Optimal design of reactive distillation systems: Application to the production of ethyl tert-butyl ether (ETBE)

被引:25
作者
Domingues, Luis [1 ]
Pinheiro, Carla I. C. [1 ]
Oliveira, Nuno M. C. [2 ]
机构
[1] Univ Lisbon, Inst Super Tecn, IBB Inst Biotechnol & Bioengn, P-1049001 Lisbon, Portugal
[2] Univ Coimbra, Dept Chem Engn, CIEPQPF, P-3030790 Coimbra, Portugal
关键词
Reactive distillation; Catalyst deactivation; Dynamic optimisation; Evolutionary algorithms; ETBE production; PARTICLE SWARM OPTIMIZATION; GENETIC ALGORITHM; MODEL DEVELOPMENT; SIMULATION; HYDRATION; CRACKING; COLUMN; MTBE;
D O I
10.1016/j.compchemeng.2014.01.014
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This work addresses the design of reactive distillation columns to produce ETBE, based on a detailed first-principles model that considers equilibrium and kinetic information, rigorous physical property data, and catalyst deactivation. An evolutionary algorithm is used to generate a sequence of feasible designs with improved characteristics in a sequential solution/optimisation strategy, by specifying the design variables (both integer and continuous) that characterise a particular column configuration. Two classes of optimisation algorithms are compared: genetic algorithms and particle swarm optimisation. The objective function considered is the gross annual profit. The results demonstrate that both algorithms are adequate to solve this design problem. The effect of catalyst deactivation included in the design stage played a determinant role in the optimal column specification. A post-design sensitivity analysis is developed to assess the quality of the solutions obtained, together with the individual effects of each design variable in the optimal configuration identified. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:81 / 94
页数:14
相关论文
共 44 条
[1]  
ABUFARES AA, 1995, CHEM ENG RES DES, V73, P3
[2]  
AGREDA VH, 1990, CHEM ENG PROG, V86, P40
[3]   Control study of ethyl tert-butyl ether reactive distillation [J].
Al-Arfaj, MA ;
Luyben, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (16) :3784-3796
[4]   Feasibility of equilibrium-controlled reactive distillation process: application of residue curve mapping [J].
Almeida-Rivera, C ;
Grievink, J .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (1-2) :17-25
[5]   Process simulation of reactive distillation in dividing wall column for ETBE synthesis process [J].
Bumbac, Gheorghe ;
Ene, Adriana ;
Isopescu, Raluca ;
Toma, Aurelian .
PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 :487-+
[6]   Optimization of reactive distillation processes with simulated annealing [J].
Cardoso, MF ;
Salcedo, RL ;
de Azevedo, SF ;
Barbosa, D .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (21) :5059-5078
[7]   SYNTHESIS OF NONEQUILIBRIUM REACTIVE DISTILLATION PROCESSES BY MINLP OPTIMIZATION [J].
CIRIC, AR ;
GU, DY .
AICHE JOURNAL, 1994, 40 (09) :1479-1487
[8]   Evolutionary algorithms approach to the solution of mixed integer non-linear programming problems [J].
Costa, L ;
Oliveira, P .
COMPUTERS & CHEMICAL ENGINEERING, 2001, 25 (2-3) :257-266
[9]   Model Development and Validation of Ethyl tert-Butyl Ether Production Reactors Using Industrial Plant Data [J].
Domingues, Luis ;
Pinheiro, Carla I. C. ;
Oliveira, Nuno M. C. ;
Fernandes, Jorge ;
Vilelas, Andre .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (46) :15018-15031
[10]   A mixed integer nonlinear programming formulation for optimal design of a catalytic distillation column based on a generic nonequilibrium model [J].
Gómez, JM ;
Reneaume, JM ;
Roques, M ;
Meyer, M ;
Meyer, X .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (04) :1373-1388