Mathematical Modeling of the Unsteady Hydrocarbon Pyrolysis Process


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Mathematical modeling of the hydrocarbon (HC) pyrolysis kinetics has been performed using the propane–butane fraction as feedstock. The calculated data have been compared with the results of the examination of industrial pyrolysis furnaces after operation with a significant sporadic change in the feedstock composition. The mathematical model has been adapted to the operation of the real pyrolysis furnace. The adequacy of the adapted mathematical model and its suitability for the operational control of the pyrolysis process have been proved. Regression equations have been obtained for the subsequent use in automatic process control systems.

作者简介

F. Samedov

Ufa State Oil Technical University

Email: agidel@ufanet.ru
俄罗斯联邦, Ufa, Bashkortostan

A. Morozov

Ufa State Oil Technical University

Email: agidel@ufanet.ru
俄罗斯联邦, Ufa, Bashkortostan

N. Samoilov

Ufa State Oil Technical University

编辑信件的主要联系方式.
Email: naum.samoilow@yandex.ru
俄罗斯联邦, Ufa, Bashkortostan

T. Prosochkina

Ufa State Oil Technical University

编辑信件的主要联系方式.
Email: agidel@ufanet.ru
俄罗斯联邦, Ufa, Bashkortostan

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