Process intensification of reactive distillation using improved RCMs: Acetic acid production

被引:5
作者
Park, Jonghyun [1 ]
Jeong, Youngmin [1 ]
Han, Myungwan [1 ]
机构
[1] Chungnam Natl Univ, Dept Chem Engn & Appl Chem, 99 Daehak Ro, Daejeon 34134, South Korea
关键词
Process intensification; Optimal process structure; Residue curve maps; Reactive distillation; Acetic acid; RESIDUE CURVE MAPS; MINIMUM-REFLUX CALCULATIONS; SHORTCUT DESIGN; EQUILIBRIUM; KINETICS; COLUMNS; SYSTEMS;
D O I
10.1016/j.cep.2020.108136
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 ; 0820 ;
摘要
Residue curve maps (RCMs) are useful for the synthesis and analysis of both conventional multicomponent separation and reactive distillation (RD). However, the RCMs do not provide any quantitative performance measure to compare the process alternatives for process intensification. We develop a new velocity vector concept that consists of the speed and direction of the composition change in RCMs for process intensification of reactive distillation. Process intensification in reactive distillation can be thought of as locating multiple process operations in a single continuous column. Optimizing the process intensification in a continuous column can be transformed into finding an optimal path from the initial composition to the target one in RCMs. The optimal path can be determined by minimizing the total processing time required for travelling the path in RCMs. We propose a two-step design method for the RD process consisting of conceptual or structural design based on the new residue curve map and parameter optimization of the process based on rigorous simulation. This new process design method is illustrated by application to a reactive distillation system using an auxiliary reaction for the production of methyl acetate.
引用
收藏
页数:17
相关论文
共 26 条
[1]   Shortcut design of reactive distillation columns [J].
Avami, Akram ;
Marquardt, Wolfgang ;
Saboohi, Yadollah ;
Kraemer, Korbinian .
CHEMICAL ENGINEERING SCIENCE, 2012, 71 :166-177
[2]   DESIGN AND MINIMUM-REFLUX CALCULATIONS FOR SINGLE-FEED MULTICOMPONENT REACTIVE DISTILLATION-COLUMNS [J].
BARBOSA, D ;
DOHERTY, MF .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (07) :1523-1537
[3]   DESIGN AND MINIMUM-REFLUX CALCULATIONS FOR DOUBLE-FEED MULTICOMPONENT REACTIVE DISTILLATION-COLUMNS [J].
BARBOSA, D ;
DOHERTY, MF .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (09) :2377-2389
[4]   THE SIMPLE DISTILLATION OF HOMOGENEOUS REACTIVE MIXTURES [J].
BARBOSA, D ;
DOHERTY, MF .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (03) :541-550
[5]   Design of processes with reactive distillation line diagrams [J].
Bessling, B ;
Schembecker, G ;
Simmrock, KH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (08) :3032-3042
[6]   NEW TOOLS FOR THE DESIGN OF KINETICALLY CONTROLLED REACTIVE DISTILLATION-COLUMNS FOR TERNARY MIXTURES [J].
BUZAD, G ;
DOHERTY, MF .
COMPUTERS & CHEMICAL ENGINEERING, 1995, 19 (04) :395-408
[7]   A Short Method To Calculate Residue Curve Maps in Multireactive and Multicomponent Systems [J].
Carrera-Rodriguez, Marcelino ;
Gabriel Segovia-Hernandez, Juan ;
Bonilla-Petriciolet, Adrian .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (04) :2157-2166
[8]  
de Villiers WE, 2002, CHEM ENG PROG, V98, P66
[9]   Entrainer-enhanced reactive distillation [J].
Dimian, AC ;
Omota, F ;
Bliek, A .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (03) :411-420
[10]  
Doherty M.F., 2001, CONCEPTUAL DESIGN DI, V1st ed.