• Membrane Journal
• /
• v.25 no.2
• /
• pp.107-114
• /
• 2015

PTMSP-NaA zeolite composite membranes were prepared by adding 0~50 wt% NaA zeolite to PTMSP. The membranes were characterized by FT-IR, $^1H$-NMR, GPC, DSC, TGA, SEM. The permeabilities of $H_2$ and $N_2$ gases through PTMSP-NaA zeolite composite membranes was studied as a function of NaA zeolite contents. According to TGA measurements, when zeolite was inserted into the polymer, weight loss temperature and weight loss wt% of PTMSP-NaA zeolite composite membranes were decreased. Based on SEM observation, NaA zeolite was dispersed in the PTMSP-NaA zeolite composite membrane with the size $2{\sim}5{\mu}m$. The permeability of PTMSP-NaA zeolite composite membranes increased added as NaA zeolite content increased. On the contrary, the selectivity ($H_2/N_2$) of the composite membranes decreased as NaA zeolite content increased. PTMSP-NaA zeolite composite membrane showed better permeability and selectivity ($H_2/N_2$) of $H_2$ and $N_2$ than PTMSP-NaY zeolite composite membrane.

• Korean Journal of Food Science and Technology
• /
• v.22 no.7
• /
• pp.812-816
• /
• 1990

This study describes the sorbitol production with permeabilized cells of Zymomonas mobilis immobilized in Ca-alginate. Toluene treated cells lose activity of glucose-fructose oxidoreductase due to the leaking of enzyme from the cells. To prevent this leakage, the permeabilized cells were treated with 0.25% glutaraldehyde by stirring for 1 h at room temperature. A continuous process with glutaraldehyde treated cells was developed and no significant reduction in the degree of conversion occurred during 210 h operation. The productivities were estimated to be about $7.2{\sim}7.5\;g/l-h$ for sorbitol at dilution rate $0.18\;h^{-1}$.

• Membrane Journal
• /
• v.15 no.3
• /
• pp.206-212
• /
• 2005

Acid-resistant poly(vinyl alcohol) (PVA) membranes connected with ethylene and ether groups were prepared via a thermal crosslinking reaction by varying the ratio of PVA to ethylene glycol diglycidyl ether (EGDE). The crosslinked membranes were characterized using FT-IR and swelling tests, respectively. Pervaporation behaviors with the PVA membranes were investigated for aqueous TFEA (2,2,2-trifluoroethanol) as a function of EGDE content and operating temperature. The pervaporation properties far MA (methacrylic acid)/water mixture were also carried out with the optimized PVA membrane. The PVA membranes prepared with EGDE showed more excellent acid-resistance than those crosslinked with gluaraldehyde. The membranes showed high permeation fluxes of 0.1 and $0.3\;km^2h$ and high separation factors of 100 and 900 in the $96\;wt\%$ TFEA and MA aqueous fred mixtures at high temperature above $80^{\circ}C$, respectively. These confirmed theses membranes could be used in esterification membrane reactor process for the production of 2,2,2-trifluoroethylmetacrylate (TFEMA).

• Membrane Journal
• /
• v.33 no.6
• /
• pp.377-382
• /
• 2023

In this study, a PEBAX/PVDF composite membrane was fabricated, and its pervaporation performance was tested in an ethanol/water mixture. In addition, we attempted to improve the pervaporation performance of the composite membrane by forming a ZIF-8 layer on the surface of the PVDF substrate. The thickness of selective layer was optimized by comparing the pervaporation performance depending on the PEBAX thickness. A pervaporation test was performed on the Ethanol/Water mixture. As a result, the composite membrane using PVDF substrate with ZIF-8 layer had a flux of 1.98 kg/m²h and separation factor of 3.88, showing higher values of both permeation flux and selectivity than the composite membrane using bare PVDF substrate.

• Membrane Journal
• /
• v.10 no.3
• /
• pp.148-154
• /
• 2000

Poly(vinyl alcohol)(PVA)/sulfur-siccinic acid(SSA) membrane performances have been studied for the vapor permeation separation of methyl tort-butyl ether(MTBE)/methanol mixtures with varying operation temperatures, amount of cross-linking agents, and feed compositions. 1'here are two factors, the membrane network and the hydrogen bonding, in the swelling measurements of PVA/SSA membranes. These two factors act interdependently on the membrane swelling. The sulfuric acid group in SSA took an important role in the membrane performance. The cross-linking effect might be more dominant than the hydrogen bonding effect due to the sulfuric acid group at 7% SSA membrane. Hydrogen bonding effect was more important for 5% SSA membrane. In vapor permeation, density or concentration of methanol in vapor feed is lower than that of methanol in liquid feed, as a result, the hydrogen bonding portion between the solvent and the hydroxyl group in PVA is reduced in vapor permeation. In this case, the 7% SSA membrane shows the highest separation factor of 2187 with the flux of 4.84g/$m^2$hr for MTBE/methanol=80/20 mixtures at 3$0^{\circ}C$.

• Proceedings of the Korean Vacuum Society Conference
• /
• 2014.02a
• /
• pp.275.2-275.2
• /
• 2014

현재 자동차 분야에서 차량 경량화의 한 수단으로 자동차용 유리를 고강도 투명 플라스틱 소재인 Polycarbonate(PC)로 대체하고자 하는 연구가 이루어지고 있다. 하지만, PC의 낮은 내마모 특성과 자외선에 의한 열화 및 변색 현상은 해결하여야 할 문제점으로 지적되고 있으며, 에너지 소비 저감을 위하여 적외선 영역 반사율(reflectance)이 높은 저방사(low emissivity) 특성이 요구되고 있다. 본 연구에서는, ICP-assisted reactive magnetron sputtering 장비를 이용하여 투과율(transmittance)이 확보되고, 고경도 특성을 갖는 Al-Si-N와 300 nm 파장 이하의 자외선 차단 특성이 있는 SiN:H 그리고 저방사 특성을 위해 Al을 증착하였고, 박막의 증착 순서는 SiN:H 박막을 가장 아래에 증착하고 그 위에 Al/Al-Si-N 박막을 다층으로 형성하였다. 박막의 chemical state와 crystallinity를 확인하기 위하여 XPS(X-ray Photoelectron Spectroscopy), XRD (X-ray Diffraction)를 이용하여 분석하였다. Knoop ${\mu}$-hardness tester와 Taber tester를 이용하여 경도 및 내마모 특성을 분석하였다. 제작된 샘플의 Al-Si-N 박막 경도는 Si 비율에 따라 다른 경도 특성을 갖는데, 실제 Si/(Al+Si) 비율이 24%에서 최대 31 GPa의 경도 값을 갖는 것을 확인하였다. UV-Vis Spectrometer를 이용하여 250 nm~700 nm 파장의 투과율을 측정하였고, 자외선 영역의 경우 SiN:H 박막에 의해 300 nm 이하의 파장에서 2% 이하의 투과율을 확인하였다. 그리고 FT-IR(Fourier Transform Infrared Spectroscopy)를 이용하여 $2.5{\mu}m{\sim}15{\mu}m$ 파장의 반사율을 이용하여 방사율을 측정하였는데, 3*(Al/Al-Si-N) 구조의 다층 박막의 경우 방사율은 0.27로 측정되었다.

• Membrane Journal
• /
• v.4 no.2
• /
• pp.106-112
• /
• 1994

The ultrafiltration(UF) and reverse osmosis(RO) tests for a model metal plating wastewater prepared with zinc sulfate, showed the zinc ion rejection coefficient of over 99% and the permeate flux of $1.49 {\times} 10^{-3}cm/sec$ at pH = 8.3. The effect of cyanide on the zinc removal was investigated. When the amount of cyanide addition was same the zinc content, the zinc was removed over 99% and the cyanide was excluded about 93%. The addition of the surfactants such a LAS-Na and EDTA-Na was found to reduce the permeate flux down to $0.76 {\times} 10^{-3}cm/sec$ at the RO membrane.

• Membrane Journal
• /
• v.30 no.4
• /
• pp.252-259
• /
• 2020

Olefins are industrially important materials used for the synthesis of various petrochemicals. During the polymerization process, unreacted olefin monomers are discharged together with a large amount of nitrogen. For economic benefits, these olefin gases should be efficiently separated from nitrogen. In this study, a poly(glycidyl methacrylate-co-methyl methacrylate) (PGM) comb-like copolymer was synthesized and 4,4'-diaminoazobenzene (DAAB) was introduced to the copolymer to prepare a cross-linked membrane for C₃H₆/N₂ separation. PGM and DAAB were readily reacted at room temperature through an epoxide-amine reaction without additional thermal treatment. PGM-based membrane, which is a glassy polymer, showed a faster permeation of N₂ compared to C₃H₆. The pristine PGM membrane exhibited the N₂ permeability of 0.12 barrer and the high N₂/C₃H₆ selectivity of 32.4. As DAAB was introduced as a cross-linker, the thermal stability of the membrane was significantly improved, which was confirmed by TGA result. The N₂/C₃H₆ selectivity was decreased at 1 wt% of DAAB content, but the N₂ permeability increased by approximately 4.7 times. We analyzed N₂/C₃H₆ gas separation properties through a glassy polymer-based membrane, which has not been widely studied. Also, we proposed that thermal stability of the membrane can be greatly improved by the cross-linking method.

• Membrane Journal
• /
• v.24 no.4
• /
• pp.285-291
• /
• 2014

The PTMSP[Poly(1-trimethylsilyl-1-propyne)]-NaY zeolite composite membranes were prepared by adding 0~50 wt% NaY zeolite to PTMSP. In order to investigate the characteristics of these membranes, we used the analytical methods such as FT-IR, $^1H$-NMR, GPC, DSC, TGA, and SEM. Gas permeation experiments were carried out at $23{\sim}26^{\circ}C$, $2kgf/cm^2$, and the permselectivity of $H_2$ and $N_2$ gases through the composite membranes was studied as a function of the NaY zeolite contents. According to TGA measurements, when NaY zeolite was inserted within the PTMSP, thermal stability of PTMSP was enhanced. Based on SEM observation, NaY zeolite was dispersed in the PTMSP-NaY zeolite composite membrane with a size of $1.5{\mu}m$. The permeability of $H_2$ and $N_2$ through the PTMSP-NaY zeolite composite membranes increased as NaY zeolite content increased. On the contrary, the selectivity($H_2/N_2$) of the PTMSP-NaY zeolite composite membranes decreased as zeolite content increased.

• Applied Chemistry for Engineering
• /
• v.31 no.1
• /
• pp.90-96
• /
• 2020

This paper aims to reuse sewage by a forward osmosis using a blended fertilizer as a draw solution. This work deals with the primary sedimentation basin influent, effluent, and secondary sedimentation basin effluent from J sewage treatment plant. The average permeate water flux was higher in the order of the blend of KCl and NH₄Cl > KCl and NH₄H₂PO₄ > KCl and (NH₄)₂HPO₄, and the reverse solute flux was lower in the order of the blend of KCl and NH₄H₂PO₄ < KCl and NH₄Cl < KCl and (NH₄)₂HPO₄. Regardless of the blended fertilizer, the permeate water flux of the effluent from the secondary sedimentation basin was the highest. The blended fertilizer of KCl and NH₄H₂PO₄ was found to be most useful for the reuse of sewage because it contains nitrogen, phosphorus and potassium, which are the major components of a fertilizer, and has a low reverse solute flux. When the blend of KCl and NH₄H₂PO₄ was used as a draw solution, the average permeate water and reverse solute flux for the secondary sedimentation basin effluent were 12.14 L/㎡hr and 0.012 mol/㎡s, respectively.