Hydrolysis of methyl acetate via catalytic distillation: Simulation and design of new technological process

Doherty, 1992, Reactive distillation by design, IChemE, 70, 448 Sundmacher, 1994, Multicomponent mass and energy transport on different length scale in a packed reactive distillation column for heterogeneously catalyzed fuel ether production, Chemical Engineering Science, 49, 4443, 10.1016/S0009-2509(05)80032-6 Fuchigami, 1990, Hydrolysis of methyl acetate in distillation column packed with reactive packing of ion exchange resin, Journal of Chemical Engineering Japan, 23, 354, 10.1252/jcej.23.354 Kaymak, 2004, Quantitative comparison of reactive distillation with conventional multiunit reactor/column/recycle systems for different chemical equilibrium constants, Industrial and Engineering Chemistry Research, 43, 2493, 10.1021/ie030832g Lin, 2008, Process alternatives for methyl acetate conversion using reactive distillation. 1. Hydrolysis, Chemical Engineering Science, 63, 1668, 10.1016/j.ces.2007.11.009 Yu, 2005, Optimization of reactive simulated moving bed and Varicol systems for hydrolysis of methyl acetate, Chemical Engineering Journal, 112, 57, 10.1016/j.cej.2005.06.008 Han, 1997, Application of a fluidized reaction-distillation column for hydrolysis of methyl acetate, Chemical Engineering Journal, 66, 227, 10.1016/S1385-8947(96)03194-4 Wang, 2001, Experimental studies on catalytic distillation for hydrolysis of methyl acetate, Chemical Engineering and Technology, 24, 155, 10.1002/1521-4125(200102)24:2<155::AID-CEAT155>3.0.CO;2-G Popken, 2001, Synthesis and hydrolysis of methyl acetate by reactive distillation using structured catalytic packings: experiments and simulation, Industrial and Engineering Chemical Research, 40, 1566, 10.1021/ie0007419 Xiao, 2001, Increase MeOAc conversion in PVA production by replacing the fixed bed reactor with a catalytic distillation column, Chemical Engineering Science, 56, 6553, 10.1016/S0009-2509(01)00305-0 Smejkal, 2002, Comparison of computer simulation of reactive distillation using ASPEN PLUS and HYSYS software, Chemical Engineering and Processing, 41, 413, 10.1016/S0255-2701(01)00160-X Abrams, 1975, Statistical thermodynamics of liquid mixture: a new expression for the excess Gibbs energy of partly or completely miscible system, AIChE Journal, 21, 116, 10.1002/aic.690210115 Popken, 2000, Reaction kinetics and chemical equilibrium of homogeneously and heterogeneously catalyzed acetic acid esterification with methanol and methyl acetate hydrolysis, Industrial and Engineering Chemical Research, 39, 2601, 10.1021/ie000063q Wu, 1999, Kinetics of hydrolysis of methyl acetate and the effectiveness factor of catalyst capsule, Engineering Chemistry and Metallurgy, 20, 241 Zheng, 1992, Study on catalytic distillation processes. Part I. Mass transfer characteristics in catalyst bed within the column, TransIChemE, Chemical Engineering Research and Design, 70, 459 Xu, 1997, Study on catalytic distillation processes Part III: Prediction of pressure drop and holdup in catalyst bed, TransIChemE, Chemical Engineering Research and Designing, 75, 625, 10.1205/026387697524155 Cheng, 2005, Effects of feed tray locations to the design of reactive distillation and its implication to control, Chemical Engineering Science, 60, 4661, 10.1016/j.ces.2005.03.033 Subawalla, 1999, Design guidelines for solid-catalyzed reactive distillation systems, Industrial and Engineering Chemical Research, 38, 3696, 10.1021/ie990008l