Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle
This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost...
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| Autor*in: |
Li, You-Rong [verfasserIn] Du, Mei-Tang [verfasserIn] Wang, Jian-Ning [verfasserIn] |
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E-Artikel |
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Walter de Gruyter GmbH ; 2012 |
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19 |
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Walter de Gruyter Online Zeitschriften |
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Enthalten in: Journal of non-equilibrium thermodynamics - Berlin [u.a.] : de Gruyter, 1976, 37(2012), 4 vom: 20. Nov., Seite 413-431 |
| Übergeordnetes Werk: |
volume:37 ; year:2012 ; number:4 ; day:20 ; month:11 ; pages:413-431 ; extent:19 |
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| DOI / URN: |
10.1515/jnetdy-2012-0013 |
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NLEJ247110477 |
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| 520 | |a This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. | ||
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10.1515/jnetdy-2012-0013 doi artikel_Grundlieferung.pp (DE-627)NLEJ247110477 DE-627 ger DE-627 rakwb Li, You-Rong verfasserin aut Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle Walter de Gruyter GmbH 2012 19 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. Walter de Gruyter Online Zeitschriften Organic rankine cycle (ORC) exergoeconomic analysis evaporation of binary mixtures condensation of binary mixtures Du, Mei-Tang verfasserin aut Wang, Jian-Ning verfasserin aut Enthalten in Journal of non-equilibrium thermodynamics Berlin [u.a.] : de Gruyter, 1976 37(2012), 4 vom: 20. Nov., Seite 413-431 (DE-627)NLEJ248236164 (DE-600)2021304-9 1437-4358 nnns volume:37 year:2012 number:4 day:20 month:11 pages:413-431 extent:19 https://doi.org/10.1515/jnetdy-2012-0013 Deutschlandweit zugänglich GBV_USEFLAG_U ZDB-1-DGR GBV_NL_ARTICLE AR 37 2012 4 20 11 413-431 19 |
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10.1515/jnetdy-2012-0013 doi artikel_Grundlieferung.pp (DE-627)NLEJ247110477 DE-627 ger DE-627 rakwb Li, You-Rong verfasserin aut Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle Walter de Gruyter GmbH 2012 19 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. Walter de Gruyter Online Zeitschriften Organic rankine cycle (ORC) exergoeconomic analysis evaporation of binary mixtures condensation of binary mixtures Du, Mei-Tang verfasserin aut Wang, Jian-Ning verfasserin aut Enthalten in Journal of non-equilibrium thermodynamics Berlin [u.a.] : de Gruyter, 1976 37(2012), 4 vom: 20. Nov., Seite 413-431 (DE-627)NLEJ248236164 (DE-600)2021304-9 1437-4358 nnns volume:37 year:2012 number:4 day:20 month:11 pages:413-431 extent:19 https://doi.org/10.1515/jnetdy-2012-0013 Deutschlandweit zugänglich GBV_USEFLAG_U ZDB-1-DGR GBV_NL_ARTICLE AR 37 2012 4 20 11 413-431 19 |
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10.1515/jnetdy-2012-0013 doi artikel_Grundlieferung.pp (DE-627)NLEJ247110477 DE-627 ger DE-627 rakwb Li, You-Rong verfasserin aut Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle Walter de Gruyter GmbH 2012 19 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. Walter de Gruyter Online Zeitschriften Organic rankine cycle (ORC) exergoeconomic analysis evaporation of binary mixtures condensation of binary mixtures Du, Mei-Tang verfasserin aut Wang, Jian-Ning verfasserin aut Enthalten in Journal of non-equilibrium thermodynamics Berlin [u.a.] : de Gruyter, 1976 37(2012), 4 vom: 20. Nov., Seite 413-431 (DE-627)NLEJ248236164 (DE-600)2021304-9 1437-4358 nnns volume:37 year:2012 number:4 day:20 month:11 pages:413-431 extent:19 https://doi.org/10.1515/jnetdy-2012-0013 Deutschlandweit zugänglich GBV_USEFLAG_U ZDB-1-DGR GBV_NL_ARTICLE AR 37 2012 4 20 11 413-431 19 |
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10.1515/jnetdy-2012-0013 doi artikel_Grundlieferung.pp (DE-627)NLEJ247110477 DE-627 ger DE-627 rakwb Li, You-Rong verfasserin aut Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle Walter de Gruyter GmbH 2012 19 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. Walter de Gruyter Online Zeitschriften Organic rankine cycle (ORC) exergoeconomic analysis evaporation of binary mixtures condensation of binary mixtures Du, Mei-Tang verfasserin aut Wang, Jian-Ning verfasserin aut Enthalten in Journal of non-equilibrium thermodynamics Berlin [u.a.] : de Gruyter, 1976 37(2012), 4 vom: 20. Nov., Seite 413-431 (DE-627)NLEJ248236164 (DE-600)2021304-9 1437-4358 nnns volume:37 year:2012 number:4 day:20 month:11 pages:413-431 extent:19 https://doi.org/10.1515/jnetdy-2012-0013 Deutschlandweit zugänglich GBV_USEFLAG_U ZDB-1-DGR GBV_NL_ARTICLE AR 37 2012 4 20 11 413-431 19 |
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10.1515/jnetdy-2012-0013 doi artikel_Grundlieferung.pp (DE-627)NLEJ247110477 DE-627 ger DE-627 rakwb Li, You-Rong verfasserin aut Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle Walter de Gruyter GmbH 2012 19 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. Walter de Gruyter Online Zeitschriften Organic rankine cycle (ORC) exergoeconomic analysis evaporation of binary mixtures condensation of binary mixtures Du, Mei-Tang verfasserin aut Wang, Jian-Ning verfasserin aut Enthalten in Journal of non-equilibrium thermodynamics Berlin [u.a.] : de Gruyter, 1976 37(2012), 4 vom: 20. Nov., Seite 413-431 (DE-627)NLEJ248236164 (DE-600)2021304-9 1437-4358 nnns volume:37 year:2012 number:4 day:20 month:11 pages:413-431 extent:19 https://doi.org/10.1515/jnetdy-2012-0013 Deutschlandweit zugänglich GBV_USEFLAG_U ZDB-1-DGR GBV_NL_ARTICLE AR 37 2012 4 20 11 413-431 19 |
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Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle |
| abstract |
This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. |
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This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. |
| abstract_unstemmed |
This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. In addition,optimal design parameters of evaporators were compared with those of condensers. |
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10.1515/jnetdy-2012-0013 |
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2024-07-06T09:58:16.860Z |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">NLEJ247110477</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20220820030336.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">220814s2012 xx |||||o 00| ||und c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1515/jnetdy-2012-0013</subfield><subfield code="2">doi</subfield></datafield><datafield tag="028" ind1="5" ind2="2"><subfield code="a">artikel_Grundlieferung.pp</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)NLEJ247110477</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Li, You-Rong</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Exergoeconomic analysis and optimization of an evaporator for a binary mixture of fluids in an organic Rankine cycle</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="b">Walter de Gruyter GmbH</subfield><subfield code="c">2012</subfield></datafield><datafield tag="300" ind1=" " ind2=" "><subfield code="a">19</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">This paper focuses on the research of an evaporator with a binary mixture oforganic working fluids in the organic Rankine cycle. Exergoeconomic analysisand performance optimization were performed based on the first andsecond laws of thermodynamics, and the exergoeconomic theory. The annualtotal cost per unit heat transfer rate was introduced as the objectivefunction. In this model, the exergy loss cost caused by the heat transferirreversibility and the capital cost were taken into account; however, theexergy loss due to the frictional pressure drops, heat dissipation tosurroundings, and the flow imbalance were neglected. The variation laws ofthe annual total cost with respect to the number of transfer units and thetemperature ratios were presented. Optimal design parameters that minimizethe objective function had been obtained, and the effects of some importantdimensionless parameters on the optimal performances had also beendiscussed for three types of evaporator flow arrangements. 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