Molar heat capacity of constant volume of difluoromethane (R32) and pentafluoroethane (R125) from the triple-point temperature to 345 K at pressures to 35 MPa
Molar heat capacities at constant volume (C sub(v)) of difluoromethane (R32) and pentafluoroethane (R125) were measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its...
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Veröffentlicht in: | International Journal of Thermophysics 1996-07, Vol.17 (4), p.823-849 |
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description | Molar heat capacities at constant volume (C sub(v)) of difluoromethane (R32) and pentafluoroethane (R125) were measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of a high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase (C super(() sub(v) super(2))), saturated liquid (C sub( sigma ) or C' sub(x)), and single-phase (C sub(v)) molar heat capacities. The C sub( sigma ) data were used to estimate vapor pressures for values less than 0.3 MPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. The triple-point temperature (T sub(tr)) and the enthalpy of fusion ( Delta sub(fus)H) were also measured for each substance. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded uncertainty (at the two-sigma level) for C sub(v) is estimated to be 0.7%, for C super(() sub(v) super(2)) it is 0.5%, and for C sub( sigma ) it is 0.7%. |
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O ; MAGEE, J. W</creator><creatorcontrib>LÜDDECKE, T. O ; MAGEE, J. W</creatorcontrib><description>Molar heat capacities at constant volume (C sub(v)) of difluoromethane (R32) and pentafluoroethane (R125) were measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of a high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase (C super(() sub(v) super(2))), saturated liquid (C sub( sigma ) or C' sub(x)), and single-phase (C sub(v)) molar heat capacities. The C sub( sigma ) data were used to estimate vapor pressures for values less than 0.3 MPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. The triple-point temperature (T sub(tr)) and the enthalpy of fusion ( Delta sub(fus)H) were also measured for each substance. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded uncertainty (at the two-sigma level) for C sub(v) is estimated to be 0.7%, for C super(() sub(v) super(2)) it is 0.5%, and for C sub( sigma ) it is 0.7%.</description><identifier>ISSN: 0195-928X</identifier><identifier>EISSN: 1572-9567</identifier><identifier>DOI: 10.1007/bf01439192</identifier><identifier>CODEN: IJTHDY</identifier><language>eng</language><publisher>New York, NY: Springer</publisher><subject>Applied sciences ; Calorimetry ; Condensed matter: structure, mechanical and thermal properties ; Energy ; Energy. Thermal use of fuels ; Enthalpy ; Ethane ; Exact sciences and technology ; Fluorocarbons ; HIGH PRESSURE ; MATERIALS SCIENCE ; MEDIUM PRESSURE ; Methane ; ORGANIC FLUORINE COMPOUNDS ; Physics ; Pressure effects ; REFRIGERANTS ; Refrigerating engineering ; Refrigerating engineering. Cryogenics. Food conservation ; SPECIFIC HEAT ; Specific heat of liquids ; TEMPERATURE RANGE 0065-0273 K ; TEMPERATURE RANGE 0273-0400 K ; Thermal properties of condensed matter ; Thermal properties of crystalline solids ; Thermodynamic properties ; Vapor pressure</subject><ispartof>International Journal of Thermophysics, 1996-07, Vol.17 (4), p.823-849</ispartof><rights>1996 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c382t-52757025bf4b40a772e3a171fd8156685393234579cb9d31bc7cdcec412d2c373</citedby><cites>FETCH-LOGICAL-c382t-52757025bf4b40a772e3a171fd8156685393234579cb9d31bc7cdcec412d2c373</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,885,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=3166028$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/376928$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>LÜDDECKE, T. O</creatorcontrib><creatorcontrib>MAGEE, J. W</creatorcontrib><title>Molar heat capacity of constant volume of difluoromethane (R32) and pentafluoroethane (R125) from the triple-point temperature to 345 K at pressures to 35 MPa</title><title>International Journal of Thermophysics</title><description>Molar heat capacities at constant volume (C sub(v)) of difluoromethane (R32) and pentafluoroethane (R125) were measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of a high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase (C super(() sub(v) super(2))), saturated liquid (C sub( sigma ) or C' sub(x)), and single-phase (C sub(v)) molar heat capacities. The C sub( sigma ) data were used to estimate vapor pressures for values less than 0.3 MPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. The triple-point temperature (T sub(tr)) and the enthalpy of fusion ( Delta sub(fus)H) were also measured for each substance. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded uncertainty (at the two-sigma level) for C sub(v) is estimated to be 0.7%, for C super(() sub(v) super(2)) it is 0.5%, and for C sub( sigma ) it is 0.7%.</description><subject>Applied sciences</subject><subject>Calorimetry</subject><subject>Condensed matter: structure, mechanical and thermal properties</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Enthalpy</subject><subject>Ethane</subject><subject>Exact sciences and technology</subject><subject>Fluorocarbons</subject><subject>HIGH PRESSURE</subject><subject>MATERIALS SCIENCE</subject><subject>MEDIUM PRESSURE</subject><subject>Methane</subject><subject>ORGANIC FLUORINE COMPOUNDS</subject><subject>Physics</subject><subject>Pressure effects</subject><subject>REFRIGERANTS</subject><subject>Refrigerating engineering</subject><subject>Refrigerating engineering. Cryogenics. Food conservation</subject><subject>SPECIFIC HEAT</subject><subject>Specific heat of liquids</subject><subject>TEMPERATURE RANGE 0065-0273 K</subject><subject>TEMPERATURE RANGE 0273-0400 K</subject><subject>Thermal properties of condensed matter</subject><subject>Thermal properties of crystalline solids</subject><subject>Thermodynamic properties</subject><subject>Vapor pressure</subject><issn>0195-928X</issn><issn>1572-9567</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1996</creationdate><recordtype>article</recordtype><recordid>eNo9kV9LHDEUxYNUcKu--AlSKLQWRvNnMtk8tuJacUUpFXwb7mRu2CkzkzHJFPwyflajqz4Fzv3lHO65hBxxdsIZ06eNY7yUhhuxQxZcaVEYVelPZMG4UYURy_s98jnGf4wxo41ckKdr30OgG4RELUxgu_RIvaPWjzHBmOh_388Dvkht5_rZBz9g2sCI9PsfKY4pjC2dcEywHX7MuFDH1GWapg3SFLqpx2LyXbZMOEwYIM0hDzyVpaJXNOdPAWPMYnxVFb2-hQOy66CPePj27pO71fnfs9_F-ubi8uznurByKVKhhFaaCdW4sikZaC1QAtfctUuuqmqppJEi52hjG9NK3lhtW4u25KIVVmq5T75sfX1MXR1zC2g3uYMRbaqlrnJzmfm2ZabgH2aMqR66aLHv88J-jrUuK1YyI0wmf2xJG3yMAV09hW6A8FhzVr_cqf61er9Thr--2UK00LsAo-3ixw_Jq4rl9GdoGJC8</recordid><startdate>19960701</startdate><enddate>19960701</enddate><creator>LÜDDECKE, T. O</creator><creator>MAGEE, J. W</creator><general>Springer</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TC</scope><scope>OTOTI</scope></search><sort><creationdate>19960701</creationdate><title>Molar heat capacity of constant volume of difluoromethane (R32) and pentafluoroethane (R125) from the triple-point temperature to 345 K at pressures to 35 MPa</title><author>LÜDDECKE, T. O ; MAGEE, J. W</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c382t-52757025bf4b40a772e3a171fd8156685393234579cb9d31bc7cdcec412d2c373</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1996</creationdate><topic>Applied sciences</topic><topic>Calorimetry</topic><topic>Condensed matter: structure, mechanical and thermal properties</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Enthalpy</topic><topic>Ethane</topic><topic>Exact sciences and technology</topic><topic>Fluorocarbons</topic><topic>HIGH PRESSURE</topic><topic>MATERIALS SCIENCE</topic><topic>MEDIUM PRESSURE</topic><topic>Methane</topic><topic>ORGANIC FLUORINE COMPOUNDS</topic><topic>Physics</topic><topic>Pressure effects</topic><topic>REFRIGERANTS</topic><topic>Refrigerating engineering</topic><topic>Refrigerating engineering. Cryogenics. Food conservation</topic><topic>SPECIFIC HEAT</topic><topic>Specific heat of liquids</topic><topic>TEMPERATURE RANGE 0065-0273 K</topic><topic>TEMPERATURE RANGE 0273-0400 K</topic><topic>Thermal properties of condensed matter</topic><topic>Thermal properties of crystalline solids</topic><topic>Thermodynamic properties</topic><topic>Vapor pressure</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>LÜDDECKE, T. O</creatorcontrib><creatorcontrib>MAGEE, J. W</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical Engineering Abstracts</collection><collection>OSTI.GOV</collection><jtitle>International Journal of Thermophysics</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>LÜDDECKE, T. O</au><au>MAGEE, J. W</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Molar heat capacity of constant volume of difluoromethane (R32) and pentafluoroethane (R125) from the triple-point temperature to 345 K at pressures to 35 MPa</atitle><jtitle>International Journal of Thermophysics</jtitle><date>1996-07-01</date><risdate>1996</risdate><volume>17</volume><issue>4</issue><spage>823</spage><epage>849</epage><pages>823-849</pages><issn>0195-928X</issn><eissn>1572-9567</eissn><coden>IJTHDY</coden><abstract>Molar heat capacities at constant volume (C sub(v)) of difluoromethane (R32) and pentafluoroethane (R125) were measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of a high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase (C super(() sub(v) super(2))), saturated liquid (C sub( sigma ) or C' sub(x)), and single-phase (C sub(v)) molar heat capacities. The C sub( sigma ) data were used to estimate vapor pressures for values less than 0.3 MPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. The triple-point temperature (T sub(tr)) and the enthalpy of fusion ( Delta sub(fus)H) were also measured for each substance. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded uncertainty (at the two-sigma level) for C sub(v) is estimated to be 0.7%, for C super(() sub(v) super(2)) it is 0.5%, and for C sub( sigma ) it is 0.7%.</abstract><cop>New York, NY</cop><pub>Springer</pub><doi>10.1007/bf01439192</doi><tpages>27</tpages></addata></record> |
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subjects | Applied sciences Calorimetry Condensed matter: structure, mechanical and thermal properties Energy Energy. Thermal use of fuels Enthalpy Ethane Exact sciences and technology Fluorocarbons HIGH PRESSURE MATERIALS SCIENCE MEDIUM PRESSURE Methane ORGANIC FLUORINE COMPOUNDS Physics Pressure effects REFRIGERANTS Refrigerating engineering Refrigerating engineering. Cryogenics. Food conservation SPECIFIC HEAT Specific heat of liquids TEMPERATURE RANGE 0065-0273 K TEMPERATURE RANGE 0273-0400 K Thermal properties of condensed matter Thermal properties of crystalline solids Thermodynamic properties Vapor pressure |
title | Molar heat capacity of constant volume of difluoromethane (R32) and pentafluoroethane (R125) from the triple-point temperature to 345 K at pressures to 35 MPa |
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