ASTM D6426-2007 Standard Test Method for Determining Filterability of Middle Distillate Fuel Oils《中间馏出燃料油可过滤性测定的标准试验方法》.pdf
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1、Designation: D 6426 07An American National StandardStandard Test Method forDetermining Filterability of Middle Distillate Fuel Oils1This standard is issued under the fixed designation D 6426; the number immediately following the designation indicates the year oforiginal adoption or, in the case of r
2、evision, 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 determining thefilterability of distillate fuel oils wi
3、thin the viscosity range from1.70 to 6.20 mm2/s (cSt) at 40C.NOTE 1ASTM specification fuels falling within the scope of this testmethod are Specification D 396 Grade Nos. 1 and 2, Specification D 975Grades 1-D, low sulfur 1-D, 2-D, and low sulfur 2-D, and SpecificationD 2880 Grade Nos. 1-GT and 2-GT
4、.1.2 This test method is not applicable to fuels that containundissolved water.1.3 The values stated in SI units are to be regarded as thestandard. The values given in parentheses are for informationonly.1.4 This standard does not purport to address all of thesafety concerns, if any, associated with
5、 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 regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D 396 Specification for Fuel OilsD 975 Specification for Diesel Fuel
6、 OilsD 2880 Specification for Gas Turbine Fuel OilsD 4057 Practice for Manual Sampling of Petroleum andPetroleum ProductsD 4176 Test Method for Free Water and Particulate Con-tamination in Distillate Fuels (Visual Inspection Proce-dures)D 4177 Practice for Automatic Sampling of Petroleum andPetroleu
7、m ProductsD 4860 Test Method for Free Water and Particulate Con-tamination in Mid-Distillate Fuels (Clear and Bright Nu-merical Rating)E1 Specification for ASTM Liquid-in-Glass Thermometers2.2 ASTM Adjuncts:ADJ6300 D2PP, Version 4.43, Determination of Precisionand Bias Data for Use in Test Methods f
8、or PetroleumProducts33. Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 For this test method, filterability is a measure of therapidity with which a standard filter medium is plugged byinsoluble matter in fuel and can be described in either of thefollowing two ways:3.1.1.1 filter
9、ability (by pressure)the pressure drop acrossa filter medium when 300 mL of fuel is passed at a rate of 20mL/min.3.1.1.2 filterability (by volume)the volume of fuel passedwhen 104 kPa (15 psi) is reached. This method of report is usedwhen less than 300 mL passes at that pressure.3.1.1.3 filterabilit
10、y quality factor (F-QF)a value that de-fines the filter plugging tendency of a fuel caused by particu-late. The value is calculated using the volume and pressureattained at the end of the test cycle. Depending on the outcomeof the test, two different equations are applied.3.1.1.4 DiscussionEq 1 is a
11、pplied if the total sample wasdischarged prior to reaching the maximum pressure or Eq 2 ifthe maximum pressure was reached prior to discharging theentire sample. The equations proportion the results so that acontinuous range of 0 100 is attained. Eq 1 yields valuesfrom 50 to 100, whereas Eq 2 yields
12、 values from 0 to 50.Higher values signify less particulate that can plug a filter of agiven pore size and porosity.(1) If the total sample (300 mL) is discharged prior to reaching themaximum pressure (104 kPa or 15 psi), the F-QF is calculated by thefollowing equation:F2QF300 mL at P F!5 15 psi 2 P
13、F! /15psi!50! 1 50! (1)where:P(F)= final pressure when the total sample (300 mL) wasdischarged.(2) If the total sample is not discharged prior to reaching themaximum pressure (104 kPa or 15 psi), the F-QF is calculated by thefollowing equation:1This test method is under the jurisdiction of ASTM Comm
14、ittee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.14 on Stability and Cleanliness of Liquid Fuels.Current edition approved July 1, 2007. Published August 2007. Originallyapproved in 1999. Last previous edition approved in 2004 as D 642604.2For referenc
15、ed 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.3Available from ASTM International Headquarters. Order Adjunct No.ADJD6300
16、.1*A Summary of Changes 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.F2QFV F! at 15 psi!5 VF!/ 6 (2)where:V(F)= final volume when the maximum pressure wasreached.3.1.1.5 DiscussionThe fin
17、al volume (V(F) is divided bysix, since the maximum possible volume is 300 mL. Bydividing by six, the values for that test result are proportionedto fit the range from 0 to 50.4. Summary of Test Method4.1 A sample is passed at a constant rate (20 mL/min)through a standard porosity filter medium. The
18、 pressure dropacross the filter and the volume of filtrate are monitored. Thetest is concluded either when the pressure drop across the filterexceeds 104 kPa (15 psi) or when 300 mL have passed throughthe filter.4.2 Results are reported as either the volume that has passedthrough the filter when a p
19、ressure of 104 kPa (15 psi) has beenreached or the pressure drop when 300 mL have passedthrough the filter.4.3 Verification of the apparatus is required when there is adoubt of a test result, or when the apparatus has not been usedfor three months or more. It is not necessary to verify apparatusperf
20、ormance prior to each test.5. Significance and Use5.1 This test method is intended for use in the laboratory orfield in evaluating distillate fuel cleanliness.5.2 A change in filtration performance after storage, pre-treatment, or commingling can be indicative of changes in fuelcondition.5.3 Relativ
21、e filterability of fuels may vary depending onfilter porosity and structure and may not always correlate withresults from this test method.5.4 Causes of poor filterability in industrial/refinery filtersinclude fuel degradation products, contaminants picked upduring storage or transfer, incompatibili
22、ty of commingledfuels, or interaction of the fuel with the filter media. Any ofthese could correlate with orifice or filter system plugging, orboth.6. Apparatus6.1 Micro-Filter Analyzer:4NOTE 2The Micro-Filter can display the pressure in either kPa or psiunits by changing an internal jumper wire.6.1
23、.1 The apparatus is shown diagrammatically in Fig. 1 andphotographically in Fig. 2. It is capable of measuring pressureupstream of the filtering element and the volume of samplepassed through the filter at a preset pressure level. Theapparatus is comprised of the following parts:6.1.1.1 Peristaltic
24、Pump, variable speed/flow rate, withfeedback speed control, adjusted to provide fuel delivery at aconstant rate of 20 6 1 mL/min, and incorporating a pulsedampening mechanism to produce a smooth flow.6.1.1.2 Pressure TransducerPressure transducer capableof measuring gage pressure in the range from 0
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