세 가지의 다른 화학 성분으로 구성된 터폴리머는 기체분리막에 거의 활용되지 못하였다. 본 연구에서는 poly(2-[3-(2H-Benzotriazol-2-yl)-4-hydroxyphenyl] ethylmethacrylate)(PBEM), poly(oxyethylene methacrylate)(POEM), methyl methacrylate (MMA)로 구성된 터폴리머를 자유라디칼 중합법으로 합성하였고, 이를 기반으로 하여 이산화탄소/질소 분리를 위한 복합막 제조 공정을 개발하였다. 합성된 PBEM-PMMA-POEM 용액을 다공성 폴리설폰 지지체위에 코팅하여 복합막을 제조하였다. 성공적인 중합, 특성 및 구조분석을 위하여 푸리에 변환 적외선 분광학, X-ray 회절분석법, 열중량 분석 및 전계방사 주사전자 현미경을 사용하였다. PBEM-PMMA-POEM 터폴리머 분리막의 기체 투과도 및 이산화탄소/질소 선택도를 $25^{\circ}C$에서 측정하였다. 최고의 이산화탄소/질소 선택도는 30.2에 도달하였으며, 이산화탄소 투과도는 57.4 GPU ($1GPU=10^{-6}cm^3$(STP)/($s\;cm^2\;cmHg$))이었다.
세 가지의 다른 화학 성분으로 구성된 터폴리머는 기체분리막에 거의 활용되지 못하였다. 본 연구에서는 poly(2-[3-(2H-Benzotriazol-2-yl)-4-hydroxyphenyl] ethylmethacrylate)(PBEM), poly(oxyethylene methacrylate)(POEM), methyl methacrylate (MMA)로 구성된 터폴리머를 자유라디칼 중합법으로 합성하였고, 이를 기반으로 하여 이산화탄소/질소 분리를 위한 복합막 제조 공정을 개발하였다. 합성된 PBEM-PMMA-POEM 용액을 다공성 폴리설폰 지지체위에 코팅하여 복합막을 제조하였다. 성공적인 중합, 특성 및 구조분석을 위하여 푸리에 변환 적외선 분광학, X-ray 회절분석법, 열중량 분석 및 전계방사 주사전자 현미경을 사용하였다. PBEM-PMMA-POEM 터폴리머 분리막의 기체 투과도 및 이산화탄소/질소 선택도를 $25^{\circ}C$에서 측정하였다. 최고의 이산화탄소/질소 선택도는 30.2에 도달하였으며, 이산화탄소 투과도는 57.4 GPU ($1GPU=10^{-6}cm^3$(STP)/($s\;cm^2\;cmHg$))이었다.
Terpolymers, which are chemical compounds composed of three different chemical compounds, have rarely been utilized for gas separation membranes. In this study, we demonstrate a simple process to fabricate a composite membrane for $CO_2/N_2$ separation based on a terpolymer synthesized fr...
Terpolymers, which are chemical compounds composed of three different chemical compounds, have rarely been utilized for gas separation membranes. In this study, we demonstrate a simple process to fabricate a composite membrane for $CO_2/N_2$ separation based on a terpolymer synthesized from poly(2-[3-(2H-benzotriazol-2-yl)-4-hydroxyphenyl] ethylmethacrylate)(PBEM), poly(oxyethylene methacrylate)(POEM), and methyl methacrylate (MMA) via free radical polymerization. A solution of the as-synthesized PBEM-PMMA-POEM was coated onto a microporous polysulfone (PSf) support to form a composite membrane. The successful polymerization and the characteristics and morphology of the membrane were characterized by Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD) analysis, thermogravimetric analysis (TGA), and field emission scanning electron microscopy (FE-SEM). The gas permeance and $CO_2/N_2$ selectivity of the PBEM-PMMA-POEM terpolymer membrane were measured at $25^{\circ}C$. A maximum $CO_2/N_2$ selectivity of 30.2 was obtained at a $CO_2$ permeance of 57.4 GPU ($1GPU=10^{-6}cm^3$(STP)/($s\;cm^2\;cmHg$)).
Terpolymers, which are chemical compounds composed of three different chemical compounds, have rarely been utilized for gas separation membranes. In this study, we demonstrate a simple process to fabricate a composite membrane for $CO_2/N_2$ separation based on a terpolymer synthesized from poly(2-[3-(2H-benzotriazol-2-yl)-4-hydroxyphenyl] ethylmethacrylate)(PBEM), poly(oxyethylene methacrylate)(POEM), and methyl methacrylate (MMA) via free radical polymerization. A solution of the as-synthesized PBEM-PMMA-POEM was coated onto a microporous polysulfone (PSf) support to form a composite membrane. The successful polymerization and the characteristics and morphology of the membrane were characterized by Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD) analysis, thermogravimetric analysis (TGA), and field emission scanning electron microscopy (FE-SEM). The gas permeance and $CO_2/N_2$ selectivity of the PBEM-PMMA-POEM terpolymer membrane were measured at $25^{\circ}C$. A maximum $CO_2/N_2$ selectivity of 30.2 was obtained at a $CO_2$ permeance of 57.4 GPU ($1GPU=10^{-6}cm^3$(STP)/($s\;cm^2\;cmHg$)).
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제안 방법
FT-IR spectra of the synthesized copolymer were obtained in the frequency range from 4000 to 500 cm-1 with an Excalibur series FT-IR instrument (DIGLAB CO., Hannover, Germany) to confirm the successful polymerization. XRD patterns of the sample were collected at 30 kV and 15 mA for structural analysis.
In this work, we demonstrate a simple process to fabricate a composite membrane for CO2/N2 separation based on a terpolymer synthesized from PBEM, POEM, and methyl methacrylate (MMA) via free radical polymerization. A solution containing the as-synthesized PBEM-PMMA-POEM was coated onto a polysulfone (PSf) substrate.
The selectivity of the membrane was calculated by the ratio of the permeances of the gases, in this case, the permeability of the more permeable gas, CO2, was divided by that of the less permeable gas, N2. The gas permeance of the membrane was measured for 2 h using the individual gases to determine their steady-state performance, and the flowrate measurements were taken under pressures of 1 to 5 bar to investigate the effect of changes in pressure on the permeability and selectivity of the membrane.
In conclusion, we fabricated a high-performance gas separation membrane based on the CO2-philic terpolymer PBEM-PMMA-POEM, which was synthesized via free radical polymerization. The PBEM-PMMAPOEM terpolymer was composed of rigid hydrophobic BEM and MMA segments and flexible hydrophilic POEM segments.
2°, and the peak at 32° was thought to be related to the PMMA peak at 30°. These XRD results suggest that overall, the copolymerization was successful based on the evidence of POEM and PMMA nanostructures in the terpolymer; the PBEM peak was not significantly expressed because of the low ratio of PBEM used in the synthesis.
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