Standard Test Method for Determination of Vapor Pressure of Crude Oil: VPCR<sub>x</sub> (Expansion Method)

SCOPE
1.1 This test method covers the use of automated vapor pressure instruments to determine the vapor pressure of crude oils at temperatures between 5 and 80 °C for vapor-liquid ratios from 4:1 to 0.02:1 (X= 4 to 0.02) and pressures from 7 to 500 kPa (1.0 to 70 psi).
1.2 The values stated in SI units are regarded as standard. The inch-pound units given in parentheses are provided for information only.
1.3 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 Note 5.

General Information

Status
Historical
Publication Date
09-Jan-1999
Current Stage
Ref Project

Relations

Buy Standard

Standard
ASTM D6377-99 - Standard Test Method for Determination of Vapor Pressure of Crude Oil: VPCR<sub>x</sub> (Expansion Method)
English language
5 pages
sale 15% off
Preview
sale 15% off
Preview

Standards Content (Sample)

NOTICE: This standard has either been superseded and replaced by a new version or withdrawn.
Contact ASTM International (www.astm.org) for the latest information
An American National Standard
Designation: D 6377 – 99
Standard Test Method for
Determination of Vapor Pressure of Crude Oil: VPCR
x
1
(Expansion Method)
This standard is issued under the fixed designation D 6377; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
1. Scope 3.1.1 dead crude oil—a term usually employed for crude
oils that, when exposed to normal atmospheric pressure at
1.1 This test method covers the use of automated vapor
room temperature, will not result in actual boiling of the
pressure instruments to determine the vapor pressure of crude
sample.
oils at temperatures between 5 and 80°C for vapor-liquid ratios
3.1.1.1 Discussion—Sampling and handling of dead crude
from 4:1 to 0.02:1 (X=4to 0.02) and pressures from 7 to 500
oils can usually be done without problems in normal sample
kPa (1.0 to 70 psi).
containers, such as cans and so forth. The use of pressure
1.2 The values stated in SI units are regarded as standard.
cylinders for (sub)sampling and sample storage is a necessary
The inch-pound units given in parentheses are provided for
and mandatory requirement in this test method for live crude
information only.
oils and, to prevent the loss of volatile material and preserve
1.3 This standard does not purport to address all of the
precision, is strongly recommended for dead crude oils as well.
safety concerns, if any, associated with its use. It is the
3.1.2 live crude oil—a term usually employed for crude oils
responsibility of the user of this standard to establish appro-
contained in pressurized systems that, when brought to normal
priate safety and health practices and determine the applica-
atmospheric pressure at room temperature, will result in actual
bility of regulatory limitations prior to use. For specific
boiling of the sample.
warning statements, see Note 5.
3.1.2.1 Discussion—Sampling and handling of samples of
2. Referenced Documents
live crude oils will necessitate the use of pressure cylinders and
preclude the use of normal sample containers, such as cans and
2.1 ASTM Standards:
so forth.
D 323 Test Method for Vapor Pressure of Petroleum Prod-
2
3.1.3 REID vapor pressure equivalent (RVPE)— a value
ucts (REID Method)
calculated by a correlation equation (see 14.3) from VPCR ,
D 1160 Test Method for Distillation of Petroleum Products 4
2
which is related to the value obtained on the sample by Test
at Reduced Pressure
Method D 323.
D 3700 Practice for Containing Hydrocarbon Fluid Samples
3
3.1.4 vapor-liquid ratio (V/L), n—the ratio of the vapor
Using a Floating Piston Cylinder
volume to the liquid specimen volume.
D 4057 Practice for Manual Sampling of Petroleum and
3
3.1.4.1 Discussion—The total measuring chamber volume
Petroleum Products
is the sum of the vapor volume and the liquid specimen
D 4177 Practice for Automatic Sampling of Petroleum and
3
volume.
Petroleum Products
3.1.5 vapor pressure of crude oil (VPCR , n—the pressure
D 5191 Test Method for Vapor Pressure of Petroleum Prod- x)
3
exerted in an evacuated chamber at a vapor-liquid ratio of X:1
ucts (Mini Method)
4
by conditioned or unconditioned crude oil, which may contain
D 5853 Test Method for Pour Point of Crude Oils
gas, air or water, or a combination thereof, where X may vary
3. Terminology
from 4 to 0.02.
3.1 Definitions of Terms Specific to This Standard:
4. Summary of Test Method
4.1 Employing a measuring chamber with a built-in piston,
1
This test method is under the jurisdiction of ASTM Committee D-2 on
a sample of known volume is drawn from a pressurized
Petroleum Products and Lubricants and is the direct responsibility of Subcommittee
sampling system (floating piston cylinder) into the temperature
D02.08 on Volatility.
controlled chamber at 20°C or higher. After sealing the
Current edition approved Jan. 10, 1999. Published March 1999.
2
Annual Book of ASTM Standards, Vol 05.01. chamber, the volume is expanded by moving the piston until
3
Annual Book of ASTM Standards, Vol 05.02.
4
Annual Book of ASTM Standards, Vol 05.03.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.
1

---------------------- Page: 1 ----------------------
D6377–99
Measuring chambers exceedinga5mL capacity and having a different
the final volume produces the desired V/L value. The tempera-
design can be used, but the precision and bias statements (see Section 14)
ture of the measuring chamber is then regulated to the
are not known to apply.
measuring temperature.
6.1.2 The pressure transducer shall have a minimum opera-
4.2 After temperature and pressure equi
...

Questions, Comments and Discussion

Ask us and Technical Secretary will try to provide an answer. You can facilitate discussion about the standard in here.