Relay simulated moving bed chromatography: Concept and design criteria
► The R-SMB is a new implementation of SMB chromatography with intermittent or pulsed outlets. ► The R-SMB is an analog of the SMB in terms of displaced volumes of fluid per switch interval. ► The R-SMB has the same separation region as the SMB for linear isotherms. ► The R-SMB is compared against t...
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Veröffentlicht in: | Journal of Chromatography A 2012-10, Vol.1260, p.132-142 |
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description | ► The R-SMB is a new implementation of SMB chromatography with intermittent or pulsed outlets. ► The R-SMB is an analog of the SMB in terms of displaced volumes of fluid per switch interval. ► The R-SMB has the same separation region as the SMB for linear isotherms. ► The R-SMB is compared against the SMB under conditions of finite column efficiency. ► The R-SMB performs increasingly better than the SMB with decreasing column efficiency.
We present a new class of multicolumn chromatographic processes that change the classical way of handling the product outlets of simulated moving-bed (SMB) chromatography to avoid the use of flow controllers or an extra pump—the objective is to have just two- or three-way valves at a column outlet—while maintaining the analogy with the SMB in terms of displaced volumes of fluid per switch interval. In this class of processes the flow through a zone (or column) is always in one of the three states: (i) frozen, (ii) completely directed to the next zone (or column), or (iii) entirely diverted to a product line. We use the term relayed stream to refer to this particular type of manipulation of the outflow from a column. For this class of processes we derive a SMB analog—the R-SMB process—and demonstrate, under the framework of the equilibrium theory, that this process has the same separation region as the classical SMB for linear adsorption systems. In addition, the results from the equilibrium theory show that the R-SMB process consists of two distinct cycles that differ only in their intermediate sub-step: one cycle for selectivities α smaller than (3+5)/2 and another cycle for larger values of α; in the former case no product stream is collected during the intermediate sub-step, whereas in the latter case both product streams are collected. We also examine the R-SMB process under conditions of finite column efficiency and compare its performance against those of the classical open- and closed-loop SMBs. Our simulation results show that the R-SMB process requires less desorbent and is more productive than the standard SMB processes under conditions of finite column efficiency and that the comparison increasingly favors the R-SMB as the column efficiency decreases. |
doi_str_mv | 10.1016/j.chroma.2012.08.076 |
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We present a new class of multicolumn chromatographic processes that change the classical way of handling the product outlets of simulated moving-bed (SMB) chromatography to avoid the use of flow controllers or an extra pump—the objective is to have just two- or three-way valves at a column outlet—while maintaining the analogy with the SMB in terms of displaced volumes of fluid per switch interval. In this class of processes the flow through a zone (or column) is always in one of the three states: (i) frozen, (ii) completely directed to the next zone (or column), or (iii) entirely diverted to a product line. We use the term relayed stream to refer to this particular type of manipulation of the outflow from a column. For this class of processes we derive a SMB analog—the R-SMB process—and demonstrate, under the framework of the equilibrium theory, that this process has the same separation region as the classical SMB for linear adsorption systems. In addition, the results from the equilibrium theory show that the R-SMB process consists of two distinct cycles that differ only in their intermediate sub-step: one cycle for selectivities α smaller than (3+5)/2 and another cycle for larger values of α; in the former case no product stream is collected during the intermediate sub-step, whereas in the latter case both product streams are collected. We also examine the R-SMB process under conditions of finite column efficiency and compare its performance against those of the classical open- and closed-loop SMBs. Our simulation results show that the R-SMB process requires less desorbent and is more productive than the standard SMB processes under conditions of finite column efficiency and that the comparison increasingly favors the R-SMB as the column efficiency decreases.</description><identifier>ISSN: 0021-9673</identifier><identifier>EISSN: 1873-3778</identifier><identifier>DOI: 10.1016/j.chroma.2012.08.076</identifier><identifier>PMID: 22980644</identifier><language>eng</language><publisher>Netherlands: Elsevier B.V</publisher><subject>Adsorption ; Binary separation ; Chromatography ; Chromatography - methods ; Columns (process) ; Computer Simulation ; Controllers ; Equilibrium theory ; Intervals ; Materials handling ; Mathematical analysis ; Models, Theoretical ; Multi-column chromatography ; Research Design ; Simulated moving bed ; Simulation ; SMB analog ; Streams</subject><ispartof>Journal of Chromatography A, 2012-10, Vol.1260, p.132-142</ispartof><rights>2012 Elsevier B.V.</rights><rights>Copyright © 2012 Elsevier B.V. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c452t-f7a2976ac2768e9b3827e104734487028b63a543bd27e27af126278a70aac2e13</citedby><cites>FETCH-LOGICAL-c452t-f7a2976ac2768e9b3827e104734487028b63a543bd27e27af126278a70aac2e13</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.chroma.2012.08.076$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/22980644$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Silva, Ricardo J.S.</creatorcontrib><creatorcontrib>Rodrigues, Rui C.R.</creatorcontrib><creatorcontrib>Mota, José P.B.</creatorcontrib><title>Relay simulated moving bed chromatography: Concept and design criteria</title><title>Journal of Chromatography A</title><addtitle>J Chromatogr A</addtitle><description>► The R-SMB is a new implementation of SMB chromatography with intermittent or pulsed outlets. ► The R-SMB is an analog of the SMB in terms of displaced volumes of fluid per switch interval. ► The R-SMB has the same separation region as the SMB for linear isotherms. ► The R-SMB is compared against the SMB under conditions of finite column efficiency. ► The R-SMB performs increasingly better than the SMB with decreasing column efficiency.
We present a new class of multicolumn chromatographic processes that change the classical way of handling the product outlets of simulated moving-bed (SMB) chromatography to avoid the use of flow controllers or an extra pump—the objective is to have just two- or three-way valves at a column outlet—while maintaining the analogy with the SMB in terms of displaced volumes of fluid per switch interval. In this class of processes the flow through a zone (or column) is always in one of the three states: (i) frozen, (ii) completely directed to the next zone (or column), or (iii) entirely diverted to a product line. We use the term relayed stream to refer to this particular type of manipulation of the outflow from a column. For this class of processes we derive a SMB analog—the R-SMB process—and demonstrate, under the framework of the equilibrium theory, that this process has the same separation region as the classical SMB for linear adsorption systems. In addition, the results from the equilibrium theory show that the R-SMB process consists of two distinct cycles that differ only in their intermediate sub-step: one cycle for selectivities α smaller than (3+5)/2 and another cycle for larger values of α; in the former case no product stream is collected during the intermediate sub-step, whereas in the latter case both product streams are collected. We also examine the R-SMB process under conditions of finite column efficiency and compare its performance against those of the classical open- and closed-loop SMBs. Our simulation results show that the R-SMB process requires less desorbent and is more productive than the standard SMB processes under conditions of finite column efficiency and that the comparison increasingly favors the R-SMB as the column efficiency decreases.</description><subject>Adsorption</subject><subject>Binary separation</subject><subject>Chromatography</subject><subject>Chromatography - methods</subject><subject>Columns (process)</subject><subject>Computer Simulation</subject><subject>Controllers</subject><subject>Equilibrium theory</subject><subject>Intervals</subject><subject>Materials handling</subject><subject>Mathematical analysis</subject><subject>Models, Theoretical</subject><subject>Multi-column chromatography</subject><subject>Research Design</subject><subject>Simulated moving bed</subject><subject>Simulation</subject><subject>SMB analog</subject><subject>Streams</subject><issn>0021-9673</issn><issn>1873-3778</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkV1r2zAUhsXYWNNu_2B0vtyNPelY0VF2MSihH4PCYFuvhSwfpwq2lUlOIP9-Cm532V5JiOd9JT2HsU-CV4IL9XVbuccYBlsBF1BxXXFUb9hCaKzLGlG_ZQvOQZQrhfUZO09py7lAjvCenQGsNFdSLtjNL-rtsUh-2Pd2orYYwsGPm6LJ27l_Cptod4_Hb8U6jI52U2HHtmgp-c1YuOgnit5-YO862yf6-LResIeb6z_ru_L-5-2P9dV96eQSprJDCytU1gEqTaum1oAkuMRaSo0cdKNqu5R10-ZzQNsJUIDaIrc5Q6K-YF_m3l0Mf_eUJjP45Kjv7Uhhn4xQEkApAfp1NHMohELMqJxRF0NKkTqzi36w8WgENyfZZmtmGeYk23Btsuwcu3y6Yd8M1P4PPdvNwOcZ6GwwdhN9Mg-_c8MyT0LnuZz-830mKEs7eIomOU9Zc-sjucm0wb_8hn8UHZmB</recordid><startdate>20121019</startdate><enddate>20121019</enddate><creator>Silva, Ricardo J.S.</creator><creator>Rodrigues, Rui C.R.</creator><creator>Mota, José P.B.</creator><general>Elsevier B.V</general><scope>FBQ</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H97</scope><scope>L.G</scope><scope>7U5</scope><scope>8FD</scope><scope>L7M</scope></search><sort><creationdate>20121019</creationdate><title>Relay simulated moving bed chromatography: Concept and design criteria</title><author>Silva, Ricardo J.S. ; Rodrigues, Rui C.R. ; Mota, José P.B.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c452t-f7a2976ac2768e9b3827e104734487028b63a543bd27e27af126278a70aac2e13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Adsorption</topic><topic>Binary separation</topic><topic>Chromatography</topic><topic>Chromatography - methods</topic><topic>Columns (process)</topic><topic>Computer Simulation</topic><topic>Controllers</topic><topic>Equilibrium theory</topic><topic>Intervals</topic><topic>Materials handling</topic><topic>Mathematical analysis</topic><topic>Models, Theoretical</topic><topic>Multi-column chromatography</topic><topic>Research Design</topic><topic>Simulated moving bed</topic><topic>Simulation</topic><topic>SMB analog</topic><topic>Streams</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Silva, Ricardo J.S.</creatorcontrib><creatorcontrib>Rodrigues, Rui C.R.</creatorcontrib><creatorcontrib>Mota, José P.B.</creatorcontrib><collection>AGRIS</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</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) 3: Aquatic Pollution & Environmental Quality</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>Journal of Chromatography A</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Silva, Ricardo J.S.</au><au>Rodrigues, Rui C.R.</au><au>Mota, José P.B.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Relay simulated moving bed chromatography: Concept and design criteria</atitle><jtitle>Journal of Chromatography A</jtitle><addtitle>J Chromatogr A</addtitle><date>2012-10-19</date><risdate>2012</risdate><volume>1260</volume><spage>132</spage><epage>142</epage><pages>132-142</pages><issn>0021-9673</issn><eissn>1873-3778</eissn><abstract>► The R-SMB is a new implementation of SMB chromatography with intermittent or pulsed outlets. ► The R-SMB is an analog of the SMB in terms of displaced volumes of fluid per switch interval. ► The R-SMB has the same separation region as the SMB for linear isotherms. ► The R-SMB is compared against the SMB under conditions of finite column efficiency. ► The R-SMB performs increasingly better than the SMB with decreasing column efficiency.
We present a new class of multicolumn chromatographic processes that change the classical way of handling the product outlets of simulated moving-bed (SMB) chromatography to avoid the use of flow controllers or an extra pump—the objective is to have just two- or three-way valves at a column outlet—while maintaining the analogy with the SMB in terms of displaced volumes of fluid per switch interval. In this class of processes the flow through a zone (or column) is always in one of the three states: (i) frozen, (ii) completely directed to the next zone (or column), or (iii) entirely diverted to a product line. We use the term relayed stream to refer to this particular type of manipulation of the outflow from a column. For this class of processes we derive a SMB analog—the R-SMB process—and demonstrate, under the framework of the equilibrium theory, that this process has the same separation region as the classical SMB for linear adsorption systems. In addition, the results from the equilibrium theory show that the R-SMB process consists of two distinct cycles that differ only in their intermediate sub-step: one cycle for selectivities α smaller than (3+5)/2 and another cycle for larger values of α; in the former case no product stream is collected during the intermediate sub-step, whereas in the latter case both product streams are collected. We also examine the R-SMB process under conditions of finite column efficiency and compare its performance against those of the classical open- and closed-loop SMBs. Our simulation results show that the R-SMB process requires less desorbent and is more productive than the standard SMB processes under conditions of finite column efficiency and that the comparison increasingly favors the R-SMB as the column efficiency decreases.</abstract><cop>Netherlands</cop><pub>Elsevier B.V</pub><pmid>22980644</pmid><doi>10.1016/j.chroma.2012.08.076</doi><tpages>11</tpages></addata></record> |
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subjects | Adsorption Binary separation Chromatography Chromatography - methods Columns (process) Computer Simulation Controllers Equilibrium theory Intervals Materials handling Mathematical analysis Models, Theoretical Multi-column chromatography Research Design Simulated moving bed Simulation SMB analog Streams |
title | Relay simulated moving bed chromatography: Concept and design criteria |
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