• 제목/요약/키워드: methane oxidation

검색결과 195건 처리시간 0.033초

팔라듐 촉매의 메탄의 연소반응에 관한 연구 -담체의 크기와 소성온도에 따른 효과- (A Study of Combustion Reaction of Methane by Pd Catalyst - Effects of Support Size & Calcination Temperature -)

  • 이택홍
    • 한국가스학회지
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    • 제8권3호
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    • pp.52-56
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    • 2004
  • 팔라듐 촉매는 주로 수소화 반응, 산화반응, 저온 연소반응 등에 사용된다. 특히 최근에 연료전지에 많이 시도되고 있는 알코올 등의 개질을 통한 수소가스의 발생을 할 경우에도 이 팔라듐 촉매의 가능성에 상당한 관심이 증폭되어 왔다. 귀금속 촉매인 팔라듐 촉매가 성능이 우수하지만 고가이고 내구성과 소성후의 성능저하 등이 해결해야 할 과제로 남아 있다. 본 연구에서는 내구성과 소성 후에도 성능의 저하가 없는 팔라듐 촉매를 합성하고 반응성을 연구하였다.

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혼합 메탄자화균 생물막 반응기에 의한 Trichloroethylene 분해의 영향 인자 (Factors of Trichloroethylene Degradation by Methanotrophic Consortium Biofilm Reactor(MCBR))

  • 이무열;조현정;양지원
    • 대한환경공학회지
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    • 제22권6호
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    • pp.991-1000
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    • 2000
  • 메탄올 주요 탄소원으로 사용하며 가용성 메탄산화효소 (soluble methane monooxygenase, sMMO)를 분비하는 혼합 메탄차화균을 celite R-635에 고정화시켜 TCE를 함유한 폐수를 연속적으로 처리하였다. 2 ppm의 TCE를 공급했을 때 각각 6. 20시간의 체류시간에서 약 80.4, 84.5%의 처리 효율을 얻었으며, 체류시간이 증가함에 따라서 제거율도 서서히 증가하였다. 5 ppm의 TCE를 공급하고 10시간 동안 체류시켰을 때, '초기에는 TCE의 제거능이 낮았으나 점차 81%까지 증가하였다. 또한 산소를 공급하면서 메탄을 주기적으로 공급할 때 5 ppm의 TCE가 체류시간 10. 15시간에서 각각 88.5, 96.5%까지 제거되었다. 반응기 내에 산소가 고갈된 상태에서 메탈을 고농도로 공급하면 MMO에 흡착된 메탄의 산화반응이 쉽게 진행되지 않아 TCE 분해능이 떨어졌다. 파일롯트 플랜트 규모의 생물막 반응기에서의 TCE 분해 실험 결과, 실제 크기 규모의 공장에도 충분히 적용 가능할 것으로 사료되었다.

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Heterogeneous Catalysts Fabricated by Atomic Layer Deposition

  • Kim, Young Dok
    • 한국진공학회:학술대회논문집
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    • 한국진공학회 2013년도 제44회 동계 정기학술대회 초록집
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    • pp.128-128
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    • 2013
  • Fabrication of heterogeneous catalysts using Atomic Layer Deposition (ALD) has recently been attracting attention of surface chemists and physicists. In this talk, I will present recent results about structures and chemical activities of various catalysts prepared by ALD, particularly focusing on Ni-based catalysts. Ni has been considered as potential catalysts for $CO_2$ reforming of methane (CRM); however, Ni often undergoes rapid decrease in catalytic activity with time, and therefore, application of Ni as catalysts for CRM has been regarded as difficult so far. Deactivation of Ni catalysts during CRM reaction is from either coke formation on Ni surface or sintering of Ni particles during reaction. Two different strategies have been used for enhancing stability of Ni-based catalysts; $TiO_2$ nanoparticles were deposited on micrometer-size Ni particles by ALD, which turned out to reduce coke formation on Ni surfaces. Ni nanoparticles deposited by ALD on mesoporous silica showed high activity and long-term stability from CRM without coke deposition and sintering during CRM reaction. Ni-based catalysts have been also used for oxidation of toluene, which is one of the most notorious gases responsible for sick-building syndrome. It was shown that onset-temperature of Ni catalysts for toluene oxidation is as low as $120^{\circ}C$. At $250\circ}C$, total oxidation of toluene to $CO_2$ with a 100% conversion was found.

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비열 플라즈마에 의한 NO의 산화에 탄화수소 첨가제가 미치는 영향 (Effect of Hydrocarbons on the Promotion of NO-$NO_2$ Conversion in NonThermal Plasma DeNOx Treatment)

  • 신현호;윤웅섭
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2000년도 제21회 KOSCO SYMPOSIUM 논문집
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    • pp.33-46
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    • 2000
  • In the present study, a systematic chemical kinetic calculations were made to investigate the augmentation of NO-$NO_2$ conversion due to the addition of various hydrocarbons (methane, ethylene, ethane, propene, propane) in the nonthermal plasma treatment. It is included in the present conclusion that the reaction between hydrocarbon and oxygen radicals induced by electron collision, is believed to be a primarily process for triggering the overall NO oxidation and the eventual NOx reduction. Upon the completion of the initiating step, various radicals (OH, $NO_2$ etc.) successively produced by hydrocarbon decomposition form the primary path of NO-$NO_2$ conversion. When the initiating step is not activated, hydrocarbon consumption rate appeared to be very low, thereby the targeted level of NO conversion can only be achieved by the addition of more input energy. Present study showed ethylene and propene to have higher affinity with 0 radical under all conditions, thereby both of these hydrocarbons show very fast and efficient NO-$NO_2$ oxidation. It was also shown that propene is superior to ethylene in the aspect of NOx removal.

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비열 플라즈마에 의한 NO의 산화에 탄화수소 첨가제가 미치는 영향 (Effect of Hydrocarbons on the Promotion of $NO-NO_{2}$ Conversion in NonThermal Plasma DeNOx Treatment)

  • 신현호;윤웅섭
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2000년도 제20회 KOSCO SYMPOSIUM 논문집
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    • pp.178-188
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    • 2000
  • In the present study, a systematic chemical kinetic calculations were made to investigate the augmentation of $NO-NO_{2}$ conversion due to the addition of various hydrocarbons (methane, ethylene, ethane, propene, propane) in the nonthermal plasma treatment. It is included in the present conclusion that the reaction between hydrocarbon and oxygen radicals induced by electron collision, is believed to be a primarily process for triggering the overall NO oxidation and the eventual NOx reduction. Upon the completion of the initiating step, various radicals (OH, $HO_{2}$ etc.) successively produced by hydrocarbon decomposition form the primary path of $NO-NO_{2}$ conversion. When the initiating step is not activated, hydrocarbon consumption rate appeared to be very low, thereby the targeted level of NO conversion can only be achieved by the addition of more input energy. Present study showed ethylene and propene to have higher affinity with 0 radical under all conditions, thereby both of these hydrocarbons show very fast and efficient $NO-NO_{2}$ oxidation. It was also shown that propene is superior to ethylene in the aspect of NOx removal.

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니켈 담지촉매의 니켈 담지량에 따른 활성 변화 (Activity Changes of Supported Nickel Catalysts with Respect to Ni Loading)

  • 김상범;박은석;천한진;김영국;김명수;박홍수;함현식
    • 한국응용과학기술학회지
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    • 제20권3호
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    • pp.230-236
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    • 2003
  • Synthesis gas is commercially produced by a steam reforming process. However, the process is highly endothermic and energy-consuming. Thus, this study was conducted to produce synthesis gas by the partial oxidation of methane to decrease the energy cost. Supported Ni catalysts were prepared by the impregnation method. To examine the activity of the catalysts, a differential fixed bed reactor was used, and the reaction was carried out at $750{\sim}850^{\circ}C$ and 1 atm. The fresh and used catalysts were characterized by XRD, XPS, TGA and AAS. The highest catalytic activity was obtained with the 13wt% Ni/MgO catalyst, with which methane conversion was 81%, and $H_2$ and CO selectivities were 94% and 93%, respectively. 13wt% Ni/MgO catalyst showed the best $MgNiO_2$ solid solution state, which can explain the highest catalytic activity of the 13wt% Ni/MgO catalyst.

혐기소화에 의한 Biogas 생산과 Biomethanol 전환에 관한 고찰 (Biomethanol Conversion from Biogas Produced by Anaerobic Digestion)

  • 남재작;신중두;홍승길;함현식;박우균;소규호
    • 유기물자원화
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    • 제14권4호
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    • pp.93-103
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    • 2006
  • 바이오가스는 유기물의 혐기소화과정에서 생기는 부산물로 열에너지와 전기에너지로 사용되어왔다. 바이오디젤생산의 반응물과 연료로 사용되고 있는 메탄올의 수요는 꾸준히 증가하고 있다. 본 총설에서는 메탄올을 메탄올로 전환하는 직접부분산화법의 최근 발전 동향을 간략한 메탄올합성의 역사와 함께 다루었으며, 산업 규모에서 주로 사용되고 있는 증기개질반응과 현재 연구단계에서 발전하고 있는 촉매산화법을 비교하였다. 이 총설에서는 바이오가스로부터 메탄올전환의 가능성이 기술적인 측면과 경제적 실용성 면에서 제시되었다.

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Modified glycine-nitrate process(MGNP)로 합성한 BaCo1-x-yFexZryO3-δ 산소투과도 및 수소생산성 (Oxygen Permeation and Hydrogen Production of BaCo1-x-yFexZryO3-δ by a Modified Glycine-nitrate Process (MGNP))

  • 이은정;황해진
    • 한국수소및신에너지학회논문집
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    • 제24권1호
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    • pp.29-35
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    • 2013
  • A dense mixed ionic and electronic conducting ceramic membrane is one of the most promising materials because it can be used for separation of oxygen from the mixture gas. The $ABO_3$ perovskite structure shows high chemical stability at high temperatures under reduction and oxidation atmospheres. $BaCo_{1-x-y}Fe_xZr_yO_{3-{\delta}}$ (BCFZ) was well-known material as high mechanical strength, low thermal conductivity and stability in the high valence state. Glycine Nitrate Process (GNP) is rapid and effective method for powder synthesis using glycine as a fuel and show higher product crystallinity compared to solid state reaction and citrate-EDTA method. BCFZ was fabricated by modified glycine nitrate process. In order to control the burn-up reaction, $NH_4NO_3$ was used as extra nitrate. According to X-Ray Diffraction (XRD) results, BCFZ was single phase regardless of Zr dopants from y=0.1 to 0.3 on B sites. The green compacts were sintered at $1200^{\circ}C$ for 2 hours. Oxygen permeability, methane partial oxidation rate and hydrogen production ability of the membranes were characterized by using Micro Gas Chromatography (Micro GC) under various condition. The high oxygen permeation flux of BCFZ 1-451 was about $1ml{\cdot}cm^{-2}s^{-1}$. Using the humidified Argon gas, BCFZ 1-433 produced hydrogen about $1ml{\cdot}cm^{-2}s^{-1}$.

Ni-Pd/CeO2-ZrO2 금속모노리스 촉매체를 사용한 부분산화반응에 의한 합성가스 제조 (Syngas Production by Partial Oxidation Reaction over Ni-Pd/CeO2-ZrO2 Metallic Monolith Catalysts)

  • 양정민;최정은;김용진;이종대
    • Korean Chemical Engineering Research
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    • 제51권3호
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    • pp.319-324
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    • 2013
  • 합성가스를 생산하기 위한 메탄의 부분산화반응 특성을 $Ni/CeO_2-ZrO_2$, $Ni-Ru/CeO_2-ZrO_2$$Ni-Pd/CeO_2-ZrO_2$ 촉매체를 이용하여 조사하였다. 메탄의 부분 산화 개질 반응에서 촉매의 높은 활성과 안정성을 위하여 허니컴 구조의 금속모노리스 촉매 체를 적용하였다. 촉매분석은 XRD와 FE-SEM을 사용하였으며, 제조된 촉매들의 합성가스 제조 특성은 반응물 비(O/C), GHSV와 온도를 변화시키면서 연구하였다. 개질 실험에서 사용된 촉매 중에서 $Ni-Pd/CeO_2-ZrO_2$ 촉매 체가 가장 높은 활성을 보여 주었으며, $900^{\circ}C$, GHSV=10,000 $h^{-1}$과 O/C=0.55에서 99%의 메탄 전환율을 얻었다. O/C 비가 증가함에 따라 수소 yield는 증가되고, 반면에 CO yield는 거의 일정하게 유지됨을 확인할 수 있었다. 또한 GHSV가 증가할수록 메탄의 전환율은 감소하였으며, 높은 메탄의 전환율을 얻을 수 있는 GHSV의 범위는 10,000 $h^{-1}$ 이하임을 알 수 있었다.