AIChE Journal · 1976 · 75 citations · 12 references
EngineeringChemical EngineeringChemistryCatalysisReaction EngineeringTransport PhenomenaCatalytic Reaction EngineeringCatalytic Reaction KineticsCatalytic Reactor DesignOxidation-reduction ReactionsPacked Bed ReactorsReactor KineticsCatalytic Reactor ModelingChannelingChanneling PhenomenaFlow ChannelingReaction Kinetics In Packed BedsTrickle-bed Reactor DesignTrickle-bed ReactorsVaporization
Abstract Rates of oxidation of dilute, aqueous solutions of acetic acid were measured at 252° to 286°C and 67 atm in liquid full and trickle‐bed reactors packed with ferric oxide catalyst particles. Predicted global rates and conversions indicated that localized vaporization and liquid channeling could affect trickle‐bed performance.
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