Loading…

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...

Full description

Saved in:
Bibliographic Details
Published in:Chemical engineering & technology 2013-05, Vol.36 (5), p.829-839
Main Authors: Fan, Z., Zhang, X., Cai, W., Wang, F.
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3
cites cdi_FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3
container_end_page 839
container_issue 5
container_start_page 829
container_title Chemical engineering & technology
container_volume 36
creator Fan, Z.
Zhang, X.
Cai, W.
Wang, F.
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
format article
fullrecord <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1709774589</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>1709774589</sourcerecordid><originalsourceid>FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3</originalsourceid><addsrcrecordid>eNqFkMFP2zAUh61pSHTAlXOOXFLes504PlZpB4xqIKjE0XIdewukMdip1v73cxeEduNk_azve-_pR8g5whQB6KWxephSQApQIn4hEywo5hxp8ZVMQDLIRYHlMfkW4zMAYAoTcj-3sf3VZ7pvstr3Q_Bd5l222A1Bm6H1fTZv49B2nf4XnA_Z3P7eN2HMCV3ZhB5-vNsG3Z-SI6e7aM_e3xPy-H2xqq_z5d3VTT1b5oYzwFw0du0EdZZS6jhQUzGmuW5AAkMpJWu4XBdVuZaNoaWUukSTOKO5qJxlJ-RinPoa_NvWxkFt2mhsOrO3fhsVCpBC8KKSn6OcSVHxtDKh0xE1wccYrFOvod3osFcI6tCxOnSsPjpOghyFP21n95_Qql7MVv-7-eimfu3uw9XhRZWCiUI9_bxS9a38wR-wVsj-AqlujxM</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1439784993</pqid></control><display><type>article</type><title>Design and Control of Extraction Distillation for Dehydration of Tetrahydrofuran</title><source>Wiley-Blackwell Read &amp; Publish Collection</source><creator>Fan, Z. ; Zhang, X. ; Cai, W. ; Wang, F.</creator><creatorcontrib>Fan, Z. ; Zhang, X. ; Cai, W. ; Wang, F.</creatorcontrib><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><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 &amp; technology, 2013-05, Vol.36 (5), p.829-839</ispartof><rights>Copyright © 2013 WILEY‐VCH Verlag GmbH &amp; 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 &amp; 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 &amp; Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy &amp; Non-Living Resources</collection><collection>Aquatic Science &amp; 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 &amp; 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 &amp; 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>
fulltext fulltext
identifier ISSN: 0930-7516
ispartof Chemical engineering & technology, 2013-05, Vol.36 (5), p.829-839
issn 0930-7516
1521-4125
language eng
recordid cdi_proquest_miscellaneous_1709774589
source Wiley-Blackwell Read & Publish Collection
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
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T22%3A11%3A39IST&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=Design%20and%20Control%20of%20Extraction%20Distillation%20for%20Dehydration%20of%20Tetrahydrofuran&rft.jtitle=Chemical%20engineering%20&%20technology&rft.au=Fan,%20Z.&rft.date=2013-05&rft.volume=36&rft.issue=5&rft.spage=829&rft.epage=839&rft.pages=829-839&rft.issn=0930-7516&rft.eissn=1521-4125&rft_id=info:doi/10.1002/ceat.201200611&rft_dat=%3Cproquest_cross%3E1709774589%3C/proquest_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c4301-7debf72fe222f402c833a4ad090319993d49b586b9dc2699a61cf40ca478fe3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=1439784993&rft_id=info:pmid/&rfr_iscdi=true