Standard Test Method for Determination of the Asphaltene Solvency Properties of Bitumen, Crude Oil, Condensate and/or Related Products for the Purpose of Calculating Stability, Compatibility for Blending, Fouling, and Processibility (Manual Microscopy Method)

SIGNIFICANCE AND USE
5.1 Understanding the stability and compatibility of a petroleum product (crude oil or refinery stream, or both) is critical to facilities that receive multiple types of products and perform blending and processing operations. Blending incompatible streams can cause asphaltene precipitation with potential consequences such as but not limited to: refinery unit fouling, processing problems, throughput reduction, emulsion stabilization, pipeline and tank deposition, and equipment fouling.  
5.2 The ability to predict the results of blending operations allows operators to anticipate potential problems and mitigate those problems prior to receiving the products. It also helps facilities to manage their product movements in the most effective manner to avoid future issues.  
5.3 Some petroleum products are unstable without blending and understanding the stability of a product in terms of asphaltene precipitation is an important factor in product selection for refining. Products with poor stability can contribute to refinery unit fouling as well as the overall processibility and yield of that product.
SCOPE
1.1 This test method covers the use of a basic microscope to determine the asphaltene solvency properties of bitumen, crude oil, condensate or related products, or the combinations thereof. These properties can be used to calculate the solubility parameters required to calculate and predict asphaltene stability for blending purposes, refinery unit fouling, processibility, emulsion stabilization, pipeline and tank deposition, and equipment fouling. If the solubility properties are known for two products, then the compatibility of potential blend ratios can be predicted.  
1.2 This test method is limited to products that allow handling at atmospheric pressure and room temperature conditions without a significant loss of light end components. Loss of light ends will result in changes in the solubility properties of the product and may alter or bias the results, or both. Samples with vapor pressures (VPCR4 at 37.8 °C using Test Method D6377) greater than 100 kPa are not suitable for use with this test method.  
1.3 This test method is primarily suited to products that are freely flowing at test conditions. Samples that are too viscous to flow at test conditions, such as semi-solids, may need to be heated to allow handling (See Annex A1.)  
1.4 The values stated in SI units are to be regarded as standard. The values given in parentheses after SI units are provided for information only and are not considered standard.  
1.5 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use.  
1.6 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

General Information

Status
Published
Publication Date
31-Dec-2020

Relations

Effective Date
01-Oct-2015
Effective Date
01-Oct-2014
Effective Date
15-Apr-2012
Effective Date
01-Oct-2010
Effective Date
01-Jul-2008
Effective Date
01-Nov-2005
Effective Date
01-Dec-2003
Effective Date
10-Jun-2000
Effective Date
10-Jan-1999

Overview

ASTM D8253-21, “Standard Test Method for Determination of the Asphaltene Solvency Properties of Bitumen, Crude Oil, Condensate and/or Related Products for the Purpose of Calculating Stability, Compatibility for Blending, Fouling, and Processibility (Manual Microscopy Method),” establishes a laboratory methodology using microscopy to assess the solvency characteristics of asphaltenes in various petroleum products. Understanding asphaltene stability and compatibility is vital for refinery operations, product handling, and efficient pipeline and storage management, as asphaltene precipitation can cause process disruptions, fouling, or deposition issues.

This standard, published by ASTM International and developed by Committee D02 on Petroleum Products, Liquid Fuels, and Lubricants, provides procedures for the manual microscopic determination of asphaltene solvency, offering predictive capabilities for product stability and blend compatibility. This test method covers bitumen, crude oil, condensates, and related products that can be safely tested under atmospheric pressure and room temperature conditions.

Key Topics

  • Asphaltene Stability and Compatibility: The method supports evaluation of how petroleum products react during blending, addressing potential for asphaltene precipitation.
  • Manual Microscopy Analysis: It describes using standard laboratory microscopes at 80x-200x magnification, with cross-polarization, to observe asphaltene behavior during solvent addition.
  • Sample Applicability: Suitable for freely flowing samples at room temperature. Semi-solids may require gentle heating. Not applicable to highly volatile samples with vapor pressure (VPCR4 at 37.8°C) over 100 kPa.
  • Blending Predictability: By measuring solvency parameters, facilities can predict blend compatibility and stability, optimizing product movements and refining processes.
  • Minimizing Fouling and Deposition: Early detection and quantification of asphaltene precipitation helps mitigate refinery fouling, throughput loss, emulsion formation, and deposition in pipelines and tanks.
  • Safety Guidance: Users are responsible for adhering to all safety, health, and environmental regulations when handling petroleum samples and solvents.

Applications

ASTM D8253-21 delivers practical value at multiple points within the oil and gas industry:

  • Oil Refineries: Enables engineers to predict and avoid compatibility issues when blending different crude oils or refinery streams, thereby minimizing fouling and process upsets.
  • Blending Operations: Supports the selection of stable blend ratios, reducing asphaltene precipitation incidents.
  • Pipeline and Storage Facilities: Provides insights into asphaltene stability, aiding in preventing undesirable deposit build-up and transport blockages.
  • Product Quality Control: Facilitates routine testing of bitumen, crude oil, and condensate, ensuring that only stable, processible products proceed to downstream units.
  • Research and Development: Laboratories involved in product development can use the method to characterize new crude streams or evaluate the benefits of additives and diluents.
  • Operational Planning: Refiners and terminal operators can plan product movement, storage, or blending operations with enhanced confidence, lowering operational risks and increasing throughput efficiency.

Related Standards

Several ASTM and industry standards are closely associated with the objectives and methodologies described in ASTM D8253-21:

  • ASTM D6560: Test Method for Determination of Asphaltenes (Heptane Insolubles) in Crude Petroleum and Petroleum Products.
  • ASTM D6377: Test Method for Determination of Vapor Pressure of Crude Oil: VPCR (Expansion Method).
  • ASTM D7157: Test Method for Calculating Viscosity of Blended Crude Oils.
  • API MPMS: Manual of Petroleum Measurement Standards - various methods for crude oil and bitumen testing.

Summary

ASTM D8253-21 is an essential laboratory standard for the petroleum sector, providing a rigorous, practical method for determining asphaltene solvency in bitumen, crude oil, and condensates. Its use enables better control of product quality, operational efficiency, and safety, by empowering refiners, blenders, and transporters to anticipate and manage asphaltene precipitation, fouling, and compatibility issues. By integrating this manual microscopy method, organizations gain valuable predictive capability for blend stability, enhancing both reliability and profitability in petroleum processing and logistics.

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ASTM D8253-21 - Standard Test Method for Determination of the Asphaltene Solvency Properties of Bitumen, Crude Oil, Condensate and/or Related Products for the Purpose of Calculating Stability, Compatibility for Blending, Fouling, and Processibility (Manual Microscopy Method)

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Frequently Asked Questions

ASTM D8253-21 is a standard published by ASTM International. Its full title is "Standard Test Method for Determination of the Asphaltene Solvency Properties of Bitumen, Crude Oil, Condensate and/or Related Products for the Purpose of Calculating Stability, Compatibility for Blending, Fouling, and Processibility (Manual Microscopy Method)". This standard covers: SIGNIFICANCE AND USE 5.1 Understanding the stability and compatibility of a petroleum product (crude oil or refinery stream, or both) is critical to facilities that receive multiple types of products and perform blending and processing operations. Blending incompatible streams can cause asphaltene precipitation with potential consequences such as but not limited to: refinery unit fouling, processing problems, throughput reduction, emulsion stabilization, pipeline and tank deposition, and equipment fouling. 5.2 The ability to predict the results of blending operations allows operators to anticipate potential problems and mitigate those problems prior to receiving the products. It also helps facilities to manage their product movements in the most effective manner to avoid future issues. 5.3 Some petroleum products are unstable without blending and understanding the stability of a product in terms of asphaltene precipitation is an important factor in product selection for refining. Products with poor stability can contribute to refinery unit fouling as well as the overall processibility and yield of that product. SCOPE 1.1 This test method covers the use of a basic microscope to determine the asphaltene solvency properties of bitumen, crude oil, condensate or related products, or the combinations thereof. These properties can be used to calculate the solubility parameters required to calculate and predict asphaltene stability for blending purposes, refinery unit fouling, processibility, emulsion stabilization, pipeline and tank deposition, and equipment fouling. If the solubility properties are known for two products, then the compatibility of potential blend ratios can be predicted. 1.2 This test method is limited to products that allow handling at atmospheric pressure and room temperature conditions without a significant loss of light end components. Loss of light ends will result in changes in the solubility properties of the product and may alter or bias the results, or both. Samples with vapor pressures (VPCR4 at 37.8 °C using Test Method D6377) greater than 100 kPa are not suitable for use with this test method. 1.3 This test method is primarily suited to products that are freely flowing at test conditions. Samples that are too viscous to flow at test conditions, such as semi-solids, may need to be heated to allow handling (See Annex A1.) 1.4 The values stated in SI units are to be regarded as standard. The values given in parentheses after SI units are provided for information only and are not considered standard. 1.5 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.6 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

SIGNIFICANCE AND USE 5.1 Understanding the stability and compatibility of a petroleum product (crude oil or refinery stream, or both) is critical to facilities that receive multiple types of products and perform blending and processing operations. Blending incompatible streams can cause asphaltene precipitation with potential consequences such as but not limited to: refinery unit fouling, processing problems, throughput reduction, emulsion stabilization, pipeline and tank deposition, and equipment fouling. 5.2 The ability to predict the results of blending operations allows operators to anticipate potential problems and mitigate those problems prior to receiving the products. It also helps facilities to manage their product movements in the most effective manner to avoid future issues. 5.3 Some petroleum products are unstable without blending and understanding the stability of a product in terms of asphaltene precipitation is an important factor in product selection for refining. Products with poor stability can contribute to refinery unit fouling as well as the overall processibility and yield of that product. SCOPE 1.1 This test method covers the use of a basic microscope to determine the asphaltene solvency properties of bitumen, crude oil, condensate or related products, or the combinations thereof. These properties can be used to calculate the solubility parameters required to calculate and predict asphaltene stability for blending purposes, refinery unit fouling, processibility, emulsion stabilization, pipeline and tank deposition, and equipment fouling. If the solubility properties are known for two products, then the compatibility of potential blend ratios can be predicted. 1.2 This test method is limited to products that allow handling at atmospheric pressure and room temperature conditions without a significant loss of light end components. Loss of light ends will result in changes in the solubility properties of the product and may alter or bias the results, or both. Samples with vapor pressures (VPCR4 at 37.8 °C using Test Method D6377) greater than 100 kPa are not suitable for use with this test method. 1.3 This test method is primarily suited to products that are freely flowing at test conditions. Samples that are too viscous to flow at test conditions, such as semi-solids, may need to be heated to allow handling (See Annex A1.) 1.4 The values stated in SI units are to be regarded as standard. The values given in parentheses after SI units are provided for information only and are not considered standard. 1.5 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, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.6 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

ASTM D8253-21 is classified under the following ICS (International Classification for Standards) categories: 91.100.50 - Binders. Sealing materials. The ICS classification helps identify the subject area and facilitates finding related standards.

ASTM D8253-21 has the following relationships with other standards: It is inter standard links to ASTM D6377-15, ASTM D6377-14, ASTM D6560-12, ASTM D6377-10, ASTM D6377-08, ASTM D6560-00(2005), ASTM D6377-03, ASTM D6560-00, ASTM D6377-99. Understanding these relationships helps ensure you are using the most current and applicable version of the standard.

ASTM D8253-21 is available in PDF format for immediate download after purchase. The document can be added to your cart and obtained through the secure checkout process. Digital delivery ensures instant access to the complete standard document.

Standards Content (Sample)


This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the
Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
Designation: D8253 − 21
Standard Test Method for
Determination of the Asphaltene Solvency Properties of
Bitumen, Crude Oil, Condensate and/or Related Products
for the Purpose of Calculating Stability, Compatibility for
Blending, Fouling, and Processibility (Manual Microscopy
Method)
This standard is issued under the fixed designation D8253; 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 (´) indicates an editorial change since the last revision or reapproval.
1. Scope* 1.6 This international standard was developed in accor-
dance with internationally recognized principles on standard-
1.1 Thistestmethodcoverstheuseofabasicmicroscopeto
ization established in the Decision on Principles for the
determinetheasphaltenesolvencypropertiesofbitumen,crude
Development of International Standards, Guides and Recom-
oil, condensate or related products, or the combinations
mendations issued by the World Trade Organization Technical
thereof.Thesepropertiescanbeusedtocalculatethesolubility
Barriers to Trade (TBT) Committee.
parameters required to calculate and predict asphaltene stabil-
ity for blending purposes, refinery unit fouling, processibility,
2. Referenced Documents
emulsionstabilization,pipelineandtankdeposition,andequip-
ment fouling. If the solubility properties are known for two 2.1 ASTM Standards:
products,thenthecompatibilityofpotentialblendratioscanbe
D6560Test Method for Determination ofAsphaltenes (Hep-
predicted. tane Insolubles) in Crude Petroleum and Petroleum Prod-
ucts
1.2 This test method is limited to products that allow
D6377Test Method for Determination of Vapor Pressure of
handling at atmospheric pressure and room temperature con-
Crude Oil: VPCR (Expansion Method)
x
ditionswithoutasignificantlossoflightendcomponents.Loss
of light ends will result in changes in the solubility properties
3. Terminology
of the product and may alter or bias the results, or both.
Samples with vapor pressures (VPCR at 37.8°C using Test
3.1 Definitions:
Method D6377) greater than 100kPa are not suitable for use
3.1.1 asphaltenes, n—(rarely used in the singular), in pe-
with this test method.
troleum technology, represent an oil fraction that is soluble in
a specified aromatic solvent but separates upon the addition of
1.3 This test method is primarily suited to products that are
an excess of a specified paraffinic solvent.
freely flowing at test conditions. Samples that are too viscous
3.1.1.1 Discussion—Asphaltenes are found largely in crude
to flow at test conditions, such as semi-solids, may need to be
oils and in heavy fuel oils containing residual fractions. They
heated to allow handling (See Annex A1.)
are insoluble in alkanes such as heptane and pentane, but
1.4 The values stated in SI units are to be regarded as
soluble in aromatic solvents such as benzene or toluene.
standard. The values given in parentheses after SI units are
3.1.2 compatibility, n—of crude oils or heavy fuel oils, the
provided for information only and are not considered standard.
ability of two or more crude oils or fuel oils to blend together
1.5 This standard does not purport to address all of the
within certain concentration ranges without evidence of
safety concerns, if any, associated with its use. It is the
separation, such as the formation of multiple phases.
responsibility of the user of this standard to establish appro-
3.1.2.1 Discussion—Incompatible heavy fuel oils or crude
priate safety, health, and environmental practices and deter-
oils, when mixed or blended, result in flocculation or precipi-
mine the applicability of regulatory limitations prior to use.
tation of asphaltenes. Some oils may be compatible within
This test method is under the jurisdiction of ASTM Committee D02 on
Petroleum Products, Liquid Fuels, and Lubricants and is the direct responsibility of
Subcommittee D02.14 on Stability, Cleanliness and Compatibility of Liquid Fuels. For referenced ASTM standards, visit the ASTM website, www.astm.org, or
Current edition approved Jan. 1, 2021. Published January 2021. Originally contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM
approved in 2020. Last previous edition approved in 2020 as D8253–20. DOI: Standards volume information, refer to the standard’s Document Summary page on
10.1520/D8253-21. the ASTM website.
*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
D8253 − 21
certain concentration ranges in specific mixtures, but incom- 4. Summary of Test Method
patible outside those ranges.
4.1 The sample type is first determined as either “with
3.1.3 crude oil, n—a naturally occurring hydrocarbon asphaltenes” or “without asphaltenes” to identify if it is a
mixture, generally in a liquid state, which may also include
source of asphaltenes or not. If the sample type is “without
compounds of sulfur, nitrogen, oxygen, metals and other asphaltenes” then a second test is performed to establish if the
elements (Synonym – crude petroleum, crude).
solvency of the sample is similar in behavior to either toluene
orheptane.Thesampleiscontactedwithareferenceoilknown
3.1.4 flocculation, n—of asphaltenes from crude oils or
to contain asphaltenes. If the reference oil contacted with the
heavy fuel oils, the aggregation of colloidally dispersed as-
sample results in the precipitation of asphaltenes, then it is
phaltenes into visibly larger masses which may or may not
considered similar to heptane (low solvency). If the reference
settle.
oil contacted with the sample does not result in the precipita-
3.1.5 peptization, n—of asphaltenes in crude oils or heavy
tionofasphaltenesthenitisconsideredsimilartotoluene(high
fuel oils, the dispersion of asphaltenes to produce a colloidal
solvency).
dispersion.
4.2 For samples with asphaltenes, a known mass of sample
3.2 Definitions of Terms Specific to This Standard:
is contacted with an excess of heptane to force precipitation of
3.2.1 bitumen, n—a naturally occurring, black, highly vis-
asphaltenes. Incrementally toluene is added to the sample/
cous liquid or semi-solid form of petroleum.
heptane blend and a droplet of the mix is observed under a
3.2.1.1 Discussion—In some parts of the world, the term
microscope at each increment. The point at which asphaltenes
‘bitumen’ is also used to describe residues from petroleum
are no longer visible is recorded as the end point and the
refining.
procedure is repeated twice more with increasing sample
3.2.2 flocculationratioatcriticaldilution,n—percentageby
masses each time. The end point from the three tests is plotted
volume of solvent material to non-solvent material. and the solubility parameters calculated. (Procedure A)
3.2.3 light ends, n—components that cannot be maintained
4.3 For samples without asphaltenes that exhibit behavior
asaliquidatatmosphericpressureattemperaturesgreaterthan
similar to heptane (low solvency), a known reference oil
0°C.
containing asphaltenes is contacted with an excess of the
3.2.3.1 Discussion—This includes any materials that have sample material to force precipitation of asphaltenes. Incre-
atmospheric boiling points below 0°C including methane,
mentallytolueneisaddedtothereferenceoil/sampleblendand
ethane,propane,butane,andfixedgasessuchasH S,CO,N , a droplet of the mix is observed under a microscope at each
2 2 2
O,H , CO.
increment.Thepointatwhichasphaltenesarenolongervisible
2 2
isrecordedastheendpointandtheprocedureisrepeatedtwice
3.2.4 maximum flocculation ratio, n—of asphaltenes, mini-
more with increasing sample masses each time. The end point
mum required solvency power, expressed as percentage of
from the three tests is plotted and the solubility parameters
toluene in a mixture of toluene and heptane, to keep the
calculated. (Procedure B)
asphaltenes in a colloidal solution.
3.2.4.1 Discussion—Maximumflocculationratioisthefloc-
4.4 For samples without asphaltenes that exhibit behavior
culation ratio at the extrapolated infinite dilution of the sample similar to toluene (high solvency), a known reference oil
in other words the y-intercept of the linear regression of FR vs
containing asphaltenes is contacted with an excess of the
Dilution Number. heptanetoforceprecipitationofasphaltenes.Incrementallythe
sampleisaddedtothereferenceoil/heptaneblendandadroplet
3.2.5 peptizing power, n—available solvency power to keep
of the mix is observed under a microscope at each increment.
asphaltenes in a colloidal solution.
Thepointatwhichasphaltenesarenolongervisibleisrecorded
3.2.6 solvency, n—ability to dissolve precipitated as-
as the end point and the procedure is repeated twice more with
phaltenes in a hydrocarbon matrix.
increasing sample masses each time. The end point from the
3.2.7 thermally processed material, n—the product of crude
three tests is plotted and the solubility parameters calculated.
oil that has been processed through a thermal process for the
(Procedure C)
purpose of viscosity and density reduction; also referred to as
5. Significance and Use
a product of visbreaking, upgrading, or partial upgrading.
5.1 Understanding the stability and compatibility of a pe-
3.3 Abbreviations:
troleum product (crude oil or refinery stream, or both) is
3.3.1 FR—flocculation ratio at critical dilution
critical to facilities that receive multiple types of products and
3.3.2 FR —maximum flocculation ratio
max
perform blending and processing operations. Blending incom-
3.3.3 P —peptizing power
o patible streams can cause asphaltene precipitation with poten-
tial consequences such as but not limited to: refinery unit
3.3.4 P-value—peptization value
fouling, processing problems, throughput reduction, emulsion
3.3.5 GO—gas oil
stabilization, pipeline and tank deposition, and equipment
3.3.6 HVGO—heavy vacuum gas oil
fouling.
3.3.7 SCO—synthetic crude oil
5.2 The ability to predict the results of blending operations
3.3.8 VGO—vacuum gas oil allows operators to anticipate potential problems and mitigate
D8253 − 21
those problems prior to receiving the products. It also helps 8.2.1 Heptane, (Warning—Heptane is flammable and a
facilities to manage their product movements in the most health hazard.)
effective manner to avoid future issues. 8.2.2 Toluene, (Warning—Toluene is flammable and a
health hazard.)
5.3 Some petroleum products are unstable without blending
8.2.3 Heptane/Toluene Blend at 9:1 ratio. (Warning—
and understanding the stability of a product in terms of
Heptane/toluene is flammable and a health hazard.)
asphaltene precipitation is an important factor in product
selection for refining. Products with poor stability can contrib- 8.3 Reference Oil:
ute to refinery unit fouling as well as the overall processibility 8.3.1 Shall have ≥5% heptane insoluble asphaltene content
and yield of that product. as per Test Method D6560.
8.3.2 Shall have known solubility parameters determined
6. Interferences
using Procedure A.
8.3.3 Duplicate runs of selected reference material shall
6.1 Solids materials such as salts, sands, clays and toluene
meet method repeatability criteria.
insoluble organic material can mask the asphaltene dissolution
8.3.4 P-value > 2.0 as derived from Procedure A and
endpoint. Samples exhibiting high solids contents prior to
subsequent calculations.
solubility testing should be pre-cleaned either via centrifuge or
8.3.5 Reference oil shall not be sourced from thermally
filtration to remove insoluble solids.
processed material.
8.3.6 Known density at test conditions.
7. Apparatus
7.1 Microscope:
9. Sample Preparation
7.1.1 Total magnification between 80 and 200 times.
9.1 Samplepreparationiscarriedouttoevaluatethesample
7.1.2 Cross polarization capability.
for solids that may interfere with the test procedure.
7.1.3 Digital image capture capability.
9.2 Sample Preparation Procedure:
7.2 Analytical Balance, 4-digit accuracy.
9.2.1 Homogenize the sample using a high-speed mixer.
7.3 Magnetic Stir Plate with Heating Capability.
9.2.2 Using a Pasteur pipette, take a small sub-sample and
7.4 40 mL to 60 mL Glass Vial with Cap—Vial diameter
transfer one drop to a microscope slide and place a cover plate
shall not exceed 25mm (1in. nominal).
over the drop(s).
9.2.3 Under the microscope, focus and observe any particu-
7.5 Microscope Slides with Cover Plates.
late matter visible under normal light. Capture an image.
7.6 Magnetic Stir Bar,oflengthtofitwithintheglassvialin
9.2.4 Switch to cross-polarized light and observe again.
7.4.
Capture an image.
7.7 Pasteur Pipettes.
9.2.5 Compare the two captured images.
9.2.5.1 Crystalline particles (inorganic and waxes) will
7.8 Homogenizing Mixer.
appear white under cross polarization. See Fig. 1.
7.9 Vortex Mixer.
9.2.5.2 Black particles remaining are amorphous as-
7.10 Centrifuge:
phaltenes or other insoluble hydrocarbons. See Fig. 2.
7.10.1 100 mL conical centrifuge tubes.
7.11 Filtration Apparatus (Vacuum or Pressure):
7.11.1 0.45µm filter.
8. Reagents and Materials
8.1 Purity of Reagents—Use chemicals of at least 99%
purity. Unless otherwise indicated, it is intended that all
reagents conform to the specifications of the Committee on
Analytical Reagents of theAmerican Chemical Society where
such specifications are available. Other grades may be used,
provided it is first ascertained that the reagent is of sufficient
purity to permit its use without lessening the accuracy of the
determination.
8.2 Solvents:
ACS Reagent Chemicals, Specifications and Procedures for Reagents and
Standard-Grade Reference Materials, American Chemical Society, Washington,
DC. For suggestions on the testing of reagents not listed by theAmerican Chemical
Society, see Analar Standards for Laboratory Chemicals, BDH Ltd., Poole, Dorset,
U.K., and the United States Pharmacopeia and National Formulary, U.S. Pharma-
copeial Convention, Inc. (USPC), Rockville, MD. FIG. 1 Cross-polarization
D8253 − 21
10.4.7 Decant approximately 50mL of the upper layer into
a vial for use in further testing. Use caution not to disturb and
redistributeanysolidsfromthebottomofthetubeintothebulk
phase.
10.4.8 Dispose of the remaining sample in the centrifuge
tube.
10.5 Vacuum Filtration Method:
10.5.1 Prepare the filtration apparatus as per manufacturer
instructions.
10.5.2 Filter approximately 50mL to 60mL of sample and
start the vacuum. Typical vacuum pressure is 10mmHg.
10.5.3 Collect the filtrate in a vial for use in further testing.
10.5.4 Dispose of the filter and any remaining residue.
10.6 Pressure Filtration Method:
10.6.1 Prepare the filtration apparatus as per manufacturer
instructions.
FIG. 2 Normal Light
10.6.2 Fill the pressure reservoir with approximately 50mL
to 60mL of sample.
10.6.3 Pressurize the reservoir as per manufacturer instruc-
tions. Do not exceed the maximum working pressure of the
9.2.6 If there are significant solids present (crystalline or filtration apparatus.
amorphous) that will make differentiation of changing as-
10.6.4 Open the reservoir slowly to begin filtration and
phaltene populations during the test procedure difficult, then proceed until sample is no longer visible dripping from the
the sample will need to be cleaned as per Section 10. If there
filter outlet.
are no solids present or only solids that are easily distinguish-
10.6.5 Collect the filtrate in a vial for use in further testing.
ableasbackgroundmaterialsandwillnotinterferewiththetest
10.6.6 Dispose of the filter and any remaining residue.
procedure, then proceed to Section 11.
11. Identification of Sample Type and Solvency
10. Sample Cleaning
11.1 Sample Type Evaluation:
10.1 Sincetheintentionofthistestmethodistoevaluatethe
11.1.1 Transfer to a vial, a 1mL 6 0.1mLaliquot of either
solubility properties of the bulk sample, removing already
the neat sample or cleaned sample, depending on the outcome
insoluble material will not bias the test results.
in Section 9.
10.2 The cleaning method selected will be dependent on 11.1.2 Add5mL 60.5mLofheptanetothevialcontaining
the sample. Place the cap on the vial and mix using a vortex
whatequipmentisavailableaswellasthenatureofthesample.
mixer for 30 s.
For example, highly viscous samples may only be possible to
filter by pressure filtration. 11.1.3 Stop mixing and let stand for 5min.
10.2.1 Highly volatile samples can experience loss of low 11.1.4 Using a Pasteur pipette, take a small sub-sample and
molecular weight hydrocarbons that can alter the solvency transfer one or two drops to a microscope slide and place a
properties of the cleaned product. These types of sample shall
cover plate over the drop(s).
only be cleaned if the sample composition will not be com-
11.1.5 Using the microscope, focus and observe any par-
promised. Pressure filtration methods may be suitable.
ticulate matter is visible under normal light.
11.1.5.1 IfvisibleasphaltenesarepresentproceedtoSection
10.3 The specific cleaning technique selected is not critical
12 (Procedure A).
as cleaning is simply intended to minimize interferences but
11.1.5.2 If no asphaltenes are present proceed to 11.2 to
also to allow flexibility with respect to equipment availability.
evaluate the solvency of the sample.
10.4 Centrifuge Method:
11.2 Solvency Testing for Samples without Asphaltenes:
10.4.1 Transfer 100mL of sample to a conical centrifuge
11.2.1 Transfer to a vial, a 1mL 6 0.1mL aliquot of
tube. Do not dilute the sample with solvent.
reference oil.
10.4.2 Weigh and record the mass of the sample and
11.2.2 Add 5mL 6 0.5mLof sample to the vial containing
centrifuge tube.
the reference oil. Place the cap on the vial and mix using a
10.4.3 Fillanidenticalcentrifugetube(balancingtube)with
vortex mixer for 30s.
water.
11.2.3 Stop mixing and let stand for 5min.
10.4.4 Weigh the balancing tube and add or remove water
until it matches the mass of the sample tube. 11.2.4 Take a small sub-sample and transfer one or two
dropstoamicroscopeslideandplaceacoverplateovertheoil
10.4.5 Place tubes in centrifuge rotor directly opposite one
another. drop(s).
10.4.6 Spin at minimum 1000rpm for 30min. 11.2.5 Observe the sample under the microscope.
D8253 − 21
11.2.5.1 Ifasphalteneswereobservedunderthemicroscope, 12.10 Observe the flocculated asphaltenes under the micro-
then the test oil behaves like heptane. Proceed to Section 13 scope using total magnification of between 80× to 200×. The
(Procedure B). observation should be similar to Fig. 3.
11.2.5.2 If asphaltenes were not observed under the
NOTE 1—Based on preliminary round robin results, the mass loss from
microscope, then the test oil behaves like toluene. Proceed to
drop removal is negligible and does not impact overall results.
Section 14 (Procedure C).
12.11 Capture multiple images at various positions on the
slide and record any observations.
12. Procedure A – Samples with Asphaltenes
12.1 Measureandrecordthedensityofthetestoilsampleat 12.12 Record the volume of heptane used.
the test temperature.
12.13 To the same vial, add 1mL 6 0.01mL of toluene.
12.2 Weigh a vial including a magnetic stir bar and record
12.14 Weigh and record the mass of the vial, close the cap
the tare mass of the vial and stir bar.
and stir for 5min.
12.3 Weigh1g 60.01gofthesampleintothetared40mL
12.15 Stop stirring and remove the cap from the vial.
vial containing the magnetic stirring bar.
12.16 Using a Pasteur pipette, immediately transfer one or
12.4 Placethevialonthestirplateandbeginstirringslowly.
two drops of the mixture from the vial to a clean microscope
12.5 Using a pipette, slowly add 10mL 6 0.01mL of the
slide and cover the drop(s) with a cover slip.
9:1 heptane/toluene mixture to the vial at approximately
12.17 Observe the flocculated asphaltenes under the micro-
1mL⁄min.
scope.
12.5.1 Ifthesamplestability(P-value)isalreadyreasonably
known to the user and it is understood that the sample is
12.18 Capture multiple images at various positions on the
typically unstable (P-value < 1.5), then it is permissible to slide and record observations. The asphaltenes population
increase the sample sizes and reduce the 9:1 heptane: toluene
should be less dense than what is shown in Fig. 3.
mixturevolume.Forexample:insteadof1.0g,2.0g,and3.0g
12.19 After making the microscope observation in 12.17:
of sample and 10mL of heptane/toluene mixture, use 2.5g,
12.19.1 If there is still a large population of asphaltenes
5.0g, 7.5g of sample and 4.5mL of heptane/toluene mixture.
present, then repeat steps 12.14 – 12.20 until the population of
12.6 Close the cap and stir the mixture for 5min.
asphaltenes is reduced significantly.
12.19.2 If asphaltenes are still present but the population
12.7 Weigh and record the mass of vial and sample/heptane
density is reduced significantly, then proceed to 12.21.
mixture.
12.8 Stop stirring and remove the cap from the vial. 12.20 Reduce the step addition from 1mL of toluene to
0.5mL 6 0.01mL of toluene and stir the mixture for 5min.
12.9 Using a Pasteur pipette, immediately transfer one or
two drops of the mixture from the vial to a clean microscope 12.21 Stop stirring and capture multiple images at various
slide and cover the drop(s) with a cover slip. positions on the slide and record observations.
FIG. 3 Flocculated Asphaltenes Under Microscope
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...


This document is not an ASTM standard and is intended only to provide the user of an ASTM standard an indication of what changes have been made to the previous version. Because
it may not be technically possible to adequately depict all changes accurately, ASTM recommends that users consult prior editions as appropriate. In all cases only the current version
of the standard as published by ASTM is to be considered the official document.
Designation: D8253 − 20 D8253 − 21
Standard Test Method for
Determination of the Asphaltene Solvency Properties of
Bitumen, Crude Oil, Condensate and/or Related Products
for the Purpose of Calculating Stability, Compatibility for
Blending, Fouling, and Processibility (Manual Microscopy
Method)
This standard is issued under the fixed designation D8253; 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 (´) indicates an editorial change since the last revision or reapproval.
1. Scope Scope*
1.1 This test method covers the use of a basic microscope to determine the asphaltene solvency properties of bitumen, crude oil,
condensate or related products, or the combinations thereof. These properties can be used to calculate the solubility parameters
required to calculate and predict asphaltene stability for blending purposes, refinery unit fouling, processibility, emulsion
stabilization, pipeline and tank deposition, and equipment fouling. If the solubility properties are known for two products, then the
compatibility of potential blend ratios can be predicted.
1.2 This test method is limited to products that allow handling at atmospheric pressure and room temperature conditions without
a significant loss of light end components. Loss of light ends will result in changes in the solubility properties of the product and
may alter or bias the results, or both. Samples with vapor pressures (VPCR at 37.8 °C using Test Method D6377) greater than
100 kPa are not suitable for use with this test method.
1.3 This test method is primarily suited to products that are freely flowing at test conditions. Samples that are too viscous to flow
at test conditions, such as semi-solids, may need to be heated to allow handling (See Annex A1.)
1.4 The values stated in SI units are to be regarded as standard. The values given in parentheses after SI units are provided for
information only and are not considered standard.
1.5 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, health, and environmental practices and determine the applicability of
regulatory limitations prior to use.
1.6 This international standard was developed in accordance with internationally recognized principles on standardization
established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued
by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
This test method is under the jurisdiction of ASTM Committee D02 on Petroleum Products, Liquid Fuels, and Lubricants and is the direct responsibility of Subcommittee
D02.14 on Stability, Cleanliness and Compatibility of Liquid Fuels.
Current edition approved May 1, 2020Jan. 1, 2021. Published May 2020January 2021. Originally approved in 2020. Last previous edition approved in 2020 as D8253 – 20.
DOI: 10.1520/D8253-20.10.1520/D8253-21.
*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
D8253 − 21
2. Referenced Documents
2.1 ASTM Standards:
D6560 Test Method for Determination of Asphaltenes (Heptane Insolubles) in Crude Petroleum and Petroleum Products
D6377 Test Method for Determination of Vapor Pressure of Crude Oil: VPCR (Expansion Method)
x
3. Terminology
3.1 Definitions:
3.1.1 asphaltenes, n—(rarely used in the singular), in petroleum technology, represent an oil fraction that is soluble in a specified
aromatic solvent but separates upon the addition of an excess of a specified paraffinic solvent.
3.1.1.1 Discussion—
Asphaltenes are found largely in crude oils and in heavy fuel oils containing residual fractions. They are insoluble in alkanes such
as heptane and pentane, but soluble in aromatic solvents such as benzene or toluene.
3.1.2 compatibility, n—of crude oils or heavy fuel oils, the ability of two or more crude oils or fuel oils to blend together within
certain concentration ranges without evidence of separation, such as the formation of multiple phases.
3.1.2.1 Discussion—
Incompatible heavy fuel oils or crude oils, when mixed or blended, result in flocculation or precipitation of asphaltenes. Some oils
may be compatible within certain concentration ranges in specific mixtures, but incompatible outside those ranges.
3.1.3 crude oil, n—a naturally occurring hydrocarbon mixture, generally in a liquid state, which may also include compounds of
sulfur, nitrogen, oxygen, metals and other elements (Synonym – crude petroleum, crude).
3.1.4 flocculation, n—of asphaltenes from crude oils or heavy fuel oils, the aggregation of colloidally dispersed asphaltenes into
visibly larger masses which may or may not settle.
3.1.5 peptization, n—of asphaltenes in crude oils or heavy fuel oils, the dispersion of asphaltenes to produce a colloidal dispersion.
3.2 Definitions of Terms Specific to This Standard:
3.2.1 bitumen, n—a naturally occurring, black, highly viscous liquid or semi-solid form of petroleum.
3.2.1.1 Discussion—
In some parts of the world, the term ‘bitumen’ is also used to describe residues from petroleum refining.
3.2.2 flocculation ratio at critical dilution, n—percentage by volume of solvent material to non-solvent material.
3.2.3 light ends, n—components that cannot be maintained as a liquid at atmospheric pressure at temperatures greater than 0 °C.
3.2.3.1 Discussion—
This includes any materials that have atmospheric boiling points below 0 °C including methane, ethane, propane, butane, and fixed
gases such as H S, CO , N , O , H , CO.
2 2 2 2 2
3.2.4 maximum flocculation ratio, n—of asphaltenes, minimum required solvency power, expressed as percentage of toluene in
a mixture of toluene and heptane, to keep the asphaltenes in a colloidal solution.
3.2.4.1 Discussion—
Maximum flocculation ratio is the flocculation ratio at the extrapolated infinite dilution of the sample in other words the y-intercept
of the linear regression of FR vs Dilution Number.
3.2.5 peptizing power, n—available solvency power to keep asphaltenes in a colloidal solution.
3.2.6 solvency, n—ability to dissolve precipitated asphaltenes in a hydrocarbon matrix.
For referenced ASTM standards, visit the ASTM website, www.astm.org, or contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM Standards
volume information, refer to the standard’s Document Summary page on the ASTM website.
D8253 − 21
3.2.7 thermally processed material, n—the product of crude oil that has been processed through a thermal process for the purpose
of viscosity and density reduction; also referred to as a product of visbreaking, upgrading, or partial upgrading.
3.3 Abbreviations:
3.3.1 FR—flocculation ratio at critical dilution
3.3.2 FR —maximum flocculation ratio
max
3.3.3 P —peptizing power
o
3.3.4 P-value—peptization value
3.3.5 GO—gas oil
3.3.6 HVGO—heavy vacuum gas oil
3.3.7 SCO—synthetic crude oil
3.3.8 VGO—vacuum gas oil
4. Summary of Test Method
4.1 The sample type is first determined as either “with asphaltenes” or “without asphaltenes” to identify if it is a source of
asphaltenes or not. If the sample type is “without asphaltenes” then a second test is performed to establish if the solvency of the
sample is similar in behavior to either toluene or heptane. The sample is contacted with a reference oil known to contain
asphaltenes. If the reference oil contacted with the sample results in the precipitation of asphaltenes, then it is considered similar
to heptane (low solvency). If the reference oil contacted with the sample does not result in the precipitation of asphaltenes then
it is considered similar to toluene (high solvency).
4.2 For samples with asphaltenes, a known mass of sample is contacted with an excess of heptane to force precipitation of
asphaltenes. Incrementally toluene is added to the sample/heptane blend and a droplet of the mix is observed under a microscope
at each increment. The point at which asphaltenes are no longer visible is recorded as the end point and the procedure is repeated
twice more with increasing sample masses each time. The end point from the three tests is plotted and the solubility parameters
calculated. (Procedure A)
4.3 For samples without asphaltenes that exhibit behavior similar to heptane (low solvency), a known reference oil containing
asphaltenes is contacted with an excess of the sample material to force precipitation of asphaltenes. Incrementally toluene is added
to the reference oil/sample blend and a droplet of the mix is observed under a microscope at each increment. The point at which
asphaltenes are no longer visible is recorded as the end point and the procedure is repeated twice more with increasing sample
masses each time. The end point from the three tests is plotted and the solubility parameters calculated. (Procedure B)
4.4 For samples without asphaltenes that exhibit behavior similar to toluene (high solvency), a known reference oil containing
asphaltenes is contacted with an excess of the heptane to force precipitation of asphaltenes. Incrementally the sample is added to
the reference oil/heptane blend and a droplet of the mix is observed under a microscope at each increment. The point at which
asphaltenes are no longer visible is recorded as the end point and the procedure is repeated twice more with increasing sample
masses each time. The end point from the three tests is plotted and the solubility parameters calculated. (Procedure C)
5. Significance and Use
5.1 Understanding the stability and compatibility of a petroleum product (crude oil or refinery stream, or both) is critical to
facilities that receive multiple types of products and perform blending and processing operations. Blending incompatible streams
can cause asphaltene precipitation with potential consequences such as but not limited to: refinery unit fouling, processing
problems, throughput reduction, emulsion stabilization, pipeline and tank deposition, and equipment fouling.
D8253 − 21
5.2 The ability to predict the results of blending operations allows operators to anticipate potential problems and mitigate those
problems prior to receiving the products. It also helps facilities to manage their product movements in the most effective manner
to avoid future issues.
5.3 Some petroleum products are unstable without blending and understanding the stability of a product in terms of asphaltene
precipitation is an important factor in product selection for refining. Products with poor stability can contribute to refinery unit
fouling as well as the overall processibility and yield of that product.
6. Interferences
6.1 Solids materials such as salts, sands, clays and toluene insoluble organic material can mask the asphaltene dissolution
endpoint. Samples exhibiting high solids contents prior to solubility testing should be pre-cleaned either via centrifuge or filtration
to remove insoluble solids.
7. Apparatus
7.1 Microscope:
7.1.1 Total magnification between 80 and 200 times.
7.1.2 Cross polarization capability.
7.1.3 Digital image capture capability.
7.2 Analytical Balance, 4-digit accuracy.
7.3 Magnetic Stir Plate with Heating Capability.
7.4 40 mL to 60 mL Glass Vial with Cap—Vial diameter shall not exceed 25 mm (1 in. nominal).
7.5 Microscope Slides with Cover Plates.
7.6 Magnetic Stir Bar, of length to fit within the glass vial in 7.4.
7.7 Pasteur Pipettes.
7.8 Homogenizing Mixer.
7.9 Vortex Mixer.
7.10 Centrifuge:
7.10.1 100 mL conical centrifuge tubes.
7.11 Filtration Apparatus (Vacuum or Pressure):
7.11.1 0.45 μm filter.
8. Reagents and Materials
8.1 Purity of Reagents—Use chemicals of at least 99 % purity. Unless otherwise indicated, it is intended that all reagents conform
D8253 − 21
to the specifications of the Committee on Analytical Reagents of the American Chemical Society where such specifications are
available. Other grades may be used, provided it is first ascertained that the reagent is of sufficient purity to permit its use without
lessening the accuracy of the determination.
8.2 Solvents:
8.2.1 Heptane, (Warning—Heptane is flammable and a health hazard.)
8.2.2 Toluene, (Warning—Toluene is flammable and a health hazard.)
8.2.3 Heptane/Toluene Blend at 9:1 ratio. (Warning—Heptane/toluene is flammable and a health hazard.)
8.3 Reference Oil:
8.3.1 Shall have ≥5 % heptane insoluble asphaltene content as per Test Method D6560.
8.3.2 Shall have known solubility parameters determined using Procedure A.
8.3.3 Duplicate runs of selected reference material shall meet method repeatability criteria.
8.3.4 P-value > 2.0 as derived from Procedure A and subsequent calculations.
8.3.5 Reference oil shall not be sourced from thermally processed material.
8.3.6 Known density at test conditions.
9. Sample Preparation
9.1 Sample preparation is carried out to evaluate the sample for solids that may interfere with the test procedure.
9.2 Sample Preparation Procedure:
9.2.1 Homogenize the sample using a high-speed mixer.
9.2.2 Using a Pasteur pipette, take a small sub-sample and transfer one drop to a microscope slide and place a cover plate over
the drop(s).
9.2.3 Under the microscope, focus and observe any particulate matter visible under normal light. Capture an image.
9.2.4 Switch to cross-polarized light and observe again. Capture an image.
9.2.5 Compare the two captured images.
9.2.5.1 Crystalline particles (inorganic and waxes) will appear white under cross polarization. See Fig. 1.
9.2.5.2 Black particles remaining are amorphous asphaltenes or other insoluble hydrocarbons. See Fig. 2.
9.2.6 If there are significant solids present (crystalline or amorphous) that will make differentiation of changing asphaltene
populations during the test procedure difficult, then the sample will need to be cleaned as per Section 10. If there are no solids
present or only solids that are easily distinguishable as background materials and will not interfere with the test procedure, then
proceed to Section 11.
ACS Reagent Chemicals, Specifications and Procedures for Reagents and Standard-Grade Reference Materials, American Chemical Society, Washington, DC. For
suggestions on the testing of reagents not listed by the American Chemical Society, see Analar Standards for Laboratory Chemicals, BDH Ltd., Poole, Dorset, U.K., and
the United States Pharmacopeia and National Formulary, U.S. Pharmacopeial Convention, Inc. (USPC), Rockville, MD.
D8253 − 21
FIG. 1 Cross-polarization
FIG. 2 Normal Light
10. Sample Cleaning
10.1 Since the intention of this test method is to evaluate the solubility properties of the bulk sample, removing already insoluble
material will not bias the test results.
10.2 The cleaning method selected will be dependent on what equipment is available as well as the nature of the sample. For
example, highly viscous samples may only be possible to filter by pressure filtration.
10.2.1 Highly volatile samples can experience loss of low molecular weight hydrocarbons that can alter the solvency properties
of the cleaned product. These types of sample shall only be cleaned if the sample composition will not be compromised. Pressure
filtration methods may be suitable.
10.3 The specific cleaning technique selected is not critical as cleaning is simply intended to minimize interferences but also to
allow flexibility with respect to equipment availability.
10.4 Centrifuge Method:
10.4.1 Transfer 100 mL of sample to a conical centrifuge tube. Do not dilute the sample with solvent.
D8253 − 21
10.4.2 Weigh and record the mass of the sample and centrifuge tube.
10.4.3 Fill an identical centrifuge tube (balancing tube) with water.
10.4.4 Weigh the balancing tube and add or remove water until it matches the mass of the sample tube.
10.4.5 Place tubes in centrifuge rotor directly opposite one another.
10.4.6 Spin at minimum 1000 rpm for 30 min.
10.4.7 Decant approximately 50 mL of the upper layer into a vial for use in further testing. Use caution not to disturb and
redistribute any solids from the bottom of the tube into the bulk phase.
10.4.8 Dispose of the remaining sample in the centrifuge tube.
10.5 Vacuum Filtration Method:
10.5.1 Prepare the filtration apparatus as per manufacturer instructions.
10.5.2 Filter approximately 50 mL to 60 mL of sample and start the vacuum. Typical vacuum pressure is 10 mmHg.
10.5.3 Collect the filtrate in a vial for use in further testing.
10.5.4 Dispose of the filter and any remaining residue.
10.6 Pressure Filtration Method:
10.6.1 Prepare the filtration apparatus as per manufacturer instructions.
10.6.2 Fill the pressure reservoir with approximately 50 mL to 60 mL of sample.
10.6.3 Pressurize the reservoir as per manufacturer instructions. Do not exceed the maximum working pressure of the filtration
apparatus.
10.6.4 Open the reservoir slowly to begin filtration and proceed until sample is no longer visible dripping from the filter outlet.
10.6.5 Collect the filtrate in a vial for use in further testing.
10.6.6 Dispose of the filter and any remaining residue.
11. Identification of Sample Type and Solvency
11.1 Sample Type Evaluation:
11.1.1 Transfer to a vial, a 1 mL 6 0.1 mL aliquot of either the neat sample or cleaned sample, depending on the outcome in
Section 9.
11.1.2 Add 5 mL 6 0.5 mL of heptane to the vial containing the sample. Place the cap on the vial and mix using a vortex mixer
for 30 s.
11.1.3 Stop mixing and let stand for 5 min.
11.1.4 Using a Pasteur pipette, take a small sub-sample and transfer one or two drops to a microscope slide and place a cover plate
over the drop(s).
11.1.5 Using the microscope, focus and observe any particulate matter is visible under normal light.
D8253 − 21
11.1.5.1 If visible asphaltenes are present proceed to Section 12 (Procedure A).
11.1.5.2 If no asphaltenes are present proceed to 11.2 to evaluate the solvency of the sample.
11.2 Solvency Testing for Samples without Asphaltenes:
11.2.1 Transfer to a vial, a 1 mL 6 0.1 mL aliquot of reference oil.
11.2.2 Add 5 mL 6 0.5 mL of sample to the vial containing the reference oil. Place the cap on the vial and mix using a vortex
mixer for 30 s.
11.2.3 Stop mixing and let stand for 5 min.
11.2.4 Take a small sub-sample and transfer one or two drops to a microscope slide and place a cover plate over the oil drop(s).
11.2.5 Observe the sample under the microscope.
11.2.5.1 If asphaltenes were observed under the microscope, then the test oil behaves like heptane. Proceed to Section 13
(Procedure B).
11.2.5.2 If asphaltenes were not observed under the microscope, then the test oil behaves like toluene. Proceed to Section 14
(Procedure C).
12. Procedure A – Samples with Asphaltenes
12.1 Measure and record the density of the test oil sample at the test temperature.
12.2 Weigh a vial including a magnetic stir bar and record the tare mass of the vial and stir bar.
12.3 Weigh 1 g 6 0.01 g of the sample into the tared 40 mL vial containing the magnetic stirring bar.
12.4 Place the vial on the stir plate and begin stirring slowly.
12.5 Using a pipette, slowly add 10 mL 6 0.01 mL of the 9:1 heptane/toluene mixture to the vial at approximately 1 mL ⁄min.
12.5.1 If the sample stability (P-value) is already reasonably known to the user and it is understood that the sample is typically
unstable (P-value < 1.5), then it is permissible to increase the sample sizes and reduce the 9:1 heptane: toluene mixture volume.
For example: instead of 1.0 g, 2.0 g, and 3.0 g of sample and 10 mL of heptane/toluene mixture, use 2.5 g, 5.0 g, 7.5 g of sample
and 4.5 mL of heptane/toluene mixture.
12.6 Close the cap and stir the mixture for 5 min.
12.7 Weigh and record the mass of vial and sample/heptane mixture.
12.8 Stop stirring and remove the cap from the vial.
12.9 Using a Pasteur pipette, immediately transfer one or two drops of the mixture from the vial to a clean microscope slide and
cover the drop(s) with a cover slip.
12.10 Observe the flocculated asphaltenes under the microscope using total magnification of between 80× to 200×. The
observation should be similar to Fig. 3.
NOTE 1—Based on preliminary round robin results, the mass loss from drop removal is negligible and does not impact overall results.
D8253 − 21
FIG. 3 Flocculated Asphaltenes Under Microscope
12.11 Capture multiple images at various positions on the slide and record any observations.
12.12 Record the volume of heptane used.
12.13 To the same vial, add 1 mL 6 0.01 mL of toluene.
12.14 Weigh and record the mass of the vial, close the cap and stir for 5 min.
12.15 Stop stirring and remove the cap from the vial.
12.16 Using a Pasteur pipette, immediately transfer one or two drops of the mixture from the vial to a clean microscope slide and
cover the drop(s) with a cover slip.
12.17 Observe the flocculated asphaltenes under the microscope.
12.18 Capture multiple images at various positions on the slide and record observations. The asphaltenes population should be less
dense than what is shown in Fig. 3.
12.19 After making the microscope observation in 12.17:
12.19.1 If there is still a large population of asphaltenes present, then repeat steps 12.14 – 12.20 until the population of asphaltenes
is reduced significantly.
12.19.2 If asphaltenes are still present but the population density is reduced significantly, then proceed to 12.21.
12.20 Reduce the step addition from 1 mL of toluene to 0.5 mL 6 0.01 mL of toluene and stir the mixture for 5 min.
12.21 Stop stirring and capture multiple images at various positions on the slide and record observations.
12.22 Continue with the addition of toluene in 0.5 mL 6 0.01 mL steps until the asphaltenes are almost gone. See Fig. 4.
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