Abstract:
PURPOSE: Provided is a coolant composition containing difluoromethane, 1,1,1-trifluoroethane, and 1,1,1,2-tetrafluoroethane, which is a substitute for chlorodifluoromethane(CHClF2, HCFC-22) and dose not contain the material destroying an ozone layer. CONSTITUTION: The coolant composition comprises: the difluoromethane(CH2F2, HFC-32); the 1,1,1-trifluoroethane(CH3CF3, HFC-143a); the 1,1,1,2-tetrafluoroethane(CH2FCF3, HFC-134a); a compound selected from the group consisting of 1,1-difluoroethane(CH3CHF2, HFC-152a), 1,1,1,2,3,3,3-heptafluoropropane(CF3CHFCF3, HFC-227ea), 1,1,1,2,3,3-hexafluoropropane(CHF2CHFCF3, HFC-236ea), and butane(C4H10, R-600). The composition of HFC-32, HFC-143a, HFC-134a, and HFC-152a is 20-70wt%, 10-50wt%, 10-50wt%, and 10-40wt%.
Abstract:
PURPOSE: Provided is a method for synthesizing alkylene carbonate using catalysts comprising metal halogen compounds and pyridine ligands. Therefore, the alkylene carbonate can rapidly and cheaply produced in higher yield under conditions of low temperature and low pressure. CONSTITUTION: The alkylene carbonate represented by formula (2) is synthesized by reacting alkylene with carbon dioxide using organic metal compounds as catalysts represented by formula (1) of a(Py)/b(MXm), wherein Py is pyridines represented by formulas (3), (4) or (5), M is a metal selected from Zn, Fe, Mn, Pb and In, X is halogen selected from Cl, Br and I, and m is an integer of 2 or 3; R1 and R2 are individually hydrogen, C1 to C4 alkyl or phenyl; and R3, R4 and R5 are individually hydrogen, C1 to C4 alkyl or phenyl; and x, y and z are individually 0 to 3 and c is an integer of 2 to 4.
Abstract:
PURPOSE: A refrigerant mixture containing difluoromethane, pentafluoroethane, 1,1,1-trifluoroethane is provided to substitute HCFC-22(chlorodifluoromethane, CHClF2) without worry of use restraint as being no risk of ozone layer destruction. CONSTITUTION: The refrigerant mixture comprises difluoromethane(CH2F2, HFC-32) as first component; pentafluoroethane(CHF2CF3, HFC-125) as second component; 1,1,1-trifluoro ethane(CH3CF3, HFC-143a) as third component; one component selected from cyclopropane(C3H6, RC-270), 1,1,1,2,3,3,3-heptafluoropropane(CF3CHFCF3, HFC-227ea), 1,1,1,2,2-pentafluoropropane(CH3CF2CF3, HFC-245cb), isobutane(CH(CH3)2CH3, R-600a), octafluorocyclobutane(C4F8, RC-318), 1,1,1,2,3,3-hexafluoropropane(CHF2CHFCF3, HFC- 236ea), butane(C4H10, R-600), bis(difluoromethyl)ether(CHF2OCHF2, HFE-134), penta fluoroethylmethylether(CF3CF2OCH3, HFE-245).
Abstract:
PURPOSE: A method for preparing alkylene carbonate is provided which can synthesize high yield of alkylene carbonate under unstringent condition by using a catalyst comprising manganese halide compounds and alkaline metal halide. The catalyst system has a high catalytic activity, and is easy to separate from a product because it consists of simple inorganic salts. CONSTITUTION: The alkaline carbonate of formula (1) is prepared by reacting alkylene oxide with carbon dioxide using the catalyst system consisting of one or more alkaline metal halides selected from MX (wherein, M=alkaline metal and X=Cl, Br or I) and one or more manganese halide compounds selected from MnY2 (wherein, Y=Cl, Br or I), wherein R1 and R2 are independently hydrogen or C1-C4 alkyl. The alkaline metal M is Na or K. The conditions are as follows: 90-170deg.C of a reaction temperature and 10-100 atm of an air pressure.
Abstract:
The catalyst for fluorizing 1,1,1-trifluoro-2,2-dichloroethan consisted of a compound selected from a group comprising of magnesium and calcium, one or more metal element selected from a group comprising of zinc, cerium and nickel, and chrome and the preparing method thereof are disclosed. The mole ratio of chrome to magnesium or calcium is 1:1 to 1:32 and the mole ratio of chrome to metal element is at least 1:0.5. Thereby, the active ingredient of the catalyst is more uniformly distributed, thus the activity and the life of the catalyst are remarkably improved.
Abstract:
본원발명은 제1단계 반응에서 1,1,1-트리플루오로-2-클로로에탄과 불화수소와 염소를 반응시켜 HFC-134a와 HFC-125를 함께 제조하고, 제2단계 반응에서 제1단계 반응생성물에 트리클로로에틸렌을 첨가하여 HFC-133a를 제조한 다음, 제2단계 반응생성물에서 HFC-134a와 HFC-125 및 염화수소를 분리하고, 그 나머지 혼합물을 상기 제1단계 반응으로 순환시키는 것으로 이루어지는 HFC-134a와 HFC-125를 동시에 제조하는 방법에 관한 것이다.