ASTM D2892-03a
(Test Method)Standard Test Method for Distillation of Crude Petroleum (15-Theoretical Plate Column)
Standard Test Method for Distillation of Crude Petroleum (15-Theoretical Plate Column)
SCOPE
1.1 This test method covers the procedure for the distillation of stabilized crude petroleum (see Note 1) to a final cut temperature of 400°C Atmospheric Equivalent Temperature (AET). This test method employs a fractionating column having an efficiency of 14 to 18 theoretical plates operated at a reflux ratio of 5:1. Performance criteria for the necessary equipment is specified. Some typical examples of acceptable apparatus are presented in schematic form. This test method offers a compromise between efficiency and time in order to facilitate the comparison of distillation data between laboratories.
Note 1—Defined as having a Reid vapor pressure less than 82.7 kPa (12 psi).
1.2 This test method details procedures for the production of a liquefied gas, distillate fractions, and residuum of standardized quality on which analytical data can be obtained, and the determination of yields of the above fractions by both mass and volume. From the preceding information, a graph of temperature versus mass % distilled can be produced. This distillation curve corresponds to a laboratory technique, which is defined at 15/5 (15 theoretical plate column, 5:1 reflux ratio) or TBP (true boiling point).
1.3 This test method can also be applied to any petroleum mixture except liquefied petroleum gases, very light naphthas, and fractions having initial boiling points above 400°C.
1.4 This test method contains the following annexes and appendixes:
1.4.1 Annex A1—Test Method for the Determination of the Efficiency of a Distillation Column,
1.4.2 Annex A2—Test Method for the Determination of the Dynamic Holdup of a Distillation Column,
1.4.3 Annex A3—Test Method for the Determination of the Heat Loss in a Distillation Column (Static Conditions),
1.4.4 Annex A4—Test Method for the Verification of Temperature Sensor Location,
1.4.5 Annex A5—Test Method for Determination of the Temperature Response Time,
1.4.6 Annex A6—Practice for the Calibration of Sensors,
1.4.7 Annex A7—Test Method for the Verification of Reflux Dividing Valves,
1.4.8 Annex A8—Practice for Conversion of Observed Vapor Temperature to Atmospheric Equivalent Temperature (AET),
1.4.9 Appendix X1—Test Method for Dehydration of a Sample of Wet Crude Oil, and
1.4.10 Appendix X2—Practice for Performance Check.
1.5 The values stated in SI units are to be regarded as standard. The values given in parentheses are provided for information only.
1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use. For specific warning statements, see Section 10.
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An American National Standard
Designation: D 2892 – 03a
Standard Test Method for
Distillation of Crude Petroleum (15-Theoretical Plate
1
Column)
This standard is issued under the fixed designation D2892; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision.Anumber in parentheses indicates the year of last reapproval.A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
1. Scope* 1.4.5 Annex A5—Test Method for Determination of the
Temperature Response Time,
1.1 Thistestmethodcoverstheprocedureforthedistillation
1.4.6 Annex A6—Practice for the Calibration of Sensors,
of stabilized crude petroleum (see Note 1) to a final cut
1.4.7 AnnexA7—TestMethodfortheVerificationofReflux
temperature of 400°C Atmospheric Equivalent Temperature
Dividing Valves,
(AET). This test method employs a fractionating column
1.4.8 Annex A8—Practice for Conversion of Observed
having an efficiency of 14 to 18 theoretical plates operated at a
Vapor Temperature to Atmospheric Equivalent Temperature
reflux ratio of 5:1. Performance criteria for the necessary
(AET),
equipment is specified. Some typical examples of acceptable
1.4.9 Appendix X1—Test Method for Dehydration of a
apparatus are presented in schematic form. This test method
Sample of Wet Crude Oil, and
offers a compromise between efficiency and time in order to
1.4.10 Appendix X2—Practice for Performance Check.
facilitate the comparison of distillation data between laborato-
1.5 The values stated in SI units are to be regarded as
ries.
standard. The values given in parentheses are provided for
NOTE 1—Defined as having a Reid vapor pressure less than 82.7 kPa
information only.
(12 psi).
1.6 This standard does not purport to address all of the
1.2 Thistestmethoddetailsproceduresfortheproductionof
safety concerns, if any, associated with its use. It is the
a liquefied gas, distillate fractions, and residuum of standard-
responsibility of the user of this standard to establish appro-
ized quality on which analytical data can be obtained, and the
priate safety and health practices and determine the applica-
determinationofyieldsoftheabovefractionsbybothmassand
bility of regulatory limitations prior to use. For specific
volume. From the preceding information, a graph of tempera-
warning statements, see Section 10.
ture versus mass % distilled can be produced. This distillation
2. Referenced Documents
curve corresponds to a laboratory technique, which is defined
at 15/5 (15 theoretical plate column, 5:1 reflux ratio) or TBP
2.1 ASTM Standards:
(true boiling point).
D941 Test Method for Density and Relative Density (Spe-
1.3 This test method can also be applied to any petroleum
cific Gravity) of Liquids by Lipkin Bicapillary Pycnom-
2
mixture except liquefied petroleum gases, very light naphthas,
eter
and fractions having initial boiling points above 400°C.
D1217 Test Method for Density and Relative Density
1.4 This test method contains the following annexes and
(Specific Gravity) of Liquids by Bingham Pycnometer
appendixes:
D1298 TestMethodforDensity,RelativeDensity(Specific
1.4.1 AnnexA1—Test Method for the Determination of the
Gravity), or API Gravity of Crude Petroleum and Liquid
Efficiency of a Distillation Column,
Petroleum Products by Hydrometer Method
1.4.2 AnnexA2—Test Method for the Determination of the
D2427 Test Method for Determination of C through C
2 5
Dynamic Holdup of a Distillation Column,
Hydrocarbons in Gasolines by Gas Chromatography
1.4.3 AnnexA3—Test Method for the Determination of the
D2887 Test Method for Boiling Range Distribution of
Heat Loss in a Distillation Column (Static Conditions),
Petroleum Fractions by Gas Chromatography
1.4.4 AnnexA4—Test Method for the Verification of Tem-
D3710 Test Method for Boiling Range Distribution of
perature Sensor Location,
Gasoline and Gasoline Fractions by Gas Chromatography
D4006 Test Method for Water in Crude Oil by Distillation
D4052 Test Method for Density and Relative Density of
Liquids by Digital Density Meter
1
This test method is under the jurisdiction of ASTM Committee D02 on
PetroleumProductsandLubricantsandisthedirectresponsibilityofSubcommittee
D02.08 on Volatility.
Current edition approved Nov. 1, 2003. Published November 2003. Originally
2
approved in 1970. Last previous edition approved in 2003 as D2892–03. Withdrawn.
*A Summary of Changes section appears at the end of this standard.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.
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D 2892 – 03a
D4057 Practice for Manual Sampling of Petroleum and distillation rate up to the flood point and varies from one kind
Petroleum Products of fractionator to another.
D4177
...
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