ASTM E2071-2000(2015) Standard Practice for Calculating Heat of Vaporization or Sublimation from Vapor Pressure Data《采用蒸气压力数据计算汽化热或蒸馏热的标准实践规程》.pdf

《ASTM E2071-2000(2015) Standard Practice for Calculating Heat of Vaporization or Sublimation from Vapor Pressure Data《采用蒸气压力数据计算汽化热或蒸馏热的标准实践规程》.pdf》由会员分享，可在线阅读，更多相关《ASTM E2071-2000(2015) Standard Practice for Calculating Heat of Vaporization or Sublimation from Vapor Pressure Data《采用蒸气压力数据计算汽化热或蒸馏热的标准实践规程》.pdf（4页珍藏版）》请在麦多课文档分享上搜索。

1、Designation: E2071 00 (Reapproved 2015)Standard Practice forCalculating Heat of Vaporization or Sublimation from VaporPressure Data1This standard is issued under the fixed designation E2071; 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 () indicates an editorial change since the last revision or reapproval.1. Scope1.1 This practice describes the calculation of the heat ofvaporization of a liquid or the heat of subl

3、imation of a solidfrom measured vapor pressure data. It is applicable to pureliquids, azeotropes, pure solids, and homogenous solid solu-tions over the temperature range for which the vapor pressureequation fitted to the measured data is applicable.NOTE 1This practice is generally not applicable to

4、liquid mixtures.For a pure liquid or azeotrope, composition does not change uponvaporization so that the integral heat of vaporization is identical to thedifferential heat of vaporization. Non-azeotropic liquid mixtures changecomposition upon vaporizing. Heat of vaporization data computed fromthis p

5、ractice for a liquid mixture are valid only as an approximation to themixture differential heat of vaporization; it is not a valid approximation tothe mixture integral heat of vaporization.1.2 The values stated in SI units are to be regarded asstandard. No other units of measurement are included in

6、thisstandard.1.3 There is no ISO standard equivalent to this practice.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 establish appro-priate safety and health practices and determine the

7、 applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D2879 Test Method for Vapor Pressure-Temperature Rela-tionship and Initial Decomposition Temperature of Liq-uids by IsoteniscopeE1142 Terminology Relating to Thermophysical PropertiesE1194 Test Method f

8、or Vapor Pressure (Withdrawn 2013)3E1719 Test Method for Vapor Pressure of Liquids by Ebul-liometryE1782 Test Method for Determining Vapor Pressure byThermal Analysis3. Terminology3.1 Symbols:3.1.1 A, B, CAntoine vapor pressure equation constants(log10, kPa, K), Antoine vapor pressure equation:log10

9、P 5 A 2 B/T1C!3.1.2 Pvapor pressure, kPa.3.1.3 Pccritical pressure, kPa.3.1.4 Prreduced pressure = P/Pc.3.1.5 Tabsolute temperature, K.3.1.6 Tccritical temperature, K.3.1.7 Trreduced temperature = T/Tc.3.1.8 Vmolar volume, cm3/mol.3.1.9 Rgas constant, 8.31433 J/mol-K; 8314330 kPa-cm3/mol-K.3.1.10 HV

10、heat of vaporization, J/mol.3.1.11 ZVdifference in compressibility factor (Z = PV/RT) upon vaporization. Clapeyron equation:HV52RZVdlnP!/d1/T!#3.1.11.1 DiscussionThe subscript “V” will be usedthroughout this practice to designate the vaporization of aliquid. If the vapor pressure data were measured

11、for a solid,substitute the subscript “S” for the sublimation of a solid.3.2 Definitions:3.2.1 Specialized terms used in this practice are defined inTerminology E1142.3.2.2 sublimationtransition from a solid phase to a gas-eous phase.3.2.3 vaporizationtransition from a liquid phase to agaseous phase.

12、1This practice is under the jurisdiction of Committee E37 on Thermal Measure-ments and is the direct responsibility of Subcommittee E37.10 on Fundamental,Statistical and Mechanical Properties.Current edition approved May 1, 2015. Published May 2015. Originallyapproved in 2000. Last previous edition

13、approved in 2010 as E2071 00 (2010).DOI: 510.1520/E2071-00R15.2For 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

14、.3The last approved version of this historical standard is referenced onwww.astm.org.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States14. Summary of Practice4.1 Vapor pressure data are measured by other referencedASTM standards and then

15、 correlated with the Antoine equa-tion. The heat of vaporization or sublimation is computed at thedesired temperature from the vapor-pressure temperature de-rivative from the fitted Antoine equation by use of theClapeyron equation (1).4In the Clapeyron equation, ZVisdetermined by either the Clausius

16、-Clapeyron(2) approxima-tion:ZV5 1!or the Haggenmacher (3) approximation:SZV5$1 2Pr/Tr!3#%12D4.2 An example calculation is given in Annex A1.5. Significance and Use5.1 If the heat of vaporization or sublimation is absorbed orliberated in a process at constant pressure, it is called enthalpyof vapori

17、zation or sublimation. Enthalpy of vaporization orsublimation is a fundamental thermodynamic property of aliquid or solid. It is an important quantity in the design of heatexchangers and other chemical process units. Enthalpy ofvaporization is also used to calculate solubility parameters (4).5.2 Thi

18、s practice may be used in research, regulatorycompliance, and quality assurance applications.6. Experimental Vapor Pressure Data6.1 Vapor pressure data are measured by Test MethodsD2879, E1194, E1719,orE1782. Note the safety precautionscontained in the test method used.6.1.1 Vapor pressure data from

19、 other reliable sources, forexample, peer-review technical journals, may be used. Thesource of the vapor pressure data must be noted.6.2 The measured vapor pressure data are fitted to anAntoine vapor pressure equation. See 10.3 in Test MethodE1719 for details on least-squares regression of vapor pre

20、ssuredata.7. Calculation7.1 At each temperature of interest, calculate the vaporpressure from the Antoine equation and calculate the vapor-pressure temperature derivative from the fitted Antoine equa-tion constants from:dlnP!/d1/T!# 522.3025851BT2/T1C!2#7.2 Calculate an approximation to ZVat each te

21、mperature.7.2.1 The Clausius-Clapeyron approximation to ZVis:ZV1.07.2.2 The Haggenmacher approximation to ZVis:ZV5$1 2Pr/Tr!3#%12NOTE 2The Clausius-Clapyeron approximation is generally used forsolids and for liquids at low Tr. The Haggenmacher approximation isgenerally used for liquids up to Tr 0.75

22、.7.2.3 If equation of state (Z) data are available for both thecondensed and gaseous phases, ZVmay be calculated directlyfrom the equation of state data.7.3 Calculate the heat of vaporization or heat of sublimationat each temperature from the Clapeyron equation:HV52RZVdlnP!/d1/T!#8. Report8.1 Report

23、 the following information:8.1.1 The test method and source of the vapor pressure dataused in the heat of vaporization or heat of sublimationcalculation. A vapor pressure data table shall also be reported.8.1.2 The Antoine equation constants fitted to the vaporpressure data.8.1.3 The approximation t

24、o ZVused in the calculation.8.1.4 The values and source of the critical temperature andcritical pressure data if the Haggenmacher approximation wasused for Z.8.1.5 A table that contains temperature, vapor pressure, thevapor pressure temperature derivative d(lnP)/ d(1/T), differ-ence in compressibili

25、ty factor (ZV), and HV, the heat ofvaporization or heat of sublimation.8.1.6 The specific dated version of this practice used.8.2 See the sample calculations and report in Annex A1.9. Keywords9.1 Antoine equation; Clausius-Clapeyron equation; en-thalpy of sublimation; enthalpy of vaporization; Hagge

26、n-macher equation; heat of sublimation; heat of vaporization;vapor pressure4The boldface numbers given in parentheses refer to a list of references at theend of the text.E2071 00 (2015)2ANNEX(Mandatory Information)A1. SAMPLE CALCULATIONS AND REPORTA1.1 Source of Sample Vapor Pressure DataA1.1.1 This

27、 sample calculation is performed on the samplevapor pressure data given for a toluene specimen in Annex A3of Test Method E1719. Heat of vaporization is calculated in10 K increments between 290 and 400 K. Calculations for boththe Clausius-Clapeyron and Haggenmacher approximations toZVare listed.A1.2

28、Sample Experimental DataA1.2.1 These controlled pressure-boiling temperature datapairs were measured by Test Method E1719 ona75cm3specimen charged to a vapor-lift pump ebulliometer:P (kPa) T (K)10.0 318.420.0 335.430.0 345.850.0 360.770.0 371.285.0 377.9100.0 383.3A1.2.2 A non-linear least-squares f

29、it of the Antoineequation, log10P = A - B/(T + C), produced these constants:A (fit) = 6.168057B (fit) = 1397.23C (fit) = 48.10A1.3 Sample CalculationA1.3.1 The critical temperature and pressure for toluene (5)are:Tc= 591.75 KPc= 4108.69 kPaAt 290 K:Tr= 0.490071821Pr= 0.000600191Vapor pressure 5 10 6

30、.168057 2 1397.23/290 2 48.10!#5 2.465997 kPadlnP!/d1/T!# 522.3025851 1397.23*2902/290 2 48.10!2# 524623.8938 KA1.3.2 Haggenmacher approximation to ZV:ZV5 $1 2 0.000600191/0.4900718121!3#%12 5 0.997447A1.3.3 HVfrom Clausius-Clapeyron approximation:HV5 28.31433!*1.00*24623.8938! 5 38444.6 J/molA1.3.4

31、 HVfrom Haggenmacher approximation:HV5 28.31433!*0.997447*24623.8938! 5 38346.4 J/molA1.4 Sample Heat of Vaporization ReportA1.4.1 Clausius-Clapeyron Approximation Report:A1.4.1.1 Data are for a toluene specimen and are listed inAnnex A3 of Test Method E1719. These controlled pressure-boiling temper

32、ature data pairs were measured by Test MethodE1719 ona75cm3specimen charged to a vapor-lift pumpebulliometer:P (kPa) T (K)10.0 318.420.0 335.430.0 345.850.0 360.770.0 371.285.0 377.9100.0 383.3A1.4.1.2 A non-linear least-squares fit of the Antoine equa-tion:log10P 5 A 2 B/T1C!produced these constant

33、s:A (fit) = 6.168057B (fit) = 1397.23C (fit) = 48.10A1.4.1.3 The Clausius Clapeyron approximation for ZVwas used.Temperature Pressured(lnP)/d(1/T) ZVHVK kPa K J/mol290 2.4659968 4623.8938 1.00000000 38444.6300 4.1811179 4563.2028 1.00000000 37940.0310 6.8089762 4507.5026 1.00000000 37476.9320 10.697

34、757 4456.2047 1.00000000 37050.4330 16.277326 4408.8094 1.00000000 36656.3340 24.064868 4364.8893 1.00000000 36291.1350 34.668504 4324.0774 1.00000000 35951.8360 48.788774 4286.0560 1.00000000 35635.7370 67.217970 4250.5496 1.00000000 35340.5380 90.837442 4217.3173 1.00000000 35064.2390 120.61303 41

35、86.1482 1.00000000 34805.0400 157.58889 4156.8566 1.00000000 34561.5A1.4.2 Haggenmacher Approximation Report:A1.4.2.1 Data are for a toluene specimen and are listed inAnnex A3 of Test Method E1719. These controlled pressure-boiling temperature data pairs were measured by Test MethodE1719 ona75cm3spe

36、cimen charged to a vapor-lift pumpebulliometer:P (kPa) T (K)10.0 318.420.0 335.430.0 345.850.0 360.770.0 371.285.0 377.9100.0 383.3A1.4.2.2 A non-linear least-squares fit of the Antoine equa-tion:log10P 5 A 2 B/T1C!produced these constants:A (fit) = 6.168057B (fit) = 1397.23C (fit) = 48.10E2071 00 (

37、2015)3A1.4.2.3 The Haggenmacher approximation for ZVwasused. The critical temperature and pressure used for toluene (5)are:Tc= 591.75 KPc= 4108.69 kPaTemperature Pressured(lnP)/d(1/T) ZVHVK kPa K J/mol290 2.4659968 4623.8938 0.99744709 38346.4300 4.1811179 4563.2028 0.99608744 37791.5Temperature Pre

38、ssured(lnP)/d(1/T) ZVHVK kPa K J/mol310 6.8089762 4507.5026 0.99421990 37260.2320 10.697757 4456.2047 0.99173347 36744.1330 16.277326 4408.8094 0.98851253 36235.2340 24.064868 4364.8893 0.98443961 35726.4350 34.668504 4324.0774 0.97939800 35211.1360 48.788774 4286.0560 0.97327384 34683.3370 67.21797

39、0 4250.5496 0.96595780 34137.4380 90.837442 4217.3173 0.95734617 33568.5390 120.61303 4186.1482 0.94734133 32972.2400 157.58889 4156.8566 0.93585171 32344.4REFERENCES(1) Van Ness, H. C., and Abbott, M. M., Classical Thermodynamics ofNonelectrolyte Solutions, McGraw-Hill, New York, NY, 1982, pp.96100

40、.(2) Van Ness, H. C., and Abbott, M. M., Classical Thermodynamics ofNonelectrolyte Solutions, McGraw-Hill, New York, NY, 1982, p. 100.(3) Haggenmacher, J. E., Journal of the American Chemical Society,Vol68, 1946.(4) Barton, A. F. M., CRC Handbook of Solubility Parameters and OtherCohesion Parameters

41、, CRC Press, Boca Raton, FL, 1991.(5) Daubert, T. E., ed., The DIPPR Project 801 Data Compilation, DesignInstitute of Physical Property Data, AICHE, New York, NY, 1990,CAS#, 108883.ASTM International takes no position respecting the validity of any patent rights asserted in connection with any item

42、mentionedin this standard. Users of this standard are expressly advised that determination 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 commit

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44、ting of theresponsible technical committee, which you may attend. If you feel that your comments 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,

45、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). Permission rights to photocopy the standard may also be secured from the Copyright Clearance Center, 222Rosewood Drive, Danvers, MA 01923, Tel: (978) 646-2600; http:/ 00 (2015)4