• 제목/요약/키워드: Adsorption/Catalytic Process

검색결과 57건 처리시간 0.021초

Mesoporous Carbon as a Metal-Free Catalyst for the Reduction of Nitroaromatics with Hydrazine Hydrate

  • Wang, Hui-Chun;Li, Bao-Lin;Zheng, Yan-Jun;Wang, Wen-Ying
    • Bulletin of the Korean Chemical Society
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    • 제33권9호
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    • pp.2961-2965
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    • 2012
  • Mesoporous carbons with tailored pore size were prepared by using sucrose as the carbon source and silicas as the templates. The silica templates were obtained from a hydroxypropyl-${\beta}$-cyclodextrin-silica hybrids using ammonium perchlorate oxidation at different temperatures to remove the organic matter. The structures and surface chemistry properties of these carbon materials were characterized by $N_2$ adsorption, TEM, SEM and FTIR measurements. The catalytic performances of these carbon materials were investigated through the reduction of nitroaromatic using hydrazine hydrate as the reducing agent. Compared with other carbon materials, such as active carbon, and carbon materials from the silica templates obtained by using calcination to remove the organic matter, these carbon materials exhibited much higher catalytic activity, no obvious deactivation was observed after recycling the catalyst four times. Higher surface area and pore volume, and the presence of abundant surface oxygen-containing functional groups, which originate from the special preparation process of carbon material, are likely responsible for the high catalytic property of these mesoporous carbon materials.

Ni, Ru-ZSM-5를 첨가한 NSR 촉매의 NOx 정화 특성 (Characteristics of NOx Reduction on NSR(NOx Storage and Reduction) Catalyst Supported by Ni, Ru-ZSM-5 Additives)

  • 최병철;이춘희;정종우
    • 한국자동차공학회논문집
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    • 제15권5호
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    • pp.105-111
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    • 2007
  • In this study, we investigated the conversion performance of de-NOx catalyst for lean-burn natural gas engine. As a de-NOx catalyst, NOx storage reduction catalyst was composed of Pt, Pd and Rh with washcoat including Ba and Ni, Ru-ZSM-5. Ni, Ru-ZSM-5, which was regarded as a NOx direct decomposition catalyst, was made up of ion exchanged ZSM-5 by 5wt.% Ni or Ru. The performance of de-NOx catalyst was evaluated by NOx storage capacity and catalytic reduction in air/fuel, $\lambda=1.6$. The catalytic reaction was also observed when the added fuel was supplied to fuel rich atmosphere by fuel spike period of 5 seconds. The NOx conversion of the catalysts with Ni-ZSM-5 or Ru-ZSM-5 was mainly caused by the effect of NOx adsorption of Ba rather than the catalytic reduction of Ni, Ru-ZSM-5. Ni, Ru-ZSM-5 catalysts can not use for the NSR catalyst because they have quick process in thermal deactivation.

OXIDATION CHARACTERISTICS OF PARTICULATE MATTER ON DIESEL WARM-UP CATALYTIC CONVERTER

  • Choi, B.C.;Yoon, Y.B.;Kang, H.Y.;Lim, M.T.
    • International Journal of Automotive Technology
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    • 제7권5호
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    • pp.527-534
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    • 2006
  • Modern passenger cars with diesel engines are equipped with DOC(diesel oxidation catalyst) for the purpose of reducing HC and CO in the exhaust stream. Cold start exhaust emissions pose troubles here as on gasoline engine vehicles. As a result, some of the diesel passenger cars roll off todays the assembly lines with WCC(warm-up catalytic converter). Oxidation characteristics of the particulates in WCC is analyzed in this study by EEPS(engine exhaust particulate size spectrometer). The maximum number of PM is found to come out of WCC in sizes near 10nm when an HSDI diesel engine is operated under the conditions of high speed and medium to heavy load. When the temperature of the WCC exceeds $300^{\circ}C$, the number of PM smaller than 30 nm in diameter sharply increases upon passing through the WCC. Total mass of emitted PM gets reduced downstream of the WCC under low speed and light load conditions due to adsorption of PM onto the catalyst. Under conditions of high speed and medium to heavy load, the relatively large PM shrink or break into fine particles during oxidation process within the WCC, which results in more mass fraction of fine particles downstream of the WCC.

포피린-메탈 복합체를 이용한 TNT 폐수의 처리 (Abatement Study of TNT Wastes by Porphyrin-Metal Complexes)

  • 조정국;우인성
    • 한국안전학회지
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    • 제8권4호
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    • pp.127-132
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    • 1993
  • Porphyrin-catalyzed reduction of TNT to triaminotoluene was performed in both batch reactions and a continuous process. Packed-bed reactors were used to study porphyrin-catalyzed reduction in a continuous process. A reactor was packed with DEAD(diethylaminoethyl)-substituted glass beads on which $Co^{+3}$_centered deuteroporpgyrin Ⅸ, -2, 4-disulfonic acid was immobilized, and another containing only DEAE glass beads was used as a control. The porphyrin exhibited catalytic activity in its immobilized state up to 100 hours of operation. Based on the successful abatement of nitrobodies by porphyrin-catalyzed reduction in both batch and continuous process, this process is recommended to be used as a pretreatment for biological treatment or carbon adsorption treatment of TNT wastes.

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광산화 및 광촉매 공정에서 VOCs의 산화반응 속도 산출에 관한 연구 (A Study on the reaction rate constant by UV Photooxidation and Photo-catalytic oxidation process)

  • 정창훈;이경호
    • 한국환경과학회지
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    • 제13권1호
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    • pp.37-40
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    • 2004
  • In this study, the decomposition of gas-phase TCE, Benzene and Toluene, in air streams by direct UV Photolysis and UV/TiO$_2$ process was studied. For direct UV Photolysis, by regressing with computer calculation to the experimental results the value of reaction rate constant k of TCE, Toluene and Benzene in this work were determined to be 0.00392s$\^$-l/, 0.00230s$\^$-1/ and 0.00126s$\^$-1/, respectively. And the adsorption constant K of TCE, Toluene and Benzene in this work were determined to be 0.0519 mol$\^$-l/ ,0.0313mo1$\^$-1/ and 0.0084mo1$\^$-1/, respectively. For UV/TiO$_2$ system by regressing with computer calculation to the experimental results the value of reaction rate constant k of TCE, Toluene, and Benzene in this work were determined to be 5.74g/$\ell$$.$min, 3.85g/$\ell$$.$min, and 1.18g/$\ell$$.$min, respectively. And the catalyst adsorption constant K of TCE, Toluene, and Benzene in this work were determined to be 0.0005㎥/mg, 0.0043㎥/mg and 0.0048㎥/mg, respectively.

석탄가스의 초정밀 정제를 위한 변형된 활성탄의 흡착특성 연구 (The Adsorption of COS with a Modified-Activated Carbon for Ultra-Cleanup of Coal Gas)

  • 이유진;박노국;이태진
    • 청정기술
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    • 제13권4호
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    • pp.266-273
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    • 2007
  • 본 연구에서는 석탄가스화 복합발전시스템용 고온건식탈황공정에 포함된 직접황회수공정의 $SO_2$ 촉매환원 반응에서 발생되는 COS의 효과적인 제거를 위한 활성탄계 흡착제의 흡착특성이 연구되었다. $SO_2$의 촉매적 환원을 위하여 전이금속 담지촉매와 복합금속산화물 촉매가 사용되었으며, 이들 촉매의 반응기구에 따라 COS 생성과정과 반응온도에 따른 유출량이 조사되었다. 생성된 저농도의 COS를 효과적으로 제거하기 위하여 상용활성탄과 활성탄의 COS흡착특성을 개선하기 위하여 알칼리금속 수용액(KOH)으로 담지시킨 활성탄이 이용되었다. TGA를 이용하여 온도에 따른 COS 흡착량과 흡착속도를 알 수 있었고, GC-PFPD가 장착된 고정층 흡착시스템을 이용하여 COS 흡착실험을 수행한 결과, 높은 BET 표면적을 지니는 KOH로 처리된 활성탄의 COS 파과시간이 상용활성탄에 비해 장시간 유지되었다. 이와 같은 결과로부터 활성탄 흡착시스템으로 $SO_2$ 환원으로부터 생성되는 COS를 효과적으로 제거할 수 있으며, 알칼리성 금속을 담지할 경우 흡착특성이 향상됨을 확인할 수 있었다.

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반도체 공정에서 발생하는 유해물질 제거를 위한 흡착 및 촉매 공정에 대한 고찰 (Reviews on Adsorption and Catalyst Technology for Removal of Hazardous Substances from Semiconductor Process)

  • 윤성진;김유진;강유진;장민혁;조형근;한경재;서동진;조혜령;박주일
    • 유기물자원화
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    • 제30권4호
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    • pp.51-57
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    • 2022
  • 본 논문은 반도체 공정에서 발생하는 유해물질의 제거기술들 중 촉매식과 흡착식에 대해 알아보았다. 반도체 산업이 발전함에 따라 반도체 공정에서 세척을 위해 사용되어 배출되는 유해물질 또한 증가하고 있다. 유해물질들은 지구 환경에 대기, 수질적으로 악영향을 준다. 21세기에 들어서면서 유해물질 배출에 대한 규제가 강화됨에 따라 향후 산업발전에 한계가 생길 것으로 예상된다. 따라서 반도체 공정에서 발생되는 유해물질의 제거기술이 반드시 필요하다. 본 논문에서는 흡착기술과 촉매기술을 통해 유해물질인 PFCs의 제거를 목표를 두고 정리하였다. 반도체 공정에서부터 생성되는 유해물질이 제거되는 기술까지의 설명을 집약하였다.

Preparation of Alumino-silicate Membrane and Its Application to a Gas Separation

  • 김태환
    • 한국막학회:학술대회논문집
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    • 한국막학회 2002년도 제15회 심포지움
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    • pp.23-46
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    • 2002
  • The cryogenic, pressure swing adsorption and membrane methods have been used to separate air into nitrogen and oxygen. The air separation membrane is made of the polymers, of which manufacturing process is complicate and it causes a little high production cost. Polymer membrane has temperature limit in usage and low durability even at moderate temperature. Therefore, inorganic membranes have been studied for years. As formation of unit alumino-silicate membrane, unit cells of membrane were made with a few coating methods. In this study the dipping of substrate into sols, application of vacuum to the opposite side of substrate with coating and rotating of the substrate in the sols were found as good coating memthods to make a uniform coating and to control the thickness of membrane. The membrane coats were examined by SEM and XRD. The sample ESZl-1 was compared with those of samples that prepared by another method. The present developed coating methods could be applied to the various types of zeolite membrane formation, that is A- X-, Y- ZSM- and MCM-types of membranes. Also these membrane forming methods could be applied to formation of catalyst absorbed zeolite membrane, of which zeolite absorb the catalytic metals. The product obtained from these coating methods could be applied to the industrial gas and liquid phase catalytic reaction and separation processes.

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Phosphoric Acid Modified Nb2O5: A Selective and Reusable Catalyst for Dehydration of Sorbitol to Isosorbide

  • Tang, Zhen-Chen;Yu, Ding-Hua;Sun, Peng;Li, Heng;Huang, He
    • Bulletin of the Korean Chemical Society
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    • 제31권12호
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    • pp.3679-3683
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    • 2010
  • Niobium oxide ($Nb_2O_5$) and phosphated $Nb_2O_5$ were synthesized and used as catalysts for sorbitol dehydration to isosorbide. The characterization results of $N_2$ adsorption, XRD and $NH_3$-TPD revealed that the phosphoric acid modification could well prevent the crystallization of $Nb_2O_5$. And the amorphous phosphated $Nb_2O_5$ catalysts kept the relatively large surface area and stable acidity at high calcination temperature. The catalytic results showed that the selectivity to isosorbide could be dramatically enhanced over phosphated $Nb_2O_5$. The excellent catalytic performance with 100.0% sorbitol conversion and 62.5% isosorbide selectivity were obtained over the 0.8P/NBO-400 catalyst. Comparing with $Nb_2O_5$ catalysts, phosphated $Nb_2O_5$ catalysts regenerated through a simple calcination process showed no significant activity loss after recycling three runs.

촉매가 충진된 플라즈마 반응기에서의 Toluene 제거특성 (Characteristics of Toluene Destruction by Non-thermal Plasma in Packed with Catalyst Reactor)

  • 한소영;송영훈;차민석;김석준;최경일;신동준
    • 한국대기환경학회지
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    • 제18권1호
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    • pp.51-58
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    • 2002
  • Destruction process of toluene using a wire-cylindrical BBD (Dielectric Barrier Discharge) reactor packed with catalysts was investigated to characterize the synergetic effects of non-thermal plasma and catalyst process. The catalysts used in the present study were ${\gamma}$-Al$_2$BO$_3$ and Pt/${\gamma}$-Al$_2$O$_3$. Under the numerous test conditions, specific energy density (SED (J/L)) and the conversion of toluene, defined as (1 -[C$_{f}$]/[C$_{i}$]), were measured. The test results showed that toluene decomposition efficiency followed the pseudo-first order in the case of plasma only process. The pseudo-first order process, however, was modified to pseudo-zeroth order reaction in the case of catalyst-assisted plasma process. This modification of the reaction order was verified based on a simple kinetic model proposed in the present study. Owing to the modification of reaction order, which resulted from the catalytic process, the specific energy to achieve the high removal efficiencies, i.e. 80~90%, was reduced significantly.y.y.