Enhancement of Heat Transfer in a Tube Channel of a Tubular Heat Exchanger
Thermal engineering experiments were carried out with laboratory water-to-water tube-in-tube heat exchangers of the same design parameters with smooth and profiled inner tubes. The tubes were profiled by confuser–diffuser constrictions of the flow section of the inner channel, which were formed by t...
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Veröffentlicht in: | Theoretical foundations of chemical engineering 2023-10, Vol.57 (5), p.869-875 |
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creator | Konoplev, A. A. Rytov, B. L. Berlin, Al. Al Romanov, S. V. |
description | Thermal engineering experiments were carried out with laboratory water-to-water tube-in-tube heat exchangers of the same design parameters with smooth and profiled inner tubes. The tubes were profiled by confuser–diffuser constrictions of the flow section of the inner channel, which were formed by the deformation of their walls and placed along the length at a step that was constant and equal for all profiled tubes. The obtained results showed a dependence of the heat transfer enhancement in the tube channel on the Reynolds and Prandtl numbers, with the dependence on the latter being much stronger than that on the former, at least in cases where the heat carrier is water. |
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A. ; Rytov, B. L. ; Berlin, Al. Al ; Romanov, S. V.</creator><creatorcontrib>Konoplev, A. A. ; Rytov, B. L. ; Berlin, Al. Al ; Romanov, S. V.</creatorcontrib><description>Thermal engineering experiments were carried out with laboratory water-to-water tube-in-tube heat exchangers of the same design parameters with smooth and profiled inner tubes. The tubes were profiled by confuser–diffuser constrictions of the flow section of the inner channel, which were formed by the deformation of their walls and placed along the length at a step that was constant and equal for all profiled tubes. The obtained results showed a dependence of the heat transfer enhancement in the tube channel on the Reynolds and Prandtl numbers, with the dependence on the latter being much stronger than that on the former, at least in cases where the heat carrier is water.</description><identifier>ISSN: 0040-5795</identifier><identifier>EISSN: 1608-3431</identifier><identifier>DOI: 10.1134/S0040579523050433</identifier><language>eng</language><publisher>Moscow: Pleiades Publishing</publisher><subject>Chemistry ; Chemistry and Materials Science ; Design parameters ; Diffusers ; Heat transfer ; Industrial Chemistry/Chemical Engineering ; Thermal engineering ; Tube heat exchangers ; Tubes</subject><ispartof>Theoretical foundations of chemical engineering, 2023-10, Vol.57 (5), p.869-875</ispartof><rights>Pleiades Publishing, Ltd. 2023. ISSN 0040-5795, Theoretical Foundations of Chemical Engineering, 2023, Vol. 57, No. 5, pp. 869–875. © Pleiades Publishing, Ltd., 2023. Russian Text © The Author(s), 2023, published in Teoreticheskie Osnovy Khimicheskoi Tekhnologii, 2023, Vol. 57, No. 5, pp. 589–595.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c268t-400b3038474fd5f85a248df8d3cdfff3fcbe7d060f9b000b897ddeeda101eecb3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1134/S0040579523050433$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1134/S0040579523050433$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27924,27925,41488,42557,51319</link.rule.ids></links><search><creatorcontrib>Konoplev, A. A.</creatorcontrib><creatorcontrib>Rytov, B. L.</creatorcontrib><creatorcontrib>Berlin, Al. Al</creatorcontrib><creatorcontrib>Romanov, S. 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The obtained results showed a dependence of the heat transfer enhancement in the tube channel on the Reynolds and Prandtl numbers, with the dependence on the latter being much stronger than that on the former, at least in cases where the heat carrier is water.</description><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Design parameters</subject><subject>Diffusers</subject><subject>Heat transfer</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Thermal engineering</subject><subject>Tube heat exchangers</subject><subject>Tubes</subject><issn>0040-5795</issn><issn>1608-3431</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><recordid>eNp1kEFLxDAQhYMouK7-AG8Bz9VJk7bJUZbVVRY8WM8lTSa6y266Ji3ovze1ggfxNDDvezPzhpBLBteMcXHzDCCgqFSRcyhAcH5EZqwEmXHB2TGZjXI26qfkLMYtAKiyVDPyuPRv2hvco-9p5-gKdU_roH10GOjGU03roUW6SJTH3Yh8d4adDhO8_DBJe8VwTk6c3kW8-Klz8nK3rBerbP10_7C4XWcmL2WfCYCWA5eiEs4WThY6F9I6abmxzjnuTIuVhRKcatOZrVSVtYhWM2CIpuVzcjXNPYTufcDYN9tuCD6tbHKVMnMFOU8UmygTuhgDuuYQNnsdPhsGzfiy5s_LkiefPDGxY6Tfyf-bvgCHBGxu</recordid><startdate>20231001</startdate><enddate>20231001</enddate><creator>Konoplev, A. 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The tubes were profiled by confuser–diffuser constrictions of the flow section of the inner channel, which were formed by the deformation of their walls and placed along the length at a step that was constant and equal for all profiled tubes. The obtained results showed a dependence of the heat transfer enhancement in the tube channel on the Reynolds and Prandtl numbers, with the dependence on the latter being much stronger than that on the former, at least in cases where the heat carrier is water.</abstract><cop>Moscow</cop><pub>Pleiades Publishing</pub><doi>10.1134/S0040579523050433</doi><tpages>7</tpages></addata></record> |
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subjects | Chemistry Chemistry and Materials Science Design parameters Diffusers Heat transfer Industrial Chemistry/Chemical Engineering Thermal engineering Tube heat exchangers Tubes |
title | Enhancement of Heat Transfer in a Tube Channel of a Tubular Heat Exchanger |
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