Abstract:
본 발명은 나노 세공을 갖는 VSB-5 분자체의 제조방법에 관한 것으로서, 더욱 상세하게는 인화합물과 니켈화합물로 구성되는 원료물질에 종래의 필수요소인 주형물질을 배제하고 pH 조절제로서 저가이면서 손쉽게 구할 수 있는 무기염기 또는 모노아민을 선택 혼입하여 결정화하므로써 공정의 단순화가 가능하고 값싸고 효율적인 방법으로 수소저장물질, 촉매, 촉매지지체 및 흡착제 등의 분야에 널리 이용 가능한 나노 세공을 갖는 VSB-5 분자체를 제조하는 방법에 관한 것이다.
Abstract:
PURPOSE: To provide a method for preparing a VSB-5 molecular sieve, which is able to prepare the VSB-5 molecular sieve having good physical properties 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 nickel compound and a phosphorous compound using a base, an inorganic base or a mono-amine is used as the base, and the crystallization is performed under pH of 7.0-12.0 and at the temperature of 50-350 deg.C.
Abstract:
PURPOSE: A method for preparing an aromatic carboxylic acid is provided, to improve the reaction activity remarkably and to suppress the generation of by-product by the liquid oxidation of an alkyl aromatic compound. CONSTITUTION: The method comprises the step of oxidizing an alkyl aromatic compound and its partial oxide intermediate with an oxygen-containing gas in an acetic acid solvent in the presence of a cobalt/manganese/bromine catalyst, a brominated alkyl ammonium and carbon dioxide. Preferably the ratio of the brominated alkyl ammonium and manganese is 0.04-5 by weight. Preferably the brominated alkyl ammonium is at least one selected from the group consisting of tetramethyl ammonium bromide, tetraethyl ammonium bromide, tetrapropyl ammonium bromide and tetrabutyl ammonium bromide; alkyl aromatic compound is selected from the group consisting of toluene, o-xylene, m-xylene, p-xylene, 1,3,4-trimethylbenzene, 1,3,5-trimethylbenzene, 2,3,5,6-tetramethylbenzene, methylnaphthalene, 2,6-dimethylnaphthalene and 4,4'-dimethyl biphenyl; and the aromatic carboxylic acid is selected from the group consisting of benzoic acid, phthalic acid, isophthalic acid, terephthalic acid, trimellitic acid, trimesic acid, pyromellitic acid, carboxynaphthalic acid, 2,6-dicarboxynaphthalic acid and 4,4'-dicarboxyphenylic acid.
Abstract:
PURPOSE: Provided are a selective hydrogenation catalyst and a selective hydrogenation process of diolefin compound using the catalyst. The above catalyst is tetragonal Ni/Zr type and is used in the selective hydrogenation of diolefin compounds that are contained in the carbohydrate mixtures into mono-olefin compounds. CONSTITUTION: The preparation method of the above catalyst comprises: 0.1-5wt.% (based on the hydrate) of Ni alone or having 0.1-5mol.% (based on Zr carrier) of a cocatalyst selected from Pd, Pt, Ag, Cu, Mo and B and its carrier of Zr alone or modified by one metal chosen from Ca, lanthanide metals such as Se and La, IIIB group metal(silicone) or IVB group metal(Al). The above selective hydrogenation is conducted in the temperature range of 80 to 250°C at a pressure of 1 to 12 atm. and at space velocity of 4 to 12/h (based on the volume of liquid reactant).
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: Provided is a hybrid molecular sieve DeNOx catalyst containing highly dispersed noble metals, which show excellent poisoning resistance even in the coexistence of moisture, CO2, and SO2, therefore it is applicable to gas emission purification in gas turbine, boiler, and mobile air pollution sources such as lean burn vehicles. CONSTITUTION: In the manufacture process of DeNOx catalyst by supporting silica or H-beta zeolite with noble metals, the method of preparing a hybrid molecular sieve DeNOx catalyst containing highly dispersed noble metals includes the steps of (i) supporting a composite substrate with 0.1-1.5 wt.% of noble metals including Pt, Rh, and Pd, wherein the weight ratio of protonic or ammonium zeolite and metal oxides is 1:1; (ii) chemically and physically fixing volatile hydrocarbons having a boiling point of 60 to 200°C and hydrocarbons containing hetero atom; and (iii) dispersing noble metals into the composite substrate via carbonization at 250-300°C in oxygen atmosphere and calcination at 450-550°C. The protonic or ammonium zeolite is selected from BEA, MFI, MOR and FAU structured zeolites of which Si/Al ratio is within 10-100. The metal oxides are selected from zirconia, seria, and titania containing 0.2-2.0wt.% of sulfate or persulfate. Volatile hydrocarbons and hydrocarbons are selected from TEAOH, furfuryl alcohol, TPAOH, TBACl, TPA, aqueous sucrose solution, and aqueous glucose solution.
Abstract:
PURPOSE: Provided is a process for producing aromatic carboxylic acid by a liquid phase oxidation of an alkyl aromatic compound, which can maximize yield and prevent explosion. CONSTITUTION: The aromatic carboxylic acid is produced by oxidizing the alkyl aromatic compound and a partially oxidized intermediate thereof by oxygen contained gas in the presence of a cobalt/manganese/bromine catalyst and an acetic acid solvent, wherein metal nickel and carbon dioxide are added to the reaction. The weight ratio of nickel/manganese is 0.01-1 and the oxygen concentration is 2-75%(v/v) based on the total gas and the carbon dioxide concentration is 1-90%(v/v) based on the total gas.
Abstract:
PURPOSE: The modified nickel-alumina catalyst for selective hydrogenation of diolefins of the present invention is manufactured by surface modifying gamma-alumina support with one element selected from zirconium, lanthanum and tin, and then it is further supported by nickel. CONSTITUTION: In a modified nickel-alumina catalyst for selective hydrogenation of diolefins that is manufactured by surface modifying gamma-alumina support with one element selected from zirconium, lanthanum and tin, and then it is further supported by nickel, the present invention is characterized in that gamma-alumina support is supported by one element selected from zirconium, lanthanum and tin in an amount of 0.2 to 10 wt.% and nickel in an amount of 0.5 to 10 wt.%, based on the weight of the gamma-alumina support. Before the modified nickel-alumina catalyst is used to convert diolefins to corresponding mono olefins through selective hydrogenation reaction, the modified nickel-alumina catalyst should undergo reduction stage at 400-500deg.C and pretreatment at 300-450deg.C in H2S gas atmosphere.
Abstract:
PURPOSE: Provided is a multifunctional oxidation catalysts, which can remove chlorinated volatile organic compounds at low temperatures of 20 to 220°C as well as minimize generation of another forms of chlorinated volatile organic compounds after reaction. CONSTITUTION: The present invention is characterized in that sulfated metal oxide support is impregnated with (i) as active species, 0.5-2.0 wt.% of one novel metal selected from Pt, Pd, Ir and Rh; (ii) as subsidiary active species, Cu 2.0-10.0 wt.%, Ni 0.1-1.0 wt.%. The sulfated metal oxide support is selected from zirconia, titania and ceria containing SO4 in an amount of 0.3 to 2.3 wt.%. And a porous molecular sieve material is used as support, together with the sulfated metal oxide support within the range of less than 50%. The porous molecular sieve material, such as protonic zeolite or ammonium zeolite, is selected from BEA, MFI, MOR and FAU zeolite with a Si/Al ratio within the range of 10 to 100.