Fabrication of novel polyetherimide-fluorinated silica organic-inorganic composite hollow fiber membranes intended for membrane contactor application

被引:71
作者
Zhang, Yuan [1 ,2 ]
Wang, Rong [1 ,2 ]
机构
[1] Nanyang Technol Univ, Sch Civil & Environm Engn, Singapore 639798, Singapore
[2] Nanyang Technol Univ, Singapore Membrane Technol Ctr, Nanyang Environm Water Res Inst, Singapore 637141, Singapore
基金
新加坡国家研究基金会;
关键词
PEI hollow fiber membranes; Fluorinated silica; Organic-inorganic composite membranes; Hydrophobicity; Gas-liquid membrane contactor; MIXED-MATRIX MEMBRANE; MASS-TRANSFER; SURFACE MODIFICATION; PERFORMANCE; CO2; SEPARATION; NANOPARTICLES; DESALINATION; ABSORPTION;
D O I
10.1016/j.memsci.2013.04.062
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrophobic surface can be produced by either lowering the surface free energy or enhancing the surface roughness or a combination of both. This study explored a novel method to form a highly hydrophobic organic-inorganic composite hollow fiber membrane by incorporating the fluorinated silica (fSiO(2)) inorganic layer on the polyetherimide (PEI) organic substrate. The formation of the composite membrane was examined and confirmed by ATR-FTIR, TGA and SEM. Ultrasonication test was conducted to examine the structural stability of the composite membrane. The experimental results revealed that the fSiO(2) layer was tightly bonded to the PEI substrate through silane chemical reactions. The incorporation of the fSiO(2) layer on the membrane surface could enhance the surface roughness and greatly reduce the surface free energy due to the hydrophobic compound perfluorodecyltriethoxysilane (PETS). The hydrophobicity of the composite membrane surface was dramatically elevated, as evidenced by the dynamic contact angles increment, e.g. from original 66.7 degrees to 124.8 degrees for advancing values, and from 49.5 degrees to 100.6 degrees for receding values. In addition, it was observed the mechanical property of the composite membrane was better than some of the conventional polymeric membranes such as polyethersulfone (PES), and polyvinylidene fluoride (PVDF). The composite membrane was also not as brittle as the pure inorganic membrane. Highly hydrophobic membrane is the core element in gas-liquid membrane contactor and the newly developed PEI-fSiO(2) composite hollow fiber membranes were intended for the use in such application. The CO2 absorption flux of the composite membranes was investigated in both physical and chemical absorptions in a gas-liquid membrane contactor system. Moreover, the membrane contactor showed a reasonably stable performance throughout the 31 days long-term operation using a 2 M sodium taurinate aqueous solution as the liquid absorbent and pure CO2 as the feed gas. The chemical compatibility test indicated that after the long-term constant contact with the sodium taurinate, the hydrophobicity of the PEI-fSiO(2) composite membrane still maintained and was much higher than that of original PEI substrate and conventional hydrophobic polymeric membranes such as PVDF. The incorporation of the fSiO(2) inorganic layer not only offered high hydrophobicity, but also would protect the polymeric substrate from the attacks of chemical absorbents, making the membrane a longer lifespan. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:170 / 180
页数:11
相关论文
共 48 条
[1]   Amination of poly(ether imide) membranes using di- and multivalent amines [J].
Albrecht, W ;
Seifert, B ;
Weigel, T ;
Schossig, M ;
Holländer, A ;
Groth, T ;
Hilke, R .
MACROMOLECULAR CHEMISTRY AND PHYSICS, 2003, 204 (03) :510-521
[2]   Synthesis and characterization of Nafion/60SiO2-30P2O5-10ZrO2 sol-gel composite membranes for PEMFCs [J].
Aparicio, M ;
Klein, LC .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2005, 152 (03) :A493-A496
[3]   Mass transfer study and modeling of gas-liquid membrane contacting process by multistage cascade model for CO2 absorption [J].
Atchariyawut, Supakorn ;
Jiraratananon, Ratana ;
Wang, Rong .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 63 (01) :15-22
[4]   Separation of CO2 from CH4 by using gas-liquid membrane contacting process [J].
Atchariyawut, Supakorn ;
Jiraratananon, Ratana ;
Wang, Rong .
JOURNAL OF MEMBRANE SCIENCE, 2007, 304 (1-2) :163-172
[5]   Effect of membrane structure on mass-transfer in the membrane gas-liquid contacting process using microporous PVDF hollow fibers [J].
Atchariyawut, Supakorn ;
Feng, Chunsheng ;
Wang, Rong ;
Jiraratananon, Ratana ;
Liang, D. T. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :272-281
[6]   Development of high performance surface modified polyetherimide hollow fiber membrane for gas-liquid contacting processes [J].
Bakeri, Gh. ;
Ismail, A. F. ;
Rana, D. ;
Matsuura, T. .
CHEMICAL ENGINEERING JOURNAL, 2012, 198 :327-337
[7]   Effect of polymer concentration on the structure and performance of polyetherimide hollow fiber membranes [J].
Bakeri, Gh. ;
Ismail, A. F. ;
Shariaty-Niassar, M. ;
Matsuura, T. .
JOURNAL OF MEMBRANE SCIENCE, 2010, 363 (1-2) :103-111
[8]   Nafion/PTFE and zirconium phosphate modified Nafion/PTFE composite membranes for direct methanol fuel cells [J].
Chen, Li-Chun ;
Yu, T. Leon ;
Lin, Hsiu-Li ;
Yeh, Sin-Hsien .
JOURNAL OF MEMBRANE SCIENCE, 2008, 307 (01) :10-20
[9]   Effect of shear rate within the spinneret on morphology, separation performance and mechanical properties of ultrafiltration polyethersulfone hollow fiber membranes [J].
Chung, TS ;
Qin, JJ ;
Gu, J .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (06) :1077-1091
[10]   Ultem®/ZIF-8 mixed matrix hollow fiber membranes for CO2/N2 separations [J].
Dai, Ying ;
Johnson, J. R. ;
Karvan, Oguz ;
Sholl, David S. ;
Koros, W. J. .
JOURNAL OF MEMBRANE SCIENCE, 2012, 401 :76-82