An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube
In this paper, flow patterns and their transitions for refrigerant R134a boiling in a microfinned helically coiled tube are experimentally observed and analyzed. All the flow patterns occurred in the test can be divided into three dominant regimes, i.e., stratified-wavy flow, intermittent flow and a...
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Veröffentlicht in: | International journal of heat and mass transfer 2008, Vol.51 (1), p.169-175 |
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creator | Cui, Wenzhi Li, Longjian Xin, Mingdao Jen, Tien-Chien Liao, Quan Chen, Qinghua |
description | In this paper, flow patterns and their transitions for refrigerant R134a boiling in a microfinned helically coiled tube are experimentally observed and analyzed. All the flow patterns occurred in the test can be divided into three dominant regimes, i.e., stratified-wavy flow, intermittent flow and annular flow. Experimental data are plotted in two kinds of flow maps, i.e., Taitel and Dukler flow map and mass flux versus vapor quality flow map. The transitions between various flow regimes and the differences from that in smooth straight tube have also been discussed. Martinelli parameter can be used to indicate the transition from intermittent flow to annular flow. The transition from stratified-wavy flow to annular or intermittent flow is identified in the vapor quality versus mass flux flow map. The flow regime is always in stratified-wavy flow for a mass flux less than 100
kg/m
2
s.
The two-phase frictional pressure drop characteristics in the test tube are also experimentally studied. The two-phase frictional multiplier data can be well correlated by Lockhart–Martinelli parameter. Considering the corresponding flow regimes, i.e., stratified and annular flow, two frictional pressure drop correlations are proposed, and show a good agreement with the respective experimental data. |
doi_str_mv | 10.1016/j.ijheatmasstransfer.2007.04.014 |
format | Article |
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kg/m
2
s.
The two-phase frictional pressure drop characteristics in the test tube are also experimentally studied. The two-phase frictional multiplier data can be well correlated by Lockhart–Martinelli parameter. Considering the corresponding flow regimes, i.e., stratified and annular flow, two frictional pressure drop correlations are proposed, and show a good agreement with the respective experimental data.</description><identifier>ISSN: 0017-9310</identifier><identifier>EISSN: 1879-2189</identifier><identifier>DOI: 10.1016/j.ijheatmasstransfer.2007.04.014</identifier><identifier>CODEN: IJHMAK</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Energy ; Energy. Thermal use of fuels ; Exact sciences and technology ; Flow boiling ; Flow pattern ; Helically coiled tube ; Microfin tube ; Pressure drop ; Refrigerants ; Refrigerating engineering ; Refrigerating engineering. Cryogenics. Food conservation</subject><ispartof>International journal of heat and mass transfer, 2008, Vol.51 (1), p.169-175</ispartof><rights>2007 Elsevier Ltd</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c469t-fba308da21ae0df53bfdb140d1ff726f68cd656334c043bc664d0e8c4e295f903</citedby><cites>FETCH-LOGICAL-c469t-fba308da21ae0df53bfdb140d1ff726f68cd656334c043bc664d0e8c4e295f903</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0017931007003237$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,4010,27900,27901,27902,65534</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=19987891$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Cui, Wenzhi</creatorcontrib><creatorcontrib>Li, Longjian</creatorcontrib><creatorcontrib>Xin, Mingdao</creatorcontrib><creatorcontrib>Jen, Tien-Chien</creatorcontrib><creatorcontrib>Liao, Quan</creatorcontrib><creatorcontrib>Chen, Qinghua</creatorcontrib><title>An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube</title><title>International journal of heat and mass transfer</title><description>In this paper, flow patterns and their transitions for refrigerant R134a boiling in a microfinned helically coiled tube are experimentally observed and analyzed. All the flow patterns occurred in the test can be divided into three dominant regimes, i.e., stratified-wavy flow, intermittent flow and annular flow. Experimental data are plotted in two kinds of flow maps, i.e., Taitel and Dukler flow map and mass flux versus vapor quality flow map. The transitions between various flow regimes and the differences from that in smooth straight tube have also been discussed. Martinelli parameter can be used to indicate the transition from intermittent flow to annular flow. The transition from stratified-wavy flow to annular or intermittent flow is identified in the vapor quality versus mass flux flow map. The flow regime is always in stratified-wavy flow for a mass flux less than 100
kg/m
2
s.
The two-phase frictional pressure drop characteristics in the test tube are also experimentally studied. The two-phase frictional multiplier data can be well correlated by Lockhart–Martinelli parameter. Considering the corresponding flow regimes, i.e., stratified and annular flow, two frictional pressure drop correlations are proposed, and show a good agreement with the respective experimental data.</description><subject>Applied sciences</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Exact sciences and technology</subject><subject>Flow boiling</subject><subject>Flow pattern</subject><subject>Helically coiled tube</subject><subject>Microfin tube</subject><subject>Pressure drop</subject><subject>Refrigerants</subject><subject>Refrigerating engineering</subject><subject>Refrigerating engineering. Cryogenics. Food conservation</subject><issn>0017-9310</issn><issn>1879-2189</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNqNkE2PFCEQhonRxHH1P3DReOm26Gbo5uZm4_qRTbzomdBQuEwY6AVanX8vk9nEgxdPlao8eavqIeQtg54BE-8OvT_co65HXUrNOhaHuR8Aph54D4w_ITs2T7Ib2Cyfkh0Amzo5MnhOXpRyOLfAxY48XEeKv1fM_oix6kBL3eyJJkddSL_oqmvFHKmOlq4ZS9kyUpvTSl3KF2RJPvj4g_pYvEV69CYn52NES-8xeKNDOFHToDao24IvyTOnQ8FXj_WKfL_98O3mU3f39ePnm-u7znAha-cWPcJs9cA0gnX7cXF2YRwsc24ahBOzsWIvxpEb4ONihOAWcDYcB7l3EsYr8uaSu-b0sGGp6uiLwRB0xLQVNbKZD0yIBr6_gO3wUjI6tTYbOp8UA3V2rQ7qX9fq7FoBV811i3j9uEuX9rBrjPHlb46U8zRL1rgvFw7b4z99SynGYzRofUZTlU3-_5f-AfKCpLA</recordid><startdate>2008</startdate><enddate>2008</enddate><creator>Cui, Wenzhi</creator><creator>Li, Longjian</creator><creator>Xin, Mingdao</creator><creator>Jen, Tien-Chien</creator><creator>Liao, Quan</creator><creator>Chen, Qinghua</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>2008</creationdate><title>An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube</title><author>Cui, Wenzhi ; Li, Longjian ; Xin, Mingdao ; Jen, Tien-Chien ; Liao, Quan ; Chen, Qinghua</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c469t-fba308da21ae0df53bfdb140d1ff726f68cd656334c043bc664d0e8c4e295f903</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Applied sciences</topic><topic>Energy</topic><topic>Energy. Thermal use of fuels</topic><topic>Exact sciences and technology</topic><topic>Flow boiling</topic><topic>Flow pattern</topic><topic>Helically coiled tube</topic><topic>Microfin tube</topic><topic>Pressure drop</topic><topic>Refrigerants</topic><topic>Refrigerating engineering</topic><topic>Refrigerating engineering. Cryogenics. Food conservation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Cui, Wenzhi</creatorcontrib><creatorcontrib>Li, Longjian</creatorcontrib><creatorcontrib>Xin, Mingdao</creatorcontrib><creatorcontrib>Jen, Tien-Chien</creatorcontrib><creatorcontrib>Liao, Quan</creatorcontrib><creatorcontrib>Chen, Qinghua</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering 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>International journal of heat and mass transfer</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Cui, Wenzhi</au><au>Li, Longjian</au><au>Xin, Mingdao</au><au>Jen, Tien-Chien</au><au>Liao, Quan</au><au>Chen, Qinghua</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube</atitle><jtitle>International journal of heat and mass transfer</jtitle><date>2008</date><risdate>2008</risdate><volume>51</volume><issue>1</issue><spage>169</spage><epage>175</epage><pages>169-175</pages><issn>0017-9310</issn><eissn>1879-2189</eissn><coden>IJHMAK</coden><abstract>In this paper, flow patterns and their transitions for refrigerant R134a boiling in a microfinned helically coiled tube are experimentally observed and analyzed. All the flow patterns occurred in the test can be divided into three dominant regimes, i.e., stratified-wavy flow, intermittent flow and annular flow. Experimental data are plotted in two kinds of flow maps, i.e., Taitel and Dukler flow map and mass flux versus vapor quality flow map. The transitions between various flow regimes and the differences from that in smooth straight tube have also been discussed. Martinelli parameter can be used to indicate the transition from intermittent flow to annular flow. The transition from stratified-wavy flow to annular or intermittent flow is identified in the vapor quality versus mass flux flow map. The flow regime is always in stratified-wavy flow for a mass flux less than 100
kg/m
2
s.
The two-phase frictional pressure drop characteristics in the test tube are also experimentally studied. The two-phase frictional multiplier data can be well correlated by Lockhart–Martinelli parameter. Considering the corresponding flow regimes, i.e., stratified and annular flow, two frictional pressure drop correlations are proposed, and show a good agreement with the respective experimental data.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijheatmasstransfer.2007.04.014</doi><tpages>7</tpages></addata></record> |
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subjects | Applied sciences Energy Energy. Thermal use of fuels Exact sciences and technology Flow boiling Flow pattern Helically coiled tube Microfin tube Pressure drop Refrigerants Refrigerating engineering Refrigerating engineering. Cryogenics. Food conservation |
title | An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube |
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