Abstract:
본 발명은 질소산화물 정화용 촉매 및 이를 이용한 질소산화물의 정화방법에 관한 것으로, 보다 상세하게는 바나듐(V), 인(P) 및 표면에 히드록시기를 보유하고 있는 물질로 이루어진 V X -P Y -(히드록시기 보유물질) Z 담체 95 내지 99.99 중량% 및 백금(Pt) 0.01 내지 5 중량%를 포함하는 질소산화물 정화용 촉매는 200℃ 이하의 낮은 온도에서 95% 이상의 NOx 전환율과 70% 이상의 N 2 로의 전환율로 질소산화물을 환원시킬 수 있기 때문에 촉매의 활성이 높아 자동차 운전 초기 배기가스의 온도가 낮을 때에도 NOx를 정화할 수 있고, 수소를 환원제로 사용하기 때문에 환원제가 대기에 누출되더라도 환경오염 문제가 없을 뿐만 아니라, 수증기와 SOx 분위기에서도 열화되지 않아 디젤자동차에서 배출되는 질소산화물을 정화하는데에 매우 유용하다. 질소산화물 정화용 촉매, 수소 환원, 선택적 환원, 디젤자동차
Abstract:
본 발명은 결정성 멜라민포스페이트의 제조방법에 관한 것으로서, 보다 상세하게는 분말상의 멜라민에 고농도의 인산수용액을 첨가하여 반응용매의 효과가 거의 나타나지 않는 건식법에 의한 멜라민포스페이트 제조반응을 일정수준까지 진행하고, 여기에 저농도의 인산수용액을 첨가하여 반응계를 물 분산상으로 전환하는 습식법에 의하여 멜라민포스페이트 제조반응을 진행함으로써, 결과적으로 수득된 멜라민포스페이트의 입자가 균일하고 미세한 크기를 나타내며, 멜라민과 인산의 반응이 효율적으로 일어나 반응 생성물 중에 잔류하는 미반응 멜라민 또는 인산 성분이 최소화되어, 과량의 물만을 사용하여 반응을 수행할 경우에 발생하는 반응 분산물의 엉킴현상에 의한 반응물 교착화 현상을 극복함으로써 반응 효율성을 개선한 결정성 멜라민 포스페이트의 제조방법에 관한 것이다.
Abstract:
본 발명은 올레핀, 특별히 에틸렌 소량화 촉매 조성물과 소량화 반응 방법에 관한 것으로, 더욱 상세하게는 Cr 화합물, 리간드, 알킬알루미늄로 구성되고, 리간드 성분으로 피리딘 골격의 2,6 위치에 적절한 배위자리를 갖는 원자를 포함하는 작용기가 치환된 3배위 피리딘 골격 리간드를 적용하며 또한 이들 구성 성분의 조합 비율을 조절함으로써, 올레핀, 특별히 에틸렌의 소량화 반응을 통하여 C 4 ∼C 10 범위의 올레핀을 선택적이며 높은 반응활성으로 제조하는 화학반응에 적용되는 새로운 형태의 촉매 조성물과 이의 적용 방법에 관한 것이다.
Abstract:
PURPOSE: A method for preparing gamma-butyrolactone from maleic acid ester is provided, thereby improving the preparation yield and purity of gamma-butyrolactone under mild condition, and stably preparing the gamma-butyrolactone for a long time. CONSTITUTION: The method for preparing gamma-butyrolactone from maleic acid ester comprises hydrogenation of maleic acid ester in the presence of catalyst of formula: CuO(a)MnO2(b)M(c)SiO2(d) at atmospheric pressure to 12 atmosphere and 150 to 280 deg. C, wherein a, b, c and d are percentage of weight; a is 40 to 90: b is 0.15 to 5; c is 0.001 to 5; d is 5 to 50; and M is one or more metal oxides selected from Zn, Pt, Pd, Re, Ru, Rh, Ca and Mg; the catalyst is activated at 100 to 250 deg. C for 1 to 60 hours prior to the hydrogenation; the maleic acid ester is selected from dimethyl maleate, diethyl maleate, dipropyl maleate, diisopropyl maleate and dibutyl maleate.
Abstract:
PURPOSE: A preparation method of silica stabilized copper catalyst used in hydrogenating or dehydrogenating organic compounds is provided, and the catalyst prepared by the method is provided. CONSTITUTION: The preparation method of Cu/SiO2 catalyst comprises the steps of (a) preparing a slurry solution of copper hydroxide by adding a precipitant solution to an aqueous copper salt solution; (b) preparing a copper hydroxide-silica slurry solution by stirring the mixed solution after adding a colloidal silica solution to the slurry solution; (c) separating sediments from the solution and cleaning the sediment after aging the copper hydroxide-silica slurry solution at a temperature of 50 to 100 deg.C; and (d) drying and baking the cleaned sediment, wherein the precipitant is carbonate or hydroxide of alkaline metal, a weight ratio of copper oxide (CuO) to silica (SiO2) of catalyst is 9:1 to 3:7, the colloidal silica is stabilized by ammonium (NH4¬+), Na¬+ or other alkali metal, has a particle size of 4 to 60 nm, surface area of 100 to 300 m¬2/g and concentration of 5 to 60 wt.% on the basis of silica, and the aging is performed at a temperature of 60 to 90 deg.C for 0.5 to 24 hours.
Abstract:
PURPOSE: Provided are catalyst and a method for ethylene oligomerization. The method can produce olefin with high reaction activity and selectivity by using pyridine derivatives as ligand in catalyst comprised of Cr compound, ligand and alkyl aluminum. CONSTITUTION: The catalyst is consisted of Cr compounds, 3-coordinative pyridine structure ligand, and alkyl aluminum, wherein the ligand is expressed as the formula 1, where R is hydrogen or C1-C6 alkyl group, -X1 and -X2 are =N and -P, respectively, wherein if the X1 or X2 is N(nitrogen), n is 1 whereas if X1 or X2 is P, n is 2, and wherein Ph is phenyl group or replaced phenyl group, and if the Ph is replaced phenyl group, the substituent is selected from a group being consisted of C1-C6 alkyl group and C1-C6 alkoxy group.
Abstract:
PURPOSE: A hydrogenation catalyst which is capable of producing 1,3-propanediol at a high yield and has extended life time and industrial values is provided, and an optimized method for hydrogenating 3-hydroxy alkylpropane using the catalyst is provided. CONSTITUTION: The hydrogenation catalyst is characterized in that it is prepared by adding nano size colloidal silica to the produced particles and aging the nano size colloidal silica added particles after primarily producing particles in a mixed hydroxide form by adding an alkaline precipitant to an aqueous solution containing copper salt, manganese salt and zinc salt and represented as CuO(A)MnO2(B)ZnO(C)SiO2(D), where A is 40 to 85 wt.%, B is 0.15 to 4 wt.%, C is 0.001 to 2.5 wt.%, D is 10 to 60 wt.%, and the total sum of B and C is 5 wt.% or less. The method for preparing 1,3-propanediol comprises a step of activating the hydrogenation catalyst by reducing the hydrogenation catalyst in a stationary phase reactor using hydrogen gas or hydrogen contained gas; and a step of gas phase hydrogenating 3-hydroxy alkylpropane using hydrogen gas or hydrogen contained gas in the presence of the activated catalyst.
Abstract:
PURPOSE: Provided are a composite metal oxide catalyst for vapour phase hydrogenation, a preparation method thereof and a method for preparing phthalide from ester phthalate using the composite metal oxide catalyst, wherein the catalyst exhibits high selectivity, productivity and extended catalytic activity in the process of preparing phthalide from ester phthalate by vapour phase hydrogenation even under the mild conditions of low temperature at 130 to 220 deg.C, low pressure of 1 to 10 atm and low hydrogen/ester phthalate ratio ranging from 500 to 3,000. CONSTITUTION: The catalyst is represented as follows: £CuO(a)ZnO(b)MnO2(c)SiO2(d)|(100-x)M(x), where M is at least one oxide selected from the group consisting of Re oxides, Ru oxides and Ag oxides, a is 20 to 90, b is 0.01 to 10, c is 0.01 to 5, d is 5 to 65 and x is 0.001 to 5, wherein a, b, c, d and x are expressed on the basis of weight. The preparation method of the catalyst comprises the steps of preparing a mixed solution containing copper salt, zinc salt and manganese salt; adding an alkali solution to the mixed solution to coprecipitate copper, zinc and manganese in the form of hydrogel, wherein the temperature of the mixed solution is in the range of 1 to 30 deg.C and pH is kept in the range of 6 to 9; adding nano size colloidal silica to the hydrogel, thereby obtaining a mixed slurry, wherein the colloidal silica is stabilized by NH4¬+, Na¬+ and other alkali metal, and particle size and specific surface area thereof are 4 to 60 nm and 100 to 300 m¬2/g, respectively; hydrothermal aging the mixed slurry at 50 to 100 deg.C for more than 0.5 hr; filtering the mixed slurry after hydrothermal aging to separate cake, followed by washing the cake, wherein the washing is conducted until residual concentration of alkali metal is less than 1000 ppm; and drying and tableting the washed cake.
Abstract:
PURPOSE: A method for preparing copper/silica catalyst used in hydrogenation and dehydrogenation of organic compounds using acidic waste solution containing copper is provided. CONSTITUTION: The method for preparing copper/silica catalyst comprises a step (a) of preparing an aqueous copper solution by adding copper compound and arbitrary zinc compound to an acidic waste solution containing copper; a step (b) of preparing a copper slurry solution by adding a precipitant solution to the aqueous copper solution; a step (c) of preparing copper/silica slurry solution by adding colloidal silica solution to the copper slurry solution and stirring the colloidal silica solution and copper slurry solution; a step (d) of separating sediment and rinsing the separated sediment after aging the copper/silica slurry solution at a temperature of 50 to 100 deg.C; and a step (e) of drying and firing the rinsed sediment, wherein the precipitant is ammonia, or bicarbonate, carbonate or hydroxide of alkali metal, wherein the colloidal silica solution is added to the copper slurry solution in such a way that a weight ratio (CuO/SiO2) of copper oxide to silica in produced catalyst is in the range of 0.3-9.0/1, wherein zinc compound is used, and the colloidal silica solution is added to the copper slurry solution in such a way that a weight ratio (CuO/ZnO/SiO2) of copper oxide to zinc oxide to silica in produced catalyst is in the range of 0.3-9.0/0.01-3.0/1, wherein colloidal silica is stabilized by ammonium (NH4¬+) or Na¬+ or other alkali metal and has particle size of 4 to 60 nm, surface area of 100 to 300 m¬2/g and concentration of 5 to 60 wt.% based on silica, and wherein the aging is performed at a temperature of 50 to 100 deg.C for 0.5 to 24 hours.