Study on apparent kinetics and reaction processes of catalytic oxidation of wastewater from ethyl acetate production

被引:0
|
作者
Zhou Y. [1 ]
Pu X. [1 ]
Cui M.-F. [1 ]
Liu Q. [1 ]
Chen X. [1 ]
Fei Z.-Y. [2 ]
Tang J.-H. [1 ,2 ]
Zhang Z.-X. [1 ]
Qiao X. [1 ,2 ]
机构
[1] College of Chemical Engineering, Nanjing Tech University, Nanjing
[2] State Key Laboratory of Materials-Oriented Chemical Engineering, Nanjing Tech University, Nanjing
关键词
Catalytic oxidation; Ethyl acetate wastewater; Kinetics; Oxygen consumption rate;
D O I
10.3969/j.issn.1003-9015.2020.01.020
中图分类号
学科分类号
摘要
Ethyl acetate production usually comes with a large amount of high concentration organic wastewater. This study proposed a method for treating ethyl acetate wastewater by vaporization followed with catalytic oxidation in a fixed-bed reactor using a self-made composite oxide catalyst. The reaction process was optimized and the apparent reaction kinetic data were obtained at 290~410 ℃ and φ = 4% oxygen concentration after eliminating the effects of catalyst external diffusion. The apparent reaction kinetic model based on oxygen consumption rate was established and its parameters were obtained via data fitting. The calculated apparent activation energy was 50.17 kJ∙mol-1. The calculated results were in agreement with the experimental data, and the model was verified with good accuracy. This study provides guidelines for the design of industrial catalytic oxidation reactors. © 2020, Editorial Board of "Journal of Chemical Engineering of Chinese Universities". All right reserved.
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页码:157 / 162
页数:5
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