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

書目詳細資料
Parent link:Procedia Chemistry
Vol. 10 : Chemistry and Chemical Engineering in XXI century.— 2014.— [P. 127-136]
企業作者: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
其他作者: 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.
總結: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
語言:英语
出版: 2014
主題:
在線閱讀:http://dx.doi.org/10.1016/j.proche.2014.10.023
http://earchive.tpu.ru/handle/11683/35483
格式: 電子 Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639471