Abstract:
PURPOSE: Provided is a method for producing nitrogen trifluoride NF3 at low temperature with high yields by effectively making ammonium bifluoride molten salt come into contact with fluoride. CONSTITUTION: The method comprises the steps of forming fine liquid droplets of ammonium bifluoride molten salt by spraying ammonium bifluoride molten salt in a reactor(10) from a lower part to an upper part thereof through nozzles, and making the ammonium bifluoride molten salt droplets come into contact with fluoride gas being introduced into the reactor(10) by a fluoride suction pipe(32), wherein the fluoride gas supply into the reactor is intermittently stopped and ammonia gas is introduced into the reactor(10) at that time to regenerate ammonium bifluoride in the reactor to keep concentration of ammonium bifluoride molten salt in the reactor(10) to a certain degree.
Abstract:
PURPOSE: Provided is a mixed coolant composition having new composition, which can show similar ability to that of the existing HCFC-22, and does not have the danger such as destruction of the ozone layer. CONSTITUTION: The mixed coolant composition for low temperature freezers, containing a mixture of fluorinated hydrocarbons, comprises a mixture containing 40-70 wt% of difluoromethane(HFC-32), 10-40 wt% of 1,1-difluoroethane(HFC-152a), and 10-20 wt% of 1,1,1,2,3,3,3-heptafluoropropane(HFC-227ea); and 5-15 wt% of isobutane(R-600a). Also, the mixed coolant composition comprises a mixture containing 50-70 wt% of difluoromethane(HFC-32), 10-30 wt% of 1,1-difluoroethane(HFC-152a), and 10-20 wt% of 1,1,1,2,3,3,3-heptafluoropropane(HFC-227ea); and 5-15 wt% of 1,1,1,2,3,3-hexafluoropropane(HFC-236ea).
Abstract:
The present invention relates to a method to prepare alkylene carbonate of the formula (1)wherein, R1 and R2 are each independently H; C1-C4 alkyl or phenyl group;which method characterized by reacting alkylene oxide with carbon dioxide in the presence of a catalyst system comprising a) metal halide [MXm] and b) pyridine or pyridine derivative [Py], wherein Py is selected from a group of pyridines; M is a metal atom selected from the group consisting of Zn, Fe, Mn, Pb and In; X is a halogen selected from the group consisting of Cl, Br and I; and m is 2 or 3.
Abstract:
PURPOSE: A refrigerant composition is provided which shows the similar performance to HCFC-22 that is currently used by additionally mixing one constituent from RC-270, HFC-227ea, HFC-245cb, HFC-236ea, R-600, HFE-134 or HFE-245 to a mixture of HFC-32 and HFC-143a. CONSTITUTION: In a composition of a refrigerant mixture which can be used instead of HCFC-22, the refrigerant mixture comprises 20 to 70 wt.% of difluoromethane (CH3F2, HFC-32) as a first constituent, 10 to 70 wt.% of 1,1,1-trifluoroethane (CH3CF3, CFC-143a) as a second constituent, and 45 wt.% or less of cyclopropane (C3H6, RC-270) or butane (C4H10, R-600) as a third constituent, wherein each of the HFC-32, HFC-143a and RC-270 comprise 20 to 40 wt.%, 30 to 70 wt.% and 30 wt.% or less respectively, and wherein each of the HFC-32, HFC-143a and R-600 comprise 30 to 50 wt.%, 38 to 70 wt.% and 12 wt.% or less respectively.
Abstract translation:目的:提供了一种制冷剂组合物,其显示了与通过额外混合来自RC-270,HFC-227ea,HFC-245cb,HFC-236ea,R-600,HFE-134的一种成分或目前使用的HCFC-22类似的性能 HFE-245与HFC-32和HFC-143a的混合物。 构成:在可用于代替HCFC-22的制冷剂混合物的组合物中,制冷剂混合物包含20至70重量%的作为第一组分的二氟甲烷(CH 3 F 2,HFC-32),10至70重量% 作为第二成分的1,1,1-三氟乙烷(CH 3 CF 3,CFC-143a)和作为第三成分的环丙烷(C 3 H 6,RC-270)或丁烷(C 4 H 10,R-600)45重量% HFC-32,HFC-143a和RC-270中的每一个分别包含20至40重量%,30至70重量%和30重量%或更少,并且其中每个HFC-32,HFC-143a和 R-600分别包含30至50重量%,38至70重量%和12重量%或更少。
Abstract:
PURPOSE: A refrigerant mixture added one component of RC-270, HFC-227ea, HFC-245cb, HFC-236ea, R-600, HFE-134, and HFE-245 to a mixture of HFC-32 and HFC-143a additionally is provided which exhibits performance similar to HCFC-22. CONSTITUTION: A refrigerant mixture free from ozonosphere destruction danger, which can be used as a substitute for chlorodifluoromethane(CHClF2) comprises difluoromethane(CH3F2, HFC-32) as a first component, 1,1,1-trifluoroethane(CH3CF3, HFC-143a) as a second component and one component selected from the group of 1,1,1,2,3,3,3-heptafluoropropane(CF3CHFCF3, HFC-227ea), 1,1,1,2,3,3-hexafluoropropane(CHF2CHFCF3, HFC-235ea), butane(C4H10, R-600), bis(difluoromethyl)ether(CHF2OCHF2, HFE-134), and pentafluoroethylmethylether(CF3CF2OCH3, HFC-245) as a third component. The composition of HFC-32, HFC-143a and RC-270 is 20 to 40% by weight, 30 to 70% by weight and 0 to 30% by weight respectively.
Abstract:
PURPOSE: A cyclic hydrogenation method of aromatic diamine is provided for reducing reaction time and decreasing amount of by-product to raise yield of product by preliminarily surface treating ruthenium catalyst with oxygen or air without using basic materials. CONSTITUTION: The method for producing cyclo-aromatic diamine is to cyclically hydrogenate aromatic diamine at 50-250 deg.C and 300-4000 psig of pressure under 0.1-5 wt.% ruthenium catalyst surface-treated with air or oxygen at 50-200 deg.C. and in the presence of organic solvent. The ruthenium catalyst is prepared by immersing the catalyst into a carrier selected from a group consisting of activated carbon, calcium carbonate, ceria, alumina, zirconia, titania and silica in an amount of 1-10 wt.%. The organic solvent is any one selected from a group consisting of diethylether, isopropylether, methanol, ethanol, isopropylalcohol, butanol, tetrahydrofuran and dioxane.
Abstract:
PURPOSE: A process is provided which decreases corrosion properties of apparatus not using a strong base such as sodium methoxylate and prepares difluoromethyl methyl ether of high recovery rate. CONSTITUTION: Cholrodifluoromethane and methanol are reacted at 30-150°C in the presence of 0.05-2 times of alkali carbonate in a mole ratio of chlorodifluoromethane as a base such as Li2CO3, Na2CO3, K2CO3, Rb2CO3 or Cs2CO3 to give difluoromethyl methyl ether. Thus, 17.2 g of chlorodifluoromethane is reacted in 16.7 g of K2CO3 and 50 cc of methanol at 60°C for 2 hours to give difluoromethyl methyl ether(CF2HOCH3).
Abstract translation:目的:提供一种降低不使用强碱如甲氧基钠的设备的腐蚀性能并制备高回收率的二氟甲基甲醚的方法。 构成:在二氯甲基甲基醚中,在二氯甲基甲基醚中,在二氯甲烷和二氯甲基甲醚中,在二氯甲烷和二氯甲基甲醚中,在二氯甲烷与二氯甲基甲醚的摩尔比为0.05-2的碱性碳酸盐存在下,将三氟甲烷和甲醇在30-150℃反应。 因此,将17.2g氯二氟甲烷在16.7g的K 2 CO 3和50cc的甲醇中在60℃下反应2小时,得到二氟甲基甲基醚(CF 2 CHOCH 3)。
Abstract:
PURPOSE: 1,1-difluoroethyl methyl ether as a CFC substitutional material is prepared which protects a corrosion of apparatus, and decreases by-product by using alkali carbonate catalyst instead of strong base. CONSTITUTION: 1,1-Difluoroethylene and methanol are reacted at 30- 150°C in the presence of 1- 20 mole % of difluoroethylene alkali carbonate such as Li2CO3, Na2CO3, K2CO3, Rb2CO3 and CS2CO3 to give the title compound. Thus, 12.8 g of 1,1-difluoroethylene and 64 g of methanol are reacted at 80°C for 3 hours in the presence of 2.78 g of potassium carbonate to give the title compound.
Abstract translation:目的:制备作为CFC取代材料的1,1-二氟乙基甲基醚,其保护装置的腐蚀,并且通过使用碱金属碳酸盐催化剂代替强碱来减少副产物。 构成:1,1-二氟乙烯和甲醇在1-20摩尔%的二氟乙烯碱金属碳酸盐如Li 2 CO 3,Na 2 CO 3,K 2 CO 3,Rb 2 CO 3和CS 2 CO 3的存在下,在30-150℃下反应,得到标题化合物。 因此,在2.78g碳酸钾存在下,将12.8g 1,1-二氟乙烯和64g甲醇在80℃下反应3小时,得到标题化合物。