Abstract:
본 발명은 생분해성 고분자 소재의 중합에 있어서, 압축기체(compressed gas)를 반응 용매로 사용하여 용액 중합하여, 입자크기가 0.01 ~ 1000 ㎛인 미세 분말 형태의 고분자량 생분해성 단일중합 폴리에스테르 및 공중합 폴리에스테르를 제조하는 방법에 관한 것이다. 본 발명의 생분해성 폴리에스테르의 제조방법은 락티드(Lactide)와 글리콜리드(Glycolide) 등을 포함하는 화합물과 카프로락톤으로 이루어지는 군 중에서 선택되는 화합물 및 이들의 혼합물로 된 단량체를 개시제 및 유기금속촉매와 함께 압축기체의 존재 하에서 용액 중합시킴으로써, 지방족 생분해성 폴리에스테르를 중합하고 미세 분말 또는 구형의 입자형태의 지방족 생분해성 폴리에스테르 및 공중합 폴리에스테르를 제조하는 것을 특징으로 한다.
Abstract:
PURPOSE: A method for producing a biodegradable polyester polymer in a particulate form, is provided to simplify a conventional complicated process by excluding a milling process or use of any special device, and prevent discharge of hazardous solvents to environment. CONSTITUTION: The method for producing a biodegradable polyester polymer in a particulate form comprises the steps of: charging at least one cyclic monomer into a high pressure reactor; adding an organometallic or acid catalyst and an initiator; injecting compressed gas as a solvent, selected from the group consisting of HFC-23, HFC-32, HFC-152a, HFC-143a, HFC-134a, HFC-125, HFC-227ea, HFC-236fa, HFC-245fa, HFC-254cb, SF6, HFC-4-10-mee, C-318(perfluoro cyclobutane), HCFC-22, HCFC-1416, HCFC-1426, HCFC-225ca/cb, dimethyl ether, N2O, propane, butane, a mixture thereof and a mixture further comprising CO2 and the above mixture, into the reactor; and carrying out solution polymerization.
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: 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 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: 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:
본 발명은 지구의 오존층을 파괴하는 것으로 알려진 R-502를 대체하기 위한 저온용 냉매 조성물에 관한 것으로, 지구의 오존층을 파괴하는 CFC나 HCFC를 함유하지 않은 새로운 냉매 조성물을 제공하는 것이 목적이다. 상기 목적을 달성하기 위한 본 발명의 냉매 조성물은, 디플루오로메탄 (CH 2 F 2 , 이하 HFC-32라 함)과; 1,1,1-트리플루오로에탄 (CH 3 CF 3 , 이하 HFC-143a라 함)과; 사이클로프로판 (C 3 H 6 , 이하 RC-270라 함) 또는 프로판 (C 3 H 8 , 이하 R-290라 함) 중에서 선택되는 하나의 화합물로 이루어진다.
Abstract:
PURPOSE: A method for synthesizing terephthalic acid using a subcritical or supercritical fluid as a reaction medium is provided to reduce toxicity and erosion in a manufacturing device owing to excluding the use of a catalyst, thereby being safer and more economic as compared to the conventional methods. CONSTITUTION: The method for synthesizing terephthalic acid which includes the oxidization of para-xylene comprises the use of excessive amount of a subcritical or a supercritical fluid as a reaction medium and hydrogen peroxide or oxygen as an oxidizing agent for partial oxidization of para-xylene contained in a tank(A11), while excluding the use of a catalyst. The oxidization of para-xylene is carried out at 240-400deg.C under 220-300bar in a reactor(A4).