Position:Home >> Abstract

Research on structure optimization and mass transfer performance for G-L membrane contactor
Authors: Chen Ying1,2, Guan Yipeng1, Guo Chungang1, Zhang Zhaocai1,
Units: Liu Guochang1, Li Xiaoming1
KeyWords: Hollow fiber membrane; G-L membrane contactor; Membrane gas absorption; Seawater flue gas desulfurization
ClassificationCode:TQ028.8 X701.3
year,volume(issue):pagination: 2012,32(3):48-51

Abstract:
In this paper, G-L membrane contactor was applied for SO2 removal from simulation flue gas using seawater as absorbent. The effects of membrane contactor structure parameters, flow rate and mode between gas and seawater, pressure gradient and SO2 concentration on mass transfer, desulfurization efficiency and membrane utility were investigated. The results showed that flow rate and pressure gradient evidently affected overall gas mass transfer coefficient on condition of low gas pressure, but the effect of SO2 concentration could be ignored. Increasing membrane absorber packing density, membrane absorption stage and cross flow mode could improve gas distribution in the flow field, increase the efficient mass transfer area and membrane utility. Compared with traditional absorption tower, novel membrane gas absorption equipment can control the gas and seawater independently, coping with gas concentration variation flexibly. In addition, the main advantages of membrane absorber are low pressure drop, resistant fouling and easy scale-up membrane absorber, so has broad industrialization application prospect.

Funds:
2008海洋公益性行业科研专项经费项目(200805033)

AuthorIntro:
陈颖(1960-),女,吉林长春人,学士,教授级高工,从事膜技术研发与应用.E-mail:chy786@tom.com

Reference:
[1] Rob Klaassen. Achieving flue gas desulphurization with membrane gas absorption [J]. Filtration & Separation, 2003, 40(10): 26-28.
[2] S.Mohebi, S.M.Mousavi, S.Kiani. Modeling and simulation of sour gas membrane-absorption system: Influence of operational parameters on species removal [J]. Journal of Natural Gas Science and Engineering, 2009, 1(6): 195-204.
[3] S.N.Ashrafizadeh, Z.Khorasani. Ammonia removal from aqueous solutions using hollow-fiber membrane contactors [J]. Chemical Engineering Journal, 2010,162(1):242-249.
[4] V.Y. Dindorea,D.W.F. Brilmanc, G.F. Versteegb. Modelling of cross-flow membrane contactors: physical mass transfer processes [J]. Journal of Membrane Science, 2005,251(1-2): 209–222.
[5] S. B. Iversen, V. K. Bhatia, K. DaNm-Johansen, G.Jonsson. Characterization of microporous membranes for use in membrane contactors [J]. Journal of Membrane Science, 1997,130(1-2):205- 217.
[6] H. Kreulen, C. A. Smolders, G. F. Verstee. Micro-
  porous hollow fiber membrane modules as gas- liquid contactors Part2. Mass transfer with chemical reaction[J]. Journal of Membrane Science, 1993, 78(3): 217-238.
[7] Matsuda N, Sakai K, Yamamoto K, et al. Effects of hollow fiber packing fraction on blood flow pattern and gas transfer rate of an intravascular oxygenator (IVOX) [J]. Journal of Membrane Science, 2000, 179(1-2):231-241.

Service:
Download】【Collect

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com

京公网安备11011302000819号