306-83-2Relevant articles and documents
Selective hydrogenolysis of CFC-113a by Group VIII transition metal complexes
Cho, Ook-Jae,Lee, Ik-Mo,Park, Kun-You,Kim, Hoon-Sik
, p. 107 - 110 (1995)
Highly efficient and selective hydrogenolysis of CFC-113a (CF3CCl3) to produce HCFC-123 (CF3CHCl2) has been achieved through the use of Group VIII transition metal complexes.The catalytic activity observed was sensitive to solvents and to the structure of the metal complexes. - Keywords: Selective hydrogenolysis; CFC-113a; Group VIII transition metal complexes; Catalysis; Selectivity
Dmowski,Kolinski
, p. 210 (1972)
Transfer hydrogenolysis of CFC-113a with aldehydes and metallic Fe or Ni
Seo, Sang Hyun,Hong, Seung-Pyo,Kwag, Chong-Yun,Lee, Hyun-Joo,Kim, Hoonsik,Lee, Ik-Mo
, p. 73 - 78 (1999)
Highly selective transfer hydrogenolysis of CFC-113a (CF3CCl3) to HCFC-123 (CF3CHCl2) was accomplished in the presence of metal powder (Fe or Ni) in THF at 90°C under 8 atm of He. Pressure effects on the catalytic activities depend on the nature of metal catalysts and this behavior can be explained by a different rate determining step in each system. Activation of the C-H bond of THF on metal powder aided by η2 coordinated aldehydes is believed to occur first to produce electron-rich metal hydrides, which enhance the activation of the C-Cl bond of CFC-113a. Then reductive elimination follows to produce HCFC-123. This series of reactions was supported by experiments using deuterated THF and/or DMF and with p-substituted benzaldehydes.
Manufacturing method of HCFC-123 and/or HCFC-122
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Paragraph 0139-0141, (2019/12/25)
The present invention relates to a method for producing HCFC-123 (2,2-dichloro-1,1,1-trifluoroethane) and/or HCFC-122 (1,1,2-trichloro-2,2-difluoroethane), wherein at least one reaction step is performed in a microreactor. In particular, a preferred embodiment of the present invention relates to a method for producing HCFC-123 (2,2-dichloro-1,1,1-trifluoroethane) and/or HCFC-122 (1,1,2-trichloro-2,2-difluoroethane), wherein at least one reaction step is performed in a microreactor composed of or made of SiC ("SiC microreactor") or in a microreactor composed of or made of alloy (such as Hastelloy C). In one embodiment, the method for producing HCFC-123 (2,2-dichloro-1,1,1-trifluoroethane) and/or HCFC-122 (1,1,2-trichloro-2,2-difluoroethane) can be effectively combined, because the HCFC-122(1,1,2-trichloro-2,2-difluoroethane) produced by the method according to the present invention using a microreactor, preferably a SiC microreactor, can be preferably and advantageously used as a raw material and/or intermediate material for the production of the HCFC-123 (2,2-dichloro-1,1,1-trifluoroethane), and preferably also used for manufacturing the HCFC-123 (2,2-dichloro-1,1,1-trifluoroethane) in a microreactor. During the manufacturing of the HCFC-123 and/or the HCFC-122, the HCFC-123 and/or the HCFC-122 can be easily purified and/or separated by using only a low energy consumption method, and the method for performing purification and/or separation preferably requires no distillation. Advantageously, the the HCFC-123 and/or the HCFC-122 can be easily separated from the excess HF and a catalyst in an energy-saving manner by phase separation.
A liquid-phase fluorination preparing 1,2-dichloro -3, 3, 3-trifluoropropene method
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Paragraph 0056; 0057, (2017/03/14)
The invention discloses a liquid-phase fluorination preparation method for 1, 2-dichloro-3, 3, 3-trifluoropropene, and in particular relates to the preparation of 1, 2-dichloro-3, 3, 3-trifluoropropene through the liquid-phase fluorination reaction between a compound with the general formula of CF3-xClxCH2-yCLyCH3-zClz and hydrogen fluoride in presence of a fluorination catalyst, wherein in the general formula of the compound, x is 0, 1, 2 or 3; y is 1 or 2; z is 1 or 2; y plus z is 3. The method is mainly used for preparing 1, 2-dichloro-3, 3, 3-trifluoropropene.
PROCESS FOR PRODUCING FLUOROETHANE
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Paragraph 0035-0037; 0040, (2015/12/04)
Fluorochromium oxide having a fluorine content of not less than 30 wt.% is used for the fluorination reaction. To provide a manufacturing method for fluorine-containing ethane which contains 1, 1, 1, 2, 2-pentafluoroethane as the main component in which the reaction can be performed while controlling the generation of CFCs to the greatest possible extent by fluorinating at least one selected from the group composed of tetrachloroethylene, 2, 2-dichloro-1, 1, 1-trifluoroethane and 2-chloro-1, 1, 1, 2-tetrafluoroethane with hydrogen fluoride.