共 31 条
A developed asymmetric PVDF hollow fiber membrane structure for CO2 absorption
被引:74
作者:
Mansourizadeh, Amir
[1
,2
]
Ismail, Ahmad Fauzi
[1
]
机构:
[1] Univ Teknol Malaysia, Adv Membrane Technol Res Ctr AMTEC, Skudai 81310, Johor, Malaysia
[2] Islamic Azad Univ, Dept Chem Engn, Gachsaran Branch, Gachsaran, Iran
关键词:
PVDF hollow fiber membrane;
Characterization;
CO2;
absorption;
Membrane contactor;
MASS-TRANSFER;
GAS SEPARATION;
CONTACTING PROCESS;
PERFORMANCE;
REMOVAL;
RESISTANCE;
MORPHOLOGY;
CAPTURE;
PROGRAM;
MODEL;
D O I:
10.1016/j.ijggc.2010.09.007
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Carbon dioxide (CO2), the main greenhouse gas, has been associated with global climate change. Therefore, it is important to develop technologies to mitigate this issue. In present study, porous hydrophobic polyvinylidene fluoride (PVDF) hollow fiber membranes with developed structure for CO2 absorption were prepared via a wet spinning process. The prepared membranes were characterized in terms of morphology examination, gas permeability, critical water entry pressure (CERW) and mass transfer resistance. From the morphology examination, the membrane showed an almost sponge-like structure with inner skinless layer and ultra-thin outer skin layer. Results of gas permeation test indicated that the membrane possess very small mean pore size (3.96 nm) with high surface porosity. The CO2 absorption experiment demonstrated a significant improvement in the CO2 flux of the prepared PVDF membrane compared to the commercial porous polytetrafluoroethylene (PTFE) hollow fiber membrane. At the absorbent flow rate of 200 ml/min, CO2 flux of the PVDF membrane (4.10 x 10(-4) mol/m(2) s) was approximately 68% higher than the CO2 flux of the PTFE membrane. In addition, the results indicated that an approximate 25% CO2 flux reduction was gradually occurred at initial 26h, then the CO2 flux maintained constant over 140h of the operation. (C) 2010 Elsevier Ltd. All rights reserved.
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页码:374 / 380
页数:7
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