ASTM D5482-2001 Standard Test Method for Vapor Pressure of Petroleum Products (Mini Method-Atmospheric)《石油产品蒸气压力的标准试验方法(大气的小型法)》.pdf
《ASTM D5482-2001 Standard Test Method for Vapor Pressure of Petroleum Products (Mini Method-Atmospheric)《石油产品蒸气压力的标准试验方法(大气的小型法)》.pdf》由会员分享,可在线阅读,更多相关《ASTM D5482-2001 Standard Test Method for Vapor Pressure of Petroleum Products (Mini Method-Atmospheric)《石油产品蒸气压力的标准试验方法(大气的小型法)》.pdf(5页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: D 5482 01An American National StandardStandard Test Method forVapor Pressure of Petroleum Products (Mini MethodAtmospheric)1This standard is issued under the fixed designation D 5482; the number immediately following the designation indicates the year oforiginal adoption or, in the case
2、 of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. Asuperscript epsilon (e) indicates an editorial change since the last revision or reapproval.1. Scope *1.1 This test method covers a procedure for the determina-tion of total vapor pressure of pet
3、roleum products usingautomatic vapor pressure instruments. The test method issuitable for testing samples with boiling points above 0C(32F) that exert a vapor pressure between 7 and 110 kPa (1.0and 16 psi) at 37.8C (100F) at a vapor-to-liquid ratio of 4:1.The test method is applicable to gasolines c
4、ontaining oxygen-ates. No account is made of dissolved water in the sample.NOTE 1Because the external atmospheric pressure does not influencethe resultant vapor pressure, this vapor pressure is an absolute pressure at37.8C (100F) in kPa (psi). This vapor pressure differs from the truevapor pressure
5、of the sample due to some small vaporization of the sampleand dissolved air into the air of the confined space.1.1.1 Some gasoline-oxygenate blends my show a hazewhen cooled to 0 to 1 C. If a haze is observed in 8.5, it shallbe indicated in the reporting of results. The precision and biasstatements
6、for hazy samples have not been determined (seeNote 6).1.2 This test method is a modification of Test MethodD 5191 (Mini Method) in which the test chamber is atatmospheric pressure prior to sample injection.1.3 This test method covers the use of automated vaporpressure instruments that perform measur
7、ements on liquidsample sizes in the range from 1 to 10 mL.1.4 This test method is suitable for the determination of thedry vapor pressure equivalent (DVPE) of gasoline andgasoline-oxygenate blends by means of a correlation equation(see 13.2). The calculated DVPE is considered equivalent tothe result
8、 obtained on the same material when tested by TestMethod D 4953.1.5 The values stated in acceptable SI units are regarded asstandard. The values given in parentheses are provided forinformation only.1.6 This standard does not purport to address all of thesafety concerns, if any, associated with its
9、use. It is theresponsibility of the user of this standard to establish appro-priate safety and health practices and determine the applica-bility of regulatory limitations prior to use. (For specific hazardstatements, see 7.2 through 7.7.)2. Referenced Documents2.1 ASTM Standards:D 4057 Practice for
10、Manual Sampling of Petroleum andPetroleum Products2D 4953 Test Method for Vapor Pressure of Gasoline andGasoline-Oxygenate Blends (Dry Method)2D 5190 Test Method for Vapor Pressure of Petroleum Prod-ucts (Automatic Method)2D 5191 Test Method for Vapor Pressure of Petroleum Prod-ucts (Mini Method)23.
11、 Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 dry vapor pressure equivalent (DVPE)a value cal-culated by a correlation equation (see 13.2) from the totalpressure.3.1.1.1 DiscussionThe DVPE is expected to be equivalentto the value obtained on the sample by Test Method D 4953.3.
12、1.2 total pressurethe observed pressure measured in theexperiment that is the resultant pressure increase from theinitial ambient atmospheric pressure.4. Summary of Test Method4.1 A known volume of chilled, air-saturated sample isintroduced into a thermostatically controlled test chamber, theinterna
13、l volume of which is five times that of the total testspecimen introduced into the chamber. The test chamber is atatmospheric pressure prior to introduction of the sample. Afterintroduction of the sample into the test chamber, the testspecimen is allowed to reach thermal equilibrium at the testtempe
14、rature, 37.8C (100F). The resulting rise in pressure inthe chamber is measured using a pressure transducer sensorand indicator.4.2 The measured total vapor pressure is converted to aDVPE by use of a correlation equation (see 13.2).1This test method is under the jurisdiction of ASTM Committee D02 onP
15、etroleum products and Lubricants and is the direct responsibility of SubcommitteeD02.08.ODon RVP and V/L Ratio.Current edition approved May 10, 2001. Published July 2001. Originallypublished as D 5482 93. Last previous edition D 5482 99.2Annual Book of ASTM Standards, Vol 05.02.1*A Summary of Change
16、s section appears at the end of this standard.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.5. Significance and Use5.1 Vapor pressure is an important physical property ofvolatile liquids.5.2 Vapor pressure is critically important fo
17、r both automo-tive and aviation gasolines, affecting starting, warm-up, andtendency to vapor lock with high operating temperatures orhigh altitudes. Maximum vapor pressure limits for gasoline arelegally mandated in some areas as a measure of air pollutioncontrol.6. Apparatus6.1 Vapor Pressure Appara
18、tusThe type of apparatus3suitable for use in this test method employs a small volume testchamber incorporating a transducer for pressure measurementsand associated equipment for thermostatically controlling thechamber temperature.6.1.1 The test chamber shall be designed to contain between2 and 50 mL
19、 of liquid and vapor and be capable of maintaininga vapor-liquid ratio between 3.95 and 1.00 and 4.05 and 1.00.6.1.2 The pressure transducer shall have a minimum opera-tional range from 0 to 172 kPa (0 to 25.0 psi) with a minimumresolution of 0.1 kPa (0.01 psi) and a minimum accuracy of60.3 kPa (60.
20、05 psi). The pressure measurement system shallinclude associated electronics and readout devices to displaythe resulting pressure reading.6.1.3 A thermostatically controlled heater shall be used tomaintain the test chamber at 37.8 6 0.1C (100 6 0.2F) forthe duration of the test.6.1.4 A platinum resi
21、stance thermometer shall be used formeasuring the temperature of the test chamber. The minimumtemperature range of the measuring device shall be fromambient to 75C (167F) with a resolution of 0.1C (0.2F) andaccuracy of 0.1C (0.2F).6.1.5 The vapor pressure apparatus shall have provisions forintroduct
22、ion of the test specimen into the test chamber and forthe cleaning or purging of the chamber following the test.6.2 Syringe, if required, gas tight, 1 to 20 mL capacity witha 61 %, or better, accuracy and a 61 %, or better, precision.The capacity of the syringe shall not exceed two times thevolume o
23、f the test specimen being dispensed, and shall bechosen so as to provide maximum accuracy and resolution forthe volume to be injected.6.3 Iced-Water Bath or Air Bath, for chilling the samplesand syringe to temperatures between 0 and 1C (32 and 34F).6.4 Pressure Measuring Device, capable of measuring
24、 am-bient and above ambient pressures with an accuracy of 0.20kPa (0.03 psi) or better at the same elevation relative to sealevel as the apparatus in the laboratory.6.4.1 When a mercury manometer is not used as thepressure measuring device, the calibration of the pressuremeasuring device employed sh
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