Abstract:
PURPOSE: Provided are a catalyst for vapour phase hydrogenation, a preparation method thereof and a method for preparing gamma-butyrolactone (GBL) from maleic anhydride (MAn) using the catalyst, wherein the catalyst exhibits high selectivity, productivity and extended catalytic activity in the process of preparing gamma-butyrolactone (GBL) from maleic anhydride (MAn) by vapour phase hydrogenation even under the mild conditions of low temperature, low pressure and low hydrogen/maleic anhydride ratio. CONSTITUTION: The catalyst is represented as follows: CuO(a)ZnO(b)MnO2(c)SiO2(d), where a is 20 to 90, b is 0.01 to 10, c is 0.01 to 5 and d is 5 to 50, wherein a, b, c and d 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: Provided is a method for producing 1,3-alkanediol from 3-hydroxyester compound, which can increase the selectivity of 1,3-alkanediol by 90% or more, and improve the stability of catalyst. CONSTITUTION: The method comprises the steps of (i) adding an alkaline precipitating agent to aqueous copper solution to form a particle, adding a colloidal silica to the solution and aging the solution to form a catalyst, (ii) activating the formed catalyst by reducing the catalyst in the presence of activating solvent at 100-250 deg.C by using hydrogen gas or mixed hydrogen/nitrogen gas having pressure of 5-2000 psig and activating the, and (iii) hydrogenating 3-hydroxyester compound at 100-250 deg.C by using hydrogen gas or mixed hydrogen/nitrogen gas in the presence of the activated catalyst and reaction solvent by an liquid slurry method .
Abstract:
PURPOSE: Provided is a method for separating a liquid alkoxylation product efficiently from an alkoxylation product containing a gel type by-product, which can increase filtering velocity and maximize the yield of the alkoxylation product. CONSTITUTION: The method is performed by adding 10-100vol%(based on an alkoxylation mixture) of a C1-C4 alcohol having a boiling point of 50-100deg.C to the alkoxylation mixture comprising the alkoxylation product produced by alkoxylation of an aliphatic alcohol or an aliphatic acid ester in the presence of a solid catalyst, the gel type by-product, and a catalyst residue to disperse uniformly and filtering the dispersed solution and then distilling and removing the alcohol from the filtrate.
Abstract:
본 발명은 표면 활성금속 농도가 제어된 혼합금속 산화물 촉매 및 이의 제조방법에 관한 것으로, 더욱 상세하게는 다음 화학식 1로 표시되는 하이드로탈사이트 형태의 혼합금속 수산화물의 표면에 3가금속(M(Ⅲ)) 이온을 흡착시킨 후, 분리하고, 일정 온도범위에서 열처리하므로써 촉매 표면의 활성금속 성분의 농도가 증가되고 또 활성금속이온이 촉매 표면에 균일하게 분포되어 있어 알콕시 부가반응에 촉매로 적용되어서는 알콕시 부가수 분포를 좁은 범위로 제어하고 기존의 촉매와 비교하여 반응속도를 크게 증가시킬 수 있으므로 최소량의 촉매 사용으로도 반응기내에서 균일성 확보가 가능하고, 촉매잔유물과 반응생성물의 젤(gel)형 복합체 생성을 크게 감소시켜 반응후 처리단계에서 생산성을 향상시키는 등의 우수성을 가지게 되는 표면 활성금 속 농도가 제어된 혼합금속 산화물 촉매와 이의 제조방법에 관한 것이다.
Abstract:
PURPOSE: A method for preparing a crystalline melamine cyanurate composite is provided, to control the shape and size of particles by controlling the content of water-insoluble metal oxides and water-soluble hydroxides and the reaction conditions. CONSTITUTION: The method comprises the step of reacting melamine and cyanuric acid with a water-insoluble metal hydroxide or metal oxide and a water-soluble hydroxide. Preferably the reaction is carried out at a temperature of 80-100 deg.C for 0.5-2 hours. The water-insoluble metal hydroxide is selected from the group consisting of Mg(OH)2, Al(OH)3, Ca(OH)2 and magnesium/aluminum composite hydroxide; the water-insoluble metal oxide is selected from the group consisting of MgO, Al2O3, CaO and magnesium/aluminum composite oxide; and the water-soluble hydroxide is selected from the group consisting of NH4OH, LiOH, NaOH and KOH. Preferably the particle size of the water-insoluble metal hydroxide or metal oxide is 0.5-10 micrometers. The content of the water-insoluble metal hydroxide or metal oxide is 0.1-5.0 wt% based on the weight of solid reactant; and the content of water-soluble hydroxide is less than 20 wt% based on the weight of the water-insoluble metal hydroxide or metal oxide.
Abstract:
고분자 물질 등에 첨가하기 위하여 적절한 입자크기를 갖고 얇은 판상을 이루며 표면적이 상대적으로 큰 범위에서 미세 특성제어가 용이한 결정성 층상 혼합금속 수산화물을 빠른 속도로 제조하는 방법이 개시되어 있다. 본 발명에 따르면, 결정성 M (II) (OH) 2 (M (II) 는 +2 산화상태를 갖는 금속원소)와 결정성 M (III) (OH) 3 (M (III) 는 +3 산화상태를 갖는 금속원소) 화합물의 물 분산물에, 이들 M (II) 및 M (III) 금속원소를 포함하는 수용성 화합물류와 층간 음이온 성분을 포함하는 화합물을 첨가하고, 혼합물 용액의 pH를 조절하여 수용성 금속 성분을 점성을 띠는 젤 형태의 혼합금속 수산화물로 변환시키고, 상기 결정성 M (II) (OH) 2 , M (III) (OH) 3 와 수용성 금속 성분으로 부터 변형된 점성을 띠는 젤 형태의 금속수산화물을 포함하는 반응 혼합물로부터, 수열 반응과정을 거쳐, 결정성 층상 혼합금속 수산화물을 제조한다. 반응에 첨가되는 수용성 화합물류의 종류, 금속수산화물에 대한 수용성 금속화합물의 첨가 비율 및 방법, 층간 음이온 성분의 종류, 반응온도, 반응시간의 적절한 선택으로 생성물인 층상 혼합금속 수산화물의 입자크기를 0.2∼2μ범위, 입자형상을 규칙적인 육각 판상으로부터 불규칙적인 모양의 판상, 비표면적의 크기를 20∼90m 2 /g 범위, 두께대 직경비를 10∼50 범위에서 유연하게 제어한다.