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本文(ASTM D1555M-2008e1 Standard Test Method for Calculation of Volume and Weight of Industrial Aromatic Hydrocarbons and Cyclohexane [Metric]《工业香烃类计量的体积和重量计算的标准试验方法》.pdf)为本站会员(boatfragile160)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 D1555M-2008e1 Standard Test Method for Calculation of Volume and Weight of Industrial Aromatic Hydrocarbons and Cyclohexane [Metric]《工业香烃类计量的体积和重量计算的标准试验方法》.pdf

1、Designation: D 1555M 081Standard Test Method forCalculation of Volume and Weight of Industrial AromaticHydrocarbons and Cyclohexane Metric1This standard is issued under the fixed designation D 1555M; the number immediately following the designation indicates the year oforiginal adoption or, in the c

2、ase 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.1NOTEThe units statements in 1.3 and 1.3.1 were corrected editorially in May 2009.1. Scope*1.1 This s

3、tandard is for use in calculating the weight andvolume of benzene, toluene, mixed xylenes, styrene, ortho-xylene, meta-xylene, para-xylene, cumene, ethylbenzene,148.9 to 176.7C and 176.7 to 204.4C aromatic hydrocarbons,and cyclohexane. A method is given for calculating the volumeat 15C and 20C from

4、an observed volume at tC. Table 1 liststhe density in grams per cubic centimetre at 15C and 20C forhigh purity chemicals.1.2 Calculated results shall be rounded off in accordancewith the rounding-off method of Practice E29.1.3 The values stated in SI units are to be regarded asstandard. No other uni

5、ts of measurement are included in thisstandard.1.3.1 A complete inch-pound unit companion standard hasbeen developed in Test Method D 1555.1.4 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

6、 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 1217 Test Method for Density and Relative Density(Specific Gravity) of Liquids by Bingham PycnometerD 1555 Test Method for Calculat

7、ion of Volume and Weightof Industrial Aromatic Hydrocarbons and CyclohexaneD 3505 Test Method for Density or Relative Density ofPure Liquid ChemicalsD 4052 Test Method for Density and Relative Density ofLiquids by Digital Density MeterE29 Practice for Using Significant Digits in Test Data toDetermin

8、e Conformance with Specifications2.2 Other Documents:Patterson, J. B., and Morris, E. C., Metrologia, 31, 1994,pp. 277-288TRC Thermodynamic TablesHydrocarbons, NSRDS-NIST 75-121, Supplement No. 121, April 30, 20013. Significance and Use3.1 This test method is suitable for use in calculatingweights a

9、nd volumes of the products outlined in Section 1. Theinformation presented can be used for determining quantities ofthe above-stated aromatic hydrocarbons in tanks, shippingcontainers, etc.4. Basic Data4.1 Densities of pure materials at 15C and 20C are derivedfrom densities furnished by NSRDS-NIST 7

10、5-121 (NationalStandard Reference Data SeriesNational Institute of Stan-dards and Technology). Densities of impure materials shouldbe determined by actual measurement (see Section 7).4.2 The VCF (Volume Correction Factor) equations pro-vided below are derived from the Volume Correction imple-mentati

11、on procedures presented in Method D 1555 - 04a.4.3 The former VCF tables were based on data for com-pounds of the highest purity, but were reported to be usable formaterials in the ranges indicated in Table 2. The data support-ing this conclusion appears to be unavailable at the presenttime; however

12、 there is no reason to change this recommenda-tion. If, depending on the composition of the impurities, thereis reason to suspect that the VCF implementation procedurespresented below do not apply to a particular impure product, aseparate implementation procedure should be independentlydetermined. T

13、his may be done by measuring the density of arepresentative sample at different temperatures throughout theexpected working temperature range, regressing the data toobtain a temperature/density equation that best reproduces theobserved data, and then dividing the constants of thetemperature/density

14、equation by the calculated density at 15Cand 20C. Alternatively, if the composition has been quantified1This test method is under the jurisdiction of ASTM Committee D16 onAromatic Hydrocarbons and Related Chemicals and is the direct responsibility ofSubcommittee D16.01 on Benzene, Toluene, Xylenes,

15、Cyclohexane and TheirDerivatives.Current edition approved Feb. 1, 2008. Published March 2008. Originallyapproved in 1993. Last previous edition approved in 2004 as D 1555M 04a.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. Fo

16、r 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.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.one

17、can use the VCFs of each component (if available) tocalculate a weighted average density at different temperaturesand then process the data as mentioned above.5. Volume Correction Factor Implementation Procedure5.1 The following general equation is used to generate theVolume Correction Factors:VCF 5

18、a 1 b 1.8t132! 1 c 1.8t132!21 d 1.8t132!31e 1.8t132!4!/VCFXX(1)where:t = temperature in C,VCFXX5 VCF59For VCF68F, andconstants a through e and VCFXXare specific to eachcompound (obtained from Method D 1555 04a and presentedin Table 3).5.2 Temperature may be entered in tenths of a degreeCentigrade.5.

19、3 The final result is rounded to 5 places past the decimal.No intermediate rounding or truncation should be done.5.4 The equations are valid for liquid product up to 60C(65.5C for p-xylene).5.5 This implementation procedure replaces the printedtables of previous editions of this Method for determini

20、ngVCFs. The implementation procedure is the Standard, notthe printed tables. However, a printout from the implemen-tation procedure is provided in 0.5C increments for the usersconvenience (Tables 4 and 5).6. Use of the Implementation Procedure6.1 Volume Reduction to 15CEnter the appropriate equa-tio

21、n with the temperature to the nearest 0.1 degree CentigradeTABLE 1 Physical PropertiesProductFreezingPointCBoilingPointCDensity in Vacuoat 15Cg/ccA,B,CDensity in Airat 15Cg/ccDDensity in Vacuoat 20Cg/ccC,E,FDensity in Airat 20Cg/ccDBenzene 5.6 80.1 0.88431 0.88324 0.87908 0.87801Cumene -96.1 152.4 0

22、.86586 0.86479 0.86160 0.86053Cyclohexane 6.6 80.7 0.78317 0.78209 0.77849 0.77741Ethylbenzene -95.0 136.2 0.87126 0.87019 0.86685 0.86578Styrene -30.6 145.2 0.91028 0.90922 0.90586 0.90480Toluene -95.0 110.6 0.87147 0.87040 0.86686 0.86579m-Xylene -47.9 139.1 0.86831 0.86724 0.86408 0.86301o-Xylene

23、 -25.2 144.4 0.88387 0.88280 0.87968 0.87861p-Xylene 13.3 138.3 0.86503 0.86396 0.86076 0.85969AObtained from Method D 1555 04a by multiplying the chemicals 60F density by the volume correction factor for 59F.BSpecific Gravity at 15C is not presented in this table as it is unnecessary to this standa

24、rd. If needed, divide 15C density in g/cc by 0.999102 g/cc. See AppendixX1.Cg/cc can be converted to kg/1000L or kg/m3by multiplying by 1000.DProduced using g/cc = (Density 1.00014992597 0.00119940779543) and rounding to 5 decimal places. See Appendix X2.EObtained from Method D 1555 - 04a by multipl

25、ying the chemicals 60F density by the volume correction factor for 68F.FSpecific Gravity at 20C is not presented in this table as it is unnecessary to this standard. If needed, divide 20C density in g/cc by 0.998206 g/cc. See Appendix X1.NOTE 1Densities (or weights) “in vacuo” represent the true den

26、sity (or weight) if measured in a vacuum without the buoyancy effect of air actingon the liquid. It is representative of the actual amount of product present. Densities (or weights) “in air” represent what would actually be measured ona scale. The difference is on the order of 0.13 %. Modern densito

27、meters measure density in vacuo and the ASTM and API recommend the use of in vacuodensities (or weights); however, the purchaser and seller should agree on which to use in their transactions.TABLE 2 Application Range of Implementation ProcedureImpure Products RangeBenzene 95 to 100%Cumene 95 to 100%

28、Cyclohexane 90 to 100%Ethylbenzene 95 to 100%Styrene 95 to 100%Toluene 95 to 100%Mixed Xylenes All proportionsm-Xylene 95 to 100%o-Xylene 95 to 100%p-Xylene 94 to 100%148.9-176.7C Aromatic Hydrocarbons All proportions176.7-204.4C Aromatic Hydrocarbons All proportionsTABLE 3 VCF ConstantsProduct a b

29、c d e VCF59FVCF68FBenzene 1.038382492 -6.2307 3 10-4-2.8505 3 10-71.2692 3 10-100 1.00066 0.99474Cumene 1.032401114 -5.3445 3 10-4-9.5067 3 10-83.6272 3 10-110 1.00055 0.99563Cyclohexane 1.039337296 -6.4728 3 10-4-1.4582 3 10-71.03538 3 10-100 1.00066 0.99468Ethylbenzene 1.033346632 -5.5243 3 10-48.

30、37035 3 10-10-1.2692 3 10-95.55061 3 10-121.00056 0.99550Styrene 1.032227515 -5.3444 3 10-4-4.4323 3 10-80 0 1.00054 0.99568Toluene 1.035323647 -5.8887 3 10-42.46508 3 10-9-7.2802 3 10-120 1.00059 0.99529m-XyleneA1.031887514 -5.2326 3 10-4-1.3253 3 10-7-7.35960 3 10-110 1.00054 0.99567o-Xylene 1.031

31、436449 -5.2302 3 10-4-2.5217 3 10-9-2.13840 3 10-100 1.00053 0.99579p-Xylene 1.032307000 -5.2815 3 10-4-1.8416 3 10-71.89256 3 10-100 1.00054 0.99560148.9-176.7C 1.031118000 -5.1827 3 10-4-3.5109 3 10-9-1.98360 3 10-110 1.00052 0.99585176.7-204.4C 1.029099000 -4.8287 3 10-4-3.7692 3 10-83.78575 3 10

32、-110 1.00049 0.99610Aand Mixed Xylenes.D 1555M 0812TABLE 4 Volume Correction FactorsVolume Correction to 15CTemperatureCBenzene Cumene CyclohexaneEthylBenzeneStyrene Toluenem-XyleneandMixedXyleneso-Xylene p-Xylene148.9 to176.7CAromaticHydrocarbons176.7 to204.4CAromaticHydrocarbons-20.5 . . . . . . .

33、 . . . .-20.0 . . . . . 1.03707 . . . . .-19.5 . . . . . 1.03654 . . . . .-19.0 . . . . . 1.03601 . . . . .-18.5 . . . . . 1.03548 . . . . .-18.0 . . . . . 1.03495 . . . . .-17.5 . . . . . 1.03442 . . . . .-17.0 . . . . . 1.03389 . . . . .-16.5 . . . . . 1.03336 . . . . .-16.0 . . . . . 1.03283 . .

34、. . .-15.5 . . . . . 1.03230 . . . . .-15.0 . 1.02916 . 1.03001 . 1.03177 1.02871 1.02828 . 1.02799 1.02618-14.5 . 1.02868 . 1.02951 . 1.03124 1.02824 1.02781 . 1.02753 1.02575-14.0 . 1.02820 . 1.02901 . 1.03071 1.02777 1.02734 . 1.02706 1.02531-13.5 . 1.02771 . 1.02852 . 1.03018 1.02730 1.02686 . 1

35、.02659 1.02488-13.0 . 1.02723 . 1.02802 . 1.02965 1.02682 1.02639 . 1.02613 1.02444-12.5 . 1.02675 . 1.02752 . 1.02912 1.02635 1.02592 . 1.02566 1.02401-12.0 . 1.02627 . 1.02702 . 1.02859 1.02588 1.02545 . 1.02519 1.02357-11.5 . 1.02579 . 1.02653 . 1.02806 1.02540 1.02498 . 1.02473 1.02314-11.0 . 1.

36、02530 . 1.02603 . 1.02753 1.02493 1.02451 . 1.02426 1.02270-10.5 . 1.02482 . 1.02553 . 1.02700 1.02446 1.02404 . 1.02380 1.02227-10.0 . 1.02434 . 1.02504 . 1.02647 1.02398 1.02357 . 1.02333 1.02183-9.5 . 1.02385 . 1.02454 . 1.02594 1.02351 1.02310 . 1.02286 1.02140-9.0 . 1.02337 . 1.02404 1.02322 1.

37、02542 1.02303 1.02263 . 1.02240 1.02096-8.5 . 1.02289 . 1.02354 1.02274 1.02489 1.02256 1.02216 . 1.02193 1.02052-8.0 . 1.02240 . 1.02304 1.02226 1.02436 1.02208 1.02169 . 1.02146 1.02009-7.5 . 1.02192 . 1.02255 1.02177 1.02383 1.02161 1.02122 . 1.02100 1.01965-7.0 . 1.02144 . 1.02205 1.02129 1.0233

38、0 1.02113 1.02075 . 1.02053 1.01922-6.5 . 1.02095 . 1.02155 1.02081 1.02277 1.02066 1.02028 . 1.02007 1.01878-6.0 . 1.02047 . 1.02105 1.02033 1.02224 1.02018 1.01980 . 1.01960 1.01835-5.5 . 1.01998 . 1.02055 1.01984 1.02171 1.01971 1.01933 . 1.01913 1.01791-5.0 . 1.01950 . 1.02006 1.01936 1.02118 1.

39、01923 1.01886 . 1.01867 1.01747-4.5 . 1.01901 . 1.01956 1.01888 1.02065 1.01875 1.01839 . 1.01820 1.01704-4.0 . 1.01853 . 1.01906 1.01840 1.02012 1.01828 1.01792 . 1.01773 1.01660-3.5 . 1.01804 . 1.01856 1.01791 1.01959 1.01780 1.01745 . 1.01727 1.01617-3.0 . 1.01756 . 1.01806 1.01743 1.01906 1.0173

40、2 1.01698 . 1.01680 1.01573-2.5 . 1.01707 . 1.01756 1.01695 1.01853 1.01685 1.01651 . 1.01633 1.01529-2.0 . 1.01659 . 1.01706 1.01646 1.01800 1.01637 1.01604 . 1.01587 1.01486-1.5 . 1.01610 . 1.01656 1.01598 1.01747 1.01589 1.01557 . 1.01540 1.01442-1.0 . 1.01562 . 1.01606 1.01550 1.01694 1.01541 1.

41、01510 . 1.01493 1.01399-0.5 . 1.01513 . 1.01557 1.01502 1.01641 1.01494 1.01462 . 1.01447 1.013550.0 . 1.01464 . 1.01507 1.01453 1.01588 1.01446 1.01415 . 1.01400 1.013110.5 . 1.01416 . 1.01457 1.01405 1.01535 1.01398 1.01368 . 1.01354 1.012681.0 . 1.01367 . 1.01407 1.01357 1.01482 1.01350 1.01321 .

42、 1.01307 1.012241.5 . 1.01319 . 1.01357 1.01308 1.01429 1.01302 1.01274 . 1.01260 1.011802.0 . 1.01270 . 1.01307 1.01260 1.01376 1.01254 1.01227 . 1.01214 1.011372.5 . 1.01221 . 1.01257 1.01211 1.01324 1.01206 1.01180 . 1.01167 1.010933.0 . 1.01173 . 1.01206 1.01163 1.01271 1.01158 1.01132 . 1.01120

43、 1.010493.5 . 1.01124 . 1.01156 1.01115 1.01218 1.01110 1.01085 . 1.01074 1.010064.0 . 1.01075 . 1.01106 1.01066 1.01165 1.01062 1.01038 . 1.01027 1.009624.5 . 1.01026 . 1.01056 1.01018 1.01112 1.01014 1.00991 . 1.00980 1.009185.0 . 1.00978 . 1.01006 1.00970 1.01059 1.00966 1.00944 . 1.00934 1.00875

44、5.5 . 1.00929 . 1.00956 1.00921 1.01006 1.00918 1.00897 . 1.00887 1.008316.0 1.01054 1.00880 . 1.00906 1.00873 1.00953 1.00870 1.00850 . 1.00840 1.007876.5 1.00995 1.00831 . 1.00856 1.00824 1.00900 1.00822 1.00802 . 1.00794 1.007447.0 1.00937 1.00782 1.00952 1.00805 1.00776 1.00847 1.00774 1.00755 .

45、 1.00747 1.007007.5 1.00879 1.00734 1.00893 1.00755 1.00727 1.00794 1.00725 1.00708 . 1.00700 1.006568.0 1.00821 1.00685 1.00833 1.00705 1.00679 1.00741 1.00677 1.00661 . 1.00654 1.006128.5 1.00762 1.00636 1.00774 1.00655 1.00631 1.00688 1.00629 1.00614 . 1.00607 1.005699.0 1.00704 1.00587 1.00715 1

46、.00605 1.00582 1.00635 1.00581 1.00566 . 1.00560 1.005259.5 1.00645 1.00538 1.00655 1.00554 1.00534 1.00582 1.00532 1.00519 . 1.00514 1.0048110.0 1.00587 1.00489 1.00596 1.00504 1.00485 1.00529 1.00484 1.00472 . 1.00467 1.0043710.5 1.00528 1.00440 1.00536 1.00454 1.00437 1.00476 1.00436 1.00425 . 1.

47、00420 1.0039411.0 1.00470 1.00391 1.00477 1.00403 1.00388 1.00423 1.00387 1.00378 . 1.00374 1.0035011.5 1.00411 1.00342 1.00417 1.00353 1.00340 1.00370 1.00339 1.00330 . 1.00327 1.0030612.0 1.00352 1.00294 1.00358 1.00303 1.00291 1.00317 1.00291 1.00283 . 1.00280 1.0026212.5 1.00294 1.00245 1.00298

48、1.00252 1.00243 1.00264 1.00242 1.00236 . 1.00234 1.0021913.0 1.00235 1.00196 1.00239 1.00202 1.00194 1.00212 1.00194 1.00189 . 1.00187 1.0017513.5 1.00176 1.00147 1.00179 1.00152 1.00146 1.00159 1.00145 1.00141 1.00148 1.00140 1.00131D 1555M 0813TABLE 4 ContinuedVolume Correction to 15CTemperatureC

49、Benzene Cumene CyclohexaneEthylBenzeneStyrene Toluenem-XyleneandMixedXyleneso-Xylene p-Xylene148.9 to176.7CAromaticHydrocarbons176.7 to204.4CAromaticHydrocarbons14.0 1.00117 1.00098 1.00119 1.00101 1.00097 1.00106 1.00097 1.00094 1.00099 1.00094 1.0008714.5 1.00058 1.00049 1.00060 1.00051 1.00049 1.00053 1.00048 1.00047 1.00050 1.00047 1.0004315.0 1.00000 1.00000 1.00000 1.00000 1.00000 1.00000 1.00000 1.00000 1.00000 1.00000 1.0000015.5 0.99941 0.99950 0.99940 0.99950 0.99952 0.99947 0.99951 0.99952 0.99951 0.99

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