2020
DOI: 10.1002/app.50251
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Mechanochemically synthesized ZIF‐8 nanoparticles blended into 6FDA‐TrMPD membranes for C3H6/C3H8 separation

Abstract: The mixed matrix membranes (MMMs) consisting zeolitic‐imidazolate framework‐8 (ZIF‐8) nanoparticles in a polymer have been of considerable interest in separation applications. The fillers used are mostly synthesized using the solvothermal method. In this study, the ZIF‐8 nanoparticles were synthesized using a solvent‐less and salt‐free mechanochemical method and were added to 6FDA‐TrMPD polyimide to prepare MMMs. The single gas permeation of C3H6 and C3H8 through the MMMs was investigated. The C3H6 permeabilit… Show more

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Cited by 8 publications
(5 citation statements)
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“…[ 47 ] It is worth mentioning that good ZIF‐PIM compatibility and porous PIM‐1 endow ZIF‐8 86 ‐CN 14 @tPIM‐1 with top‐class selectivity among reported ZIF‐8 MMMs and most advanced permeability over the others (Figure 5c). [ 18–31 ] Another comparison with ZIF‐8 polycrystalline membranes shows that ZIF‐8 86 ‐CN 14 @tPIM‐1 has superior C 3 H 6 permeability and moderate competence in C 3 H 6 /C 3 H 8 selectivity (Table S5, Supporting Information). The selectivity–permeability points lie well above the latest upper bound, [ 48 ] and C 3 H 6 /C 3 H 8 selectivity (23.4) and C 3 H 8 permeance (≈22 GPU) are of the industrial interest for C 3 H 6 /C 3 H 8 separation from purge gas or olefin cracker according to selectivity and permeance requirements of 6–10/15–20 and 20–40 GPU.…”
Section: Resultsmentioning
confidence: 99%
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“…[ 47 ] It is worth mentioning that good ZIF‐PIM compatibility and porous PIM‐1 endow ZIF‐8 86 ‐CN 14 @tPIM‐1 with top‐class selectivity among reported ZIF‐8 MMMs and most advanced permeability over the others (Figure 5c). [ 18–31 ] Another comparison with ZIF‐8 polycrystalline membranes shows that ZIF‐8 86 ‐CN 14 @tPIM‐1 has superior C 3 H 6 permeability and moderate competence in C 3 H 6 /C 3 H 8 selectivity (Table S5, Supporting Information). The selectivity–permeability points lie well above the latest upper bound, [ 48 ] and C 3 H 6 /C 3 H 8 selectivity (23.4) and C 3 H 8 permeance (≈22 GPU) are of the industrial interest for C 3 H 6 /C 3 H 8 separation from purge gas or olefin cracker according to selectivity and permeance requirements of 6–10/15–20 and 20–40 GPU.…”
Section: Resultsmentioning
confidence: 99%
“…Minor decline in permeability and selectivity for C 3 H 6 from 1.5 bars to 3.0 bars are attributable to dual adsorption and competitive diffusion mechanisms respectively. [ 19 ] The membrane performance was examined against time in Figure 6d. High values in terms of permeability and selectivity are retained even after 7 days, signifying that the membrane is robust.…”
Section: Resultsmentioning
confidence: 99%
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“…Metal‐organic frameworks (MOFs) are emerging multifunctional materials consisting of metal ions/clusters bridged with organic linkers (via coordination bonds) 2–4 . They have been utilized in various fields, including material storage, 5 separation, 6 catalysis, 7 bioimaging, 8 drug delivery, 9 among many others. MOFs provide a number of benefits over conventional nanomaterials, including high surface areas, tunable pore size, improved degradation resistance, less time‐consuming and simpler surface modification capability.…”
Section: Introductionmentioning
confidence: 99%