Kinetic model of the catalytic reforming of gasolines in moving-bed reactors; Catalysis in Industry; Vol. 2, iss. 4

Kinetic model of the catalytic reforming of gasolines in moving-bed reactors; Catalysis in Industry; Vol. 2, iss. 4

Bibliographic Details
Parent link:Catalysis in Industry: Scientific Journal
Vol. 2, iss. 4.— 2010.— [P. 374-380]
Other Authors: Gyngazova M. S. Mariya Sergeevna, Kravtsov A. V. Anatoly Vasilyevich, Ivanchina E. D. Emilia Dmitrievna, Korolenko M. V. Mikhail Vladimirovich, Uvarkina D. D.
Summary:Title screen
A mathematical model of the catalytic reforming of gasolines in a reactor with continuous catalyst regeneration is proposed. The model takes into account the motion of the catalyst, changes in its activity along the bed height, and the dependence of its activity on the circulation ratio. The kinetic parameters of the Pt-Sn catalyst are determined under operational conditions by solving the inverse kinetic problem. The composition of the reformate component as calculated by the model coincides with the experimental data within the accuracy of chromatographic analysis. The proposed model is invariant to the composition of raw materials and can be used for predictive calculations.
Режим доступа: по договору с организацией-держателем ресурса
Language:English
Published: 2010
Subjects:
электронный ресурс
труды учёных ТПУ
каталитический риформинг
бензины
модели
реакторы
Online Access:http://dx.doi.org/10.1134/S2070050410040124
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655719

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