Agglomeration Control of l-Ornithine Aspartate Crystals by Operating Variables in Drowning-out Crystallization
The agglomeration of l-ornithine aspartate crystallized by the drowning-out method was investigated in a turbulent agitated semi-batch reactor. To modify the agglomeration conditions, the crystallization operating factors, including the agitation, feed flow rate, feed concentration, and drowning rat...
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Veröffentlicht in: | Industrial & engineering chemistry research 2006-03, Vol.45 (5), p.1631-1635 |
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creator | Chang, Sang-Mok Kim, Jong-Min Kim, In-Ho Shin, Dong-Myung Kim, Woo-Sik |
description | The agglomeration of l-ornithine aspartate crystallized by the drowning-out method was investigated in a turbulent agitated semi-batch reactor. To modify the agglomeration conditions, the crystallization operating factors, including the agitation, feed flow rate, feed concentration, and drowning ratio (volume ratio of antisolvent to feed solution), were all varied. The mean particle size of the l-ornithine aspartate in the product suspension increased with increasing feed concentration, drowning ratio, and feeding time, as crystal agglomeration was promoted via an increased crystal population and holding time in the agitated reactor. Conversely, it was sensitively reduced with increasing agitation speed because of the enhanced external force of the turbulent impact. Furthermore, the agglomeration behavior of the crystals was monitored during and after the crystallization to determine the role of supersaturation and turbulent fluid motion. |
doi_str_mv | 10.1021/ie050831j |
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To modify the agglomeration conditions, the crystallization operating factors, including the agitation, feed flow rate, feed concentration, and drowning ratio (volume ratio of antisolvent to feed solution), were all varied. The mean particle size of the l-ornithine aspartate in the product suspension increased with increasing feed concentration, drowning ratio, and feeding time, as crystal agglomeration was promoted via an increased crystal population and holding time in the agitated reactor. Conversely, it was sensitively reduced with increasing agitation speed because of the enhanced external force of the turbulent impact. Furthermore, the agglomeration behavior of the crystals was monitored during and after the crystallization to determine the role of supersaturation and turbulent fluid motion.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie050831j</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Chemical engineering ; Crystallization, leaching, miscellaneous separations ; Exact sciences and technology ; Sintering, pelletization, granulation ; Solid-solid systems</subject><ispartof>Industrial & engineering chemistry research, 2006-03, Vol.45 (5), p.1631-1635</ispartof><rights>Copyright © 2006 American Chemical Society</rights><rights>2006 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a393t-941bc652436cce114caf896d8ff42a8e3d96b93a6c51835b37d4c3fdcdc9fc313</citedby><cites>FETCH-LOGICAL-a393t-941bc652436cce114caf896d8ff42a8e3d96b93a6c51835b37d4c3fdcdc9fc313</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie050831j$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie050831j$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,777,781,2752,27057,27905,27906,56719,56769</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=17736238$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Chang, Sang-Mok</creatorcontrib><creatorcontrib>Kim, Jong-Min</creatorcontrib><creatorcontrib>Kim, In-Ho</creatorcontrib><creatorcontrib>Shin, Dong-Myung</creatorcontrib><creatorcontrib>Kim, Woo-Sik</creatorcontrib><title>Agglomeration Control of l-Ornithine Aspartate Crystals by Operating Variables in Drowning-out Crystallization</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>The agglomeration of l-ornithine aspartate crystallized by the drowning-out method was investigated in a turbulent agitated semi-batch reactor. To modify the agglomeration conditions, the crystallization operating factors, including the agitation, feed flow rate, feed concentration, and drowning ratio (volume ratio of antisolvent to feed solution), were all varied. The mean particle size of the l-ornithine aspartate in the product suspension increased with increasing feed concentration, drowning ratio, and feeding time, as crystal agglomeration was promoted via an increased crystal population and holding time in the agitated reactor. Conversely, it was sensitively reduced with increasing agitation speed because of the enhanced external force of the turbulent impact. Furthermore, the agglomeration behavior of the crystals was monitored during and after the crystallization to determine the role of supersaturation and turbulent fluid motion.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Crystallization, leaching, miscellaneous separations</subject><subject>Exact sciences and technology</subject><subject>Sintering, pelletization, granulation</subject><subject>Solid-solid systems</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2006</creationdate><recordtype>article</recordtype><recordid>eNptkEtPAyEUhYnRxPpY-A_YuHAxCsNjmGVTn7FJNVZdEoaBSh2hARqtv97R-ti4usm93zkn9wBwgNExRiU-cQYxJAieb4ABZiUqGKJsEwyQEKJgQrBtsJPSHCHEGKUD4IezWRdeTFTZBQ9HwecYOhgs7IpJ9C4_OW_gMC1UzCobOIqrlFWXYLOCk8WXzM_gg4pONZ1J0Hl4GsOr77dFWOYfvnPvXwF7YMv2arP_PXfB_fnZdHRZjCcXV6PhuFCkJrmoKW40ZyUlXGuDMdXKipq3wlpaKmFIW_OmJoprhgVhDalaqoltdatrqwkmu-Bo7atjSCkaKxfRvai4khjJz6Lkb1E9e7hmFypp1dmovHbpT1BVhJdE9Fyx5lzK5u33ruKz5BWpmJze3MlHestvp-Nryf98lU5yHpbR9x__k_8BWtaF-Q</recordid><startdate>20060301</startdate><enddate>20060301</enddate><creator>Chang, Sang-Mok</creator><creator>Kim, Jong-Min</creator><creator>Kim, In-Ho</creator><creator>Shin, Dong-Myung</creator><creator>Kim, Woo-Sik</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20060301</creationdate><title>Agglomeration Control of l-Ornithine Aspartate Crystals by Operating Variables in Drowning-out Crystallization</title><author>Chang, Sang-Mok ; Kim, Jong-Min ; Kim, In-Ho ; Shin, Dong-Myung ; Kim, Woo-Sik</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a393t-941bc652436cce114caf896d8ff42a8e3d96b93a6c51835b37d4c3fdcdc9fc313</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2006</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Crystallization, leaching, miscellaneous separations</topic><topic>Exact sciences and technology</topic><topic>Sintering, pelletization, granulation</topic><topic>Solid-solid systems</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chang, Sang-Mok</creatorcontrib><creatorcontrib>Kim, Jong-Min</creatorcontrib><creatorcontrib>Kim, In-Ho</creatorcontrib><creatorcontrib>Shin, Dong-Myung</creatorcontrib><creatorcontrib>Kim, Woo-Sik</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chang, Sang-Mok</au><au>Kim, Jong-Min</au><au>Kim, In-Ho</au><au>Shin, Dong-Myung</au><au>Kim, Woo-Sik</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Agglomeration Control of l-Ornithine Aspartate Crystals by Operating Variables in Drowning-out Crystallization</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2006-03-01</date><risdate>2006</risdate><volume>45</volume><issue>5</issue><spage>1631</spage><epage>1635</epage><pages>1631-1635</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>The agglomeration of l-ornithine aspartate crystallized by the drowning-out method was investigated in a turbulent agitated semi-batch reactor. To modify the agglomeration conditions, the crystallization operating factors, including the agitation, feed flow rate, feed concentration, and drowning ratio (volume ratio of antisolvent to feed solution), were all varied. The mean particle size of the l-ornithine aspartate in the product suspension increased with increasing feed concentration, drowning ratio, and feeding time, as crystal agglomeration was promoted via an increased crystal population and holding time in the agitated reactor. Conversely, it was sensitively reduced with increasing agitation speed because of the enhanced external force of the turbulent impact. Furthermore, the agglomeration behavior of the crystals was monitored during and after the crystallization to determine the role of supersaturation and turbulent fluid motion.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie050831j</doi><tpages>5</tpages></addata></record> |
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subjects | Applied sciences Chemical engineering Crystallization, leaching, miscellaneous separations Exact sciences and technology Sintering, pelletization, granulation Solid-solid systems |
title | Agglomeration Control of l-Ornithine Aspartate Crystals by Operating Variables in Drowning-out Crystallization |
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