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The heat transfer and entropy generation of fin and inclined flat tube heat exchanger
The present work determines the appropriate inclination angles for each flat tube aspect ratio to increase the thermohydraulic performance without extending the heat exchange area. Furthermore, the amount of entropy generation was investigated to evaluate the exergy destruction for device configurat...
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Published in: | Case studies in thermal engineering 2024-04, Vol.56, p.104202, Article 104202 |
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description | The present work determines the appropriate inclination angles for each flat tube aspect ratio to increase the thermohydraulic performance without extending the heat exchange area. Furthermore, the amount of entropy generation was investigated to evaluate the exergy destruction for device configuration. A numerical simulation was performed with an inlet air velocity in a range from 3.5 to 5.0 m/s, flat tube aspect ratios (e) from 0.3 to 0.6, and tube inclination angles (β) from 10 to 50°. Analysis results indicated that the highest thermohydraulic performance of configuration e = 0.4 and e = 0.5 was obtained at β = 20°, and for configuration e = 0.3, it was obtained at β = 10−20°. The best thermohydraulic performance for configuration e = 0.6 was obtained at β = 20−30°. The thermohydraulic performance at optimal inclination angles extended from 1.011 to 1.069. The lowest entropy generation occurred at configurations with β = 50°. Increasing the aspect ratio and tube inclination angle increased the Colburn factor, increased the friction factor, and decreased entropy generation. |
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Furthermore, the amount of entropy generation was investigated to evaluate the exergy destruction for device configuration. A numerical simulation was performed with an inlet air velocity in a range from 3.5 to 5.0 m/s, flat tube aspect ratios (e) from 0.3 to 0.6, and tube inclination angles (β) from 10 to 50°. Analysis results indicated that the highest thermohydraulic performance of configuration e = 0.4 and e = 0.5 was obtained at β = 20°, and for configuration e = 0.3, it was obtained at β = 10−20°. The best thermohydraulic performance for configuration e = 0.6 was obtained at β = 20−30°. The thermohydraulic performance at optimal inclination angles extended from 1.011 to 1.069. The lowest entropy generation occurred at configurations with β = 50°. 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Increasing the aspect ratio and tube inclination angle increased the Colburn factor, increased the friction factor, and decreased entropy generation.</description><subject>Entropy generation</subject><subject>Fin tube heat exchanger</subject><subject>Flat tube</subject><subject>Thermohydraulic performance</subject><issn>2214-157X</issn><issn>2214-157X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><sourceid>DOA</sourceid><recordid>eNp9kM1qwzAQhEVpoaHNE_TiF3C6smRbPvRQQn8CgV4S6E0o0iqRceUgqaV5-zpxKD31NMss87E7hNxRmFGg1X0709ElnBVQ8MHhg16QSVFQntOyfr_8M1-TaYwtANCaCcr5hKxXO8x2qFKWgvLRYsiUNxn6FPr9Iduix6CS633W28w6f9o6rzvn0WS2OwY_N2cEfuud8lsMt-TKqi7i9Kw3ZP38tJq_5su3l8X8cZlrVvGUG6igoVgbRkVJjSqbhiprqeawKWth0RgqWCN0w22ltQXBxKZCy8EoCtCwG7IYuaZXrdwH96HCQfbKyZPRh61UITndoVQF2oHPgIua8xIaLIVmWHFktah4ObDYyNKhjzGg_eVRkMeiZStPRctj0XIsekg9jCkc3vxyGGTUDr1G4wLqNNzh_s3_AINOhqE</recordid><startdate>202404</startdate><enddate>202404</enddate><creator>Thanh, Luan Nguyen</creator><creator>Nhut, Le Minh</creator><creator>Hoang, An-Quoc</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>6I.</scope><scope>AAFTH</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>DOA</scope><orcidid>https://orcid.org/0000-0002-0254-2730</orcidid><orcidid>https://orcid.org/0000-0002-0603-8689</orcidid><orcidid>https://orcid.org/0000-0003-1241-2611</orcidid></search><sort><creationdate>202404</creationdate><title>The heat transfer and entropy generation of fin and inclined flat tube heat exchanger</title><author>Thanh, Luan Nguyen ; Nhut, Le Minh ; Hoang, An-Quoc</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c364t-d06091e7d31851da5991aff1c40b578fedd18398c94f6ccf0838b6ef40da10093</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Entropy generation</topic><topic>Fin tube heat exchanger</topic><topic>Flat tube</topic><topic>Thermohydraulic performance</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Thanh, Luan Nguyen</creatorcontrib><creatorcontrib>Nhut, Le Minh</creatorcontrib><creatorcontrib>Hoang, An-Quoc</creatorcontrib><collection>ScienceDirect Open Access Titles</collection><collection>Elsevier:ScienceDirect:Open Access</collection><collection>CrossRef</collection><collection>Directory of Open Access Journals</collection><jtitle>Case studies in thermal engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Thanh, Luan Nguyen</au><au>Nhut, Le Minh</au><au>Hoang, An-Quoc</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The heat transfer and entropy generation of fin and inclined flat tube heat exchanger</atitle><jtitle>Case studies in thermal engineering</jtitle><date>2024-04</date><risdate>2024</risdate><volume>56</volume><spage>104202</spage><pages>104202-</pages><artnum>104202</artnum><issn>2214-157X</issn><eissn>2214-157X</eissn><abstract>The present work determines the appropriate inclination angles for each flat tube aspect ratio to increase the thermohydraulic performance without extending the heat exchange area. Furthermore, the amount of entropy generation was investigated to evaluate the exergy destruction for device configuration. A numerical simulation was performed with an inlet air velocity in a range from 3.5 to 5.0 m/s, flat tube aspect ratios (e) from 0.3 to 0.6, and tube inclination angles (β) from 10 to 50°. Analysis results indicated that the highest thermohydraulic performance of configuration e = 0.4 and e = 0.5 was obtained at β = 20°, and for configuration e = 0.3, it was obtained at β = 10−20°. The best thermohydraulic performance for configuration e = 0.6 was obtained at β = 20−30°. The thermohydraulic performance at optimal inclination angles extended from 1.011 to 1.069. The lowest entropy generation occurred at configurations with β = 50°. 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subjects | Entropy generation Fin tube heat exchanger Flat tube Thermohydraulic performance |
title | The heat transfer and entropy generation of fin and inclined flat tube heat exchanger |
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