Selective Ethane/Ethylene Separation in a Robust Microporous Hydrogen-Bonded Organic Framework

The separation of ethane (C2H6) from ethylene (C2H4) is of prime importance in the production of polymer-grade C2H4 for industrial manufacturing. It is very challenging and still remains unexploited to fully realize efficient C2H6/C2H4 separation in the emerging hydrogen-bonded organic frameworks (H...

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Published inJournal of the American Chemical Society Vol. 142; no. 1; pp. 633 - 640
Main Authors Zhang, Xu, Li, Libo, Wang, Jia-Xin, Wen, Hui-Min, Krishna, Rajamani, Wu, Hui, Zhou, Wei, Chen, Zhong-Ning, Li, Bin, Qian, Guodong, Chen, Banglin
Format Journal Article
LanguageEnglish
Published United States American Chemical Society 08.01.2020
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Summary:The separation of ethane (C2H6) from ethylene (C2H4) is of prime importance in the production of polymer-grade C2H4 for industrial manufacturing. It is very challenging and still remains unexploited to fully realize efficient C2H6/C2H4 separation in the emerging hydrogen-bonded organic frameworks (HOFs) due to the weak nature of hydrogen bonds. We herein report the benchmark example of a novel ultrarobust HOF adsorbent (termed as HOF-76a) with a Brunauer–Emmett–Teller surface area exceeding 1100 m2 g–1, exhibiting the preferential binding of C2H6 over C2H4 and thus highly selective separation of C2H6/C2H4. Theoretical calculations indicate the key role of the nonpolar surface and the suitable triangular channel-like pores in HOF-76a to sterically “match” better with the nonplanar C2H6 molecule than the planar C2H4, thus affording overall stronger multipoint van der Waals interactions with C2H6. The exceptional separation performance of HOF-76a for C2H6/C2H4 separation was clearly demonstrated by gas adsorption isotherms, ideal adsorbed solution theory calculations, and simulated and experimental breakthrough curves. Breakthrough experiments on HOF-76a reveal that polymer-grade ethylene gas can be straightforwardly produced from 50/50 (v/v) C2H6/C2H4 mixtures during the first adsorption cycle with a high productivity of 7.2 L/kg at 298 K and 1.01 bar and 18.8 L/kg at 298 K and 5.0 bar, respectively.
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ISSN:0002-7863
1520-5126
DOI:10.1021/jacs.9b12428