in North America are available on the internet at www.emerson.com or through your local Micro Motion support center.
Information affixed to equipment that complies with the Pressure Equipment Directive, can be found on the internet at
www.emerson.com. For hazardous installations in Europe, refer to standard EN 60079-14 if national standards do not apply.
Other information
Full product specifications can be found in the product data sheet. Troubleshooting information can be found in the configuration manual. Product data sheets and manuals are available from the Micro Motion web site at www.emerson.com.
Return policy
Follow Micro Motion procedures when returning equipment. These procedures ensure legal compliance with government transportation agencies and help provide a safe working environment for Micro Motion employees. Micro Motion will not accept your returned equipment if you fail to follow Micro Motion procedures.
Return procedures and forms are available on our web support site at www.emerson.com, or by phoning the Micro Motion Customer Service department.
Emerson Flow customer service
Email:
Worldwide: flow.support@emerson.com
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Telephone:
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2
Supplement Contents
MMI-20026578 January 2022

Contents

Chapter 1 Before you begin........................................................................................................5
1.1 About this application manual..................................................................................................... 5
1.2 ProLink III requirements............................................................................................................... 5
1.3 Ordering options......................................................................................................................... 6
1.4 Additional documentation from Micro Motion ............................................................................6
1.5 Terms and definitions.................................................................................................................. 7
1.6 PVR, TBR, and TMR applications...................................................................................................8
Chapter 2 Production Volume Reconciliation (PVR).................................................................. 11
2.1 Understanding the PVR application............................................................................................11
2.2 Density determination...............................................................................................................14
2.3 Configure Production Volume Reconciliation (PVR) using ProLink III ......................................... 18
Chapter 3 Transient Bubble Remediation (TBR)........................................................................ 21
3.1 Understanding the TBR application............................................................................................21
3.2 Configure Transient Bubble Remediation (TBR) using ProLink III ................................................23
Chapter 4 Transient Mist Remediation (TMR)........................................................................... 25
4.1 Understanding the TMR application...........................................................................................25
4.2 Configure Transient Mist Remediation (TMR) using ProLink III ...................................................27
Chapter 5 Display variables...................................................................................................... 29
5.1 Display variables available with PVR, TBR, and TMR....................................................................29
Appendix A Application parameters and data............................................................................. 31
A.1 PVR parameters and data.......................................................................................................... 31
A.2 TBR parameters and data...........................................................................................................37
A.3 TMR parameters and data..........................................................................................................38
Appendix B Best practices for two-phase measurement performance......................................... 41
B.1 Entrained gas performance........................................................................................................41
B.2 Entrained liquid (mist) performance.......................................................................................... 42
B.3 Density determination...............................................................................................................44
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4 Micro Motion Multiphase Applications
Supplement Before you begin
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1 Before you begin

1.1 About this application manual

This application manual explains how to configure the Production Volume Reconciliation application (PVR), the Transient Bubble Remediation application (TBR), and the Transient Mist Remediation application (TMR), using ProLink III.
These three applications are available for Micro Motion MVD™ Coriolis meters in an MVD Direct Connect installation.
PVR, TMR, and TBR are also available for Micro Motion Model 1500, Model 1700, Model 2500, and Model 2700 transmitters.
This application manual does not provide information on installation of any sensors or transmitters, or on general configuration. This information can be found in the applicable sensor installation manual, transmitter installation manual, or transmitter configuration manual.
Related information
Additional documentation from Micro Motion

1.2 ProLink III requirements

To use this manual, you must have ProLink III Professional v4.0 or later, and you must be able to connect from ProLink III to the transmitter or core processor.
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1.3 Ordering options

For 800 core processor direct connect installations, PVR, TBR, and TMR are available as Engineering To Order (ETO) applications. PVR and TMR are available individually or in combination with Smart Meter Verification.
PVR, TMR, and TBR features are now available in the standard product when ordered on 1500, 1700, and 2500 Transmitter Models. The ETO is not required on the 800 core processor when used with a transmitter.
To order one of these applications, an ETO must be purchased for the core processor (see
Table 1-1). This ETO enables use of the application in an MVD™ Direct Connect installation.
Table 1-1: Core processor ETOs for PVR, TBR, and TMR
Application Direct connect
core processor
PVR Enhanced 22166 22701 Mixture of oil and
TBR Enhanced 13386 25699 Liquid with gas Liquid flow rate and
Standard 12806 Not available. Liquid with gas Liquid flow rate and
TMR Enhanced 18922 22706 Gas with entrained
Individual application
ETO number Process fluid Desired
Application with Smart Meter Verification (SMV)
water
liquid (mist)
measurement
Net oil (dry oil at reference conditions) and net water flow
totals
totals
Gas flow rate and totals
Restriction
Only one ETO can be installed in the transmitter or core processor at a time.

1.4 Additional documentation from Micro Motion

Table 1-2: Additional documentation for PVR, TBR, and TMR installations
Document Use
Micro Motion® MVD™ Direct Connect Meters: Installation Manual
Sensor installation manual for your sensor Installation and wiring for the sensor
Configuration manual for your transmitter Configuration, operation, maintenance, and
ProLink III User Manual
Modbus Interface Tool
6 Micro Motion Multiphase Applications
Installation and wiring for the MVD Direct Connect flowmeter
troubleshooting for features that are not related to PVR, TBR, or TMR
Installation and use of ProLink III
Programming the Modbus host
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1.5 Terms and definitions

The terms used to describe Multiphase applications vary widely. This manual, and the PVR, TBR, and TMR applications, use the terms defined here.
Terms used in PVR, TBR, and TMR
at Reference
At Line
At Reference density
At Line volume
At Reference volume
Mixture
Water cut
Entrained, entrainment
Remediation
Shrinkage
The process of calculating the value of a process variable at reference temperature, starting from the value of the process variable at line temperature (the measured value)
The density of the process fluid at line temperature
The density of the process fluid at reference temperature (60 °F) that is equivalent to its density at line temperature
The volume of the process fluid at line temperature
The volume of the process fluid at reference temperature (60 °F) that is equivalent to its volume at line temperature
The process fluid before separation, such as a combination of oil and water, or gas, oil, and water
The volume fraction of water in the liquid mixture, in %
The presence of small amounts of gas in a liquid stream, or liquid in a gas stream
An adjustment applied to a process variable during periods of entrained gas or mist when a substitute density value has been used for volume calculation (PVR and TBR) or the flow rate has been increased or decreased to compensate for unmeasured flow (TMR).
The change in liquid volume between the measurement point and a stock tank due to lighter hydrocarbons evaporating. This is caused by the stock tank being at a lower pressure, further below the bubble point of the oil. The shrinkage factor is a user-input factor, based on a PVT (pressure-volume-temperature) test of the oil.
Shrinkage Meter Factor
These terms can be combined in several ways to describe different process variables. The following table provides several examples, but is not a complete list of possibilities.
Table 1-3: Examples of process variable names
Process variable name Description
Volume Total (unremediated) The total, by volume, of the mixture (oil/water/gas combination),
Volume Total (remediated) The total, by volume, of the oil/water minus the volume
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Used just like the normal Meter Factor, when proving the meter against liquid measurement at stock tank conditions.
as measured
attributable to gas
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Table 1-3: Examples of process variable names (continued)
Process variable name Description
Oil Total at Line The total amount of oil measured since the last totalizer reset, at
line temperature, with no adjustment for temperature variation
Water Cut at Reference The percentage of water in the oil, as if the measurement had
been taken at 60 °F
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1.6 PVR, TBR, and TMR applications

PVR, TBR, and TMR are applications designed to provide more accurate process data in the presence of multiple phases. For example, if bubbles are present in the process fluid, or the process fluid is flashing, the volume measurements are often incorrect.
Production Volume Reconciliation (PVR)
Provides oil and water volumes through density-based calculations for both line and
reference conditions
Detects bubble entrainment or flashing in the sensor, and can correct volumes
accordingly
Best for undersized three-phase separators that frequently have intermittent gas or
water contamination in the oil leg
Offers a simple, low-cost solution for net oil and net water measurement for two-phase
separators
Transient Bubble Remediation (TBR)
Used with single-component liquid streams that may experience intermittent low
levels of gas entrainment, that is, gas carryunder
Enables accurate measurement of a single fluid during periods of entrained gas by
providing a substitute density value based on the immediately preceding process density (standard configuration)
Tracks total time of aerated flow to assist in diagnosing process issues that may cause
aeration
Transient Mist Remediation (TMR)
Used with gas streams that may experience intermittent low levels of liquid
entrainment, i.e., liquid carry-over
Allows gas measurement to continue during periods of entrained liquid (mist) by
providing a substitute flow rate value based on the immediately preceding process flow rate
Returns to reporting the measured flow rate when the mist interval is over, increased
or decreased by a maximum of 10%, until flow totals are appropriately adjusted for the unmeasured flow
Provides an indication of the amount of time that liquid was present in the stream —
identifying process improvements to reduce gas stream contamination
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1.6.1 Illustrations of PVR, TBR, and TMR installations

PVR, TBR, and TMR can be used with two-phase separators and three-phase separators.
Note
These illustrations do not show all possible combinations.
Figure 1-1: PVR, TBR, or TMR with two-phase separator
A. From wellhead B. Separator C. Gas leg
D. Oil/water leg
E. Coriolis sensor with PVR or TBR F. Coriolis sensor with TMR
G. Modbus host (flow computer)
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Figure 1-2: PVR, TBR, or TMR with three-phase separator
A. From wellhead B. Separator C. Water leg
D. Oil leg
E. Gas leg F. Coriolis sensor with PVR or TBR
G. Coriolis sensor with PVR (optional, used in applications where oil measurement is needed in the water leg to
detect a malfunctioning separator)
H. Coriolis sensor with TMR
I. Modbus host (flow computer)
10 Micro Motion Multiphase Applications
A
B
C
t
ρ
D

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2 Production Volume Reconciliation
(PVR)

2.1 Understanding the PVR application

PVR is used in oil and gas separation applications to compensate for gas and/or water contamination in the oil leg of a three-phase separator. It is also used to quantify the oil and water volumes in the liquid leg of a two-phase separator.
PVR uses the meter's drive gain to indicate if there is entrained gas or transient bubbles in the liquid stream, and adjust the measurement accordingly. Under normal circumstances, i.e., no entrained gas or bubbles, the application uses the Net Oil Computer (NOC) algorithm to calculate and quantify the volumes of oil and water in the liquid stream.
Net Oil Computer (NOC)
The Net Oil Computer algorithm calculates the water fraction of the liquid stream so that the amount of oil and the amount of water can be determined. The algorithm measures the volume of oil, corrected to a reference temperature, that is contained within the gross volume of produced fluid.
Compensating for gas in the liquid
Entrained gas, or bubbles in the process fluid, has a negative effect on liquid volume measurement accuracy. The Coriolis sensor calculates volume based on direct density and mass measurements. When a bubble is present, mixture density is reduced, causing the reported volume to be higher than the actual liquid volume. The presence of bubbles is reflected in the drive gain. The following figure shows how the change in drive gain affects density measurement.
Figure 2-1: Effect of transient bubbles on drive gain and density measurement
A. Density
B. Drive gain (actual) C. Transient bubble condition D. Drive gain (%)
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A transient bubble condition is defined in terms of the sensor's drive gain: If the drive gain exceeds the configured threshold for more than a specified interval, the selected PVR action is performed. The transient bubble interval persists until drive gain is below the configured threshold for the specified interval.
PVR volume calculation during bubble events
If the drive gain threshold is exceeded, the volume calculation for the period of high drive gain can be handled in one of three ways.
Option Description
Hold Last Value
Use Input Density of Dry Oil Converted to Line Conditions
Alert Only
Use an average density value from an earlier point in the process to calculate volume. If this option is chosen, the water cut from the point just before the bubble event is effectively held constant throughout the bubble event.
Convert the density of dry oil at reference temperature (a user­configured value) to density at line temperature, and calculate volume. This option assumes that all volume during the bubble event is dry oil.
Post an alert.
12 Micro Motion Multiphase Applications
C
B
E
A
F
D D
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Processing for Hold Last Value
This option directs the application to retrieve measured density data from an earlier point in the process. The earlier point is identified by the configured PVR Lookback Period. The density values around this point are averaged, and this average is then used in oil calculations.
The following figure shows the substitution of average density data during the transient bubble interval.
Figure 2-2: Hold Last Value in operation
A. Density
B. PVR Drive Gain Threshold C. Drive gain (actual) D. PVR Lookback Period
E. Averaged density values
F. Drive gain (%)
Note
If the point defined by PVR Lookback Period happens to fall into a previous transient bubble interval, the application automatically extends the lookback interval as required so that the average is calculated from measured density data rather than substituted density values. In the illustration, the first average is applied to several transient bubble events.
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2.2 Density determination

To configure Production Volume Reconciliation (PVR), you must know the density of dry oil at reference temperature, and the density of produced water at reference temperature.
Related information
Density determination using the data log from ProLink III Density determination using a petroleum laboratory

2.2.1 Density determination using the data log from ProLink III

To configure Production Volume Reconciliation (PVR), you must know the density of dry oil at reference temperature, and the density of produced water at reference temperature. You can use log data from ProLink III, with the Oil & Water Density Calculator, to obtain these values.
Note
Even after separation, oil typically contains some amount of interstitial water. The water cut may be as high as 1% to 3%. For purposes of this application, this is considered dry oil.
This procedure assumes the following:
The highest density value in the logged data represents produced water.
The lowest density value in the logged data represents dry oil.
Prerequisites
You must be able to connect to the transmitter or core processor with ProLink III.
You must know how to use the data logging feature in ProLink III.
You must be able to run data logging for the necessary time period, which may be a few minutes or a few hours, depending on your separator.
You must have the Oil & Water Density Calculator. This is a spreadsheet tool developed by Micro Motion. You can obtain a copy from your Micro Motion representative.
Procedure
1. Connect to the core processor or transmitter with ProLink III.
For two-phase separators, connect to the core processor or transmitter on the
oil/water leg. See Figure 1-1.
For three-phase separators, connect to the core processor or transmitter on the
oil leg. See Figure 1-2.
2. Set up data logging to record the following process variables, with a logging interval of 1 second:
Mass flow rate
Volume flow rate
Density
Temperature
14 Micro Motion Multiphase Applications
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Drive gain
3. Collect data.
a) Open the level control valve on the separator, and allow the separator to
drop to the lowest safe level, or until gas is first drawn into the liquid leg.
b) Close the level control valve and allow the level to rise to the maximum safe
level.
This will increase the residence time for the liquid in the separator, and may allow the water to settle to the bottom and the oil to rise to the top.
c) Open the level control valve partially, so that the level drops slowly.
d) Start data logging.
e) Allow the separator to drop to the lowest safe level, or until gas is first drawn
into the liquid leg.
f) Stop data logging.
g) Return the separator to automatic level control.
4. Obtain maximum and minimum density data from the log.
Shortly after the control valve is opened or the dump phase begins, you should see the temperature stabilizing and the density rising to a maximum value and stabilizing. This may represent produced water. Just before the lowest safe level, or before the point where gas is drawn into the liquid leg, you should see the density falling to a minimum value and stabilizing. This may represent dry oil.
a) Record the maximum density and the corresponding temperature.
b) Record the minimum density and the corresponding temperature.
Important
Never use an unstable density value, or any density value that has an elevated drive gain.
5. Use the Oil & Water Density Calculator to calculate the density of dry oil at reference temperature and the density of produced water at reference temperature.
Tip
Unless the oil is light hot condensate, the oil will almost always contain some interstitial water. This is generally acceptable for allocation measurements. However, if further accuracy is desired, you can determine the water cut and use it in the calculation. To determine or estimate the water cut, take a shakeout sample from one of the following:
The current flow/dump cycle, at the time of minimum density
Similar oils produced from the same reservoir
The tank or tanks that the separator flows into
Enter this water cut into the Oil & Water Density Calculator to calculate the density of dry oil at reference temperature.
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