A review on process intensification in HiGee distillation

被引:84
作者
Garcia, German E. Cortes [1 ]
van der Schaaf, John [1 ]
Kiss, Anton A. [2 ,3 ]
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Eindhoven, Netherlands
[2] AkzoNobel Res, Deventer, Netherlands
[3] Univ Twente, Fac Sci & Technol, Enschede, Netherlands
关键词
HiGee; distillation; gas-liquid contactor; heterogeneous catalyst; rotating packed bed; ROTATING PACKED-BED; MASS-TRANSFER CHARACTERISTICS; VOLATILE ORGANIC-COMPOUNDS; CARBON-DIOXIDE ABSORPTION; BLADE PACKINGS; GAS-LIQUID; ZIGZAG BED; TRANSFER PERFORMANCE; PRESSURE-DROP; VISCOUS MEDIA;
D O I
10.1002/jctb.5206
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
This review paper describes the state-of-the-art in the field of HiGee contactors used for gas-liquid mass transfer processes, with a special focus on distillation, and for heterogeneously catalyzed reactions. Several types of rotating beds are discussed, including single-block rotating packed-bed, split-packing rotating bed, rotating zigzag bed, two-stage counter-current rotating packed bed, blade packing rotating packed bed, rotating bed with blade packing and baffles, counter-flow concentric-ring rotating bed and crossflowconcentric-baffle rotating bed. The working principles of HiGee technology, as well as the modeling, design and control aspects, and practical applications are explained and discussed. In addition, this paper addresses the advantages and disadvantages with respect to mass-transfer performance, pressure drop, rotor complexity and suitability to perform continuous distillation and to be filled with catalyst packing for heterogeneous reactions. (C) 2017 Society of Chemical Industry
引用
收藏
页码:1136 / 1156
页数:21
相关论文
共 143 条
[1]   Process Intensification in HiGee Absorption and Distillation: Design Procedure and Applications [J].
Agarwal, Lava ;
Pavani, V. ;
Rao, D. P. ;
Kaistha, N. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (20) :10046-10058
[2]   Development of a Higee bioreactor (HBR) for production of polyhydroxyalkanoate: Hydrodynamics, gas-liquid mass transfer and fermentation studies [J].
Boodhoo, Kamelia V. K. ;
Cartwright, Craig D. ;
Vicevic, Marija ;
Prieto, Maria A. ;
Tortajada, Marta .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (07) :748-758
[3]   Process intensification: Visual study of liquid maldistribution in rotating packed beds [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (08) :1347-1352
[4]   Process intensification: operating characteristics of rotating packed beds - determination of liquid hold-up for a high-voidage structured packing [J].
Burns, JR ;
Jamil, JN ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (13) :2401-2415
[5]   Characteristics of flow in a rotating packed bed (HIGEE) with split packing [J].
Chandra, A ;
Goswami, PS ;
Rao, DP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (11) :4051-4060
[6]   Pt-catalyzed ozonation of aqueous phenol solution using high-gravity rotating packed bed [J].
Chang, Chia-Chi ;
Chiu, Chun-Yu ;
Chang, Ching-Yuan ;
Chang, Chiung-Fen ;
Chen, Yi-Hung ;
Ji, Dar-Ren ;
Tseng, Jyi-Yeong ;
Yu, Yue-Hwa .
JOURNAL OF HAZARDOUS MATERIALS, 2009, 168 (2-3) :649-655
[7]   Combined photolysis and catalytic ozonation of dimethyl phthalate in a high-gravity rotating packed bed [J].
Chang, Chia-Chi ;
Chiu, Chun-Yu ;
Chang, Ching-Yuan ;
Chang, Chiung-Fen ;
Chen, Yi-Hung ;
Ji, Dar-Ren ;
Yu, Yue-Hwa ;
Chiang, Pen-Chi .
JOURNAL OF HAZARDOUS MATERIALS, 2009, 161 (01) :287-293
[8]  
Chen J-F, 2009, GPE 24 EP C VEN IT, V25
[9]   Control of Product Distribution of Fischer-Tropsch Synthesis with a Novel Rotating Packed-Bed Reactor: From Diesel to Light Olefin [J].
Chen, Jian-Feng ;
Liu, Yi ;
Zhang, Yi .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (25) :8700-8703
[10]   Modeling ozonation process with pollutant in a rotating packed bed [J].
Chen, YH ;
Chiu, CY ;
Chang, CY ;
Huang, YH ;
Yu, YH ;
Chiang, PC ;
Shie, JL ;
Chiou, CS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (01) :21-29