• 한국재료학회지
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• 제16권10호
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• pp.619-623
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• 2006

Selective vapor deposition of conductive poly(3,4-ethylenedioxythiophene) (PEDOT), thin films has been carried out on self assembled monolayers patterned oxide substrate. Since the 3,4-ethylenedioxythiophene(EDOT) monomer can be polymerized only in the presence of oxidant such as $FeCl_3$, the PEDOT thin film is selectively deposited on patterned $FeCl_3$, which only adsorbs on the partly removed SAMs region due to the inability of $FeCl_3$ to adsorb on SAMs. Therefore, the partly removed SAMs can act as an adsorption layer for the $FeCl_3$ and also as a glue layer for the deposition of PEDOT, resulting in the significantly increased adhesion of PEDOT to $SiO_2$ substrate. The use of UV lithography and Cr patterned quartz mask provided the formation of SAMs patterns on oxide substrates, which allowed for the selective deposition of conductive PEDOT thin films.$^{oo}The$ new process was successfully developed for the selective deposition of PEDOT thin films on SAMs patterned oxide substrate, providing a new way for the patterning of vapor phase deposition of PEDOT thin films with accurate alignment and addressing the inherent adhesion issues between PEDOT and dielectrics.

• 멤브레인
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• 제21권1호
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• pp.72-83
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• 2011

고탁도 원수의 고도정수처리를 위해 관형 세라믹 정밀여과막 외부와 원통형 막 모듈 내부 사이의 공간에 광촉매를 충전한 혼성 모듈을 사용하였다. 광촉매는 PP (polypropylene) 구(bead)에 $TiO_2$ 분말을 플라즈마 화학증착(chemical vapor deposition) 공정으로 코팅한 것이다. 정수 원수 중 자연산 유기물(NOM)과 미세 무기 입자를 대체하기 위해, 휴믹산(humic acid)과 카올린(kaolin) 모사용액을 대상으로 하였다. 혼성공정에서 막오염을 최소화하기 위해 10분 주기로 10초 동안 물 역세척을 시행하였다. 휴믹산을 10 mg/L부터 2 mg/L로 변화시킴에 따라, 막오염에 의한 저항($R_f$)이 감소하고 J가 증가하여 2 mg/L에서 가장 높은 총여과부피($V_T$)를 얻었다. 탁도 및 $UV_{254}$ 흡광도의 처리효율은 각각 98.5% 및 85.7% 이상이었다. MF 공정 및 MF + $TiO_2$ 공정, MF + $TiO_2$ + UV 공정의 막여과 및 광촉매 흡착, 광산화의 처리 분율을 알아본 결과, 광촉매 흡착과 광산화에 의해 탁도는 거의 처리되지 않았으나, 광촉매 흡착 및 광산화에 의한 휴믹산 처리 분율은 각각 10.7, 8.6% 이상이었다.

• 공업화학
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• 제9권2호
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• pp.286-293
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• 1998

연소배가스로부터 $CO_2$를 선택적으로 분리하기 위한 활성탄 흡착공정 사용시 흡착능 향상을 위하여 $CO_2$와 친화력이 있는 화합물을 함침시키는 방법과 KOH를 함침시킨 후 고온에서 열처리하므로서 활성화시키는 방법이 사용되었다. 알칼리금속, 알칼리토금속, 또는 전이금속의 염화물을 함침시킨 활성탄에 대한 $CO_2$의 흡착량을 측정한 결과 함침 전의 활성탄의 흡착량보다 적었다. 이것은 함침되는 물질이 $CO_2$에 대한 친화력이 없이 단지 활성탄의 미세기공만 막는 결과임을 알 수 있었다. 알칼리금속수산화물 중 KOH를 함침시킨 활성탄에 대한 $CO_2$의 파과실험 결과 유입되는 기체에 수분이 있을 경우 흡착량이 증가했는데 이것은 KOH가 $CO_2$를 흡수하는 성질 때문이었다. 그러나 이 흡착제에 함친된 KOH가 $CO_2$와 반응하여 $K_2CO_3$로 변함에 따라 재현성이 없음을 알 수 있었다. KOH를 함침시킨 후 $800^{\circ}C$에서 열처리하여 활성화시킨 활성탄의 경우 함침된 KOH의 양이 증가할수록 $CO_2$의 흡착량이 증가했으며, KOH와 활성탄의 무게비(KOH/Activated-Carbon)가 4일 때 최대였다. 이 흡착제에 대해 온도별로 측정된 $CO_2$의 흡착량으로부터 Clausius-Clapeyron식을 이용하여 등량흡착열을 구했다. 그리고 고정층 파과실험을 통해 $CO_2$농도와 유속에 따른 파과특성을 살펴보았다.

• 공업화학
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• 제17권2호
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• pp.201-209
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• 2006

활성탄과 제올라이트 13X를 충진시킨 흡착탑에 흡착질인 벤젠을 포화 흡착시킨 후 여러 가지 탈착 방법에 대한 효율을 살펴보았다. 뜨거운 수증기에 의한 탈착, 세정 기체에 의한 탈착, 진공에 의한 탈착 등을 실험하였고, 그 결과 뜨거운 수증기에 의한 탈착이 가장 좋은 탈착 방법으로 판단되었다. 또한 뜨거운 수증기는 흡착탑 내의 온도를 상승시키면서 탈착을 야기시키고 수증기 탈착 과정 이후에는 건조 공정이 수반되어야만 효율이 높아짐을 알 수 있었다. 건조 공정이 수반되지 않을 경우는 수증기가 추후에 흡착을 방해하는 결과를 초래하였다. 진공에 의한 탈착은 효과가 매우 적은 것으로 나타났는데 이로부터 벤젠의 경우에 압력 변화에 의한 탈착 보다는 온도 변화에 의한 탈착이 더 효과적인 것으로 판단되었다. 세정 기체에 의한 탈착에서는 진공 탈착과 함께 이루어질 때 좋은 탈착 성능이 나타남을 알 수 있었다.

• 한국재료학회지
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• 제24권11호
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• pp.573-577
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• 2014

The existing metal getters are invariably covered with thin oxide layers in air and the native oxide layer must be dissolved into the getter materials for activation. However, high temperature is needed for the activation, which leads to unavoidable deleterious effects on the devices. Therefore, to improve the device efficiency and gas-adsorption properties of the device, it is essential to synthesize the getter with a method that does not require a thermal activation temperature. In this study, getter material was synthesized using palladium oxide (PdOx) which can adsorb $H_2$ gas. To enhance the efficiency of the hydrogen and moisture absorption, a porous layer with a large specific area was fabricated by an etching process and used as supporting substrates. It was confirmed that the moisture-absorption performance of the $SiO_2/Si$ was characterized by water vapor volume with relative humidity. The gas-adsorption properties occurred in the absence of the activation process.

• 접착 및 계면
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• 제21권2호
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• pp.51-57
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• 2020

최근 산업활동을 통해 배출되는 유해 오염물질 제거에 대한 관심이 증가하고 있다. 본 연구에서는 수증기 활성화 법을 이용하여 활성탄소섬유를 제조하고, 이의 유해가스 흡착 및 전기화학적 감응 특성을 분석하였다. 활성탄소섬유의 균일한 기공 구조, 활성 반응 면적 및 반응 위치를 조절하기 위하여, 활성화 온도(750-850 ℃) 및 활성화 시간(30-240 min)을 조절하였고, 다양한 활성화 조건을 통해 제조된 활성탄소섬유의 SO₂와 NO 가스 흡착 및 가스 센서를 통한 감응 특성을 분석하였다. 특히, 850 ℃에서 45 min동안 수증기 활성화 반응을 통해 제조된 활성탄소섬유가 가장 높은 비표면적(1,041.9 ㎡/g)과 기공 특성(0.42 ㎤/g)을 보였으며, 우수한 SO₂ (1.061 mg/g) 및 NO (1.210 mg/g) 가스 흡착 특성을 보였다.

• 한국산업보건학회지
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• 제7권1호
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• pp.21-31
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• 1997

Toluene, n-hexane, and methyl ethyl ketone(MEK) were exposed to the activated carbon fiber(ACF) and 3M(Model 3500) diffusive samplers under low and high humidity levels. In order to evaluate these two samplers, the sampling capacity, sampling rate, reverse diffusion, and storage stability were obtained. At low humidity level($8{\pm}3%RH$), the adsorption amount of all three organic vapors to the ACF diffusive sampler showed a positive linear relationship up to 8 hours. However, at high humidity level($90{\pm}5%RH$), n-hexane and MEK maintained a positive linear relationship up to 1.5 hrs, but decreased in their adsorption amounts afterwards. On the other hand, the adsorption amount of n-hexane, MEK, and toluene to 3M diffusive sampler showed almost a positive linear relationship up to 8 hours at both humidity levels. At low humidity level, there was almost no reverse diffusion for both 3M and ACF diffusive samplers. However, when the ACF diffusive sampler was used at high humidity level, there was about 52.63% of MEK sample loss and about 92.59% of n-hexane sample loss. The storage stabilities of the ACF and 3M diffusive samplers were both relative stable except for MEK. In the case of MEK, the difference between the analysis of the organic vapor right after the sampling and that of 3 weeks later at room temperature was 45% for the ACF diffusive sampler and 18% for the 3M diffusive sampler. Since the storage stability of the samples stored in a refrigerator was relatively stable, they need to be refrigerated until the analysis is done.

• 한국의류학회지
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• 제37권1호
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• pp.113-123
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• 2013

Clothes that retain and emanate body odor feel uncomfortable and unclean; subsequently, the adsorption, desorption and removal amounts of malodorous compounds from fabrics with different polarities were examined. 1-Octen-3-one, octanal and isovaleric acid, which are important malodor compounds from the body, were used as volatile organic compounds (VOC). Samples were prepared with unfinished and ${\beta}$-CD finished cotton, nylon and PET fabrics. The amounts of VOCs retained on the fabrics were measured using headspace GC-MS; in addition, the odor intensity of the samples were evaluated by 10 trained panelists. The amounts adsorbed were estimated by weight gain; however, moisture was found to have a larger effect on the increase in weight than VOCs. The polarity of the VOCs decreased in the order of isovaleric acid, octanal and 1-octen-3-one. Despite the exceptionally large amounts of octanal adsorbed on the nylon sample, the amounts of malodorous compounds adsorbed on fabrics increased with the decreasing VOC molecular weight. The unfinished PET sample adsorbed more VOCs than the unfinished-fabric samples. The odor intensity was mostly weaker in the ${\beta}$-CD finished fabrics than in the unfinished fabrics. The odor intensity of the ${\beta}$-CD finished fabrics was lower than unfinished fabrics. The amount of VOCs that remained on the soiled fabric samples after storing in air for 24 hrs decreased with the increasing VOC vapor pressure. Most VOCs were removed by washing; however, more VOCs were left on the ${\beta}$-CD finished fabrics than unfinished fabrics. The intensity of the odor from the unfinished PET and ${\beta}$-CD finished fabrics was stronger and weaker, respectively, than that of other fabrics, even when the same amounts of VOCs remained.

• 멤브레인
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• 제21권4호
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• pp.351-359
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• 2011

For advanced drinking water treatment of high turbidity water, we used the hybrid process that was composed of photocatalyst packing in space of between outside of multi-channel ceramic microfiltration membrane and membrane module inside. Photocatalyst was polypropylene (PP) beads coated $TiO_2$ powder by CVD (chemical vapor deposition) process. Instead of natural organic matters (NOM) and fine inorganic particles in natural water source, standard NOM 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 ($R_f$) increased and J decreased as concentration of humic acid changed from 2 mg/L to 10 mg/L, and finally the highest total permeate volume ($V_T$) could be obtained at 2 mg/L. Then, treatment efficiency of turbidity and $UV_{254}$ absorbance were above 96.4% and 78.9%, respectively. As results of treatment portions by membrane filtration, photocatalyst adsorption, and photo-oxidation in (MF), (MF + $TiO_2$), (MF + $TiO_2$ + UV) processes, turbidity was treated little by photocatalyst adsorption, and photo-oxidation. However, treatment portions of $UV_{254}$ absorbance by adsorption (MF + $TiO_2$) and photo-oxidation (MF + $TiO_2$ + UV) at humic acid of 4 mg/L and 6 mg/L were above 9.0, 9.5 and 8.1, 10.9%, respectively.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 1999년도 춘계 학술발표회 논문집
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• pp.185-191
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• 1999

An air-conditioning system based on the chemical heat storage principle was considered. $H_2O$ was chosen as the reaction gas and the working fluid as well. Na$_2$S, CaCl$_2$, MnCl$_2$, BaCl$_2$, MgCl$_2$, Fe$_2$(SO$_4$)$_3$ and MnSO$_4$ were tested as the solid reactants by using Cahn pressure balance. Na$_2$S was superior to other salts in respect of high capability of absorption of water gas, 5 moles of $H_2O$ per unit mole of Na$_2$S, and adequate temperature of adsorption, $65^{\circ}C$ at 7torr, and of desorption, 13$0^{\circ}C$ at 76torr. Clausius-Clapeyron diagram of Na$_2$S was obtained via adsorption experiments at several vapor pressures of water gas. To enhance heat and mass transfer characteristics, usually below 1W/m K, of the reactor bed of general adsorption systems, expanded graphite block was adapted as the support of Na$_2$S salt. Expanded graphite blocks had thermal conductivity values of 20~80W/mK with respect to 100~400kg/㎥ of block bulk density. Permeability values of expanded graphite blocks were 10$^{-13}$ ~ 10$^{-14}$ $m^2$ with respect to 100~300kg/㎥ of block bulk density showing highly decreasing values of permeability, below 10$^{-l4}$$m^2$, in the range of above 150kg/㎥ of block bulk density.y.