Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems
The modeling equations for the temperature distribution and pure water productivity in a parallel-plate direct contact membrane distillation module under countercurrent-flow were derived theoretically with the use of the mass balance on each subchannel. The analytical solution is obtained by using t...
Gespeichert in:
| Veröffentlicht in: | Desalination and water treatment 2013-07, Vol.51 (25-27), p.5113-5120 |
|---|---|
| Hauptverfasser: | , , |
| Format: | Artikel |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | 5120 |
|---|---|
| container_issue | 25-27 |
| container_start_page | 5113 |
| container_title | Desalination and water treatment |
| container_volume | 51 |
| creator | Ho, Chii-Dong Yang, Tz-Jin Chuang, Yu-Chuan |
| description | The modeling equations for the temperature distribution and pure water productivity in a parallel-plate direct contact membrane distillation module under countercurrent-flow were derived theoretically with the use of the mass balance on each subchannel. The analytical solution is obtained by using the separated variables method with an orthogonal expansion technique extended in power series. The pure water productivity, average Nusselt number, and temperature distributions of both hot and cold feed streams are represented graphically with the feed velocity and the inlet saline temperature as parameters. The improvements of device performance were achieved under the countercurrent-flow operation. The influences of operation and design parameters on the pure water productivity are also discussed. |
| doi_str_mv | 10.1080/19443994.2013.768385 |
| format | Article |
| fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1778010347</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S1944398624188832</els_id><sourcerecordid>1778010347</sourcerecordid><originalsourceid>FETCH-LOGICAL-c402t-f2759069394ce903d34d10c4cbf87b43571f3a0e30af1a0400dcfe588e8d958e3</originalsourceid><addsrcrecordid>eNqFUcFq3DAQNaWBhk3-oAdfAr3sZmTJK-kSKCFtAwvpoTkLrTwCFVtKNNos-_eRcVJ6anUZ8eaN3ui9pvnMYMNAwTXTQnCtxaYDxjdyq7jqPzTnM7zmWm0__nX_1FwS_YZ6eiF70Z035Sdmn_Jko8M2TE85veCEsbTJty4dYsHsDjlXZO3HdGyHkNGV2orF1jrhtM82YsWphHG0JaTYhtgS2qOtw-2AZMcQlwadqOBEF82ZtyPh5VtdNY_f7n7d_ljvHr7f337drZ2Argp2stew1VwLhxr4wMXAwAm390ruBe8l89wCcrCeWRAAg_PYK4Vq0L1Cvmq-LO_Wbz0fkIqZAjmsa0ZMBzJMSgUMuJD_pwouZqJglSoWqsuJKKM3TzlMNp8MAzNHYt4jMXMkZomkjl29KVhydvTVNhfoz2wnt0xLPm9ys_CwOvMSMBtyAWs8i_VmSOHfQq9W86FX</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1434034741</pqid></control><display><type>article</type><title>Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems</title><source>Alma/SFX Local Collection</source><creator>Ho, Chii-Dong ; Yang, Tz-Jin ; Chuang, Yu-Chuan</creator><creatorcontrib>Ho, Chii-Dong ; Yang, Tz-Jin ; Chuang, Yu-Chuan</creatorcontrib><description>The modeling equations for the temperature distribution and pure water productivity in a parallel-plate direct contact membrane distillation module under countercurrent-flow were derived theoretically with the use of the mass balance on each subchannel. The analytical solution is obtained by using the separated variables method with an orthogonal expansion technique extended in power series. The pure water productivity, average Nusselt number, and temperature distributions of both hot and cold feed streams are represented graphically with the feed velocity and the inlet saline temperature as parameters. The improvements of device performance were achieved under the countercurrent-flow operation. The influences of operation and design parameters on the pure water productivity are also discussed.</description><identifier>ISSN: 1944-3986</identifier><identifier>ISSN: 1944-3994</identifier><identifier>EISSN: 1944-3986</identifier><identifier>DOI: 10.1080/19443994.2013.768385</identifier><language>eng</language><publisher>L'Aquila: Elsevier Inc</publisher><subject>Applied sciences ; Conjugated Graetz problems ; Contact ; Countercurrent ; Desalination ; Direct contact membrane distillation ; Distillation ; Drinking water and swimming-pool water. Desalination ; Exact sciences and technology ; Marine ; Mathematical analysis ; Mathematical models ; Nusselt number ; Performance enhancement ; Pollution ; Productivity ; Pure water productivity ; Temperature distribution ; Water treatment and pollution</subject><ispartof>Desalination and water treatment, 2013-07, Vol.51 (25-27), p.5113-5120</ispartof><rights>2013 Elsevier Inc.</rights><rights>2014 INIST-CNRS</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c402t-f2759069394ce903d34d10c4cbf87b43571f3a0e30af1a0400dcfe588e8d958e3</citedby><cites>FETCH-LOGICAL-c402t-f2759069394ce903d34d10c4cbf87b43571f3a0e30af1a0400dcfe588e8d958e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,780,784,789,790,23930,23931,25140,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=27619737$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Ho, Chii-Dong</creatorcontrib><creatorcontrib>Yang, Tz-Jin</creatorcontrib><creatorcontrib>Chuang, Yu-Chuan</creatorcontrib><title>Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems</title><title>Desalination and water treatment</title><description>The modeling equations for the temperature distribution and pure water productivity in a parallel-plate direct contact membrane distillation module under countercurrent-flow were derived theoretically with the use of the mass balance on each subchannel. The analytical solution is obtained by using the separated variables method with an orthogonal expansion technique extended in power series. The pure water productivity, average Nusselt number, and temperature distributions of both hot and cold feed streams are represented graphically with the feed velocity and the inlet saline temperature as parameters. The improvements of device performance were achieved under the countercurrent-flow operation. The influences of operation and design parameters on the pure water productivity are also discussed.</description><subject>Applied sciences</subject><subject>Conjugated Graetz problems</subject><subject>Contact</subject><subject>Countercurrent</subject><subject>Desalination</subject><subject>Direct contact membrane distillation</subject><subject>Distillation</subject><subject>Drinking water and swimming-pool water. Desalination</subject><subject>Exact sciences and technology</subject><subject>Marine</subject><subject>Mathematical analysis</subject><subject>Mathematical models</subject><subject>Nusselt number</subject><subject>Performance enhancement</subject><subject>Pollution</subject><subject>Productivity</subject><subject>Pure water productivity</subject><subject>Temperature distribution</subject><subject>Water treatment and pollution</subject><issn>1944-3986</issn><issn>1944-3994</issn><issn>1944-3986</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqFUcFq3DAQNaWBhk3-oAdfAr3sZmTJK-kSKCFtAwvpoTkLrTwCFVtKNNos-_eRcVJ6anUZ8eaN3ui9pvnMYMNAwTXTQnCtxaYDxjdyq7jqPzTnM7zmWm0__nX_1FwS_YZ6eiF70Z035Sdmn_Jko8M2TE85veCEsbTJty4dYsHsDjlXZO3HdGyHkNGV2orF1jrhtM82YsWphHG0JaTYhtgS2qOtw-2AZMcQlwadqOBEF82ZtyPh5VtdNY_f7n7d_ljvHr7f337drZ2Argp2stew1VwLhxr4wMXAwAm390ruBe8l89wCcrCeWRAAg_PYK4Vq0L1Cvmq-LO_Wbz0fkIqZAjmsa0ZMBzJMSgUMuJD_pwouZqJglSoWqsuJKKM3TzlMNp8MAzNHYt4jMXMkZomkjl29KVhydvTVNhfoz2wnt0xLPm9ys_CwOvMSMBtyAWs8i_VmSOHfQq9W86FX</recordid><startdate>20130701</startdate><enddate>20130701</enddate><creator>Ho, Chii-Dong</creator><creator>Yang, Tz-Jin</creator><creator>Chuang, Yu-Chuan</creator><general>Elsevier Inc</general><general>Desalination Publications</general><scope>6I.</scope><scope>AAFTH</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7ST</scope><scope>7TN</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope><scope>SOI</scope><scope>7SU</scope><scope>8FD</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>20130701</creationdate><title>Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems</title><author>Ho, Chii-Dong ; Yang, Tz-Jin ; Chuang, Yu-Chuan</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c402t-f2759069394ce903d34d10c4cbf87b43571f3a0e30af1a0400dcfe588e8d958e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Applied sciences</topic><topic>Conjugated Graetz problems</topic><topic>Contact</topic><topic>Countercurrent</topic><topic>Desalination</topic><topic>Direct contact membrane distillation</topic><topic>Distillation</topic><topic>Drinking water and swimming-pool water. Desalination</topic><topic>Exact sciences and technology</topic><topic>Marine</topic><topic>Mathematical analysis</topic><topic>Mathematical models</topic><topic>Nusselt number</topic><topic>Performance enhancement</topic><topic>Pollution</topic><topic>Productivity</topic><topic>Pure water productivity</topic><topic>Temperature distribution</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ho, Chii-Dong</creatorcontrib><creatorcontrib>Yang, Tz-Jin</creatorcontrib><creatorcontrib>Chuang, Yu-Chuan</creatorcontrib><collection>ScienceDirect Open Access Titles</collection><collection>Elsevier:ScienceDirect:Open Access</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Environment Abstracts</collection><collection>Oceanic Abstracts</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>Environment Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Desalination and water treatment</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ho, Chii-Dong</au><au>Yang, Tz-Jin</au><au>Chuang, Yu-Chuan</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems</atitle><jtitle>Desalination and water treatment</jtitle><date>2013-07-01</date><risdate>2013</risdate><volume>51</volume><issue>25-27</issue><spage>5113</spage><epage>5120</epage><pages>5113-5120</pages><issn>1944-3986</issn><issn>1944-3994</issn><eissn>1944-3986</eissn><abstract>The modeling equations for the temperature distribution and pure water productivity in a parallel-plate direct contact membrane distillation module under countercurrent-flow were derived theoretically with the use of the mass balance on each subchannel. The analytical solution is obtained by using the separated variables method with an orthogonal expansion technique extended in power series. The pure water productivity, average Nusselt number, and temperature distributions of both hot and cold feed streams are represented graphically with the feed velocity and the inlet saline temperature as parameters. The improvements of device performance were achieved under the countercurrent-flow operation. The influences of operation and design parameters on the pure water productivity are also discussed.</abstract><cop>L'Aquila</cop><pub>Elsevier Inc</pub><doi>10.1080/19443994.2013.768385</doi><tpages>8</tpages><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 1944-3986 |
| ispartof | Desalination and water treatment, 2013-07, Vol.51 (25-27), p.5113-5120 |
| issn | 1944-3986 1944-3994 1944-3986 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_1778010347 |
| source | Alma/SFX Local Collection |
| subjects | Applied sciences Conjugated Graetz problems Contact Countercurrent Desalination Direct contact membrane distillation Distillation Drinking water and swimming-pool water. Desalination Exact sciences and technology Marine Mathematical analysis Mathematical models Nusselt number Performance enhancement Pollution Productivity Pure water productivity Temperature distribution Water treatment and pollution |
| title | Performance improvement of countercurrent-flow direct contact membrane distillation in seawater desalination systems |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-26T12%3A00%3A23IST&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=Performance%20improvement%20of%20countercurrent-flow%20direct%20contact%20membrane%20distillation%20in%20seawater%20desalination%20systems&rft.jtitle=Desalination%20and%20water%20treatment&rft.au=Ho,%20Chii-Dong&rft.date=2013-07-01&rft.volume=51&rft.issue=25-27&rft.spage=5113&rft.epage=5120&rft.pages=5113-5120&rft.issn=1944-3986&rft.eissn=1944-3986&rft_id=info:doi/10.1080/19443994.2013.768385&rft_dat=%3Cproquest_cross%3E1778010347%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=1434034741&rft_id=info:pmid/&rft_els_id=S1944398624188832&rfr_iscdi=true |