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本文(ASTM D341-2003 Standard Test Method for Viscosity-Temperature Charts for Liquid Petroleum Products《液体石油产品用粘温图的标准试验方法》.pdf)为本站会员(roleaisle130)主动上传,麦多课文库仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对上载内容本身不做任何修改或编辑。 若此文所含内容侵犯了您的版权或隐私,请立即通知麦多课文库(发送邮件至master@mydoc123.com或直接QQ联系客服),我们立即给予删除!

ASTM D341-2003 Standard Test Method for Viscosity-Temperature Charts for Liquid Petroleum Products《液体石油产品用粘温图的标准试验方法》.pdf

1、Designation: D 341 03An American National StandardStandard Test Method forViscosity-Temperature Charts for Liquid PetroleumProducts1This standard is issued under the fixed designation D 341; the number immediately following the designation indicates the year oforiginal adoption or, in the case of re

2、vision, 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.This standard has been approved for use by agencies of the Department of Defense.1. Scope1.1 The kinematic vi

3、scosity-temperature charts (see Figs. 1and 2) covered by this standard are a convenient means toascertain the kinematic viscosity of a petroleum oil or liquidhydrocarbon at any temperature within a limited range, pro-vided that the kinematic viscosities at two temperatures areknown.1.2 The charts ar

4、e designed to permit petroleum oil kine-matic viscosity-temperature data to plot as a straight line. Thecharts here presented provide a significant improvement inlinearity over the charts previously available under MethodD 341 43. This increases the reliability of extrapolation tohigher temperatures

5、.2. Referenced Documents2.1 ASTM Standards:2D 445 Test Method for Kinematic Viscosity of Transparentand Opaque Liquids (the Calculation of Dynamic Viscos-ity)2.2 ASTM Adjuncts:Adjunct D 341, Viscosity-Temperature Charts 1733. Technical Hazard3.1 CautionThe charts should be used only in that rangein

6、which the hydrocarbon or petroleum fluids are homogeneousliquids. The suggested range is thus between the cloud point atlow temperatures and the initial boiling point at higher tem-peratures. The charts provide improved linearity in both lowkinematic viscosity and at temperatures up to 340C (approxi

7、-mately 650F) or higher. Some high-boiling point materials canshow a small deviation from a straight line as low as 280C(approximately 550F), depending on the individual sample oraccuracy of the data. Reliable data can be usefully plotted inthe high temperature region even if it does exhibit somecur

8、vature. Extrapolations into such regions from lower tem-peratures will lack accuracy, however. Experimental data takenbelow the cloud point or temperature of crystal growth willgenerally not be of reliable repeatability for interpolation orextrapolation on the charts. It should also be emphasized th

9、atfluids other than hydrocarbons will usually not plot as a straightline on these charts.1These charts are under the jurisdiction ofASTM Committee D02 on PetroleumProducts and Lubricants and are the direct responsibility of Subcommittee D02.07on Flow Properties.Current edition approved Dec. 1, 2003.

10、 Published January 2004. Originallyapproved in 1932. Last previous edition approved in 1998 as D 34193 (1998).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 st

11、andards Document Summary page onthe ASTM website.3Available from ASTM International Headquarters. Order Adjunct No.ADJD0341CS.1Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.FIG. 1 Facsimile of Kinematic Viscosity-Temperature Chart I

12、 High Range (Temperature in degrees Celsius)FIG. 2 Facsimile of Kinematic Viscosity-Temperature Chart II Low Range (Temperature in degrees Celsius)D3410324. Description4.1 The charts are designed to permit kinematic viscosity-temperature data for a petroleum oil or fraction, and hydrocar-bons in gen

13、eral, to plot as a straight line over a wide range.Seven charts are available as follows:3Chart IKinematic Viscosity, High Range:Kinematic Viscosity: 0.3 to 20 000 000 cStTemperature: 70 to +370CSize: 680 by 820 mm (26.75 by 32.25 in.)Pad of 50ADJD034101Chart IIKinematic Viscosity, Low Range:Kinemat

14、ic Viscosity: 0.18 to 6.5 cStTemperature: 70 to +370CSize: 520 by 820 mm (20.5 by 32.25 in.)Pad of 50ADJD034102Chart IIIKinematic Viscosity, High Range:Kinematic Viscosity: 0.3 to 20 000 000 cStTemperature: 70 to +370CSize: 217 by 280 mm (8.5 by 11.0 in.)Pad of 50ADJD034103Chart IVKinematic Viscosit

15、y, Low Range:Kinematic Viscosity: 0.18 to 6.5 cStTemperature: 70 to +370CSize: 217 by 280 mm (8.5 to 11.0 in.)Pad of 50ADJD034104Chart VKinematic Viscosity, High Range:Kinematic Viscosity: 0.3 to 20 000 000 cStTemperature: 100 to +700FSize: 680 by 820 mm (26.75 by 32.25 in.)Pad of 50ADJD034105Chart

16、VIKinematic Viscosity, Low Range:Kinematic Viscosity: 0.18 to 3.0 cStTemperature: 100 to +700FSize: 520 by 820 mm (20.5 by 32.25 in.)Pad of 50ADJD034106Chart VIIKinematic Viscosity, Middle Range:Kinematic Viscosity: 3 to 200 000 cStTemperature: 40 to +150CSize: 217 by 280 mm (8.5 by 11.0 in.)Pad of

17、50ADJD0341074.2 Charts I, II, V, and VI are preferred when convenienceand accuracy of plotting are desired. Chart VII is the middlerange section of Chart I at somewhat reduced scale. It isprovided for convenience in connection with reports and dataevaluation. Charts III and IVare the same as Charts

18、I and II andare provided in greatly reduced scale for convenience inconnection with reports or quick evaluation of data. Theselatter charts are not recommended for use where the mostaccurate interpolations or extrapolations are desired.5. Procedure5.1 Plot two known kinematic viscosity-temperature p

19、ointson the chart. Draw a sharply defined straight line through them.A point on this line, within the range defined in Section 3,shows the kinematic viscosity at the corresponding desiredtemperature and vice versa.45.2 Alternatively, the interpolated and extrapolated kine-matic viscosities and tempe

20、ratures may be calculated asdescribed in Annex A1, within the range identified for thecharts in Section 3.6. Extrapolation6.1 Kinematic viscosity-temperature points on the extrapo-lated portion of the line, but still within the range defined inSection 3, are satisfactory provided the kinematic visco

21、sity-temperature line is located quite accurately. For purposes ofextrapolation, it is especially important that the two knownkinematic viscosity-temperature points be far apart. If thesetwo points are not sufficiently far apart, experimental errors inthe kinematic viscosity determinations and in dr

22、awing the linemay seriously affect the accuracy of extrapolated points,particularly if the difference between an extrapolated tempera-ture and the nearest temperature of determination is greaterthan the difference between the two temperatures of determi-nation. In extreme cases, an additional determ

23、ination at a thirdtemperature is advisable.7. Keywords7.1 charts; kinematic viscosity; MacCoull; viscosity;viscosity-temperature chartsANNEX(Mandatory Information)A1. MATHEMATICAL EQUATIONSA1.1 The complete design equation for the chart as given inAppendix X1.1 is not useful for inter-calculations o

24、f kinematicviscosity and temperature over the full chart kinematic viscos-ity range. More convenient equations5that agree closely withthe chart scale are given below. These are necessary whencalculations involve kinematic viscosities smaller than 2.0(mm2/s (cSt).log log Z 5 A 2 B log T (A1.1)Z 5n10.

25、7 1 exp 21.47 2 1.84n20.51n2! (A1.2)n5Z 2 0.7 2 exp 20.7487 2 3.295 Z 2 0.71 0.6119 Z 2 0.722 0.3193 Z 2 0.73! (A1.3)4If the kinematic viscosities are not known, they should be determined inaccordance with Test Method D 445.5Manning, R. E., “Computational Aids for Kinematic Viscosity Conversionsfrom

26、 100 and 210F to 40 and 100C,” Journal of Testing and Evaluation, JTEVA,Vol 2, No. 6, 1974 pp. 5228.D341033where:log = logarithm to base 10,n = kinematic viscosity, mm2/s (or cSt),T = temperature, K (or t + 273.15, where t is C),andA and B = constants.A1.2 Inserting EqA1.2 into EqA1.1 will permit so

27、lving forthe constants A and B for a fluid in which some of theexperimental kinematic viscosity data fall below 2.0 mm2/s(cSt). This form can also be used to calculate the temperatureassociated with a desired kinematic viscosity.A1.3 Conversely, the kinematic viscosity associated with astated temper

28、ature can be found from the equation determinedas inA1.2 by solving for Z in the substituted EqA1.1, and thensubsequently deriving the kinematic viscosity from the value ofZ by the use of Eq A1.3.APPENDIX(Nonmandatory Information)X1. HISTORY OF THE ASTM VISCOSITY-TEMPERATURE CHARTSX1.1 The forerunne

29、r of these charts was published by NeilMacCoull.6His continuation of the study of these chartsresulted in publication in 19277of the chart based onlog log cSt 1 0.7! 5 A 2 B log T (X1.1)An ASTM committee undertook study of this chart at thattime, resulting in the first ASTM chart publication in 1932

30、using a constant of 0.8 in the equation. The constant wasallowed to vary in charts published after 1937.X1.2 In 1928, Walther8published the log-log Eq X1.1without the constant, and in 1931, the log-log equation with aconstant of 0.8.X1.3 The present MacCoull-Wright charts are based largelyon the wor

31、k of MacCoull, Wright, and ASTM SubcommitteeD02.07.X1.4 The current charts were derived9with computerassistance to provide linearity over a greater range on the basisof the most reliable of modern data. The general relationship is:log log Z 5 A 2 B log T (X1.2)where:Z =(v + 0.7 + C D + E F + G H),lo

32、g = logarithm to base 10,v = kinematic viscosity, mm2/s (or cSt),T = temperature, K (or t + 273.15, where t is C),A and B = constants,C = exp (1.14883 2.65868v),D = exp (0.0038138 12.5645v),E = exp (5.46491 37.6289v),F = exp (13.0458 74.6851v),G = exp (37.4619 192.643v), andH = exp (80.4945 400.468v

33、).X1.4.1 Terms C through H are exponentials on the naturalbase e since this simplifies computer programming. Eq X1.1uses logarithms to the base 10 for general convenience whenused in short form.X1.4.2 The limits of applicability are listed below:Z =(v + 0.7) 2 3 107to 2.00 cStZ =(v + 0.7 + C)23 107t

34、o 1.65 cStZ =(v + 0.7 + C D 3 107to 0.90 cStZ =(v + 0.7 + C D + E) 2 3 107to 0.30 cStZ =(v + 0.7 + C D + E F + G)23 107to 0.24 cStZ =(v + 0.7 + C D + E F + G H)23 107to 0.21 cStX1.5 It is obvious that Eq X1.1 in the simplified form: loglog (v + 0.7) = AB log T will permit kinematic viscositycalculat

35、ions for a given fluid in the majority of instancesrequired. The constants A and B can be evaluated for a fluidfrom two data points. Kinematic viscosities or temperatures forother points can then be readily calculated.X1.6 Older literature refers to a value called the ASTMSlope. It should be noted t

36、hat this value is not the value of Bgiven in Eq X1.2. TheASTM Slope was originally obtained byphysically measuring the slope of the kinematic viscosity-temperature data plotted on the older charts given in TestMethod D 341 43. The kinematic viscosity and temperaturescales were not made to the same r

37、atios in Test MethodD 341 43. The improved charts given here utilize evendifferent scale ratios for dimensional convenience and a differ-ent constant (0.7) from the older charts; consequently, theoriginal ASTM Slope is not numerically equivalent to B in EqX1.1 from any of the new charts, nor directl

38、y convertible fromEq X1.1.6MacCoull, N., Lubrication, The Texas Company, New York, June 1921, p. 65.71927 International Critical Tables, p. 147.8Walther, C., “The Variation of Viscosity with TemperatureI, II, III,” Erdol undTeer, Vol 5, 1928, p. 510, 526, 614.9Wright, W.A., “An Improved Viscosity-Te

39、mperature Chart for Hydrocarbons,”Journal of Materials, Vol 4, No. 1, 1969, pp. 1927.D341034ASTM International takes no position respecting the validity of any patent rights asserted in connection with any item mentionedin this standard. Users of this standard are expressly advised that determinatio

40、n of the validity of any such patent rights, and the riskof infringement of such rights, are entirely their own responsibility.This standard is subject to revision at any time by the responsible technical committee and must be reviewed every five years andif not revised, either reapproved or withdra

41、wn. Your comments are invited either for revision of this standard or for additional standardsand should be addressed to ASTM International Headquarters. Your comments will receive careful consideration at a meeting of theresponsible technical committee, which you may attend. If you feel that your c

42、omments have not received a fair hearing you shouldmake your views known to the ASTM Committee on Standards, at the address shown below.This standard is copyrighted by ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959,United States. Individual reprints (single or multiple copies) of this standard may be obtained by contacting ASTM at the aboveaddress or at 610-832-9585 (phone), 610-832-9555 (fax), or serviceastm.org (e-mail); or through the ASTM website(www.astm.org).D341035

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