Abstract:
본 발명에서는, Ca X Ni Y (PO 4 ) 6 으로 구성되는 것을 특징으로 하는 산화물 담체를 사용하지 않는 탄화수소의 부분산화용 촉매를 개시하고, 또한, 이염기 암모늄 수용액, 질산니켈 수용액, 질산칼슘 수용액을 제공하는 단계(S1); 상기 수용액을 혼합하는 단계(S2); 및 상기 혼합된 수용액을 가열하고, 건조한 후, 소성하는 단계(S3);를 포함하는 것을 특징으로 하는 산화물 담체를 사용하지 않는 탄화수소의 부분산화용 촉매의 제조 방법을 개시하며, 또한, 상기한 촉매를 환원시킨 후, 수소로 환원시키는 추가 과정 없이, 탄화수소의 부분산화 반응을 수행하는 것을 특징으로 하는 산화물 담체를 사용하지 않는 촉매를 이용한 탄화수소의 부분산화 방법을 개시한다. 본 발명에 따른 산화물 담체를 사용하지 않는 탄화수소의 부분산화용 촉매, 그 제조 방법 및 그 촉매를 이용한 탄화수소의 부분산화 방법은, 탄화수소의 부분산화 반응에 이용되었던 종래의 산화물 담체에 담지된 Ni 촉매의 문제점을 해결하여, Ni 입자가 미세하고 잘 분산되어 반응 활성을 유지할 수 있고 탄소침적에 대한 저항성을 크게 하여 촉매의 안정성을 제공할 수 있다. 또한, 본 발명은 일단 한번만 환원시키고 나면, 공기에 노출되어도 수소로 환원시키는 과정을 다시 거치지 않고, 즉 CH 4 /O 2 만으로도 비교적 낮은 온도에서 재활성화가 가능하므로, 그 취급이 용이하고, 콤팩트한 형태의 소형 장치 및 설비에적용하는 것이 적합하다. 따라서, 탑재(on-board)되는 중소형 고정형 설비나 자동차용 연료전지등 콤팩트한 형태의 소형 장치등에 유용하다.
Abstract:
본 발명은 직접메탄올 연료전지에 사용되는 고분자 전해질막의 메탄올 크로스오버 현상을 줄이고, 전지의 성능을 향상시키기 위해 플라즈마 화학기상증착(PECVD) 방법으로 고분자 전해질막 표면에 무기질 박막을 코팅하는 직접메탄올 연료전지용 복합 고분자 전해질막의 제조 방법에 관한 것이다. 본 발명에 의한 무기질 박막이 코팅된 직접메탄올 연료전지용 복합고분자 전해질막의 제조 방법은 플라즈마 화학기상 증착법을 이용하여 상용의 직접메탄올 연료전지용 고분자 전해질막의 표면에 실리콘 옥사이드(SiO 2 ), 티타늄 옥사이드(TiO 2 ), 지르코늄 옥사이드(ZrO 2 ), 지르코늄 포스페이트(Zr(HPO 4 ) 2 ), 제올라이트, 실리카라이트 및 알루미늄 옥사이드(Al 2 O 3 )로 구성되는 군으로부터 1 이상 선택되는 무기질로 구성되는 무기질 박막을 1.0 내지 500 나노미터의 두께로 코팅하여 복합막을 얻는 것을 특징으로 한다. 본 발명은 PECVD 장치를 이용하여 직접메탄올 연료전지용 고분자 전해질막에 무기질 박막을 코팅함으로써, 고분자 전해질막의 이온 전도도를 크게 감소시키지 않으면서 메탄올 크로스오버를 상당히 감소시키며, 직접메탄올 연료전지에 적용하였을 때 높은 전지 성능을 구현할 수 있다.
Abstract:
PURPOSE: Provided is a supported ceramic on metal catalyst for water gas shift reaction, in which the catalyst has higher catalytic activity and thermal stability than supported metal on ceramic catalyst, and further provided is a method for preparing the same. CONSTITUTION: The catalyst comprises metal carrier such as gold, silver, copper, nickel, zinc, chrome and aluminum and ceramics supported on the metal carrier, wherein the ceramic is ceria, zirconia, bismuth, perovskite or bismuth oxides. The method comprises the steps of (a) on one or more metal selected from a group consisted of gold, silver, copper, nickel, zinc, chrome and aluminum, supporting ceramics based on ceria, zirconia, bismuth, perovskite or bismuth oxides, (b) drying the ceramics supported on metal at room temperature, (c) oxidizing the ceramics at a temperature of 500 to 1000°C, and (d) reducing the ceramic on metal at a temperature of 300 to 450°C in hydrogen ambient.
Abstract:
PURPOSE: A fuel electrode for a molten carbonate fuel cell and a molten carbonate fuel cell containing the electrode are provided, to inhibit the deterioration of the performance of fuel cell due to the cracking of an electrolyte matrix and the increase of polarization of fuel cell and to lower the manufacturing cost. CONSTITUTION: The fuel electrode is prepared by mixing at least one reinforcing powder selected from the group consisting of a Ni-containing metal mixture, a Ni-containing alloy and a Ni-containing metal compound for improving the resistance against sintering and compression molding during the operation of a fuel electrode, and a pure Ni or Cu powder for improving the sintering property. Preferably the content of the reinforcing powder is 30-70 vol%.
Abstract:
PURPOSE: A gas supply apparatus for the operation of a fuel cell is provided, to allow the apparatus to be operated under a high pressure, the humidification state of the gas supplied to a fuel cell to be controlled easily and the water necessary for the humidification to be supplemented even during operation. CONSTITUTION: The gas supply apparatus supplies the reaction gas to a fuel cell after humidifying the reaction gas supplied from a gas source in a humidifier, wherein the humidifier comprises a container(30) receiving the reaction gas and humidifying it by using water; a humidifier gas supply pipe(13) whose one side is inserted into the container to supply the reaction gas to be humidified; a water supply pipe(33) supplying the water to be used for humidifying the reaction gas to the container; and a fuel cell gas supply pipe(15) connected with the container to supply the humidified reaction gas to a fuel cell. Preferably a detachable jacket-shaped container heater(35) is set at the outer circumference of the container for humidifying the reaction gas by heating; and a water supplement valve(34) is set at the water supply pipe.
Abstract:
PURPOSE: A porous gas distribution plate for a small fuel cell which can be formed in the shape of a sheet maintaining suitable physical strength is provided. A metal separation plate comprising the gas distribution plate is also provided. CONSTITUTION: The porous gas distribution plate for a small fuel cell comprises a metal plate through which a number of holes(130) having a diameter less than 2 mm are formed by etching. One side of the metal plate is flat while fine gas channels(120) having a depth less than 0.6 mm and a width less than 2 mm are formed on the other side with separating by a constant distance less than 2 mm. The small fuel cell comprising the separation plate formed from the gas distribution plate has improved output density, confidence and low manufacturing costs.
Abstract:
PURPOSE: Provided is an anode which has the inner surface of pore coated with porous ceramic film, shows improved wettability to electrolyte, and prevents the consumption of electrolyte, and thus can stably retain an excellent capability of battery when the battery works for a long time. CONSTITUTION: The anode for molten carbonate fuel cell comprising an anode, an electrolyte and a cathode, is characterized in that the anode has pore side coated with porous ceramic film. The anode consists of any one selected from the group consisting of pure Ni, Ni-containing metal mixture, Ni-containing alloy, and Ni-containing metal compound. The porous ceramic film is formed from any sol selected from the group Al oxide, Ce oxide, Zr oxide, Al hydroxide, Ce-hydroxide, and Zr hydroxide. The porous ceramic film is formed by sol gel process comprising the steps of impregnating the anode with ceramic sol and drying the anode.
Abstract:
PURPOSE: Provided are an easy and fast process for producing an electrode for a fuel cell having high catalyst utilization rate and performance and performance reproducibility, and the electrode produced by using the process. CONSTITUTION: The process for producing the electrode for the fuel cell contains the steps of: forming a carbon layer(12) on a support(13) for the electrode by screen printing, wherein the carbon layer(12) uses a carbon slurry produced by using carbon powder having a particle size of 10-2000nm, teflon suspension as an adhesive agent, glycerol as a thickener, and a solvent such as water, isopropyl alcohol, or ethanol; forming a catalyst layer(11) on the carbon layer(12) by screen printing, wherein the catalyst layer(11) uses a catalyst slurry produced by using a catalyst having a particle size of 10-2000nm, an ionomer as an adhesive agent, glycerol as a thickener, and a solvent such as water, isopropyl alcohol, or ethanol.
Abstract:
PURPOSE: A direct interior-modified melt carbonate fuel cell is provided, which is provided with a carbonate blocking membrane to increase the lifetime and to improve the efficiency without the increase of internal resistance and the consumption of carbonate. CONSTITUTION: The melt carbonate fuel cell comprises a carbonate blocking membrane which is made of nickel or nickel-containing alloy and blocks the delivery of the hydroxide vapor converted from the carbonate vapor or the carbonates into a catalyst, between a fuel electrode and an interior-modified catalyst layer. Preferably the carbonate blocking membrane contains pores whose mean pore size is 0.01-10 micrometers, by the degree of 30-90 %, and has the thickness of 0.1-1 mm. The carbonate blocking membrane is prepared by coating nickel or nickel-containing alloy on the surface of porous inorganic carrier selected from the group consisting of Al2O3, SiO2, TiO2 and ZrO2.
Abstract:
PURPOSE: Provided are a process for producing a Li/Na electrolyte green sheet for a molten carbonate fuel cell(MCFC) and a method for pretreating and operating the MCFC containing the Li/Na electrolyte. CONSTITUTION: The Li/Na electrolyte green sheet is produced by the process comprising the steps of: ball-milling 100pts.wt. of a carbonate mixture powder comprising Li2CO3 and Na2CO3, 10-20pts.wt. of a binder, 10-20pts.wt. of a plasticizer, 1-2pts.wt. of a dispersing agent, 1-2pts.wt. of an antifoaming agent, and 50-100pts.wt. of ethanol solvent to prepare powdery slurry; tape-casting the powdery slurry; drying at a temperature of 40-90 deg.C. The method for pretreating and operating the MCFC containing the Li/Na electrolyte includes the steps of: supplying air at an ordinary temperature-300 deg.C, a mixture gas containing carbon dioxide and 5M of hydrogen at 300-650 deg.C, and a mixture gas comprising the hydrogen, the carbon dioxide, and steam after the temperature reaches 650 deg.C to an anode of the MCFC; supplying the air at an ordinary temperature-450 deg.C, inert gas or a mixture gas containing the inert gas and less than 10M of the hydrogen at 450-650 deg.C, and a mixture gas comprising the air and the carbon dioxide after the temperature reaches 650 deg.C to a cathode of the MCFC.