2008
DOI: 10.1016/j.ces.2008.07.010
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Catalytic vapour phase epoxidation of propene with nitrous oxide as an oxidant II. Development of a kinetic model

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Cited by 3 publications
(7 citation statements)
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“…The maximum value for S P is 0.43, indicating that a maximum selectivity to PO of 43% at almost zero conversion can be obtained. As mentioned before, , this comparably low selectivity is a result of the parallel and consecutive formation of coke and higher molecular weight products, which are formed with selectivities between 50 and 80%. Product stability reached a maximum value of 0.21 for the sample Fe1.0Cs2.4ex.…”
Section: Resultsmentioning
confidence: 71%
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“…The maximum value for S P is 0.43, indicating that a maximum selectivity to PO of 43% at almost zero conversion can be obtained. As mentioned before, , this comparably low selectivity is a result of the parallel and consecutive formation of coke and higher molecular weight products, which are formed with selectivities between 50 and 80%. Product stability reached a maximum value of 0.21 for the sample Fe1.0Cs2.4ex.…”
Section: Resultsmentioning
confidence: 71%
“…Previous studies with a catalyst containing 0.1 wt % Fe and 0.2 wt % Cs on SiO 2 revealed that low propene concentrations (1 vol %) and a surplus of N 2 O (15 vol %, rest: He) are necessary for high PO selectivities. , The product spectrum is known to a large extent, and a detailed reaction network was postulated, which provided a basis for the development of a kinetic model . The current study continues these investigations and is divided in two parts: In the first part, it will be shown how preparation and physicochemical characteristics (e.g., iron and alkaline content and calcination temperature) affect catalytic properties of the CsO x /FeO y /SiO 2 catalyst in the propene epoxidation using N 2 O as oxidant.…”
Section: Introductionmentioning
confidence: 77%
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“…According to Lifshitz and Tamburu [34] the formation of PA and ACT as a result of PO isomerization is a simple process involving C-O rapture and hydrogen shift. However, according to Thömmas et al [35] a very high rate of PA conversion, especially in the presence of N 2 O, results in a lowering of the PA contribution in the oxidation product. Taking into account the high concentration of the active centers on V/MCF catalysts it is possible to explain the low selectivity to PA in propene oxidation recorded on the studied samples, especially with higher vanadium concentration.…”
Section: Discussionmentioning
confidence: 99%