Standard Test Method for Evaluation of the Type and Viscoelastic Stability of Water-in-oil Mixtures Formed from Crude Oil and Petroleum Products Mixed with Water

SIGNIFICANCE AND USE
4.1 A standard test is necessary to establish a behavior pattern for spilled crude oils or petroleum products at different oil weathering stages.  
4.2 Water-in-oil mixtures vary with oil type and oil conditions such as weathering. Results from this test method form a baseline, and usually are a measure of behavior at sea.  
4.3 This test has been developed over many years using standardized equipment, test procedures, and to overcome difficulties noted in other test procedures.  
4.4 This test should be performed at the temperatures and degrees of weathering corresponding to the spill conditions of interest.
SCOPE
1.1 This test method covers a procedure to determine the water-in-oil emulsification tendencies and stabilities of crude oils and petroleum products in the laboratory. The results of this test method can provide oil behavior data for input into oil spill models.  
1.2 This test method covers a specific method of determining emulsion tendencies and does not cover other procedures that may be applicable to determining emulsion tendencies.  
1.3 The test results obtained using this test method are intended to provide baseline data for the behavior of oil and petroleum products at sea and input to oil spill models.  
1.4 The test results obtained using this test method can be used directly to predict certain facets of oil spill behavior or as input to oil spill models.  
1.5 The accuracy of the test method depends very much on the representative nature of the oil sample used. Certain oils can form a variety of water-in-oil types depending on their chemical contents at the moment a sample is taken. Other oils are relatively stable with respect to the type formed  
1.6 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.  
1.7 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.  
1.8 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-Aug-2021

Overview

ASTM F3045-21: Standard Test Method for Evaluation of the Type and Viscoelastic Stability of Water-in-oil Mixtures Formed from Crude Oil and Petroleum Products Mixed with Water defines a laboratory procedure to assess how crude oils and petroleum products form and stabilize water-in-oil emulsions, often encountered during oil spills. The method generates critical data to predict oil behavior in marine environments, contributing to oil spill modeling, response planning, and environmental risk assessment.

This test method determines the tendencies and stability of water-in-oil emulsions using standardized procedures and equipment, ensuring consistent and comparable results. The classification of mixtures-such as stable, meso-stable, unstable emulsions, and entrained water-supports understanding of how various oils will behave after interacting with water, particularly under different weathering and temperature conditions.

Key Topics

  • Emulsification of Oil and Water
    The standard focuses on laboratory evaluation of how oils react when mixed with water, particularly regarding the formation of water-in-oil emulsions.
  • Mixture Classification
    The resulting mixtures are categorized as stable, meso-stable, unstable emulsions, or entrained water. Each type displays distinct physical and chemical properties affecting oil spill response.
  • Viscoelastic Stability Measurement
    Rheological measurements determine the viscoelastic properties and classify the stability index of each oil-water mixture, providing quantitative data for modeling.
  • Influencing Factors
    Oil type, degree of weathering, temperature, and the representative nature of samples significantly impact emulsion stability and classification.
  • Testing Conditions
    The method requires physical mixing of oil and saltwater at controlled temperature, detailed cleaning protocols to prevent contamination, and strict calibration of measurement devices.

Applications

  • Oil Spill Response Planning
    Data from ASTM F3045-21 directly informs oil spill contingency plans by predicting the formation and persistence of water-in-oil emulsions, which can significantly hinder cleanup efforts.
  • Environmental Risk Assessment
    Understanding emulsion stability helps estimate the potential impact of different crude oils and petroleum products if spilled, aiding in regulatory compliance and environmental protection.
  • Oil Spill Modeling
    Results serve as input for oil spill modeling software, enabling more accurate predictions of spill behavior, spreading, and the physicochemical evolution of the oil on water surfaces.
  • Product Comparison and Development
    Refineries, oil producers, and product developers use this method to compare emulsion tendencies across various oil blends and optimize formulations for environmental compatibility.
  • Quality and Compliance Testing
    Laboratories and regulatory agencies rely on this standardized procedure to evaluate oil samples for compliance, reporting, and research.

Related Standards

  • ASTM F2067 – Standard Practice for Deployment and Documentation of Spilled Oil Monitoring of Surface Water and Shoreline
  • ASTM F2534 – Standard Guide for Visually Estimating Oil Spill Thickness on Water
  • EPA Method 1311 – Toxicity Characteristic Leaching Procedure (TCLP) for sample preparation
  • ISO 8217 – Petroleum products-Fuels (class F)-Specifications of marine fuels

Practical Value

ASTM F3045-21 provides a robust, standardized framework for laboratories, oil spill responders, and modelers to evaluate the stability and behavior of oil-water mixtures. By simulating real-world conditions and classifying results, it enhances predictive capabilities essential for effective marine oil spill response and environmental stewardship. The standard's emphasis on reproducibility, detailed sample handling, and the importance of oil composition ensures meaningful, actionable data for industry and regulatory applications.

Keywords: water-in-oil emulsion, oil spill modeling, viscoelastic stability, crude oil, petroleum products, emulsion stability, oil spill response, ASTM F3045-21, entrained water, marine environment.

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Frequently Asked Questions

ASTM F3045-21 is a standard published by ASTM International. Its full title is "Standard Test Method for Evaluation of the Type and Viscoelastic Stability of Water-in-oil Mixtures Formed from Crude Oil and Petroleum Products Mixed with Water". This standard covers: SIGNIFICANCE AND USE 4.1 A standard test is necessary to establish a behavior pattern for spilled crude oils or petroleum products at different oil weathering stages. 4.2 Water-in-oil mixtures vary with oil type and oil conditions such as weathering. Results from this test method form a baseline, and usually are a measure of behavior at sea. 4.3 This test has been developed over many years using standardized equipment, test procedures, and to overcome difficulties noted in other test procedures. 4.4 This test should be performed at the temperatures and degrees of weathering corresponding to the spill conditions of interest. SCOPE 1.1 This test method covers a procedure to determine the water-in-oil emulsification tendencies and stabilities of crude oils and petroleum products in the laboratory. The results of this test method can provide oil behavior data for input into oil spill models. 1.2 This test method covers a specific method of determining emulsion tendencies and does not cover other procedures that may be applicable to determining emulsion tendencies. 1.3 The test results obtained using this test method are intended to provide baseline data for the behavior of oil and petroleum products at sea and input to oil spill models. 1.4 The test results obtained using this test method can be used directly to predict certain facets of oil spill behavior or as input to oil spill models. 1.5 The accuracy of the test method depends very much on the representative nature of the oil sample used. Certain oils can form a variety of water-in-oil types depending on their chemical contents at the moment a sample is taken. Other oils are relatively stable with respect to the type formed 1.6 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard. 1.7 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. 1.8 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 4.1 A standard test is necessary to establish a behavior pattern for spilled crude oils or petroleum products at different oil weathering stages. 4.2 Water-in-oil mixtures vary with oil type and oil conditions such as weathering. Results from this test method form a baseline, and usually are a measure of behavior at sea. 4.3 This test has been developed over many years using standardized equipment, test procedures, and to overcome difficulties noted in other test procedures. 4.4 This test should be performed at the temperatures and degrees of weathering corresponding to the spill conditions of interest. SCOPE 1.1 This test method covers a procedure to determine the water-in-oil emulsification tendencies and stabilities of crude oils and petroleum products in the laboratory. The results of this test method can provide oil behavior data for input into oil spill models. 1.2 This test method covers a specific method of determining emulsion tendencies and does not cover other procedures that may be applicable to determining emulsion tendencies. 1.3 The test results obtained using this test method are intended to provide baseline data for the behavior of oil and petroleum products at sea and input to oil spill models. 1.4 The test results obtained using this test method can be used directly to predict certain facets of oil spill behavior or as input to oil spill models. 1.5 The accuracy of the test method depends very much on the representative nature of the oil sample used. Certain oils can form a variety of water-in-oil types depending on their chemical contents at the moment a sample is taken. Other oils are relatively stable with respect to the type formed 1.6 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard. 1.7 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. 1.8 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 F3045-21 is classified under the following ICS (International Classification for Standards) categories: 13.020.40 - Pollution, pollution control and conservation; 75.080 - Petroleum products in general. The ICS classification helps identify the subject area and facilitates finding related standards.

ASTM F3045-21 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: F3045 − 21
Standard Test Method for
Evaluation of the Type and Viscoelastic Stability of Water-in-
oil Mixtures Formed from Crude Oil and Petroleum Products
Mixed with Water
This standard is issued under the fixed designation F3045; 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 mendations issued by the World Trade Organization Technical
Barriers to Trade (TBT) Committee.
1.1 This test method covers a procedure to determine the
water-in-oil emulsification tendencies and stabilities of crude
2. Summary of Test Method
oils and petroleum products in the laboratory. The results of
2.1 Oil is mixed with 33 ‰ (3.3 %) saline water for 12 h in
this test method can provide oil behavior data for input into oil
a standard rotating apparatus. The resulting mixture is charac-
spill models.
terized after this mixing period.
1.2 This test method covers a specific method of determin-
2.2 The resulting mixture as created in step 2.1, is charac-
ing emulsion tendencies and does not cover other procedures
terized by visual qualities, by measuring water content and by
that may be applicable to determining emulsion tendencies.
rheological measurements. The mixture is then classified as a
1.3 The test results obtained using this test method are
stable, meso-stable, unstable emulsion or an entrained water
intended to provide baseline data for the behavior of oil and
mixture. Each of these four types of mixtures has different
petroleum products at sea and input to oil spill models.
characteristics affecting the behavior of oil in the aquatic
environment.
1.4 The test results obtained using this test method can be
used directly to predict certain facets of oil spill behavior or as
3. Terminology
input to oil spill models.
3.1 Definitions:
1.5 The accuracy of the test method depends very much on
3.1.1 complex modulus—One of the results of viscoelastic
the representative nature of the oil sample used. Certain oils
measurement, a measure of the resistance of a viscoelastic
can form a variety of water-in-oil types depending on their
substance to flow under an applied dynamic stress, combining
chemical contents at the moment a sample is taken. Other oils
both the non-reversible (viscous) flow of the test substance and
are relatively stable with respect to the type formed
the reversible (elastic) deformation of the test substance.
1.6 The values stated in SI units are to be regarded as
3.1.2 emulsion—Atype of colloid, specifically, a dispersion
standard. No other units of measurement are included in this
of small droplets of one immiscible liquid in another.
standard.
3.1.2.1 meso-stable emulsions—Emulsions that lack one or
1.7 This standard does not purport to address all of the
more of the compositional factors necessary to form a stable
safety concerns, if any, associated with its use. It is the
emulsion, but that are sufficiently stable to persist for short
responsibility of the user of this standard to establish appro-
periods, typically a few hours to days.
priate safety, health, and environmental practices and deter-
3.1.2.2 stable emulsions—Emulsions that persist
mine the applicability of regulatory limitations prior to use.
indefinitely, consisting of fine droplets with a rigid film
1.8 This international standard was developed in accor-
interface which resists coalescence.
dance with internationally recognized principles on standard-
3.1.2.3 unstable emulsions—Mixtures of water and oil that
ization established in the Decision on Principles for the
resolve rapidly into two phases, usually within a few minutes
Development of International Standards, Guides and Recom-
to hours. There may be residual water remaining in low
percentages.
3.1.2.4 water-in-oil emulsion—An emulsion consisting of a
This test method is under the jurisdiction of ASTM Committee F20 on
continuous phase of oil containing a dispersed phase of water.
Hazardous Substances and Oil Spill Response and is the direct responsibility of
Subcommittee F20.16 on Surveillance and Tracking.
3.1.3 entrained water—This is not an emulsion but a me-
Current edition approved Sept. 1, 2021. Published September 2021. Originally
chanical mixture of oil and water which has not separated due
approved in 2015. Last previous edition approved in 2020 as F3045–20. DOI:
10.1520/F3045–21. to the physical properties of the water and oil.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
F3045 − 21
3.1.3.1 Discussion—Typically, the oil and water have simi- 5.6 Since the test results may be affected by salinity,
lar densities and the oil phase has a high viscosity. thorough mixing of the salt water is required. Salinity should
be verified using a salinity meter before use.
3.1.4 rag—The remnant of a broken water-in-oil emulsion.
3.1.4.1 Discussion—Rag will not reform an emulsion. Rag
5.7 Oil recovered for a source, especially crude oil fields,
is thought to consist of tightly bound asphaltenes and resins. vary with production conditions and over time. Oil samples
should be considered as indicative of the oil source at a
3.1.5 stability index—Anindexdescribingthestabilityofan
moment within a range of variability and are not necessarily
emulsion.
representative of all oil recovered from the source. Some oils
3.1.5.1 Discussion—In this standard, it is calculated using
are near the threshold of two different water-in-oil types.
data derived from rheological measurements.
Depending on the actual conditions under which the oil was
3.1.6 storage modulus—One of the results of viscoelastic
sampled, different results may occur. Other oils are not as
measurement, a measure of the elastic (reversible) deformation
sensitive.
behavior of a viscoelastic substance under an applied dynamic
5.8 Additives introduced in the production and transport of
stress.
oils can change their emulsification behavior. Some oils have
added asphaltene suspenders or emulsion inhibitors. These
4. Significance and Use
may significantly alter the outcome of this test. Information on
4.1 A standard test is necessary to establish a behavior
the oil treatment should be obtained before making the test.
pattern for spilled crude oils or petroleum products at different
oil weathering stages.
6. Apparatus
4.2 Water-in-oil mixtures vary with oil type and oil condi-
6.1 2.2-litre fluorinated HDPE wide-mouth bottles, approxi-
tions such as weathering. Results from this test method form a
mately 24 cm in height and 6 cm in radius (Nalgene or
baseline, and usually are a measure of behavior at sea.
equivalent), used as the test vessel. These vessels match the
4.3 This test has been developed over many years using shaker as described below.
standardized equipment, test procedures, and to overcome
6.2 Variable speed end-over-end rotary mixer capable of
difficulties noted in other test procedures.
maintaining 55 RPM, with a radius of rotation of 15 cm (7.5
4.4 This test should be performed at the temperatures and cm from center of vessel) (Associated Design or equivalent).
degrees of weathering corresponding to the spill conditions of
6.3 Automated Karl Fischer titration analyser, This device
interest.
is used to measure the water content of the resulting water-in-
oil mixture.
5. Interferences and Sources of Error
6.4 Rheometer, capable of functioning in forced-oscillation
5.1 Interferences can be caused by contaminants, such as
mode with parallel plate geometry. This device is used to
residual oil or surfactants on labware, and other sample
measure the rheological properties of the resulting water-in-oil
handling supplies and apparatus that lead to irregular results.
mixture.
Surfactants in particular will influence results, as small
6.5 Circulating bath with a range from 0 to 25 °C (60.1).
amounts will disrupt the stability of a water-in-oil emulsion.
All glassware must be thoroughly cleaned. The cleaning
6.6 Salinometer or water quality meter, SensIon 745 or
process includes rinsing with dichloromethane to remove the
equivalent with a sensitivity of 60.1 PSU (practical salinity
oil, followed by rinsing three times each with tap water,
unit).
purified water (reverse osmosis), and acetone. Once cleaned,
6.7 Oil-mixing devices including a shaker for mixing the
precautions must be taken to minimize contact of the labware
small samples prior to use and devices to mix the oil contained
with contaminants to prevent interferences.
in drums.
5.2 Emulsion formation is somewhat susceptible to energy
6.8 The following is a list of other necessary supplies.
levels. The rotational speed of the shaker should be verified
Equivalent supplies are acceptable.
with a tachometer before each use. The specified direction of
6.8.1 Disposable 30- and 1-mL plastic syringes,
rotation should be followed (vessel cap leads rotation on
6.8.2 20-Lplastic or glass carboy, stirring plate and stir bar.
start-up).
6.8.3 Spatulas, scoops and wide-mouth bottles for sample
5.3 The specified fill volumes of the test vessels must be
handling and storage,
observed as the energy level varies with the amount of fill.
6.8.4 Electronic timer switch.
5.4 Temperature is a factor in emulsification, so it is
important that all components (salt water, oil, and temperature
controlled chamber) are stable at 15° C or the selected test
These devices are described in EPA standards for use in extraction tests: EPA
temperature, before starting.
Method 1310 Extraction Procedure (EP) Toxicity Test Method And Structural
Integrity Test, EPA Method 1311 Toxicity Characteristic Leaching Procedure
5.5 The handling of the samples after the mixtures are
(TCLP), and EPA 1312 Synthetic Precipitation Leaching Procedure (SPLP).
formed is important. Care must be taken to take a representa-
Environmental Protection Agency 1200 Pennsylvania Avenue, N.W. Washington,
tive sample. Excess water should be avoided when sampling. DC 20460. http://www3.epa.gov/
F3045 − 21
7. Reagents 8.2.6 The mixing is initiated using an electronic timer
switch. The vessels are mixed continuously for 12 h at a
7.1 Reagents—Water purified by reverse osmosis or equiva-
rotation speed of 55 RPM.
lent means is used for the test water. Fine granular sodium
8.2.7 After 12 h mixing, the water-in-oil mixtures are
chloride or table salt, non-iodized, is used for making the salt
collected from the vessels and transferred to appropriately
water. The typical brine solution of 33 ‰ (3.3 %) NaCl is
sized glass wide-mouthed jars for observation and analysis.
prepared from salt and purified water and stored in a 20 L
8.2.8 The emulsions are stored at 15 °C or the selected
carboy at ambient temperatures until needed. Alternate salini-
operating temperature for one week, followed by additional
ties may also be prepared for testing. Reagent-grade sea salt
observation and analysis.
mix (for example, SigmaAldrich or equivalent) may be substi-
8.2.9 Each oil is tested in triplicate.
tuted for preparing brine solutions. Fresh water may also be
8.2.10 The visual observations, viscosity, viscoelastic prop-
used for the test to mimic non-saline conditions.
erties and water content of the starting oil and the resulting
7.1.1 Oil—is used as received, but is shaken for 30 minutes
water-in-oil mixture are measured for comparison as outlined
prior to use and is maintained at the test temperature of 15 °C
in the procedures described below.
or the chosen test temperature.
7.1.2 Karl Fischer reagent, 5 mg/mLH O is recommended, 8.3 Sampling and analysis—A small sample is withdrawn
single component, pyridine free.
from each wide-mouth jar for further analysis as described
7.1.3 Toluene, methanol and chloroform, reagent grade, as below. Analysis is performed twice, immediately after mixing
solvent for the Karl-Fischer titration.
and after one week.
7.1.4 Dichloromethane and acetone, as clean-up solvents,
8.4 Sample Analysis for Water Content—Water content is
and RO purified water
measured by a volumetric titrator using an appropriate Karl
Fischer reagent. The solvent is 1:1:2 methanol:chloroform-
8. Procedure
:toluene.Aset of three measurements is made for each sample.
8.1 Crude Oil Sample Collection and Storage—The bulk oil
8.5 Viscosity Measurement of oils—Dynamic viscosities of
as received is mechanically mixed to attain homogeneity prior
the oils are measured at 15 °C using a rotational viscometer
to obtaining a working sample. Working samples are stored in
using concentric cylinder geometry. The appropriate cup and
clean, airtight containers. The working sample is mechanically
spindle combination is selected on the basis of the valid
shaken for 30 min at 15 °C or the selected operating tempera-
viscosity range for each type, as provided by the manufacturer.
ture prior to removing a sub-sample for testing. When not in
The highest suitable shear rate is selected from the manufac-
use, all samples should be stored in a temperature-controlled
turer’s guidance manual. The measurement protocol follows a
room at 5 °C.
one-minute ramp up to the target shear rate, holding for five
8.2 Generating the water-in-oil mixture—In summary,
minutes, then ramping back down to zero to evaluate thixot-
water-in-oilmixturesareformedin2.2 Lfluorinatedvesselson
ropy. The reported value for the oil is the average viscosity
an end-over-end rotary mixer (Associated Design, VA or
over the period of constant shear. Triplicates are performed for
equivalent) at a rotational speed of 55 RPM.
each sample.
8.2.1 Each 2.2 L mixing vessel is filled with 600 mL of
8.6 Viscoelastic Measurements of the water-in-oil
water, either salt or fresh water as selected for the test. The
mixtures—The viscoelastic properties are determined on a
water should be at the test temperature at the time of addition.
rotational rheometer using plate-plate geometry. The sample
8.2.2 Oil is introduced at a ratio of 1:20 oil:water by adding
stage height is set for a 2.00 mm gap to allow for larger water
30 mL of the test oil to the vessel.
th
droplets in the sample (1/10 the gap or less). The sample is
8.2.3 Thevesselsaresealedandmountedintherotarymixer
measured at 15 °C in forced oscillation mode using a stress
such that the cap of each mixing vessel leads the direction of
sweep from 0.100 to 10.0 Pa at a frequency of one reciprocal
rotation to maximize the turbulence of mixing.
second. Values of the complex modulus, storage modulus, loss
8.2.4 The rotary mixer and vessels are held at 15 °C or the
modulus, and the phase shift of the strain response (tan (δ)) are
selectedoperatingtemperatureinatemperaturecontrolledcold
obtained in the linear viscoelastic range (stress independent
roomforthedurationoftheexperiment.(Notethat15 °Cisthe
region of the stress response curve). Samples are measured in
standard temperature for measuring oil properties.) If the
duplicate.
temperature(s)ofinterestsforaspillisdifferent,thetestshould
be performed at those temperatures as well.Testing at different
8.7 Data recording of the measurements—The visual obser-
temperatures necessitate that the entire study be performed at
vations and the data on the water content and the viscoelastic
the new chosen temperature.
measurements are recorded for the water-in-oil mixtures on the
8.2.5 The vessels and their contents are allowed to stand for
test day following the 12-h mixing and again after one week.
4 h to thermally equilibrate.
The water content and viscosity measurements are taken of the
starting oil. All values are recorded to 3-significant-figure
accuracy. For the viscoelastic measurements, it is necessary to
ACS Reagent Chemicals, Specifications and Procedures for Reagents and
Standard-Grade Reference Materials, American Chemical Society, Washington,
record the complex modulus (mPa), storage modulus (mPa).
DC. For suggestions on the testing of reagents not listed by theAmerican Chemical
Viscosity modulus (mPa) and tan delta (V/E). The water
Society, see Analar Standards for Laboratory Chemicals, BDH Ltd., Poole, Dorset,
content is measured as recorded as percentage water in oil by
U.K., and the United States Pharmacopeia and National Formulary, U.S. Pharma-
copeial Convention, Inc. (USPC), Rockville, MD. weight. Three oil samples are taken for the tests, the water
F3045 − 21
content and viscosity are measured in triplicate and the 9.1.1 The values for the replicate sets within each measure-
viscoelastic measurements are taken in duplicate. ment on the oil and on the resulting mixtures should agree
within the percentage specified:
8.8 Calibration Standards and Methods:
Water content - 62%
8.8.1 The mixing apparatus is verified daily with a tachom-
Viscosity - 65%
eter to ensure a rotational rate of 55 RPM 62 RPM.
Viscoelasticity measurements - 6 15 %
8.8.2 The salinity of the salt solution is verified using a
waterqualitymeter(SensIon745orequivalent),3.3.0 % 60.1 A sample measurement is valid if it is within the specified
PSU. tolerance compared with the average values of other individual
8.8.3 The rheometer calibration is checked with certified measurements.
viscosity standards. If the rheometer reading is out of the Water content - 65%
manufacturer’s specification (65 % mPa.s of certified value),
Viscoelasticity measurements - 6 30 %
the instrument is to be serviced by certified technicians.
9.2 The stability is calculated using:
8.8.4 The Karl-Fischer titrant is calibrated following each
complex modulus storage modulus
addition to the titrant reservoir following the manufacturer’s
protocolusingpurifiedwater.Therelativestandarddeviationis starting oil viscosity starting oil viscosity
FS D G
Stability 5 ln
acceptable if less than 1 %. 10000
8.8.5 The Karl-Fischer titration apparatus is checked daily
(1)
using purified Type 1 water (Ultrapure water as defined by
where:
laboratory water standards) in Sample Mode. A response of
complex and storage modulus = mPa
100 % 6 1 % water (by weight) is acceptable.
Starting oil viscosity = mPa.s, and
8.9 Cleaning Labware—A thorough cleaning program is
ln = is the natural logarithm
undertaken throughout the procedure to reduce possible cross-
9.3 The data taken are compared to values in Table 2 to
contamination and accumulation of cont
...


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: F3045 − 20 F3045 − 21
Standard Test Method for
Evaluation of the Type and Viscoelastic Stability of Water-in-
oil Mixtures Formed from Crude Oil and Petroleum Products
Mixed with Water
This standard is issued under the fixed designation F3045; 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
1.1 This test method covers a procedure to determine the water-in-oil emulsification tendencies and stabilities of crude oils and
petroleum products in the laboratory. The results of this test method can provide oil behavior data for input into oil spill models.
1.2 This test method covers a specific method of determining emulsion tendencies and does not cover other procedures that may
be applicable to determining emulsion tendencies.
1.3 The test results obtained using this test method are intended to provide baseline data for the behavior of oil and petroleum
products at sea and input to oil spill models.
1.4 The test results obtained using this test method can be used directly to predict certain facets of oil spill behavior or as input
to oil spill models.
1.5 The accuracy of the test method depends very much on the representative nature of the oil sample used. Certain oils can form
a variety of water-in-oil types depending on their chemical contents at the moment a sample is taken. Other oils are relatively stable
with respect to the type formed
1.6 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.
1.7 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.
1.8 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.
2. Summary of Test Method
2.1 Oil is mixed with 33 ‰ (3.3 %) saline water for 12 h in a standard rotating apparatus. The resulting mixture is characterized
after this shakingmixing period.
This test method is under the jurisdiction of ASTM Committee F20 on Hazardous Substances and Oil Spill Response and is the direct responsibility of Subcommittee
F20.16 on Surveillance and Tracking.
Current edition approved April 1, 2020Sept. 1, 2021. Published April 2020September 2021. Originally approved in 2015. Last previous edition approved in 20152020 as
ɛ1
F3045–15–20. . DOI: 10.1520/F3045–20.10.1520/F3045–21.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
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2.2 The resulting mixture as created in step 2.1, is characterized visually, by by visual qualities, by measuring water content and
by rheological measurements. The mixture is then classified as a stable, meso-stable, unstable emulsion or an entrained water
mixture. Each of these four types of mixtures has different characteristics affecting the oils behavior once spilled.behavior of oil
in the aquatic environment.
3. Terminology
3.1 Definitions:
3.1.1 complex modulus—One of the results of viscoelastic measurement, a measure of the resistance of a viscoelastic substance
to flow under an applied dynamic stress, combining both the non-reversible (viscous) flow of the test substance and the reversible
(elastic) deformation of the test substance.
3.1.2 emulsion—A type of colloid, specifically, a dispersion of small droplets of one immiscible liquid in another.
3.1.2.1 meso-stable emulsions—Emulsions that lack one or more of the compositional factors necessary to form a stable
emulsion, but that are sufficiently stable to persist for short periods, typically a few hours to days.
3.1.2.2 stable emulsions—Emulsions that persist indefinitely, consisting of fine droplets with a rigid film interface which resists
coalescence.
3.1.2.3 unstable emulsions—Mixtures of water and oil that resolve rapidly into two phases, usually within a few minutes to
hours. There may be residual water remaining in low percentages.
3.1.2.4 water-in-oil emulsion—An emulsion consisting of a continuous phase of oil containing a dispersed phase of water.
3.1.3 entrained water—This is not an emulsion but a mechanical mixture of oil and water which has not separated due to the
physical properties of the water and oil.
3.1.3.1 Discussion—
Typically, the oil and water have similar densities and the oil phase has a high viscosity.
3.1.4 rag—The remnant of a broken water-in-oil emulsion.
3.1.4.1 Discussion—
Rag will not reform an emulsion. Rag is thought to consist of tightly bound asphaltenes and resins.
3.1.5 stability index—An index describing the stability of an emulsion.
3.1.5.1 Discussion—
In this standard, it is calculated using data derived from rheological measurements.
3.1.6 storage modulus—One of the results of viscoelastic measurement, a measure of the elastic (reversible) deformation behavior
of a viscoelastic substance under an applied dynamic stress.
4. Significance and Use
4.1 A standard test is necessary to establish a behavior pattern for spilled crude oils or petroleum products at different oil
weathering stages.
4.2 Water-in-oil mixtures vary with oil type and oil conditions such as weathering. Results from this test method form a baseline,
and usually are a measure of behavior at sea.
4.3 This test has been developed over many years using standardized equipment, test procedures, and to overcome difficulties
noted in other test procedures.
4.4 This test should be performed at the temperatures and degrees of weathering corresponding to the spill conditions of interest.
5. Interferences and Sources of Error
5.1 Interferences can be caused by contaminants, particularly such as residual oil or surfactants on labware, and other sample
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handling supplies and apparatus that lead to irregular results. Surfactants in particular will influence results, as small amounts will
disrupt the stability of a water-in-oil emulsion. All glassware must be thoroughly cleaned. The cleaning process includes rinsing
with dichloromethane to remove the oil, followed by rinsing three times each with tap water, purified water (reverse osmosis), and
acetone. Once cleaned, precautions must be taken to minimize contact of the labware with contaminants to prevent interferences.
5.2 Emulsion formation is somewhat susceptible to energy levels. The rotational speed of the shaker should be checkedverified
with a tachometer every day. before each use. The specified direction of rotation should be followed (vessel cap leads rotation on
start-up).
5.3 The specified fill volumes of the test vessels must be observed as the energy level varies with the amount of fill.
5.4 Temperature is a factor in emulsification, so it is important that all components (salt water, pre-mix,oil, and temperature
controlled chamber) are stable at 15° C or the selected test temperature, before starting.
5.5 The handling of the samples after the mixtures are formed is important. Care must be taken to take a representative sample.
Excess water should be avoided when sampling.
5.6 Since the test results may be affected by salinity, thorough mixing of the salt water is required. Salinity should be verified using
a salinity meter before use.
5.7 Oil sources, recovered for a source, especially crude oil sources,fields, vary much with production timeconditions and
conditions. over time. Oil samples mustshould be treated as unique considered as indicative of the oil source at a moment within
a range of variability and are not necessarily representative of all oil recovered from the source. Some oils are near the threshold
of two different water-in-oil types. Depending on the actual conditions under which thisthe oil was sampled, different results may
occur. Other oils are not as sensitive.
5.8 Additives introduced in the production and transport of oils can change their emulsification behavior. Some oils have added
asphaltene suspenders or emulsion inhibitors. These may significantly alter the outcome of this test. Information on the oil
treatment should be obtained before making the test.
6. Apparatus
6.1 2.2-litre fluorinated HDPE wide-mouth bottles, approximately 24 cm in height and 6 cm in radius (Nalgene or equivalent),
used as the test vessel. These vessels match the shaker as described below.
6.2 Variable speed end-over-end rotary mixer capable of maintaining 55 RPM, with a radius of rotation of 15 cm (7.5 cm from
center of vessel) (Associated Design or equivalent).
6.3 Automated Karl Fischer titration analyser, This device is used to measure the water content of the resulting water-in-oil
mixture.
6.4 Rheometer, with a 35 mm parallel-plate geometry, capable of functioning in forced-oscillation mode. mode with parallel plate
geometry. This device is used to measure the rheological properties of the resulting water-in-oil mixture.
6.5 Circulating bath with a range from 0 to 25 °C (60.1).
6.6 Salinometer or water quality meter, SensIon 745 or equivalent.equivalent with a sensitivity of 60.1 PSU (practical salinity
unit).
6.7 Oil-mixing devices including a shaker for mixing the small samples prior to use and devices to mix the oil contained in drums.
These devices are described in EPA standards for use in extraction tests: EPA Method 1310 Extraction Procedure (EP) Toxicity Test Method And Structural Integrity Test,
EPA Method 1311 Toxicity Characteristic Leaching Procedure (TCLP), and EPA 1312 Synthetic Precipitation Leaching Procedure (SPLP). Environmental Protection Agency
1200 Pennsylvania Avenue, N.W. Washington, DC 20460. http://www3.epa.gov/
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6.8 The following is a list of other necessary supplies. Equivalent supplies are acceptable.
6.8.1 Disposable 30- and 1-mL plastic syringes,
6.8.2 20-L plastic or glass carboy, stirring plate and stir bar.
6.8.3 Spatulas Spatulas, scoops and wide-mouth bottles for sample handling and storage,
6.8.4 Electronic timer switch.
7. Reagents
7.1 Reagents—Water purified by reverse osmosis or equivalent means is used for the test water. Fine granular sodium chloride or
table salt, non-iodized, is used for making the salt water. The typical brine solution of 33 ‰ (3.3 %) NaCl is prepared from salt
and purified water, iswater and stored in a 20 L carboy at ambient temperatures until needed. Alternate salinities may also be
prepared for testing. Reagent-grade sea salt mix (for example, SigmaAldrich or equivalent) may be substituted for preparing brine
solutions. Fresh water may also be used for the test to mimic non-saline conditions.
7.1.1 Oil—is used as received, but is shaken for 30 minutes prior to use and is maintained at the test temperature of 15 °C or the
chosen test temperature.
7.1.2 Karl Fischer reagent, 5 mg/mL H O, O is recommended, single component, pyridine free.
7.1.3 Toluene, methanol and chloroform, reagent grade, as solvent for the Karl-Fischer titration.
7.1.4 Dichloromethane and acetone, as clean-up solvents, and RO purified water
8. Procedure
8.1 Crude Oil Sample Collection and Storage—The bulk oil as received is mechanically mixed for 1 to 2 hto attain homogeneity
prior to obtaining a working sample. Working samples are stored in 2-L high-density polyethylene bottles with polypropylene
screw closures. clean, airtight containers. The working sample is mechanically shaken for 30 min at 15 °C or the selected operating
temperature prior to removing a sub-sample for testing. When not in use, all samples should be stored in a temperature-controlled
room at 5 °C.
8.2 Generating the water-in-oil mixture—In summary, water-in-oil mixtures are formed in 2.2 L fluorinated vessels on an
end-over-end rotary mixer (Associated Design, VA or equivalent) at a rotational speed of 55 RPM.
8.2.1 Each 2.2 L mixing vessel is filled with 600 mL of water, either salt or fresh water as selected for the test. The water should
be at the test temperature at the time of addition.
8.2.2 Oil is introduced at a ratio of 1:20 oil:water by adding 30 mL of the test oil to the vessel.
8.2.3 The vessels are sealed and mounted in the rotary mixer such that the cap of each mixing vessel leads the direction of rotation
to maximize the turbulence of mixing.
8.2.4 The rotary mixer and vessels are held at 15 °C or the selected operating temperature in a temperature controlled cold room
for the duration of the experiment. This temperature (15 °C) or the selected operating temperature (Note that 15 °C is the standard
temperature for measuring oil properties,properties.) If the predicted temperatures the time of temperature(s) of interests for a spill
are differentis different, the test should be performed at those predicted temperatures as well. Testing at different temperatures
necessitate that the entire study be performed at the new chosen temperature.
8.2.5 The vessels and their contents are allowed to stand for 4 h to thermally equilibrate.
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.
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8.2.6 The mixing is initiated using an electronic timer switch. The vessels are mixed continuously for 12 h at a rotation speed of
55 RPM.
8.2.7 After 12 h mixing, the water-in-oil mixtures are collected from the vessels and transferred to appropriately sized glass
wide-mouthed jars for observation and analysis.
8.2.8 The emulsions are stored in the cold room at 15 °C or the selected operating temperature for one week, followed by
additional observation and analysis.
8.2.9 Each oil is tested in triplicate.
8.2.10 The visual observations, viscosity, viscoelastic properties and water content of the starting oil and the resulting water-in-oil
mixture are measured for comparison as outlined in the procedures described below.
8.3 Sampling and analysis—A small sample is withdrawn from each wide-mouth jar for further analysis as described below.
Analysis is performed twice, immediately after mixing and after one week.
8.4 Sample Analysis for Water Content—Water content is measured using a Metrohm 784 KFP Titrino Karl Fischer volumetric
titrator (or equivalent) and Metrohm 703 Ti Stand (or equivalent). The titre reagent is Aquastar Comp 5 (or equivalent) and the
by a volumetric titrator using an appropriate Karl Fischer reagent. The solvent is 1:1:2 methanol:chloroform:toluene. A set of three
measurements areis made for each sample.
8.5 Viscosity Measurement of oils—Dynamic viscosities of the oils are measured at 15 °C using a VT550 with rotational
viscometer using concentric cylinder geometry. The appropriate cup and spindle combination is selected on the basis of the valid
viscosity range for each type, as provided by the manufacturer. The highest suitable shear rate is selected from the manufacturer’s
guidance manual. The measurement protocol follows a one-minute ramp up to the target shear rate, holding for five minutes, then
ramping back down to zero to evaluate thixotropy. The reported value for the oil is the average viscosity over the five minutes hold
period.period of constant shear. Triplicates are performed for each sample.
8.6 Viscoelastic Measurements of the water-in-oil mixtures—The viscoelastic properties are determined on a ThermoHaake
RheoStress RS6000 rheometer with RheoWin software (or equivalent) using 35 mm plate-plate geometry in forced oscillation
mode. rotational rheometer using plate-plate geometry. The sample stage height is set for a 2.00 mm gap. gap to allow for larger
th
water droplets in the sample (1/10 the gap or less). The sample is measured at 15 °C in forced oscillation mode using a stress
sweep from 0.100 to 10.0 Pa at a frequency of one reciprocal second. Values of the complex modulus, storage modulus, loss
modulus, and tan (δ) the phase shift of the strain response (tan (δ)) are obtained in the linear viscoelastic range (stress independent
region of the stress response curve). Samples are measured in duplicate.
8.7 Data recording of the measurements—The visual observations and the data on the water content and the viscoelastic
measurements are recorded for the water-in-oil mixtures on the test day following the 12-h mixing and again after one week. The
water content and viscosity measurements are taken of the starting oil. All values are recorded to 3-significant-figure accuracy. For
the viscoelastic measurements, it is necessary to record the complex modulus (mPa), storage modulus (mPa). Viscosity modulus
(mPa) and tan delta (V/E). The water content is measured as recorded as percentage water in oil by weight. Three oil samples are
taken for the tests, the water content and viscosity are measured in triplicate and the viscoelastic measurements are taken in
duplicate.
8.8 Calibration Standards and Methods:
8.8.1 The mixing apparatus is checkedverified daily with a tachometer to ensure a rotational rate of 55 RPM 62 RPM.
8.8.2 The salinity of the salt solution is verified using a water quality meter (SensIon 745 or equivalent), 3.3%0.05 degrees
salinity or ppt.3.3.0 % 6 0.1 PSU.
8.8.3 The rheometer calibration is checked with certified viscosity standards. If the rheometer reading is out of the manufacturer’s
specification (5%(65 % mPa.s of certified value), the instrument is to be serviced by certified technicians.
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8.8.4 The Karl-Fischer titrant is calibrated following each addition to the titrant reservoir following the manufacturer’s protocol
using purified water. The relative standard deviation is acceptable if less than 1 %.
8.8.5 The Karl-Fischer titration apparatus is checked daily using purified Type 1 water (Ultrapure water as defined by laboratory
water standards) in Sample Mode. A response of 100 % 6 1 % water (by weight) is acceptable.
8.9 Cleaning Labware—A thorough cleaning program is undertaken throughout the procedure to reduce possible cross-
contamination and accumulation of contaminants on the labware. Labware is thoroughly rinsed with, DCM, cleaned with DCM
and rinsed with tap and purified (RO) water, between each experimental run. Glassware is dried at 180 °C while plastic ware is
air dried. run and allowed to dry. Rheometer spindles are cleaned with DCM and acetone.
9. Calculation and Reporting
9.1 The values of viscosity, water content and the values from the viscoelastic measurements are ev
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