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公开(公告)号:US20160039729A1
公开(公告)日:2016-02-11
申请号:US14822497
申请日:2015-08-10
Applicant: HONEYWELL INTERNATIONAL INC.
Inventor: Hsueh S. Tung , Sudip Mukhopadhyay , Michael Van Der Puy , Daniel C. Merkel , Jing Ji Ma , Cheryl L. Bortz , Barbara A. Light , Steven D. Phillips , Kim M. Fleming , Susan A. Ferguson
CPC classification number: C07C17/23 , C07C17/087 , C07C17/10 , C07C17/206 , C07C17/21 , C07C17/25 , C07C19/08 , C07C19/10 , C07C21/18
Abstract: Disclosed is a process for producing fluorinated organic compounds, including hydrofluoropropenes, which preferably comprises converting at least one compound of Formula (I): C(X)3CF2C(X)3 (I) to at least one compound of Formula (II) CF3CF═CHZ (II) where each X and Z is independently H, F, Cl, I or Br, said process preferably not including any substantial amount of oxygen-containing catalyst in certain embodiments.Preferably Z is H.
Abstract translation: 公开了一种制备氟化有机化合物的方法,包括氢氟丙烯,其优选包括将至少一种式(I)化合物:C(X)3CF 2 C(X)3(I)转化为至少一种式(II)化合物CF 3 CF ≡CHZ(II)其中每个X和Z独立地为H,F,Cl,I或Br,在某些实施方案中,所述方法优选不包括任何显着量的含氧催化剂。 Z优选为
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公开(公告)号:US20190263736A1
公开(公告)日:2019-08-29
申请号:US16112058
申请日:2018-08-24
Applicant: HONEYWELL INTERNATIONAL INC.
Inventor: Sudip Mukhopadhyay , Hsueh S. Tung , Michael Van Der Puy , Daniel C. Merkel , Jing Ji Ma , Cheryl L. Bortz , Barbara A. Light , Steven D. Phillips , Rajesh K. Dubey
IPC: C07C17/25 , C07C21/18 , C07C17/278 , C07C17/272 , C07C17/269 , C07C17/26 , C07C17/00 , C07C17/20 , C07C17/087 , C07C17/04 , C07C17/21
Abstract: Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF3CF═CH2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl2═CClCH2Cl (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 CF3CCl═CH2, preferably in a 80-96% selectivity. The CF3CCl═CH2 is preferably converted to CF3CFClCH3 (244-isomer) using a SbCl5 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 FeCl3/C is preferably used as the catalyst to achieve high selectivity to CF3CCl═CH2 (96%). In the second step, SbCl5/C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF3CFClCH3. 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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