1994
DOI: 10.1002/aic.690400313
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Effect of pressure on the oxidative coupling of methane in the absence of catalyst

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1994
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Cited by 54 publications
(66 citation statements)
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“…Ethene is not detected at 1000 Pa since the formation also has to occur in the gas phase by involvement of dioxygen. The direct decomposition of ethyl radicals toward ethene can be ruled out at pressures of 1000 Pa (54). Hence, as a result of the low pressures the yield of C 2 products is less than 1% in the present study and the experimental data obtained with methane pulses will provide information on the generation of methyl radicals rather than on the global coupling reaction.…”
Section: Reaction Mechanismmentioning
confidence: 67%
“…Ethene is not detected at 1000 Pa since the formation also has to occur in the gas phase by involvement of dioxygen. The direct decomposition of ethyl radicals toward ethene can be ruled out at pressures of 1000 Pa (54). Hence, as a result of the low pressures the yield of C 2 products is less than 1% in the present study and the experimental data obtained with methane pulses will provide information on the generation of methyl radicals rather than on the global coupling reaction.…”
Section: Reaction Mechanismmentioning
confidence: 67%
“…This phenomenon is related to the branched chain nature of the reaction mechanism [ 61 as will be shown using the model in Table 1. This model is based on the model from Chen et al [4] with some small modifications that allowed an adequate simulation of the experiments with cofeeding of ethane. It should be noted, however, that these modifications do not significantly alter the simulation results reported in [ 41.…”
Section: Methodsmentioning
confidence: 99%
“…The experimental reactor was designed such that mass-transport and mass-transfer limitations for the reactants and the products were negligible. The way of calculating the conversions, selectivities, and yields is similar to Chen et al (1994a).…”
Section: Methodsmentioning
confidence: 99%
“…The setup used for the kinetic experiments in this study has been described previously by Chen et al (1994a) for the measurement of the kinetics in the absence of catalyst. For the present study a continuousflow, sintered R-Al 2 O 3 tubular reactor with a length of 650 mm, an external diameter of 12 mm, and an internal diameter of 8 mm was used.…”
Section: Methodsmentioning
confidence: 99%
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