ASTM D5188-2010a Standard Test Method for Vapor-Liquid Ratio Temperature Determination of Fuels (Evacuated Chamber Method)《燃料的汽液比温度测定的标准试验方法(真空室法)》.pdf
《ASTM D5188-2010a Standard Test Method for Vapor-Liquid Ratio Temperature Determination of Fuels (Evacuated Chamber Method)《燃料的汽液比温度测定的标准试验方法(真空室法)》.pdf》由会员分享,可在线阅读,更多相关《ASTM D5188-2010a Standard Test Method for Vapor-Liquid Ratio Temperature Determination of Fuels (Evacuated Chamber Method)《燃料的汽液比温度测定的标准试验方法(真空室法)》.pdf(5页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: D5188 10aStandard Test Method forVapor-Liquid Ratio Temperature Determination of Fuels(Evacuated Chamber Method)1This standard is issued under the fixed designation D5188; the number immediately following the designation indicates the year oforiginal adoption or, in the case of revision
2、, the year of last revision. A number 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 covers the determination of the tem-perature at which the vapor formed from a selected
3、 volume ofvolatile petroleum product saturated with air at 0 to 1C (32 to34F) produces a pressure of one atmosphere in an evacuatedchamber of fixed volume. This test method is applicable tosamples for which the determined temperature is between 36and 80C (97 and 176F) and the vapor-liquid ratio is b
4、etween8 to 1 and 75 to 1.NOTE 1When the vapor-liquid ratio is 20:1, the result is intended tobe comparable to the results determined by Test Method D2533.NOTE 2This test method may also be applicable at pressures otherthan one atmosphere, but the stated precision may not apply.1.2 This test method i
5、s applicable to both gasoline andgasoline-oxygenate blends.1.2.1 Some gasoline-oxygenate blends may show a hazewhen cooled to 0 to 1C. If a haze is observed in 12.5, it shallbe indicated in the reporting of results. The precision and biasstatements for hazy samples have not been determined (seeNote
6、10).1.3 The values stated in SI units are to be regarded asstandard. The values given in parentheses are provided forinformation only.1.4 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 standard to esta
7、blish appro-priate safety and health practices and determine the applica-bility of regulatory limitations prior to use. For specificwarnings, see 7.2 and 8.1.1.2. Referenced Documents2.1 ASTM Standards:2D2533 Test Method for Vapor-Liquid Ratio of Spark-Ignition Engine Fuels3D2892 Test Method for Dis
8、tillation of Crude Petroleum(15-Theoretical Plate Column)D4057 Practice for Manual Sampling of Petroleum andPetroleum ProductsD6299 Practice for Applying Statistical Quality Assuranceand Control Charting Techniques to Evaluate AnalyticalMeasurement System Performance3. Terminology3.1 Definitions of
9、Terms Specific to This Standard:3.1.1 T(V/L = 20), nthe equilibrium temperature at whichthe partial pressure of a sample under test conditions is equalto 101.3 kPa (14.69 psia) and the vapor-liquid ratio is 20.3.1.2 vapor-liquid ratio of a fuel, nthe ratio at a specifiedtemperature and pressure of t
10、he volume of vapor in equilibriumwith liquid to the volume of sample charged, as a liquid, at 0C(32F).4. Summary of Test Method4.1 A known volume of chilled, air-saturated sample isintroduced into an evacuated, thermostatically controlled testchamber of known volume. The sample volume is calculated
11、togive the desired vapor-liquid ratio for the chamber volume inuse. After injection, the chamber temperature is adjusted untila stable chamber pressure of 101.3 kPa (14.69 psia) isachieved.5. Significance and Use5.1 The tendency of a fuel to vaporize in automotive enginefuel systems is indicated by
12、the vapor-liquid ratio of the fuel.5.2 Automotive fuel specifications generally include T(V/L = 20) limits to ensure products of suitable volatility perfor-mance. For high ambient temperatures, a fuel with a high valueof T(V/L = 20), indicating a fuel with a low tendency to vaporize,is generally spe
13、cified; conversely for low ambient tempera-tures, a fuel with a low value of T(V/L = 20)is specified.1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.08 on Volatility.Current edition approved Oct
14、. 1, 2010. Published November 2010. Originallyapproved in 1991. Last previous edition approved in 2010 as D518810. DOI:10.1520/D5188-10A.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStandards volume i
15、nformation, refer to the standards Document Summary page onthe ASTM website.3Withdrawn. The last approved version of this historical standard is referencedon www.astm.org.1*A Summary of Changes section appears at the end of this standard.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C7
16、00, West Conshohocken, PA 19428-2959, United States.6. Apparatus6.1 Apparatus suitable for use shall employ a small volumetest chamber incorporating a transducer for pressure measure-ments and associated equipment for thermostatically control-ling the chamber temperature, evacuating the test chamber
17、prior to sample introduction, and cleaning and purging thechamber following the test. Critical elements of the apparatusshall meet the following specifications:6.1.1 Test Chamber, constructed of stainless steel or alumi-num, designed to contain between 5 and 50 mL of liquid plusvapor with a toleranc
18、e of 61 % of the nominal capacity.NOTE 3The test chamber volumes of the instruments used for the1991 cooperative test program to determine the precision and biasstatements were between 5 and 15 mLof liquid plus vapor with a toleranceof 61 % of the nominal capacity.6.1.2 Pressure Transducer, minimum
19、operational rangefrom 1 to 177 kPa (0 to 25.6 psia) with minimum resolution of0.1 kPa (0.01 psi) and minimum accuracy of 60.8 kPa (60.12psi). The pressure measurement system shall include associ-ated electronics and readout devices to display the resultingpressure reading.6.1.3 Heater, thermostatica
20、lly controlled heater capable ofmaintaining the test chamber within 0.1C of the set tempera-ture for a minimum of 5 min.NOTE 4The use of automated instruments that automatically adjustthe temperature, after sample injection, to give a pressure of 101.3 kPa(14.69 psia) is allowed.6.1.4 Platinum Resis
21、tance Thermometer, used to measurethe temperature of the test chamber, having a minimumtemperature range of 36 to 80C, minimum resolution of 0.1C(0.2F) and minimum accuracy of 60.1C (60.2F).6.2 Vacuum Pump, capable of reducing the pressure in thetest chamber to less than 0.01 kPa (0.001 psia).6.3 Sy
22、ringes, (if required for sample introduction), gas-tight, 1- to 20-mL capacity with minimum accuracy andprecision of 61%.6.4 Bath, iced water or air, for chilling the samples andsyringe (if required) to between 0 and 1C (32 to 34F).6.5 Pressure Measuring Device, capable of measuring localstation pre
23、ssure with an accuracy of 0.20 kPa (0.03 psi) orbetter, at the same elevation relative to sea level as theapparatus in the laboratory.6.5.1 When a mercury manometer is not used as thepressure measuring device, the calibration of the pressuremeasuring device employed shall be periodically checked(wit
24、h traceability to a nationally recognized standard) to ensurethat the device remains within the required accuracy specifiedin 6.5.6.6 McLeod Vacuum Gage or Calibrated Electronic VacuumMeasuring Device for Calibration, to cover at least the rangefrom 0.01 to 0.67 kPa (0.1 to 5 mm Hg). The calibration
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