Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model
Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction avera...
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| Autor*in: |
Matsuda, Hiroyuki [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2022 |
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| Anmerkung: |
© The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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| Übergeordnetes Werk: |
Enthalten in: Journal of solution chemistry - New York, NY [u.a.] : Springer Science + Business Media B.V., 1972, 52(2022), 1 vom: 11. Nov., Seite 105-133 |
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| Übergeordnetes Werk: |
volume:52 ; year:2022 ; number:1 ; day:11 ; month:11 ; pages:105-133 |
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| DOI / URN: |
10.1007/s10953-022-01220-9 |
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SPR048978736 |
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| 520 | |a Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. | ||
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10.1007/s10953-022-01220-9 doi (DE-627)SPR048978736 (SPR)s10953-022-01220-9-e DE-627 ger DE-627 rakwb eng Matsuda, Hiroyuki verfasserin (orcid)0000-0003-3580-8483 aut Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 Tochigi, Katsumi aut Kurihara, Kiyofumi aut Funazukuri, Toshitaka aut Enthalten in Journal of solution chemistry New York, NY [u.a.] : Springer Science + Business Media B.V., 1972 52(2022), 1 vom: 11. Nov., Seite 105-133 (DE-627)317881876 (DE-600)2017287-4 1572-8927 nnns volume:52 year:2022 number:1 day:11 month:11 pages:105-133 https://dx.doi.org/10.1007/s10953-022-01220-9 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 52 2022 1 11 11 105-133 |
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10.1007/s10953-022-01220-9 doi (DE-627)SPR048978736 (SPR)s10953-022-01220-9-e DE-627 ger DE-627 rakwb eng Matsuda, Hiroyuki verfasserin (orcid)0000-0003-3580-8483 aut Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 Tochigi, Katsumi aut Kurihara, Kiyofumi aut Funazukuri, Toshitaka aut Enthalten in Journal of solution chemistry New York, NY [u.a.] : Springer Science + Business Media B.V., 1972 52(2022), 1 vom: 11. Nov., Seite 105-133 (DE-627)317881876 (DE-600)2017287-4 1572-8927 nnns volume:52 year:2022 number:1 day:11 month:11 pages:105-133 https://dx.doi.org/10.1007/s10953-022-01220-9 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 52 2022 1 11 11 105-133 |
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10.1007/s10953-022-01220-9 doi (DE-627)SPR048978736 (SPR)s10953-022-01220-9-e DE-627 ger DE-627 rakwb eng Matsuda, Hiroyuki verfasserin (orcid)0000-0003-3580-8483 aut Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 Tochigi, Katsumi aut Kurihara, Kiyofumi aut Funazukuri, Toshitaka aut Enthalten in Journal of solution chemistry New York, NY [u.a.] : Springer Science + Business Media B.V., 1972 52(2022), 1 vom: 11. Nov., Seite 105-133 (DE-627)317881876 (DE-600)2017287-4 1572-8927 nnns volume:52 year:2022 number:1 day:11 month:11 pages:105-133 https://dx.doi.org/10.1007/s10953-022-01220-9 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 52 2022 1 11 11 105-133 |
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10.1007/s10953-022-01220-9 doi (DE-627)SPR048978736 (SPR)s10953-022-01220-9-e DE-627 ger DE-627 rakwb eng Matsuda, Hiroyuki verfasserin (orcid)0000-0003-3580-8483 aut Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 Tochigi, Katsumi aut Kurihara, Kiyofumi aut Funazukuri, Toshitaka aut Enthalten in Journal of solution chemistry New York, NY [u.a.] : Springer Science + Business Media B.V., 1972 52(2022), 1 vom: 11. Nov., Seite 105-133 (DE-627)317881876 (DE-600)2017287-4 1572-8927 nnns volume:52 year:2022 number:1 day:11 month:11 pages:105-133 https://dx.doi.org/10.1007/s10953-022-01220-9 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 52 2022 1 11 11 105-133 |
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10.1007/s10953-022-01220-9 doi (DE-627)SPR048978736 (SPR)s10953-022-01220-9-e DE-627 ger DE-627 rakwb eng Matsuda, Hiroyuki verfasserin (orcid)0000-0003-3580-8483 aut Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 Tochigi, Katsumi aut Kurihara, Kiyofumi aut Funazukuri, Toshitaka aut Enthalten in Journal of solution chemistry New York, NY [u.a.] : Springer Science + Business Media B.V., 1972 52(2022), 1 vom: 11. Nov., Seite 105-133 (DE-627)317881876 (DE-600)2017287-4 1572-8927 nnns volume:52 year:2022 number:1 day:11 month:11 pages:105-133 https://dx.doi.org/10.1007/s10953-022-01220-9 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 52 2022 1 11 11 105-133 |
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Matsuda, Hiroyuki |
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Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model Thermal conductivity (dpeaa)DE-He213 Excess thermal conductivity model (dpeaa)DE-He213 Wilson-ThermConduct model (dpeaa)DE-He213 |
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estimation of thermal conductivities for binary and ternary liquid mixtures using excess thermal conductivity model |
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Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model |
| abstract |
Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
| abstractGer |
Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
| abstract_unstemmed |
Abstract The objective of this work is the estimation of thermal conductivities for binary and ternary liquid mixtures using an excess thermal conductivity model. Firstly, calculation methods for thermal conductivities of ideal solutions are discussed using four models, including mole fraction average, One intuitively similar to Eyring’s model for kinematic viscosity and mass fraction average. Next, the Wilson-ThermConduct model was applied as the excess thermal conductivity model. The binary parameters in the model were determined from non-aqueous and aqueous binary thermal conductivity data. The prediction of the thermal conductivities for the ternary systems was done using the binary parameters of the binary constituent systems. The model presented in this work gave a 0.66% average absolute relative deviation of overall datasets. The evaluated results were compared with those using the mass fraction average (ideal) model, the Vredeveld’s power-law model, and Rowley’s local composition model with NRTL parameters determined from VLE data. © The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2022. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model |
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https://dx.doi.org/10.1007/s10953-022-01220-9 |
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Tochigi, Katsumi Kurihara, Kiyofumi Funazukuri, Toshitaka |
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Tochigi, Katsumi Kurihara, Kiyofumi Funazukuri, Toshitaka |
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10.1007/s10953-022-01220-9 |
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2024-07-03T22:36:07.419Z |
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| score |
7.3991528 |