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    • 21. 发明授权
    • Process for the preparation of fluorinated compounds
    • 氟化合物的制备方法
    • US09255047B2
    • 2016-02-09
    • US12602707
    • 2009-08-19
    • Anne PigamoMichel DevicLaurent Wendlinger
    • Anne PigamoMichel DevicLaurent Wendlinger
    • C07C17/354C07C17/25C07C21/18
    • C07C17/25C07C17/354C07C21/18Y02P20/582C07C19/08
    • A subject-matter of the invention is a process for the preparation of 2,3,3,3-tetrafluoro-1-propene which comprises the following stages: (i) hydrogenation of hexafluoropropylene to give 1,1,1,2,3,3-hexafluoropropane; (ii) dehydrofluorination of the 1,1,1,2,3,3-hexafluoropropane obtained in the preceding stage to give 1,2,3,3,3-pentafluoro-1-propene; (iii) hydrogenation of the 1,2,3,3,3-pentafluoro-1-propene obtained in the preceding stage to give 1,1,1,2,3-pentafluoropropane; and (iv) dehydrofluorination of the 1,1,1,2,3-pentafluoropropane obtained in the preceding stage to give 2,3,3,3-tetrafluoro-1-propene. Stages (ii) and (iv) are carried out using a water and potassium hydroxide mixture with the potassium hydroxide representing between 58 and 86% by weight of the mixture and at a temperature of between 110 and 180° C.
    • 本发明的主题是制备2,3,3,3-四氟-1-丙烯的方法,其包括以下步骤:(i)六氟丙烯的氢化,得到1,1,1,2,3 ,3-六氟丙烷; (ii)前段得到的1,1,1,2,3,3-六氟丙烷的脱氟化氢,得到1,2,3,3,3-五氟-1-丙烯; (iii)在前一阶段获得的1,2,3,3,3-五氟-1-丙烯的氢化,得到1,1,1,2,3-五氟丙烷; 和(iv)前一阶段获得的1,1,1,2,3-五氟丙烷的脱氟化氢,得到2,3,3,3-四氟-1-丙烯。 阶段(ii)和(iv)使用氢氧化钾与氢氧化钾混合物进行,其中氢氧化钾占混合物重量的58-86%,在110-180℃的温度下进行。
    • 24. 发明申请
    • Catalytic Gas Phase Fluorination of 243db to 1234yf
    • 催化气相氟化243db至1234yf
    • US20110160499A1
    • 2011-06-30
    • US12978288
    • 2010-12-23
    • Laurent WendlingerAnne PigamoDominique Deur-Bert
    • Laurent WendlingerAnne PigamoDominique Deur-Bert
    • C07C17/357
    • C07C17/206B01J23/866B01J37/26C07C17/25C07C17/42C07C21/08Y02P20/582C07C19/10C07C21/18
    • The invention provides a process for preparing 1234yf, comprising: (i) contacting 243db with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into a first stream comprising HCl, 1234yf and a second stream comprising HF, 1233xf and 245cb; (iii) recycling at least a part of the second stream at least in part back to step (i). The invention also provides a process for preparing 1234yf, comprising: (i) contacting 243db with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into HCl and a stream containing the fluorinated products; (iii) separating said stream containing the fluorinated products into a first stream comprising 1234yf and a second stream comprising HF, 1233xf and 245cb; (iv) recycling at least a part of the second stream at least in part back to step (i).
    • 本发明提供了一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,使气体中的243db与氟化氢HF接触; (ii)将反应混合物分离成包含HCl,1234yf和包含HF,1233xf和245cb的第二料流的第一料流; (iii)至少部分地将第二流的至少一部分再循环回到步骤(i)。 本发明还提供了一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,将气体中的243db与氟化氢HF气相接触; (ii)将反应混合物分离成HCl和含有氟化产物的料流; (iii)将含有氟化产物的物流分离成包含1234yf的第一物流和包含HF,1233xf和245cb的第二物流; (iv)至少部分地将至少一部分第二流再循环到步骤(i)。
    • 26. 发明授权
    • Catalytic gas phase fluorination of 243db to 1234yf
    • 催化气相氟化243db至1234yf
    • US08207384B2
    • 2012-06-26
    • US12978288
    • 2010-12-23
    • Laurent WendlingerAnne PigamoDominique Deur-Bert
    • Laurent WendlingerAnne PigamoDominique Deur-Bert
    • C07C17/00
    • C07C17/206B01J23/866B01J37/26C07C17/25C07C17/42C07C21/08Y02P20/582C07C19/10C07C21/18
    • The invention provides a process for preparing 1234yf, comprising: (i) contacting 243db with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into a first stream comprising HCl, 1234yf and a second stream comprising HF, 1233xf and 245cb; (iii) recycling at least a part of the second stream at least in part back to step (i). The invention also provides a process for preparing 1234yf, comprising: (i) contacting 243db with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into HCl and a stream containing the fluorinated products; (iii) separating said stream containing the fluorinated products into a first stream comprising 1234yf and a second stream comprising HF, 1233xf and 245cb; (iv) recycling at least a part of the second stream at least in part back to step (i).
    • 本发明提供一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,使气体中的243db与氟化氢HF接触; (ii)将反应混合物分离成包含HCl,1234yf和包含HF,1233xf和245cb的第二料流的第一料流; (iii)至少部分地将第二流的至少一部分再循环回到步骤(i)。 本发明还提供了一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,将气体中的243db与氟化氢HF气相接触; (ii)将反应混合物分离成HCl和含有氟化产物的料流; (iii)将含有氟化产物的物流分离成包含1234yf的第一物流和包含HF,1233xf和245cb的第二物流; (iv)至少部分地将至少一部分第二流再循环到步骤(i)。
    • 28. 发明申请
    • Catalytic Gas Phase Fluorination of 1233xf to 1234yf
    • 催化气相氟化1233xf至1234yf
    • US20110319675A2
    • 2011-12-29
    • US12978241
    • 2010-12-23
    • Dominique Deur-bertLaurent WendlingerAnne Pigamo
    • Dominique Deur-bertLaurent WendlingerAnne Pigamo
    • C07C17/20
    • C07C17/087C07C17/206Y02P20/582C07C19/08C07C21/18
    • The present invention provides a process for preparing 1234yf, comprising: (i) contacting 1233xf with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into a first stream comprising HCl, 1234yf and a second stream comprising HF, unreacted 1233xf and 245cb; (iii) recycling at least a part of the second stream at least in part back to step (i). The present invention also provides a process for preparing 1234yf, comprising: (i) contacting 1233xf with hydrogen fluoride HF in gas phase in the presence of a fluorination catalyst under conditions sufficient to produce a reaction mixture; (ii) separating the reaction mixture into HCl and a stream containing the fluorinated products; (iii) separating said stream containing the fluorinated products into a first stream comprising 1234yf and a second stream comprising HF, unreacted 1233xf and 245cb; (iv) recycling at least a part of the second stream at least in part back to step (i).
    • 本发明提供一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,在气相中使1233xf与氟化氢HF接触; (ii)将反应混合物分离成包含HCl,1234yf的第一料流和包含HF,未反应的1233xf和245cb的第二料流; (iii)至少部分地将第二流的至少一部分再循环回到步骤(i)。 本发明还提供了一种制备1234yf的方法,其包括:(i)在足以产生反应混合物的条件下,在氟化催化剂存在下,在气相中将1233xf与氟化氢HF接触; (ii)将反应混合物分离成HCl和含有氟化产物的料流; (iii)将含有氟化产物的物流分离成包含1234yf的第一物流和包含HF,未反应的1233xf和245cb的第二物流; (iv)至少部分地将至少一部分第二流再循环到步骤(i)。