Intensified Reaction and Separation Systems

被引:63
作者
Gorak, Andrzej [1 ,2 ]
Stankiewicz, Andrzej [3 ]
机构
[1] Dortmund Univ Technol, Lab Fluid Separat, Dept Biochem & Chem Engn, D-44227 Dortmund, Germany
[2] Lodz Univ Technol, Dept Proc & Environm Engn, PL-90924 Lodz, Poland
[3] Delft Univ Technol, Proc & Energy Dept, NL-2628 CA Delft, Netherlands
来源
ANNUAL REVIEW OF CHEMICAL AND BIOMOLECULAR ENGINEERING, VOL 2 | 2011年 / 2卷
关键词
process intensification; reactive separations; hybrid separations; structured reactors; alternative energy forms; multifunctionality; HEXAPOLE STATE-SELECTION; STRUCTURED PACKINGS; MASS-TRANSFER; BRUTE FORCE; INDUSTRIAL APPLICATIONS; HYBRID SEPARATION; REACTION DYNAMICS; VAPOR PERMEATION; PROCESS DESIGN; FLUE-GAS;
D O I
10.1146/annurev-chembioeng-061010-114159
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Process intensification follows four main goals: to maximize the effectiveness of intra- and intermolecular events, to give each molecule the same processing experience, to optimize the driving forces/maximize specific interfacial areas, and to maximize the synergistic effects of partial processes. This paper shows how these goals can be reached in reaction and separation systems at all relevant time and length scales and is focused on the structuring of reactors and separation units, on the use of different energy forms to improve the reaction and separation, on combining and superimposing of different phenomena in one integrated unit or reactor, and on the application of oscillations for intensification of reaction and separation processes.
引用
收藏
页码:431 / 451
页数:21
相关论文
共 131 条
[71]   Reactive distillation in a dividing wall column: Rate-based modeling and simulation [J].
Mueller, Ivo ;
Kenig, Eugeny Y. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (11) :3709-3719
[72]  
NEIS U, 2002, REP SANIT ENG, V35, P79
[73]  
Ni X., 2006, INNOV PHARM TECHNOL, V20, P90
[74]   Reactant-selective hydrogenation over composite silicalite-1-coated Pt/TiO2 particles [J].
Nishiyama, N ;
Ichioka, K ;
Park, DH ;
Egashira, Y ;
Ueyama, K ;
Gora, L ;
Zhu, WD ;
Kapteijn, F ;
Moulijn, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (05) :1211-1215
[75]   Attainable regions for reaction with separation [J].
Nisoli, A ;
Malone, MF ;
Doherty, MF .
AICHE JOURNAL, 1997, 43 (02) :374-387
[76]   Modelling of reactive separation processes:: reactive absorption and reactive distillation [J].
Noeres, C ;
Kenig, EY ;
Górak, A .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2003, 42 (03) :157-178
[77]  
Notz R, 2007, CHEM ENG RES DES, V85, P510, DOI [10.1205/cherd06085, 10.1205/cherd.06085]
[78]  
OHLIGSCHLAGER A, 2006, P DISTILLATION ABSOR, P854
[79]   Equipment improvement trends in distillation [J].
Olujic, Z. ;
Joedecke, M. ;
Shilkin, A. ;
Schuch, G. ;
Kaibel, B. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2009, 48 (06) :1089-1104
[80]   Evaluation of spinning disk reactor technology for the manufacture of pharmaceuticals [J].
Oxley, P ;
Brechtelsbauer, C ;
Ricard, F ;
Lewis, N ;
Ramshaw, C .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (07) :2175-2182