2019
DOI: 10.1039/c9ta02822f
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Pore environment engineering in metal–organic frameworks for efficient ethane/ethylene separation

Abstract: Methyl groups are introduced on the pore walls of a metal–organic framework to enhance the separation performance of C2H6/C2H4.

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Cited by 96 publications
(71 citation statements)
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References 51 publications
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“…Pore width [c] []S O 2 uptake (293 K) [mmol g À1 ]a t: SO 2 /CO 2 selectivity [d] at SO 2 /CO 2 molar ratio: 0.01 bar 0.1 bar 0.97 bar 0.01 0.1 0.5 DMOF [37] 2050 [39] /-0.80 [39] /-7.5, 5.6 6.9 [37][e] --9.97 (298) [17] - [39] 894 [39] /-0.39 [39] /-4.5 [39][e] --% 4.9 (298) [25] --- Angewandte Chemie (3.0 mmol g À1 ), and is only slightly lower than that of SIFSIX-2-Cu-i (4.16 mmol g À1 ) [31,40] and MIL-160 (4.2 mmol g À1 ). [31] Thel atter two feature polar groups (SiF 6 2À and af uran ring, respectively) together with optimal micropore widths of approximately % 5 (see below).…”
Section: Methodsmentioning
confidence: 99%
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“…Pore width [c] []S O 2 uptake (293 K) [mmol g À1 ]a t: SO 2 /CO 2 selectivity [d] at SO 2 /CO 2 molar ratio: 0.01 bar 0.1 bar 0.97 bar 0.01 0.1 0.5 DMOF [37] 2050 [39] /-0.80 [39] /-7.5, 5.6 6.9 [37][e] --9.97 (298) [17] - [39] 894 [39] /-0.39 [39] /-4.5 [39][e] --% 4.9 (298) [25] --- Angewandte Chemie (3.0 mmol g À1 ), and is only slightly lower than that of SIFSIX-2-Cu-i (4.16 mmol g À1 ) [31,40] and MIL-160 (4.2 mmol g À1 ). [31] Thel atter two feature polar groups (SiF 6 2À and af uran ring, respectively) together with optimal micropore widths of approximately % 5 (see below).…”
Section: Methodsmentioning
confidence: 99%
“… [37, 38] DMOFs with different metals and linkers, mixed metals, and mixed linkers, including BDC‐TM and Ni‐DMOF‐TM, were recently tested for SO 2 sorption with the focus on stability in humid conditions [25] . The addition of methyl groups to the BDC linker yields isostructural DMOFs [39] . The increased density of methyl groups in methyl‐functionalized DMOF‐X (X represents M, DM, and TM) is then correlated with the SO 2 adsorption and separation properties.…”
Section: Introductionmentioning
confidence: 99%
“…Various porous materials, such as activated carbons, [8] silica [9] and metal‐organic frameworks (MOFs), [3, 10–19] have been studied for the adsorptive separation of C 2 H 2 /CO 2 . MOFs attracted particular attention because of their abundant structural diversity and design flexibility [20–24] . Zeolites, as conventional sorbent materials, [25, 26] are potentially superior to MOFs for gas separations at an industrial scale owing to their high hydrothermal stability, recyclability and low production cost.…”
Section: Introductionmentioning
confidence: 99%
“…[4][5][6][7] Va rious porous materials,s uch as activated carbons, [8] silica [9] and metal-organic frameworks (MOFs), [3,[10][11][12][13][14][15][16][17][18][19] have been studied for the adsorptive separation of C 2 H 2 /CO 2 .M OFs attracted particular attention because of their abundant structural diversity and design flexibility. [20][21][22][23][24] Zeolites,a sc onventional sorbent materials, [25,26] are potentially superior to MOFs for gas separations at an industrial scale owing to their high hydrothermal stability,recyclability and low production cost. However,the separation of mixtures of C 2 H 2 /CO 2 in zeolites has not been achieved to date because physisorption of C 2 H 2 and CO 2 within pristine zeolites often exhibits similar uptakes and adsorption profiles,l eading to no apparent selectivity to afford any practical separation.…”
Section: Introductionmentioning
confidence: 99%