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Phase split in parallel vertical channels in presence of a variable depth protrusion header
•Experimental study of air–water phase distribution in parallel vertical channels.•Comparison between different protrusion configurations and reference (no fitting).•Minimum protrusion depth (0.5D) useful for improving the phase.•Best distribution figure of merits measured with variable depth protru...
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Published in: | Experimental thermal and fluid science 2016-06, Vol.74, p.257-264 |
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creator | Marchitto, Annalisa Fossa, Marco Guglielmini, Giovanni |
description | •Experimental study of air–water phase distribution in parallel vertical channels.•Comparison between different protrusion configurations and reference (no fitting).•Minimum protrusion depth (0.5D) useful for improving the phase.•Best distribution figure of merits measured with variable depth protrusions.
The air and water flow distribution are experimentally studied in a test section simulating a heat exchanger composed by a round header and 16 parallel upward channels. The effects of the tube protrusion depth as well as the gas and liquid superficial velocities are investigated and the results are compared with previous data. A new fitting solution to be inserted in the header has been developed based on previous findings by the Authors. The fitting geometry belongs to the family of the protruding pipes but the protruding depth has been varied along the header in order to cope with expected liquid and gas mass flow rates in the parallel channels. The flow at the header inlet is intermittent and annular and water and air have been employed as two phase mixture. The new header fitting demonstrated to yield meaningful improvements in phase distribution in terms of either dimensionless liquid and gas flow ratios or standard deviation of phase flow ratio (the overall performance parameter STD2 here presented decreased by 64%) when compared to the previous configurations. |
doi_str_mv | 10.1016/j.expthermflusci.2015.12.017 |
format | article |
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The air and water flow distribution are experimentally studied in a test section simulating a heat exchanger composed by a round header and 16 parallel upward channels. The effects of the tube protrusion depth as well as the gas and liquid superficial velocities are investigated and the results are compared with previous data. A new fitting solution to be inserted in the header has been developed based on previous findings by the Authors. The fitting geometry belongs to the family of the protruding pipes but the protruding depth has been varied along the header in order to cope with expected liquid and gas mass flow rates in the parallel channels. The flow at the header inlet is intermittent and annular and water and air have been employed as two phase mixture. The new header fitting demonstrated to yield meaningful improvements in phase distribution in terms of either dimensionless liquid and gas flow ratios or standard deviation of phase flow ratio (the overall performance parameter STD2 here presented decreased by 64%) when compared to the previous configurations.</description><identifier>ISSN: 0894-1777</identifier><identifier>EISSN: 1879-2286</identifier><identifier>DOI: 10.1016/j.expthermflusci.2015.12.017</identifier><language>eng</language><publisher>Elsevier Inc</publisher><subject>Air–water mixture ; Channels ; Fittings ; Flow distribution ; Fluid flow ; Flute fitting ; Headers ; Heat exchangers ; Liquids ; Parallel channels ; Plate heat exchangers ; Standard deviation ; Water flow</subject><ispartof>Experimental thermal and fluid science, 2016-06, Vol.74, p.257-264</ispartof><rights>2016 Elsevier Inc.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c396t-3b18f44d7d878a8de4292215a9c29a1bd94d573385dbdef1d6b6d714a84dc3f13</citedby><cites>FETCH-LOGICAL-c396t-3b18f44d7d878a8de4292215a9c29a1bd94d573385dbdef1d6b6d714a84dc3f13</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>Marchitto, Annalisa</creatorcontrib><creatorcontrib>Fossa, Marco</creatorcontrib><creatorcontrib>Guglielmini, Giovanni</creatorcontrib><title>Phase split in parallel vertical channels in presence of a variable depth protrusion header</title><title>Experimental thermal and fluid science</title><description>•Experimental study of air–water phase distribution in parallel vertical channels.•Comparison between different protrusion configurations and reference (no fitting).•Minimum protrusion depth (0.5D) useful for improving the phase.•Best distribution figure of merits measured with variable depth protrusions.
The air and water flow distribution are experimentally studied in a test section simulating a heat exchanger composed by a round header and 16 parallel upward channels. The effects of the tube protrusion depth as well as the gas and liquid superficial velocities are investigated and the results are compared with previous data. A new fitting solution to be inserted in the header has been developed based on previous findings by the Authors. The fitting geometry belongs to the family of the protruding pipes but the protruding depth has been varied along the header in order to cope with expected liquid and gas mass flow rates in the parallel channels. The flow at the header inlet is intermittent and annular and water and air have been employed as two phase mixture. The new header fitting demonstrated to yield meaningful improvements in phase distribution in terms of either dimensionless liquid and gas flow ratios or standard deviation of phase flow ratio (the overall performance parameter STD2 here presented decreased by 64%) when compared to the previous configurations.</description><subject>Air–water mixture</subject><subject>Channels</subject><subject>Fittings</subject><subject>Flow distribution</subject><subject>Fluid flow</subject><subject>Flute fitting</subject><subject>Headers</subject><subject>Heat exchangers</subject><subject>Liquids</subject><subject>Parallel channels</subject><subject>Plate heat exchangers</subject><subject>Standard deviation</subject><subject>Water flow</subject><issn>0894-1777</issn><issn>1879-2286</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNqNkD1PwzAURS0EEqXwHzwwsCT4OR92JBZUUUCqBANMDJZjvyiu3CTYaQX_npSysHV6wz336ukQcg0sBQbl7TrFr2FsMWwav43GpZxBkQJPGYgTMgMpqoRzWZ6SGZNVnoAQ4pxcxLhmjEkObEY-XlsdkcbBu5G6jg46aO_R0x2G0RntqWl116GPv2nAiJ1B2jdU050OTtceqcXpiynsx7CNru9oi9piuCRnjfYRr_7unLwvH94WT8nq5fF5cb9KTFaVY5LVIJs8t8JKIbW0mPOKcyh0ZXilobZVbguRZbKwtcUGbFmXVkCuZW5N1kA2JzeH3emDzy3GUW1cNOi97rDfRgWSF7koRCWOQJkUe2XZhN4dUBP6GAM2aghuo8O3Aqb2-tVa_dev9voVcDXpn-rLQ31ShzuHQU3E3p11Ac2obO-OG_oBGBKYYg</recordid><startdate>201606</startdate><enddate>201606</enddate><creator>Marchitto, Annalisa</creator><creator>Fossa, Marco</creator><creator>Guglielmini, Giovanni</creator><general>Elsevier Inc</general><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>201606</creationdate><title>Phase split in parallel vertical channels in presence of a variable depth protrusion header</title><author>Marchitto, Annalisa ; Fossa, Marco ; Guglielmini, Giovanni</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c396t-3b18f44d7d878a8de4292215a9c29a1bd94d573385dbdef1d6b6d714a84dc3f13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><topic>Air–water mixture</topic><topic>Channels</topic><topic>Fittings</topic><topic>Flow distribution</topic><topic>Fluid flow</topic><topic>Flute fitting</topic><topic>Headers</topic><topic>Heat exchangers</topic><topic>Liquids</topic><topic>Parallel channels</topic><topic>Plate heat exchangers</topic><topic>Standard deviation</topic><topic>Water flow</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Marchitto, Annalisa</creatorcontrib><creatorcontrib>Fossa, Marco</creatorcontrib><creatorcontrib>Guglielmini, Giovanni</creatorcontrib><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>Marchitto, Annalisa</au><au>Fossa, Marco</au><au>Guglielmini, Giovanni</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Phase split in parallel vertical channels in presence of a variable depth protrusion header</atitle><jtitle>Experimental thermal and fluid science</jtitle><date>2016-06</date><risdate>2016</risdate><volume>74</volume><spage>257</spage><epage>264</epage><pages>257-264</pages><issn>0894-1777</issn><eissn>1879-2286</eissn><abstract>•Experimental study of air–water phase distribution in parallel vertical channels.•Comparison between different protrusion configurations and reference (no fitting).•Minimum protrusion depth (0.5D) useful for improving the phase.•Best distribution figure of merits measured with variable depth protrusions.
The air and water flow distribution are experimentally studied in a test section simulating a heat exchanger composed by a round header and 16 parallel upward channels. The effects of the tube protrusion depth as well as the gas and liquid superficial velocities are investigated and the results are compared with previous data. A new fitting solution to be inserted in the header has been developed based on previous findings by the Authors. The fitting geometry belongs to the family of the protruding pipes but the protruding depth has been varied along the header in order to cope with expected liquid and gas mass flow rates in the parallel channels. The flow at the header inlet is intermittent and annular and water and air have been employed as two phase mixture. The new header fitting demonstrated to yield meaningful improvements in phase distribution in terms of either dimensionless liquid and gas flow ratios or standard deviation of phase flow ratio (the overall performance parameter STD2 here presented decreased by 64%) when compared to the previous configurations.</abstract><pub>Elsevier Inc</pub><doi>10.1016/j.expthermflusci.2015.12.017</doi><tpages>8</tpages></addata></record> |
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language | eng |
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source | ScienceDirect Journals |
subjects | Air–water mixture Channels Fittings Flow distribution Fluid flow Flute fitting Headers Heat exchangers Liquids Parallel channels Plate heat exchangers Standard deviation Water flow |
title | Phase split in parallel vertical channels in presence of a variable depth protrusion header |
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