Coke formation reduction in the cataltic reforming reactors at the optimal catalyst activity; Petroleum and Coal; Vol. 58, iss. 7

Detalhes bibliográficos
Parent link:Petroleum and Coal
Vol. 58, iss. 7.— 2016.— [P. 746-752]
Autor Corporativo: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Outros Autores: Chernyakova E. S. Ekaterina Sergeevna, Ivanchina E. D. Emilia Dmitrievna, Yakupova I. V. Inna Vagizovna, Vinidiktova M. V. Margarita Vladimirovna, Seytenova G. Zh.
Resumo: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.
Idioma:inglês
Publicado em: 2016
Assuntos:
Acesso em linha:http://www.vurup.sk/sites/vurup.sk/files/downloads/pc_7_2016_chernyakova_xx.pdf
Formato: Recurso Electrónico Capítulo de Livro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654808

MARC

LEADER 00000naa0a2200000 4500
001 654808
005 20250313134737.0
035 |a (RuTPU)RU\TPU\network\20495 
090 |a 654808 
100 |a 20170523d2016 k||y0rusy50 ba 
101 0 |a eng 
102 |a SK 
135 |a drcn ---uucaa 
181 0 |a i  
182 0 |a b 
200 1 |a Coke formation reduction in the cataltic reforming reactors at the optimal catalyst activity  |f E. S. Chernyakova [et al.] 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [References: p. 751-752 (16 tit.)] 
330 |a 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. 
461 |t Petroleum and Coal 
463 |t Vol. 58, iss. 7  |v [P. 746-752]  |d 2016 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a каталитический риформинг 
610 1 |a коксообразование 
610 1 |a математическое моделирование 
610 1 |a катализаторы 
701 1 |a Chernyakova  |b E. S.  |c chemist  |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences  |f 1984-  |g Ekaterina Sergeevna  |3 (RuTPU)RU\TPU\pers\34057  |9 17621 
701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |3 (RuTPU)RU\TPU\pers\31274 
701 1 |a Yakupova  |b I. V.  |g Inna Vagizovna 
701 1 |a Vinidiktova  |b M. V.  |g Margarita Vladimirovna 
701 1 |a Seytenova  |b G. Zh. 
712 0 2 |a Национальный исследовательский Томский политехнический университет (ТПУ)  |b Институт природных ресурсов (ИПР)  |b Кафедра химической технологии топлива и химической кибернетики (ХТТ)  |3 (RuTPU)RU\TPU\col\18665 
801 2 |a RU  |b 63413507  |c 20170523  |g RCR 
856 4 |u http://www.vurup.sk/sites/vurup.sk/files/downloads/pc_7_2016_chernyakova_xx.pdf 
942 |c CF