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
Hauptverfasser: Chen, Le, Yuan, Sheng, Qian, Jun-Feng, Fan, Wei, He, Ming-Yang, Chen, Qun, Zhang, Zhi-Hui
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container_end_page 10757
container_issue 40
container_start_page 10751
container_title Industrial & engineering chemistry research
container_volume 55
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.
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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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