ASTM D1837 - 17 Standard Test Method for Volatility of Liquefied Petroleum (LP) Gases (Withdrawn 2017).pdf
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1、Designation: D1837 17Standard Test Method forVolatility of Liquefied Petroleum (LP) Gases1This standard is issued under the fixed designation D1837; the number immediately following the designation indicates the year oforiginal adoption or, in the case of revision, the year of last revision. A numbe
2、r in parentheses indicates the year of last reapproval. Asuperscript epsilon () indicates an editorial change since the last revision or reapproval.1. Scope*1.1 This test method is a measure of the relative purity ofthe various types of liquefied petroleum (LP) gases and helpsto ensure suitable vola
3、tility performance. The test results, whenproperly related to vapor pressure and density of the product,can be used to indicate the presence of butane and heaviercomponents in propane-type LP-gas, and pentane and heaviercomponents in propane-butane and butane-type fuels. Thepresence of hydrocarbon c
4、ompounds less volatile than those ofwhich the LP-gas is primarily composed is indicated by anincrease in the 95 % evaporated temperature.1.2 When the type and concentration of higher boilingcomponents is required, chromatographic analysis should beused.1.3 The values stated in SI units are to be reg
5、arded as thestandard.1.3.1 ExceptionThe non-SI values are provided for infor-mation only.1.4 WARNINGMercury has been designated by manyregulatory agencies as a hazardous material that can causecentral nervous system, kidney and liver damage. Mercury, orits vapor, may be hazardous to health and corro
6、sive tomaterials. Caution should be taken when handling mercury andmercury containing products. See the applicable product SafetyData Sheet (SDS) for details and EPAs websitehttp:/www.epa.gov/mercury/faq.htmfor additional information.Users should be aware that selling mercury and/or mercurycontainin
7、g products into your state or country may be prohib-ited by law.1.4.1 Note that thallium in a mercury-thallium thermometeris also a hazardous material.1.5 This standard does not purport to address all of thesafety concerns, if any, associated with its use. It is theresponsibility of the user of this
8、 standard to establish appro-priate safety and health practices and determine the applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D96 Test Method for Water and Sediment in Crude Oil byCentrifuge Method (Field Procedure) (Withdrawn 2000)3D1796 Test Met
9、hod for Water and Sediment in Fuel Oils bythe Centrifuge Method (Laboratory Procedure)E1 Specification for ASTM Liquid-in-Glass Thermometers3. Summary of Test Method3.1 Refrigerate the sample by means of a cooling coil andcollect 100 mL of liquid in a weathering tube. Allow toevaporate (“weather”) a
10、t ambient pressure under specifiedconditions that approximate a single plate distillation. Measurethe observed temperature when 5 mL of liquid test portionremains. Correct this observed temperature for barometricpressure and thermometer ice point error, and report as the95 % evaporation temperature.
11、4. Significance and Use4.1 Volatility, expressed in terms of the 95 % evaporatedtemperature of the product, is a measure of the amount of leastvolatile components present in the product. Coupled with avapor pressure limit, it serves to ensure essentially single-component products in the cases of com
12、mercial grades ofpropane and butane. When volatility is coupled with a vaporpressure limit which has been related to density, as in the caseof the commercial PB-mixture, the combination serves toassure essentially two component mixtures for such fuels.When coupled with a proper vapor pressure limit,
13、 this mea-surement serves to assure that special-duty propane productswill be composed chiefly of propane and propylene and thatpropane will be the major constituent.5. Apparatus5.1 Weathering TubeA centrifuge tube, cone-shaped, con-forming to the dimensions given in Fig. 1 and made of1This test met
14、hod is under the jurisdiction of ASTM Committee D02 onPetroleum Products, Liquid Fuels, and Lubricants and is the direct responsibility ofSubcommittee D02.H0 on Liquefied Petroleum Gas.Current edition approved Jan. 1, 2017. Published February 2017. Originallyapproved in 1961. Last previous edition a
15、pproved in 2011 as D1837 11. DOI:10.1520/D1837-17.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStandards volume information, refer to the standards Document Summary page onthe ASTM website.3The last a
16、pproved version of this historical standard is referenced onwww.astm.org.*A Summary of Changes section appears at the end of this standardCopyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United StatesNOTICE: This standard has either been superseded
17、and replaced by a new version or withdrawn.Contact ASTM International (www.astm.org) for the latest information1thoroughly annealed heat-resistant glass.4The shape of thelower tip of the tube is especially important. The taper shall beuniform and the bottom shall be rounded as shown in Fig. 1.The tu
18、bes shall comply in wall thickness to ASTM centrifugetube requirements (Note 1). The graduation tolerances aregiven in Table 1.NOTE 1Requirements for centrifuge tubes appear in Test MethodsD96 and D1796.5.2 Tube SupportMeans shall be provided for supportingthe weathering tube by its neck in a vertic
19、al position.5.3 Water Bath (for use in tests on butane and propane-butane mixture types of liquefied petroleum gas only). Ashallow container filled with clean water having a maintainedtemperature ranging from 15 C to 21 C (60 F to 70 F) anda depth of 38 mm (112 in.).5.4 ThermometerASTM Armored Weath
20、ering Test Ther-mometer having a range from 50 C to 5 C (58 F to 41 F)and conforming to the requirements for Thermometer 99C92(99F86) as prescribed in Specification E1. Do not remove thearmor from the thermometer.5.5 BarometerA pressure measuring device capable ofmeasuring local station pressure wit
21、h an accuracy of 0.1 kPa(1 mm Hg) or better, at the same elevation relative to sea levelas the apparatus in the laboratory. (WarningDo not takereadings from ordinary aneroid barometers, such as those usedat weather stations and airports, since these are precorrected togive sea level readings.)5.6 Sa
22、mpling Precooling Equipment:5.6.1 Cooling VesselAny suitable wide-mouthed metalcontainer or Dewar flask at least 64 mm (212 in.) in insidediameter by 292 mm (1112 in.) deep.5.6.2 Cooling CoilApproximately 6 m (20 ft) of 4.8 mm(316 in.) outside diameter soft copper tubing, wound around ahollow mandre
23、l at least 54 mm (218 in.) in outside diameter,with adjacent turns touching. Run the lower end of the tube upthrough the center of the mandrel before winding so that thefinished coil will fit snugly inside the cooling vessel. Whenassembled, the top of the coil shall be at least 25 mm (1 in.)below th
24、e top of the cooling vessel and the open ends of thecoil shall not be more than 100 mm (4 in.) above. Connect thedownstream end of the coil to a 3.2 mm (18 in.) needle valvehaving an outlet connection not more than 76 mm (3 in.) long(see Fig. 2).5.6.3 PrecoolantThis may be the liquefied petroleum ga
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