Reactive and membrane-assisted distillation: Recent developments and perspective

被引:78
作者
Lutze, Philip [1 ]
Gorak, Andrzej [1 ,2 ]
机构
[1] Tech Univ Dortmund, Lab Fluid Separat, Dept Biochem & Chem Engn, D-44227 Dortmund, Germany
[2] Lodz Univ Technol, Dept Proc & Environm Engn, PL-90924 Lodz, Poland
关键词
Hybrid separations; Reactive distillation; Organic solvent nanofiltration; Pervaporation; Vapor permeation; PROCESS INTENSIFICATION; HYBRID SEPARATION; OPTIMAL-DESIGN; SOLVENT NANOFILTRATION; GRAPHICAL-METHOD; SHORTCUT DESIGN; N-BUTANOL; PERVAPORATION; OPTIMIZATION; METHODOLOGY;
D O I
10.1016/j.cherd.2013.07.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The number of design and processing requirements in the chemical and biochemical industries are increasing to adapt to rapidly changing markets and the global competition, as well as to shift toward more sustainable production and to meet the need for new and innovative products. Hence, more efficient processes are needed. Reactive and membrane-assisted distillation can achieve higher efficiencies and high capacities. They are believed to be important technologies for retrofitting existing processes and for incorporation into future processes for efficient and flexible (bio)chemical production. This manuscript aims to briefly summarize past research with a more detailed view on current research areas within the application, modeling, design and optimization of reactive- and membrane-assisted distillation processes, with a special focus on pervaporation, vapor permeation and organic solvent nanofiltration. By identifying the current challenges combined with future perspectives of the chemical processing industry, a personal opinion on future research trends, needs and challenges for these technologies is given. These technologies need to be addressed to increase trust in the potential and reliability of reactive- and membrane-assisted distillation, which would enable the intensification of manufacturing processes. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1978 / 1997
页数:20
相关论文
共 101 条
[1]   Semicontinuous reactive extraction and reactive distillation [J].
Adams, Thomas A., II ;
Seider, Warren D. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (3A) :245-262
[2]   Designing reactive distillation processes: present and future [J].
Almeida-Rivera, CP ;
Swinkels, PLJ ;
Grievink, J .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (10) :1997-2020
[3]   Phase Equilibria for Reactive Distillation of Propyl Propanoate. Pure Component Property Data, Vapor-Liquid Equilibria, and Liquid-Liquid Equilibria [J].
Altman, Ernesto ;
Stefanidis, Georgios D. ;
van Gerven, Thomas ;
Stankiewicz, Andrzej I. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (05) :2322-2328
[4]   Process Intensification of Reactive Distillation for the Synthesis of n-Propyl Propionate: The Effects of Microwave Radiation on Molecular Separation and Esterification Reaction [J].
Altman, Ernesto ;
Stefanidis, Georgios D. ;
van Gerven, Thomas ;
Stankiewicz, Andrzej I. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (21) :10287-10296
[5]  
[Anonymous], 2007, MODELING PROCESS INT
[6]   Shortcut design of reactive distillation columns [J].
Avami, Akram ;
Marquardt, Wolfgang ;
Saboohi, Yadollah ;
Kraemer, Korbinian .
CHEMICAL ENGINEERING SCIENCE, 2012, 71 :166-177
[7]   Simultaneous optimal synthesis, design and operation of batch and continuous hybrid separation processes [J].
Barakat, Tajalasfia M. M. ;
Sorensen, Eva .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2008, 86 (A3) :279-298
[8]   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
[9]   Shortcut design methods for hybrid membrane/distillation processes for the separation of nonideal multicomponent mixtures [J].
Bausa, J ;
Marquardt, W .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (06) :1658-1672
[10]   Design and synthesis of distillation systems using a driving-force-based approach [J].
Bek-Pedersen, E ;
Gani, R .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (03) :251-262