ASTM D6616-2007(2012) 1875 Standard Test Method for Measuring Viscosity at High Shear Rate by Tapered Bearing Simulator Viscometer at 100° C《在100摄氏度时用锥形轴承模拟器粘度计测量高剪切率时粘度的标准试验方法》.pdf
《ASTM D6616-2007(2012) 1875 Standard Test Method for Measuring Viscosity at High Shear Rate by Tapered Bearing Simulator Viscometer at 100° C《在100摄氏度时用锥形轴承模拟器粘度计测量高剪切率时粘度的标准试验方法》.pdf》由会员分享,可在线阅读,更多相关《ASTM D6616-2007(2012) 1875 Standard Test Method for Measuring Viscosity at High Shear Rate by Tapered Bearing Simulator Viscometer at 100° C《在100摄氏度时用锥形轴承模拟器粘度计测量高剪切率时粘度的标准试验方法》.pdf(13页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: D6616 07 (Reapproved 2012)Standard Test Method forMeasuring Viscosity at High Shear Rate by Tapered BearingSimulator Viscometer at 100C1This standard is issued under the fixed designation D6616; the number immediately following the designation indicates the year oforiginal adoption or,
2、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 the laboratory determination ofthe viscosity of engine oi
3、ls at 100C and 1106s1using theTapered Bearing Simulator (TBS) viscometer.2NOTE 1This test method is similar to Test Method D4683 which usesthe same TBS viscometer to measure high shear viscosity at 150C.1.2 The Newtonian calibration oils used to establish this testmethod range from approximately 5 t
4、o 12 mPas (cP) at 100Cand either the manual or automated protocol was used by eachparticipant in developing the precision statement. The viscosityrange of the test method at this temperature is from 1 mPas(cP) to above 25 mPas (cP), depending on the model of TBS.1.3 The non-Newtonian reference oil u
5、sed to establish theshear rate of 1106s1for this test method has a viscosity ofapproximately 10 mPas at 100C.1.4 Application to petroleum products other than engine oilhas not been determined in preparing the viscometric informa-tion for this test method.1.5 The values stated in SI units are to be r
6、egarded asstandard. No other units of measurement are included in thisstandard. This test method uses the milliPascal second (mPas)as the unit of viscosity. This unit is equivalent to the centiPoise(cP), which is shown in parentheses.1.6 This standard does not purport to address all of thesafety con
7、cerns, if any, associated with its use. It is theresponsibility of the user of this standard to establish appro-priate safety and health practices and to determine theapplicability of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:3D4683 Test Method for Measuring Visco
8、sity of New andUsed Engine Oils at High Shear Rate and High Tempera-ture by Tapered Bearing Simulator Viscometer at 150 CD4741 Test Method for Measuring Viscosity at High Tem-perature and High Shear Rate by Tapered-Plug Viscometer3. Terminology3.1 Definitions:3.1.1 density, nmass per unit volume. In
9、 the SI, the unit ofdensity is the kilogram per cubic metre. For practical use, thesubmultiple, gram per cubic centimetre, is more convenient.The density in gram per cubic centimetre is equal to 1/1000 thedensity in kg/m3.3.1.2 Newtonian oil or fluid, nan oil or fluid that at a giventemperature exhi
10、bits a constant viscosity at all shear rates orshear stresses.3.1.3 non-Newtonian oil or fluid, nan oil or fluid thatexhibits a viscosity that varies with changing shear stress orshear rate.3.1.4 shear rate, nthe velocity gradient in fluid flow. TheSI unit for shear rate is s1.3.1.5 shear stress, nt
11、he motivating force per unit area forfluid flow. The area is the area under shear. The SI unit forshear stress is the Pa.3.1.6 viscosity, nthe ratio between the applied shear stressand the rate of shear. It is sometimes called the coefficient ofdynamic viscosity. This coefficient is a measure of the
12、 resis-tance to flow of the liquid. In the SI, the unit of viscosity is thePascalsecond; often the milliPascalsecond or its equivalentthe centiPoise is found more convenient.3.1.6.1 apparent viscosity, nthe viscosity of a non-Newtonian fluid at a given shear rate or shear stress determinedby this te
13、st method.1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.07 on Flow Properties.Current edition approved Nov. 1, 2012. Published November 2012. Originallyapproved in 2001. Last previous edition
14、approved in 2007 as D661607. DOI:10.1520/D6616-07R12.2Available from Tannas Co., 4800 James Savage Rd., Midland, MI 48642. Thisviscometer and associated equipment as listed in the research report was used todevelop the precision statement. To date, no other equipment has demonstrated,throughASTM Int
15、ernational interlaboratory testing, the ability to meet the precisionof this test. This is not an endorsement or certification by ASTM International.3For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStanda
16、rds volume information, refer to the standards Document Summary page onthe ASTM website.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States13.2 Definitions of Terms Specific to This Standard:3.2.1 idling oil2, n an oxidatively stable Newt
17、onian oilinjected into the operating viscometer stator when the instru-ment is likely to be held for periods of time greater than 30 minand up to two weeks at 100C. Use of this oil prevents statordeposits from additives, which may decompose after longerexposure times in the operating viscometer and
18、permits con-tinuous operation of the viscometer without need to shut theinstrument off.3.2.2 Newtonian Reference Oil2, na specially blendedNewtonian oil that has the same viscosity at 100C as thenon-Newtonian reference oil of 3.2.3.3.2.3 non-Newtonian reference oil2, na specially formu-lated non-New
19、tonian oil, identified as NNR-10, having aselected apparent viscosity at 1106s1shear rate. The oil isused to establish an operating gap between the rotor and statorwhich will produce 1106s1shear rate when the rotor height isadjusted to give a torque output equivalent to that of the specialreference
20、oil described in 3.2.2.3.2.4 reciprocal torque intersection, 1/Ti,nthe rotorposition on the micrometer defined by the intersection of twostraight lines generated by the reciprocal torque method usingthe Newtonian reference oil of 3.2.2 and non-Newtonianreference oil of 3.2.3. Reciprocal torque versu
21、s rotor heightmeasurements on both oils gives straight lines whoseintersection, 1/Ti, establishes the desired rotor position foroperation at 1106s1shear rate.3.2.5 reference Newtonian calibration oils2, nspeciallychosen Newtonian oils used to determine the viscosity-torquerelationship of the TBS vis
22、cometer at 100C from which theviscosity of an unknown oil is calculated.3.2.6 rotor height (rotor position), n the vertical positionof the rotor relative to the stator and measured by the platformmicrometer.3.2.6.1 stored rotor height (rotor position), nthe rotorposition with the rotor 0.50 mm above
23、 the rubbing contactposition (see 3.2.7) when the instrument is shut down.3.2.7 rubbing contact position, nthe rotor height deter-mined when the tapered rotor is lightly brought into contactwith the similarly tapered stator.3.2.8 test oil, nany oil for which the apparent viscosity isto be determined
24、 by this test method.4. Summary of Test Method4.1 A motor drives a tapered rotor closely fitted inside amatched tapered stator. Appropriate technique establishes op-eration of the viscometer to yield 1106s1at a temperature of100C at which point test oils are introduced into the gapbetween the spinni
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