Abstract:
Provided are a precious metal-supported catalyst comprising: 100 parts by weight of carbon carrier which has uniform pore structure; 1-20 parts by weight of transition metal supported on the carbon carrier; and 1-10 parts by weight of precious metal supported on the carbon carrier, having a specific surface area of greater than or equal to 450 m^2/g, and preparing a mixture of 1,4-butanediol and dimethylsuccinate from a solution including succinic acid, and a method for preparing the precious metal-supported catalyst. Also, provided is a novel catalyst reaction process which can effectively prepare 1,4-butandiol from succinic acid using the precious metal-supported catalyst.
Abstract:
PURPOSE: A three-kind-complex-metallic-oxide catalyst for manufacturing dimethyl carbonate, a manufacturing method thereof, and a manufacturing method of dimethyl carbonate using the same are provided to be manufacture dimethyl carbonate with high yield in a milder reaction condition when being used as a catalyst for the synthesis of dimethyl carbonate from urea and methanol. CONSTITUTION: A three-kind-complex-metallic-oxide catalyst for manufacturing dimethyl carbonate comprises a first metal oxide, a second metal oxide, and a third metal oxide. The first metal oxide is a zinc oxide. The second metal oxide is a cerium oxide. The third metal oxide is selected from a gallium oxide, zirconium oxide, cobalt oxide, yttrium oxide, and lanthanum oxide. [Reference numerals] (AA) Condenser; (BB) Adverse pressure controller; (CC) Repeater; (DD) Carbon dioxide
Abstract:
PURPOSE: A ruthenium catalyst supported on porous carbon support synthesized by a surfactant-templating method, a method for preparing the same, and a method for producing gamma-butyrolactone using the catalyst are provided to activate the hydrogenation of succinic acid. CONSTITUTION: A method for preparing a ruthenium catalyst supported on porous carbon support includes the following: a carbon precursor and a surfactant are dissolved in an acid solution, and a silica precursor is added into the dissolved solution to obtain a carbon/surfactant/silica complex; the complex is dried and aged at a temperature between 80 and 120 deg C under an air condition to obtain partially carbonated carbon/surfactant/silica complex; the partially carbonized complex is treated with a sulfuric acid aqueous solution; the treated complex is washed, filtered, and carbonated at a temperature between 800 and 1000 deg C; silica template components are eliminated from the carbonated complex based on hydrofluoric acid to obtain a porous carbon support; and a ruthenium precursor is impregnated in the porous carbon support. [Reference numerals] (AA,BB,CC) Sucrose; (DD) Hydrothermal synthesis; (EE) Silica precursor; (FF,HH) Heat; (GG) Surfactant silica precursor; (II) Carbon slurry; (JJ) Carbon/silica slurry; (KK) Carbon/silica/surfactant slurry; (LL,MM,OO) Carbonization; (NN,PP) Hydrofluoric acid treatment; (QQ) Carbon support manufactured by a hydrothermal method; (RR) Carbon support manufactured by a templating method; (SS) Carbon support manufactured by a surfactant-templating method
Abstract:
본 발명은 양이온 치환된 헤테로폴리산 촉매를 이용한 리그닌 화합물 분해방법에 관한 것으로, 보다 상세하게는 리그닌 화합물을 분해하여 방향족 화합물을 생산하는 리그닌 화합물 분해방법에 있어서, 화학식 N y M x H 3.0-ny-x PW 12 O 40 (상기 화학식 중 N은 팔라듐 이온, 로디움 이온, 백금 이온, 망간 이온, 수은 이온, 철 이온, 코발트 이온 및 구리 이온으로 구성된 군으로부터 선택된 1종 이상이고, M은 알칼리금속 이온 또는 암모늄 이온이며, 0≤y≤0.2이고 1≤x≤3이며, n은 N의 전하수)으로 표현되는 양이온 치환된 헤테로폴리산을 촉매 존재하에 분해반응이 수행되는 것을 특징으로 하는 양이온 치환된 헤테로폴리산 촉매를 이용한 리그닌 화합물 분해방법 본 발명에 제시된 공정은 기존의 리그닌 분해에 사용된 열분해 방법과 수첨 분해 방법보다 저온 (120~280 o C)과 저압 (10 기압)에서 반응이 이루어지며, 리그닌 분해 효율이 70%이상 보이는 고효율 에너지 절약형 리그닌 분해 공정이다.
Abstract:
PURPOSE: A palladium catalyst supported on an alumina xerogel support with controlled acidity and a method for preparing γ-butyrolactone based on the hydrogenation of succinic acid using the catalyst are provided to thermo-chemically stabilize a catalytic process by optimally combining the acid characteristic of the support and the hydrogenation activity of palladium. CONSTITUTION: A palladium catalyst supported on an alumina xerogel support with controlled acidity is obtained by gelating an aluminum precursor based on a sol-gel method and implementing a thermal treatment. The average pore size of the palladium catalyst is between 2 and 10nm. The surface area of the palladium catalyst is between 100 and 300m^2/g. The temperature of the thermal treatment is between 700 and 900 degrees Celsius. 1-10 parts by weight of the palladium catalyst is supported by 100 parts by weight of the alumina xerogel support.
Abstract:
PURPOSE: A heteropoly acid support catalyst fixed on a porous spherical carbon containing nitrogen is provided to enhance support amount of the heteropoly acid. CONSTITUTION: A heteropoly acid support catalyst fixed on a porous spherical carbon containing nitrogen is prepared by synthesizing, thermal treating and reducing a carbon precursor containing a nitrogen ingredient with a spherical resin. The catalyst is fixed by reacting a porous spherical carbon with heteropoly acid in a weight ratio of 1 : 0.01-2 in an ion form of amine group and heteropoly acid. The carbon precursor is selected from melamine-formaldehyde resin, polypyrrole, polyanyline and polythiophene.
Abstract:
PURPOSE: A nickel catalyst dipped in a porous zirconia carrier including a metal oxide stabilizer, a producing method thereof, and a hydrogen producing method using thereof are provided to secure the excellent surface area, stability, and the stable catalyst activation of the catalyst. CONSTITUTION: A nickel catalyst dipped in a porous zirconia carrier including a metal oxide stabilizer contains 0.01~0.5mol of metal oxide precursor selected from the group consisting of magnesium, calcium, strontium, barium, scandium, and lanthanum, and 1mol of zirconium precursor. The nickel catalyst uses a surfactant as a template. The nickel catalyst is produced by a hydrothermal polymerization method.