Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF.sub.3CFCH.sub.2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl.sub.2CClCH.sub.2Cl (which may be purchased or synthesized from 1,2,3-trichloropropane) is fluorinated (preferably with HF in gas-phase in the presence of a catalyst) to synthesize a compound such as CF.sub.3CClCH.sub.2, preferably in a 80-96% selectivity. The CF.sub.3CClCH.sub.2 is preferably converted to CF.sub.3CFClCH.sub.3 (244-isomer) using a SbCl.sub.5 as the catalyst which is then transformed selectively to 1234yf, preferably in a gas-phase catalytic reaction using activated carbon as the catalyst. For the first step, a mixture of Cr.sub.2O.sub.3 and FeCl.sub.3/C is preferably used as the catalyst to achieve high selectivity to CF.sub.3CClCH.sub.2 (96%). In the second step, SbCl.sub.5/C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF.sub.3CFClCH.sub.3. The intermediates are preferably isolated and purified by distillation and used in the next step without further purification, preferably to a purity level of greater than about 95%.

A liquid composition according to one embodiment of the present invention contains 0.0001 mol % to 40 mol % (Z)-1,2-dichloro-3,3,3-trifluoropropene (1223Z) and 99.9999 mol % to 60 mol % (E)-1,2-dichloro-ethylene (t-DCE). The liquid composition has less influence on the global environment and azeotropic (or azeotrope-like) properties. There occurs practically no composition change even when the liquid composition is used in an open system or used for a long term. Further, it is less likely that there will occur a composition change even when the liquid composition is recovered by distillation. The liquid composition is thus suitably usable as a cleaning agent (solvent). In particular, the liquid composition of 90 mol % or less of t-DCE is classified as non-hazardous under the Fire Serves Act.

A liquid composition according to one embodiment of the present invention contains 0.0001 mol % to 40 mol % (Z)-1,2-dichloro-3,3,3-trifluoropropene (1223Z) and 99.9999 mol % to 60 mol % (E)-1,2-dichloro-ethylene (t-DCE). The liquid composition has less influence on the global environment and azeotropic (or azeotrope-like) properties. There occurs practically no composition change even when the liquid composition is used in an open system or used for a long term. Further, it is less likely that there will occur a composition change even when the liquid composition is recovered by distillation. The liquid composition is thus suitably usable as a cleaning agent (solvent). In particular, the liquid composition of 90 mol % or less of t-DCE is classified as non-hazardous under the Fire Serves Act.

The invention relates to the separation of a mixture comprising 2-chloro-1,1-difluoroethane (R142) and trans-dichloroethylene (TDCE) by extractive distillation and more particularly to a separation process wherein the TDCE is removed selectively by extractive distillation, thus leading to purified 2-chloro-1,1-difluoroethane.

The invention relates to the separation of a mixture comprising 2-chloro-1,1-difluoroethane (R142) and trans-dichloroethylene (TDCE) by extractive distillation and more particularly to a separation process wherein the TDCE is removed selectively by extractive distillation, thus leading to purified 2-chloro-1,1-difluoroethane.

The invention relates to the separation of a mixture comprising 2-chloro-1,1-difluoroethane (R142) and trans-dichloroethylene (TDCE) by extractive distillation and more particularly to a separation process wherein the TDCE is removed selectively by extractive distillation, thus leading to purified 2-chloro-1,1-difluoroethane.

There are provided a solvent composition containing tDCE, which does not exert an adverse effect on the global environment, has high solubility and incombustibility, and can maintain initial incombustibility even in use accompanied by a phase change, a cleaning method using the solvent composition, a coating film-forming composition including the solvent composition, and a method of forming a homogeneous coating film using the coating film-forming composition. A solvent composition includes: tDCE; at least one HFE (A) selected from HFE-347pc-f, HFE-365mf-c, and HFE-467sc-f; and at least one HFC (X) selected from cHFC-447, and HFC-76-13sf, in which a ratio of tDCE with respect to a total amount of tDCE, HFE (A), and HFC (X) is 65 to 80 mass %, a ratio of HFE (A) with respect to the total amount is 5 to 25 mass %, and a ratio of HFC (X) with respect to the total amount is 5 to 25 mass %.

There are provided a solvent composition containing tDCE, which does not exert an adverse effect on the global environment, has high solubility and incombustibility, and can maintain initial incombustibility even in use accompanied by a phase change, a cleaning method using the solvent composition, a coating film-forming composition including the solvent composition, and a method of forming a homogeneous coating film using the coating film-forming composition. A solvent composition includes: tDCE; at least one HFE (A) selected from HFE-347pc-f, HFE-365mf-c, and HFE-467sc-f; and at least one HFC (X) selected from cHFC-447, and HFC-76-13sf, in which a ratio of tDCE with respect to a total amount of tDCE, HFE (A), and HFC (X) is 65 to 80 mass %, a ratio of HFE (A) with respect to the total amount is 5 to 25 mass %, and a ratio of HFC (X) with respect to the total amount is 5 to 25 mass %.

Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF.sub.3CFCH.sub.2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl.sub.2CClCH.sub.2Cl (which may be purchased or synthesized from 1,2,3-trichloropropane) is fluorinated (preferably with HF in gas-phase in the presence of a catalyst) to synthesize a compound such as CF.sub.3CClCH.sub.2, preferably in a 80-96% selectivity. The CF.sub.3CClCH.sub.2 is preferably converted to CF.sub.3CFClCH.sub.3 (244-isomer) using a SbCl.sub.5 as the catalyst which is then transformed selectively to 1234yf, preferably in a gas-phase catalytic reaction using activated carbon as the catalyst. For the first step, a mixture of Cr.sub.2O.sub.3 and FeCl.sub.3/C is preferably used as the catalyst to achieve high selectivity to CF.sub.3CClCH.sub.2 (96%). In the second step, SbCl.sub.5/C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF.sub.3CFClCH.sub.3. The intermediates are preferably isolated and purified by distillation and used in the next step without further purification, preferably to a purity level of greater than about 95%.

Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF.sub.3CFCH.sub.2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl.sub.2CClCH.sub.2Cl (which may be purchased or synthesized from 1,2,3-trichloropropane) is fluorinated (preferably with HF in gas-phase in the presence of a catalyst) to synthesize a compound such as CF.sub.3CClCH.sub.2, preferably in a 80-96% selectivity. The CF.sub.3CClCH.sub.2 is preferably converted to CF.sub.3CFClCH.sub.3 (244-isomer) using a SbCl.sub.5 as the catalyst which is then transformed selectively to 1234yf, preferably in a gas-phase catalytic reaction using activated carbon as the catalyst. For the first step, a mixture of Cr.sub.2O.sub.3 and FeCl.sub.3/C is preferably used as the catalyst to achieve high selectivity to CF.sub.3CClCH.sub.2 (96%). In the second step, SbCl.sub.5/C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF.sub.3CFClCH.sub.3. The intermediates are preferably isolated and purified by distillation and used in the next step without further purification, preferably to a purity level of greater than about 95%.