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Nonlinear Phenomena in a Downward Gas–Liquid Flow through a Fixed Granular Catalyst Bed

Nonlinear Phenomena in a Downward Gas–Liquid Flow through a Fixed Granular Catalyst Bed Doklady Chemistry, Vol. 380, Nos. 1–3, 2001, pp. 271–275. Translated from Doklady Akademii Nauk, Vol. 380, No. 1, 2001, pp. 77–81. Original Russian Text Copyright © 2001 by Slin’ko, Kirillov, Kuzin, Shigarov. CHEMICAL TECHNOLOGY Nonlinear Phenomena in a Downward Gas–Liquid Flow through a Fixed Granular Catalyst Bed Corresponding Member of the RAS M. G. Slin’ko*, V. A. Kirillov**, N. A. Kuzin**, and A. B. Shigarov** Received April 2, 2001 Many industrial catalytic processes, such as hydro- saturate hydrogen with a -methylstyrene vapor at the genation and partial oxidation of hydrocarbons, liquid reactor inlet, a separator for separating the liquid from fuel synthesis, hydration, etc., are performed in active the gas–vapor mixture at the reactor outlet, a condenser media consisting of solid, liquid, and gas phases. An for condensing the a -methylstyrene and cumene vapor important feature of such processes is nonlinear phe- mixture, and a device for chromatographic analysis of nomena, e.g., multiplicity of steady states, hystereses, the a -methylstyrene and cumene mixtures. In the exper- and emergence of dry hot spots within a catalyst bed in iments, hydrogen from a cylinder was fed through a exothermic reactions accompanied by liquid evapora- system of pressure and flow regulators together http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Doklady Chemistry Springer Journals

Nonlinear Phenomena in a Downward Gas–Liquid Flow through a Fixed Granular Catalyst Bed

Doklady Chemistry , Volume 380 (3) – Oct 12, 2004

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References (3)

Publisher
Springer Journals
Copyright
Copyright © 2001 by MAIK “Nauka/Interperiodica”
Subject
Chemistry; Chemistry/Food Science, general; Industrial Chemistry/Chemical Engineering
ISSN
0012-5008
eISSN
1608-3113
DOI
10.1023/A:1011906805954
Publisher site
See Article on Publisher Site

Abstract

Doklady Chemistry, Vol. 380, Nos. 1–3, 2001, pp. 271–275. Translated from Doklady Akademii Nauk, Vol. 380, No. 1, 2001, pp. 77–81. Original Russian Text Copyright © 2001 by Slin’ko, Kirillov, Kuzin, Shigarov. CHEMICAL TECHNOLOGY Nonlinear Phenomena in a Downward Gas–Liquid Flow through a Fixed Granular Catalyst Bed Corresponding Member of the RAS M. G. Slin’ko*, V. A. Kirillov**, N. A. Kuzin**, and A. B. Shigarov** Received April 2, 2001 Many industrial catalytic processes, such as hydro- saturate hydrogen with a -methylstyrene vapor at the genation and partial oxidation of hydrocarbons, liquid reactor inlet, a separator for separating the liquid from fuel synthesis, hydration, etc., are performed in active the gas–vapor mixture at the reactor outlet, a condenser media consisting of solid, liquid, and gas phases. An for condensing the a -methylstyrene and cumene vapor important feature of such processes is nonlinear phe- mixture, and a device for chromatographic analysis of nomena, e.g., multiplicity of steady states, hystereses, the a -methylstyrene and cumene mixtures. In the exper- and emergence of dry hot spots within a catalyst bed in iments, hydrogen from a cylinder was fed through a exothermic reactions accompanied by liquid evapora- system of pressure and flow regulators together

Journal

Doklady ChemistrySpringer Journals

Published: Oct 12, 2004

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