• Title/Summary/Keyword: 선택적 환원촉매

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A Study on the Deactivation of Commercial DeNOx Catalyst in Fired Power Plant (화력발전소 상용 탈질 촉매의 활성저하 원인에 관한 연구)

  • Park, Kwang Hee;Lee, Jun Yub;Hong, Sung Ho;Choi, Sang Hyun;Hong, Sung Chang
    • Applied Chemistry for Engineering
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    • v.19 no.4
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    • pp.376-381
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    • 2008
  • The deactivation of $V/TiO_2$ catalyst used in SCR (Selective Catalytic Reduction) using ammonia as a reductant to remove the nitrogen oxides (NOx) in the exhaust gas from fired power plant has been studied. The activity and surface area of the catalyst (Used-cat) which was exposed to the exhaust gas for long period have considerably decreased. The characterizations of these SCR catalysts were performed by XRD, FT-IR, FE-SEM, and IC/ICP. The crystal structure of $TiO_2$ both fresh and used catalyst has not been changed. However, $(NH_4)HSO_4$ deposited on the used catalyst surface verified from FT-IR, FE-SEM, and IC/ICP analysis. Moreover, the durability of $SO_2$ was increased by diminishing sulfate ($SO_4^{-2}$)f form.

Deactivation of V2O5/TiO2 catalytic system on the sulfuric oxides (V2O5/TiO2 촉매시스템의 황산화물에 대한 비활성화 특성)

  • Jang, Hyun Tae;Cha, Wang Seog
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.16 no.11
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    • pp.7433-7438
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    • 2015
  • Deactivation characteristics of $V_2O_5/TiO_2$ catalysts were studied for selective catalytic reduction(SCR) of NOx with ammonia in the presence of $SO_2$. Performance of catalyst was investigated for $deNO_x$ activity while changing temperature, $SO_2$ concentration. The activity of catalyst was decreased with the increase of $SO_2$ concentration and reaction time. Also, degree of activity drop was largely decreased with the increase of reaction temperature in the range of $250{\sim}300^{\circ}C$. Physicochemical properties of deactivated catalysts were characterized by BET, XRD, SEM, TPD analysis. According to the analysis results, deactivation phenomena occur due to the relatively high formation of ammonium sulfate salts, which created by unreacted ammonia and water in the presence of $SO_2$. It was revealed that ammonium sulfate cause the pore plogging of support and deposition of active matter.

Preparation and Activity of the Extruded SCR Catalyst for NOx Reduction in Coal Fired Power Plant (석탄화력발전소 질소산화물 제거를 위한 압출성형 SCR 촉매의 제조 및 활성)

  • 이인영;김동화;이정빈;김우영
    • Proceedings of the Korea Air Pollution Research Association Conference
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    • 2001.11a
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    • pp.143-144
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    • 2001
  • 질소산화물(NOx) 제거기술 중, 선택적촉매환원(Selective Catalytic Reduciton: SCR)공정은 배기가스 중에 포함되어 있는 질소산화물을 암모니아와 촉매상에서 반응시켜 무해한 질소와 물로 전환하는 기술로 높은 탈질율 및 안정적인 기술로 인하여 상업적으로 널리 이용되고 있다(Bosch, 1988). 귀금속촉매, Cu/Zeolite 촉매 및 V$_2$O$_{5}$/TiO$_2$ 등 다양한 촉매들이 SCR 공정에 적용되는데 V$_2$O$_{5}$/TiO$_2$ 촉매가 높은 활성과 황 등 피독 물질에 대한 우수한 내구성으로 인하여 가장 효과적인 촉매로 알려져있다(Heck, 1999). (중략)

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Catalytic Reduction of Oxidized Mercury to Elemental Form by Transition Metals for Hg CEMS (수은 연속측정시스템에서 전이금속에 의한 산화수은의 원소수은으로의 촉매환원)

  • Ham, Sung-Won
    • Clean Technology
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    • v.20 no.3
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    • pp.269-276
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    • 2014
  • This study was aimed to develop catalytic system for the dry-based reduction of oxidized mercury ($Hg^{2+}$) to elemental mercury ($Hg^0$) which is one of the most important components comprising mercury continuous emission monitoring system (Hg-CEMS). Based on the standard potential in oxidation-reduction reaction, transition metals including Fe, Cu, Ni and Co were selected as possible candidates for catalyst proceeding spontaneous reduction of $Hg^{2+}$ into $Hg^0$. These transition metal catalysts revealed high activity for reduction of $Hg^{2+}$ into $Hg^0$ in the absence of oxygen in reactant gases. However, their activities were greatly decreased in the presence of oxygen, which was attributed to the transformation of transition metals by oxygen to the corresponding transition metal oxides with less catalytic activity for the reduction of oxidized mercury. Hydrogen supplied to the reactant gases significantly enhanced $Hg^{2+}$ reduction activity even in the presence of oxygen. It might be due to occurrence of combustion reaction between $H_2$ and $O_2$ causing the consumption of $O_2$ at such high reaction temperature at which oxidized mercury reduction reaction took place. Because the system showed high activity for $Hg^{2+}$ reduction to $Hg^0$, which was compatible to that of wet-chemistry technology using $SnCl_2$ solution, the catalytic reduction system of Fe catalyst with the supply of $H_2$ could be employed as a commercial system for the reduction of oxidized mercury to elemental mercury.

The Performance Test of SCR System in a Heavy-Duty Diesel Engine (대형디젤기관에 적용된 선택적 환원촉매장치 성능시험에 관한 연구)

  • Baik, Doo-Sung;Lee, Seang-Wock
    • Transactions of the Korean Society of Automotive Engineers
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    • v.16 no.6
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    • pp.19-25
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    • 2008
  • Selective Catalytic Reduction is effective in the reduction of NOx emission. This research focused to evaluate the performance of a urea-SCR system and was conducted in two procedures. One is SCR reactor test using model gas in order to provide an optimal injection condition itself. In this step, some parametric study on emission temperature, space velocity, aspect ratio and the formation of urea spray were made by using flow visualization and Computation Fluid Dynamics techniques. The basic simulation results contributed in determining the layout for an actual engine test. The other is an engine performance and emission test. The urea injector was placed at the opposite direction of exhaust gases emitted into an exhaust duct and an optimal amount of a reducing agent is estimated accurately under different engine loads and speeds. Furthermore, the variation of NOx emission and applied amount of urea was investigated in terms of modes under the condition of with and without SCR, and other emissions such as PM, CO and NMHC were evaluated quantitatively as well. This research may provide fundamental data for the practical use of urea-SCR in future.

Removal of Nitrogen Oxides Using Hydrocarbon Selective Catalytic Reduction Coupled with Plasma (플라즈마가 결합된 탄화수소 선택적 촉매환원 공정에서 질소산화물(NOx)의 저감)

  • Ihm, Tae Heon;Jo, Jin Oh;Hyun, Young Jin;Mok, Young Sun
    • Applied Chemistry for Engineering
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    • v.27 no.1
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    • pp.92-100
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    • 2016
  • Low-temperature conversion of nitrogen oxides using plasma-assisted hydrocarbon selective catalytic reduction of (HC-SCR) was investigated. Plasma was created in the catalyst-packed bed so that it could directly interact with the catalyst. The effect of the reaction temperature, the shape of catalyst, the concentration of n-heptane as a reducing agent, the oxygen content, the water vapor content and the energy density on $NO_x$ removal was examined. $NO_x$ conversion efficiencies achieved with the plasma-catalytic hybrid process at a temperature of $250^{\circ}C$ and an specific energy input (SIE) of $42J\;L^{-1}$ were 83% and 69% for one-dimensional Ag catalyst ($Ag\;(nanowire)/{\gamma}-Al_2O_3$) and spherical Ag catalyst ($Ag\;(sphere)/{\gamma}-Al_2O_3$), respectively, whereas that obtained with the catalyst-alone was considerably lower (about 30%) even with $Ag\;(nanowire)/{\gamma}-Al_2O_3$ under the same condition. The enhanced catalytic activity towards $NO_x$ conversion in the presence of plasma can be explained by the formation of more reactive $NO_2$ species and partially oxidized hydrocarbon intermediates from the oxidation of NO and n-heptane under plasma discharge. Increasing the SIE tended to improve $NO_x$ conversion efficiency, and so did the increase in the n-heptane concentration; however, a further increase in the n-heptane concentration beyond $C_1/NO_x$ ratio of 5 did not improve the $NO_x$ conversion efficiency any more. The increase in the humidity affected negatively the $NO_x$ conversion efficiency, resulting in lowering the $NO_x$ conversion efficiency at the higher water vapor content, because water molecules competed with $NO_x$ species for the same active site. The $NO_x$ conversion efficiency increased with increasing the oxygen content from 3 to 15%, in particular at low SIE values, because the formation of $NO_2$ and partially oxidized hydrocarbon intermediates was facilitated.

Study of the Dehydrogenation Characteristics of Pt-Sn Catalysts by Propane Pulse Injection (프로판 펄스 주입에 의한 백금주석촉매의 탈수소반응 특성 연구)

  • Koh, Hyoung Lim;Jung, Jae-Won;Choi, Yi-Sun
    • Korean Chemical Engineering Research
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    • v.57 no.4
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    • pp.575-583
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    • 2019
  • The results of the catalytic reaction by pulsed injection of reactants are useful for studying the initial reaction characteristics in the case of many coke invloved reactions. The dehydrogenation characteristics of alumina supported platinum tin catalysts were investigated by pulsed injection of propane. The yield of propylene was maximized when the reduction time of propane injection catalyst was $550^{\circ}C$. Raman analysis showed that the amount of coke was very small when PtSn (4.5) catalyst was used and the short contact time was simulated by propane pulse injection. n order to differentiate the degree of dispersion of platinum, PtSn (4.5) catalyst was sintered at $900^{\circ}C$ with hydrogen, and then the temperature of air - redispersion was varied and propane pulse was injected. As a result, conversione and yield were the highest when air-redispersion temperature is $600^{\circ}C$. The lower the air-redispersion temperature, the higher the selectivity. As the tin content in the platinum catalyst increased, the propane conversion was lowered, but the selectivity to propylene increased and the yield increased. From this, it can be seen that the tin-added platinum catalyst is less active than the platinum catalyst from the beginning of the reaction, which is less affected by coke. The dehydrogenation reaction by the propane pulse injection shows a higher conversion rate than the result of continuous injection due to the formation of COx, and the amount of coke is very small. Decrease in selectivity due to the formation of COx can be reduced by increasing the reduction temperature and time.

Removal of NOx by Selective Catalytic Reduction Using Ceramic Foam Supports (SCR반응에서 세라믹 폼 지지제를 이용한 NOx 제거)

  • 한요섭;김현중;박재구
    • Proceedings of the Korea Air Pollution Research Association Conference
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    • 2003.11a
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    • pp.141-142
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    • 2003
  • 최근 자동차 수요증가 및 산업용 보일러 둥 급증하는 추세이며 이로 인한 대도시 대기오염 문제는 위험수위에 도달해 있다. 이러한 산업용 보일러, 화력발전소등 고정배출원과 자동차에서 발생하는 배기가스에는 인체에 유해한 일산화탄소(CO), 질소산화물(NOx), 황산화물(SOx)등이 다량 함유되어 있다. 유독성 가스중 질소산화물(NOx) 저감방법에는 특히 선택적 촉매환원법(Selective Catalytic Reduction, SCR)이 가장 널리 적용되고 있다. SCR법은 촉매하에서 NH$_3$, CO, 탄화수소(메탄, 에탄올, 프로판 등)의 환원제를 사용하여 NOx를 $N_2$로 전환하시키는 기술이다. (중략)

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The Effect of HCl Gas on Selective Catalytic Reduction of Nitrogen Oxide (질소산화물의 선택적 환원 제거시 염화수소기체가 촉매에 미치는 영향)

  • Choung, Jin-Woo;Choi, Kwang-Ho;Seong, Hee-Je;Chai, Ho-Jung;Nam, In-Sik
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.4
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    • pp.609-617
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    • 2000
  • This study is aimed at investigating an effect of HCl gas on selective reduction of NOx over a CuHM and $V_2O_5-WO_3/TiO_2$ catalyst. SCR process is the most effective method to remove NOx, but catalyst can be deactivated by the acidic gas such as HCl gas which is also included in flue gas from the incinerator. In dry condition of flue gas, the CuHM catalyst treated by HCl gas has shown higher NO removal activity than the fresh catalyst. The activity of the catalyst can be restored by treating at $500^{\circ}C$. On the contrary. $V_2O_5-WO_3/TiO_2$ catalyst is obviously deactivated by HCl and the deactivation increases in proportion to the concentration of HCl gas. The deactivated catalyst is not restored to it's original activity by heat treatment for regeneration. In wet flue gas stream, the CuHM catalyst has shown lower activity than fresh catalyst and $V_2O_5-WO_3/TiO_2$ catalyst was severely deactivated by HCl treatment. The activity loss of catalysts are mainly due to the decrease of Br$\ddot{o}$nsted acid site on the catalyst surface by $NH_3$ TPD. The change of BET surface area of CuHM catalyst after the reaction isn't observed but $V_2O_5-WO_3/TiO_2$ catalyst is observed. The amount of $Cu^{{+}{+}}$ and $V_2O_5$ is decreased after the reaction. From these results, it is expected that CuHM catalyst should be better than $V_2O_5-WO_3/TiO_2$ catalyst for its application to the incineration of flue gas.

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Long-term Stability of the $V_2O_5/TiO_2$ Honeycomb Catalyst in Flue Gas from Coal Fired Power Plant (석탄화력발전소 배기가스를 이용한 $V_2O_5/TiO_2$ 촉매의 내구성 연구)

  • 이인영;김동화;이정빈;엄희문;지평삼
    • Proceedings of the Korea Air Pollution Research Association Conference
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    • 1999.10a
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    • pp.235-236
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    • 1999
  • 보일러와 같은 고정원에서 배출되는 질소산화물을 제거하기 위한 후처리 기술인 선택적촉매환원공정(SCR:Selective Catalytic Reduction)은 안정적이며 탈질효율이 높아 상업적으로 가장 많이 이용되고 있다(Bosch, 1988). 본 연구팀은 가격 및 성능 측면에서 외국산 상업용 촉매와 경쟁할 수 있는 국산 SCR 촉매의 개발을 위하여 국내에서 안료용으로 생산되는 TiO$_2$를 촉매의 담체로 이용, V$_2$O$_{5}$/TiO$_2$ 하니콤 촉매를 제조하여 촉매의 활성 및 특성을 연구 중에 있다(이정빈, 1999).(중략)

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