Process Intensification in HiGee Absorption and Distillation: Design Procedure and Applications

被引:122
作者
Agarwal, Lava [1 ]
Pavani, V. [1 ]
Rao, D. P. [1 ]
Kaistha, N. [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Kanpur 208016, Uttar Pradesh, India
关键词
ROTATING PACKED-BED; PRESSURE-DROP; SPLIT PACKING; MASS-TRANSFER; GAS-FLOW; MALDISTRIBUTION; CONTACTOR; REMOVAL;
D O I
10.1021/ie101195k
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hi Gee technology is emerging as an alternative to conventional tray and packed towers for mass-transfer applications. To evaluate the process intensification (volume reduction) potential of the technology, a systematic design procedure is developed in this work. Hi Gee designs using split packing innovation of Chandra et al. [Ind. Eng. Chem. Res. 2005, 44, 4051-4060] are developed for four industrially relevant distillation and absorption systems. Comparison with conventional packed or tray tower designs shows that significant volume reduction is possible. For the systems studied, the process intensification achieved is particularly impressive when the gas side mass-transfer resistance is dominant. The results suggest that split packing design innovation may be particularly suitable for intensification of gas side mass-transfer resistance controlled processes.
引用
收藏
页码:10046 / 10058
页数:13
相关论文
共 28 条
[1]   Process intensification: Visual study of liquid maldistribution in rotating packed beds [J].
Burns, JR ;
Ramshaw, C .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (08) :1347-1352
[2]   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
[3]   Packing characteristics for mass transfer in a rotating packed bed [J].
Chen, Yu-Shao ;
Lin, Fang-Yi ;
Lin, Chia-Chang ;
Tai, Clifford Yi-Der ;
Liu, Hwai-Shen .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (20) :6846-6853
[4]  
Harbold G, 2008, 7 INT C PROC INT ALB
[5]  
Ji J, 2008, US Patent, Patent No. [7,344,126 B2, 7344126]
[6]   Distillation studies in a high-gravity contactor [J].
Kelleher, T ;
Fair, JR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (12) :4646-4655
[7]  
Kolev Nikolai., 2006, PACKED BED COLUMNS A, VLst
[8]   SOLUBILITY OF CRBON DIOXIDE IN AQUEOUS DIETHANOLAMINE SOLUTIONS AT HIGH-PRESSURES [J].
LEE, JIL ;
MATHER, AE ;
OTTO, FD .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1972, 17 (04) :465-&
[9]   Removal of VOCs from gaseous streams in a high-voidage rotating packed bed [J].
Lin, CC ;
Wei, TY ;
Liu, WT ;
Shen, KP .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2004, 37 (12) :1471-1477
[10]   Distillation in a rotating packed bed [J].
Lin, CC ;
Ho, TJ ;
Liu, WT .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2002, 35 (12) :1298-1304