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API MPM CH11.2.4:2007

Superseded

Superseded

A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

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MANUAL OF PETROLEUM MEASUREMENT STANDARDS - CHAPTER 11 - PHYSICAL PROPERTIES DATA - SECTION 2 - PART 4 - TEMPERATURE CORRECTION FOR THE VOLUME OF NGL AND LPG TABLES 23E, 24E, 53E, 95E, AND 60E

Available format(s)

Hardcopy , PDF

Superseded date

18-10-2018

Language(s)

English

Published date

01-01-2012

€188.44
Excluding VAT

Foreword
API Special Notes
ASTM Note
GPA Disclaimer
Table of Contents
Nomenclature
1 Introduction
2 Scope
3 Significant Digits
4 Comparison to the Previous Standard
5 Implementation Procedures
  5.1 CTL (Table 24) and Relative Density (Table 23) for NGL and
      LPG using a 60 degrees F Base Temperature
      5.1.1 Implementation Procedure for Table 24E
            (60 degrees F Basis)
            5.1.1.1 Inputs and Outputs
            5.1.1.2 Outline of Calculations
            5.1.1.3 T24 Implementation Procedure
            5.1.1.4 Examples for Section 5.1.1 (Table 24E)
      5.1.2 Implementation Procedure for Table 23E (60 degrees
            F Basis)
            5.1.2.1 Inputs and Outputs
            5.1.2.2 Outline of Calculations
            5.1.2.3 T23 Implementation Procedure
            5.1.2.4 Examples for Section 5.1.2 (Table 23E)
  5.2 CTL (Table 54) and Density (Table 53) for NGL and LPG using
      a 15 degrees C Base Temperature
      5.2.1 Implementation Procedure for Table 54E (15 degrees C
            Basis)
            5.2.1.1 Inputs and Outputs
            5.2.1.2 Outline of Calculations
            5.2.1.3 T54 Implementation Procedure
            5.2.1.4 Examples for Section 5.2.2 (Table 54E)
      5.2.2 Implementation Procedure for Table 53E (15 degrees C
            Basis)
            5.2.2.1 Inputs and Outputs
            5.2.2.2 Outline of Calculations
            5.2.2.3 T53 Implementation Procedure
            5.2.2.4 Examples for Section 5.2.2 (Table 53E)
  5.3 CTL (Table 60) and Density (Table 59) for NGL and LPG using a
      20 degrees C Base Temperature
      5.3.1 Implementation Procedure for Table 60E (20 degrees C
            Basis)
            5.3.1.1 Inputs and Outputs
            5.3.1.2 Outline of Calculations
            5.3.1.3 T60 Implementation Procedure
            5.3.1.4 Examples for Section 5.3.1 (Table 60)
      5.3.2 Implementation Procedure for Table 59E (20 degrees C
            Basis)
            5.3.2.1 Inputs and Outputs
            5.3.2.2 Outline of Calculations
            5.3.2.3 T59 Implementation Procedure
            5.3.2.4 Examples for Section 5.3.2 (Table 59E)
6 Sample Sections of Printed Tables
7 References

Describes a 60 degrees F relative density range of 0,3500 to 0,6880 which normally equates to a density at 15 degrees C of 351.7 to 687.8 kg/m[3] and a density at 20 degrees c of 331.7 TO 683.6 kg/m[3].

DevelopmentNote
Also numbered as GPA TP-27 & ASTM PETROLTBL-TP27. (10/2007)
DocumentType
Standard
Pages
162
ProductNote
Reconfirmed 2007
PublisherName
American Petroleum Institute
Status
Superseded
SupersededBy

GPA 2142 : 1957 STANDARD FACTORS FOR VOLUME CORRECTION AND SPECIFIC GRAVITY CONVERSION OF LIQUEFIED PETROLEUM GASES
API MPMS CH11.2.1 : 1984 MANUAL OF PETROLEUM MEASUREMENT STANDARDS - COMPRESSIBILITY FACTORS FOR HYDROCARBONS: 0-90 DEGREES API GRAVITY RANGE
API MPM CH11.2.1M : 1984 MANUAL OF PETROLEUM MEASUREMENT STANDARDS - COMPRESSIBILITY FACTORS FOR HYDROCARBONS: 638-1074 KILOGRAMS PER CUBIC METER RANGE

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