Application of a fluidized reaction-distillation column for hydrolysis of methyl acetate

被引：18
|
作者：
Han, SJ
Jin, Y
Yu, ZQ
机构：
[1] Department of Chemical Engineering, Tsinghua University
来源：
CHEMICAL ENGINEERING JOURNAL | 1997年 / 66卷 / 03期
关键词：
reactive distillation; hydrolysis of MeOAc;
D O I：
10.1016/S1385-8947(96)03194-4
中图分类号：
X [环境科学、安全科学];
学科分类号：
08 ; 0830 ;
摘要：
A new method for the hydrolysis of methyl acetate, which consists of a prereactor and a reactive distillation column, has been proposed. The operating variables, including the feed rate, feed ratio of water to MeOAc and reflux ratio, are investigated. It has been found that the conversion of MeOAc increases with increasing reflux ratio, but decreases with increasing feed rate. The feed ratio of water to MeOAc has a considerable effect on the conversion of MeOAc, and an optimum feed ratio has been obtained for the present process. (C) 1997 Elsevier Science S.A.
引用
收藏
页码：227 / 230
页数：4
相关论文
共 50 条
  • [41] Calculation of radial reactors with a moving bed of catalyst in reaction-distillation processes
    A. I. Vladimirov
    V. A. Luk'yanov
    I. I. Mukhin
    [J]. Chemistry and Technology of Fuels and Oils, 1997, 33 : 17 - 22
  • [42] Numerical Investigation of the Reactive Dividing Wall Column Exemplified by Methyl Acetate Hydrolysis
    Mueller, Ivo
    Kenig, Eugeny Y.
    [J]. CHEMIE INGENIEUR TECHNIK, 2010, 82 (12) : 2109 - 2118
  • [43] APPLICATION OF INTERFEROMETRY TO REACTION KINETICS - HYDROLYSIS OF ETHYL ACETATE
    OBRIEN, RN
    GLASEL, A
    [J]. CANADIAN JOURNAL OF CHEMISTRY, 1969, 47 (02): : 223 - &
  • [44] High Conversion of Methyl Acetate Hydrolysis in a Reactive Dividing Wall Column by Weakening the Self-Catalyzed Esterification Reaction
    Wang, Xiaoda
    Wang, Hongxing
    Chen, Jinyi
    Zheng, Weiyue
    Qiu, Ting
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (32) : 9177 - 9187
  • [45] Design and Control of a Heat-Integrated Reactive Distillation System for the Hydrolysis of Methyl Acetate
    Lee, Hao-Yeh
    Lee, Yi-Chen
    Chien, I-Lung
    Huang, Hsiao-Ping
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (16) : 7398 - 7411
  • [46] Thermodynamic analysis of reaction-distillation processes based on piecewise linear models
    Ryll, O.
    Blagov, S.
    Hasse, H.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2014, 109 : 284 - 295
  • [47] Calculation of radial reactors with a moving bed of catalyst in reaction-distillation processes
    Vladimirov, AI
    Lukyanov, VA
    Mukhin, II
    [J]. CHEMISTRY AND TECHNOLOGY OF FUELS AND OILS, 1997, 33 (01) : 17 - 22
  • [48] Calculation of radial reactors with a moving bed of catalyst in reaction-distillation processes
    Vladimirov, A.I.
    Luk'yanov, V.A.
    Mukhin, I.I.
    [J]. Chemistry and Technology of Fuels and Oils, 33 (01): : 17 - 22
  • [49] Design and Control of Different Pressure Thermally Coupled Reactive Distillation for Methyl Acetate Hydrolysis
    Li, Lumin
    Sun, Lanyi
    Wang, Jun
    Zhai, Jian
    Liu, Yuliang
    Zhong, Wang
    Tian, Yuanyu
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (49) : 12342 - 12353
  • [50] Hydrolysis of methyl acetate via catalytic distillation: Simulation and design of new technological process
    Gao, Xin
    Li, Xingang
    Li, Hong
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (12) : 1267 - 1276
12345