Improving the Efficiency of Dehydrogenation Catalyst Resource while Reducing the H[2] Gas Circulation Rat; Procedia Chemistry; Vol. 10 : Chemistry and Chemical Engineering in XXI century

Detalhes bibliográficos
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 127-136]
Autor Corporativo: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Outros Autores: Ivashkina E. N. Elena Nikolaevna, Ivanchina E. D. Emilia Dmitrievna, Frantsina E. V. Evgeniya Vladimirovna, Platonov V. V., Glik P. A., Volkov M. A., Kolmogorova V. А.
Resumo:Title screen
In the research the various ways of increasing the selectivity of the dehydrogenation process and reducing the intensity of coke formation have been studied. All results were received by means of the mathematical model of the dehydrogenation process with the calculating technique of optimal water flow. The main conclusion consists in the fact that the decrease in molar ratio H[2]/feed leads to increasing the catalyst deactivation by coke. It can be partially compensated by increasing the supplied water flow to the reactor to 13-14 l/h instead of 9-10 l/h at the end of cycle. Reducing the life of the catalyst to 270-290 days even at an increased water flow is determined by the intensity of the coking reactions. However, the economic feasibility of operating in such condition causes a considerable increase in production of LAB to 181-186 t/day.
Режим доступа: по договору с организацией-держателем ресурса
Idioma:inglês
Publicado em: 2014
Assuntos:
Acesso em linha:http://dx.doi.org/10.1016/j.proche.2014.10.023
http://earchive.tpu.ru/handle/11683/35483
Formato: Recurso Electrónico Capítulo de Livro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639471