Реферат: A mathematical model describing the destruction of catalyst particles during operation in an industrial fluidized-bed reactor with allowance for the crushing and abrasion of particles is proposed. Differences between the mechanical properties of IM-2201 and KDI catalysts used in the dehydrogenation of iso-butane to iso-butylene at PAO Nizhnekamskneftekhim are established. Using KDI catalyst with modification of the cyclone group and retention of the equilibrium distribution of particles according to size in a reactor is shown to provide a more than a 2.5-fold reduction in catalyst consumption.

Библиографическая ссылка: Kataev A.N. , Egorov A.G. , Egorova S.R. , Lamberov A.A.
Mathematical modeling of changes in the fractional composition of dehydrogenation catalysts in a fluidized-bed reactor
Catalysis in Industry. 2015. V.7. N3. P.221-226. DOI: 10.1134/s2070050415030071 WOS Scopus РИНЦ OpenAlex

Оригинальная версия: Катаев А.Н. , Егоров А.Г. , Егорова С.Р. , Ламберов А.А.
Математическое моделирование изменения фракционного состава катализаторов дегидрирования в реакторе с кипящим слоем
Катализ в промышленности. 2015. №3. С.60-66. DOI: 10.18412/1816-0387-2015-3-60-66 РИНЦ CAPlusCAРЖ ВИНИТИ

Даты:

Опубликована в печати:

1 июл. 2015 г.

Идентификаторы БД:

Web of science:	WOS:000372437400006
Scopus:	2-s2.0-84942412390
РИНЦ:	24952585
OpenAlex:	W2160467506

Цитирование в БД:

БД	Цитирований
OpenAlex	4
Web of science	4
Scopus	3

Альметрики: