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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
Doklady Chemistry – Springer Journals
Published: Oct 12, 2004
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