2013
DOI: 10.1016/j.memsci.2012.11.013
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Mixed matrix membranes containing MOFs for ethylene/ethane separation—Part B: Effect of Cu3BTC2 on membrane transport properties

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Cited by 62 publications
(31 citation statements)
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“…Nanocrystal HKUST-1 was incorporated into two glassy polymers, namely ODPA-TMPDA and 6FDA-TMPDA (The abbreviations of these polymers will be explained in Section 2.1). These polymers were selected for its higher C 2 H 4 permeability as compared to commercially available glassy polymers (e.g., Matrimid ® , polysulfone, and Ultem ® /P84) [32,33,51,52]. Our results showed that, with the addition of HKUST-1 nanocrystals, a clear improvement in C 2 H 4 permeability of the membranes can be observed.…”
Section: Introductionmentioning
confidence: 88%
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“…Nanocrystal HKUST-1 was incorporated into two glassy polymers, namely ODPA-TMPDA and 6FDA-TMPDA (The abbreviations of these polymers will be explained in Section 2.1). These polymers were selected for its higher C 2 H 4 permeability as compared to commercially available glassy polymers (e.g., Matrimid ® , polysulfone, and Ultem ® /P84) [32,33,51,52]. Our results showed that, with the addition of HKUST-1 nanocrystals, a clear improvement in C 2 H 4 permeability of the membranes can be observed.…”
Section: Introductionmentioning
confidence: 88%
“…Apart from this, inorganic membranes, such as those based on pure zeolites and metal-organic frameworks (MOFs), are typically high-performing but hampered by their poor scalability potential [30]. Beyond membrane performances, other real-life challenges, such as effects of high temperatures and pressures, presence of moisture in the feed gas and impurities such as H 2 S that are damaging to the membranes, must be addressed to realize industrial applications [31][32][33][34][35][36][37]. However, in this work, our aim is to develop mixed-matrix membranes, which amalgamate the merits of both polymeric and inorganic membranes, to achieve enhanced C 2 H 4 /C 2 H 6 separation.…”
Section: Introductionmentioning
confidence: 99%
“…It originated from the partial decomposition of MOF-199 at higher concentration, which would be verified later. [35] The cross-sectional structures of the membranes are shown in Figure 3. The pristine PVDF membrane, M0, possessed typical asymmetric structure of finger-like sublayer on the top and sponge-like structure on the bottom (Figure 3a), [36] and the composite membrane, M3, showed the similar structure compared with M0 ( Figure 3b).…”
Section: Membrane Morphologymentioning
confidence: 99%
“…In the petrochemical, natural gas, and fuel industry [1,2], for example, the purification of commodity gases, like propane, propylene, hydrogen, methane, and ammonia, is vital for the production of other goods like fuels (e.g., propane, hydrogen, methane) [3][4][5][6][7][8][9][10][11], polymers (e.g., polypropylene from propylene) [12][13][14][15], and fertilizers (e.g., ammonium salts) [16,17]. Recently, environmental applications for gas separations have also been explored mainly for the capture and sequestration of carbon dioxide from the burning and gasification of coal in the generation of electricity and the production of hydrogen [18][19][20].…”
Section: Introductionmentioning
confidence: 99%
“…A variety of industrial, energy, and environmental membrane-based gas separation applications have been targeted, some already at the industrial scale. Separations such as H2/N2, H2/CO2, He/H2, CH4/CO2, N2/CO2, O2/N2, NH3/H2/N2, N2/CH4, C3H6/C3H8 [11], C3H8/N2 [5], C3H6/C3H8/N2 [12], and C2H4/C2H6 [8,9], and other organic vapors are some examples of where membranes could be employed to provide a cost effective separation process [51,52]. Owing to the nature of membranes as barrier materials, the operating conditions required in industry to separate a particular gas mixture impose constraints and challenges on the materials and manufacturing processes required for a membrane to be successfully used in industry.…”
Section: Introductionmentioning
confidence: 99%