Process improvement for three-column extractive distillation by feed split

被引:15
作者
Duan, Cong [1 ]
Li, Chunli [1 ]
机构
[1] Hebei Univ Technol, Sch Chem Engn & Technol, Natl Local Joint Engn Lab Energy Conservat Chem P, Tianjin 300130, Peoples R China
基金
中国国家自然科学基金;
关键词
Extractive distillation; Azeotropic component; Feed split; Energy saving; COMBINING PRECONCENTRATION COLUMN; TRANSITION-TEMPERATURE MIXTURES; DIVIDING-WALL COLUMN; ETHYL-ACETATE; SEPARATION; DESIGN; WATER; OPTIMIZATION; ENTRAINER; RECOVERY;
D O I
10.1016/j.seppur.2022.121467
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A three-column extractive distillation process may often be used when separating azeotropic components at a dilute feed condition. A feed-split method is innovatively proposed to save energy for this process. The method is to split the fresh feed stream into two streams, one for the pre-concentrator, and the other for the extractive distillation column. The applicability of this method is initially estimated. Four systems are used as main case studies including acetonitrile/water with ethylene glycol as the solvent, acetone/methanol with dimethyl sulfoxide as the solvent, n-propanol/water with N-methylpyrrolidone as the solvent and ethyl acetate/ethanol with furfural as the solvent. The results show that most three-column extractive distillation process can save energy by feed split. This method can be used alone or used for other energy-saving methods to save further energy.
引用
收藏
页数:13
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