Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study
催化、动力学与反应工程|Updated:2026-01-06
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Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study
Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study
中国化学工程学报(英文版)2015年23卷第9期 页码:1469-1474
Affiliations:
1. Hubei Key Laboratory of Material Chemistry & Service Failure, School of Chemistry and Chemical Engineering, Huazhong University of Science and Technology,Wuhan,China,430074
2. Key Laboratory for Large-Format Battery Materials and System, Ministry of Education, School of Chemistry and Chemical Engineering, Huazhong University of Science and Technology,Wuhan,China,430074
Huajun Wang, Lei Pang, Chao Yang, 等. Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study[J]. 中国化学工程学报(英文版), 2015,23(9):1469-1474.
Huajun Wang, Lei Pang, Chao Yang, Yihua Liu. Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study[J]. , 2015, 23(9): 1469-1474.
Huajun Wang, Lei Pang, Chao Yang, 等. Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study[J]. 中国化学工程学报(英文版), 2015,23(9):1469-1474.DOI: 10.1016/j.cjche.2015.06.011.
Huajun Wang, Lei Pang, Chao Yang, Yihua Liu. Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study[J]. , 2015, 23(9): 1469-1474.DOI: 10.1016/j.cjche.2015.06.011.
Production of glycerol carbonate via reactive distillation and extractive distillation: An experimental study
A process for the production of glycerol carbonate (GC) is proposed with the transesterification of glycerol (GL) and dimethyl carbonate (DMC)with CaO as catalyst by reactive distillation and extractive distillation. The performance of solvents in separating DMC-methanol azeotrope and the effects of operation parameters on the reactive distillation process are investigated experimentally. The results indicate that both the GL conversion and GC yield increase with the DMC/GL molar ratio
reflux ratio
final temperature of tower bottom
and CaO/GL molar ratio and decrease as the recycle number of CaO increases. The calciumconcentration in the residual reaction mixture also decreases remarkably as the DMC/GL molar ratio increases. At DMC/GL molar ratio 4.0
reflux ratio 1.0
final temperature of tower bottom 358 K
and CaO/GL molar ratio 0.05
both the GL conversion and GC yield can reach above 99.0%
and the mass concentration of calcium in the product is less than 0.08%.
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相关作者
Qinglian Wang
Dingbang Zhao
Huaifang Li
Xin Gao
Weifeng Shen
Chen Yang
Changshen Ye
Ting Qiu
相关机构
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
Qingyuan Innovation Laboratory
School of Chemical Engineering and Technology, National Engineering Research Center of Distillation Technology, Collaborative Innovation Center of Chemical Science and Engineering, Tianjin University
School of Chemistry and Chemical Engineering, Chongqing University
Engineering Research Center of Reaction Distillation, Fujian Province University, College of Chemical Engineering, Fuzhou University