Methyl-tert-butyl-ether catalytic distillation column - Part II: Optimization

被引:12
作者
Eldarsi, HS [1 ]
Douglas, PL [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
关键词
MTBE catalytic distillation; steady state simulation; optimization;
D O I
10.1205/026387698524992
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This is the second of two papers on the catalytic distillation process to produce methyl-tert-butyl-ether (MTBE) from methanol and isobutylene contained in a mixed butylenes stream. In this paper, an MTBE catalytic distillation column was optimized using AspenPlus. The optimization studies indicate that the market price of the MTBE product and the cost of the butylenes feed play a key role in determining the MTBE column profit. The profit is also affected by isobutylene composition changes. In addition, there are significant economic penalties if the column decision variables are not updated for changes in utility costs.
引用
收藏
页码:517 / 524
页数:8
相关论文
共 12 条
[1]  
ABUFARES AA, 1995, CHEM ENG RES DES, V73, P3
[2]  
CLEMENTI A, 1979, HYDROCARBON PROC DEC, P109
[3]  
EDGER TF, 1988, OPTIMIZATION CHEM PR
[4]  
ELDARSI HS, 1998, T I CHEM ENG-LOND, V76, P509
[5]   MULTIPLE SOLUTIONS IN REACTIVE DISTILLATION FOR METHYL TERT-BUTYL ETHER SYNTHESIS [J].
JACOBS, R ;
KRISHNA, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (08) :1706-1709
[6]  
KZYONSEK M, COMMUNICATION
[7]  
PECCI G, 1977, HYDROCARB PROCESS, V56, P98
[8]  
PLATT, 1996, OILGRAM PRICE REPORT
[9]  
RASMUSSEN DJ, 1995, COMMUNICATION DEC
[10]   KINETICS OF METHYL TERTIARY BUTYL ETHER LIQUID-PHASE SYNTHESIS CATALYZED BY ION-EXCHANGE RESIN .1. INTRINSIC RATE EXPRESSION IN LIQUID-PHASE ACTIVITIES [J].
REHFINGER, A ;
HOFFMANN, U .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (06) :1605-1617