Abstract:
PURPOSE: A process for preparing hexafluoropropylene oxide from hexafluoropropylene and sodium hypochlorite is provided, thereby rapidly and selectively preparing the hexafluoropropylene oxide in higher yields. CONSTITUTION: A process for preparing hexafluoropropylene oxide from hexafluoropropylene and sodium hypochlorite comprises the steps of: (1) mixing an organic solvent with a sodium hypochlorite(NaOCl) solution; (2) adding a phase shift catalyst and an oxidation catalyst into the mixture; (3) cooling the mixture to -20 to 0 deg. C, followed by vacuum pumping it to remove air, and dissolving hexafluoropropylene(HFP) in it; (4) reacting the mixture at -20 to 0 deg. C; and (5) slowly increasing temperature of the mixture from -20-0 deg. C to 40-60 deg. C, wherein the phase shift catalyst is halogenide of quaternary ammonium salt(R-tetraammonium-X), in which R is C2-7 of alkyl and X is Cl, Br or I; and the oxidation catalyst is transition metal chloride.
Abstract:
PURPOSE: Provided is a process for preparing 2,2,2-trifluoroethanol with high yield in a short time by adding a specific salt. CONSTITUTION: The process for preparing 2,2,2-trifluoroethanol by the hydrolysis of 1-chloro-2,2,2-trifluoroethane in the presence of base comprises adding to the reactants an imidazolium salt represented by the formula 1, an ammonium salt represented by the formula 2 or a phosphate salt represented by the formula 3. In the formulae 1-3, each of R1 to R4 is independently alkyl group of C1-C8, benzyl group or phenyl group and X is selected from F, Cl, Br and I. In the process, the base is selected from hydroxide salt, carbonate salt and acetate salt of lithium, sodium and potassium, and organic acid salt represented by the formula 4, wherein A is O or NH, n is 3, 4 or 5, and M is Li, Na or K.
Abstract:
PURPOSE: Provided is a process for producing 2,2,2-trifluoroethanol at a low reaction temperature for a short time in a high yield by using an imidazolium-based ionic solvent. CONSTITUTION: The 2,2,2-trifluoroethanol is produced by hydrolyzing 1-chloro-2,2,2-trifluoroethane in the presence of the imidazolium-based ionic solvent represented by the formula 1 and a base such a hydroxide salt of lithium, sodium and potassium, a carbonate, an acetate, and an organic acid salt. In the formula, R1 and R2 are independently C1-C8 alkyl or benzyl and X is PF6, BF4, NO3, NO2, CH3CO2, CF3CO2, or CF3SO3.
Abstract translation:目的:提供使用咪唑鎓系离子溶剂,在低反应温度下短时间高收率地制备2,2,2-三氟乙醇的方法。 构成:2,2,2-三氟乙醇是通过在由式1表示的基于咪唑鎓的离子溶剂存在下水解1-氯-2,2,2-三氟乙烷和碱如锂的氢氧化物盐, 钠和钾,碳酸盐,乙酸盐和有机酸盐。 在该式中,R 1和R 2独立地为C 1 -C 8烷基或苄基,X为PF 6,BF 4,NO 3,NO 2,CH 3 CO 2,CF 3 CO 2或CF 3 SO 3。
Abstract:
PURPOSE: A mixture coolant composition is provided, which can replace chlorodifluoromethane(CHClF2, referred as HCFC-22), does not destroy an ozone layer and is used in a refrigerator and an air conditioner for a car. CONSTITUTION: The mixture coolant composition comprises 50-60 wt% of difluoromethane(HFC-32); 10-30 wt% of 1,1,1,2-tetrafluoroethane(HFC-134a); 10-20 wt% of 1,1,1,2,3,3,3,-heptafluoropropane(HFC-227ea); and 5-15 wt% of isobutane(R-600a). The mixture coolant composition comprises 50-70 wt% of HFC-32; 10-30 wt% of HFC-134a; 10-20 wt% of HFC-227ea; and 5-15 wt% of 1,1,1,2,3,3-hexafluoropropane(HFC-2363a). The mixture coolant composition comprises 50-70 wt% of HFC-32; 10-30 wt% of HFC-134a; 10-20 wt% of HFC-227ea; and 5-12 wt% of butane(R-600). Also the mixture coolant composition comprises 40-70 wt% of HFC-32; 10-40 wt% of 1,1-difluoroethane(HFC-152a); 10-20 wt% of HFC-227ea; and 5-15 wt% of one selected from the group consisting of R-600a. The mixture coolant composition comprises 50-70 wt% of HFC-32; 10-40 wt% of HFC-152a; 10-20 wt% of HFC-227ea; and 5-15 wt% of HFC-2363a. The mixture coolant composition comprises 40-70 wt% of HFC-32; 10-40 wt% of HFC-152a; 10-20 wt% of HFC-227ea; and 5-12 wt% of R-600.
Abstract:
PURPOSE: A method is provided which manufactures 2,2,2-trifluoroethyl difluoromethyl ether simply and in a high yield by reacting CF3CH2OH with CHCl3 and HF under the existence of a catalyst. CONSTITUTION: In a method for manufacturing 2,2,2-trifluoroethyl difluoromethyl ether, the method is characterized in that CF3CH2OH is reacted with CHCl3 and HF under the existence of a catalyst, that is, chlorides, fluorides or oxides of a metal selected from the group consisting of B, Sn, Ti, Al, Zn, and Ce, wherein an amount of the catalyst is 0.005 to 1 mole per one mole of trifluoroethanol, wherein an amount of CHCl3 is 1 to 10 moles per one mole of trifluoroethanol, wherein an amount of HF is 5 to 50 moles per one mole of trifluoroethanol, and wherein a temperature of the reaction is 100 to 200 deg.C.
Abstract:
M 2 CO 3 (M=알칼리금속)의 일반식을 가지는 탄산알칼리의 촉매하에서, 1,1-디플루오로에틸렌과 메탄올을 반응시켜 1,1-디플루오로에틸메틸에테르를 제조하는 방법에 관한 것이다. 본 발명에 따른 신규의 디플루오로메틸에테르의 제조방법은 탄산알칼리 촉매를 사용함으로써, 강염기를 사용한 종래의 제조방법을 개선하여, 장치의 부식을 막고, 부산물의 생성을 감소시키고, 고수율의 산물을 얻을 수 있는 장점이 있다.
Abstract:
PURPOSE: A fluorine manufacturing method is provided to prevent the explosive recombination of the fluorine and the hydrogen and to improve the fluorine manufacture efficiency. CONSTITUTION: The fluorine manufacturing method is formed by the steps of: electrolyzing the anhydrous fluoric acid by using the fused alkali metal fluoric acid compound as an electrolytic solution; and leading the electrolytic solution to naturally convert to a specific direction by installing a few louver-typed horizontal gap only on the upper area of the whole area of a cathode(2) and by using a plate on the lower area.
Abstract:
본 발명은 트리클로로에틸렌과 불화수소를 원료로 사용하여 2단계 반응으로 1,1,1-트리플루오로-2-클로로에탈을 거쳐 1,1,1,2-테트라플루오로에탄을 제조하는 방법에 관한 것이다. 본 발명의 제조방법에서는 2단계 반응을 서로 다른 반응기에서 수행하며 반응기를 병렬로 배열하여 한개 반응기에서 생성된 부산물(HCl)이 다른 반응기로 투입되지 않는 것을 특징으로 한다. 1,1,1-트리플루오로-2-클로로에탄의 제조반응기에서 생성된 반응 생성 혼합물을 증류탑에서 상부 유출물과 하부 유출물로 분리할 때, 공비혼합물 형성을 이용하여 상부 유출물에서 1,1,1-트리플루오로-2-클로로에탄과 불화수소의 몰비 조성이 1 대 1 이상이 되도록 조절하여 이를 1,1,1,2-테트라플루오로에탄 제조반응에 공급되도록 한다. 본 발명에 의해 두개의 반응기에 공급되는 원료의 조성을 각각, 용이하게 조절하는 방법이 제공되며 반응에 영향을 미칠 수 있는 미반응 물질 및 부산물이 다른 반응기에 투입되지 않도록 할 수 있다.
Abstract:
불화칼슘과, 삼산화크롬, 염화아연 및 염화제2철의 수용액을 혼합한 후 에탄올과 반응시켜 얻어지는 생성물을 소성함으로써 제조된 촉매의 존재하에, 1단계 반응으로서, 1,1,1-트리플루오로-2-클로로에탄(HCFC-133a)과 불화수소를 반응시켜 1,1,1,2-테트라플루오로에탄(HFC-134a), 펜타플루오로에탄(HFC-125) 및 1,1,1-트리플루오로에탄(HFC-143a)을 얻고, 2단계 반응으로서 1단계 반응생성물에 트리클로로에틸렌을 첨가하여 HCFC-133a를 제조한 다음 HFC-134a, HFC-125 및 HFC-143a를 분리하고 HCFC-133a를 1단계 반응으로 재순환시키는 것으로 이루어지는 2단계 기상반응에 의해, HFC-134a, HFC-125 및 HFC-143a를 동시에 제조하는 방법이 제공된다.