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AUTHOR(S): Salim Asadov, Ali Akhundov, Dilgam Tagiyev
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ABSTRACT The technology of hydrocarbon processing, in addition to methane, also implies the involvement in the processing of its higher homologues - hydrocarbons. Currently, non-oxidative methods are being developed for gas feedstock processing, including their dehydrogenation to olefins. Technological schemes for the process of oxidative dehydrogenation of hydrocarbons are diverse and depend on the method of carrying out the process - continuous or periodic. This article presents the results of the development of modeling and determining the optimal parameters of the catalytic continuous processing of hydrocarbons on the example of oxidative dehydrogenation. On the basis of the constructed mathematical model of the kinetics of the process of oxidative dehydrogenation of hydrocarbons, the problem was solved by constructing a theoretically optimal temperature profile. Our laboratory data on the oxidative dehydrogenation of n-butane to divinyl and isopentane to isoprene were used as initial data when choosing a model, constructing an algorithm and calculations. This made it possible to identify the optimal regions of the regime parameters of the studied processes. |
KEYWORDS mathematical model, catalytic process, hydrocarbon processing, optimal parameters |
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Cite this paper Salim Asadov, Ali Akhundov, Dilgam Tagiyev. (2019) Mathematical Modeling of the Hardware Design of the Catalytic Process of Hydrocarbon Processing at the Design Stage. International Journal of Chemistry and Chemical Engineering Systems, 4, 28-31 |
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