Study on gas–liquid phase mass transfer coefficient of entrained flow reactor
The gas–liquid phase mass transfer coefficient of entrained flow reactor is studied in the paper. The liquid solvent is atomized into the entrained flow reactor after going through a type of pressure nozzle used in the experiment. The isometric decompression technique is used to investigate the mass...
Gespeichert in:
Veröffentlicht in: | Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2008-07, Vol.141 (1), p.278-283 |
---|---|
Hauptverfasser: | , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 283 |
---|---|
container_issue | 1 |
container_start_page | 278 |
container_title | Chemical engineering journal (Lausanne, Switzerland : 1996) |
container_volume | 141 |
creator | Hu, Lishun Wang, Xinjun Yu, Guangsuo Wang, Fuchen Yu, Zunhong |
description | The gas–liquid phase mass transfer coefficient of entrained flow reactor is studied in the paper. The liquid solvent is atomized into the entrained flow reactor after going through a type of pressure nozzle used in the experiment. The isometric decompression technique is used to investigate the mass transfer coefficient of the entrained flow reactor in seven different gas–liquid systems. The effect on mass transfer coefficient of
Re and
We number of droplet is sufficiently discussed. A mass transfer coefficient correlation model is proposed and the parameters in the model are obtained by nonlinear regression method. The residual shows that the model values are in good agreement with the experiment values. |
doi_str_mv | 10.1016/j.cej.2007.12.032 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_14022202</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S1385894708000107</els_id><sourcerecordid>14022202</sourcerecordid><originalsourceid>FETCH-LOGICAL-c358t-55492f90adc7594eac11a1fcbfedc43a7c286ec927a4d7e2dd9cdfeb27776fa83</originalsourceid><addsrcrecordid>eNp9kLtOAzEQRVcIJCDwAXRuoNvFnn14V1QI8ZIipQBqy4zH4GizDvYGRMc_8Id8CY4SUVLNFOfe0ZwsOxG8EFw05_MCaV4A57IQUPASdrID0coyL0HAbtrLts7brpL72WGMc85504nuIJs9jCvzyfzAXnT8-fru3dvKGbZ81ZHYQsfIxqCHaCkw9GStQ0fDyLxlaQTtBjLM9v6DBdI4-nCU7VndRzrezkn2dHP9eHWXT2e391eX0xzLuh3zuq46sB3XBmXdVSkrhBYWny0ZrEotEdqGsAOpKyMJjOnQWHoGKWVjdVtOsrNN7zL4txXFUS1cROp7PZBfRSUqDgAcEig2IAYfYyCrlsEtdPhUgqu1OjVXSZ1aq1MCVFKXMqfbch1R9zYZQBf_gsCrpqlhzV1sOEqfvjsKKq71IBkXCEdlvPvnyi-yVIYw</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>14022202</pqid></control><display><type>article</type><title>Study on gas–liquid phase mass transfer coefficient of entrained flow reactor</title><source>Elsevier ScienceDirect Journals</source><creator>Hu, Lishun ; Wang, Xinjun ; Yu, Guangsuo ; Wang, Fuchen ; Yu, Zunhong</creator><creatorcontrib>Hu, Lishun ; Wang, Xinjun ; Yu, Guangsuo ; Wang, Fuchen ; Yu, Zunhong</creatorcontrib><description>The gas–liquid phase mass transfer coefficient of entrained flow reactor is studied in the paper. The liquid solvent is atomized into the entrained flow reactor after going through a type of pressure nozzle used in the experiment. The isometric decompression technique is used to investigate the mass transfer coefficient of the entrained flow reactor in seven different gas–liquid systems. The effect on mass transfer coefficient of
Re and
We number of droplet is sufficiently discussed. A mass transfer coefficient correlation model is proposed and the parameters in the model are obtained by nonlinear regression method. The residual shows that the model values are in good agreement with the experiment values.</description><identifier>ISSN: 1385-8947</identifier><identifier>EISSN: 1873-3212</identifier><identifier>DOI: 10.1016/j.cej.2007.12.032</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Atomization ; Chemical engineering ; Entrained flow reactor ; Exact sciences and technology ; Gas–Liquid phase mass transfer coefficient ; Heat and mass transfer. Packings, plates ; Pressure type nozzle ; Reactors</subject><ispartof>Chemical engineering journal (Lausanne, Switzerland : 1996), 2008-07, Vol.141 (1), p.278-283</ispartof><rights>2008 Elsevier B.V.</rights><rights>2008 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c358t-55492f90adc7594eac11a1fcbfedc43a7c286ec927a4d7e2dd9cdfeb27776fa83</citedby><cites>FETCH-LOGICAL-c358t-55492f90adc7594eac11a1fcbfedc43a7c286ec927a4d7e2dd9cdfeb27776fa83</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S1385894708000107$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65534</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=20466522$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Hu, Lishun</creatorcontrib><creatorcontrib>Wang, Xinjun</creatorcontrib><creatorcontrib>Yu, Guangsuo</creatorcontrib><creatorcontrib>Wang, Fuchen</creatorcontrib><creatorcontrib>Yu, Zunhong</creatorcontrib><title>Study on gas–liquid phase mass transfer coefficient of entrained flow reactor</title><title>Chemical engineering journal (Lausanne, Switzerland : 1996)</title><description>The gas–liquid phase mass transfer coefficient of entrained flow reactor is studied in the paper. The liquid solvent is atomized into the entrained flow reactor after going through a type of pressure nozzle used in the experiment. The isometric decompression technique is used to investigate the mass transfer coefficient of the entrained flow reactor in seven different gas–liquid systems. The effect on mass transfer coefficient of
Re and
We number of droplet is sufficiently discussed. A mass transfer coefficient correlation model is proposed and the parameters in the model are obtained by nonlinear regression method. The residual shows that the model values are in good agreement with the experiment values.</description><subject>Applied sciences</subject><subject>Atomization</subject><subject>Chemical engineering</subject><subject>Entrained flow reactor</subject><subject>Exact sciences and technology</subject><subject>Gas–Liquid phase mass transfer coefficient</subject><subject>Heat and mass transfer. Packings, plates</subject><subject>Pressure type nozzle</subject><subject>Reactors</subject><issn>1385-8947</issn><issn>1873-3212</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNp9kLtOAzEQRVcIJCDwAXRuoNvFnn14V1QI8ZIipQBqy4zH4GizDvYGRMc_8Id8CY4SUVLNFOfe0ZwsOxG8EFw05_MCaV4A57IQUPASdrID0coyL0HAbtrLts7brpL72WGMc85504nuIJs9jCvzyfzAXnT8-fru3dvKGbZ81ZHYQsfIxqCHaCkw9GStQ0fDyLxlaQTtBjLM9v6DBdI4-nCU7VndRzrezkn2dHP9eHWXT2e391eX0xzLuh3zuq46sB3XBmXdVSkrhBYWny0ZrEotEdqGsAOpKyMJjOnQWHoGKWVjdVtOsrNN7zL4txXFUS1cROp7PZBfRSUqDgAcEig2IAYfYyCrlsEtdPhUgqu1OjVXSZ1aq1MCVFKXMqfbch1R9zYZQBf_gsCrpqlhzV1sOEqfvjsKKq71IBkXCEdlvPvnyi-yVIYw</recordid><startdate>20080715</startdate><enddate>20080715</enddate><creator>Hu, Lishun</creator><creator>Wang, Xinjun</creator><creator>Yu, Guangsuo</creator><creator>Wang, Fuchen</creator><creator>Yu, Zunhong</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope></search><sort><creationdate>20080715</creationdate><title>Study on gas–liquid phase mass transfer coefficient of entrained flow reactor</title><author>Hu, Lishun ; Wang, Xinjun ; Yu, Guangsuo ; Wang, Fuchen ; Yu, Zunhong</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-55492f90adc7594eac11a1fcbfedc43a7c286ec927a4d7e2dd9cdfeb27776fa83</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>Applied sciences</topic><topic>Atomization</topic><topic>Chemical engineering</topic><topic>Entrained flow reactor</topic><topic>Exact sciences and technology</topic><topic>Gas–Liquid phase mass transfer coefficient</topic><topic>Heat and mass transfer. Packings, plates</topic><topic>Pressure type nozzle</topic><topic>Reactors</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Hu, Lishun</creatorcontrib><creatorcontrib>Wang, Xinjun</creatorcontrib><creatorcontrib>Yu, Guangsuo</creatorcontrib><creatorcontrib>Wang, Fuchen</creatorcontrib><creatorcontrib>Yu, Zunhong</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Hu, Lishun</au><au>Wang, Xinjun</au><au>Yu, Guangsuo</au><au>Wang, Fuchen</au><au>Yu, Zunhong</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Study on gas–liquid phase mass transfer coefficient of entrained flow reactor</atitle><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle><date>2008-07-15</date><risdate>2008</risdate><volume>141</volume><issue>1</issue><spage>278</spage><epage>283</epage><pages>278-283</pages><issn>1385-8947</issn><eissn>1873-3212</eissn><abstract>The gas–liquid phase mass transfer coefficient of entrained flow reactor is studied in the paper. The liquid solvent is atomized into the entrained flow reactor after going through a type of pressure nozzle used in the experiment. The isometric decompression technique is used to investigate the mass transfer coefficient of the entrained flow reactor in seven different gas–liquid systems. The effect on mass transfer coefficient of
Re and
We number of droplet is sufficiently discussed. A mass transfer coefficient correlation model is proposed and the parameters in the model are obtained by nonlinear regression method. The residual shows that the model values are in good agreement with the experiment values.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.cej.2007.12.032</doi><tpages>6</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 1385-8947 |
ispartof | Chemical engineering journal (Lausanne, Switzerland : 1996), 2008-07, Vol.141 (1), p.278-283 |
issn | 1385-8947 1873-3212 |
language | eng |
recordid | cdi_proquest_miscellaneous_14022202 |
source | Elsevier ScienceDirect Journals |
subjects | Applied sciences Atomization Chemical engineering Entrained flow reactor Exact sciences and technology Gas–Liquid phase mass transfer coefficient Heat and mass transfer. Packings, plates Pressure type nozzle Reactors |
title | Study on gas–liquid phase mass transfer coefficient of entrained flow reactor |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-15T02%3A57%3A35IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Study%20on%20gas%E2%80%93liquid%20phase%20mass%20transfer%20coefficient%20of%20entrained%20flow%20reactor&rft.jtitle=Chemical%20engineering%20journal%20(Lausanne,%20Switzerland%20:%201996)&rft.au=Hu,%20Lishun&rft.date=2008-07-15&rft.volume=141&rft.issue=1&rft.spage=278&rft.epage=283&rft.pages=278-283&rft.issn=1385-8947&rft.eissn=1873-3212&rft_id=info:doi/10.1016/j.cej.2007.12.032&rft_dat=%3Cproquest_cross%3E14022202%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=14022202&rft_id=info:pmid/&rft_els_id=S1385894708000107&rfr_iscdi=true |