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API MPMS Chapter 14.10 Manual of Petroleum Measurement Standards Chapter 14.10 Natural Gas Fluids Measurement - Measurement of Flow to Flares, Second Edition
Handbook / Manual / Guide by American Petroleum Institute, 12/01/2021
Measurement of flow to flares is important from accounting, mass balance, energy conservation, emissions reduction, and regulatory perspectives. Flares are safety relief systems that typically receive highly unpredictable rates of flow and varying compositions, and for safety reasons do not often lend themselves to being taken out of service to accommodate measurement concerns, even for short periods.
The standard addresses measurement of flow to flares, and includes:
- application considerations;
- selection criteria and other considerations for flare meters and related instrumentation;
- installation considerations;
- limitations of flare measurement technologies;
- calibration;
- operation;
- uncertainty and propagation of error;
- calculations.
The scope of this standard does not include analytical instrumentation.
This second edition includes discussion on using tracer technology and incorporates reference to API MPMS Chapter 22.3, Testing Protocol for Flare Gas Metering, another API standard that supports industry safety, sustainability, and emission reductions.
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SECOND EDITION, DECEMBER 2021
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Page
Scope 1
General 1
Field of Application 1
Normative References 1
Terms and Definitions 2
Application Considerations for Meters in Flare Systems 3
Overview 3
Flare Metering Technologies 4
General Considerations for Design and Selection of an FFMS 6
Location of Flare Meters 6
Application-specific Factors Affecting Flow Meter Performance 7
Meter Sizing 8
Measurement Uncertainty 9
Flow Meter Selection 9
Specific Meter Considerations 12
Secondary Instrumentation 17
Design Considerations 17
Record-keeping 18
Factory Calibrations/Verifications 18
Flow Meter 18
Pressure And Temperature Instruments 18
Commissioning and Startup 19
General 19
Flare Meter Commissioning 19
Periodic Verification 21
General 21
Periodic Verification Method—Flow Meter 21
Periodic Verification Method—Secondary Devices 22
Reevaluation of Existing FFMS 22
General 22
Reevaluation Procedure 22
Performance Test Protocol Scope 23
Uncertainty and Propagation of Error 23
Objective 23
Uncertainty Analysis Procedure 23
Simplified Uncertainty Analysis Procedure 24
Uncertainty Estimate for Flare Composition 26
Meter-specific Examples 29
Documentation 30
Procedural Documentation 30
Scaling Documentation 30
Page
Other Documentation 30
Audit Trail Documentation and Retention 30
Annex A (informative) Process Stream Data Sheet 32
Annex B (informative) Flare Meter Calculations 33
Annex C (informative) Compressibility Effects on Flare Gas Measurement Uncertainty 38
Annex D (informative) General Flare Design Considerations 39
Annex E (informative) Guidance on Management of Change Process FFMS Systems 48
Annex F (informative) Velocity Profile and Velocity Integration for Flare Gas Measurement 50
Annex G (informative) Uncertainty Calculation Examples 56
Bibliography 63
Flare Flow Measurement System (FFMS) Graphical Representation of an FFMS and its
Relation to Other Devices 4
Vortex Shedding Principle 6
Thermal Flow Meter Detail 15
In-line and Insertion Vortex Shedding Meters 16
FFMS Commissioning and Verification 20
Measurement Error Caused by Gas Composition Analysis Delay 28
Single Point Flare Burner 39
Purge Reduction Seals 40
Plant or Operating Unit Knock-out Drum 40
Local Knock-out Drum 40
Local Water Seal 40
Local Water Seal with Local Knock-out Drum 41
Air-assisted Flare 41
Enclosed Ground Flare 41
Flare Gas Recovery Unit 41
Waste Gas Riser 42
Staged Multi-burners 42
Purge Gas Injection Point 42
Assist Gas Injection Point 42
FFMS in a Horizontal Section with No Additional Equipment 43
FFMS with an Optional Connection and an LWS 44
FFMS with an LKO 45
FFMS Following a PKO 46
FFMS in a Staged Multi-burner Flare System 46
Typical Staging Curve 46
Annulus Area vs Distance from the Center of the Pipe 51
Page
Point Velocity vs Area Weighted Velocity 52
Predicted Velocity Contours through the Downstream of the Single Bend: a) Flow through the
Bend (Insert—Predicted Vortices), b) Development after the Bend 53
Comparison of Axial Velocity on the Horizontal Axis with NIST Data at Various Axial Distances
from the Bend 54
Guidance on Sensitivity to Entrained Mist, Liquid, Particulates, and Fouling 11
Guidance on Installation effects and Secondary Instrument Requirements for Pressure,
Temperature, and Composition 11
Upstream or Downstream Location of Pressure Devices Relative to the Flare Flow Meter 17
Example Table of Combined Uncertainties 26
Errors Related to Use of Fixed Composition for Different Meter and Calculations Types (Absolute
Value of Error) 29
Procedures and Responsibilities for Documentation 30
Velocity/Pipe Bulk Average Velocity 53
Table of Meter Errors Meter Using the Fully Developed Profile vs 11.2D Profile 54
Table of Meter Errors Meter Using the Fully Developed Profile vs 2.7D Profile 54
Linear Volume Meter Measuring Standard Volumetric Flowrate 57
Random Uncertainty—Linear Volume Meter Measuring Standard Volumetric Flowrate 57
Systematic Uncertainty—Linear Volume Meter Measuring Standard Volumetric Flowrate 58
Averaging Pitot Tube Measuring Standard Volumetric Flowrate 60
Random Uncertainty—Averaging Pitot Tube Measuring Standard Volumetric Flowrate 60
Systematic Uncertainty—Averaging Pitot Tube Measuring Standard Volumetric Flowrate 61
Thermal Flow Meter Measuring Mass Flowrate 61
Random Uncertainty—Thermal Flow Meter Measuring Mass Flowrate 62
Systematic Uncertainty—Thermal Flow Meter Measuring Mass Flowrate 62
Measurement of flow to flares is important from accounting, mass balance, energy conservation, emissions reduction, and regulatory perspectives. However, measurement of flow to flares remains distinctly different from traditional fiscal measurement practices. Flares are safety-relief systems, which typically receive highly unpredictable rates of flow and varying compositions; for safety reasons, they do not often lend themselves to being taken out of service to accommodate measurement concerns, even for short periods. Therefore, some of the traditional paradigms applicable to fiscal measurement systems, such as reasonably predictable flow rates and composition, the use of in-line proving, capability to readily remove meters from the piping system, the use of by-pass connections, and the use of master meters, for example, have to be abandoned altogether or highly modified in flare measurement applications. Use of measurement systems with diagnostic and verification capability might be one solution to ensure the performance.
Natural Gas Fluids Measurement—Measurement of Flow to Flares
The standard addresses measurement of flow to flares, and includes:
application considerations;
selection criteria and other considerations for flare meters and related instrumentation;
installation considerations;
limitations of flare measurement technologies;
calibration;
operation;
uncertainty and propagation of error;
calculations.
The scope of this standard does not include analytical instrumentation.
For safety and other considerations, it is highly undesirable to directly flare multiphase mixtures of liquids and gases. Therefore, this standard is primarily concerned with flare flow measurement in the gas or vapor phase. However, considering that fouling substances such as liquid droplets and/or mist or other contaminants may be present even in well-designed flare systems, this standard provides appropriate cautionary detail as to the effects of such contaminants that may impact flare flow measurements.
Most flare header applications are designed to operate during non-upset conditions at near-atmospheric pressure and ambient temperature, where compressibility of the mixture is near unity. Extreme conditions have been noted to be between 97.925 kPa-a (14.196 psia) and 414 kPa-a (60 psia), and between –150 °C and 300 °C (–238 °F and 572 °F). Flare gas compositions are highly variable and can range from average molecular weights approaching that of hydrogen to that of iso-pentanes and heavier. The uncertainty in flare gas density associated with varying pressure, temperature, and composition is discussed in more detail in 10.4.
Most flare headers are designed to operate at maximum velocities of 91 m/s (300 ft/s), with extremes up to 183 m/s (600 ft/s). This standard does not exclude pressures, temperatures, and velocity ranges different than those suggested above, as long as all applicable requirements are met.
The following documents are referred to in the text in such a way that some or all of their content constitutes requirements of this document. For dated references, only the edition cited applies. For undated references, the latest edition of the referenced document (including any addenda) applies.
API Manual of Petroleum Measurement Standards (MPMS) Chapter 21.1, Flow Measurement Using Electronic Metering Systems—Electronic Gas Measurement