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    ASTM D6377-2010 5000 Standard Test Method for Determination of Vapor Pressure of Crude Oil VPCRx (Expansion Method)《测定原油蒸气压力的标准试验方法 VPCRx(膨胀法)》.pdf

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    ASTM D6377-2010 5000 Standard Test Method for Determination of Vapor Pressure of Crude Oil VPCRx (Expansion Method)《测定原油蒸气压力的标准试验方法 VPCRx(膨胀法)》.pdf

    1、Designation: D6377 10Standard Test Method forDetermination of Vapor Pressure of Crude Oil:VPCRx(Expansion Method)1This standard is issued under the fixed designation D6377; the number immediately following the designation indicates the year oforiginal adoption or, in the case of revision, the year o

    2、f 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 use of automated vaporpressure instruments to determine the vapor pressure exerted inva

    3、cuum of crude oils. This test method is suitable for testingsamples that exert a vapor pressure between 25 and 180 kPa at37.8C at vapor-liquid ratios from 4:1 to 0.02:1 (X=4to0.02).NOTE 1This test method is suitable for the determination of the vaporpressure of crude oils at temperatures from 0 to 1

    4、00C and pressures upto 500 kPa, but the precision and bias statements (see Section 14) may notbe applicable.1.2 This test method allows the determination of vaporpressure for crude oil samples having pour points above 0C.1.3 The values stated in SI units are to be regarded asstandard. No other units

    5、 of measurement are included in thisstandard.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 establish appro-priate safety and health practices and determine the applica-bility of regula

    6、tory limitations prior to use. For specificwarning statements, see 7.2.1-7.3.2.2. Referenced Documents2.1 ASTM Standards:2D323 Test Method for Vapor Pressure of Petroleum Prod-ucts (Reid Method)D2892 Test Method for Distillation of Crude Petroleum(15-Theoretical Plate Column)D3700 Practice for Obtai

    7、ning LPG Samples Using a Float-ing Piston CylinderD4057 Practice for Manual Sampling of Petroleum andPetroleum ProductsD4177 Practice for Automatic Sampling of Petroleum andPetroleum ProductsD5191 Test Method for Vapor Pressure of Petroleum Prod-ucts (Mini Method)D5853 Test Method for Pour Point of

    8、Crude OilsD6708 Practice for StatisticalAssessment and Improvementof Expected Agreement Between Two Test Methods thatPurport to Measure the Same Property of a Material3. Terminology3.1 Definitions:3.1.1 platinum resistance thermometer, ntemperaturemeasuring device constructed with a length of platin

    9、um wire,whose electrical resistance changes in relation to temperature.3.1.2 vapor-liquid ratio (V/L), nthe ratio of the vaporvolume to the liquid volume of specimen, in equilibrium, underspecified conditions.3.2 Definitions of Terms Specific to This Standard:3.2.1 dead crude oila term usually emplo

    10、yed for crudeoils that, when exposed to normal atmospheric pressure atroom temperature, will not result in actual boiling of thesample.3.2.1.1 DiscussionSampling and handling of dead crudeoils can usually be done without problems in normal, non-pressurized sample containers, such as cans and so fort

    11、h.3.2.2 live crude oila term usually employed for crude oilscontained in pressurized systems that, when brought to normalatmospheric pressure at room temperature, will result in actualboiling of the sample.3.2.2.1 DiscussionSampling and handling of samples oflive crude oils will necessitate the use

    12、of pressure cylinders andpreclude the use of normal sample containers, such as cans andso forth.3.2.3 Reid vapor pressure equivalent (RVPE)a value cal-culated by a defined correlation equation (see 14.3) fromVPCR4, that is expected to be comparable to the vapor pressurevalue obtained by Test Method

    13、D323.3.2.4 vapor pressure of crude oil (VPCRx), nthe pressureexerted in an evacuated chamber at a vapor-liquid ratio of X:1by conditioned or unconditioned crude oil, which may containgas, air or water, or a combination thereof, where X may varyfrom 4 to 0.02.1This test method is under the jurisdicti

    14、on of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.08 on Volatility.Current edition approved Oct. 1, 2010. Published November 2010. Originallyapproved in 1999. Last previous edition approved in 2008 as D637708. DOI:10.1520/D6377-10.2For r

    15、eferenced 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.1*A Summary of Changes section appears at the end of this standard.

    16、Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.3.3 Abbreviations:3.3.1 ARV, naccepted reference value3.3.2 RVPE, nReid vapor pressure equivalent3.3.3 V/L, nvapor liquid ratio3.3.4 VPCRx, nvapor pressure of crude oil at x vaporliquid

    17、ratio4. Summary of Test Method4.1 Employing a measuring chamber with a built-in piston,a sample of known volume is drawn from the sample containerinto the temperature controlled chamber at 20C or higher.After sealing the chamber, the volume is expanded by movingthe piston until the final volume prod

    18、uces the desired V/Lvalue. The temperature of the measuring chamber is thenregulated to the measuring temperature.4.2 After temperature and pressure equilibrium, the mea-sured pressure is recorded as the VPCRXof the sample. Thetest specimen shall be mixed during the measuring procedureby shaking the

    19、 measuring chamber to achieve pressure equi-librium in a reasonable time of 5 to 30 min.4.3 For results related to Test Method D323, the finalvolume of the measuring chamber shall be five times the testspecimen volume and the measuring temperature shall be37.8C.5. Significance and Use5.1 Vapor press

    20、ure of crude oil at various V/Ls is animportant physical property for shipping and storage.NOTE 2A vapor-liquid ratio of 0.02:1 (X = 0.02) mimics closely thesituation of an oil tanker.5.2 Vapor pressure of crude oil is important to crude oilproducers and refiners for general handling and initial ref

    21、inerytreatment.5.3 The vapor pressure determined by this test method at avapor-liquid ratio of 4:1 (VPCR4) of crude oil at 37.8C can berelated to the vapor pressure value determined on the samematerial when tested by Test Method D323 (seeAppendix X1).5.4 Chilling and air saturation of the sample pri

    22、or to thevapor pressure measurement is not required.5.5 This test method can be applied in online applications inwhich an air saturation procedure prior to the measurementcannot be performed.6. Apparatus6.1 The apparatus suitable for this test method employs asmall volume, cylindrically shaped measu

    23、ring chamber withassociated equipment to control the chamber temperaturewithin the range from 0 to 100C. The measuring chambershall contain a movable piston with a minimum dead volume ofless than 1 % of the total volume at the lowest position to allowsample introduction into the measuring chamber an

    24、d expansionto the desired V/L. A static pressure transducer shall beincorporated in the piston. The measuring chamber shallcontain an inlet/outlet valve combination for sample introduc-tion and expulsion. The piston and the valve combination shallbe at the same temperature as the measuring chamber t

    25、o avoidany condensation or excessive evaporation.6.1.1 The measuring chamber shall be designed to have atotal volume of 5 to 15 mL and shall be capable of maintaininga V/L of 4:1 to 0.02:1. The accuracy of the adjusted V/L shallbe within 0.01.NOTE 3The measuring chambers employed by the instruments

    26、usedin generating the precision and bias statements were constructed of nickelplated aluminium, stainless steel and brass with a total volume of 5 mL.Measuring chambers exceedinga5mLcapacity and different design canbe used, but the precision and bias statement (see Section 14) may not beapplicable.6

    27、.1.2 The pressure transducer shall have a minimum opera-tional range from 0 to 500 kPa with a minimum resolution of0.1 kPa and a minimum accuracy of 60.5 kPa. The pressuremeasurement system shall include associated electronics andreadout devices to display the resulting pressure reading.6.1.3 Electr

    28、onic temperature control shall be used to main-tain the measuring chamber at the prescribed temperaturewithin 60.1C for the duration of the test.6.1.4 A platinum resistance thermometer shall be used formeasuring the temperature of the measuring chamber. Theminimum temperature range of the measuring

    29、device shall befrom 0C to 100C with a resolution of 0.1C and an accuracyof 60.1C.6.1.5 The vapor pressure apparatus shall have provisions forrinsing the measuring chamber with the next sample to betested or with a solvent of low vapor pressure.6.1.6 The vapor pressure apparatus shall have provisions

    30、 forshaking the sample during the measuring procedure with aminimum frequency of 1.5 cycles per second.6.2 Vacuum Pump for Calibration, capable of reducing thepressure in the measuring chamber to less than 0.01 kPaabsolute.6.3 McLeod Vacuum Gage or Calibrated Electronic VacuumMeasuring Device for Ca

    31、libration, to cover at least the rangeof 0.01 to 0.67 kPa. The calibration of the electronic measuringdevice shall be regularly verified in accordance with Annex Aof Test Method D2892.6.4 Pressure Measuring Device for Calibration, capable ofmeasuring local station pressure with an accuracy and areso

    32、lution of 0.1 kPa or better, at the same elevation relative tosea level as the apparatus in the laboratory.NOTE 4This standard does not give full details of instruments suitableTABLE 1 Accepted Reference Value (ARV) and Acceptable Testing Range for Air Saturated Reference FluidsAReference FluidARV P

    33、tot 6 Uncertainty,(kPa)Recommended InstrumentManufacturer Tolerance,(kPa)Acceptable Testing Rangefor Reference Fuel Ptot,(kPa)Pentane 112.8 6 0.2 6 1.0 112.8 6 1.2 (111.6 to 114.0)2,2 Dimethylbutane 74.1 6 0.2 6 1.0 74.1 6 1.2 (72.9 to 75.3)2,3 Dimethylbutane 57.1 6 0.2 6 1.0 57.1 6 1.2 (55.9 to 58.

    34、3)ASupporting data have been filed at ASTM International Headquarters and may be obtained by requesting Research Report RR:D02-1619.D6377 102for carrying out this test. Details on the installation, operation andmaintenance of each instrument may be found in the manufacturersmanual.7. Reagents and Ma

    35、terials7.1 Purity of ReagentsUse chemicals of at least 99 %purity for verification of instrument performance (see Section11). Unless otherwise indicated, it is intended that all reagentsconform to the specifications of the Committee on AnalyticalReagents of the American Chemical Society where suchsp

    36、ecifications are available.3Other grades may be used, pro-vided it is first ascertained that the reagent is of sufficient purityto permit its use without lessening the accuracy of thedetermination.7.1.1 The chemicals in 7.2.1, 7.2.2, and 7.2.3 are suggestedfor verification of instrument performance

    37、(see Section 11),based on the air saturated reference fuels analyzed in the TestMethod D5191 2003 interlaboratory study (ILS)4(see Table 1).Ptotused in Test Method D5191 is equivalent to VPCR4used inthis test method). Such reference fuels are not to be used forinstrument calibration. Table 1 identif

    38、ies the accepted referencevalue (ARV) and uncertainty limits, as well as the acceptabletesting range for each of the reference fuels listed.7.1.2 The chemicals in 7.3.1 and 7.3.2 are suggested for useas rinsing solvents capable of cleaning the measuring chamber,the valves and the inlet and outlet tu

    39、bes.7.2 Verification Fluids:7.2.1 2,2-Dimethylbutane,(Warning2,2-dimethylbutaneis flammable and a health hazard.)7.2.2 2,3-Dimethylbutane,(Warning2,3-dimethylbutaneis flammable and a health hazard.)7.2.3 Pentane,(WarningPentane is flammable and ahealth hazard.)7.3 Solvents:7.3.1 Toluene,(WarningTolu

    40、ene is flammable and ahealth hazard.)7.3.2 Acetone,(WarningAcetone is flammable and ahealth hazard.)8. Sampling and Sample Introduction8.1 General Requirements:8.1.1 The extreme sensitivity of vapor pressure measure-ments to losses through evaporation and the resulting changesin composition requires

    41、 the utmost precaution and the mostmeticulous care in the drawing and handling of samples.Sampling of live crude oil shall be performed in accordancewith Practice D3700. Sampling in accordance with PracticeD4057 shall only be used for dead crude oil and if PracticeD3700 is impractical.NOTE 5Sampling

    42、 in accordance with Practice D4177 may also beused instead of Practice D4057.8.1.2 For sampling in accordance with Practice D3700,afloating piston cylinder with a minimum sample volume of 200mL shall be used if the overall volume of the test specimenrequired for the vapor pressure determination, inc

    43、luding therinsing procedure is not larger than 20 mL. Larger floatingpiston cylinders can be used. The minimum piston back-pressure shall be higher than the sample vapor pressure at theintroduction temperature of the measuring chamber plus 100kPa for the shifting of the piston. The maximum back-pres

    44、sureshall not exceed the maximum measurement pressure of theapparatus pressure transducer. Compressed air, or any other,non-flammable compressed gas, can be used as the back-pressuring agent. The floating piston cylinder shall haveprovisions for mechanical stirring of the sample and a secondvalve at

    45、 the inlet for rinsing.8.1.3 Do not unnecessarily expose the samples to tempera-tures exceeding 30C during sampling and storage. For pro-longed storage, store the samples in an appropriate room orrefrigerator.8.1.4 Perform the vapor pressure determination on the firsttest specimen withdrawn from the

    46、 cylinder after the rinsingstep in 9.3. Do not use the remaining sample in the floatingpiston cylinder for more than three repeat vapor pressuredeterminations.8.1.5 In the case of quality control checks with purecompounds (see 11.1), smaller sample containers withoutapplied pressure can be used.8.2

    47、Sampling Procedures:8.2.1 If the sample is contained in a pressurized source likea pipeline, use a floating piston cylinder and obtain the sampledirectly from the source under pressure. Rinse the cylinder byopening the rinsing valve until the crude oil emerges at thesecond inlet. Close the rinsing v

    48、alve and let the piston moveslowly until at least 200 mL of sample has entered the cylinder.Close the inlet valve and apply the back pressure immediately.Check the filling of the cylinder to be at least 200 mL.NOTE 6The current precision statements were derived from the 2005ILS using samples in 250

    49、mL floating piston cylinders (see 14.3).8.2.2 If the sample is taken from a non-pressurized sourcelike a storage tank, oil tanker, drum or other container, obtaina sample and test specimen in accordance with Practice D4057.Use either a 250-mL or 1-L sized container filled between 70and 80 % with sample. For best testing precision (reproduc-ibility), it is recommended that a 1-L sized container be used.NOTE 7The current precision statements were derived from the 2005ILS using samples in 1-L amber glass containers (see 14.3). However,samples i


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