2015
DOI: 10.1016/j.cattod.2015.03.011
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Catalytic nonthermal plasma assisted co-processing of methane and nitrous oxide for methanol production

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Cited by 21 publications
(9 citation statements)
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References 43 publications
(58 reference statements)
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“…That means at high temperatures, the methanol is more reactive than methane, which might lead to the decomposition of methanol to low grade product [52,[54][55][56]. In addition, the gas phase homogeneous is a free radical reaction, which means that it is difficult to control the process on the large scale [51,54,57].…”
Section: Challenges In Technologies For the Conventional Methodsmentioning
confidence: 99%
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“…That means at high temperatures, the methanol is more reactive than methane, which might lead to the decomposition of methanol to low grade product [52,[54][55][56]. In addition, the gas phase homogeneous is a free radical reaction, which means that it is difficult to control the process on the large scale [51,54,57].…”
Section: Challenges In Technologies For the Conventional Methodsmentioning
confidence: 99%
“…The non-thermal plasma can be developed by integrating the reactor with catalyst to improve the activity and selectivity of methane oxidation. In a recent study, the Cu-doped Ni was loaded on CeO 2 , which led to enhance the selectivity of methanol until 36% [65]. In another study, multicomponent catalysts were combined with plasma in two different approaches, in-plasma catalysis (IPC) and post-plasma catalysis (PPC), for achieving high levels in both methane conversion and aimed methanol selectivity through the synergetic effect of the…”
Section: Unconventional Approach To Convert Methane To Oxygenates 31mentioning
confidence: 99%
“…Co-processing of CH 4 and nitrous oxide into high-value products, like CH 3 OH, CH 2 O, etc., was attempted in plasma under ambient conditions [121][122][123]136]. In a DBD reactor, it was observed that the mole ratio of CH 4 /N 2 O significantly affected the conversion and the product selectivity, and the highest selectivity (28%) of CH 3 OH could be realized at 5:1 CH 4 /N 2 O mole ratio, decreasing to 23% and 13%, respectively, for 1: 1 and 1: 5 ratios.…”
Section: Nitrous Oxide As An Oxidantmentioning
confidence: 99%
“…In order to improve the selectivity to CH 3 OH, CuO(10%)/CeO 2 , NiO(10%)/CeO 2 and Cu-Ni(5-5%)/CeO 2 catalysts were packed in a DBD reactor [122]. The catalytic activity followed the order of CuO-NiO/CeO 2 > NiO/CeO 2 > CuO/CeO 2 , with the best CH 3 OH selectivity of ∼36% on NiO/CeO 2 catalyst.…”
Section: Nitrous Oxide As An Oxidantmentioning
confidence: 99%
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