Inter‐integration reactive distillation with vapor permeation for ethyl levulinate production: Equipment development and experimental validating

AIChE Journal ◽  
2021 ◽  
Author(s):  
Wen‐tao Han ◽  
Zhen‐wei Han ◽  
Xue‐chao Gao ◽  
Zhou Hong ◽  
Xin‐gang Li ◽  
...  



Author(s):  
Wentao Han ◽  
Zhenwei Han ◽  
Xuechao Gao ◽  
Zhou Hong ◽  
Xingang Li ◽  
...  

Ethyl levulinate, one of main derivatives of levulinic acid (LA), is of significant potential as platform chemicals for bio-based materials. The esterification of LA was generally carried out in a conventional batch reactor or in a conventional reactive distillation column. However, traditional methods are hard to deal with equilibrium limited reactions and azeotropic issues. Therefore, the reactive-vapor permeation-distillation (R-VP-D) process, which integrated reaction, distillation and membrane dehydration into one single unit, is proposed in this paper and validated in the pilot-scale experiments. A comparative study is made between a pilot-scale RD column with and without vapor permeation membrane module. Owing to the water-selective membrane and the ingenious design of related apparatuses, the R-VP-D process reveal a superiority in LA conversion of 21.9% maximum higher than RD without VP process and removing of product water about 53.6% from VP module, which indicates its promising industrial application in process intensification field.



2018 ◽  
Vol 190 ◽  
pp. 297-311 ◽  
Author(s):  
Felicia Januarlia Novita ◽  
Hao-Yeh Lee ◽  
Moonyong Lee


Author(s):  
Rong Bi ◽  
Xiaoyang Sun

Toluene diisocyanate (TDI) is an important chemical intermediate prepared by phosgenation reaction between toluene diamine and phosgene with two steps name cold and thermal phosgenation respectively. In this paper, the reactive distillation model for the thermal phosgenation reaction based the kinetics equations was established for an industrial installation, and the effects of the different parameters on the process performance were studied firstly; then based on the analysis results, a thermal coupling process between the towers of reactive distillation and phosgene purification was presented and investigated; finally, the optimal operation scheme was simulated and the results showed that the proposed process can save the heat and cold energy with 7.29% and 32.78%, respectively, and reduce the total annual cost about 17.11%. The result of the paper can be used to guide the operation configuration or the revampment of the TDI production equipment.



2019 ◽  
Vol 94 (7) ◽  
pp. 2131-2140 ◽  
Author(s):  
José A Vázquez‐Castillo ◽  
Gabriel Contreras‐Zarazúa ◽  
Juan G Segovia‐Hernández ◽  
Anton A Kiss


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