The effective adsorption separation of n-hexane/3-methylpentane by vapor-phase linker exchange of Zeolitic-imidazolate framework ZIF-8

Zeolitic-Imidazolate Framework 8 (ZIF-8), a porous crystalline absorbent, could be synthesized from the coordination reaction of zinc ions and 2-methylimidazole (2-mIM). ZIF-8 has a large specific surface area and a high adsorption capacity for n -hexane ( n HEX). However, ZIF-8 suffers from low selectivity for both linear and mono-chain alkanes. Therefore, ZIF-8 was modified through 2-mIM ligand being partly replaced by 2-nitroimidazole (2-nIM) through Vapor-Phase post-synthesis modification. The modified materials were denoted as ZIF-8-2-nIM-X (X = 24h, 48h, 72h). ZIF-8-2-nIM-X has a higher specific surface area and better thermal stability than ZIF-8. Further thermodynamic and kinetic calculations show that the affinity of hexane isomers on ZIF-8-2-nIM-X is spontaneous physical adsorption combined with an exothermic process. In contrast, kinetic studies show that the adsorption of hexane isomers on ZIF-8-2-nIM-X is a pseudo-second-order kinetic model. The batch and dynamic adsorption and separation properties of ZIF-8-2-nIM-X for hexane isomers were studied. The results of the one-component vapor adsorption equilibrium experiment show that ZIF-8-2-nIM-72h has the best adsorption separation coefficient at 293 K. The adsorption capacity of n HEX and 3-methylpentane (3 MP) were 211.63 mg/g and 33.91 mg/g, respectively. Compared with ZIF-8 (selectivity coefficient: 1.08), the adsorption selectivity coefficient of the modified material is greatly improved. The adsorption selectivity coefficient of n HEX/3 MP is 6.24 (ZIF-8-2-nIM-72h). ZIF-8 was modified by partly replacing the ligand 2-methylimidazole (2-mIM) with 2-nitroimidazole (2-nIM) using Vapor-Phase post-synthesis modification. Compared with ZIF-8, the adsorption selectivity of nHEX/3 MP over modified materials ZIF-8-2-nIM-X (X = 24h, 48h, 72h) was improved. • ZIF-8-2-nIM-X (X = 24h, 48h, 72h) material was prepared by Vapor-phase post-modification method. • ZIF-8-2-nIM-X (X = 24h, 48h, 72h) materials have larger specific surface areas than that of ZIF-8. • The adsorption selectivity coefficient of ZIF-8-2-nIM-72h for nHEX/3 MP is up to 6 times that of ZIF-8.

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Publication Details

Journal
Journal of Solid State Chemistry
Published
2024-12-28
DOI
https://doi.org/10.1016/j.jssc.2024.125168
Citations
3
Primary Topic
Metal-Organic Frameworks: Synthesis and Applications
Type
article
Field-Weighted Citation Impact
0.48

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article

The effective adsorption separation of n-hexane/3-methylpentane by vapor-phase linker exchange of Zeolitic-imidazolate framework ZIF-8

Jianjun Yin, Nan Zhang, Qun Chen, Le Chen et al.
3 citations
Journal of Solid State Chemistry
Metal-Organic Frameworks: Synthesis and Applications
0.48
article

The effective adsorption separation of n-hexane/3-methylpentane by vapor-phase linker exchange of Zeolitic-imidazolate framework ZIF-8

Jianjun Yin, Nan Zhang, Qun Chen, Le Chen, Zhi‐Hui Zhang, An Xie, Mingyang He
article en
3 citations

Abstract

Zeolitic-Imidazolate Framework 8 (ZIF-8), a porous crystalline absorbent, could be synthesized from the coordination reaction of zinc ions and 2-methylimidazole (2-mIM). ZIF-8 has a large specific surface area and a high adsorption capacity for n -hexane ( n HEX). However, ZIF-8 suffers from low selectivity for both linear and mono-chain alkanes. Therefore, ZIF-8 was modified through 2-mIM ligand being partly replaced by 2-nitroimidazole (2-nIM) through Vapor-Phase post-synthesis modification. The modified materials were denoted as ZIF-8-2-nIM-X (X = 24h, 48h, 72h). ZIF-8-2-nIM-X has a higher specific surface area and better thermal stability than ZIF-8. Further thermodynamic and kinetic calculations show that the affinity of hexane isomers on ZIF-8-2-nIM-X is spontaneous physical adsorption combined with an exothermic process. In contrast, kinetic studies show that the adsorption of hexane isomers on ZIF-8-2-nIM-X is a pseudo-second-order kinetic model. The batch and dynamic adsorption and separation properties of ZIF-8-2-nIM-X for hexane isomers were studied. The results of the one-component vapor adsorption equilibrium experiment show that ZIF-8-2-nIM-72h has the best adsorption separation coefficient at 293 K. The adsorption capacity of n HEX and 3-methylpentane (3 MP) were 211.63 mg/g and 33.91 mg/g, respectively. Compared with ZIF-8 (selectivity coefficient: 1.08), the adsorption selectivity coefficient of the modified material is greatly improved. The adsorption selectivity coefficient of n HEX/3 MP is 6.24 (ZIF-8-2-nIM-72h). ZIF-8 was modified by partly replacing the ligand 2-methylimidazole (2-mIM) with 2-nitroimidazole (2-nIM) using Vapor-Phase post-synthesis modification. Compared with ZIF-8, the adsorption selectivity of nHEX/3 MP over modified materials ZIF-8-2-nIM-X (X = 24h, 48h, 72h) was improved. • ZIF-8-2-nIM-X (X = 24h, 48h, 72h) material was prepared by Vapor-phase post-modification method. • ZIF-8-2-nIM-X (X = 24h, 48h, 72h) materials have larger specific surface areas than that of ZIF-8. • The adsorption selectivity coefficient of ZIF-8-2-nIM-72h for nHEX/3 MP is up to 6 times that of ZIF-8.

Journal of Solid State ChemistryVol. 343
Changzhou University (CN)
National Natural Science Foundation of China, Qinglan Project of Jiangsu Province of China, Jiangsu Key Laboratory of Advanced Catalytic Materials and Technology Department
Clean water and sanitation
Openalex Percentile: Top 41%
Metal-Organic Frameworks: Synthesis and Applications
0.48
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