Effective Adsorption Separation of n‑Hexane/2-Methylpentane in Facilely Synthesized Zeolitic Imidazolate Frameworks ZIF‑8 and ZIF-69
A facile synthesis procedure was built to synthesize zeolitic imidazolate frameworks (ZIFs) ZIF-8 and ZIF-69 under ambient conditions with the prevention of organic solvents. ZIF-69 adsorbent was first introduced in the liquid-phase separation of hexane isomers. A sieving test was carried out using...
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Veröffentlicht in: | Industrial & engineering chemistry research 2016-10, Vol.55 (40), p.10751-10757 |
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creator | Chen, Le Yuan, Sheng Qian, Jun-Feng Fan, Wei He, Ming-Yang Chen, Qun Zhang, Zhi-Hui |
description | A facile synthesis procedure was built to synthesize zeolitic imidazolate frameworks (ZIFs) ZIF-8 and ZIF-69 under ambient conditions with the prevention of organic solvents. ZIF-69 adsorbent was first introduced in the liquid-phase separation of hexane isomers. A sieving test was carried out using samples of n-hexane (nHEX) or 2-methylpentane (2MP) over two ZIFs and commercial 5A zeolite materials. According to batch adsorption performances and modeling, ZIF-8 exhibits the highest adsorption selectivity and capacity for nHEX, followed by ZIF-69 and 5A zeolite. The equilibrium data at 25 °C show that a significant amount (0.51 g/g) of nHEX and only 0.09 g/g 2MP can be adsorbed in ZIF-8. And the maximum adsorption capacity of nHEX and 2MP on ZIF-69 are 0.34 g/g and 0.10 g/g, respectively. Breakthrough experiments performed at 150 °C with a binary mixture of nHEX/2MP confirm the shape selectivity and adsorption capacities of ZIF-8 toward nHEX at various total pressures from 0.5 to 1.3 MPa and with different feed concentrations, which is attributed to the flexible architecture of ZIF-8 and its excellent shape match with nHEX. |
doi_str_mv | 10.1021/acs.iecr.6b02175 |
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ZIF-69 adsorbent was first introduced in the liquid-phase separation of hexane isomers. A sieving test was carried out using samples of n-hexane (nHEX) or 2-methylpentane (2MP) over two ZIFs and commercial 5A zeolite materials. According to batch adsorption performances and modeling, ZIF-8 exhibits the highest adsorption selectivity and capacity for nHEX, followed by ZIF-69 and 5A zeolite. The equilibrium data at 25 °C show that a significant amount (0.51 g/g) of nHEX and only 0.09 g/g 2MP can be adsorbed in ZIF-8. And the maximum adsorption capacity of nHEX and 2MP on ZIF-69 are 0.34 g/g and 0.10 g/g, respectively. Breakthrough experiments performed at 150 °C with a binary mixture of nHEX/2MP confirm the shape selectivity and adsorption capacities of ZIF-8 toward nHEX at various total pressures from 0.5 to 1.3 MPa and with different feed concentrations, which is attributed to the flexible architecture of ZIF-8 and its excellent shape match with nHEX.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/acs.iecr.6b02175</identifier><language>eng</language><publisher>American Chemical Society</publisher><ispartof>Industrial & engineering chemistry research, 2016-10, Vol.55 (40), p.10751-10757</ispartof><rights>Copyright © 2016 American Chemical Society</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a317t-b7c644c0030ae12bc5d7f01aae894346e5eae8f8fc8eaf714d6b5ceed2713c603</citedby><cites>FETCH-LOGICAL-a317t-b7c644c0030ae12bc5d7f01aae894346e5eae8f8fc8eaf714d6b5ceed2713c603</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/acs.iecr.6b02175$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/acs.iecr.6b02175$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids></links><search><creatorcontrib>Chen, Le</creatorcontrib><creatorcontrib>Yuan, Sheng</creatorcontrib><creatorcontrib>Qian, Jun-Feng</creatorcontrib><creatorcontrib>Fan, Wei</creatorcontrib><creatorcontrib>He, Ming-Yang</creatorcontrib><creatorcontrib>Chen, Qun</creatorcontrib><creatorcontrib>Zhang, Zhi-Hui</creatorcontrib><title>Effective Adsorption Separation of n‑Hexane/2-Methylpentane in Facilely Synthesized Zeolitic Imidazolate Frameworks ZIF‑8 and ZIF-69</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>A facile synthesis procedure was built to synthesize zeolitic imidazolate frameworks (ZIFs) ZIF-8 and ZIF-69 under ambient conditions with the prevention of organic solvents. ZIF-69 adsorbent was first introduced in the liquid-phase separation of hexane isomers. A sieving test was carried out using samples of n-hexane (nHEX) or 2-methylpentane (2MP) over two ZIFs and commercial 5A zeolite materials. According to batch adsorption performances and modeling, ZIF-8 exhibits the highest adsorption selectivity and capacity for nHEX, followed by ZIF-69 and 5A zeolite. The equilibrium data at 25 °C show that a significant amount (0.51 g/g) of nHEX and only 0.09 g/g 2MP can be adsorbed in ZIF-8. And the maximum adsorption capacity of nHEX and 2MP on ZIF-69 are 0.34 g/g and 0.10 g/g, respectively. Breakthrough experiments performed at 150 °C with a binary mixture of nHEX/2MP confirm the shape selectivity and adsorption capacities of ZIF-8 toward nHEX at various total pressures from 0.5 to 1.3 MPa and with different feed concentrations, which is attributed to the flexible architecture of ZIF-8 and its excellent shape match with nHEX.</description><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2016</creationdate><recordtype>article</recordtype><recordid>eNp1kL1OwzAUhS0EEqWwM_oBSGsnceKOVdXQSkUMhaVL5DjXqktqR3b4SSdGVl6RJyGhXZnuObr3HF19CN1SMqIkpGMh_UiDdKOk6GzKztCAspAEjMTsHA0I5zxgnLNLdOX9jhDCWBwP0NdcKZCNfgM8Lb11daOtwWuohRN_0ipsfj6_F_AhDIzD4AGabVvVYJrOY21wJqSuoGrxujXNFrw-QIk3YCvdaImXe12Kg61EAzhzYg_v1r14vFlmXSnHwpS9DpLJNbpQovJwc5pD9JzNn2aLYPV4v5xNV4GIaNoERSqTOJaEREQADQvJylQRKgTwSRzFCTDopOJKchAqpXGZFEwClGFKI5mQaIjIsVc6670DlddO74Vrc0rynmTekcx7kvmJZBe5O0b6zc6-OtM9-P_5L3l5e-E</recordid><startdate>20161012</startdate><enddate>20161012</enddate><creator>Chen, Le</creator><creator>Yuan, Sheng</creator><creator>Qian, Jun-Feng</creator><creator>Fan, Wei</creator><creator>He, Ming-Yang</creator><creator>Chen, Qun</creator><creator>Zhang, Zhi-Hui</creator><general>American Chemical Society</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20161012</creationdate><title>Effective Adsorption Separation of n‑Hexane/2-Methylpentane in Facilely Synthesized Zeolitic Imidazolate Frameworks ZIF‑8 and ZIF-69</title><author>Chen, Le ; Yuan, Sheng ; Qian, Jun-Feng ; Fan, Wei ; He, Ming-Yang ; Chen, Qun ; Zhang, Zhi-Hui</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a317t-b7c644c0030ae12bc5d7f01aae894346e5eae8f8fc8eaf714d6b5ceed2713c603</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2016</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chen, Le</creatorcontrib><creatorcontrib>Yuan, Sheng</creatorcontrib><creatorcontrib>Qian, Jun-Feng</creatorcontrib><creatorcontrib>Fan, Wei</creatorcontrib><creatorcontrib>He, Ming-Yang</creatorcontrib><creatorcontrib>Chen, Qun</creatorcontrib><creatorcontrib>Zhang, Zhi-Hui</creatorcontrib><collection>CrossRef</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chen, Le</au><au>Yuan, Sheng</au><au>Qian, Jun-Feng</au><au>Fan, Wei</au><au>He, Ming-Yang</au><au>Chen, Qun</au><au>Zhang, Zhi-Hui</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Effective Adsorption Separation of n‑Hexane/2-Methylpentane in Facilely Synthesized Zeolitic Imidazolate Frameworks ZIF‑8 and ZIF-69</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2016-10-12</date><risdate>2016</risdate><volume>55</volume><issue>40</issue><spage>10751</spage><epage>10757</epage><pages>10751-10757</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>A facile synthesis procedure was built to synthesize zeolitic imidazolate frameworks (ZIFs) ZIF-8 and ZIF-69 under ambient conditions with the prevention of organic solvents. ZIF-69 adsorbent was first introduced in the liquid-phase separation of hexane isomers. A sieving test was carried out using samples of n-hexane (nHEX) or 2-methylpentane (2MP) over two ZIFs and commercial 5A zeolite materials. According to batch adsorption performances and modeling, ZIF-8 exhibits the highest adsorption selectivity and capacity for nHEX, followed by ZIF-69 and 5A zeolite. The equilibrium data at 25 °C show that a significant amount (0.51 g/g) of nHEX and only 0.09 g/g 2MP can be adsorbed in ZIF-8. And the maximum adsorption capacity of nHEX and 2MP on ZIF-69 are 0.34 g/g and 0.10 g/g, respectively. Breakthrough experiments performed at 150 °C with a binary mixture of nHEX/2MP confirm the shape selectivity and adsorption capacities of ZIF-8 toward nHEX at various total pressures from 0.5 to 1.3 MPa and with different feed concentrations, which is attributed to the flexible architecture of ZIF-8 and its excellent shape match with nHEX.</abstract><pub>American Chemical Society</pub><doi>10.1021/acs.iecr.6b02175</doi><tpages>7</tpages></addata></record> |
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title | Effective Adsorption Separation of n‑Hexane/2-Methylpentane in Facilely Synthesized Zeolitic Imidazolate Frameworks ZIF‑8 and ZIF-69 |
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