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公开(公告)号:EP3336074A1
公开(公告)日:2018-06-20
申请号:EP17201423.5
申请日:2007-01-03
发明人: MERKEL, Daniel C. , TUNG, Hsueh Sung , VAN DER PUY, Michael , MA, Jing Ji , DUBEY, Rajesh , LIGHT, Barbara , BORTZ, Cheryl , PHILLIPS, Steven D. , MUKHOPAHYAY, Sudip
IPC分类号: C07C17/087 , C07C21/19 , C09K5/00
CPC分类号: C07C19/10 , C07C17/04 , C07C17/06 , C07C17/087 , C07C17/206 , C07C17/21 , C07C17/25 , C07C21/18 , C07C19/01 , C07C21/073
摘要: Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF 3 CF=CH 2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl 2 =CClCH 2 Cl (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 CFaCCl=CH2, preferably in a 80-96% selectivity. The CF 3 CCl=CH 2 is preferably converted to CF 3 CFClCH 3 (244-isomer) using a SbCl 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 Cr2O3 and FeCl 3 /C is preferably used as the catalyst to achieve high selectivity to CF 3 CCl=CH 2 (96%). In the second step, SbCl 5 /C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF 3 CFClCH 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%.
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公开(公告)号:EP3336073A1
公开(公告)日:2018-06-20
申请号:EP17201421.9
申请日:2007-01-03
发明人: MERKEL, Daniel C. , TUNG, Hsueh Sung , VAN DER PUY, Michael , MA, Jing Ji , DUBEY, Rajesh , LIGHT, Barbara , BORTZ, Cheryl , PHILLIPS, Steven D. , MUKHOPAHYAY, Sudip
IPC分类号: C07C17/087 , C07C21/19 , C09K5/00
CPC分类号: C07C19/10 , C07C17/04 , C07C17/06 , C07C17/087 , C07C17/206 , C07C17/21 , C07C17/25 , C07C21/18 , C07C19/01 , C07C21/073
摘要: Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF 3 CF=CH 2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl 2 =CClCH 2 Cl (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 CFaCCl=CH2, preferably in a 80-96% selectivity. The CF 3 CCl=CH 2 is preferably converted to CF 3 CFClCH 3 (244-isomer) using a SbCl 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 Cr2O3 and FeCl 3 /C is preferably used as the catalyst to achieve high selectivity to CF 3 CCl=CH 2 (96%). In the second step, SbCl 5 /C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF 3 CFClCH 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%.
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