• Title/Summary/Keyword: 일산화탄소

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Effect of Water Addition on Activity of Gold Catalysts Supported on Metal Oxide at Low Temperature CO Oxidation (일산화탄소 저온 산화에서 금속산화물에 담지된 금촉매의 활성에 미치는 수분첨가의 영향)

  • Ahn, Ho-Geun;Kim, Ki-Joong;Chung, Min-Chul
    • Korean Chemical Engineering Research
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    • v.49 no.6
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    • pp.720-725
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    • 2011
  • Gold catalysts supported on metal-oxides were prepared by co-precipitation using the various metal nitrates and chloroauric acid as precursors, and effect of water addition on the catalytic activity in CO oxidation was investigated. Among the various supported gold catalysts, Au/$Co_{3}O_{4}$ and Au/ZnO catalysts showed the excellent activity for CO oxidation. Water in the reactant gas had a negative effect on the oxidation activity over Au/$Co_{3}O_{4}$ catalysts and a positive effect on that over Au/ZnO, which means the activity depends strongly on the nature of support. It was also confirmed that no significant change in the particle size of gold was observed after reaction both in dry and wet conditions. This fact suggested that the deactivated catalyst due to a carbonate species could be regenerated by water addition in the reactant gas.

Design of Water Gas Shift Reactor for Rapid Start-Up in 200 W Portable Fuel Cell System (200 W급 휴대용 연료전지 시스템의 빠른 기동 특성을 위한 수성 가스 반응기 설계)

  • Choi, Jong-Rock;Lee, Sungchul
    • Korean Chemical Engineering Research
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    • v.51 no.4
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    • pp.455-459
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    • 2013
  • The fuel processor for the portable fuel cell includes multi-step processes consisting of hydrogen generator, heat generator and several CO clean-up stages. One of requirements of the fuel processor for portable fuel cell system is a rapid start-up time. Especially, the warm-up time for WGS reactor is crucial factors for total start-up time. In this paper, active heating protocol, which is the heating protocol of WGS reactor supplied by the oxidation of CO rich reformate in the initial stage, is used for a rapid start-up. The air stream fed to the inlet of WGS reactor rapidly oxidize the CO rich reformate in the WGS reactor. Therefore, CO concentration in reformate quickly stabilized at the desired concentration without CO surges.

Performance and Operational Characteristics of Natural Gas Fuel Processor for 1kW Class PEMFCs (1kW급 고분자 연료전지용 통합형 천연가스 개질 수소 제조 시스템의 성능 및 운전 특성)

  • Seo, Yu-Taek;Seo, Dong-Joo;Seo, Young-Seog;Roh, Hyun-Seog;Jeong, Jin-Hyeok;Yoon, Wang-Lai
    • 한국신재생에너지학회:학술대회논문집
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    • 2006.06a
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    • pp.17-20
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    • 2006
  • 한국에너지기술연구원에서는 가정용 고분자연료전지 열병합 발전시스템을 위한 통합형 천연가스 연료처리 시스템을 개발해 왔다. 가정용 시스템으로서 필수적인 소형화와 고효율을 현실화하기 위해, 연료처리 시스템의 각 단위 공정 즉 수증기 개질, 수성가스 전이, 선택적 산화 공정 등을 이중 동 심관형 반응기에 통합하여 상호 열교환이 용이하도록 반응기를 설계하였다. 현재 시험 운전 중인 Prototype-I 연료 처리 시스템은 1kW급 고분자 연료전지 열병합 발전 시스템에 개질 가스를 공급하기 위해 설계되었으며, 기초 성능은 정격 부하 운전시 열효율 78% (HHV 기준), 메탄 전환율 91%이다. 개질 가스 내 일산화탄소 농도는 고분자 연료전지 전극의 피독을 피하기 위해 10ppm 이하로 유지되어야 하며, Prototype-I 연료 처리 시스템은 백금과 루테늄 촉매를 적용한 선택적 산화 반응기를 통해 개질 가스 내 일산화탄소 농도를 10ppm 이하로 제거하였다. 일반 가정에서는 고분자 연료전지 시스템의 부하 변동이 예상되기 때문에 연료 처리 시스템의 부하 변동 운전 특성도 살펴보았다 정격 부하에서 80%, 60%, 40%로 부하를 변동하며 운전하였고, 각 부하에서 안정한 메탄 전환율과 10ppm이하의 일산화탄소 농도를 보였다. 80%까지는 열효율이 77%로 큰 변화를 보이지 않았으며, 60%에서는 76%, 40%에서는 72%로 열효율이 감소하는 현상을 보였다 연료 처리 시스템의 일일 시동-정지 운전시 내구성을 테스트 중이다. 현재까지 50여회의 일일-시동 정지를 시도하였다 시동 후 약 세 시간가량의 정력 부하 운전을 실시한 후 부하 변동을 실시하였고, 총 운전 시간 8시간 정도 운전한 후 시스템을 정지하였다 메탄 전환율과 일산화 탄소 농도, 열효율을 모니터링 하고 있으며, 현재까지 초기 성능을 그대로 유지하고 있다. 앞으로 일일시동-정지 운전 시험을 지속하면서 초기 시동 특성 및 부하 변동에 따른 응답 특성 개선, 그리고 연료전지와의 연계 운전을 실시할 예정이다

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Effects of CO and $CO_2$ on Hydrogen Permeation through Pd-coated V-Ti-Ni Alloy Membranes (Pd 코팅된 V-Ti-Ni 합금 분리막을 통한 수소투과에서 CO와 $CO_2$의 영향)

  • Jeon, Sung-Il;Park, Jung-Hoon;Lee, Yong-Taek
    • Membrane Journal
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    • v.21 no.3
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    • pp.290-298
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    • 2011
  • The influence of co-existing gases on the hydrogen permeation was studied through a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane. The hydrogen permeation characteristics of Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane have been investigated in the pressure range 1-3 bar under pure hydrogen and hydrogen mixture gas with carbon dioxide and carbon monoxide at $450^{\circ}C$. Preliminary hydrogen permeation experiments have been confirmed that hydrogen flux was $5.36mL/min/cm^2$ for a Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane (thick: 0.5 mm) using pure hydrogen as the feed gas. In addition, hydrogen fluxes were 4.46, 5.20, $3.91mL /min/cm^2$ for$V_{53}Ti_{26}Ni_{21}$ alloy membrane using $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ as the feed gas respectively. Therefore, the hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of temperature and pressure when $H_2/CO_2$, $H_2/CO$ and $H_2/CO_2/CO$ mixture applied as feed gas respectively and permeation fluxes were satisfied with Sievert's law in different feed conditions. It was found from XRD results after permeation test that the Pd-coated $V_{53}Ti_{26}Ni_{21}$ alloy membrane had good stability and durability for various mixtures feeding condition.

Dispersion and Stability of Platinum Catalysts Supported on Titania-, Vanadia-, Zirconia- and Ceria-Incorporated Silicas (티타니아, 바나디아, 지르코니아, 세리아를 고정한 실리카에 담지된 백금 촉매의 분산성과 안정성)

  • Kim, Mi-Young;Seo, Gon;Park, Jung-Hyun;Shin, Chae-Ho;Kim, Eun-Seok
    • Korean Chemical Engineering Research
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    • v.49 no.1
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    • pp.1-9
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    • 2011
  • Platinum catalysts were prepared by impregnating platinum precursor on titania-, vanadia-, zirconia- and ceria-incorporated silicas followed by hydrogen peroxide treatment. The effects of the oxide incorporation and the hydrogen peroxide treatment in the preparation of the platinum catalysts on their platinum dispersion and catalytic activity in carbon monoxide oxidation were investigated. XRD, TEM, EXAFS, XPS and carbon monoxide chemisorption studies confirmed the high dispersion of platinum even on silica by the oxide incorporation and hydrogen peroxide treatment. However, the type of oxides incorporated on silica caused considerable variances in the adsorption and the catalytic activity in the oxidation of carbon monoxide on them. The incorporation of titania, zirconia and ceria on silica and further hydrogen peroxide treatment enhanced the platinum dispersion, resulting in the improved catalytic activities. Among the catalysts supported on the oxide-incorporated silicas, the platinum catalyst supported on zirconia-incorporated silica exhibited the highest activity because of the highest platinum dispersion due to the formation of Pt-O-Zr bonds.

The Risk Assessment of Carbon Monoxide Poisoning by Gas Boiler Exhaust System and Development of Fundamental Preventive Technology (가스보일러 CO중독 위험성 예측 및 근원적 예방기술 개발)

  • Park, Chan Il;Yoo, Kee-Youn
    • Journal of the Korean Institute of Gas
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    • v.25 no.3
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    • pp.27-38
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    • 2021
  • We devised the system to automatically shutdown the boiler and to fundamentally block the harmful gases, including carbon monoxide, into the indoor when the exhaust system swerves: (1) The discharge pressure of the exhaust gas decreases when the exhaust pipe is disconnected. The monitoring system of the exhaust pipe is implemented by measuring the output voltage of APS(Air Pressure Sensor) installed to control the amount of combustion air. (2) The operating software was modified so that when the system recognizes the fault condition of a flue pipe, the boiler control unit displays the fault status on the indoor regulator while shutting down the boiler. In accordance with the ventilation facility standards in the "Rules for Building Equipment Standards" by the Ministry of Land, Infrastructure and Transport, experiments were conducted to ventilate indoor air. When carbon monoxide leaked in worst-case scenario, it was possible to prevent poisoning accidents. However, since 2013, the number of indoor air exchange times has been mitigated from 0.7 to 0.5 times per hour. We observed the concentration exceeding TWA 30 ppm occasionally and thus recommend to reinforce this criterion. In conclusion, if the flue pipe fault detection and the indoor air ventilation system are introduced, carbon monoxide poisoning accidents are expected to decrease significantly. Also when the manufacturing and inspection steps, the correct installation and repair are supplemented with the user's attention in missing flue, it will be served to prevent human casualties from carbon monoxide poisoning.