Standard Guide for Evaluation of Hydrocarbon Heat Transfer Fluids

SCOPE
1.1 This guide provides information, without specific limits, for selecting standard test methods for testing heat transfer fluids for quality and aging. These test methods are considered particularly useful in characterizing hydrocarbon heat transfer fluids in closed systems.

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Publication Date
09-Nov-1998
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ASTM D5372-93(1998) - Standard Guide for Evaluation of Hydrocarbon Heat Transfer Fluids
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NOTICE: This standard has either been superseded and replaced by a new version or withdrawn.
Contact ASTM International (www.astm.org) for the latest information
An American National Standard
Designation: D 5372 – 93 (Reapproved 1998)
Standard Guide for
Evaluation of Hydrocarbon Heat Transfer Fluids
This standard is issued under the fixed designation D 5372; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
2 3
1. Scope Petroleum Products by Hydrometer Method
D 1500 Test Method for ASTM Color of Petroleum Prod-
1.1 This guide provides information, without specific limits,
ucts (ASTM Color Scale)
for selecting standard test methods for testing heat transfer
D 2160 Test Method for Thermal Stability of Hydraulic
fluids for quality and aging. These test methods are considered
Fluids
particularly useful in characterizing hydrocarbon heat transfer
D 2270 Practice for Calculating Viscosity Index from Kine-
fluids in closed systems.
matic Viscosity at 40 and 100°C
2. Referenced Documents D 2717 Test Method for Thermal Conductivity of Liquids
D 2766 Test Method for Specific Heat of Liquids and
2.1 ASTM Standards:
Solids
D 86 Test Method for Distillation of Petroleum Products
D 2887 Test Method for Boiling Range Distribution of
D 91 Test Method for Precipitation Number of Lubricating
Petroleum Fractions by Gas Chromatography
Oils
D 3241 Test Method for Thermal Oxidation Stability of
D 92 Test Method for Flash and Fire Points by Cleveland
Aviation Turbine Fuels (JFTOT Procedure)
Open Cup
D 4530 Test Method for Micro Carbon Residue of Petro-
D 93 Test Methods for Flash Point by Pensky-Martens
leum Products
Closed Tester
E 659 Test Method for Autoignition Temperature of Liquid
D 95 Test Method for Water in Petroleum Products and
Chemicals
Bituminous Materials by Distillation
G 4 Method for Conducting Corrosion Coupon Tests in
D 97 Test Methods for Pour Point of Petroleum Oils
Plant Equipment
D 189 Test Method for Conradson Carbon Residue of
Petroleum Products
3. Terminology
D 445 Test Method for Kinematic Viscosity of Transparent
3.1 Description of Term Specific to This Standard:
and Opaque Liquids (and the Calculation of Dynamic
3 3.1.1 heat transfer fluid—in this guide, a petroleum oil or
Viscosity)
related hydrocarbon material which remains essentially a liquid
D 471 Test Method for Rubber Property—Effect of Liq-
4 while transferring heat to or from an apparatus or process.
uids
Small percentages of nonhydrocarbon components such as
D 524 Test Method for Ramsbottom Carbon Residue of
3 antioxidants and dispersants can be present.
Petroleum Products
D 664 Test Method for Acid Number of Petroleum Products
4. Significance and Use
by Potentiometric Titration
3 4.1 The significance of each test method will depend upon
D 893 Test Method for Insolubles in Used Lubricating Oils
the system in use and the purpose of the test method as listed
D 1160 Test Method for Distillation of Petroleum Products
3 under Section 5. Use the most recent editions of ASTM test
at Reduced Pressure
methods.
D 1298 Test Method for Density, Relative Density (Specific
Gravity), or API Gravity of Crude Petroleum and Liquid
5. Recommended Test Procedures
5.1 Pumpability of the Fluid:
5.1.1 Flash Point, closed cup (Test Method D 93)—This
This guide is under the jurisdiction of ASTM Committee D02 on Petroleum
test method will detect low flash ends which are one cause of
Products and Lubricants and is the direct responsibility of Subcommittee D02.N0 on
cavitation during pumping. In closed systems, especially when
Hydraulic Fluids.
Current edition approved March 15, 1993. Published May 1993.
The background for this standard was developed by a questionnaire circulated
by ASTM-ASLE technical division L-VI-2 and reported in Lubrication Engineer-
ing, Vol 32, No. 8, August 1976, pp. 411–416. Annual Book of ASTM Standards, Vol 05.02.
3 6
Annual Book of ASTM Standards, Vol 05.01. Annual Book of ASTM Standards, Vol 14.02.
4 7
Annual Book of ASTM Standards, Vol 09.01. Annual Book of ASTM Standards, Vol 03.02.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.
D 5372 – 93 (1998)
fluids are exposed to temperatures of 225°C (approximately 5.3 Effect on Equipment:
400°F) or higher, the formation of volatile hydrocarbons by 5.3.1 Effect on Rubber or Elastomeric Seals (Test Method
breakdown of the oil may require venting through a pressure D 471)— Most seals in heat exchange equipment are made of
relief system to prevent dangerous pressure build-up. steel or other metal. If rubber seals are present, it is desirable
5.1.2 Pour Point (Test Method D 97)—The pour point can to maintain rubber swelling in the range of 1 to 5 % to prevent
be used as an approximate guide to the minimum temperature leakage because of poor seal contact. Seals may degrade in
for normal pumping and as a general indication of fluid type some fluids. As an oil deteriorates in service, additional tests
and low temperature properties. Should a heat transfer system may be required to assure that seals remain compatible with the
be likely to be subjected to low temperatures when not in use, altered oil. The temperature ranges of the tests should corre-
the system should be trace heated to warm the fluid above spond to temperatures to which seals will be exposed in
minimum pumping temperature before start-up. service.
5.1.3 Viscosity (Test Method D 445)—Fluid viscosity is of 5.3.2 Corrosion (Guide G 4)—The above tests concern
importance in the determination of Reynolds and Prandtl selection of materials of construction with fluids usable for heat
numbers for heat transfer systems, to estimate fluid turbulence, transfer systems. Guide G 4 uses test metal specimens fixed
heat transfer coefficient, and heat flow. Generally, a fluid that is within the stream of test fluid under use. The specimens and
above approximately 200 centistokes is difficult to pump. The conditions for test must be specified for each system.
pump and system design will determine the viscosity limit 5.4 Effıciency:
required for pumping. The construction of a viscosity/ 5.4.1 Thermal Conductivity (Test Method D 2717) and Spe-
temperature curve using determined viscosities can be used to cific Heat (Test Method D 2766)—These thermal conductivity
estimate minimum pumping temperature. and specific heat tests are difficult to carry out, facilities for
5.1.4 Specific Gravity (Test Method D 1298)—Hydraulic performing them are few, and the precision data is yet to be
shock during pumping has been predicted via the use of a established. Values can be estimated for design use from the
combination of density and compressibility data. general chemical composition. Differences contribute to effi-
5.1.5 Water Content (Test Method D 95)—The water con- ciency to a lesser degree than values such as viscosity, moisture
tent of a fresh heat transfer fluid can be used to indicate how contamination, and other measurable values in 5.1 and 5.5 of
long the heat transfer system must be dried out during this guide. The values for thermal conductivit
...

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