Project/Area Number |
11450299
|
Research Category |
Grant-in-Aid for Scientific Research (B).
|
Allocation Type | Single-year Grants |
Section | 一般 |
Research Field |
反応・分離工学
|
Research Institution | Kyoto Institute of Technology |
Principal Investigator |
TERAMOTO Masaaki Kyoto Inst.of Technology, Faculty of Engineering and Design, Professor, 工芸学部, 教授 (60026086)
|
Co-Investigator(Kenkyū-buntansha) |
MAKI Taisuke Kyoto Inst.of Technology, Faculty of Engineering and Design, Research Associate, 工芸学部, 助手 (10293987)
MATSUYAMA Hideto Kyoto Inst.of Technology, Faculty of Engineering and Design, Associate Prof., 工芸学部, 助教授 (50181798)
|
Project Period (FY) |
1999 – 2000
|
Project Status |
Completed (Fiscal Year 2000)
|
Budget Amount *help |
¥6,500,000 (Direct Cost: ¥6,500,000)
Fiscal Year 2000: ¥2,000,000 (Direct Cost: ¥2,000,000)
Fiscal Year 1999: ¥4,500,000 (Direct Cost: ¥4,500,000)
|
Keywords | sapercritica / CO_2 / phase Separation / Microporous Membrane / Polystyrene / Cellulose Acetate / 光散乱法 / spinodal分解 |
Research Abstract |
Microporous polystyrene membranes were prepared by the phase separation process using the supercritical CO_2 as a nonsolvent for the polymer solution. The thin polymer solution in a laboratory dish was located inside a cell and the supercritical CO_2 was introduced to induce the phase separation. The dry flat microporous membranes were obtained without collapse of the structure after the CO_2 pressure was diminished. Effects of the experimental conditions such as the CO_2 pressure, the polymer concentration and the temperature on the average pore size and membrane porosity were investigated. In the preparation of porous cellulose acetate membrane by phase separation with supercritical CO_2, five kinds of diluents were used and effect of the diluent on the membrane structure and performance was investigated. As the mutual affinity between diluent and supercritical CO_2 decreased, the membrane porosity and the average pore size near the center position increased and the thicker skin layer was formed at the top surface. In all cases, macrovoid was not formed, although the phase separation occurred instantaneously after CO_2 was introduced. This was a contrast to the macrovoid formation in the condition of instantaneous phase separation using water as nonsolvent. The membrane performances such as the solute rejection coefficient and the water permeability were measured for the obtained porous membranes.
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