addressing uncertainty in oil and natural gas industry greenhouse

More documents

Recommendations

Info

Appendix B LIST OF INDUSTRY MEASUREMENT STANDARDS This Appendix provides a list of over 300 hydrocarbon measurement standards used to measure quantities of petroleum products and natural gas liquids. Entire series of standards from particular standards developers are listed as many of the standards are inter-related and have to be used in conjunction with one another for measurement of quantities. This list is provided for users’ convenience to highlight the fact that companies may use different sets of measurement standards that fit their operating environment and available instrumentation. Each of the standards cited is designed to meet a variety of data needs and a defined level of accuracy, precision and uncertainty ranges. The compilation provided here includes standards developed by the American Petroleum institute (API); the American Society of Testing and Materials (ASTM)’ the American Gas Association (AGA); the Gas Processors Association (GPA), and the international organization for standardization (ISO). The list does not comprise an exhaustive reference to all standards; it does not cite applicable standards from the EU, Japan, or other standards setting organizations. B.1 API Manual of Petroleum Measurement Standards (MPMS) Chapter 1 Chapter 2.2A Chapter 2.2B Chapter 2.2C Chapter 2.2D Chapter 2.2E Chapter 2.2F Std 2552 Std 2554 Std 2555 RP 2556 Chapter 2.7 Chapter 2.8A Vocabulary Measurement and Calibration of Upright Cylindrical Tanks by the Manual Strapping Method [Chapter 2.2A should be used in conjunction with Chapter 2.2B. These two standards combined supersede the previous API Standard 2550, Measurement and Calibration of Upright Cylindrical Tanks] Calibration of Upright Cylindrical Tanks Using the Optical Reference Line Method Calibration of Upright Cylindrical Tanks Using the Optical-Triangulation Method Calibration of Upright Cylindrical Tanks Using the Internal Electro-optical Distance Ranging Method Petroleum and Liquid Petroleum Products—Calibration of Horizontal Cylindrical Tanks— Part 1: Manual Methods Petroleum and Liquid Petroleum Products—Calibration of Horizontal Cylindrical Tanks— Part 2: Internal Electro-optical Distance-ranging Method Measurement and Calibration of Spheres and Spheroids Measurement and Calibration of Tank Cars Liquid Calibration of Tanks Correcting Gauge Tables for Incrustation Calibration of Barge Tanks Calibration of Tanks on Ships and Oceangoing Barges Pilot Version, September 2009 B-1
Chapter 2.8B Establishment of the Location of the Reference Gauge Point and the Gauge Height of Tanks on Marine Tank Vessels Chapter 3.1A Standard Practice for the Manual Gauging of Petroleum and Petroleum Products Chapter 3.1B Standard Practice for Level Measurement of Liquid Hydrocarbons in Stationary Tanks by Automatic Tank Gauging Chapter 3.2 Standard Practice for Gauging Petroleum and Petroleum Products in Tank Cars Chapter 3.3 Standard Practice for Level Measurement of Liquid Hydrocarbons in Stationary Pressurized Storage Tanks by Automatic Tank Gauging Chapter 3.4 Standard Practice for Level Measurement of Liquid Hydrocarbons on Marine Vessels by Automatic Tank Gauging Chapter 3.5 Standard Practice for Level Measurement of Light Hydrocarbon Liquids Onboard Marine Vessels by Automatic Tank Gauging Chapter 3.6 Measurement of Liquid Hydrocarbons by Hybrid Tank Measurement Systems Chapter 4.1 Proving Systems – Introduction Chapter 4.2 Displacement Provers Chapter 4.4 Tank Provers Chapter 4.5 Master-Meter Provers Chapter 4.6 Pulse Interpolation Chapter 4.7 Field-Standard Test Measures Chapter 4.8 Operation of Proving Systems Chapter 4.9.1 Methods of Calibration for Displacement and Volumetric Tank Provers, Part 1— Introduction to the Determination of the Volume of Displacement and Tank Provers Chapter 4.9.2 Methods of Calibration for Displacement and Volumetric Tank Provers, Part 2— Determination of the Volume of Displacement and Tank Chapter 5.1 General Consideration for Measurement by Meters Chapter 5.2 Measurement of Liquid Hydrocarbons by Displacement Meters Chapter 5.3 Measurement of Liquid Hydrocarbons by Turbine Meters Chapter 5.4 Accessory Equipment for Liquid Meters Chapter 5.5 Fidelity and Security of Flow Measurement Pulsed-Data Transmission Systems Chapter 5.6 Measurement of Liquid Hydrocarbons by Coriolis Meters Chapter 5.8 Measurement of Liquid Hydrocarbons by Ultrasonic Flowmeters Using Transit Time Technology Draft Standard Vortex Shedding Flowmeter for Measurement of Hydrocarbon Fluids Chapter 6.1 Lease Automatic Custody Transfer (LACT) Systems Chapter 6.2 Loading Rack Metering Systems Chapter 6.4 Metering Systems for Aviation Fueling Facilities Chapter 6.5 Metering Systems for Loading and Unloading Marine Bulk Carriers Chapter 6.6 Pipeline Metering Systems Chapter 6.7 Metering Viscous Hydrocarbons Pilot Version, September 2009 B-2
Page 1 and 2:
Prepared by the LEVON Group, LLC an
Page 3 and 4:
Table of Contents SECTION Page FORE
Page 5 and 6:
List of Tables SECTION Page 2-1 Ove
Page 7 and 8:
FOREWORD The global oil and natural
Page 9 and 10:
DOCUMENT AT A GLANCE This document
Page 11 and 12:
1.0 INTRODUCTION Policymakers use e
Page 13 and 14:
The Intergovernmental Panel on Clim
Page 15 and 16:
2.0 SOURCES OF UNCERTAINTY There ar
Page 17 and 18:
Table 2-1. Overview of Methods Used
Page 19 and 20:
the uncertainty associated with cur
Page 21 and 22:
d. Data processing uncertainty Typi
Page 23 and 24:
d. Material Balance For some emissi
Page 25 and 26:
3.0 OVERVIEW OF MEASUREMENT PRACTIC
Page 27 and 28:
3.1 Flow Measurement Practices Cont
Page 29 and 30:
All these factors should be assesse
Page 31 and 32:
Table 3-1. Example of FFMS Combined
Page 33 and 34:
3.2 Uncertainties of Flow Measureme
Page 35 and 36:
Table 3-3. Compilation of Specifica
Page 37 and 38:
EXHIBIT 3-3: FACTORS TO CONSIDER WH
Page 39 and 40:
3.3.2 Quantifying Sampling Precisio
Page 41 and 42:
Table 3-4. Summary of Selected Carb
Page 43 and 44:
3.5 Heat Content Determination The
Page 45 and 46:
3.5.2 Computational Methods Heating
Page 47 and 48:
using standard methods, non-standar
Page 49 and 50:
0.6 0.4 0.2 Error 0 -0.2 -0.4 -0.6
Page 51 and 52:
s ± t × (Equation 4-1) n where s
Page 53 and 54:
4.2.1 Propagation Equations There a
Page 55 and 56:
For two terms that might be correla
Page 57 and 58:
EXHIBIT 4-1: Uncertainty Example fo
Page 59 and 60:
Page 61 and 62:
Further guidance for assigning unce
Page 63 and 64:
4.4 Quantifying Measurement Uncerta
Page 65 and 66:
Page 67 and 68: EXHIBIT 4-5: Uncertainty Example fo
Page 69 and 70: Are the data based on a single poin
Page 71 and 72: Two methods are compared. The first
Page 73 and 74: . EXHIBIT 4-6: Uncertainty Example
Page 75 and 76: EXHIBIT 4-6: Uncertainty Example fo
Page 77 and 78: Table 4-13 shows the uncertainty in
Page 79 and 80: Table 4-13. Comparison of Annual Em
Page 81 and 82: • The evolution of activity and e
Page 83 and 84: These guidelines concentrate solely
Page 85 and 86: (Reprinted from the API Compendium)
Page 87 and 88: Table 5-2. Onshore Oil Field (High
Page 89 and 90: associated with them are assigned b
Page 91 and 92: Table 5-4. Onshore Oil Field (High
Page 93 and 94: 5.2.4 Propagating Assymetric Uncert
Page 95 and 96: U( rel) = U( rel) + U( rel) + U( re
Page 97 and 98: Coke burn rate approach (Equation 5
Page 99 and 100: Wt% C ∑ lbmole x lbmole C 12 lb C
Page 101 and 102: The CO 2 emissions are calculated u
Page 103 and 104: GHG Emissions, tonnes/yr 60,000 50,
Page 105 and 106: vast majority of the uncertainty fo
Page 107 and 108: 6.0 REFERENCES AGA, 2008, Greenhous
Page 109 and 110: The Alberta Energy and Utilities Bo
Page 111 and 112: Appendix A GLOSSARY OF STATISTICAL
Page 117: APPENDIX B LIST OF INDUSTRY MEASURE
Page 121 and 122: Chapter 11.5.3 Chapter 12.1.1 Chapt
Page 123 and 124: Chapter 19.4 Chapter 20.1 RP 85 RP
Page 125 and 126: ISO 8222:2002 ISO 8697:1999 ISO 902
Page 127 and 128: ISO 7194:2008 Measurement of fluid
Page 129 and 130: ASTM D4292 ASTM D4892 ASTM D5002 AS
Page 131 and 132: APPENDIX C OPERATING CONDITIONS, IN
Page 133 and 134: Appendix C OPERATING CONDITIONS, IN
Page 135 and 136: Appendix D SELECT MEASUREMENT METHO
Page 137 and 138: c. ASTM UOP539-97, Refinery Gas Ana
Page 139 and 140: interference between known componen
Page 141 and 142: maintained over the room temperatur
Page 143 and 144: APPENDIX E UNITS CONVERSION
Page 145 and 146: − Gasoline density (average) = 0.
Page 147 and 148: Appendix F UNCERTAINTY ESTIMATION D
Page 149 and 150: The uncertainty for the heaters/reb
Page 151 and 152: ∑ 2 U ( abs) = U( abs) ∑(Wt%C)
Page 153 and 154: Combining the fuel usage for the tw
Page 155 and 156: Uncertainty Estimate of CO 2 e Emis
Page 157 and 158: U ( abs) = ( U ( abs) + U ( abs) +
Page 159 and 160: E E CO2e 219 tonne CO ⎛ 2 0.0108
Page 161 and 162: E CO 2 6 500× 10 scf gas lbmole ga
Page 163 and 164: • Fuel Economy (miles per gallon)
Page 165 and 166: Upper: U ( abs) = (U( abs) +U( abs)
Page 167 and 168: default CH 4 content is 5.53% from
Page 169 and 170:
Uncertainty Estimate of CO 2 e Emis
Page 171 and 172:
( ) Urel ( ) = Urel ( ) = Urel ( )
Page 173 and 174:
Uncertainty Estimate for CH 4 and C
Page 175 and 176:
specific mole % for CH 4 and CO 2 i
Page 177 and 178:
E CO2 0.07239 tonne CH 4 tonne mole
Page 179 and 180:
U ( rel) = U( rel) +U( rel) +U( rel
Page 181 and 182:
Table F-14. Fugitive Emission and U
Page 183 and 184:
U ( abs) = (U( abs) +U( abs) +U( ab
Page 185 and 186:
Table F-15. Onshore Oil Field (High
show all

addressing uncertainty in oil and natural gas industry greenhouse

You also want an ePaper? Increase the reach of your titles

Delete template?

Save as template?