Elevation of performance of gas–liquid reactors on solid catalyst | Sciact

Elevation of performance of gas–liquid reactors on solid catalyst Научная публикация

Конференция

XV International Conference on Chemical Reactors
05-08 июн. 2001 , Хельсинки

Журнал

Chemical Engineering Journal
ISSN: 1385-8947

Вых. Данные

Год: 2003, Том: 91, Номер: 2-3, Страницы: 199-204 Страниц : 6 DOI: 10.1016/s1385-8947(02)00154-7

Авторы

Stefoglo E.F. ¹ , Drobyshevich V.I. ² , Semikolenov V.A. ³ , Kuchin I.V. ¹ , Zhukova O.P. ¹

Организации

1	Institute of Coal and Coal Chemistry, Rukavishnikov, 21, Kemerovo 650610, Russia
2	Institute of Computational Mathematics and Math. Geoph., Novosibirsk 630090, Russia
3	Boreskov Institute of Catalysis, Pr. Lavrentieva, 5, Novosibirsk 630090, Russia

Different kinds of initial conditions for the gas–liquid process on a solid catalyst are discussed in the paper. The advantages of process with preliminary saturation of liquid with gas are considered. For the liquid batch reactor it is theoretically shown that preliminary saturation of the initial solution with gas prior to reaction profits more in comparison with “usual” mode. The experiments on hydrogenation of ethyl ether of p-nitrobenzoic acid to anesthesyne on suspended 5% Pd/C catalyst in a batch reactor were carried out for verification of the main results from the proposed model (PH2=40 bar, T=20–120 °C). As an example of a reactor, where the preliminary saturation effect can be used, the trickle-bed reactor operating without pumping was considered. Mathematical simulation of such type reactor is presented.

Stefoglo E.F. , Drobyshevich V.I. , Semikolenov V.A. , Kuchin I.V. , Zhukova O.P.
Elevation of performance of gas–liquid reactors on solid catalyst
Chemical Engineering Journal. 2003. V.91. N2-3. P.199-204. DOI: 10.1016/s1385-8947(02)00154-7 WOS Scopus OpenAlex

Опубликована online:

2 окт. 2002 г.

Web of science:	WOS:000181148600014
Scopus:	2-s2.0-0037445354
OpenAlex:	W1980277568

БД	Цитирований
OpenAlex	1