Comparison of multiplicity patterns of a single catalytic pellet and a fixed catalytic bed for ethylene oxidation
Author:
Publisher
Elsevier BV
Subject
Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Reference18 articles.
1. On the dynamic behavior of the catalytic fixed-bed reactor in the region of multiple steady-states. I. The influence of heat conduction in two phase models;Eigenberger;Chem. Engng Sci.,1972
2. On the dynamic behavior of the catalytic fixed-bed reactor in the region of multiple steady-states. II. the influence of boundary conditions in the catalyst phase;Eigenberger;Chem. Engng Sci.,1972
3. Analysis and modelling of multiplicity features. I. Nonisothermal experiments;Harold;Ind. Engng Chem. Res.,1987
4. Multiple steady states in an isothermal integral reactor: the catalytic oxidation of carbon-monoxide over platinum-alumina;Hegedus;A.I.Ch.E.J.,1977
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1. Ignition–extinction analysis of catalytic reactor models;Reviews in Chemical Engineering;2021-04-20
2. Novel Multiplicity and Stability Criteria for Non-Isothermal Fixed-Bed Reactors;Frontiers in Energy Research;2021-01-12
3. Decoupling the relative rate of hydrogen uptake via convection and mass transfer by a single catalytic pellet in a scaled down trickle bed reactor;Chemical Engineering Journal;2020-08
4. Selective Hydrogenation of Acetylene in an Ethylene Stream in an Adiabatic Reactor;Chemical Engineering & Technology;2002-05
5. Spatiotemporal patterns in catalytic reactors;AIChE Journal;1996-04
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