• Title/Summary/Keyword: $TiO_2$ membrane

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Preparation of Spherical TiO2 Nanoparticles Using Amphiphilic PCZ-r-PEG Random Copolymer Template Membrane (양친성 PCZ-r-PEG 랜덤 공중합체 분리막을 이용한 구형 이산화티타늄 나노입자의 제조)

  • Lee, Jae Hun;Patel, Rajkumar
    • Membrane Journal
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    • v.29 no.3
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    • pp.183-189
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    • 2019
  • Amphiphilic PCZ-r-PEG random copolymer assisted solvothermal process is used to prepare mesoporous $TiO_2$ microspheres generated from nanoparticles by self-assembly method. Synthesized PCZ-r-PEG is characterized by Fourier transform infrared spectroscopy (FT-IR), nuclear magnetic resonance (NMR), gel permeation chromatography (GPC) and transmission electron microscopy (TEM). The mesoporous $TiO_2$ are prepared by PCZ-r-PEG, glucose, water in tertrahydrofuran solution at $150^{\circ}C$ for 12 h and the $TiO_2$ microspheres are calcined at $550^{\circ}C$ for 30 min to further crystallize and organic residue are removed. Morphology and crystallization phase is characterized by scanning electron microscopy (SEM) and X-ray diffraction (XRD) respectively. The mesoporous $TiO_2$ crystallized in pure anatase phase with diameter of $300{\pm}20nm$.

Advanced Water Treatment of High Turbidity Source by Hybrid Process of Photocatalyst and Ceramic Microfiltration: Effect of Organic Materials in Water-back-flushing (광촉매 및 세라믹 정밀여과 혼성공정에 의한 고탁도 원수의 고도정수처리: 물 역세척시 유기물의 영향)

  • Park, Jin-Yong;Lee, Gwon-Seop
    • Membrane Journal
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    • v.21 no.1
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    • pp.72-83
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    • 2011
  • For advanced drinking water treatment of high turbidity water, we used the hybrid module that was composed of photocatalyst packing between outside of tubular ceramic microfiltration membrane and membrane module inside. Photocatalyst was PP (polypropylene) bead coated $TiO_2$ powder by CVD (chemical vapor deposition) process. Instead of natural organic matters (NOM) and fine inorganic particles in natural water source, modified solution was prepared with humic acid and kaolin. Water-back-flushing of 10 sec was performed per every period of 10 min to minimize membrane fouling. Resistance of membrane fouling ($R_f$) decreased and J increased as concentration of humic acid changed from 10 mg/L to 2 mg/L, and finally the highest total permeate volume ($V_T$) could be obtained at 2 mg/L. Then, treatment efficiencies of turbidity and $UV_{254}$ absorbance were above 98.5% and 85.7%, respectively. As results of treatment portions by membrane filtration, photocatalyst adsorption, and photo-oxidation in MF, MF + $TiO_2$, and MF + $TiO_2$ + UV processes, turbidity was treated little by photocatalyst adsorption, and photo-oxidation. However, treatment portions of humic acid by adsorption and photo-oxidation were above 10.7 and 8.6%, respectively.

Composite TiN-Al2O3 Syntheses and Hydrogen Permeability Characteristics Evaluation (복합 TiN-Al2O3 합성과 수소투과도 특성 평가)

  • CHO, KYOUNG-WON;LEE, YOUNG-HWAN;HAN, JEONG-HEUM;YU, JE-SEON;HONG, TAE-WHAN
    • Transactions of the Korean hydrogen and new energy society
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    • v.31 no.2
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    • pp.177-183
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    • 2020
  • To utilize hydrogen energy, high-yield, high-purity hydrogen needs to be produced; therefore, hydrogen separation membrane studies are being conducted. The membrane reactor that fabricates hydrogen needs to have high hydrogen permeability, selective permeability, heatresistant and a stable mechanical membrane. Dense membranes of Pd and Pd alloys are usually used, but these have drawbacks associated with high cost and durability. Therefore, many researchers have studied replacing Pd and Pd alloys. Dense TiN membrane is highly selective and can separate high-purity hydrogen. The porous alumina has a high permeation rate but low selectivity; therefore, separating high-purity hydrogen is difficult. To overcome this drawback, the two materials are combined as composite reclamations to produce a separation membrane with a high penetration rate and high selectivity. Accordingly, TiN-alumina was manufactured using a high-energy ball mill. The TiN-alumina membrane was characterized by X-ray diffraction analysis, scanning electron microscopy, and energy dispersive spectroscopy. The hydrogen permeability of the TiN-alumina membrane was estimated by a Sievert-type hydrogen permeation membrane apparatus. Due to the change in the diffusion mechanism, the transmittance value was lower than that of the general TiN ceramic separator.

Preparation and Characterization of TiO$_2$ Ultrafiltration Membranes for Reclamation of Waste Lubrication Oil (폐윤활유 재생용 TiO$_2$ 한외여과막의 제조 및 특성평가)

  • 김계태;현상훈
    • Journal of the Korean Ceramic Society
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    • v.36 no.3
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    • pp.244-254
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    • 1999
  • 폐윤활유 재생용 TiO2 한외여과막은 정밀영과용 지르코니아 복합막(즉, 복층담채) 및 알루미나 단층 담체(기공크기 0.1$mu extrm{m}$)상에 졸-겔 코팅법에 의하여 TiO2 분리막 층을 코팅하여 제조 하였다. TiO2 졸의 특성 분석을 통하여 봉입침지(sealed dip-coating) 및 가압 코팅(pressurized coating)법으로 결함이 없는 TiO2 복합막을 제조할 수 있는 코팅조건을 최적화 하였다. 합성 TiO2 한외여과막의 분리막층 두께는 1$\mu\textrm{m}$이하의 범위에서 조절되었으며,기공값을 보여주었으며 75$0^{\circ}C$까지 열처리하여도 80%정도의 용질배제율(기공크기 22.5nm)을 유지하는 점으로 봐서 고온 공정을 요하는 폐윤활유 재생막으로서 충분한 열적 안정성을 갖고 있었다.

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세라믹막의 분획분자량 (Molecular Weight Cut-Off) 특성화

  • 현상훈;강범석;조철구;하호관
    • Proceedings of the Membrane Society of Korea Conference
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    • 1994.04a
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    • pp.58-58
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    • 1994
  • 슬립캐스팅법으로 제조한 튜브형 $\alpha$-알루미나 담체 (평균기공크기 = $0.1 \mum$)에 졸-겔 침지코팅(dipcoating) 또는 가압코팅 (pressurized coating) 법에 의하여 극미세입자 $\gamma$-AlOOH, $TiO_2, SiO_2$, 및 aluminosilicate diphasic 졸을 코팅한 후 300 ~ 500$\circ$C 에서 열처리하여 세라믹 복합막을 제조하였다. 복합막 전체에 대한 균열유무는 $N_2$ 기체투과율의 평균압력에 대한 의존성으로부터 평가하였으며, 한외여과 (ultrafiltration)에의 응용성을 규명하기 위하여 막의 재질 및 제조조건에 따른 polyethylene glycol (PEG) 수용액의 분획분자량 변화를 측정하였다. 합성 세라믹 복합막의 분획분자량 측정 결과 $SiO_2$의 경우 2,000 정도로 매우 우수하였으며 $\gamma-Al_2O_3, TiO_2$, 그리고 aluminosilcate 막들은 6,000 ~ 10,000 범위 값을 갖고 있었다. 또한 막의 기공크기 및 분획분자량을 제어하기 위한 방법으로서 $TiO_2$ 복합막을 300 ~ 700$\circ$C 에서 열처리하였으며 이들에 대한 분획분자량 변화를 비교 분석하였다.

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Fabrication of $TiO_2-CeO_2$ Composite Membranes with Thermal Stability

  • Bae, Dong-Sik;Han, Kyong-Sop;Park, Sang-Hael
    • The Korean Journal of Ceramics
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    • v.1 no.4
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    • pp.219-223
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    • 1995
  • Ceramic membranes of the supported $TiO_2-CeO_2$ were prepared by dip-coating method on an $\alpha-Al_2O_3$ porous substrate. The mean pore diameter of an alumina support was 0.125 um. The mean particle diameter of $TiO_2-CeO_2$ top layer varied with firing temperature and ranged from 20 to 85 nm. The thermal stability of the composite membranes was studied from their surface microstructure after calcination at $600-900^{\circ}C$. The supported $TiO_2-CeO_2$ composite membranes exhibited much higher heat resistance than the $TiO_2$ membrane.

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TiO2 membrane를 이용한 수소 동위원소 분리

  • Lee, Jae-Won;Lee, Hyeon-Gwon;Nam, Geon-U;Lee, Gi-Yeong
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2017.05a
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    • pp.147-147
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    • 2017
  • $TiO_2$는 의료기기, 광촉매, 태양전지 등의 여러 분야에 응용이 가능하여 많은 연구가 진행되어 왔다. 그 중 양극산화를 통하여 수직으로 잘 정렬된 나노튜브는 넓은 반응면적, 높은 전자 전도성 등의 장점으로 그 성능을 더욱 향상 시킬 수 있어 많은 연구자들이 이용하고 있다. 양극산화의 특성상 Ti 기판 위에 형성된 나노튜브의 효용성을 높이기 위하여 기판에서 분리하여 membrane의 형태로 이용하기도 한다. 이런 $TiO_2$ 나노튜브 멤브레인의 이용은 주로 오염물의 분해를 위한 광촉매, 염료감응 태양전지의 전극으로 이용되고 있다. 본 연구는 $TiO_2$ 나노튜브 멤브레인에 기체 동위 원소 분리에 이용되는 HKUST-1, ZIF-8 등과 같은 Metal Organic Frame Work (MOF)을 충진 시켜 극저온에서 수소 동위 원소를 분리 하고 자 하는데 있다. 하지만 MOF를 충진하기 위해서는 기존의 $TiO_2$ 나노 튜브 멤브레인보다 더 넓은 내경과 안정성이 요구되는 바이다. 이를 위하여 본 연구에서는 내경을 수백 나노미터 이상으로 확장하기 위한 전해질, 전류(전압) 조건 등에 대하여 연구 하였다. 또한 멤브레인의 안정적인 제조를 위하여 2-step 양극산화 조건, 열처리 조건 등의 변화를 통하여 그 목적을 달성 하고자 하였다.

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Hybrid Water Treatment of Carbon Ultrafiltration Membrane and Polypropylene Beads Coated with Photocatalyst: Effect of Organic Materials, Photo-oxidation, and Adsorption in Water Back-flushing (탄소 한외여과막 및 광촉매 코팅 폴리프로필렌 구의 혼성 수처리: 물 역세척 시 유기물 및 광산화, 흡착의 영향)

  • Park, Jin Yong;Jung, Chung Ho
    • Membrane Journal
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    • v.22 no.5
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    • pp.359-368
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    • 2012
  • For hybrid water treatment of high turbidity water, we used the hybrid module that was composed of photocatalyst packing between tubular membrane outside and module inside. Photocatalyst was PP (polypropylene) bead coated with $TiO_2$ powder by CVD (chemical vapor deposition) process. Water back-flushing of 10 sec was performed per every period of 10 min to minimize membrane fouling for modified solution was prepared with humic acid and kaolin. Resistance of membrane fouling ($R_f$) decreased as humic acid concentration changed from 10 mg/L to 2 mg/L, and finally the highest total permeate volume ($V_T$) could be obtained at 2 mg/L, which was the same with the previous results. Then, treatment efficiencies of turbidity and humic acid were above 98.9% and 88.7%, respectively. As results of treatment portions of UF, UF + $TiO_2$, and UF + $TiO_2$ + UV processes, turbidity was treated little by photocatalyst adsorption, and photo-oxidation. However, treatment portions of humic acid by adsorption and photo-oxidation were 2.5% and 12.3%, respectively. Compared with the previous results, treatment portions of humic acid by adsorption and photo-oxidation were different depending on membrane material and pore size. As simplified the process, the membrane fouling resistance after 180 minutes' operation ($R_{f,180}$) increased and the final permeate flux decreased a little.

Photocatalytic degradation of organic compounds by 2-ethylimidazole-treated titania under visible light illumination

  • Seo, Jiwon;Jeong, Junyoung;Lee, Changha
    • Membrane and Water Treatment
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    • v.10 no.3
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    • pp.223-229
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    • 2019
  • Titania modified by 2-ethylimidazole (2-EI) (denoted as $2-EI-TiO_2$) demonstrated visible light photocatalytic activity for the degradation of organic compounds. $2-EI-TiO_2$ was a bright brown powder that exhibited similar crystallinity and morphology with the control $TiO_2$. A diffuse reflectance spectrum indicated that $2-EI-TiO_2$ absorbs visible light of all wavelengths. X-ray photoelectron spectroscopy (XPS) confirmed the cationic state of nitrogen species (e.g. Ti-O-N) on the surface of $2-EI-TiO_2$. Visible light-illuminated $2-EI-TiO_2$ degraded $10{\mu}M$ 4-chlorophenol (4-CP) by approximately 85% in 4 h. The photochemical activity of $2-EI-TiO_2$ was selective in targeting the organic compound. The repeated use of $2-EI-TiO_2$ decreased the photocatalytic activity for the 4-CP degradation. Experiments using radical scavengers and oxidant probes revealed that the oxidation by photogenerated holes is responsible for the degradation of organic compounds by illuminated $2-EI-TiO_2$ and the role of $^{\bullet}OH$ is negligible.

Hydrogen-Permselective TiO$_2$2/SiO$_2$2 Membranes Formed by Chemical Vapor Deposition

  • Nam, Suk-Woo;Ha, Heung-Yong;Yoon, Sung-Pil;Jonghee Han;Lim, Tae-Hoon;Oh, In-Hwan;Seong- Ahn Hong
    • Korean Membrane Journal
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    • v.3 no.1
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    • pp.69-74
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    • 2001
  • Films of TiO$_2$/SiO$_2$ were deposited on the inner surface of the porous glass support tubes by decomposition of tetraisopropyl titanate (TIPT) and tetraethyl orthosilicate (TEOS) at atmospheric pressure. Dense and hydrogen -permselective membranes were formed at 400-600$\^{C}$. The permeation rates of H$_2$ through the membrane at 600$\^{C}$ were 0.2-0.4 ㎤(STP)/min-㎠ atm and H$_2$:N$_2$permeation ratios were above 1000. The permeation properties of the membranes were investigated at various deposition temperatures and TIPT/TEOS concentrations. Decomposition of TIPT alone at temperatures above 400$\^{C}$ produced porous crystalline TiO$_2$ films and they were not H7-selective. Decomposition of TEOS produced H$_2$-permeable SiO$_2$ films at 400-600$\^{C}$ but film deposition rate was very low. Addition of TIFT to the TEOS stream significantly accelerated the deposition rate and produced highly H$_2$-selective films. Increasing the TIPT/TEOS concentration ratio increased the deposition rate. The TiO$_2$/SiO$_2$ membranes formed at 600 $\^{C}$ have the permeation properties comparable to those of SiO$_2$ membranes produced from TEOS.

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