International Journal of Chemical Kinetics · 1998 · 13 citations · 10 references
Natural SciencesChemical EngineeringChemistryCatalysisPhysical ChemistryReaction EngineeringCatalytic Reaction EngineeringCatalytic Reaction KineticsChemical Reaction KineticsIndustrial Catalytic ProcessesKinetic ModelingDiffusion EffectsIon Exchange ReactionsLiquid-phase KineticsReaction Rate EquationsReaction Rate ModelingSolvent Effects On CatalysisSolvent Effects On Reaction PathwaysSolvent Effects On Reaction Rates
Synthesis of tert-amyl methyl ether (TAME) from methanol (MeOH) and tert-amyl alcohol (TAA) in the liquid phase was studied by using an ion exchange resin, Amberlyst15 (A15) in the H+ form. Experiments were carried out in a stirred batch reactor under atmospheric pressure. The effects of catalyst size, agitation speed, temperatures, feed ratio and water on the reaction rate were investigated. Both of intraparticle and external diffusion effects could be neglected in this system. The dehydration of TAA could be decreased by increasing the ratio of MeOH/TAA and the reaction rates were greatly inhibited by water. A kinetic model which considered the inhibition of water was proposed. The experimental results agreed well with the model. © 1998 John Wiley & Sons, Inc. Int J Chem Kinet: 30: 137–143, 1998.
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Pervaporation-aided Esterification of Oleic Acid.
Ken‐ichi Okamoto, M. Yamamoto, Yoshiharu Otoshi et al. · JOURNAL OF CHEMICAL ENGINEERING OF JAPAN · 1993 · 65 citations · Full text