Coke formation reduction in the cataltic reforming reactors at the optimal catalyst activity

Coke formation reduction in the cataltic reforming reactors at the optimal catalyst activity

Bibliographic Details
Parent link:Petroleum and Coal
Vol. 58, iss. 7.— 2016.— [P. 746-752]
Corporate Author: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Other Authors: Chernyakova E. S. Ekaterina Sergeevna, Ivanchina E. D. Emilia Dmitrievna, Yakupova I. V. Inna Vagizovna, Vinidiktova M. V. Margarita Vladimirovna, Seytenova G. Zh.
Summary:Title screen
Analysis of the catalyst operation effectiveness of the reforming process was conducted with mathematical modelling method using. The proposed method allows estimating the process unsteadiness bytaking adverse reactions and the formation of reversible and graphite coke into account. The main characteristics of two reforming catalysts were calculated and compared. The criterion of effectiveness determining the coke accumulation and selectivity for the given technological conditions was used as the comparative characteristic. It was found that the coke accumulations at the current and optimal activity operation are different, vary from 2.65 % mass. for Catalyst 2 to 3.40 % mass. for Catalyst 1 and depends on the raw material volume.
Published: 2016
Subjects:
электронный ресурс
труды учёных ТПУ
каталитический риформинг
коксообразование
математическое моделирование
катализаторы
Online Access:http://www.vurup.sk/sites/vurup.sk/files/downloads/pc_7_2016_chernyakova_xx.pdf
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654808

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