Loading…

Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization

A continuous multistage mixed suspension, mixed product removal (MSMPR) cascade crystallization system has been modeled and optimized for both the steady-state and the startup behaviors when both cooling and antisolvent addition are applied as the crystallization driving forces. The optimal steady-s...

Full description

Saved in:
Bibliographic Details
Published in:Industrial & engineering chemistry research 2015-06, Vol.54 (21), p.5673-5682
Main Authors: Yang, Yang, Nagy, Zoltan K
Format: Article
Language:English
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-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53
cites cdi_FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53
container_end_page 5682
container_issue 21
container_start_page 5673
container_title Industrial & engineering chemistry research
container_volume 54
creator Yang, Yang
Nagy, Zoltan K
description A continuous multistage mixed suspension, mixed product removal (MSMPR) cascade crystallization system has been modeled and optimized for both the steady-state and the startup behaviors when both cooling and antisolvent addition are applied as the crystallization driving forces. The optimal steady-state operating profiles of MSMPR cascade crystallizers have been obtained and found to be similar to the optimal batch trajectory. In addition, the minimum startup duration time is used as the objective function to optimize the startup behavior. Methods, including changing the initial solution compositions, applying dynamic antisolvent profiles, applying dynamic temperature profiles, and applying dynamic combined antisolvent and temperature profiles, are discussed and used to formulate the optimization problems. The optimal results indicate that for a cascade of two MSMPR crystallizers, it is possible to achieve a reduction of approximately 50% of the startup duration time and amount of waste. A model-free or direct design approach via closed-loop control to improve the startup performance is also proposed.
doi_str_mv 10.1021/ie5034254
format article
fullrecord <record><control><sourceid>acs_cross</sourceid><recordid>TN_cdi_crossref_primary_10_1021_ie5034254</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>c539480471</sourcerecordid><originalsourceid>FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53</originalsourceid><addsrcrecordid>eNptkM9KAzEQxoMoWKsH3yAXD4Krye5Omnori_-gUrF6XtLsrKTsJiXJFuvr-KKutogHTzPM95v5ho-QU84uOUv5lUFgWZ5CvkcGHFKWAMthnwyYlDIBKeGQHIWwZIwB5PmAfBauXRiLFS2ca4x9o8pWdGKjCa5Zo4208JsQVdOYDxWNs9TYHu1127ku0Efz3u_Ou7BCG3r5Yjd58q7qdKTP2Lq1amihglYV_rmGPlzTeURVbZJ5VBF_nPvOx25FZ6to2p3lMTmoVRPwZFeH5PX25qW4T6azu4diMk1UJtKY1KgFl2OQGhjjIJQGPqoFjBhgWueZ7jOokTEp1BiEWIgUR1mmJE-rBc8RsiE5397V3oXgsS5X3rTKb0rOyu90y990e_ZsyyodyqXrvO0_-4f7AlYSe8I</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization</title><source>American Chemical Society:Jisc Collections:American Chemical Society Read &amp; Publish Agreement 2022-2024 (Reading list)</source><creator>Yang, Yang ; Nagy, Zoltan K</creator><creatorcontrib>Yang, Yang ; Nagy, Zoltan K</creatorcontrib><description>A continuous multistage mixed suspension, mixed product removal (MSMPR) cascade crystallization system has been modeled and optimized for both the steady-state and the startup behaviors when both cooling and antisolvent addition are applied as the crystallization driving forces. The optimal steady-state operating profiles of MSMPR cascade crystallizers have been obtained and found to be similar to the optimal batch trajectory. In addition, the minimum startup duration time is used as the objective function to optimize the startup behavior. Methods, including changing the initial solution compositions, applying dynamic antisolvent profiles, applying dynamic temperature profiles, and applying dynamic combined antisolvent and temperature profiles, are discussed and used to formulate the optimization problems. The optimal results indicate that for a cascade of two MSMPR crystallizers, it is possible to achieve a reduction of approximately 50% of the startup duration time and amount of waste. A model-free or direct design approach via closed-loop control to improve the startup performance is also proposed.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie5034254</identifier><language>eng</language><publisher>American Chemical Society</publisher><ispartof>Industrial &amp; engineering chemistry research, 2015-06, Vol.54 (21), p.5673-5682</ispartof><rights>Copyright © American Chemical Society</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53</citedby><cites>FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53</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>Yang, Yang</creatorcontrib><creatorcontrib>Nagy, Zoltan K</creatorcontrib><title>Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization</title><title>Industrial &amp; engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>A continuous multistage mixed suspension, mixed product removal (MSMPR) cascade crystallization system has been modeled and optimized for both the steady-state and the startup behaviors when both cooling and antisolvent addition are applied as the crystallization driving forces. The optimal steady-state operating profiles of MSMPR cascade crystallizers have been obtained and found to be similar to the optimal batch trajectory. In addition, the minimum startup duration time is used as the objective function to optimize the startup behavior. Methods, including changing the initial solution compositions, applying dynamic antisolvent profiles, applying dynamic temperature profiles, and applying dynamic combined antisolvent and temperature profiles, are discussed and used to formulate the optimization problems. The optimal results indicate that for a cascade of two MSMPR crystallizers, it is possible to achieve a reduction of approximately 50% of the startup duration time and amount of waste. A model-free or direct design approach via closed-loop control to improve the startup performance is also proposed.</description><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><recordid>eNptkM9KAzEQxoMoWKsH3yAXD4Krye5Omnori_-gUrF6XtLsrKTsJiXJFuvr-KKutogHTzPM95v5ho-QU84uOUv5lUFgWZ5CvkcGHFKWAMthnwyYlDIBKeGQHIWwZIwB5PmAfBauXRiLFS2ca4x9o8pWdGKjCa5Zo4208JsQVdOYDxWNs9TYHu1127ku0Efz3u_Ou7BCG3r5Yjd58q7qdKTP2Lq1amihglYV_rmGPlzTeURVbZJ5VBF_nPvOx25FZ6to2p3lMTmoVRPwZFeH5PX25qW4T6azu4diMk1UJtKY1KgFl2OQGhjjIJQGPqoFjBhgWueZ7jOokTEp1BiEWIgUR1mmJE-rBc8RsiE5397V3oXgsS5X3rTKb0rOyu90y990e_ZsyyodyqXrvO0_-4f7AlYSe8I</recordid><startdate>20150603</startdate><enddate>20150603</enddate><creator>Yang, Yang</creator><creator>Nagy, Zoltan K</creator><general>American Chemical Society</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20150603</creationdate><title>Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization</title><author>Yang, Yang ; Nagy, Zoltan K</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Yang, Yang</creatorcontrib><creatorcontrib>Nagy, Zoltan K</creatorcontrib><collection>CrossRef</collection><jtitle>Industrial &amp; engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Yang, Yang</au><au>Nagy, Zoltan K</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization</atitle><jtitle>Industrial &amp; engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2015-06-03</date><risdate>2015</risdate><volume>54</volume><issue>21</issue><spage>5673</spage><epage>5682</epage><pages>5673-5682</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>A continuous multistage mixed suspension, mixed product removal (MSMPR) cascade crystallization system has been modeled and optimized for both the steady-state and the startup behaviors when both cooling and antisolvent addition are applied as the crystallization driving forces. The optimal steady-state operating profiles of MSMPR cascade crystallizers have been obtained and found to be similar to the optimal batch trajectory. In addition, the minimum startup duration time is used as the objective function to optimize the startup behavior. Methods, including changing the initial solution compositions, applying dynamic antisolvent profiles, applying dynamic temperature profiles, and applying dynamic combined antisolvent and temperature profiles, are discussed and used to formulate the optimization problems. The optimal results indicate that for a cascade of two MSMPR crystallizers, it is possible to achieve a reduction of approximately 50% of the startup duration time and amount of waste. A model-free or direct design approach via closed-loop control to improve the startup performance is also proposed.</abstract><pub>American Chemical Society</pub><doi>10.1021/ie5034254</doi><tpages>10</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0888-5885
ispartof Industrial & engineering chemistry research, 2015-06, Vol.54 (21), p.5673-5682
issn 0888-5885
1520-5045
language eng
recordid cdi_crossref_primary_10_1021_ie5034254
source American Chemical Society:Jisc Collections:American Chemical Society Read & Publish Agreement 2022-2024 (Reading list)
title Combined Cooling and Antisolvent Crystallization in Continuous Mixed Suspension, Mixed Product Removal Cascade Crystallizers: Steady-State and Startup Optimization
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T11%3A22%3A42IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-acs_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Combined%20Cooling%20and%20Antisolvent%20Crystallization%20in%20Continuous%20Mixed%20Suspension,%20Mixed%20Product%20Removal%20Cascade%20Crystallizers:%20Steady-State%20and%20Startup%20Optimization&rft.jtitle=Industrial%20&%20engineering%20chemistry%20research&rft.au=Yang,%20Yang&rft.date=2015-06-03&rft.volume=54&rft.issue=21&rft.spage=5673&rft.epage=5682&rft.pages=5673-5682&rft.issn=0888-5885&rft.eissn=1520-5045&rft_id=info:doi/10.1021/ie5034254&rft_dat=%3Cacs_cross%3Ec539480471%3C/acs_cross%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-a362t-fec618958c500156ac517f65705e2f43c088fe0086a9566b62e733a812db14e53%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true