Performance study of multistage membrane and hybrid distillation processes for propylene/propane separation
This article investigates the separation performance and energy efficiency of multistage membrane and hybrid processes for the separation of propane/propylene mixtures compared with the conventional distillation process. To satisfy the separation objective of 0.996 mol/mol (99.6 mol%) C3H6 purity an...
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| Veröffentlicht in: | Canadian journal of chemical engineering 2017-12, Vol.95 (12), p.2390-2397 |
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| container_title | Canadian journal of chemical engineering |
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| creator | Park, Jaedeuk Kim, Kiwoong Shin, Jae‐Wook Tak, Kyungjae Park, Yong‐Ki |
| description | This article investigates the separation performance and energy efficiency of multistage membrane and hybrid processes for the separation of propane/propylene mixtures compared with the conventional distillation process. To satisfy the separation objective of 0.996 mol/mol (99.6 mol%) C3H6 purity and 97 % C3H6 separation recovery ratio, a detailed parametric study for the multistage membrane and hybrid process systems was described. For this purpose, the effects of operating conditions and process configurations on separation performance have been evaluated using a counter‐current flow model. The numerical model using a single‐stage membrane was validated with published experimental data for the membrane system, and the model was then applied to multistage membrane and hybrid processes. The optimum variables that satisfy the targeted purity and recovery ratio were examined using the multistage membrane at a given selectivity and pressure ratio. The energy consumption of several hybrid configurations for the separation of propane/propylene mixtures was investigated with conventional distillation. |
| doi_str_mv | 10.1002/cjce.22914 |
| format | Article |
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To satisfy the separation objective of 0.996 mol/mol (99.6 mol%) C3H6 purity and 97 % C3H6 separation recovery ratio, a detailed parametric study for the multistage membrane and hybrid process systems was described. For this purpose, the effects of operating conditions and process configurations on separation performance have been evaluated using a counter‐current flow model. The numerical model using a single‐stage membrane was validated with published experimental data for the membrane system, and the model was then applied to multistage membrane and hybrid processes. The optimum variables that satisfy the targeted purity and recovery ratio were examined using the multistage membrane at a given selectivity and pressure ratio. The energy consumption of several hybrid configurations for the separation of propane/propylene mixtures was investigated with conventional distillation.</description><identifier>ISSN: 0008-4034</identifier><identifier>EISSN: 1939-019X</identifier><identifier>DOI: 10.1002/cjce.22914</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc</publisher><subject>Configuration management ; Configurations ; Distillation ; energy analysis ; Energy consumption ; gas separation ; hybrid process ; Hybrid systems ; Mathematical models ; membrane process ; Multistage ; Pressure ratio ; process simulation ; Propane ; Propylene ; Purity ; Recovery ; Selectivity ; Separation ; Studies</subject><ispartof>Canadian journal of chemical engineering, 2017-12, Vol.95 (12), p.2390-2397</ispartof><rights>2017 Canadian Society for Chemical Engineering</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c2534-66e28f28368415cdd2b447e2eac9b26437024f6de1c05c838565e14475aa4b363</citedby><cites>FETCH-LOGICAL-c2534-66e28f28368415cdd2b447e2eac9b26437024f6de1c05c838565e14475aa4b363</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fcjce.22914$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcjce.22914$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1411,27901,27902,45550,45551</link.rule.ids></links><search><creatorcontrib>Park, Jaedeuk</creatorcontrib><creatorcontrib>Kim, Kiwoong</creatorcontrib><creatorcontrib>Shin, Jae‐Wook</creatorcontrib><creatorcontrib>Tak, Kyungjae</creatorcontrib><creatorcontrib>Park, Yong‐Ki</creatorcontrib><title>Performance study of multistage membrane and hybrid distillation processes for propylene/propane separation</title><title>Canadian journal of chemical engineering</title><description>This article investigates the separation performance and energy efficiency of multistage membrane and hybrid processes for the separation of propane/propylene mixtures compared with the conventional distillation process. To satisfy the separation objective of 0.996 mol/mol (99.6 mol%) C3H6 purity and 97 % C3H6 separation recovery ratio, a detailed parametric study for the multistage membrane and hybrid process systems was described. For this purpose, the effects of operating conditions and process configurations on separation performance have been evaluated using a counter‐current flow model. The numerical model using a single‐stage membrane was validated with published experimental data for the membrane system, and the model was then applied to multistage membrane and hybrid processes. The optimum variables that satisfy the targeted purity and recovery ratio were examined using the multistage membrane at a given selectivity and pressure ratio. The energy consumption of several hybrid configurations for the separation of propane/propylene mixtures was investigated with conventional distillation.</description><subject>Configuration management</subject><subject>Configurations</subject><subject>Distillation</subject><subject>energy analysis</subject><subject>Energy consumption</subject><subject>gas separation</subject><subject>hybrid process</subject><subject>Hybrid systems</subject><subject>Mathematical models</subject><subject>membrane process</subject><subject>Multistage</subject><subject>Pressure ratio</subject><subject>process simulation</subject><subject>Propane</subject><subject>Propylene</subject><subject>Purity</subject><subject>Recovery</subject><subject>Selectivity</subject><subject>Separation</subject><subject>Studies</subject><issn>0008-4034</issn><issn>1939-019X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQhoMouK5e_AUBb0J389Vse5SyrsqCHhS8hTSZatd-mbRI_73p1rOnmWGe953hReiakhUlhK3NwcCKsZSKE7SgKU8jQtP3U7QghCSRIFycowvvD2FkRNAF-noBV7Su1o0B7PvBjrgtcD1Ufel7_QG4hjp3ugGsG4s_x9yVFtuwK6tK92Xb4M61BrwHj4PPNHVjBQ2sp27Seei0O6KX6KzQlYerv7pEb_fb1-wh2j_vHrO7fWRYzEUkJbCkYAmXiaCxsZblQmyAgTZpzqTgG8JEIS1QQ2KT8CSWMdCAxFqLnEu-RDezb3jhewDfq0M7uCacVDSVlARjTgJ1O1PGtd47KFTnylq7UVGipjDVFKY6hhlgOsM_ZQXjP6TKnrLtrPkFq6t4cw</recordid><startdate>201712</startdate><enddate>201712</enddate><creator>Park, Jaedeuk</creator><creator>Kim, Kiwoong</creator><creator>Shin, Jae‐Wook</creator><creator>Tak, Kyungjae</creator><creator>Park, Yong‐Ki</creator><general>Wiley Subscription Services, Inc</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>201712</creationdate><title>Performance study of multistage membrane and hybrid distillation processes for propylene/propane separation</title><author>Park, Jaedeuk ; Kim, Kiwoong ; Shin, Jae‐Wook ; Tak, Kyungjae ; Park, Yong‐Ki</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c2534-66e28f28368415cdd2b447e2eac9b26437024f6de1c05c838565e14475aa4b363</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Configuration management</topic><topic>Configurations</topic><topic>Distillation</topic><topic>energy analysis</topic><topic>Energy consumption</topic><topic>gas separation</topic><topic>hybrid process</topic><topic>Hybrid systems</topic><topic>Mathematical models</topic><topic>membrane process</topic><topic>Multistage</topic><topic>Pressure ratio</topic><topic>process simulation</topic><topic>Propane</topic><topic>Propylene</topic><topic>Purity</topic><topic>Recovery</topic><topic>Selectivity</topic><topic>Separation</topic><topic>Studies</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Park, Jaedeuk</creatorcontrib><creatorcontrib>Kim, Kiwoong</creatorcontrib><creatorcontrib>Shin, Jae‐Wook</creatorcontrib><creatorcontrib>Tak, Kyungjae</creatorcontrib><creatorcontrib>Park, Yong‐Ki</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Canadian journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Park, Jaedeuk</au><au>Kim, Kiwoong</au><au>Shin, Jae‐Wook</au><au>Tak, Kyungjae</au><au>Park, Yong‐Ki</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance study of multistage membrane and hybrid distillation processes for propylene/propane separation</atitle><jtitle>Canadian journal of chemical engineering</jtitle><date>2017-12</date><risdate>2017</risdate><volume>95</volume><issue>12</issue><spage>2390</spage><epage>2397</epage><pages>2390-2397</pages><issn>0008-4034</issn><eissn>1939-019X</eissn><abstract>This article investigates the separation performance and energy efficiency of multistage membrane and hybrid processes for the separation of propane/propylene mixtures compared with the conventional distillation process. To satisfy the separation objective of 0.996 mol/mol (99.6 mol%) C3H6 purity and 97 % C3H6 separation recovery ratio, a detailed parametric study for the multistage membrane and hybrid process systems was described. For this purpose, the effects of operating conditions and process configurations on separation performance have been evaluated using a counter‐current flow model. The numerical model using a single‐stage membrane was validated with published experimental data for the membrane system, and the model was then applied to multistage membrane and hybrid processes. The optimum variables that satisfy the targeted purity and recovery ratio were examined using the multistage membrane at a given selectivity and pressure ratio. The energy consumption of several hybrid configurations for the separation of propane/propylene mixtures was investigated with conventional distillation.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc</pub><doi>10.1002/cjce.22914</doi><tpages>8</tpages></addata></record> |
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| ispartof | Canadian journal of chemical engineering, 2017-12, Vol.95 (12), p.2390-2397 |
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| language | eng |
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| source | Wiley Online Library Journals Frontfile Complete |
| subjects | Configuration management Configurations Distillation energy analysis Energy consumption gas separation hybrid process Hybrid systems Mathematical models membrane process Multistage Pressure ratio process simulation Propane Propylene Purity Recovery Selectivity Separation Studies |
| title | Performance study of multistage membrane and hybrid distillation processes for propylene/propane separation |
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