2021
DOI: 10.1002/aic.17249
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Simultaneously upgrading CO2 and light alkanes into value‐added products

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Cited by 18 publications
(9 citation statements)
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“…[2][3][4][5][6] One promising route is the utilization of light alkanes to directly activate CO 2 to value-added products, such as syngas, olefins, aromatics and oxygenates. [7][8][9][10] The recent shale gas boom has significantly increased the supply of light alkanes, with the fraction of ethane (C 2 H 6 ) being up to 10 vol%. 11 Therefore, the catalytic reactions between CO 2 and C 2 H 6 provide a promising strategy to simultaneously reduce the greenhouse gas emissions and upgrade the underutilized C 2 H 6 to important industrial chemicals.…”
Section: Introductionmentioning
confidence: 99%
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“…[2][3][4][5][6] One promising route is the utilization of light alkanes to directly activate CO 2 to value-added products, such as syngas, olefins, aromatics and oxygenates. [7][8][9][10] The recent shale gas boom has significantly increased the supply of light alkanes, with the fraction of ethane (C 2 H 6 ) being up to 10 vol%. 11 Therefore, the catalytic reactions between CO 2 and C 2 H 6 provide a promising strategy to simultaneously reduce the greenhouse gas emissions and upgrade the underutilized C 2 H 6 to important industrial chemicals.…”
Section: Introductionmentioning
confidence: 99%
“…Depending on the selective bond cleavage of C 2 H 6 , there are mainly two pathways, i.e., dry reforming of ethane (DRE) to produce syngas (C 2 H 6 + 2CO 2 -4CO + 3H 2 ) via C-C and C-H bond cleavage and oxidative dehydrogenation of ethane (ODHE) to produce ethylene (C 2 H 6 + CO 2 -C 2 H 4 + CO + H 2 O) via selective C-H bond session while protecting the C-C bond. [7][8][9][10] Bimetallic-derived catalysts, either in the metallic or oxidized form, typically feature distinct catalytic properties and are often superior to those of either monometallic component due to the ligand, ensemble and strain effects. 12 A number of bimetallic-derived catalysts have been used for the reactions of C 2 H 6 with CO 2 , such as Co-Mo, 13 Ni-Mo, 13 Ni-Al, 14,15 Ni-Fe, 13,16,17 Pt-Co, 13 Pt-Ni, 18,19 Pt-Ga, 20 Pt-Ce, 21 Pt-In, 20 Pt-Sn, 22 Pd-Fe, 23 Pd-Co 24 and Pd-In.…”
Section: Introductionmentioning
confidence: 99%
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“…[19] More catalyst and process development are needed to increase the propylene yield to make this approach commercially viable. There are several reviews that compare nonoxidative PDH and ODPH processes, [5,8,9,16,[19][20][21][22] and the rest of this article will focus on the catalyst development in non-oxidative PDH.…”
Section: Introduction 1backgroundmentioning
confidence: 99%
“…Environmental issues stemming from the overreliance on fossil fuels have led to an urgent demand for renewable fuel sources, with hydrogen (H 2 ) being a particularly promising candidate. However, most of the commercial methods to produce H 2 involve thermochemical processes centered around the steam methane reforming reaction and water–gas shift reaction . These methods result in the production of undesired byproducts such as CO and CO 2 , thereby offsetting the environmental friendliness provided by H 2 .…”
Section: Introductionmentioning
confidence: 99%