Evaluation of the thermodynamic effectiveness of a plate heat exchanger integrated into an experimental single stage heat transformer operating with Water/Carrol mixture
•Thermodynamical methods for heat exchanger effectiveness were described.•Water/Carrol mixture was analyzed into an experimental absorption heat transformer.•Similar plate heat exchanger effectiveness values were obtained for both methods with experimental conditions.•Single stage heat transformer’s...
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Veröffentlicht in: | Experimental thermal and fluid science 2013-11, Vol.51, p.257-263 |
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creator | Ibarra-Bahena, J. Romero, R.J. Velazquez-Avelar, L. Valdez-Morales, C.V. Galindo-Luna, Y.R. |
description | •Thermodynamical methods for heat exchanger effectiveness were described.•Water/Carrol mixture was analyzed into an experimental absorption heat transformer.•Similar plate heat exchanger effectiveness values were obtained for both methods with experimental conditions.•Single stage heat transformer’s coefficients of performance were calculate with and without economizer.
This paper analyzes the effectiveness of a Plate Heat Exchanger (PHE) used as an economizer integrated into an experimental Single Stage Heat Transformer (SSHT). The heat exchanger effectiveness (η), sometimes referred as thermal efficiency, is an important parameter for the design of heat transfer equipment. Two thermodynamic methods for η evaluation are shown. The overall heat transfer coefficient (U) and the individual convective heat transfer coefficients (h) were calculated for Water/Carrol mixture. Four SSHT experimental tests runs were carried out, in order to evaluate the η. The economizer effectiveness ranged from 0.69 to 0.71. Finally, the η effect for Coefficient of Performance (COP) is shown as a function of absorber temperature. |
doi_str_mv | 10.1016/j.expthermflusci.2013.08.006 |
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This paper analyzes the effectiveness of a Plate Heat Exchanger (PHE) used as an economizer integrated into an experimental Single Stage Heat Transformer (SSHT). The heat exchanger effectiveness (η), sometimes referred as thermal efficiency, is an important parameter for the design of heat transfer equipment. Two thermodynamic methods for η evaluation are shown. The overall heat transfer coefficient (U) and the individual convective heat transfer coefficients (h) were calculated for Water/Carrol mixture. Four SSHT experimental tests runs were carried out, in order to evaluate the η. The economizer effectiveness ranged from 0.69 to 0.71. Finally, the η effect for Coefficient of Performance (COP) is shown as a function of absorber temperature.</description><identifier>ISSN: 0894-1777</identifier><identifier>EISSN: 1879-2286</identifier><identifier>DOI: 10.1016/j.expthermflusci.2013.08.006</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>Applied sciences ; Devices using thermal energy ; Economizer ; Effectiveness ; Energy ; Energy balance ; Energy. Thermal use of fuels ; Equipment costs ; Exact sciences and technology ; Heat exchangers (included heat transformers, condensers, cooling towers) ; Heat transfer coefficients ; Heat transformers ; Mathematical analysis ; Plate heat exchangers ; Rational use of energy: conservation and recovery of energy ; Single stage ; Single stage heat transformer ; Thermal efficiency ; Thermodynamics ; Water/Carrol ; ε – NTU method</subject><ispartof>Experimental thermal and fluid science, 2013-11, Vol.51, p.257-263</ispartof><rights>2013 Elsevier Inc.</rights><rights>2014 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c492t-13eeac736f96f2b71390464803ad937c4852fb1c754fa5de1e343cc9bb597e323</citedby><cites>FETCH-LOGICAL-c492t-13eeac736f96f2b71390464803ad937c4852fb1c754fa5de1e343cc9bb597e323</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0894177713001817$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=27830219$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Ibarra-Bahena, J.</creatorcontrib><creatorcontrib>Romero, R.J.</creatorcontrib><creatorcontrib>Velazquez-Avelar, L.</creatorcontrib><creatorcontrib>Valdez-Morales, C.V.</creatorcontrib><creatorcontrib>Galindo-Luna, Y.R.</creatorcontrib><title>Evaluation of the thermodynamic effectiveness of a plate heat exchanger integrated into an experimental single stage heat transformer operating with Water/Carrol mixture</title><title>Experimental thermal and fluid science</title><description>•Thermodynamical methods for heat exchanger effectiveness were described.•Water/Carrol mixture was analyzed into an experimental absorption heat transformer.•Similar plate heat exchanger effectiveness values were obtained for both methods with experimental conditions.•Single stage heat transformer’s coefficients of performance were calculate with and without economizer.
This paper analyzes the effectiveness of a Plate Heat Exchanger (PHE) used as an economizer integrated into an experimental Single Stage Heat Transformer (SSHT). The heat exchanger effectiveness (η), sometimes referred as thermal efficiency, is an important parameter for the design of heat transfer equipment. Two thermodynamic methods for η evaluation are shown. The overall heat transfer coefficient (U) and the individual convective heat transfer coefficients (h) were calculated for Water/Carrol mixture. Four SSHT experimental tests runs were carried out, in order to evaluate the η. The economizer effectiveness ranged from 0.69 to 0.71. Finally, the η effect for Coefficient of Performance (COP) is shown as a function of absorber temperature.</description><subject>Applied sciences</subject><subject>Devices using thermal energy</subject><subject>Economizer</subject><subject>Effectiveness</subject><subject>Energy</subject><subject>Energy balance</subject><subject>Energy. Thermal use of fuels</subject><subject>Equipment costs</subject><subject>Exact sciences and technology</subject><subject>Heat exchangers (included heat transformers, condensers, cooling towers)</subject><subject>Heat transfer coefficients</subject><subject>Heat transformers</subject><subject>Mathematical analysis</subject><subject>Plate heat exchangers</subject><subject>Rational use of energy: conservation and recovery of energy</subject><subject>Single stage</subject><subject>Single stage heat transformer</subject><subject>Thermal efficiency</subject><subject>Thermodynamics</subject><subject>Water/Carrol</subject><subject>ε – NTU method</subject><issn>0894-1777</issn><issn>1879-2286</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqNks9u1DAQxiMEEkvhHXwAiUtS_0liR-KCVi0gVeIC4mh5nXHWq8QOtrNsH6lvidNdIXFqT7Y0v_nm08xXFO8Jrggm7fWhgtOc9hAmMy5R24piwiosKozbF8WGCN6VlIr2ZbHBoqtLwjl_XbyJ8YAxFpTgTfFwc1TjopL1DnmDshh6FPT9vVOT1QiMAZ3sERzEuCIKzaNKgPagEoKT3is3QEDWJRhCLvTr1yPlcnGGYCdwSY0oWjeMgGJSw6U3BeWi8WHK3T6T2YQb0B-b9uhX1gnXWxWCH9FkT2kJ8LZ4ZdQY4d3lvSp-3t782H4t775_-bb9fFfquqOpJAxAac5a07WG7jhhHa7bWmCm-o5xXYuGmh3RvKmNanogwGqmdbfbNR0HRtlV8fGsOwf_e4GY5GSjhnFUDvwSJWm5wJg0hDwH5Z0gDLdPow1htchW-NNozZumpaxZ0U9nVAcfYwAj57xwFe4lwXKNiDzI_yMi14hILCR-NPXhMklFrUaTD6Jt_KdBuWCYki5zt2cO8t6PFoLMSuA09DbkcMje2-cN_AvQYd5y</recordid><startdate>20131101</startdate><enddate>20131101</enddate><creator>Ibarra-Bahena, J.</creator><creator>Romero, R.J.</creator><creator>Velazquez-Avelar, L.</creator><creator>Valdez-Morales, C.V.</creator><creator>Galindo-Luna, Y.R.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope><scope>7TB</scope><scope>7U5</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20131101</creationdate><title>Evaluation of the thermodynamic effectiveness of a plate heat exchanger integrated into an experimental single stage heat transformer operating with Water/Carrol mixture</title><author>Ibarra-Bahena, J. ; Romero, R.J. ; Velazquez-Avelar, L. ; Valdez-Morales, C.V. ; Galindo-Luna, Y.R.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c492t-13eeac736f96f2b71390464803ad937c4852fb1c754fa5de1e343cc9bb597e323</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Applied sciences</topic><topic>Devices using thermal energy</topic><topic>Economizer</topic><topic>Effectiveness</topic><topic>Energy</topic><topic>Energy balance</topic><topic>Energy. Thermal use of fuels</topic><topic>Equipment costs</topic><topic>Exact sciences and technology</topic><topic>Heat exchangers (included heat transformers, condensers, cooling towers)</topic><topic>Heat transfer coefficients</topic><topic>Heat transformers</topic><topic>Mathematical analysis</topic><topic>Plate heat exchangers</topic><topic>Rational use of energy: conservation and recovery of energy</topic><topic>Single stage</topic><topic>Single stage heat transformer</topic><topic>Thermal efficiency</topic><topic>Thermodynamics</topic><topic>Water/Carrol</topic><topic>ε – NTU method</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ibarra-Bahena, J.</creatorcontrib><creatorcontrib>Romero, R.J.</creatorcontrib><creatorcontrib>Velazquez-Avelar, L.</creatorcontrib><creatorcontrib>Valdez-Morales, C.V.</creatorcontrib><creatorcontrib>Galindo-Luna, Y.R.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Experimental thermal and fluid science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ibarra-Bahena, J.</au><au>Romero, R.J.</au><au>Velazquez-Avelar, L.</au><au>Valdez-Morales, C.V.</au><au>Galindo-Luna, Y.R.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaluation of the thermodynamic effectiveness of a plate heat exchanger integrated into an experimental single stage heat transformer operating with Water/Carrol mixture</atitle><jtitle>Experimental thermal and fluid science</jtitle><date>2013-11-01</date><risdate>2013</risdate><volume>51</volume><spage>257</spage><epage>263</epage><pages>257-263</pages><issn>0894-1777</issn><eissn>1879-2286</eissn><abstract>•Thermodynamical methods for heat exchanger effectiveness were described.•Water/Carrol mixture was analyzed into an experimental absorption heat transformer.•Similar plate heat exchanger effectiveness values were obtained for both methods with experimental conditions.•Single stage heat transformer’s coefficients of performance were calculate with and without economizer.
This paper analyzes the effectiveness of a Plate Heat Exchanger (PHE) used as an economizer integrated into an experimental Single Stage Heat Transformer (SSHT). The heat exchanger effectiveness (η), sometimes referred as thermal efficiency, is an important parameter for the design of heat transfer equipment. Two thermodynamic methods for η evaluation are shown. The overall heat transfer coefficient (U) and the individual convective heat transfer coefficients (h) were calculated for Water/Carrol mixture. Four SSHT experimental tests runs were carried out, in order to evaluate the η. The economizer effectiveness ranged from 0.69 to 0.71. Finally, the η effect for Coefficient of Performance (COP) is shown as a function of absorber temperature.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1016/j.expthermflusci.2013.08.006</doi><tpages>7</tpages></addata></record> |
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subjects | Applied sciences Devices using thermal energy Economizer Effectiveness Energy Energy balance Energy. Thermal use of fuels Equipment costs Exact sciences and technology Heat exchangers (included heat transformers, condensers, cooling towers) Heat transfer coefficients Heat transformers Mathematical analysis Plate heat exchangers Rational use of energy: conservation and recovery of energy Single stage Single stage heat transformer Thermal efficiency Thermodynamics Water/Carrol ε – NTU method |
title | Evaluation of the thermodynamic effectiveness of a plate heat exchanger integrated into an experimental single stage heat transformer operating with Water/Carrol mixture |
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