Aspen Plus simulation and optimization of methyl acetate synthesis by catalytic reactive distillation

被引:0
作者
Wang, Xiaoxuan [1 ,2 ]
Yu, Ling [1 ]
机构
[1] Shenghong Refining Lianyungang Co Ltd, Lianyungang, Peoples R China
[2] Shenghong Refining Lianyungang Co Ltd, Chem Engn Dept 2, Lianyungang 222000, Peoples R China
来源
PRZEMYSL CHEMICZNY | 2024年 / 103卷 / 01期
关键词
methyl acetate; reactive distillation; production cost; Aspen Plus software;
D O I
暂无
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Catalytic reactive distn. of AcOMe was simulated by using Aspen Plus software. The optimum theor. plate number was 43, the optimum AcOH feeding position was the 12thplate, the optimum MeOH feeding posi-tion was the 41st plate, the optimum reflux ratio was 1.4, and the opti-mum alkyd ratio was 1.1. Under basically the same conditions, use of the single-tower reactive distn. system can greatly reduce energy con-sumption and equipment investment when compared with the 2-tower system. The annual av. costs prodn. were by 38.88% lower than that of the 2-tower process.
引用
收藏
页码:59 / 65
页数:156
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