Modelling of the decomposition of methane at 1273 K in a plug flow reactor at low conversion
Identifieur interne : 002880 ( Main/Exploration ); précédent : 002879; suivant : 002881Modelling of the decomposition of methane at 1273 K in a plug flow reactor at low conversion
Auteurs : O. Olsvik [Norvège] ; F. Billaud [France]Source :
- Journal of Analytical and Applied Pyrolysis [ 0165-2370 ] ; 1993.
Descripteurs français
- Pascal (Inist)
- Wicri :
- topic : Hydrocarbure, Simulation.
English descriptors
- KwdEn :
- Anal, Appl, Autocatalysis, Autocatalysis effect, Billaud, Chem, Decomposition rate, Ethane, Experimental data, Experimental residence time, Feed composition, Financial support, Good agreement, Higher temperatures, Hydrocarbon, Important reactions, Kinetic parameters, Main compounds, Maximal temperature, Maximum temperature, Methane, Methane conversion, Olsvik, Plug flow reactor, Present work, Production rate coefficients, Pyrolysis, Radical mechanism, Radical reactions, Rate acceleration, Rate constants, Reaction mechanisms, Reactor tube, Residence time, Residence times, Sensitivity analysis, Sharp increase, Simulation, Simulation temperature, Temperature range.
- Teeft :
- Anal, Appl, Autocatalysis, Autocatalysis effect, Billaud, Chem, Decomposition rate, Ethane, Experimental data, Experimental residence time, Feed composition, Financial support, Good agreement, Higher temperatures, Important reactions, Kinetic parameters, Main compounds, Maximal temperature, Maximum temperature, Methane, Methane conversion, Olsvik, Plug flow reactor, Present work, Production rate coefficients, Pyrolysis, Radical reactions, Rate acceleration, Rate constants, Reaction mechanisms, Reactor tube, Residence time, Residence times, Sensitivity analysis, Sharp increase, Simulation, Simulation temperature, Temperature range.
Abstract
Abstract: The thermal decomposition of methane was investigated in a plug flow reactor at 1273 K and 1 bar. The methane feed was diluted with helium (He:CH4 = 2:1). The study was carried out at low conversion of methane ( <1%). A mechanistic simulation model was developed. The kinetic scheme consists of 35 reversible free radical reactions and one irreversible free radical reaction. The model explains the formation and consumption of CH4, C2H6, C2H4, C2H2, C3H6, a-C3H4, (allene) and p-C3H4 (propyne). A sensitivity analysis was performed to find the main free radical reactions in the formation and consumption of the reported products. The autocatalysis phenomenon in the decomposition of methane was studied and no such effect was observed.
Url:
DOI: 10.1016/0165-2370(93)80058-8
Affiliations:
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Le document en format XML
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<term>Billaud</term>
<term>Chem</term>
<term>Decomposition rate</term>
<term>Ethane</term>
<term>Experimental data</term>
<term>Experimental residence time</term>
<term>Feed composition</term>
<term>Financial support</term>
<term>Good agreement</term>
<term>Higher temperatures</term>
<term>Hydrocarbon</term>
<term>Important reactions</term>
<term>Kinetic parameters</term>
<term>Main compounds</term>
<term>Maximal temperature</term>
<term>Maximum temperature</term>
<term>Methane</term>
<term>Methane conversion</term>
<term>Olsvik</term>
<term>Plug flow reactor</term>
<term>Present work</term>
<term>Production rate coefficients</term>
<term>Pyrolysis</term>
<term>Radical mechanism</term>
<term>Radical reactions</term>
<term>Rate acceleration</term>
<term>Rate constants</term>
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<term>Experimental residence time</term>
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<term>Good agreement</term>
<term>Higher temperatures</term>
<term>Important reactions</term>
<term>Kinetic parameters</term>
<term>Main compounds</term>
<term>Maximal temperature</term>
<term>Maximum temperature</term>
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<term>Methane conversion</term>
<term>Olsvik</term>
<term>Plug flow reactor</term>
<term>Present work</term>
<term>Production rate coefficients</term>
<term>Pyrolysis</term>
<term>Radical reactions</term>
<term>Rate acceleration</term>
<term>Rate constants</term>
<term>Reaction mechanisms</term>
<term>Reactor tube</term>
<term>Residence time</term>
<term>Residence times</term>
<term>Sensitivity analysis</term>
<term>Sharp increase</term>
<term>Simulation</term>
<term>Simulation temperature</term>
<term>Temperature range</term>
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<front><div type="abstract" xml:lang="en">Abstract: The thermal decomposition of methane was investigated in a plug flow reactor at 1273 K and 1 bar. The methane feed was diluted with helium (He:CH4 = 2:1). The study was carried out at low conversion of methane ( <1%). A mechanistic simulation model was developed. The kinetic scheme consists of 35 reversible free radical reactions and one irreversible free radical reaction. The model explains the formation and consumption of CH4, C2H6, C2H4, C2H2, C3H6, a-C3H4, (allene) and p-C3H4 (propyne). A sensitivity analysis was performed to find the main free radical reactions in the formation and consumption of the reported products. The autocatalysis phenomenon in the decomposition of methane was studied and no such effect was observed.</div>
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