Kinetic-Thermodynamic Analysis of the Reactive Distillation Process of the Cyclohexene Hydration Using the Zeolite Catalyst

叶建初; 黄佳丽; 林晗丹; 曹克腾; 沙勇

doi:10.1016/S1004-9541(11)60060-8

Your Location：

Home >

Browse articles >

Kinetic-Thermodynamic Analysis of the Reactive Distillation Process of the Cyclohexene Hydration Using the Zeolite Catalyst

Updated：2026-01-06

- Kinetic-Thermodynamic Analysis of the Reactive Distillation Process of the Cyclohexene Hydration Using the Zeolite Catalyst
- Chinese Journal of Chemical Engineering Vol. 19, Issue 5, Pages: 808-814(2011)
- Affiliations：
  
  College of Chemistry and Chemical Engineering, Xiamen University,Fujian,Xiamen,China,361005
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(11)60060-8
  CLC：
- Published：2011
- Accepted：
Scan QR Code
YE Jianchu, HUANG Jiali, LIN Handan, CAO Keteng, SHA Yong. Kinetic-Thermodynamic Analysis of the Reactive Distillation Process of the Cyclohexene Hydration Using the Zeolite Catalyst[J]. , 2011, 19(5): 808-814.
DOI：

YE Jianchu, HUANG Jiali, LIN Handan, CAO Keteng, SHA Yong. Kinetic-Thermodynamic Analysis of the Reactive Distillation Process of the Cyclohexene Hydration Using the Zeolite Catalyst[J]. , 2011, 19(5): 808-814. DOI： 10.1016/S1004-9541(11)60060-8.

摘要

Abstract

Reactive distillation could be utilized to produce cyclohexanol through the cyclohexene hydration. By means of highly active zeolite catalyst HZSM-5

the kinetic-thermodynamic analysis of this reactive distillation has been carried out to get the characteristics of the reactive distillation. Results from kinetic and thermodynamic analysis indicate that the optimal pressure of this reactive distillation process should be set to higher pressure such as 0.3 or 0.4 MPa. To avoid the recovery of cyclohexanol at the top of the column

an unreactive section should be allo-cated at the upper column. In addition

the inert component benzene is more unfavorable to the reactive distillation process in comparison with the inert cyclohexane.

关键词

Keywords

references

Views

2367

Downloads

CSCD

Alert me when the article has been cited

Submit

Tools

Publicity Resources

Kinetic and process analysis of continuous catalytic distillation for high-purity propylene glycol monomethyl ether acetate production

Enhanced activity and stability of SAPO-5 zeolite supported RuMn catalyst for aqueous-phase selective hydrodeoxygenation of guaiacol to cyclohexanol

Enhanced hydration efficiency of cyclohexene to cyclohexanol over acid-modified HZSM-5 catalysts under solvent-free conditions

Rigorous design and economic optimization of reactive distillation column considering real liquid hold-up and hydraulic conditions of industrial device

Improved length of calcium sulfate crystal seeds and whiskers via ball milling and hydration treatment

Related Author

Qinglian Wang

Dingbang Zhao

Huaifang Li

Xin Gao

Weifeng Shen

Chen Yang

Changshen Ye

Ting Qiu

Related Institution

School of Chemistry and Chemical Engineering, Chongqing University

School of Chemical Engineering and Technology, National Engineering Research Center of Distillation Technology, Collaborative Innovation Center of Chemical Science and Engineering, Tianjin University

Qingyuan Innovation Laboratory

State Key Laboratory of Green and Efficient Development of Phosphorus Resources, Fuzhou University International Joint Laboratory of Thermochemical Conversion of Biomass, Fujian Universities Engineering Research Center of Reactive Distillation Technology, College of Chemical Engineering, Fuzhou University

Key Laboratory of Biomass Chemical Engineering of the Ministry of Education, College of Chemical and Biological Engineering, Zhejiang University

⁰