Abstract:
본 발명은 마이크로파에 의한 무기소재 박막의 제조방법에 관한 것으로, 더욱 상세하게는 기판(Substrate), 기판과 무기막을 접착하는 접착층, 그리고 무기 결정막이 차례로 적층되어 있는 무기소재 박막을 제조하는데 있어, 상기한 접착층에는 사용되는 무기막 소재보다 상대적으로 유전도가 높은 나노크기의 금속산화물 또는 금속 실리케이트 산화물을 박막 코팅하여 무기접착층을 형성한 후에, 무기막을 형성하기 위한 무기결정 전구용액 또는 무기결정 용액에 담그어 마이크로파를 조사하므로써 상대적으로 유전도가 높은 무기접착층에 무기결정이 선택적으로 흡수되어 규칙적인 배향으로 그리고 강력한 결합력으로 나노조립되도록 하는 마이크로파에 의한 무기소재 박막의 제조방법에 관한 것이다. 수열방법을 비롯한 무기물을 이용한 종래 방법에 의하면 무기결정 박막의 나노조립이 용이하지 않고, 또 무기 결정이 막으로부터 쉽게 분리되는 단점이 있으나, 본 발명의 제조방법에 의하면 무기결정이 무기접착층과 강력한 결합력으로 나노조립되는 우수성이 있다.
Abstract:
PURPOSE: To provide a noble VSB-5 molecular sieve composition containing metal components and a method for preparing a VSB-5 molecular sieve, which is able to prepare the VSB-5 molecular sieve through an economic and efficient method using an inexpensive inorganic base or mono-amine. CONSTITUTION: In the method for preparing nanoporous VSB-5 molecular sieve by crystallizing a raw material consisting of a nickel compound and a phosphorous compound using a base, one or two metals selected from the group consisting of transition metals, typical metals, noble metals, and lanthanium are contained in the raw material, an inorganic base or an organic amine is added to the raw material, and the crystallization is performed under pH of 7.0-12.0 and at the temperature of 50-350 deg.C.
Abstract:
PURPOSE: Provided are a photocatalyst capable of obtaining methane and methanol from carbon dioxide with high efficiency and a method for fabricating the same. CONSTITUTION: The method comprises the steps of (a) mixing acid of pH 0.5-3 with three-block copolymer of oxirane(ethylene oxide)-methyloxirane (propylene oxide)-oxirane(ethylene oxide), (b) mixing titanium precursor with tetraethylorthosilicate with silica : titanium mol ratio of 20-400 : 1, (c) mixing the solution (a) with the solution (b), and (d) drying and calcining the solution mixture.
Abstract:
본 발명은 연속식 마이크로파 합성법을 이용한 무기소재의 제조방법 및 그 장치에 관한 것으로서, 더욱 상세하게는 다공성분자체, 층상구조화합물, 세라믹소재 등 각종 무기소재의 합성 전구용액을 만든 후 슬러리 펌프를 통해 튜브형 마이크로파 반응기에 연속적으로 주입하여 합성 및 결정화시킴으로써, 종래 결정화에 장시간이 소요되었던 회분식 수열 합성법과 달리 소요시간이 수분 내지 수십분 이내로 단축되고, 기존의 회분식 수열 또는 마이크로파 합성법에 비해 제조 및 수거 공정이 연속적이므로 비교적 작은 설비로도 대량 생산에 용이할 뿐만 아니라 다공성분자체 합성시 유기 주형물질의 사용을 절감할 수 있는 무기소재의 제조방법 및 그 장치에 관한 것이다.
Abstract:
PURPOSE: Provided is a method for producing an inorganic thin film composed of an inorganic crystal selectively absorbed and nano-assembled to an inorganic adhesive layer with a high bonding force. CONSTITUTION: The method for producing a nano-assembled inorganic thin film comprising a substrate(10,20), an adhesive layer(11,21b) for bonding the substrate to the inorganic film and an inorganic crystal film successively is characterized by comprising the steps of: coating a thin film of a metal oxide or a metal silicate having a dielectric property relatively higher than that of the inorganic film material on the top of the substrate to form the inorganic adhesive layer(11,21b); and dipping the substrate-inorganic adhesive layer composite obtained from the preceding step into a pre-solution or solution(13,23) of the inorganic crystal and irradiating with microwaves to form the nano-assembled inorganic crystal on the top of the inorganic adhesive layer.
Abstract:
본 발명은 공기정화 및 산소발생용 다기능성 분자체의 제조방법에 관한 것으로서, 더욱 상세하게는 알칼리금속 혹은 알칼리 토금속이온을 함유한 제올라이트에 또다른 금속 양이온을 함유시켜 기능성 분자체를 제조함에 있어 금속 양이온 함유방법으로서 종래 수용액 이온교환법을 대신하여 마이크로파 조사법을 적용시켜 단 몇분의 마이크로파 조사로 소성효과까지도 얻을 수 있는 등 공정상의 편리성이 있음은 물론이고 악취 제거 및 항균활성을 가지며 동시에 공기 중의 질소 흡착능이 우수하여 공기 정화장치 및 산소발생장치 등 그 적용범위가 광범위한 다기능성 분자체의 제조방법에 관한 것이다.
Abstract:
PURPOSE: Provided is a catalyst for dehydrogenation of alkylaromatic hydrocarbons, which has improved reaction activity and excellent selectivity to target products in the case that the catalyst is applied to dehydrogenation of alkylaromatic hydrocarbons conducted in the presence of moisture, by adding a specific amount of zirconium to conventional iron oxides in the form of cerium-zirconium complex oxides. CONSTITUTION: In a catalyst comprising iron oxide, potassium oxide, cerium oxide, calcium oxide, molybdenum oxide and magnesium oxide, the present invention is characterized in that the catalyst further contain zirconium oxide in an amount of 0.5 to 10 wt.% and cerium oxide in an amount of 0.5 to 8.0 wt.%, based on the total weight of the catalyst.
Abstract:
PURPOSE: Provided is a titania photocatalyst which has smaller particle diameter than the conventional titania powder and enhanced photo-activity. The photocatalyst is homogeneously dispersed in the zeolite carrier and does not coagulate so that quantum efficiency of the titania powder in the UV region is maximized, making rapid and effective elimination of various harmful gases such as ammonia in the air and sulfur compounds together with organic compounds in the water by the photocatalytic oxidation. CONSTITUTION: The photocatalyst preparation comprises: the first process wherein titanium tetraisopropoxide is dissolved completely in isopropyl alcohol and adding and dissolving each 0.5-2moles of citric acid and 0.5-10 moles of ethylene glycol to 1 mole of titanium tetraisopropoxide ; the second process of adding and mixing with the above mixed solution, zeolite selected from H-type ZSM-5, USY, BEA, KL zeolite containing 20-200moles of silica; and the third process wherein the above titania/zeolite mixture is distilled at 80-100°C under pressure, irradiated with microwave and calcined. The above titania powder carried on the zeolite has the particle diameter of 5-2 nm and its quantum efficiency is 50-80% per unit photocatalyst while its UV-DRS spectrum is in the region of 370-310 nm.
Abstract:
PURPOSE: Provided is a direct preparation method of hydrogen peroxide, which is characterized in that the hydrogen carrier quinone and its derivatives are fixed to the channels of zeolite by anchoring and grafting method and the product is made in aqueous solution. Usual process uses solvent dissolving quinone and hydroquinone and in the above process the quinones are fixed to the zeolite more than 2 times than the usual process, making the method improved in the stability and reactivity of the catalyst. CONSTITUTION: The method includes the steps of: making the catalyst by anchoring or grafting quinone or its derivatives into the zeolite which is ion-exchanged with VIII group transition metals and carries them; and directly synthesizing hydrogen peroxide at 0-90deg.C by introducing reducing agent and oxygen gas. The above anchoring and grafting is conducted by using as anchoring agent tetrahydrofuran and dicyclohexylcarbodiimide and pre-grafting to zeolite with 3-aminopropyltrimethoxysilane and trimethoxysilylpropyldiethylenetriamine. The above zeolite is selected from Y, Beta, L or MCM-41 structure and Si/Al ratio is 1-160. The cationic form of zeolite is selected from Na, K and H while VIII group transition metal is chosen from Rd, Pt, Rh, Ir, Fe, Cu and Ni. The reducing agent is selected from hydrogen, ammonia and alcohol. The catalyst is washed with benzene, alcohol and acetone, and the acid is added to the above aqueous solution, the acid being chosen from 0.001-1N sulfuric acid, acetic acid and hydrochloric acid.
Abstract:
PURPOSE: Nickel-based catalyst for application in oxygen reforming or steam/oxygen mixed reforming process for the production of a synthesis gas consisting of hydrogen and carbon monoxide is provided. As nickel-based catalyst of the present invention has excellent thermal stability and catalytic activity, the production of synthesis gas from natural gas is thus less energy-consumable than conventional methods. CONSTITUTION: The nickel-based catalyst is represented by chemical formula 1, M1-M2-Ni/M3-M4-ZrO2, where M1 denotes an alkali metal, and the mole ratio of M1/nickel is in the range of 0 to 0.2; M2 and M3 denote an alkali earth metal respectively, and the mole ratio of M2/nickel is in the range of 0 to 4 and the mole ratio of M3/nickel is in the range of 0 to 1.0; M4 denotes one atom selected from either IIIB group or lanthanide group, and the mole ratio of M4/Zr is in the range of 0.01 to 1.0 and the weight ratio of nickel/zirconium is in the range of 0.01 to 0.2. The preparation method of synthesis gas from natural gas is characterized in that in the presence of the present nickel-based catalyst, oxygen reforming or steam/oxygen mixed reforming is performed in the temperature range of 600 to 1000°C under the pressure condition of 0.5 to 20 atm. In the present method, the mole ratio of O2/methane is in the range of 0.1 to 1, the mole ratio of H2O/methane is in the range of 0 to 5, and space velocity is in the range of 1,000 to 1,000,000cc/h·g-catalyst.