2017
DOI: 10.1039/c7cc03529b
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Efficient kinetic separation of propene and propane using two microporous metal organic frameworks

Abstract: An excellent performance for the kinetic separation of propene and propane is realized in two microporous MOF analogues, namely Zn(ox)(trz) and Zn(ox)(atrz). The great difference in diffusivity of propane and propene in Zn(ox)(trz) at 323 K results in a kinetic separation factor of 1565, marking the highest value among all MOFs reported for kinetic separation of the two hydrocarbon species. The high selectivity is attributed primarily to the appropriate pore apertures.

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Cited by 97 publications
(60 citation statements)
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“…[2] Thes eparation of C 3 H 6 /C 3 H 8 mixtures is performed by distillation at high pressure (20 bar). Due to the close-lying boiling points of C 3 H 6 (226 K) and C 3 H 8 (231 K), [3] their relative volatility is very small (1.09-1.15) [4] and the distillation column should have av ery large number of theoretical trays (180 +) [5] and be operated at very high reflux ratios (12)(13)(14)(15)(16)(17)(18)(19)(20), [6] resulting in huge energy consumption. [1] Without phase change,the energy requirement of adsorptive separation is much lower than distillation.…”
Section: Asoneofthemostimportantchemicalsinchemicalindustrymentioning
confidence: 99%
“…[2] Thes eparation of C 3 H 6 /C 3 H 8 mixtures is performed by distillation at high pressure (20 bar). Due to the close-lying boiling points of C 3 H 6 (226 K) and C 3 H 8 (231 K), [3] their relative volatility is very small (1.09-1.15) [4] and the distillation column should have av ery large number of theoretical trays (180 +) [5] and be operated at very high reflux ratios (12)(13)(14)(15)(16)(17)(18)(19)(20), [6] resulting in huge energy consumption. [1] Without phase change,the energy requirement of adsorptive separation is much lower than distillation.…”
Section: Asoneofthemostimportantchemicalsinchemicalindustrymentioning
confidence: 99%
“…[5] Af ew other MOFs with appropriate pore aperture sizes were considered as promising candidates for the kinetic separation of the two hydrocarbon species.T hey showed equally great interest for achieving high permeation selectivity when incorporated in membranes. [8][9][10] In particular, the zeolitic imidazolate framework-8 (ZIF-8) was revealed as ap romising MOF for such ak inetic control of the separation. [11][12][13][14] Many approaches have recently been considered, such as linker exchange,metal substitution, and configuration optimization, to enhance the C 3 H 6 /C 3 H 8 diffusion selectivity achieved by ZIF-8 derivatives.…”
Section: Bin Zheng and Guillaume Maurin*mentioning
confidence: 99%
“…On the other hand, in the case of propane/propylene separation, where the removal of a single olefin from its corresponding paraffin is needed, kinetically driven separation often proves to be more suitable and efficient . A number of adsorbents have been reported to undergo kinetic separation toward propane and propylene . Compared to conventional adsorbents, the MOF pore size can be tuned much more readily to achieve significantly improved performance for kinetic separation of the two C3 molecules, as demonstrated in several recent studies .…”
mentioning
confidence: 99%