Membrane assisted fluidized bed reactors:: Potentials and hurdles

被引:77
作者
Deshmukh, S. A. R. K.
Heinrich, S.
Moerl, L.
Annaland, M. van Sint
Kuipers, J. A. M.
机构
[1] Otto Von Guericke Univ, Inst Apparatus & Environm Technol, Fac Proc & Syst Engn, D-39106 Magdeburg, Germany
[2] Univ Twente, Fac Sci & Technol, NL-7500 AE Enschede, Netherlands
关键词
review; fluidized bed reactor; integrated membranes; selective product removal; controlled reactant dozing; mixing; heat transfer; modeling;
D O I
10.1016/j.ces.2006.08.062
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Recent advances in the development of more stable membranes with increased permeance have significantly enhanced the possibilities for integrating membranes into catalytic reactors in order to achieve a major increase in reactor performance by process integration and process intensification. Several reviews and even special issues of catalysis related journals illustrate the significant progress in the field of inorganic membrane reactors within the last two decades. Chemical engineers and material scientists have joined forces and addressed this topic from various view-points. In spite of their considerable efforts in these directions, the application of the membrane reactors, especially packed bed membrane reactors, in commercial processes has been very limited because of technical as well as economical drawbacks. The most recent trend in membrane reactor technology has been in the direction of incorporating inorganic membranes into fluidized beds to combine the perm-selective and controlled dosing capabilities of membranes with excellent gas-solid contact and heat transfer capabilities of fluidized beds, thereby overcoming the limitations often prevailing in packed bed membrane reactors. The opportunities for this novel fluidized bed membrane reactor compared to conventional reactors and packed bed membrane reactors have never been systematically reviewed before. This paper seeks to review literature and new developments in the area of membrane assisted fluidized bed reactors, with special emphasis on possible applications, integration of different membranes in the fluidized beds, reactor modelling studies, experimental demonstration of various reactor concepts and future prospects and hurdles for commercialization. Finally, an assessment of the state of the art has been given and directions for future research are indicated. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:416 / 436
页数:21
相关论文
共 102 条
[1]  
Abashar MEE, 2004, INT J HYDROGEN ENERG, V29, P799, DOI 10.1016/j.jjhydene.2003.09.010
[2]   Application of the generic fluidized-bed reactor model to the fluidized-bed membrane reactor process for steam methane reforming with oxygen input [J].
Abba, IA ;
Grace, JR ;
Bi, HT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (12) :2736-2745
[3]  
Abba IA, 2002, CHEM ENG SCI, V57, P4797
[4]   FLUIDIZED-BED REACTORS WITHOUT AND WITH SELECTIVE MEMBRANES FOR THE CATALYTIC DEHYDROGENATION OF ETHYLBENZENE TO STYRENE [J].
ABDALLA, BK ;
ELNASHAIE, SSEH .
JOURNAL OF MEMBRANE SCIENCE, 1995, 101 (1-2) :31-42
[5]   The fluidized bed membrane reactor system: A pilot scale experimental study [J].
Adris, A. M. ;
Lim, C. J. ;
Grace, J. R. .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) :5833-5843
[6]   Characteristics of fluidized-bed membrane reactors: Scale-up and practical issues [J].
Adris, AEM ;
Grace, JR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (11) :4549-4556
[7]   A FLUIDIZED-BED MEMBRANE REACTOR FOR THE STEAM REFORMING OF METHANE [J].
ADRIS, AM ;
ELNASHAIE, SSEH ;
HUGHES, R .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (05) :1061-1070
[8]  
ADRIS AM, 1994, Patent No. 5326550
[9]   Oxidative dehydrogenation of ethane in a fluidized bed membrane reactor [J].
Ahchieva, D ;
Peglow, M ;
Heinrich, S ;
Mörl, L ;
Wolff, T ;
Klose, F .
APPLIED CATALYSIS A-GENERAL, 2005, 296 (02) :176-185
[10]   Avoidance of flammability and temperature runaway during oxidative dehydrogenation using a distributed feed [J].
Al-Sherehy, FA ;
Adris, AM ;
Soliman, MA ;
Hughes, R .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (23) :3965-3976