Api mpms 17 2 1999 scan + errata 2000 (american petroleum institute)

Date of Issue: April 28,2000 Affected Publication: Manual of Petroleum Measurement Standards, Chapter 17Marine Measurement, Section 2-Measuretnent of Cargoes on Board Tank Vessels, Second Edition, May 1999 ERRATA `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Please replace page 48, Table C-24onversion of Temperature, with the following table Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST of Temperatures Degrees Fahrenheit -58.0 -56.2 -54.4 -52.6 -50.8 Degrees -15.0 -43 -42 -41 -49.0 -47.2 -45.4 -43.6 -41.8 -40 -39 -38 -37 -36 -40.0 -39.4 -38.9 -38.3 -37.8 -38.2 -36.4 -34.6 -32.8 -12.2 -11.7 -37.2 -36.7 -36.1 -35.6 -35.0 -35 -34 -33 -32 -31 -34.4 -33.9 -33.3 -32.8 -32.2 Degrees Celsius -45.6 -45.0 -44.4 -43.9 -43.3 Temperature to Be Converted -42.8 -42.2 -41.7 -41.1 -40.6 -45 -40.0 -50 -49 -48 -47 -46 -44 Celsius -17.8 -17.2 -16.7 -16.1 -15.6 -14.4 -13.9 -13.3 -12.8 Temperature to Be Converted 10.6 Temperature to Be Converted 50 51 11.1 52 11.7 12.2 53 54 Degrees Fahrenheit 122.0 123.8 125.6 127.4 129.2 41.0 42.8 44.6 46.4 48.2 12.8 13.3 13.9 14.4 55 56 57 58 59 131.0 132.8 134.6 i 36.4 138.2 10 50.0 i 5.6 16.1 16.7 17.2 17.8 60 61 62 63 64 140.0 II 12 O Degrees Fahrenheit Degrees Celsius 10.0 33.8 35.6 37.4 39.2 15.0 141.8 143.6 145.4 147.2 -10.0 13 14 51.8 53.6 55.4 57.2 -31.0 -29.2 -27.4 -25.6 -23.8 -9.4 -8.9 -8.3 -7.8 -7.2 15 16 17 18 19 59.0 60.8 62.6 64.4 66.2 18.3 18.9 19.4 20.0 20.6 65 66 67 68 69 149.0 150.8 152.6 154.4 156.2 -30 -29 -28 -27 -26 -22.0 -20.2 -18.4 -16.6 -14.8 -6.7 -6.1 -5.6 20 21.1 21.7 22.2 22.8 23.3 70 22 23 24 68.0 69.8 71.6 73.4 75.2 72 73 74 158.0 159.8 161.6 163.4 165.2 -3I -31.1 -30.6 -30.0 -29.4 -25 -24 -23 -22 -2I -13.0 - 1.2 -9.4 -7.6 -5.8 -3.9 -3.3 -2.8 25 26 27 28 29 77.0 78.8 80.6 82.4 84.2 23.9 24.4 25.0 25.6 26.i 75 76 77 78 79 167.0 168.8 170.6 172.4 174.2 -28.9 -28.3 -27.8 -27.2 -26.7 -20 -19 -18 -17 -16 -4.0 -2.2 -0.4 I 3.2 -1.1 1.1 30 31 32 33 34 86.0 87.8 89.6 91.4 93.2 26.7 27.2 27.8 28.3 28.9 80 81 82 83 84 176.0 177.8 179.6 181.4 183.2 -26.1 -25.6 -25.0 -24.4 -23.9 -15 -14 -13 -12 5.0 6.8 8.6 10.4 12.2 1.7 2.2 2.8 3.3 3.9 35 36 37 38 39 95.0 96.8 98.6 100.4 102.2 29.4 30.0 30.6 31.1 31.7 85 86 87 88 89 185.0 186.8 188.6 190.4 192.2 -23.3 -22.8 -22.2 -21.7 -10 14.0 15.8 i 7.6 19.4 21.2 4.4 5.0 5.6 i 6.7 40 41 42 43 44 104.0 90 111.2 32.2 32.8 33.3 33.9 34.4 92 93 94 194.0 195.8 197.6 199.4 201.2 23.0 24.8 26.6 28.4 30.2 7.2 7.8 8.3 8.9 9.4 45 46 47 48 49 113.0 114.8 116.6 118.4 120.2 35.0 35.6 36.1 36.7 37.2 95 96 97 98 99 203.0 204.8 206.6 208.4 210.2 32.0 10.0 122.0 37.8 100 212.0 -21.1 -20.6 -20.0 -19.4 -18.9 -18.3 -17.8 -1 -9 -8 -7 -6 -5 -4 -3 -2 -I O -11.1 -10.6 -5.0 -4.4 -2.2 -1.7 -0.6 0.0 0.6 21 105.8 107.6 109.4 50 71 91 Note: This table provides conversion values for temperatures in degrees Fahrenheit and degrees Celsius for each whole degree from -50” to +250”.The tempenture to be converted is found in the center “temperature to be converted” column If the temperature to be converted is in degrees Fahrenheit, its equivalent in degrees Celsius is found in the “degrees Celsius” column to the left If the temperature to be converted is in degrees Celsius, its equivalent in degrees Fahrenheit is found in the “degrees Fahrenheit” column to the right 48 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Table C-2-Conversion STD-API/PETRO MPMS L7-2-EMGL 1999 SB 0732270 b L h h L L 035 Manual of Petroleum Measurement Standards Chapter 17-Marine Measurement Section 2-Measurement of Cargoes On Board Tank Vessels SECOND EDITION, MAY 1999 American Petroleum Institute Helping You Get The Job Done Right? `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD-API/PETRO MPMS 17-2-ENGL 1999 H 0732290 ObLhhL2 Ti1 Saai Manual of Petroleum Measurement Standards Chapter 17-Marine Measurement Section 2-Measurement of Cargoes On Board Tank Vessels Upstream Segment SECOND EDITION, MAY 1999 American Petroleum Institute Helping You Get The Job Done Right? `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST S T D * A P I / P E T R O M P M S L - Z - E N G L 1999 B 0732290 O b h h l ~ 906 SPECIAL NOTES API publications necessarily address problems of a general nature With respect to particular circumstances,local, state, and federal laws and regulations should be reviewed API is not undertaking to meet the duties of employers, manufacturers, or suppliers to warn and properly train and equip their employees, and others exposed, concerning health and safety risks and precautions, nor undertaking their obligations under local, state, or federal laws Information concerning safety and health risks and proper precautions with respect to particular materials and conditions should be obtained from the employer, the manufacturer or supplier of that material, or the material safety data sheet Nothing contained in any API publication is to be construed as granting any right, by implication or otherwise, for the manufacture, sale, or use of any method, apparatus, or product covered by letters patent Neither should anything contained in the publication be construed as insuring anyone against liability for infringement of letters patent Generally,MI standards are reviewed and revised, reaffirmed, or withdrawn at least every five years Sometimes a one-time extension of up to two years will be added to this review cycle This publication will no longer be in effect five years after its publication date as an operative API standard or, where an extension has been granted, upon republication Status of the publication can be ascertained from the general manager of the Upstream Segment [telephone (202) 682-8000] A catalog of API publications and materials is published annually and updated quarterly by API, 1220 L Street, N.W., Washington, D.C 20005 This document was produced under MI standardizationprocedures that ensure appropriate notification and participation in the developmental process and is designated as an MI standard Questions concerning the interpretation of the content of this standard or comments and questions concerning the procedures under which this Standard was developed should be directed in writing to the general manager of the Upstream Segment, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C 20005 Requests for permission to reproduce or translate all or any part of the material published herein should also be addressed to the director API standards are published to facilitate the broad availability of proven, sound engineering and operating practices These standards are not intended to obviate the need for applying sound engineering judgment regarding when and where these standards should be utilized The formulation and publication of M I standards is not intended in any way to inhibit anyone from using any other practices Any manufacturer marking equipment or materials in conformance with the marking requirements of an API standard is solely responsible for complying with all the applicable requirements of that standard M I does not represent, warrant, or guarantee that such products in fact conform to the applicable MI standard All rights reserved No part of this work may be reproduced, stored in a retrieval system, or transmitted by any means, electronic, mechanical, photocopying, recording, or otherwise, without prior written permission from the publishez Contact the Publishel; API Publishing Services, 1220 L Street, N W , Washington, D.C 20005 Copyright O 1999 American Petroleuminstitute `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST FOREWORD `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - This publication i s intended to encourage the development of uniform practices for measurement of cargoes aboard marine tank vessels It presents current methods of cargo measurement, but this is not intended to preclude the use of any new technology or the revision of the methods presented To gain a better understanding of the methods described in this publication, the reader should review in detail the latest editions of the referenced publications Metric units are listed in this document in a manner that reflects current marine practice Nothing contained in this publication is intended to supersede any operating practices recommended by organizations such as the Oil Companies International Marine Forum or individual operating companies, nor is the publication intended to conflict with any safety or environmental considerations, local conditions, or the specific provisions of any contract Ail procedures described in this publication should be performed by or in the presence of the ship's master, the barge captain, or their representatives For reasons of safety, only nonsparking equipment shall be used for measurements on board marine tank vessels This standard requires the purchaser to specifj certain details and features Although it is recognized that the purchaser may desire to modify, delete, or amplify sections of this standard, it is strongly recommended that such modifications, deletions, and amplifications be made by supplementing this standard, rather than by rewriting or incorporating sections thereof into another complete standard MI standards are published as an aid to procurement of standardized equipment and materials These standards are not intended to inhibit purchaser or producers from purchasing or producing products made to specificationsother than those of MI AF'I publications may be used by anyone desiring to so Every effort has been made by the Institute to assure the accuracy and reliability of the data contained in them; however, the Institute makes no representation,warranty, or guarantee in connection with this publication and hereby expressly disclaims any liability or responsibility for loss or damage resulting from its use or for the violation of any federal, state, or municipal regulation with which this publication may conflict Suggested revisions are invited and should be submitted to the general manager of the Upstream Segment, American Petroleum Institute, 1220 L Street, N.W., Washington, D.C 20005 iii Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST CONTENTS Page SCOPE NORMATIVEREFERENCES DEFINITIONS AND ABBREVIATIONS 3.1 Definitions 3.2 Symbols and Abbreviations 2 4 GENERAL SAFETY PRECAUTIONS 4.1 Electrical and Operating Safety 4.2 Maintenance 4.3 Sealing 4.4 Vapor Control Valve Installation 5 5 5 OPEN MEASUREMENT EQUIPMENT AND PROCEDURES 5.1 OpenManualSampling 5.2 Open Manual Gauging 5.3 Open Temperature Determination 13 CLOSED AND RESTRICTED MEASUREMENT 6.1 Manual Closed and Restricted Systems 6.2 Automatic Closed Systems 16 16 23 SAMPLINGANDSAMPLEHANDLING 7.1 Manual Sampling of Petroleum Liquids 7.2 Dynamic Sampling 7.3 Manifold (Spot Line) Samples 7.4 Handling of Samples 7.5 Labeling of Samples 27 27 29 30 30 30 DATA COLLECTION TABLES BASIC CALCULATIONS RECORDS ANDREPORTS 8.1 DataCollection 8.2 CapacityTables 8.3 Volume Correction Tables 8.4 Observations, Measurements, and Calculations 8.5 Volume of Ship's Pipelines 30 30 30 31 31 31 SPECIAL CONSIDERATIONS 9.1 High-Viscosity and High-Pour-Point Cargoes 9.2 Heatedcargoes 9.3 Measurement On Board Rolling Marine Tank Vessels 9.4 SpikedCNdes 9.5 HighRVPCargoes 9.6 Solidified OBQROB 9.7 Out-of-Trim Vessels 9.8 Static Accumulator Cargoes 31 32 32 32 32 32 32 32 32 V `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Previous page is blank Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST S T D = A P I / P E T R O MPMS 17.2-ENGL 1979 0732270 Oblibblib bL7 11111 Page APPENDIX A PHYSICAL CHARACTERISTICSAND FIRE CONSIDERATIONS APPENDIX B ADDITIONAL INSTRUCTIONS AND CAUTIONARY NOTES APPENDIX C CONVERSION FACTORS APPENDIX D TYPICAL PROPERTIES OF CRUDE OILS 33 35 45 51 Figures I la 3a 3b 8a 8b 9a 9b 10 11 12 13 14 Tables Sample Calculations of Ullage Gauge 13 Sample Calculation of Ullage Gauge Using the Alternative Uilage Procedure 13 Sample Calculation of Innage Gauge Using the Alternative Innage Procedure 13 Liquid Temperature Measurement Location Requirements for Portable Electronic Thermometer 15 5a Recommended Immersion Times for Woodback Cup-Case Assembly 15 5b Recommended Immersion Times for Woodback Cup-Case Assembly When Temperature Differential is Less Than 5°F 15 C-1 Conversion of Lengths Weights and Volume 47 C-2 Conversion of Temperatures 48 D-1 Typical Properties of Crude Oils 53 vi Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Typical Container Assemblies for Bottle Sampling Typical Container Assemblies for Beaker Sampling Typical Bottom Sampler Typical Thief Type Sampler Typical C o r e a n e Type Sampler Typical Scoop Sampler Typical InnageIUllageEquipment ManualTankGauging 12 Measurement of Free Water 12 Typical Mercury-in-Glass ThermometerAssemblies 14 ATypeofPET 14 Typical Vapor Control Valves (VCVs) 17 Typical Deck Mountings of Vapor Control Valves PMUs Not Attached 18 Typical Deck Mountings of Vapor Control Valves PMUs Attached 18 Two Types of Portable Measurement Units (PMUs) 20 Typical Recessed Sensor 20 Type of Portable Sampling Unit (PSU) 22 Typical Special Weighted Bar and Bob Units 22 A Type of Automatic Fixed Measurement System Permanently Installed onaVessel 24 15 Type of Automatic Sampler Designed for Shipboard Use 25 27 16 Sampling Depths in Ship or Barge Tank B-1 Single Hull Ship 36 B-2 Typical Double Hull Cross Section 36 B-3 Typical Mid-Deck VLCC Design 37 B-4a Typical OB0 Cross Section 39 B-4b Typical ORO Cross Section 39 B-5 Draft Readings: US Customary Unit 40 B-6 Draft Readings: Metric Unit 40 B-7 Method To Calculate Vessel?s List Using Midships Draft Readings 41 B-8 Calculating a Trim Correction 42 B-9 Method to Calculate List Correction 42 STD-APIIPETRO MPMS 17.2-ENGL 1999 II 0732270 Ob3ibb17 553 Sl Chapter 17-Marine Measurement Section 2-Measurement of Cargoes On Board Tank Vessels O Introduction address in detail the technologies of the equipment used This standard is not intended for use with pressurized or refrigerated cargoes such as liquid petroleum gas (LPG) and liquid natural gas (LNG) Based on present technology, careful manual gauging, temperature measurement and sampling are the most accurate overall methods for measuring quantities of cargo, free water, and on-board quantity (OBQ) andor remaining on board (ROB) on marine tank vessels Automatic gauging may be as accurate as manual gauging for measuring overall volumes if the manufacturer’s instructions are followed and equipment is periodically calibrated and checked using manual gauging as a reference Safety and environmental regulations by all levels of government and other regulatory agencies worldwide, are limiting andor prohibiting the release of hydrocarbons to the atmosphere with regard to tank vessel operations This has resulted in the restriction and, in some cases, the prohibition of traditional methods of obtaining cargo measurements through open gauge hatches Consequently, numerous measurement methods and devices are now being used and additional ones developed that allow the necessary cargo measurements and samples to be taken without opening the vessel’s gauge hatches The objective of this publication is to provide guidance to vessel and shore personnel on the generally accepted methods of determining cargo quantities on board marine tank vessels using open, closed, and restricted methods This publication describes suggested techniques and procedures for measuring, calculating, reporting, and keeping records of quantities of crude oils and petroleum products transported in marine tank vessels Normative References The following standards contain provisions which, through reference in this text, constituteprovisions of this standard At the time of publication, the editions indicated were valid All standards are subject to revision, and parties to agreements based on this standard are encouraged to investigate the possibility of applying the most recent editions of the standards indicated below MPMS Chapter Vocabulary Tank Calibration MPMS Chapter MPMS Chapter 3.1A Standard Practice for Manual Gauging of Petroleum and Petroleum Products MPMS Chapter 3.1B Standard Practice for Latel Measurement of Liquid Hydrocarbons in Stationary Tanks by Automatic Tank Gauging MPMS Chapter 3.4 Standard Practice for Level Measurement of Liquid Hydrocarbons on Marine Vessels by Automatic Tank Gauging MPMS Chapter 7.1 Static Temperature Determination Using Mercury Thermometer Static Temperature Determination MPMS Chapter 7.3 Using Portable Electronic Thermometers (PETS) MPMS Chapter 7.4 Fixed Automatic Tank Thermometers MPMS Chapter 8.1 Manual Sampling of Petroleum and Petroleum Products (ANSIl/ ASTM2 D 4057) MPMS Chapter 8.2 Automatic Sampling of Petroleum and Petroleum Products (ANSI1/ ASTM2 D 4177) MPMS Chapter 9.1 Hydrometer Test Method for Density, Relative Density (Specijìc Gravity), or API Gravity of Crude Petroleum and Liquid Petroleum Products (ANS11/ASTM2D 1928) Scope To determine the quantity and quality of cargo on board marine tank vessels, it is necessary to accurately gauge, ascertain the temperature, collect a representative sample, and calculate the amount of all materials contained in the vessel’s lines, cargo tanks, and slop tanks Any void spaces that may contain cargo, such as permanent ballast tanks, double bottoms, and cofferdams, must also be checked, and any volumes contained in these spaces must be calculated This publication describes the appropriate methods of performing these procedures for Cnide oils and petroleum products normally carried on board marine tank vessels This standard covers the use of manual and automatic measurement systems commonly used on marine tank vessels It establishes the procedures for obtaining the level measurements of cargo, free water, and OBQROB as well as taking the temperaturesand samples required for the marine custody transfer of most bulk liquid petroleum cargoes It does not ‘American National Standards Institute, 11 West 42nd Street,New York, New York 10036 *American Society for Testing and Materiais, 100 Barr Harbor Drive, West Conshohocken, Pennsylvania 19428 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - API MPMS Chapter 10.1 Determination of Sediment in C d e Oils and Fuel Oils by the Extraction Method (ANS111ASTM2D 473, IP3 53) MPMS Chapter 10.2 Determination of Water in Crude Oil by Distillation (ANSI'lASTM2 D 4006) MPMS Chapter 10.3 Determination of Water and Sediment in Crude Oil by the Centnjüge Method (ANS111ASTM2D 4007) MPMS Chapter 10.4 Methods of Testfor Water and Sediment in Crude Oils (ANS111ASTM2 D 96) MPMS Chapter 11.1 Volume Correction Factors (ANSI11 ASTM2 D 1250, P3200, IS04 R914) Calculation of Petroleum Quantities MPMS Chapter 12 MPMS Chapter 17.1 Guidelines for Marine Cargo Inspection MPMS Chapter 17.4 Method for QuantiJication of Small Volumes on Marine Vessels (OBW ROB) ASTM2 D 287 Test Method for API Gravity of Crude Petroleum and Petroleum Products (Hydrometer Method) International Safety Guide for Oil Tankers and Terminals (ISGOïT) IMO8 Inert Gas Systems OS HA^ Occupational Safety and Health Standards (29 Code of Federal Regulations, Section 1910 and following) 31nstitute of Petroleum, 61 New Cavendish Street, London W1M 8AR, England 41ntemational Standards Organization, IS0 publications are available from the American National Standards Institute, 11 West 42nd Street, New York, New York 10036 51ntemational Chamber of Shipping, 30/32 Mary Axe Street, London EC3 ASET England Companies Intemational Marine Forum, Portland House, Stag Place, London SW1E SBH England 71ntemational Association of Ports and Harbors, Kotohira-Kaikan Building, 2-8 Toranomon, l-Chom Minato-Ku, Tokyo 105, Japan 81ntemationalMaritime Organization,London, England gOccupational Safety and Health Administration, U.S Department of Labor, Washington, D.C 20402 Definitions and Abbreviations 3.1 DEFINITIONS For the purpose of this standard, the following definitions apply 3.1.1 automatic sampler: A device used to extract a representative sample from the liquid flowing in a pipe The automatic sampler generally consists of a probe, a sample extractor, an associated controller, a flow-measuring device, and a sample receiver 3.1.2 automatic tank gauge (ATG): (1) An instrument that automatically measures and displays liquid levels or ullages in one or more tanks either continuously, periodically, or on demand (2) The liquid level in a tank as measured using an automatic tank gauge system 3.1.3 automatic tank temperature (ATT): A system that automatically measures and displays temperatures of liquids in one or more vessel tanks continuously, periodically, or on demand 3.1.4 automatic vessel tank gauge system: A system that automatically measures and displays liquid levels or ullage in one or more vessel tanks continuously, periodically, or on demand 3.1.5 ballast: The water taken on when a vessel is empty or partly loaded to increase draft in order to properly submerge the propeller, and to maintain stability and trim 3.1.6 bunker survey: The survey conducted to determine the quantity and quality of bunkers purchased by the vessel; or the process of accounting for bunker quantities on the vessel, before and after loading or discharging, to determine if any cargo was diverted into the vessel's bunker tanks during the cargo operations or voyage 3.1.7 capacity tables (calibration tables, innage/ ullage tables): Those tables developed by recognized industry methods that represent volumes in each tank according to the liquid (innage) or empty space (ullage) measurement in the tank The tables are entered with linear measurements (i.e., feet, inches, meters, centimeters) to obtain calibrated volumes (i.e., barrels, cubic meters, cubic feet) (See Appendix B.4) 3.1.8 closed system: For the purpose of this document, a closed system exists when a marine tank vessel is so designed that no direct exposure andor release of its cargo tank contents to the atmosphere occurs under normal operating conditions (see restricted system) 3.1.9 closed system measurement (CSM): Measurement of petroleum cargoes on a closed system marine tank vessel performed using closed measurement devices [ S e e restricted system measurement (RSM).] `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST SECTION 2-MEASUREMENT OF CARGOES ON BOARD TANKVESSELS 41 Port Legend: PA = PortDrafi SB = Starboard Draft XY = VesselBeam Theory: Angle LCV = Angle SCX = Angle of List = O Tangent O = = 10.0 m = 12.0 m = 30.0 m SX (Starboard Draft - Port Draft)/2 cx -(Vessel’s Beam)/2 This reduces to Tangent O = Starboard Draft - Port Draft Vessel’s Beam Calculation: Tangent O = (’ 2.0 - ’ 30.0 = 0.0667 From the attached chart of “Natural Functions of Angles” a tangent value of 0.0667 represents an angle of 4”, rounded to the nearest 0.5” Result: Vessel is listed 4” to Starboard ~ ~~ Figure B-7-Method To Calculate Vessel’s List Using Midships Draft Readings `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD.API/PETRO MPMS 17.2-ENGL 1999 42 CHAPTER 1-/-MARINE 0732290 ObZbb5b T MEASUREMENT The trim correction is given by the following equation: I where D S L S, = tank height, from the reference point, = observedgauge, = distance of the gauge hatch from the center of = tank, trim corrected gauge L f = length of ship between perpendiculars, T = trim of the ship All of the above must be expressed in the same units of length Note that the bracketed quantity is added when the observed gauge is forward and subtracted when aft of the center of the tank When the liquid level in the tank is such that it no longer reaches the forward end, a wedge is formed and the application of the trim correction will no longer give the true gauge I l Source: API MPMS Chapter 12.1 Figure B-€&Calculating a Trim Correction When no list correction tables are available, the observed ullage (U,,,) should be corrected for list as illustrated in Figure B-9 The correction for list may be expressed as follows: UM U, = -IZtane cos% The sign for the second portion of the expression is positive when the list is toward the side on which the ullage point is located and negative when the list is toward the side opposite from the ullage point (Refer to Figure B-9.) Source: API MPMS Chapter 2.8A Figure B-+Method Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS to Calculate List Correction Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - l STD*API/PETRO MPMS L7-2-ENGL 1999 SECTION 2-MEASUREMENT OF CARGOES O N BOARD TANKVESSELS c Extremes in atmospheric temperature require special consideration during measurement because of possible reaction of the cargo involved For example, high air or water temperatures can lead to vaporization of cargoes whereas cold water or air temperatures could lead to solidification and higher ROBS of high-pour-point cargoes B.1O Alternate Procedures for Measurement of Small Quantities 8.10.1 B.10.1.2 The free-water ullage obtained by using the PMU can then be converted to a calculated innage by subtracting the ullage from the published reference height Compare the innage obtained by using water-paste to the calculated innage and record both readings if they are different BRASS BOB PMU-WATER MEASUREMENT The traditional brass bob gauging method can be used through a VCV by using a specially designed PMU This equipment allows the bob to be attached to the end of it It then may be lowered into the tank like the usual PMU equipment, but when the procedure used is like that procedure described in 6.1.22 (see Figure 13) Size and Location of Vapor Control Valves The size and location of the vapor control valves used for closed or restricted system measurement are critical to the process A VCV of the proper size, located correctly, will allow more accurate measurements to be taken than one improperly located and of insufficient size For the best way to measure OBQROB and free water under most operating conditions, the VCV must allow access to the tank as far aft as possible and still allow the gauge tape to be lowered to the bottom of the vessel’s tank without touching the aft bulkhead during extreme trim at stem conditions When the VCV is located in the middle of a tank,it usually will be impossible to measure any free water or OBQ/ROB under normai operating conditions Note: To take sufficient samples and accurate measurements of small quantities and free water when the vessel is not on an even keel, a VCV must be located as close as possible to the aft buíkhead or to the bulkhead toward the direction of the vessel’s normal operating trim and list B.12 OperatingTemperature Ranges of PMUs The traditional brass bob and water-finding paste method can be used through a VCV by using a specially designed PMU This equipment allows the bob to be attached to the end of it It then may be lowered into the tank like the usual PMU equipment, but when the procedure is used it is then like the procedure described in AFT MPMS Chapter 17.2.4.2.1.4.2 (SeeFigure 13.) Each PMU has a designed operating range of temperatures above or below which the units may not function accurately It is necessary to know the correct operating limits of the equipment used so that the designed measurement parameters are not exceeded in the field Only a PMU with a designed operating range suited for the temperature and gravity of the cargo being measured should be used for MCTM purposes `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS 43 B.10.3 BRASS BOB PMU-ROB/OBQ MEASUREMENT B.ll ALTERNATE FREE WATER MEASUREMENT B.lO.l.l When using an interface detecting PMU, waterfinding paste may be placed on the outside of the probe before lowering it to the tank bottom When a clean strike of the tank bottom is felt, allow the probe to remain in the tank a sufficient amount of time for any water present to react with the paste Normally 30-60 seconds will be required but more time might be necessary for heavier oils After the required reaction time, retrieve the probe without hesitation and measure the cut on the probe using a calibrated tape This is the innage of the water in the tank being measured B.10.2 0732290 Oblbb57 13T aiia Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST APPENDIX C-CONVERSION FACTORS `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - 45 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Previous page is blank Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD=API/PETRO MPMS l7.2-ENGL 1999 111 0732290 O b l b b TO2 1111 Table C-1-Conversion of Lengths, Weights, and Volumes To To Convert To To Convert Multiply by Length Metres Voiumeb 1.0936 3.2808 39.370 Yards Feet Inches U.S gallons Cubic inches Cubic feet Imperial gallons U.S barreis Yards Metres 0.9144a Feet Metres 0.3048a Litres US barrels U.S gallons Cubic inches Inches Centimetres 2.54a Cubic feet Imperial gallons Litres Weight Long tons Pounds (avoirdupois) Short tons Metric tons (tonnes) Short tons Pounds (avoirdupois) Long tons Metric tons (tonnes) 22400' 1.12a 1.01605 Short tons Pounds (avoirdupois) Kilograms 0.453592 Kilograms Pounds (avoirdupois) 2.20462 Long tons Imperial gallons Cubic inches Cubic feet U.S gallons U.S barrels Litres 2000.P 0.892857 0.907185 0.984206 1.lo231 Metric tons (tonnes) Multiply by 23 1.W 0.133681 0.832674 0.0238095 3.78541 42.P 9702.W 5.61458 34.9723 158.987 277.42 O 160544 1.20095 0.0285941 4.54596 Cubic metres 6.22883 7.48052 O 178108 28.3169 0.0283169 Cubic inches Imperial galions U.S gallons Litres 0.00360465 0.0043290 0.0163871 Litres Cubic inches 61.0238 0.0353147 0.219969 0.264172 0.00628981 Cubic feet imperial gallons U.S gallons U.S barrels Litres Cubic feet Imperial gallons U.S gallons U.S barrels Cubic metres Imperial gallons U.S gallons U.S barrels Cubic feet 219.969 264.172 6.28981 35.3147 aThisrelationship is exact by definition m e s e factors are solely for conversion at the same temperature 47 `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Previous page is blank Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD-API/PETRO flPflS L7.2-ENGL 1999 of Temperatures Table C-2-Conversion Degrees Fahrenheit -58.0 -56.2 -54.4 -52.6 -50.8 Degrees Celsius -45.6 45.0 44.4 43.9 43.3 Temperature to Be Converted 42.8 42.2 41.7 45 -49.0 47.2 -45.4 43.6 41.8 40.0 40 40.0 -39.4 -38.9 -38.3 -37.8 -39 -3 -37 -36 -37.2 -36.7 -36.1 -35.6 -35.0 Degrees Celsius 45.6 45.0 -44.4 -43.9 43.3 Temperature to Be Converted -50 49 48 46 0732290 O b L b b b O 724 I I -50 49 47 46 Degrees Fahrenheit -58.0 -56.2 -54.4 -52.6 -50.8 Degrees Celsius -45.6 45.0 -44.4 43.9 43.3 Temperature to Be Converted -50 49 48 -47 Degrees Fahrenheit -58.0 -56.2 -54.4 -52.6 -50.8 49.0 -47.2 45.4 43.6 41.8 41.1 -43 49.0 -47.2 -45.4 43.6 40.6 41.8 42.8 -42.2 -41.7 41.1 40.6 40.0 -39.4 -38.9 -38.3 -37.8 40 40.0 40.0 40.0 -38.2 -36.4 -34.6 -32.8 -39 -38 -37 -36 -38.2 -36.4 -34.6 -32.8 -39.4 -38.9 -38.3 -37.8 -39 -38 -37 -36 -38.2 -36.4 -34.6 -32.8 -35 -34 -33 -32 -3 -3 1.O -29.2 -27.4 -25.6 -23.8 -37.2 -36.7 -36.1 -35.6 -35.0 -35 -34 -33 -32 -3 -31.0 -29.2 -27.4 -25.6 -23.8 -37.2 -36.7 -36.1 -35.6 -35.0 -35 -34 -33 -32 -3 -3 1.O -29.2 -21.4 -25.6 -23.8 -34.4 -33.9 -33.3 -32.8 -32.2 -30 -29 -28 -27 -26 -22.0 -20.2 -18.4 -16.6 -14.8 -34.4 -33.9 -33.3 -32.8 -32.2 -30 -29 -28 -27 -26 -22.0 -20.2 -18.4 -16.6 -14.8 -34.4 -33.9 -33.3 -32.8 -32.2 -30 -29 -28 -27 -26 -22.0 -20.2 -18.4 -16.6 -14.8 -31.7 -31.1 -30.6 -30.0 -29.4 -25 -24 -23 -22 -2 -13.0 -11.2 -9.4 -7.6 -5.8 -3 1.7 -31.1 -30.6 -30.0 -29.4 -25 -24 -23 -22 -2 -13.0 -11.2 -9.4 -1.6 -5.8 -31.7 -31.1 -30.6 -30.0 -29.4 -25 -24 -23 -22 -2 -13.0 -11.2 -9.4 -7.6 -5.8 -28.9 -28.3 -27.8 -27.2 -26.7 -20 -19 4.0 -28.9 -28.3 -27.8 -27.2 -26.7 -20 -19 -18 -17 -16 4.0 -2.2 4.4 1.4 3.2 -28.9 -28.3 -27.8 -27.2 -26.7 -20 -19 -1 -17 -16 4.0 -2.2 4.4 1.4 3.2 5.0 6.8 8.6 10.4 12.2 -26.1 -25.6 -25.0 -24.4 -23.9 -15 -14 -13 -12 -1 12.2 -26.1 -25.6 -25.0 -24.4 -23.9 -15 -14 -13 -12 -1 5.0 6.8 8.6 10.4 14.0 15.8 17.6 19.4 21.2 -23.3 -22.8 -22.2 -21.7 -21.1 -10 -9 14.0 15.8 17.6 19.4 21.2 -23.3 -22.8 -22.2 -21.7 -21.1 -10 -9 -20.6 -20.0 -19.4 -18.9 -18.3 -5 -3 -2 -1 23.0 24.8 26.6 28.4 30.2 -20.6 -20.0 -19.4 -18.9 -18.3 -5 -3 -2 -1 23.0 24.8 26.6 28.4 30.2 -3 -2 -1 23.0 24.8 26.6 28.4 30.2 O 32.0 -17.8 O 32.0 -17.8 O 32.0 42.8 42.2 -41.7 41.1 40.6 -26.1 -25.6 45 -44 43 -18 -17 -16 -1 -25.0 -14 -1 -24.4 -23.9 -1 -1 -23.3 -22.8 -22.2 -21.7 -21.1 -1 o -9 -20.6 -20.0 -19.4 -18.9 -1 8.3 -5 -17.8 -8 -7 -6 -44 -2.2 4.4 1.4 3.2 5.0 -8 -7 -6 -44 43 -8 -1 -6 6.8 8.6 10.4 12.2 14.0 15.8 17.6 19.4 21.2 Note: This table provides conversion values for temperatures in degrees Fahrenheit and degrees Celsius for each whole degree from -50?to +250? The temperature to be converted is found in the center ?temperature to be converted? column If the temperature to be converted is in degrees Fahrenheit, its equivalent in degrees Celsius is found in the ?degrees Celsius? column to the left If the temperature to be converted is in degrees Celsius, its equivalent in degrees Fahrenheit is found in the ?degrees Fahrenheit? column to the right `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS 48 Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD.API/PETRO MPMS L7-2-ENGL 1999 I0732290 O b L b b b L bbO H Table C-2-Continued Temperatureto Be Converted Degrees Fahrenheit Degrees Celsius Temperature to Be Converted Degrees Fahrenheit Degrees Celsius Temperatureto Be Converted Degrees Fahrenheit 37.8 38.3 38.9 39.4 40.0 100 101 102 103 104 212.0 213.8 215.6 217.4 219.2 65.6 66.1 66.7 67.2 67.8 150 151 152 153 154 302.0 303.8 305.6 307.4 309.2 93.3 93.9 94.4 95.0 95.6 200 201 202 203 204 392.0 393.8 395.6 397.4 399.2 40.6 41.1 41.7 42.2 42.8 105 106 107 108 109 221.0 222.8 224.6 226.4 228.2 68.3 68.9 69.4 70.0 70.6 155 156 157 158 159 311.0 312.8 314.6 316.4 318.2 96.1 96.7 97.2 97.8 98.3 205 206 207 208 209 401.O 402.8 404.6 406.4 408.2 43.3 43.9 44.4 45.0 45.6 110 111 112 113 114 230.0 231.8 233.6 235.4 237.2 71.1 71.7 72.2 72.8 73.3 160 161 162 163 164 320.0 321.8 323.6 325.4 327.2 98.9 99.4 100.0 100.6 101.1 210 21 212 213 214 410.0 411.8 413.6 415.4 417.2 46.1 46.7 47.2 47.8 48.3 115 116 117 118 119 239.0 240.8 242.6 244.4 246.2 73.9 74.4 75.0 75.6 76.1 165 166 167 168 169 329.0 330.8 332.6 334.4 336.2 101.7 102.2 102.8 103.3 103.9 215 216 217 218 219 419.0 420.8 422.6 424.4 426.2 48.9 49.4 50.6 51.1 120 121 122 123 124 248.0 249.8 251.6 253.4 255.2 76.7 77.2 77.8 78.3 78.9 170 171 172 173 174 338.0 339.8 341.6 343.4 345.2 104.4 105.0 105.6 106.1 106.7 220 221 222 223 224 428.0 429.8 431.6 433.4 435.2 51.7 52.2 52.8 53.3 53.9 125 126 127 128 129 257.0 79.4 258.8 80.0 260.6 262.4 264.2 80.6 81.1 81.7 175 176 177 178 179 347.0 348.8 350.6 352.4 354.2 107.2 107.8 108.3 108.9 109.4 225 226 227 228 229 437.0 438.8 440.6 442.4 444.2 54.4 55.0 55.6 56.1 56.7 130 131 132 133 134 266.0 267.8 269.6 271.4 273.2 82.2 82.8 83.3 83.9 84.4 180 181 182 183 184 356.0 357.8 359.6 361.4 363.2 110.0 110.6 111.1 111.7 112.2 230 231 232 233 234 446.0 57.2 57.8 58.3 58.9 59.4 135 136 137 138 139 275.0 276.8 278.6 280.4 282.2 85.0 85.6 86.1 86.7 87.2 185 186 187 188 189 365.0 366.8 368.6 370.4 372.2 112.8 113.3 113.9 114.4 115.0 235 236 237 238 239 455.0 456.8 458.6 460.4 462.2 60.0 60.6 61.1 61.7 62.2 140 141 142 143 144 284.0 87.8 88.3 88.9 89.4 90.0 190 191 192 193 194 374.0 375.8 377.6 379.4 381.2 115.6 116.1 116.7 117.2 117.8 240 24 242 243 244 464.0 465.8 467.6 469.4 471.2 62.8 63.3 63.9 64.4 65.0 145 146 147 148 149 293.0 294.8 296.6 298.4 300.2 90.6 91.1 91.7 92.2 92.8 195 196 197 198 199 383.0 384.8 386.6 388.4 390.2 118.3 118.9 119.4 120.0 120.6 245 246 247 248 249 473.0 474.8 476.6 478.4 480.2 65.6 150 302.0 93.3 200 392.0 121.1 250 482.0 50.0 285.8 287.6 289.4 291.2 447.8 449.6 451.4 453.2 Note: This table provides conversion values for temperatures in degrees Fahrenheit and degrees Celsius for each whole degree from -50” to +250”.The temperature to be convected is found in the center “temperature to be converted” column If the tempture to be converted is in degrees Fahrenheit, its equivalent in degrees Celsius is found in the “degrees Celsius” column to the Left If the temperature to be converted is in degrees Celsius, its equivalent in degrees Fahrenheit is found in the “degrees Fahrenheit” column to the right 49 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Degrees Celsius STDmAPIiPETRO MPMS L7.2-ENGL APPENDIX D-TYPICAL L999 E 0732290 Oblbbh2 5T7 ia PROPERTIES OF CRUDE OILS `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - 51 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Previous page is blank Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD.API/PETRO MPMS L7-2-ENGL 1999 I0732290 0636663 433 II Table D-1-Typical Properties of Crude Oils CAUTION: This table should be used as an informational guide only It was prepared from data contained in “Guide to Export Cmdes,” which was published by the Oil & Gas Journal It is used with their permission Country of Origin Crude Oil Aboozar (Ardeslur) Iran Abu Al Bo Khoosh Abu Dhabi Abu Dhabi Marine (see Umm Shaif) Abu Dhabi Alba UK, North Sea Gravity (“API) Sulfur (Weight) Pour Point (“F) 26.9 31.6 37.4 20.0 2.48 2.00 1.51 1.33 -30.0 -24.5 -30°C -30°C 26.4 36.1 27.9 33.4 37.8 28.5 31.1 1.O6 0.15 2.85 1.79 1.19 2.85 2.48 0.0 35.2 38.0 31.8 29.0 42.3 37.2 16.8 38.6 41.3 27.1 36.8 24.7 33.7 31.1 0.11 0.18 0.20 1.o0 ANS (see Alaska North Slope) Alaskan North Slope (Sadlerochit) USA Amna (high pour) Libya Arabian Heavy (Safaniya) Saudi Arabia Arabian Light Saudi Arabia Arabian Light-Bem Saudi Arabia Arabian Medium-Khursaniyah Saudi Arabia Arabian Medium-ZulufNarjan Saudi Arabia +75.0 -20.0 -30.0 -25.0 -10.0 -20.0 Ardeshir (see Aboozar) Ardjuna Indonesia, Java Argyll UK (North Sea) Arimbi Indonesia Ashtart Tunisia Attaka Indonesia, East Kalimantan Auk UK (North Sea) Bachaquero Venezuela Bach Ho (White Tiger) Viet Nam Badak Indonesia BahrgansadNowruz (Sirip Blend) Iran Barrow Island Australia Basrah Heavy Iraq Basrah Light Iraq Basrah Medium Iraq +75.0 42.8 +100.0 48.2 -10.0 0.09 0.45 2.40 0.03 - 0.05 0.08 2.45 0.05 3.50 1.95 +50.0 -10.0 33°C -15.0 -27.4 -30.0 -22.0 +5.0 2.58 -22.0 Bass Strait (see Gippsland) 1.85 -60.0 UK (North Sea) 23.5 38.7 0.05 +%.O Indonesia, East Kalimantan 40.0 0.08 -5.8 Bekok Malaysia Belayim EUPt 49.1 27.5 210 ppm 2.20 +26.0 42.8 36.5 26.5 39.4 36.7 25.2 10.1 0.42 0.13 O 17 0.12 0.23 5S O - BCF 24 Venezuela Beatrice Bekapai Berri (see Arabian Light) Beryl UK (North Sea) Bintulu Malaysia Bombay High India Bonny Light Nigeria Bonny Medium Nigeria Boscan Venezuela `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS +23.0 +86.0 - -16.6 +50.0 53 Previous page i s blank Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST STD-API/PETRO MPMS L7-2-ENGL L999 0732290 0636664 37T Table D-I-Typical Properties of Crude Oils (Continued) `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Crude Oil Country of Origin Gravity ("API) Sulfur (Weight) Pour Point (OF) Bow River Heavy Canada 26.7 21.0 g/kg -58.0 Brae UK (North Sea) 33.6 0.73 +21.2 Brass River Nigeria 40.9 0.09 +35.0 Brega Libya 40.4 0.2 +30.0 Brent UK (North Sea) 38.2 0.26 +26.6 Brent Blend UK (North Sea) 38.0 0.38 +5 o Bu Attife1 Libya 43.6 0.03 +90.0 Buchan UK (North Sea) 33.7 0.84 +42.8 Bunyu Indonesia, East Kalimantan 31.7 0.09 +60.0 Burgan (Wafra) Divided Zone 23.3 3.37 -5.0 Cabinda Angola (Cabinda) 31.7 0.17 +65.0 Cano Limon Colombia 30.8 0.47 60.0 Ceuta Venezuela 31.8 1.20 -35.0 Champion Export Brunei 23.9 0.12 < -32.8 Cinta Indonesia, Sumatra 33.4 0.08 +105.0 Cold Lake Blend Alberta, Canada 22.6 3.60 -50.0 Cormorant-North UK (North Sea) 34.9 0.71 +53.6 Cormorant-South (Cormorant A) UK (North Sea) 35.7 0.56 +2 1.2 CYNS(Soroosh) Iran 18.1 3.30 -10.0 Dai Hung (Big Bear) Viet Nam 36.9 0.08 Dan Denmark (North Sea) 30.4 0.34 < 45.0 Djeno Blend Congo (Brazzaville) 26.9 0.33 +37.4 Dorrood (Darius) Iran 33.6 2.35 -4.5 Dubai (Fateh) Dubai 31.1 2.00 +15.8 Dukhan (Qatar Land) 41.7 1.28 20.0 Dulang Qatar Malaysia Offshore 39.0 0.037 Dunlin UK (North Sea) 34.9 0.39 42.8 Duri (Sumatran Heavy) Indonesia, Sumatra 21.1 0.20 +54.0 East Zeit Mix Egypt Offshore 39.0 0.89 30.0 Ekofisk Norway (North Sea) 43.4 0.14 +10.0 El Borma Tunisia 36.7 0.37 Emerald U& North Sea 22.0 0.75 -20.0 Eocene (Wafra) Divided Zone 18.6 4.55 -20.0 Escravos Nigeria 36.2 0.14 +10.0 Espoir Ivory coast 31.4 0.32 +5 o Es Sider Libya 36.7 0.37 O Federated Light and Medium Canada (Alberta) 39.8 2.01 g/kg +14.0 Flotta UK (North Sea) 35.7 1.14 +21.0 Forcados Blend Nigeria 29.7 0.29 4.0 Foroozan (Fereidoon) Iran 31.3 2.50 35.0 27°C Daqing (see Taching) 84.0 7.2"C Fereidoon (see Foroozan) 54 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST Crude oil Properties of Crude Oils (Continued) Country of Origin Forties UK (North Sea) Fulmar UK (North Sea) Galeota Mix (Trinidad Blend) Triniad & Tobago Gamba Gabon Gippsland (Bass Strait) Australia Gorm Denmark (North Sea) Gulf Alberta Light and Medium Canada Gulf of Suez Mix Egypt Norway (North Sea) Gullfaks Handil Indonesia, East Kalimantan Hondo Blend california, US Hondo Monterey, California, US Hondo Sandstone California, US Hout Divided Zone ìranian Heavy Iran iranian Light Iran Isthmus Mexico Jabiru Australia Jackson Blend Australia Jatibarang Indonesia, Java Khafji Divided Zone Gravity ("API) Sulfur (Weight) Pour Point (OF) 36.6 39.3 32.8 31.8 45.4 33.9 35.1 31.9 28.6 32.8 20.8 19.4 35.2 32.8 31.0 33.8 32.8 42.3 41.9 29.0 28.5 0.30 0.26 0.27 +26.6 +9.6 -5.0 +73.4 15°C 35.0 17.5 +35.0 0.11 0.10 0.23 9.80 g k g 1.52 0.44 50.0 0.08 +85.0 4.29 4.70 0.21 1.91 1.65 1.35 1.51 -5.0 -20.0 -15.0 0.04 - 0.03 0.07 2.85 - -10.0 25.0 -13.0 -5.0 +110.0 -3 1.O KhursaniyahlAbu Safah (see Arabian Medium) Kirkuk Blend hacl Kittiwake UK, North Sea Kole Marine Blend Cameroon Ku Panik Alaska, US Kuwait Export Kuwait Labuan Blend Malaysia, Sabah Lagomedio Venezuela La Rosa Medium Venezuela 35.1 37.0 34.9 23.0 31.4 33.2 31.5 25.3 Leona Venezuela 24.1 Lloydminster, Alberta & Saskatchewan Canada Loreto Peru Lucina Marine Gabon Magnus UK (North Sea) Mandji Gabon Maureen UK (North Sea) Maya Mexico 20.7 34.0 39.5 39.3 30.5 35.5 22.0 17.4 34.5 36.3 Merey Venezuela Minas (Sumatran Light) Indonesia, Sumatra Miri Light Malaysia Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST 1.97 0.65 0.30 1.76 2.52 917 ppm 1.17 1.73 1S O 31.5 0.29 0.05 0.28 1.10 0.55 3.32 2.20 0.08 825 ppm -7.6 -11.0 +21.2 -50.0 +5.0 +52.0 -15.0 < -50.0 45.0 -32.0"C +34.0 +59.0 +26.6 +37.4 +45.0 0.0 -10.0 +97.0 +34.0 `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Table D-1-Typical STD.API/PETRO MPMS 17.2-ENGL Table D-1-Typical 1979 Properties of Crude Oils (Continued) Country of ûrigin Crude Oil W 0732290 ObLbbbb 142 111 Gravity ("API) Sulfur (Weight) Pour Point ("F) 40.1 0.23 +15.0 UK (North Sea) Mubarek Shaqa, UAE 37.0 0.62 +10.0 Murban Abu Dhabi 40.4 0.78 -1 1.2 Murchison, UK & Norway, North Sea 38.0 0.027 Northwest Shelf Cond Australia 53.1 102 ppm Ninian Blend UK (North Sea) 35.6 0.43 +35.0 Olmeca Mexico 39.8 0.80 -39.0"C Oman Export Oman 36.3 0.79 -15.0 Oriente Ecuador 29.2 1.01 +25 O Oseberg Norway 33.71 0.3 Pennington Nigeria 36.6 0.07 +43.0 pulai Malaysia 42.5 160 ppm +23.0 Qatar Nigeria 35.3 1.57 +10.0 35.8 0.12 A5.0 `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Montrose 7.2"C -36.0"C 40°C Qatar Condensate (see Dukhan) Qatar-Land (see Dukhan) Qatar Marine Qua Rainbow Light and Medium Canada (Alberta) 40.7 5.00 g k g +36.5 Rangeland South Light and Medium Canada (Alberta) 39.5 7.52 g k g 40.0 Rostam Iran 35.9 1.55 8.5 Saharan Blend Algeria 43.7 0.09 < 20.0 Salawati Indonesia 38.0 0.49 -15.0 Salmon (Sassan) Iran 33.9 1.91 Salt Pond Ghana 37.4 0.10 -5.0 - Sanga Sanga Indonesia 25.7 O 17 +5.0 Sarir Libya 38.3 0.18 +25.0 Sassan (Salmon) Iran 33.9 1.91 -5.0 sco Canada 31.4 1500 ppm - Sepinggan-Yakin-Mixed 4: Indonesia, East Kalimantan 31.7 0.11 +20.0 Seria Light Brunei 36.2 0.07 +35.0 Shadah Condensate Shadah, UAE 49.7 0.10 -25.0 Shengli People's Republic of China 24.2 1.00 +70.0 Sirri Iran 30.9 2.30 +15.8 Sirtica Libya 43.3 0.43 +26.6 Soroosh (Cyrus) Iran 18.1 3.30 Souedie Syria 24.9 3.82 -22.0 Soviet Export Blend USSR 32.5 1.38 -9.4 Soyo Blend Angola 33.1 0.23 44.4 Statfjord Norway, UX (North Sea) 38.4 0.27 AO.0 Sadierochit (see Alaska North Slope) Safaniya (see Arabian Heavy) SIRIP Blend (see BahrgansadNowruz) Sumatran Heavy (see Duri) 56 Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST 10.0 STD=API/PETRO MPMS L7-2-ENGL 3999 0732290 O b L b b b O89 Table D-1-Typical Properties of Crude Oils (Continued) Country of Origin Gravity (“API) Sulfur (Weight) Taching (Daqing) People’s Republic of China 33.0 0.08 +95.0 Cnide Oil Pour Point (“F) Sumatran Light (see Minas) Tapis Malaysia 44.3 230 ppm +39.0 Tartan UK (North Sea) 41.7 0.56 +16.0 Ternbungo Malaysia, Sabah 37.4 0.04 +25.0 Thistle UK (North Sea) 37.0 0.3 +53.6 Tia Juana Light Venezuela 32.1 1.10 -45 o Tia Juana Heavy Venezuela 12.1 2.70 +30.0 -5 o Trinidad Blend (Galeota Mix) Trinidad 32.8 0.27 U h g Indonesia 38.0 0.05 100.0 Umm Shaif (Abu Dhabi Marine) Abu Dhabi 37.4 1.51 22.0 Wainwright-Kinsella Alberta, Canada 23.1 15.80 Walio Indonesia 34.1 - - West S a k Alaska, US 22.4 1.82 -50.0 Zaire Zaire 31.7 0.13 +80.0 Wafra (see Burgan & Eocene) -39.0 Zakum @wer Zakud Abu Dhabi Marine) Abu Dhabi 40.6 1.O5 5.8 Zarzaitine (El Borna) Algeria 43 O 0.07 +10.4 Zueitina Libya 41.3 0.28 +45.o Zuluf/Madan (see Arabian Medium) `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS 57 Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST The American Petroleum Institute provides additional resources and programs to industry which are based on API Standards For more information, contact: `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Training and Seminars Ph: 202-682-8490 Fax: 202-682-8222 Inspector Certification Programs Ph: 202-682-8161 Fax: 202-962-4739 American Petroleum Institute Quality Registrar Ph: 202-962-4791 FU: 202-682-8070 Monogram Licensing Program Ph: 202-962-4791 FU: 202-682-8070 Engine Oil Licensing and Certification System Ph: 202-682-8233 Fax: 202-962-4739 Petroleum Test Laboratory Accreditation Program Ph: 202-682-8064 Fax: 202-362-4739 In addition, petroleum industry techcal, patent, and business information is available online through API EnCompass” Call 12-366-4040 or fax 12-366-4298 to discover more To obtain a free copy of the API Publications, Programs, and Services Catalog, call 202-682-8375 or fax your request to 202-362-4776 Or see the online interactive version of the catalog on our Vorld Wide Web site http ://m api.org Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST 1T)1 American Petroleum Institute Helping You G e t Th5 Job Done Right - Additional copies available from API Publications and Distribution: (202) 682-8375 Information about API Publications, Programs and Services is available on the World Wide Web at: http://www.api.org American Petroleum Institute 1220 L Street, Northwest Washington, D.C 20005-4070 202-682-8000 `,,,,,``,`,,,`,,,`,```,-`-`,,`,,`,`,,` - Copyright American Petroleum Institute Provided by IHS under license with API No reproduction or networking permitted without license from IHS Licensee=Technip Abu Dabhi/5931917101 Not for Resale, 02/22/2006 01:32:46 MST Order No H I 7022