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:
본 발명은 초임계상태의 이산화 탄소를 이용하여 벼의 미강으로부터 유지를 추출하는 방법에 관한 것으로, 미강이 들어있는 추출기에 고압·고밀도의 초임계상태 이산화탄소를 통과시킴으로써 이 이산화탄소가 미강중에 함유되어 있는 유지를 용해시켜 추출하도록 하는 것이다. 본발명에 따른 유지 추출 방법은 이산화탄소를 용매로 사용하므로, 유지중 유해물질의 잔류 문제가 없고 기존 방법보다 상대적으로 낮은 온도에서 유지가 추출될 수 있으며 유지가 이산화탄소에 의해 항시 공기로부터 차단되므로, 추출시에 유지성분의 열분해와 산화가 수반되지 않는 장점이 있다.
Abstract:
본 발명은 사염화 주석촉매 1리터 당 VCM을 1시간에 0.3~1.5몰의 속도로, 무수 불화수소산은 VCM 1몰에 대해 2.9~5.0몰의 속도로 공급하고, 두 반응물을 가열하여 기체상태로 반응기에 공급하며, 0.4~2.0MPa의 압력과 50~120℃의 반응기 온도 그리고 20~40℃의 반응응축기에서 연속적으로 액상반응 시키는 것을 특징으로 하여 HFC-152a를 제조하는 방법에 관한 것 임.
Abstract:
본 발명은 사염화 주석촉매 1리터 당 VCM을 1시간에 0.3∼1.5몰의 속도로, 무수 불화수소산은 VCM 1몰에 대해 2.0∼5.0몰의 속도로 공급하고, 두 반응물을 가열하여 기체상태로 반응기에 공급하며, 0.4∼2.0MPa의 압력과 50∼120℃의 반응기 온도 그리고 20∼40℃의 반응응축기에서 연속적으로 액상반응시키는 것을 특징으로 하여 HFC-152a를 제조하는 방법에
Abstract:
PURPOSE: A method for preparing dimethyl dipropargylmalonate polymer having the hexagonal ring structure is provided, to reduce the pollution due to an organic solvent and to prevent the production of two different structured cyclic polymers by not using an organic solvent. CONSTITUTION: The method comprises the step of cyclic polymerizing dimethyl dipropargylmalonate monomer by using supercritical or subcritical carbon dioxide as a solvent in the presence of a transition metal chloride catalyst. Preferably the reaction temperature is 15-100 deg.C, the reaction pressure is 50-400 atm, and the reaction time is 24 hours or less.
Abstract:
PURPOSE: A method for preparing dimethyl dipropargylmalonate polymer having the hexagonal ring structure is provided, to reduce the pollution due to an organic solvent and to prevent the production of two different structured cyclic polymers by not using an organic solvent. CONSTITUTION: The method comprises the step of cyclic polymerizing dimethyl dipropargylmalonate monomer by using supercritical or subcritical carbon dioxide as a solvent in the presence of a transition metal chloride catalyst. Preferably the reaction temperature is 15-100 deg.C, the reaction pressure is 50-400 atm, and the reaction time is 24 hours or less.
Abstract:
PURPOSE: Provided is a coolant composition containing difluoromethane, 1,1,1-trifluoroethane, and 1,1-difluoroethane, which is substituted for chlorodifluoromethane(CHClF2, HCFC-22) and dose not contain the material destroying an ozone layer. CONSTITUTION: The coolant composition comprises 20-70wt% of the difluoromethane(CH2F2, HFC-32), 10-50wt% of the 1,1,1-trifluoroethane(CH3CF3, HFC-143a), 10-40wt% of the 1,1-difluoroethane(CH3CHF2, HFC-152a), and 10-30wt% of 1,1,1,2,3,3,3-heptafluoropropane(CF3CHFCF3, HFC-227ea) or 5-15wt% of isobutane(CH(CH3)2CH3, R-600a). Or the coolant composition comprises 30-70wt% of the difluoromethane(CH2F2, HFC-32), 10-40wt% of the 1,1,1-trifluoroethane(CH3CF3, HFC-143a), 10-40wt% of the 1,1-difluoroethane(CH3CHF2, HFC-152a), and 10-20wt% of 1,1,1,2,3,3-hexafluoropropane(CHF2CHFCF3, HFC-236ea).
Abstract:
PURPOSE: A refrigerants mixture containing HFC-32, HFC-125, HFC-134A is provided to substitute HCFC-22(chlorodifluoromethane, CHClF2) by maintaining identical working effect without risk of ozone layer destruction. CONSTITUTION: The refrigerant mixture comprises difluoromethane(CH2F2, HFC-32) as first component; pentafluoroethane(CHF2CF3, HFC-125) as second component; 1,1,1,2-tetrafluoroethane(CH2FCF3, HFC-134A) as third component; one component selected from cyclopropane(C3H6, RC-270), 1,1-difluoroethane(CH3CHF2, HFC-152a), 1,1,1,2,3,3,3-heptafluoropropane(CF3CHFCF3, HFC-227ea), 1,1,1,2,2-pentafluoropropane (CH3CF2CF3, HFC-245cb), octafluorocyclobutane(C4F8, RC-318), 1,1,1,2,3,3-hexafluoro propane(CHF2CHFCH3, HFC-236ea), bis(difluoromethyl)ether(CHF2OCHF2, HFE-134), pentafluoroethylmethylether (CF3CF2OCH3, HFE-245), n-pentane(C5H12, R601), isopentane((CH3)2CHCH2CH3, R601a) as fourth component.