• 제목/요약/키워드: $CO_2$ conversion

검색결과 1,111건 처리시간 0.029초

A Theoretical Study of CO Molecules on Metal Surfaces: Coverage Dependent Properties

  • Sang -H. Park;Hojing Kim
    • Bulletin of the Korean Chemical Society
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    • 제12권5호
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    • pp.574-582
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    • 1991
  • The CO molecules adsorbed on Ni(111) surface is studied in the cluster approximation employing EH method with self-consistent charge iteration. The effect of CO coverage is simulated by allowing the variation of valence state ionization potentials of each Ni atom in model cluster according to the self-consistent charge iteration method. The CO coverage dependent C-O stretching frequency shift, adsorption site conversion, and metal work function change are attributed to the charge transfer between metal surface and adsorbate. For CO/Ni(111) system, net charge transfer from Ni surface to chemisorbed CO molecules makes surface Ni atoms be more positive with increasing coverage, and lowers Ni surface valence band. This leads to a weaker interaction between metal surface valence band and Co $2{\pi}^{\ast}$ MO, less charge transfer to a single CO molecule, and the bule shift of C-O stretching frequency. Further increase of coverage induces the conversion of 3-fold site CO to lower coordination site CO as well as the blue shift of C-O stretching frequency. This whole process is accompanied by the continuous increase of metal work function.

TiO2 광촉매를 이용한 CO제거 공정특성 (Characteristics of CO Removal Process Using TiO2 Photocatalyst)

  • 김진길;이상문;홍성창;이의동;강용
    • Korean Chemical Engineering Research
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    • 제51권1호
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    • pp.116-120
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    • 2013
  • 관상의 광촉매 반응기에서 Pt가 담지된 $TiO_2$ 광촉매를 사용한 CO 전환 반응에 의해 CO를 제거하는 광촉매 공정에 대해 고찰하였다. $TiO_2$ 촉매에 Pt를 담지하는 방법, CO를 포함한 기체흐름속도, 기체흐름에 포함된 CO의 농도 그리고 기체의 수분함량이 CO를 $CO_2$로 전환하는 반응의 전환율에 미치는 영향을 검토하였다. Pt/$TiO_2$ 광촉매가 관의 내부에 코팅된 관상광촉매 반응기에서 진행된 실험결과 기체의 흐름속도 범위가 0.01~0.25 m/s, CO의 농도가 20~100 ppm 그리고 기체의 상대습도가 20~40%의 범위에서 CO는 UV의 조사 조건에서 거의 100% 정도 제거될 수 있었다. 기체흐름에 포함된 CO의 전환율은 기체의 흐름속도가 증가할수록 그리고 포함된 CO의 농도가 증가할수록 점점 감소하였다. 기체 흐름에 포함된 수분은 OH 라디칼을 형성함으로써 CO의 제거를 촉진할 수 있었다.

Link-K와 KMTF 메시지 간 포맷 변환 방법 (Method of Format Conversion Between Link-K and KMTF Messages)

  • 김완식;이민식;김상준;박지현
    • 한국군사과학기술학회지
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    • 제20권2호
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    • pp.264-271
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    • 2017
  • Link-K message is the Tactical Data Link message standard developed by the Agency for Defense Development which is optimized for the Joint Operation of ROK Armed Force. KMTF message is the standard message format of Battle Management Information System. Interconversion and propagation between these messages are definitely needed to have efficient warfare such as situation data propagation using network, the convergence of collected situation data, common situational awareness, cooperative engagement. Therefore, this study suggests a way of rule and process for format conversion between Link-K and KMTF messages.

Fischer-Tropsch 합성용 SCR(Steam Carbon Dioxide Reforming) 공정 최적화 연구 (A Simulation Study on SCR(Steam Carbon Dioxide Reforming) Process Optimization for Fischer-Tropsch Synthesis)

  • 김용헌;구기영;송인규
    • Korean Chemical Engineering Research
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    • 제47권6호
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    • pp.700-704
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    • 2009
  • GTL(gas-to-liquid) 합성유 제조용 SCR(steam carbon dioxide reforming) 공정의 시뮬레이션 연구를 수행하였다. 온도 및 $CH_4/steam/CO_2$ 반응물 비와 같은 변수를 바꾸어 가면서 SCR 공정을 위한 최적 운전조건을 살펴보았다. 공정 시뮬레이션을 위해 Aspen Plus를 사용하였다. 또한 정상상태 가정하의 열역학적 물성치 계산을 위해 Aspen Plus의 RSK (Redlich-Kwong-Soave) 상태방정식을 사용하였다. FT 공정을 위한$H_2/CO$ 비, $CH_4$ 전환율, $CO_2$ 전환율을 살펴봄으로써 최적의 온도와 최적의 반응물 비를 결정하였다. 시뮬레이션 결과, SCR reformer 촉매층 출구 최적온도는 상압에서 $850^{\circ}C$ 였으며, 이 온도에서 $CH_4$ 전환율은 99%, $CO_2$ 전환율은 49%로 계산되었고, $CH_4/steam/CO_2$ 최적 반응물 비율은 1.0/1.6/0.7로 나타났다.

플라즈마 산화분해-탄화물 가스화 전환에 의한 태양연료 생산 (Production of Solar Fuel by Plasma Oxidation Destruction-Carbon Material Gasification Conversion)

  • 송희관;전영남
    • 청정기술
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    • 제26권1호
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    • pp.72-78
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    • 2020
  • 화석연료의 사용과 바이오가스 생산 과정에서 공기오염과 기후변화문제가 발생된다. 기후변화 주요 원인물질인 이산화탄소와 메탄을 양질의 에너지원으로 전환하는데 연구가 지속되고 있다. 본 연구에서는 바이오가스를 양질의 에너지로 전환하고 태양광과 풍력과 같은 연속생산의 문제가 있는 재생에너지와 연계된 태양연료를 생산하기 위해 플라즈마-탄화물 전환장치를 제안하였다. 그리고 이에 대한 가능성을 제시하기 위해 바이오가스 전환에 영향을 미치는 O2/C비, 전체가스공급량, CO2/CH4공급비의 변화에 따른 전환 및 생성가스 특성 파악하였으며 그 결과는 다음과 같다. O2/C비가 높아질수록 메탄과 이산화탄소의 전환이 증가하였다. 전체가스공급량은 임의 특정 값에서 최대의 전환을 보였다. CO2/CH4비 감소할 때 전환율이 증가되었다. 이상의 결과로 볼 때 본 연구에서 새로이 제안된 플라즈마 산화분해-탄화물 가스화 전환에 의한 태양연료 생산의 가능성이 확인되었다. 그리고 O2/C비가 0.8이고 CO2/CH4를 0.67로 하여 전체가스공급량을 40 L min-1 (VHSV = 1.37)로 공급할 경우 이산화탄소와 메탄 전환이 최대가 되어 생성가스 중 양질의 연료인 수소와 일산화탄소로의 전환이 최대를 보였다.

저급 석탄과 혼합한 폐촉매의 수증기 가스화 반응에 미치는 영향 (The Effect on the Steam Gasification Reaction of Low-Rank Coal Mixed with Waste Catalysts)

  • 곽재훈;서석진;이소정;송병호;손정민
    • 한국수소및신에너지학회논문집
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    • 제23권6호
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    • pp.647-653
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    • 2012
  • We have investigated the kinetics and activity of waste catalysts for steam-lignite gasification. Waste catalysts I, II, III and reference $K_2CO_3$ were used and physical mixed with a coal. The gasification experiments were carried out with the low rank coal loaded with 1 wt% and 5 wt% catalyst at the temperature range from 700 to $900^{\circ}C$ using thermobalance reactor. It was observed that the carbon conversion reached almost 100% regardless of the kinds of catalysts at $900^{\circ}C$. The shortest time to reach the designated conversion was obtained for 1 wt% waste catalyst II and 5 wt% $K_2CO_3$ at $900^{\circ}C$. The gasification reaction rate constant increased with increasing the temperature. Highest rate constant was obtained with $K_2CO_3$ at $900^{\circ}C$. The lowest activation energy was 69.42 kJ/mol for 5 wt% waste catalyst II. The waste catalyst had an influence on the reduction of activation energy.

고온 플라즈마 개질에 의한 메탄으로부터 고농도 수소생산 (Production of Hydrogen-Rich Gas from Methane by a Thermal Plasma Reforming)

  • 김성천;임문섭;전영남
    • 한국수소및신에너지학회논문집
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    • 제17권4호
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    • pp.362-370
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    • 2006
  • The purpose of this paper was to investigate the reforming characteristics and optimum operating condition of the plasmatron assisted $CH_4$ reforming reaction for the hydrogen-rich gas production. Also, in order to increase the hydrogen production and the methane conversion rate, parametric screening studies were conducted, in which there were the variations of the $CH_4$ flow ratio, $CO_2$ flow ratio, vapor flow ratio, mixing flow ratio and catalyst addition in reactor. High temperature plasma flame was generated by air and arc discharge. The air flow rate and input electric power were fixed 5.1 l/min and 6.4 kW, respectively. When the $CH_4$ flow ratio was 38.5%, the production of hydrogen was maximized and optimal methane conversion rate was 99.2%. Under these optimal conditions, the following synthesis gas concentrations were determined: $H_2$, 45.4%; CO, 6.9%; $CO_2$, 1.5%; and $C_2H_2$, 1.1%. The $H_2/CO$ ratio was 6.6, hydrogen yield was 78.8% and energy conversion rate was 63.6%.

상용 디젤엔진용 산화촉매의 배출가스 저감 특성 (Emission Characteristics of Diesel Oxidation Catalysts for a Commercial Diesel Engine)

  • 최병철;이춘희;박희주;정명근;권정민;신병선;김상수
    • 동력기계공학회지
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    • 제6권2호
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    • pp.18-23
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    • 2002
  • Recently, as people pay attention to the environmental pollution, the emission of diesel engine has become a serious problem. Diesel Oxidation Catalysts(DOC) were experimentally investigated for the purification of pollutants exhaust emission from the diesel engine. In this study, the conversion efficiency of exhaust gas was investigated with various washcoat materials of the DOC. It was formed that CO conversion efficiency depended on temperature, but THC conversion was dominated by temperature and space velocity. Conversion efficiency of THC and CO increased with the addition of ZSM-5 in the washcoat, whereas these conversion efficiency decreased by adding Nd and Ba additives. $V_2O_5$ additive had the thermal stability for high temperature. Thermal durability of the catalyst was improved as increase of $V_2O_5$ additive.

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An evaluation of power conversion systems for land-based nuclear microreactors: Can aeroderivative engines facilitate near-term deployment?

  • Guillen, D.P.;McDaniel, P.J.
    • Nuclear Engineering and Technology
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    • 제54권4호
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    • pp.1482-1494
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    • 2022
  • Power conversion cycles (Subcritical Steam, Supercritical Steam, Open Air Brayton, Recuperated Air Brayton, Combined Cycle, Closed Brayton Supercritical CO2 (sCO2), and Stirling) are evaluated for land-based nuclear microreactors based on technical maturity, system efficiency, size, cost and maintainability, safety implications, and siting considerations. Based upon these criteria, Air Brayton systems were selected for further evaluation. A brief history of the development and applications of Brayton power systems is given, followed by a description of how these thermal-to-electrical energy conversion systems might be integrated with a nuclear microreactor. Modeling is performed for optimized cycles operating at 3 MW(e) with turbine inlet temperatures of 500 ℃, 650 ℃ and 850 ℃, corresponding to: a) sodium fast, b) molten salt or heat pipe, and c) helium or sodium thermal reactors, coupled with three types of Brayton power conversion units (PCUs): 1) simple open-cycle gas turbine, 2) recuperated open-cycle gas turbine, and 3) recuperated and intercooled open-cycle gas turbine. Aeroderivative turboshaft engines employing the simple Brayton cycle and two industrial gas turbine engines employing recuperated air Brayton cycles are also analyzed. These engines offer mature technology that can facilitate near-term deployment with a modest improvement in efficiency.

가스분석을 이용한 석탄 종류별 $CO_2$ 가스화 반응특성 연구 (Characteristics of Various Ranks of Coal Gasification with $CO_2$ by Gas Analysis)

  • 김용택;서동균;황정호
    • 한국연소학회지
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    • 제15권2호
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    • pp.41-49
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    • 2010
  • Various coals from many countries around the world have been used for pulverized coal boiler in power plants in Korea. In this study, the gasification reactivities of various coal chars with $CO_2$ were investigated. Carbon conversion was measured using a real time gas analyzer with NDIR CO/$CO_2$ sensor. In a lab scale furnace, each coal sample was devolatilized at $950^{\circ}C$ in nitrogen atmosphere and became coal char and then further heated up to reach to a desired temperature. Each char was then gasified with $CO_2$ under isothermal conditions. The reactivities of coal chars were investigated at different temperatures. The shrinking core model (SCM) and volume reaction model(VRM) were used to interpret the experiment data. It was found that the SCM and VRM could describe well the experimental results within the carbon conversion of 0-0.98. The gasification rates for various coals were very different. The gasification rate for any coal increased as the volatile matter content increased.