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Electronically reprinted from November 2019

www.chemengonline.com Computational Dynamics

Heat Transfer Facts at Your Fingertips: Pneumatic Conveying Sustainable Supply Chains Focus on Packaging Water Treatment Production of Nitrile Rubber Security Audits ASTM Standards For Transfer This practical overview of ASTM standards can serve as a roadmap when selecting and evaluating fluids

Gerald E. Guffey II Eastman Chemical ability of the fluid, safety in use, effect Eastman Chemical Co. on equipment, efficiency (heat-trans- eat-transfer-fluid systems fer capability) and service life. are often used for pro- Pumpability. Several properties are cess heating to 500°F relevant to the pumpability of a heat Hor higher. To accomplish transfer fluid. Pumpability is briefly heating above 500°F, steam pres- discussed in this standard, but it is sure must be above 600 psig. For discussed more extensively in D8046. many plants, distributing steam Decreased flash point (measured by above 600 psig is impractical due D92 or D93) is indicative of the pres- to high cost and more stringent wa- ence of low- compounds pro- ter-purity requirements. High-tem- duced by thermal degradation of the perature heat-transfer fluids have fluid. (measured by D445 or a much lower vapor than D7042) is a measurement of the flu- water at high , so the id’s resistance to flow. The presence design pressure of a heat-transfer- of thermal degradation products can fluid system can be lower. affect the viscosity of the fluid. As fluid Most systems operate with the temperature is decreased, at some heat transfer fluid in the phase. point the fluid viscosity becomes too A few heat transfer fluids have a high to pump. There is some correla- narrow boiling range and can be FIGURE 1. One type of synthetic organic heat tion between hydraulic shock during used in a vapor-phase system, but transfer fluid is shown here pumping with the fluid’s specific grav- the design of the system is much ity (measured by D1298 or D4052) different and the process heating transfer fluids other than inorganic and compressibility properties. Water temperature must match the boiling eutectic salts. This article provides an in a heat-transfer-fluid system will va- range of the fluid. overview of these standards. ASTM porize and expand as system tem- High-temperature heat-transfer standards are listed using their ASTM perature is increased, building pres- fluids are generally classified as inor- designations, for example D5372. sure. It is therefore important to keep ganic eutectic salts, synthetic organ- “D” indicates that the standard is water out of the system as much as ics (Figure 1), aromatic oils, paraffinic administered by one of the D com- possible. Water content can be mea- oils and silicone-based fluids. The mittees. “5372” is the number of the sured using D95. chemistry of each heat-transfer fluid standard. These designations are Safety. Factors related to safety in is different, so each fluid has differ- used throughout this article. use include autoignition temperature ent properties. Considerable back- and flashpoint. Autoignition temper- ground and technical information ASTM D5372 standard guide ature can be measured using E659. about heat transfer fluids is provided ASTM D5372, “Standard Guide for The user should keep in mind that in chapter 21 of the ASTM and Evaluation of Hydrocarbon Heat a hydrocarbon fluid absorbed on a Lubricants Handbook. A new version Transfer Fluids,” covers the factors porous inert surface (such as insula- of this handbook is expected to be that should be considered to char- tion) can ignite at more published this month. acterize a heat transfer fluid. These than 50°C lower than the value de- ASTM International (formerly factors are also relevant to selection termined by E659. Flashpoint (mea- known as the American Society for of a new heat-transfer fluid, so it can sured by D92 Cleveland open cup Testing and Materials; West Con- be used as a reference when choos- tester or D93 Pensky-Martens closed shohocken, Pa.; www.astm.org) has ing a new fluid. These factors are cup tester) indicates the temperature developed several standards for heat grouped into five categories: pump- at which flammable vapors given off by a liquid form a mixture with air that ASTM D7665 standard guide of thermal degradation products is can be ignited by contact with a hot ASTM D7665, “Standard Guide for done by chromatography (GC), surface, spark, or flame. Evaluation of Biodegradable Heat distillation and weighing. Effect on equipment. Two ASTM Transfer Fluids,” addresses biode- Before D6743 was developed, standards can provide information gradable heat transfer fluids. It cov- each heat-transfer-fluid manufac- about the effect of the heat transfer ers the same factors mentioned in turer had its own method for deter- fluid on equipment. D471 provides D5372 but also includes a few oth- mining thermal stability. There were data about the effect of the fluid on ers. (measured by differences in the methods, as well rubber or elastomeric seals. G4 is a D2879) is included as a factor that in- as differences in the equipment used guide for conducting corrosion tests in fluences pumpability of the fluid. Bio- to conduct them. These differences field applications. degradation (measured by D5864) is sometimes led to conflicting test re- Efficiency. Several properties — included as a factor to consider for sults. One supplier’s test data might , specific heat, safety in use. D6384, which covers indicate that fluid A was more ther- density and viscosity — are relevant terminology related to biodegrad- mally stable than fluid B, while an- to the heat transfer capability of the ability and ecotoxicity of lubricants, other supplier’s test data might show fluid. These are the properties used to is listed as a reference document. the opposite. calculate Reynolds number, Prandtl D7044, which is a specification for D6743 provides a standard test number and , which biodegradable fire-resistant hydrau- method for developing data that a determine the heat transfer coeffi- lic fluids, is also listed as a reference. user can evaluate to compare heat cient. D2717 measures thermal con- transfer fluids. Using D6743, ther- ductivity, D1298 or D4052 measures ASTM D6743 standard test method mal stability of two or more different specific gravity, and D445 or D7042 ASTM D6743, “Standard Test heat-transfer-fluid chemistries can measures viscosity. D2766, the test Method for Thermal Stability of Or- be directly compared by heating method listed for specific heat, has ganic Heat Transfer Fluids,” is a them at the same time in the same recently been withdrawn but E1269 test method that measures ther- oven, and then analyzing them and E2716 are other methods that mal stability of a heat transfer fluid. using the same equipment. D6743 could be considered. Thermal stability is the resistance to is very specific about the type of Service life. Heat transfer fluids de- permanent change in fluid proper- equipment that can be used. For grade when exposed to sufficiently ties caused solely by heat. All heat- example, it specifies the type and high temperature. The amount of transfer fluids degrade with expo- length of the GC column, film type degradation increases as tempera- sure to high temperature over time. and thickness, type of detector, ture increases or exposure time Typically, the user wants their heat calibrant range, material and dimen- increases. Thermal stability is mea- transfer fluid to last for many years. sions of the ampoule, temperature sured using D6743. It’s important to select a fluid that is control capability of the oven, and Several tests are used to deter- thermally stable enough to last for accuracy of the balance for weigh- mine the condition of the fluid and many years at the expected system ing. Statistical analysis of test data its remaining service life. These operating temperature. from one laboratory showed very tests include precipitation number The thermal degradation products good repeatability of test results (measured by D91), insoluble con- for most heat transfer fluids include (see the precision and bias state- tent (measured by D893), flash point high- and low-boiling components, ment in the method). (measured by D92 or D93), carbon very low-boiling , and residue DIN (Deutsches Institute für Nor- residue (measured by D189, D524 that cannot be evaporated. The mung e.V.; Berlin, Germany; www. or D4530), distillation (D86, D1160 presence of degradation products in din.de) also has a test method for and D2887 are listed but D2887 is the fluid affects its properties. thermal stability, but it is less specific more commonly used), neutralization D6743 quantifies the high-boiling about the test equipment that can number (measured by D664), color components, low-boiling compo- be used. Differences in test equip- (measured by D1500), viscosity, vis- nents, very low-boiling gases, and ment used can cause significant dif- cosity index (measured by D2270) residue that cannot be evaporated ferences in test results. and water content (measured by for a heat transfer fluid that is ex- D95). Typically, a sample of used posed to specified temperature for ASTM D7863 standard guide heat-transfer fluid should be taken a specified time period. The test ASTM D7863, “Standard Guide for from each system at least once per procedure consists of weighing heat Evaluation of Convective Heat Trans- year so that these tests can be con- transfer fluid into a stainless-steel fer Coefficient of ,” provides ducted to evaluate fluid condition. ampoule, purging with nitrogen, information about the calculation of To ensure that the sample is repre- sealing the ampoule, and heating convective heat-transfer coefficient. sentative, it should be taken from it in an oven. After the ampoule is The factors that affect calculation of the main circulating loop rather than removed from the oven and cooled, convective heat-transfer coefficient from a dead leg. Some heat transfer the fluid is analyzed to quantify the are described. Results from previous fluid suppliers offer free evaluation of amount of thermal degradation studies have been presented in dif- used fluid using these tests. products produced. Measurement ferent ways, so direct comparison of LIST OF ASTM STANDARDS REFERENCED IN THIS ARTICLE D5372 Standard Guide for Evaluation of Hydrocarbon Heat Trans- due (Micro Method) fer Fluids D86 Standard Test Method for Distillation of Petroleum Products D93 Standard Test Methods for Flash Point by Pensky-Martens and Liquid Fuels at Atmospheric Pressure Closed Cup Tester D1160 Standard Test Method for Distillation of Petroleum Products D445 Standard Test Method for Kinematic Viscosity of Transpar- at Reduced Pressure ent and Opaque Liquids (and Calculation of Dynamic Vis- D2887 Standard Test Method for Boiling Range Distribution of Pe- cosity) troleum Fractions by Gas Chromatography D7042 Standard Test Method for Dynamic Viscosity and Density D664 Standard Test Method for Acid Number of Petroleum Prod- of Liquids by Stabinger Viscometer (and the Calculation of ucts by Potentiometric Titration Kinematic Viscosity) D1500 Standard Test Method for ASTM Color of Petroleum Prod- D1298 Standard Test Method for Density, Relative Density, or API ucts (ASTM Color Scale) Gravity of Crude Petroleum and Liquid Petroleum Products D2270 Standard Practice for Calculating Viscosity Index from Ki- by Hydrometer Method nematic Viscosity at 40 °C and 100 °C D4052 Standard Test Method for Density, Relative Density, and API D7665 Standard Guide for Evaluation of Biodegradable Heat Gravity of Liquids by Digital Density Meter Transfer Fluids D95 Standard Test Method for Water in Petroleum Products and D2879 Standard Test Method for Vapor Pressure-Temperature Re- Bituminous Materials by Distillation lationship and Initial Decomposition Temperature of Liquids E659 Standard Test Method for Autoignition Temperature of by Isoteniscope Chemicals D5864 Standard Test Method for Determining Aerobic Aquatic D92 Standard Test Method for Flash and Fire Points by Cleve- Biodegradation of Lubricants or Their Components land Open Cup Tester D6384 Standard Terminology Relating to Biodegradability and D471 Standard Test Method for Rubber Property—Effect of Liq- Ecotoxicity of Lubricants uids D7044 Standard Specification for Biodegradable Fire Resistant G4 Standard Guide for Conducting Corrosion Tests in Field Ap- Hydraulic Fluids plications D7863 Standard Guide for Evaluation of Convective Heat Transfer D2717 Standard Test Method for Thermal Conductivity of Liquids Coefficient of Liquids D6743 Standard Test Method for Thermal Stability of Organic Heat D8046 Standard Guide for Pumpability of Heat Transfer Fluids Transfer Fluids E794 Standard Test Method for And Tem- D91 Standard Test Method for Precipitation Number of Lubri- peratures By Thermal Analysis cating Oils D2983 Standard Test Method for Low-Temperature Viscosity of D893 Standard Test Method for Insolubles in Used Lubricating Automatic Transmission Fluids, Hydraulic Fluids, and Lubri- Oils cants using a Rotational Viscometer D189 Standard Test Method for Conradson Carbon Residue of D891 Standard Test Methods for Specific Gravity, Apparent, of Petroleum Products Liquid Industrial Chemicals D524 Standard Test Method for Ramsbottom Carbon Residue of D6304 Standard Test Method for Determination of Water in Petro- Petroleum Products leum Products, Lubricating Oils, and Additives by Coulo- D4530 Standard Test Method for Determination of Carbon Resi- metric Karl Fischer Titration convective heat-transfer-coefficient to interpret, present and report the rangement, net positive-suction head data from these studies can be chal- test results are explained. required by the pump, and electric lenging. Therefore, this guide focuses motor sizing. The need to consider on describing a standard approach ASTM D8046 standard guide how fluid viscosity will change as the for obtaining data, interpreting data, ASTM D8046, “Standard Guide for fluid degrades and how that affects and presenting results. Pumpability of Heat Transfer Flu- pump and motor selection is also This guide describes a test equip- ids,” discusses the fluid properties discussed. This guide addresses ment arrangement with turbu- and system configuration issues several considerations about pump- lent fluid flow inside an electrically that affect the ability to pump a heat ing that are a useful reference when heated tube that has a wall tem- transfer fluid. These properties in- selecting a new heat-transfer fluid.n perature higher than the bulk fluid clude flashpoint (measured by D92 Edited by Gerald Ondrey temperature. Features of this test- or D93), crystallization temperature equipment arrangement are dis- (measured by E794), viscosity (mea- Author cussed and the required measure- sured by D445, D2983 or D7042), Gerald Guffey is a senior associate ments are defined. The ASTM test relative density (measured by D891 in the Worldwide Engineer- ing and Construction Division of East- methods recommended for mak- or D4052), water content (measured man Chemical Co. (100 Eastman ing each of the required measure- by D6304), vapor pressure (mea- Road, Kingsport, TN 37660; Phone: ments are listed. Considerations for sured by D2879), and boiling range 423-229-1095; Email: gguffey@ eastman.com). He has been involved calibration of the test equipment are distribution (measured by D2887). in design and evaluation of heat discussed. Formulas used to cal- System configuration issues include transfer fluid systems and fired heat- ers for more than twenty years. He has been a member of culate the heat-transfer coefficient the type of pump used, mechanical ASTM since 1997. He holds a Bachelor of Science degree are summarized. Appropriate ways seals, the pump suction ar- in from Georgia Tech.

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