Abstract:
PURPOSE: Disclosed are a porous catalyst composed of pillard silica and metal oxide and a preparation method of ε-caprolactam from cyclohexanone oxime. CONSTITUTION: The porous catalyst is mainly composed of a pillard silica and a metal oxide. The sodium ion (Na+) on pillard silica is substituted with hydrogen ion (H+) of inorganic acid solution and a spacing width of pillard silica expands to 20 - 30 Å by using a long chained amine compound. And then metal oxide compounds are added in the spacing interval of the pillared silica. The added content of metal oxide is optimally 2 - 10 wt% and the surface area is 100 - 300 m2/g. The pillared silica is precipitated from kanemite, kenyaite, magadite, illite, octosilicate and Ta2O5, Nb2O5, TiO2 or SiO2 are used as metal oxides.
Abstract translation:目的:公开了由二氧化硅和金属氧化物组成的多孔催化剂和由环己酮肟制备的ε-己内酰胺的制备方法。 构成:多孔催化剂主要由二氧化硅和金属氧化物组成。 使用长链胺化合物,将二氧化硅上的钠离子(Na +)用无机酸溶液的氢离子(H +)代替,并将二氧化硅的间隔宽度扩大至20〜30。 然后在柱状二氧化硅的间隔间隔中加入金属氧化物。 金属氧化物的添加量最好为2〜10重量%,表面积为100〜300m2 / g。 柱状二氧化硅从可卡因,肯尼亚,magadite,伊利石,八硅酸盐和Ta 2 O 5,Nb 2 O 5,TiO 2或SiO 2中析出用作金属氧化物。
Abstract:
PURPOSE: Provided are a process for preparing a zeolite catalyst and a process for preparing ε-caprolactam from cyclohexanone oxime in the presence of the zeolite catalyst by Beckmann conversion reaction. CONSTITUTION: The MFI and MEL type zeolite catalysts having a molar ratio of Si/Al being more than 500 is treated at 20-150 °C with 0.01-0.5 N by concentration of an acid selected from the group consisting of hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, and acetic acid. The ε-caprolactam is prepared from cyclohexanone oxime by Beckman conversion reaction at 250-400 °C in the presence of the acid treated zeolite catalyst.
Abstract:
PURPOSE: Provided are a metal ion impregnated porous catalyst and a method for preparing thereof, which is able to increase the yield of a conversion rate of cyclohexanone oxime and ε-caprolactam and provides safe, economical, environmental-friendly and life span extended metal ion, and a method for preparing ε-caprolactam from cyclohexanone oxime using the catalyst. CONSTITUTION: The metal ion impregnated porous catalyst has pores formed by metal oxide pillar introduced between layers of layered silica compound, wherein the metal ion is impregnated in pores. The method comprises steps of (a) synthesizing a layered silica compound; (b) acid-ion exchanging the synthesized layered silica compound by acid titration; (c) forming pores between layers of layered silica compound by adding organic metal to the acid-ion exchanged layered silica compound and sintering; and (d) supporting the surface of the pores in metal ion by adding an aqueous solution of the metal ion thereto and sintering. The ε-caprolactam is prepared by gaseous beckmann conversion of cyclohexanone oxime solution using the metal ion impregnated porous catalyst.
Abstract:
PURPOSE: A preparation method of gallosilicate molecular sieve with a gismondine structure in K2O-Ga2O3-SiO2-H2O system is provided to control the molar ratio of structure components freely by substituting Ga and K for Al and Na of zeolite, respectively. The gallosilicate molecular sieve is applicable to catalysts, adsorbents and ion exchangers. CONSTITUTION: The gallosilicate molecular sieve is prepared by the following steps: mixing H2O, KOH, and a source of Ga such as gallium oxide or Ga2O3xH2O for 2-4hrs.; heating it for 12-24hrs. and cooling to room temperature; adding a source of Si such as colloid silica, sodium silicate and fumed silica, and stirring for 4-24hrs., resulting in a gel represented as vK2O : 1.0Ga2O3 : wSiO2 : zH2O (v=6.0-8.0, w=5.0-15.0, z=50-250); heating at 80-130deg.C for 1-10days; washing with H2O and drying.
Abstract:
본 발명은 알루미늄 및 인을 포함하는 분자체를 사용한 질소 산화물의 선택적 제거 방법에 관한 것이다. 본 발명에 따라 고온 조건이 아닌 상온에서 환원제 또는 금속을 담지시킨 촉매를 사용하지 않고도 여러 농도의 질소 산화물을 장시간에 걸쳐 제거할 수 있다.