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Performance analysis of OTEC power cycle with a liquid–vapor ejector using R32/R152a
In this paper, the condensation and evaporation capacity, turbine work, efficiency, and main component size of the Ocean Thermal Energy Conversion (OTEC) power system with a liquid–vapor ejector are presented to offer the basic design data for the operating parameters of the system. The analysis pro...
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Published in: | Heat and mass transfer 2015-11, Vol.51 (11), p.1597-1605 |
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creator | Yoon, Jung-In Son, Chang-Hyo Seol, Sung-hoon Kim, Hyeon-Uk Ha, Soo-Jung Jung, Suk-Ho Kim, Hyeon-Ju Lee, Ho-Saeng |
description | In this paper, the condensation and evaporation capacity, turbine work, efficiency, and main component size of the Ocean Thermal Energy Conversion (OTEC) power system with a liquid–vapor ejector are presented to offer the basic design data for the operating parameters of the system. The analysis procedure was performed with a simulation program called Aspentech HYSYS. The working fluid used in this system is the R32/R152a mixture. The operating parameters considered in this study include the vapor quality at the reheat outlet, the pressure ratio of the ejector, the inlet pressure of turbine 2, entrainment ratio of the liquid–vapor ejector etc. The main results are summarized as follows. The efficiency of the OTEC power cycle is closely related to the entrainment ratio of the liquid–vapor ejector. Also, the increase rate of the efficiency of proposed OTEC power cycle using the liquid–vapor ejector is 16 % higher than that of basic OTEC power cycle. Furthermore, regarding the reduction ratios of the system size that affects the initial cost, the reduction ratios of the evaporator size and the condenser size are about 13 and 14 % higher than those of basic OTEC power cycle, respectively. And, the pump power and the mass flow rate of the required refrigerant are 8 and 4 %, respectively. Therefore, the proposed OTEC power cycle is more advantageous than basic OTEC power cycle because of the compactness and high-efficiency of the system. |
doi_str_mv | 10.1007/s00231-015-1526-2 |
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The analysis procedure was performed with a simulation program called Aspentech HYSYS. The working fluid used in this system is the R32/R152a mixture. The operating parameters considered in this study include the vapor quality at the reheat outlet, the pressure ratio of the ejector, the inlet pressure of turbine 2, entrainment ratio of the liquid–vapor ejector etc. The main results are summarized as follows. The efficiency of the OTEC power cycle is closely related to the entrainment ratio of the liquid–vapor ejector. Also, the increase rate of the efficiency of proposed OTEC power cycle using the liquid–vapor ejector is 16 % higher than that of basic OTEC power cycle. Furthermore, regarding the reduction ratios of the system size that affects the initial cost, the reduction ratios of the evaporator size and the condenser size are about 13 and 14 % higher than those of basic OTEC power cycle, respectively. And, the pump power and the mass flow rate of the required refrigerant are 8 and 4 %, respectively. Therefore, the proposed OTEC power cycle is more advantageous than basic OTEC power cycle because of the compactness and high-efficiency of the system.</description><identifier>ISSN: 0947-7411</identifier><identifier>EISSN: 1432-1181</identifier><identifier>DOI: 10.1007/s00231-015-1526-2</identifier><language>eng</language><publisher>Berlin/Heidelberg: Springer Berlin Heidelberg</publisher><subject>Engineering ; Engineering Thermodynamics ; Heat and Mass Transfer ; Industrial Chemistry/Chemical Engineering ; Original ; Thermodynamics</subject><ispartof>Heat and mass transfer, 2015-11, Vol.51 (11), p.1597-1605</ispartof><rights>Springer-Verlag Berlin Heidelberg 2015</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c288t-a88fba6890594648f1d9d64d0ceeb2b06d69c9a61d0482a39e410247ba2cb25f3</citedby><cites>FETCH-LOGICAL-c288t-a88fba6890594648f1d9d64d0ceeb2b06d69c9a61d0482a39e410247ba2cb25f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Yoon, Jung-In</creatorcontrib><creatorcontrib>Son, Chang-Hyo</creatorcontrib><creatorcontrib>Seol, Sung-hoon</creatorcontrib><creatorcontrib>Kim, Hyeon-Uk</creatorcontrib><creatorcontrib>Ha, Soo-Jung</creatorcontrib><creatorcontrib>Jung, Suk-Ho</creatorcontrib><creatorcontrib>Kim, Hyeon-Ju</creatorcontrib><creatorcontrib>Lee, Ho-Saeng</creatorcontrib><title>Performance analysis of OTEC power cycle with a liquid–vapor ejector using R32/R152a</title><title>Heat and mass transfer</title><addtitle>Heat Mass Transfer</addtitle><description>In this paper, the condensation and evaporation capacity, turbine work, efficiency, and main component size of the Ocean Thermal Energy Conversion (OTEC) power system with a liquid–vapor ejector are presented to offer the basic design data for the operating parameters of the system. The analysis procedure was performed with a simulation program called Aspentech HYSYS. The working fluid used in this system is the R32/R152a mixture. The operating parameters considered in this study include the vapor quality at the reheat outlet, the pressure ratio of the ejector, the inlet pressure of turbine 2, entrainment ratio of the liquid–vapor ejector etc. The main results are summarized as follows. The efficiency of the OTEC power cycle is closely related to the entrainment ratio of the liquid–vapor ejector. Also, the increase rate of the efficiency of proposed OTEC power cycle using the liquid–vapor ejector is 16 % higher than that of basic OTEC power cycle. Furthermore, regarding the reduction ratios of the system size that affects the initial cost, the reduction ratios of the evaporator size and the condenser size are about 13 and 14 % higher than those of basic OTEC power cycle, respectively. And, the pump power and the mass flow rate of the required refrigerant are 8 and 4 %, respectively. Therefore, the proposed OTEC power cycle is more advantageous than basic OTEC power cycle because of the compactness and high-efficiency of the system.</description><subject>Engineering</subject><subject>Engineering Thermodynamics</subject><subject>Heat and Mass Transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Original</subject><subject>Thermodynamics</subject><issn>0947-7411</issn><issn>1432-1181</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><recordid>eNp9kE1OwzAQhS0EEqVwAHa-gKln4jj2ElXlR6pUVBW2luM4JVWaFLul6o47cENOgquyZvU273uj-Qi5BX4HnBejyDlmwDjkDHKUDM_IAESGDEDBORlwLQpWCIBLchXjKrWlwGxA3l58qPuwtp3z1Ha2PcQm0r6ms8VkTDf93gfqDq71dN9s36mlbfOxa6qfr-9Pu-kD9Svvtil3semWdJ7haJ7u22tyUds2-pu_HJLXh8li_MSms8fn8f2UOVRqy6xSdWml0jzXQgpVQ6UrKSruvC-x5LKS2mkroeJCoc20F8BRFKVFV2JeZ0MCp10X-hiDr80mNGsbDga4OYoxJzEmiTFHMQYTgycmpm639MGs-l1Ir8d_oF_7iWXz</recordid><startdate>20151101</startdate><enddate>20151101</enddate><creator>Yoon, Jung-In</creator><creator>Son, Chang-Hyo</creator><creator>Seol, Sung-hoon</creator><creator>Kim, Hyeon-Uk</creator><creator>Ha, Soo-Jung</creator><creator>Jung, Suk-Ho</creator><creator>Kim, Hyeon-Ju</creator><creator>Lee, Ho-Saeng</creator><general>Springer Berlin Heidelberg</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20151101</creationdate><title>Performance analysis of OTEC power cycle with a liquid–vapor ejector using R32/R152a</title><author>Yoon, Jung-In ; Son, Chang-Hyo ; Seol, Sung-hoon ; Kim, Hyeon-Uk ; Ha, Soo-Jung ; Jung, Suk-Ho ; Kim, Hyeon-Ju ; Lee, Ho-Saeng</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c288t-a88fba6890594648f1d9d64d0ceeb2b06d69c9a61d0482a39e410247ba2cb25f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>Engineering</topic><topic>Engineering Thermodynamics</topic><topic>Heat and Mass Transfer</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Original</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yoon, Jung-In</creatorcontrib><creatorcontrib>Son, Chang-Hyo</creatorcontrib><creatorcontrib>Seol, Sung-hoon</creatorcontrib><creatorcontrib>Kim, Hyeon-Uk</creatorcontrib><creatorcontrib>Ha, Soo-Jung</creatorcontrib><creatorcontrib>Jung, Suk-Ho</creatorcontrib><creatorcontrib>Kim, Hyeon-Ju</creatorcontrib><creatorcontrib>Lee, Ho-Saeng</creatorcontrib><collection>CrossRef</collection><jtitle>Heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yoon, Jung-In</au><au>Son, Chang-Hyo</au><au>Seol, Sung-hoon</au><au>Kim, Hyeon-Uk</au><au>Ha, Soo-Jung</au><au>Jung, Suk-Ho</au><au>Kim, Hyeon-Ju</au><au>Lee, Ho-Saeng</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance analysis of OTEC power cycle with a liquid–vapor ejector using R32/R152a</atitle><jtitle>Heat and mass transfer</jtitle><stitle>Heat Mass Transfer</stitle><date>2015-11-01</date><risdate>2015</risdate><volume>51</volume><issue>11</issue><spage>1597</spage><epage>1605</epage><pages>1597-1605</pages><issn>0947-7411</issn><eissn>1432-1181</eissn><abstract>In this paper, the condensation and evaporation capacity, turbine work, efficiency, and main component size of the Ocean Thermal Energy Conversion (OTEC) power system with a liquid–vapor ejector are presented to offer the basic design data for the operating parameters of the system. The analysis procedure was performed with a simulation program called Aspentech HYSYS. The working fluid used in this system is the R32/R152a mixture. The operating parameters considered in this study include the vapor quality at the reheat outlet, the pressure ratio of the ejector, the inlet pressure of turbine 2, entrainment ratio of the liquid–vapor ejector etc. The main results are summarized as follows. The efficiency of the OTEC power cycle is closely related to the entrainment ratio of the liquid–vapor ejector. Also, the increase rate of the efficiency of proposed OTEC power cycle using the liquid–vapor ejector is 16 % higher than that of basic OTEC power cycle. Furthermore, regarding the reduction ratios of the system size that affects the initial cost, the reduction ratios of the evaporator size and the condenser size are about 13 and 14 % higher than those of basic OTEC power cycle, respectively. And, the pump power and the mass flow rate of the required refrigerant are 8 and 4 %, respectively. Therefore, the proposed OTEC power cycle is more advantageous than basic OTEC power cycle because of the compactness and high-efficiency of the system.</abstract><cop>Berlin/Heidelberg</cop><pub>Springer Berlin Heidelberg</pub><doi>10.1007/s00231-015-1526-2</doi><tpages>9</tpages></addata></record> |
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title | Performance analysis of OTEC power cycle with a liquid–vapor ejector using R32/R152a |
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