Abstract:
The present invention relates to a method for preparing 1,3-butadiene and methyl ethyl ketone form 2,3-butanediol. A method for preparing 1,3-butadiene and methyl ethyl ketone form 2,3-butanediol according to the present invention uses a catalyst which is Ca_5(VO_4)_x(PO4)_(3-x)(OH); or Ca_5(NbO_4)_x(PO_4)_(3-x)(OH), wherein the mole ratio of the x is 0.01-0.3, thereby improving a conversion ratio of 2,3-butanediol and selectivity of 1,3-butadiene and methyl ethyl ketone, and maintaining high activity for the long term because of excellent response stability of the catalyst.
Abstract:
The present invention relates to a method for preparing sulfonized phenylsiloxane solid-acid catalyst, sulfonized phenylsiloxane solid-acid catalyst prepared thereby and a method for preparing 5-hydroxymethylfurfural from fructose using the same. 5-hydroxymethylfurfural (5-HMF) can be selectively prepared by applying a catalyst prepared via various methods for preparing sulfonized phenylsiloxane solid-acid catalyst to the dehydration reaction of fructose. The sulfonized phenylsiloxane solid-acid catalyst prepared via an optimized synthesis method has very excellent catalytic activities and stability, and can provide an efficient method for preparing the 5-hydroxymethylfurfural (5-HMF) because the sulfonized phenylsiloxane solid-acid catalyst can be separated and reused after reaction and provides excellent activities and stability in a continuous reaction process. [Reference numerals] (AA) Fructose conversion rate; (BB) HMF selectivity; (CC) Number of reusing
Abstract:
PURPOSE: An ethylene diamine derivative manufactures an amino acid with optical activity through a simple process without using a protection group with high yield. CONSTITUTION: An ethylene diamine derivative is represented by chemical formula 1. In chemical formula 1, R1 is hydrogen, R2 is hydrogen or an amino group-protecting group; or R1 and R2 can form a 5-6 membered heterocycle together with a nitrogen atom coupled with the R1 and R2; R3 is hydrogen; a substituted or unsubstituted C1-C4 linear or branched alkyl.; or R2 and R3 can form a 5-6 membered heterocycle including a nitrogen element by forming a ring together; and Ar is a substituted or unsubstituted C5-6 aryl or C8-13 bicycle aryl.
Abstract:
본 발명은 젖산 에스테르를 탈수하여 아크릴산과 아크릴산 에스테르를 제조하는 방법에 관한 것으로, 인산칼슘염 촉매의 존재 하에 탄소수가 1~4인 알킬기를 가진 젖산 에스테르를 탈수 반응시켜 아크릴산과 아크릴산 에스테르를 제조하는 본 발명에 따른 방법은 아크릴산과 아크릴산 에스테르를 고수율로 제조할 수 있다 : 상기 인산칼슘염 촉매는 아파타이트(Apatite, Ca 5 (PO 4 ) 3 (OH)) 및 이인산이나트륨칼슘(Disodium Calcium Diphosphate, Na 2 Ca(P 2 O 7 ))의 중량혼합비가 20:80 내지 95:5인 것을 특징으로 한다.
Abstract:
PURPOSE: A manufacturing method of 1,3-butadiene is provided to obtain 1,3-butadiene with high selectivity through a dehydration of 2,3-butandiol, and to able to manufacture 1,3-butadiene at low temperature with long term stability. CONSTITUTION: A manufacturing method of 1,3-butadiene comprises a step of manufacturing 1,3-butadiene from 2,3-butanediol under the presence of a hydroxyapatite-alumina catalyst. The catalyst contains 5-40 weight% of alumina and 60-95 weight% of hydroxyapatite. The 1,3-butadiene is manufactured through a dehydration of the 2,3-butandiols. The dehydration is conducted under conditions of a reaction temperature of 320-430 °C, a reaction pressure of 1-6 atm, and a liquid hour space velocity of 0.3-1.5 h^(-1).
Abstract:
PURPOSE: A manufacturing method of 1,3-butadiene and 2-butanone is provided to have excellent conversion rate and yield, maintaining extremely high catalytic activity, and to able to long term stably manufacture 1,3-butadiene and 2-butanol. CONSTITUTION: A manufacturing method of 1,3-butadiene and 2-butanone comprises a step of manufacture 1,3-butadine from 2,3-butandiol under the presence of a catalyst selected from hydroxyapatite, calcium pyrophosphate, or a mixture thereof. The dehydration of the 2,3-butanediol is conducted under a condition of 2,3-butane diol liquid hour space velocity(LHSV), 340-450 °C, and 1-6 atm. The catalyst is a functional catalyst manufacturing 1,3-butadiene and 2-butanone from 2,3-butandiol.
Abstract:
PURPOSE: A method for preparing acrylic acid and acrylic ester based on lactic ester is provided to implement preparing processes by continuously dehydrating the lactic ester under a calcium phosphate catalyst. CONSTITUTION: Calcium phosphate slurry is generated by mixing apatite cake and sodium diphosphate cake with deionized water. The apatide cake is obtained by mixing and filtering a first phosphate dissolved aqueous solution and a first calcium salt dissolved aqueous solution. The sodium diphosphate cake is obtained by mixing and filtering a second phosphate dissolved aqueous solution and a second calcium salt dissolved aqueous solution. The calcium phosphate slurry is filtered, washed, dried to form calcium phosphate cake. The calcium phosphate cake is dried and ground to form powder. The powder is pelletized. The pelletized product is plasticized in the air at a temperature between 300 and 700 degrees Celsius.
Abstract:
PURPOSE: A method for manufacturing long chain aliphatic tertiary amine using a liquid catalyst is provided to improve the yield of the amine under a simplified refining condition without a catalyst filtering process. CONSTITUTION: A liquid homogenous mixed metal colloid catalyst for manufacturing long chain aliphatic tertiary amine is represented by chemical formula 1. In the chemical formula 1, the a, the b, and the c are the content of the catalyst with respect to the weight of total metal elements. The M is lanthanum-based elements and is selected from a group including lanthanum(La), cerium(Ce), and samarium(Sm). A method for manufacturing aliphatic tertiary amine reacts C8 to C36 long chain aliphatic alcohol with dimethyl amine under the catalyst.