2020
DOI: 10.1016/s1872-2067(20)63544-6
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Chemical looping partial oxidation over FeWO /SiO2 catalysts

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Cited by 28 publications
(9 citation statements)
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“…An extensively investigated topics is methane to syngas/H 2 conversion. 95,[109][110][111][112][113][114][115][116][117]123,[125][126][127]130,136,185,[193][194][195][196][197][198][199][200][201][202][203][204][205][206][207][208] A few other studies explored a phase transition sorbent concept where a single mixed oxide particle combines the function of a redox oxide (for oxygen separation), a carbonate sorbent (for CO 2 separation), and a catalyst (to catalyze chemical reactions). 95,123,130,197,198,[209][210][211] For instance, a recent study adopted the chemical looping strategy to selectively oxidize ammonia with excellent NO selectivity for nitric acid production.…”
Section: Discussionmentioning
confidence: 99%
“…An extensively investigated topics is methane to syngas/H 2 conversion. 95,[109][110][111][112][113][114][115][116][117]123,[125][126][127]130,136,185,[193][194][195][196][197][198][199][200][201][202][203][204][205][206][207][208] A few other studies explored a phase transition sorbent concept where a single mixed oxide particle combines the function of a redox oxide (for oxygen separation), a carbonate sorbent (for CO 2 separation), and a catalyst (to catalyze chemical reactions). 95,123,130,197,198,[209][210][211] For instance, a recent study adopted the chemical looping strategy to selectively oxidize ammonia with excellent NO selectivity for nitric acid production.…”
Section: Discussionmentioning
confidence: 99%
“…Another way to improve the catalytic performance is to incorporate the active sites into the specific composite metal oxide structure. , Generally, the composite metal oxides are a mixture of multiple metal oxides with specific crystal structure. , Thus, they could provide various kinds of active sites to achieve high catalytic performance. Gong and co-workers described the design of an FeWO x -based oxygen carrier for partial chemical reforming in Figure a . Thermodynamic screening and kinetic analyses showed that total methane conversion and syngas yield could be increased dramatically compared to the unmodified WO 3 /SiO 2 , thereby enabling chemical looping of partial oxidation of methane (CLPOM) with 62% methane conversion, 93% CO gas phase selectivity, and 94% H 2 selectivity.…”
Section: Transport Phenomena In Structured Catalystsmentioning
confidence: 99%
“…Gong and co-workers described the design of an FeWO x - based oxygen carrier for partial chemical reforming in Figure 26a. 299 Thermodynamic screening and kinetic analyses showed that total methane conversion and syngas yield could be increased dramatically compared to the unmodified WO 3 /SiO 2 , thereby enabling chemical looping of partial oxidation of methane (CLPOM) with 62% methane conversion, 93% CO gas phase selectivity, and 94% H 2 selectivity. Moreover, FeWO x / SiO 2 demonstrated excellent catalytic performance without catalyst deactivation at 900 °C.…”
Section: Mixed Metal Oxidesmentioning
confidence: 99%
“…However, its performance and structure gradually changed during ten cycles, which needed further improvement on the stability. In order to improve the activity of the tungsten oxide oxygen carrier and maintain the structural stability of the oxygen carrier during cycling, Liu et al [206] prepared the Fe y WO x /SiO 2 oxygen carrier and applied it to CLR. The addition of iron greatly improved the performance of the oxygen carrier, and during the reduction process, the strong interaction between iron and tungsten resulted in the formation of the iron-tungsten alloy so that no phase separation occurred, ensuring structural stability.…”
Section: Other Oxygen Carriermentioning
confidence: 99%