2010
DOI: 10.1016/j.apcata.2010.03.015
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Peculiarities of oxidative coupling of methane in redox cyclic mode over Ag–La2O3/SiO2 catalysts

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Cited by 30 publications
(13 citation statements)
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“…If the oxygen diffusion rate is too slow, the oxygen in the bulk phase will have a minimal effect on the reaction. Various chemical composition and defective structures have been tested for their capacity to control the change in oxygen mobility, and hence, the reaction rate of the OCM reaction (Greish et al, 2010;Mestl et al, 2001;Sung et al, 2010). Chung et al investigated the performance of Manganese-based reducible metal oxides in the co-feed and the chemical looping schemes.…”
Section: Clocm Oxygen Carriersmentioning
confidence: 99%
“…If the oxygen diffusion rate is too slow, the oxygen in the bulk phase will have a minimal effect on the reaction. Various chemical composition and defective structures have been tested for their capacity to control the change in oxygen mobility, and hence, the reaction rate of the OCM reaction (Greish et al, 2010;Mestl et al, 2001;Sung et al, 2010). Chung et al investigated the performance of Manganese-based reducible metal oxides in the co-feed and the chemical looping schemes.…”
Section: Clocm Oxygen Carriersmentioning
confidence: 99%
“…Comparison of CLOCM systems on a C 2+ selectivity vs CH 4 conversion plot from the literature and this work. ,,,, …”
Section: Introductionmentioning
confidence: 99%
“…25−28 The higher C 2 yields are typically obtained from a highly dilute methane feed or an expensive COC composition. 26 At the commercial-scale, the addition of a diluent gas may not be practical as it imposes both an energy and capital cost for separations from an already dilute product stream while an expensive COC will increase operating costs. 29 A commercially suitable COC has three major desirable characteristics.…”
Section: ■ Introductionmentioning
confidence: 99%
“…In redox OCM, C 2 yields between 20% and 30% have been obtained. Figure shows a summary of redox OCM results. The higher C 2 yields are typically obtained from a highly dilute methane feed or an expensive COC composition . At the commercial-scale, the addition of a diluent gas may not be practical as it imposes both an energy and capital cost for separations from an already dilute product stream while an expensive COC will increase operating costs…”
Section: Introductionmentioning
confidence: 99%