Membrane contactors and catalytic membrane reactors in process intensification

被引:34
作者
Drioli, E
Criscuoli, A
Curcio, E
机构
[1] Univ Calabria, ITM NR, Res Inst Membrane Technol, I-87030 Arcavacata Di Rende, Italy
[2] Univ Calabria, Dept Chem & Mat Engn, I-87030 Arcavacata Di Rende, Italy
[3] Univ Calabria, ITM CNR, Res Inst Membrane Technol, I-87030 Arcavacata Di Rende, Italy
关键词
D O I
10.1002/ceat.200300012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane operations, with their intrinsic characteristics of efficiency and operational simplicity, high selectivity and permeability for the transport of specific components, compatibility between different membrane operations in integrated systems, low energetic requirement, good stability under operating conditions, environment-compatibility, easy control and scale-up, and large operational flexibility, represent an interesting answer for the rationalisation of chemical productions. Many membrane operations are practically based on the same hardware (materials), only differing in their software (methods). The traditional membrane separation operations (reverse osmosis, micro-, ultra- and nanofiltration, electrodialysis, pervaporation etc.), already largely utilised in many different areas, are today completed with new membrane systems such as catalytic membrane reactors and membrane contactors. At present, the possibility to redesign important industrial production cycles by combining various membrane operations available in the separation and conversion units, so realising highly integrated membrane processes, is an attractive opportunity because of the synergic effects that can be reached. Additionally, the design of the integrated membrane production cycle in principle satisfy, the requirements for an advanced process intensification strategy. Membrane crystallizers, membrane emulsifiers, membrane strippers and scrubbers, membrane distillation, membrane extractors. etc., can be realized and integrated in the production line together with other existing membrane operations for advanced molecular separation and chemical transformations, overcoming existing limits of the more traditional membrane processes.
引用
收藏
页码:975 / 981
页数:7
相关论文
共 15 条
[1]   The effect of ultrafiltration on the subsequent concentration of grape juice by osmotic distillation [J].
Bailey, AFG ;
Barbe, AM ;
Hogan, PA ;
Johnson, RA ;
Sheng, J .
JOURNAL OF MEMBRANE SCIENCE, 2000, 164 (1-2) :195-204
[2]   Clarification and concentration of citrus and carrot juices by integrated membrane processes [J].
Cassano, A ;
Drioli, E ;
Galaverna, G ;
Marchelli, R ;
Di Silvestro, G ;
Cagnasso, P .
JOURNAL OF FOOD ENGINEERING, 2003, 57 (02) :153-163
[3]   An economic feasibility study for water gas shift membrane reactor [J].
Criscuoli, A ;
Basile, A ;
Drioli, E ;
Loiacono, O .
JOURNAL OF MEMBRANE SCIENCE, 2001, 181 (01) :21-27
[4]   Energetic and exergetic analysis of an integrated membrane desalination system [J].
Criscuoli, A ;
Drioli, E .
DESALINATION, 1999, 124 (1-3) :243-249
[5]  
CRISCUOLI A, 2003, IN PRESS ANN NY ACAD
[6]   Recovery of fumaric acid by membrane crystallization in the production of L-malic acid [J].
Curcio, E ;
Di Profio, G ;
Drioli, E .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (01) :63-73
[7]   Cogeneration power desalting plants in Kuwait: a new trend with reverse osmosis desalters [J].
Darwish, MA ;
Al-Najem, N .
DESALINATION, 2000, 128 (01) :17-33
[8]   Integrated membrane operations for seawater desalination [J].
Drioli, E ;
Criscuoli, A ;
Curcio, E .
DESALINATION, 2002, 147 (1-3) :77-81
[9]   Progress and new perspectives on integrated membrane operations for sustainable industrial growth [J].
Drioli, E ;
Romano, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (05) :1277-1300
[10]   ABSORPTION OF CARBON-MONOXIDE IN HOLLOW-FIBER MEMBRANES [J].
GHOSH, AC ;
BORTHAKUR, S ;
DUTTA, NN .
JOURNAL OF MEMBRANE SCIENCE, 1994, 96 (03) :183-192