Реферат: The paper is dedicated to the mathematical modelling of Claus reaction performance in the packed catalyst bed under conditions of sulfur condensation and evaporation. The proposed mathematical model accounts for heat and mass transfer between reaction gas and solid catalyst, condensation and evaporation of sulfur, reversible catalyst deactivation by liquid sulfur, Claus reaction reversibility, intraparticle diffusion limitations, heat conductivity of the catalyst bed frame. Reverse-flow operation of the catalyst bed have been investigated. The complex process flow-sheets, comprising two and three catalyst beds with intermediate sulfur condensers, have been simulated. It has been shown, that application of the reverse-flow technique provides increase of process efficiency.

Библиографическая ссылка: Zagoruiko A.N. , Matros Y.S.
Mathematical Modelling of Claus Reactors Undergoing Sulfur Condensation and Evaporation
Chemical Engineering Journal. 2002. V.87. N1. P.73-88. DOI: 10.1016/S1385-8947(01)00203-0 WOS Scopus РИНЦ CAPlusCA OpenAlex

Даты:

Поступила в редакцию:	5 февр. 2001 г.
Принята к публикации:	23 июл. 2001 г.
Опубликована в печати:	28 мая 2002 г.
Опубликована online:	11 июн. 2002 г.

Идентификаторы БД:

Web of science:	WOS:000176014200008
Scopus:	2-s2.0-0037188303
РИНЦ:	13413830
Chemical Abstracts:	2002:357193
Chemical Abstracts (print):	137:171813
OpenAlex:	W2017078644

Цитирование в БД:

БД	Цитирований
Web of science	32
Scopus	45
РИНЦ	45
OpenAlex	40

Альметрики: