ASTM D7110-2005a(2011) 1250 Standard Test Method for Determining the Viscosity-Temperature Relationship of Used and Soot-Containing Engine Oils at Low Temperatures《测定低温状态下已用的含煤烟发动机.pdf
《ASTM D7110-2005a(2011) 1250 Standard Test Method for Determining the Viscosity-Temperature Relationship of Used and Soot-Containing Engine Oils at Low Temperatures《测定低温状态下已用的含煤烟发动机.pdf》由会员分享,可在线阅读,更多相关《ASTM D7110-2005a(2011) 1250 Standard Test Method for Determining the Viscosity-Temperature Relationship of Used and Soot-Containing Engine Oils at Low Temperatures《测定低温状态下已用的含煤烟发动机.pdf(7页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: D7110 05a (Reapproved 2011)Standard Test Method forDetermining the Viscosity-Temperature Relationship of Usedand Soot-Containing Engine Oils at Low Temperatures1This standard is issued under the fixed designation D7110; the number immediately following the designation indicates the year
2、 oforiginal adoption or, in the case of revision, 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. Scope1.1 This test method covers how to measure the apparentvisco
3、sity of used and soot-containing engine oils at lowtemperatures.1.2 A shear rate of approximately 0.2 s-1is produced atshear stresses below 200 Pa. Apparent viscosity is measuredcontinuously as the sample is cooled at a rate of 3C per hourover the range of 5 to 40C.1.3 The measurements resulting fro
4、m this test method areviscosity, the maximum rate of viscosity increase (GelationIndex) and the temperature at which the Gelation Index occurs.1.4 Applicability to petroleum products other than engineoils has not been determined in preparing this test method.1.5 The values stated in SI units are to
5、be regarded asstandard. No other units of measurement are included in thisstandard.1.6 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
6、determine the applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D341 Practice for Viscosity-Temperature Charts for LiquidPetroleum ProductsD3829 Test Method for Predicting the Borderline PumpingTemperature of Engine OilD4684 Test Method for Determinatio
7、n of Yield Stress andApparent Viscosity of Engine Oils at Low TemperatureD4057 Practice for Manual Sampling of Petroleum andPetroleum Products3. Terminology3.1 Definitions:3.1.1 apparent viscosity, nthe viscosity obtained by use ofthis test method.3.1.1.1 DiscussionSee 3.1.6 for definition of viscos
8、ity andunits.3.1.2 Newtonian oil, nan oil that, at a given temperature,exhibits a constant viscosity at all shear rates or shear stresses.3.1.3 non-Newtonian oil, nan oil that, at a given tempera-ture, exhibits a viscosity that varies with shear stress or shearrate.3.1.4 shear rate, nvelocity gradie
9、nt perpendicular to thedirection of flow.3.1.4.1 DiscussionThe SI unit for shear rate is the recip-rocal second (1/s; also s-1).3.1.5 shear stress, nforce per unit area in the direction offlow.3.1.5.1 DiscussionThe SI unit for shear stress is thepascal (Pa).3.1.6 viscosity, nthat property of a fluid
10、 which resistsflow.3.1.6.1 DiscussionViscosity is defined as the ratio of theapplied shear stress (force causing flow) and the shear rate(resultant velocity of flow per unit distance from a stationarysurface wet by the fluid). Mathematically expressed:viscosity 5 shear stress/shear rate or, symbolic
11、ally, h5t/G (1)in which the symbols in the second portion of Eq 1 aredefined by 3.1.4 and 3.1.5. The SI unit for viscosity used hereinis millipascal seconds (mPas).3.2 Definitions of Terms Specific to This Standard:3.2.1 air-binding oils, nthose engine oils whose border-line pumping temperatures are
12、 determined by a combination ofgelation and viscous flow.3.2.2 borderline pumping temperature, nthat temperatureat which an engine oil may have such poor flow characteristicsthat the engine oil pump may not be capable of supplyingsufficient lubricant to the engine.1This test method is under the juri
13、sdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.07 on Flow Properties.Current edition approved Jan. 1, 2011. Published February 2011. Originallyapproved in 2005. Last previous edition approved in 2005 as D711005a. DOI:10.1520/D71
14、10-05AR11.2For 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.1Copyright ASTM International, 100 Barr Harbor Driv
15、e, PO Box C700, West Conshohocken, PA 19428-2959, United States.3.2.3 calibration oil, nNewtonian oils developed andused to calibrate the viscometer drive module over the viscos-ity range required for this test method.3.2.3.1 DiscussionThese calibration oils are speciallyblended to give sufficient s
16、ensitivity and range for the specialviscometer head used.3.2.4 computer-programmed automated analysis, nuse oftechniques for acquiring analog data, converting these todigital values and using this information to automaticallyrecord and analyze torque output from the viscometer drivemodule and to ren
17、der this information into tabular data andplotted relationships.3.2.4.1 analog-to-digital (A-D) converter, na device forconverting continuously produced electrical signals into dis-crete numerical values capable of being analyzed by computertechnology.3.2.5 critical pumpability temperature, nthe tem
18、peratureat which an oil reaches a viscosity believed to be critical tolimiting pumpability of the oil (see 3.2.6).3.2.6 critical pumpability viscosity, nthat apparent viscos-ity believed to cause pumpability problems in an engine.3.2.7 flow-limited oils, nthose oils whose borderlinepumping temperatu
19、res are determined by viscous flow.3.2.8 gelation, na rheological condition of an oil charac-terized by a marked increase in flow resistance over and abovethe normal exponential increase of viscosity with decreasingtemperature, particularly at lower shear stresses and tempera-tures.3.2.8.1 Discussio
20、nGelation has been attributed to a pro-cess of nucleation and crystallization of oil components and theconsequent formation of a gel-like mass.33.2.9 Gelation Index, nthe maximum value of the incre-mental ratio:log log h1!2log log h2!/log T12 log T2!# (2)in which h is dynamic viscosity and T is temp
21、erature inKelvin over the temperature range scanned when the incremen-tal decrease in temperature is 1K.3.2.9.1 DiscussionThe technique of deriving GelationIndex was first developed and practiced4by collecting infor-mation from a strip-chart recording and applying the empiricalMacCoull-Walther-Wrigh
22、t equation. For further information,see Appendix 1 of Viscosity-Temperature Charts D341.3.2.10 Gelation Index reference oils, nnon-Newtonianoils chosen to give certain levels of Gelation Index as a checkon instrument performance.3.2.11 Gelation Index Temperature, nthe temperature indegrees Celsius a
23、t which the Gelation Index occurs.3.2.12 pre-treatment sample heating bath, na water or airbath to heat the samples for 1.5 h at 90 6 2C before testing.3.2.13 programmable liquid cold bath, na liquid bathhaving a temperature controller capable of being programmedto run the calibration and the analys
24、is portions of the testmethod.3.2.14 temperature controller, na programmable devicewhich, when properly programmed, ramps the temperatureupward or downward at a chosen rate or series of steps whilesimultaneously controlling temperature excursions.3.2.14.1 calibration program, na program to run there
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