Comparison of computer simulation of reactive distillation using ASPEN PLUS and HYSYS software

被引:100
作者
Smejkal, Q
Soós, M
机构
[1] ICT Prague, CZ-16628 Prague, Czech Republic
[2] STU Bratisalva, Dept Chem Engn, SK-81237 Bratislava, Slovakia
关键词
butylacetate; reactive distillation; simulation; ASPEN PLUS; HYSYS;
D O I
10.1016/S0255-2701(01)00160-X
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
A comparison of computer simulation results of reactive distillation obtained by ASPEN PLUS and HYSYS software was done. Esterification of acetic acid and 1-butanol was chosen as the model reaction proceeding in a reactor and reactive distillation column (RD) system. A nearly equimolar reaction mixture was fed into the equilibrium fixed bed reactor and the liquid product was continuously fed into reaction zone of the reactive distillation column. The same mass balance in the reactor and reactive distillation column was used to compare the adequacy of chosen simulation systems. The results of computer simulation have been consequently compared with pilot plant experimental data. A good agreement was reached. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:413 / 418
页数:6
相关论文
共 10 条
[1]
*ASP TECHN INC, 1994, ASP PLUS US MAN, V1
[2]
GHEHLING J, 1977, DECHEMA, V1, P135
[3]
GMEHLING J, 1982, DECHEMA, V1, P197
[4]
GROGGINS PH, 1952, UNIT PROCESS ORGANIS
[5]
Butylacetate via reactive distillation - modelling and experiment [J].
Hanika, J ;
Kolena, J ;
Smejkal, Q .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) :5205-5209
[6]
HODGMANN CD, 1965, HDB CHEM PHYSICS
[7]
PONGO J, 1996, FORREST HYSYS REFERE, V1
[8]
Seider W.D., 2003, Product and Process Design Principles: Synthesis, Analysis and Design
[9]
2-methylpropylacetate synthesis in a system of equilibrium reactor and reactive distillation column [J].
Smejkal, Q ;
Hanika, J ;
Kolena, J .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (02) :365-370
[10]
VENKATARAMAN S, 1990, CHEM ENG PROG, V86, P45