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Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran
Design and control of an extractive distillation system for tetrahydrofuran (THF) dehydration with ethylene glycol as entrainer is investigated. The main module is a two‐column system containing an extractive distillation column, whose top stream is the desired product THF, and an entrainer recovery...
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Published in: | Chemical engineering & technology 2013-05, Vol.36 (5), p.829-839 |
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description | Design and control of an extractive distillation system for tetrahydrofuran (THF) dehydration with ethylene glycol as entrainer is investigated. The main module is a two‐column system containing an extractive distillation column, whose top stream is the desired product THF, and an entrainer recovery column. Economic analysis with total annual cost as the objective function is developed. Two kinds of control strategies are explored for THF dehydration. The responses reveal that the control structure with fixed reflux ratio cannot maintain the bottom liquid level of the entrainer recovery column, while the control scheme with fixed reboiler heat duty/feed flow ratio exhibits good control performance in spite of large deviations in feed flow rate and feed composition.
THF dehydration is a process of economical concern, as the THF demand is increasing. A steady‐state design of two‐column extractive distillation for tetrahydrofuran‐H2O separation is introduced, and optimal conditions are evaluated by minimizing the total annual costs. Both a basic and an improved control strategy are devised. |
doi_str_mv | 10.1002/ceat.201200611 |
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THF dehydration is a process of economical concern, as the THF demand is increasing. A steady‐state design of two‐column extractive distillation for tetrahydrofuran‐H2O separation is introduced, and optimal conditions are evaluated by minimizing the total annual costs. Both a basic and an improved control strategy are devised.</description><identifier>ISSN: 0930-7516</identifier><identifier>EISSN: 1521-4125</identifier><identifier>DOI: 10.1002/ceat.201200611</identifier><language>eng</language><publisher>Weinheim: WILEY-VCH Verlag</publisher><subject>Columns (structural) ; Control strategies ; Cost engineering ; Dehydration ; Design engineering ; Distillation ; Entrainment ; Extractive distillation ; Recovery ; Strategy ; Tetrahydrofuran dehydration</subject><ispartof>Chemical engineering & technology, 2013-05, Vol.36 (5), p.829-839</ispartof><rights>Copyright © 2013 WILEY‐VCH Verlag GmbH & Co. KGaA, Weinheim</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3</citedby><cites>FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3</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>Fan, Z.</creatorcontrib><creatorcontrib>Zhang, X.</creatorcontrib><creatorcontrib>Cai, W.</creatorcontrib><creatorcontrib>Wang, F.</creatorcontrib><title>Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran</title><title>Chemical engineering & technology</title><addtitle>Chem. Eng. Technol</addtitle><description>Design and control of an extractive distillation system for tetrahydrofuran (THF) dehydration with ethylene glycol as entrainer is investigated. The main module is a two‐column system containing an extractive distillation column, whose top stream is the desired product THF, and an entrainer recovery column. Economic analysis with total annual cost as the objective function is developed. Two kinds of control strategies are explored for THF dehydration. The responses reveal that the control structure with fixed reflux ratio cannot maintain the bottom liquid level of the entrainer recovery column, while the control scheme with fixed reboiler heat duty/feed flow ratio exhibits good control performance in spite of large deviations in feed flow rate and feed composition.
THF dehydration is a process of economical concern, as the THF demand is increasing. A steady‐state design of two‐column extractive distillation for tetrahydrofuran‐H2O separation is introduced, and optimal conditions are evaluated by minimizing the total annual costs. Both a basic and an improved control strategy are devised.</description><subject>Columns (structural)</subject><subject>Control strategies</subject><subject>Cost engineering</subject><subject>Dehydration</subject><subject>Design engineering</subject><subject>Distillation</subject><subject>Entrainment</subject><subject>Extractive distillation</subject><subject>Recovery</subject><subject>Strategy</subject><subject>Tetrahydrofuran dehydration</subject><issn>0930-7516</issn><issn>1521-4125</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqFkMFP2zAUh61pSHTAlXOOXFLes504PlZpB4xqIKjE0XIdewukMdip1v73cxeEduNk_azve-_pR8g5whQB6KWxephSQApQIn4hEywo5hxp8ZVMQDLIRYHlMfkW4zMAYAoTcj-3sf3VZ7pvstr3Q_Bd5l222A1Bm6H1fTZv49B2nf4XnA_Z3P7eN2HMCV3ZhB5-vNsG3Z-SI6e7aM_e3xPy-H2xqq_z5d3VTT1b5oYzwFw0du0EdZZS6jhQUzGmuW5AAkMpJWu4XBdVuZaNoaWUukSTOKO5qJxlJ-RinPoa_NvWxkFt2mhsOrO3fhsVCpBC8KKSn6OcSVHxtDKh0xE1wccYrFOvod3osFcI6tCxOnSsPjpOghyFP21n95_Qql7MVv-7-eimfu3uw9XhRZWCiUI9_bxS9a38wR-wVsj-AqlujxM</recordid><startdate>201305</startdate><enddate>201305</enddate><creator>Fan, Z.</creator><creator>Zhang, X.</creator><creator>Cai, W.</creator><creator>Wang, F.</creator><general>WILEY-VCH Verlag</general><general>WILEY‐VCH Verlag</general><scope>BSCLL</scope><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>7U5</scope><scope>8FD</scope><scope>L7M</scope></search><sort><creationdate>201305</creationdate><title>Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran</title><author>Fan, Z. ; Zhang, X. ; Cai, W. ; Wang, F.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Columns (structural)</topic><topic>Control strategies</topic><topic>Cost engineering</topic><topic>Dehydration</topic><topic>Design engineering</topic><topic>Distillation</topic><topic>Entrainment</topic><topic>Extractive distillation</topic><topic>Recovery</topic><topic>Strategy</topic><topic>Tetrahydrofuran dehydration</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fan, Z.</creatorcontrib><creatorcontrib>Zhang, X.</creatorcontrib><creatorcontrib>Cai, W.</creatorcontrib><creatorcontrib>Wang, F.</creatorcontrib><collection>Istex</collection><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>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering & technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fan, Z.</au><au>Zhang, X.</au><au>Cai, W.</au><au>Wang, F.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran</atitle><jtitle>Chemical engineering & technology</jtitle><addtitle>Chem. Eng. Technol</addtitle><date>2013-05</date><risdate>2013</risdate><volume>36</volume><issue>5</issue><spage>829</spage><epage>839</epage><pages>829-839</pages><issn>0930-7516</issn><eissn>1521-4125</eissn><abstract>Design and control of an extractive distillation system for tetrahydrofuran (THF) dehydration with ethylene glycol as entrainer is investigated. The main module is a two‐column system containing an extractive distillation column, whose top stream is the desired product THF, and an entrainer recovery column. Economic analysis with total annual cost as the objective function is developed. Two kinds of control strategies are explored for THF dehydration. The responses reveal that the control structure with fixed reflux ratio cannot maintain the bottom liquid level of the entrainer recovery column, while the control scheme with fixed reboiler heat duty/feed flow ratio exhibits good control performance in spite of large deviations in feed flow rate and feed composition.
THF dehydration is a process of economical concern, as the THF demand is increasing. A steady‐state design of two‐column extractive distillation for tetrahydrofuran‐H2O separation is introduced, and optimal conditions are evaluated by minimizing the total annual costs. Both a basic and an improved control strategy are devised.</abstract><cop>Weinheim</cop><pub>WILEY-VCH Verlag</pub><doi>10.1002/ceat.201200611</doi><tpages>11</tpages></addata></record> |
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subjects | Columns (structural) Control strategies Cost engineering Dehydration Design engineering Distillation Entrainment Extractive distillation Recovery Strategy Tetrahydrofuran dehydration |
title | Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran |
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