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    • 9. 发明授权
    • Method for manufacturing 2,3,3,3-tetrafluoropropene
    • 制备2,3,3,3-四氟丙烯的方法
    • US09061956B2
    • 2015-06-23
    • US14347260
    • 2012-09-20
    • Anne PigamoNicolas DoucetLaurent Wendlinger
    • Anne PigamoNicolas DoucetLaurent Wendlinger
    • C07C17/20
    • C07C17/206C07C21/18
    • The present invention relates to a method for manufacturing 2,3,3,3-tetrafluoropropene from halopropanes having the formula CX3CHCICH2X and halopropenes having the formulas CX3CCI═CH2CCIX2CCI═CH2 and CX2═CCICH2X, where X is independently a fluorine or chlorine atom. The invention specifically relates to a method including at least one step during which 2-chloro-3,3,3-trifluoro-1-propene, optionally mixed with at least one halopropane having the formula CX3CHCICH2X and/or at least one halopropene having the formulas CCIX2CCI═CH2 and CX2═CCICH2X, where X is independently a fluorine or chlorine atom, reacts with HF in the gaseous phase in the presence of a fluoridation catalyst at a temperature of between 320 and 420° C. with a molar ratio of oxygen to 2-chloro-3,3,3-trifluoro-1-propene of more than 1 but no more than 2.5, and a molar ratio of HF to the total amount of organic compounds to be reacted of between 5 and 40.
    • 本发明涉及一种由具有式CX3CHCICH2X的卤代丙烷制备2,3,3,3-四氟丙烯的方法和具有式CX3CCI = CH2CCIX2CCI = CH2和CX2 = CCICH2X的卤代丙烯,其中X独立地为氟或氯原子。 本发明具体涉及包括至少一个步骤的方法,其中2-氯-3,3,3-三氟-1-丙烯,任选地与至少一种具有式CX3CHCICH2X的卤代丙烷和/或至少一种具有 式中,CCIX2CCI = CH2和CX2 = CCICH2X,其中X独立地为氟或氯原子,在氟化催化剂存在下,在温度为320至420℃之间,与气相中的HF反应,氧气摩尔比 至大于1但不超过2.5的2-氯-3,3,3-三氟-1-丙烯,HF与要反应的有机化合物的总量的摩尔比为5至40。
    • 10. 发明申请
    • Method for Manufacturing 2,3,3,3-Tetrafluoropropene
    • 制备2,3,3,3-四氟丙烯的方法
    • US20140275653A1
    • 2014-09-18
    • US14347260
    • 2012-09-20
    • Anne PigamoNicolas DoucetLaurent Wendlinger
    • Anne PigamoNicolas DoucetLaurent Wendlinger
    • C07C17/20
    • C07C17/206C07C21/18
    • The present invention relates to a method for manufacturing 2,3,3,3-tetrafluoropropene from halopropanes having the formula CX3CHCICH2X and halopropenes having the formulas CX3CCI═CH2CCIX2CCI═CH2 and CX2═CCICH2X, where X is independently a fluorine or chlorine atom. The invention specifically relates to a method including at least one step during which 2-chloro-3,3,3-trifluoro-1-propene, optionally mixed with at least one halopropane having the formula CX3CHCICH2X and/or at least one halopropene having the formulas CCIX2CCI═CH2 and CX2═CCICH2X, where X is independently a fluorine or chlorine atom, reacts with HF in the gaseous phase in the presence of a fluoridation catalyst at a temperature of between 320 and 420° C. with a molar ratio of oxygen to 2-chloro-3,3,3-trifluoro-1-propene of more than 1 but no more than 2.5, and a molar ratio of HF to the total amount of organic compounds to be reacted of between 5 and 40.
    • 本发明涉及一种由具有式CX3CHCICH2X的卤代丙烷制备2,3,3,3-四氟丙烯的方法和具有式CX3CCI = CH2CCIX2CCI = CH2和CX2 = CCICH2X的卤代丙烯,其中X独立地为氟或氯原子。 本发明具体涉及包括至少一个步骤的方法,其中2-氯-3,3,3-三氟-1-丙烯,任选地与至少一种具有式CX3CHCICH2X的卤代丙烷和/或至少一种具有 式中,CCIX2CCI = CH2和CX2 = CCICH2X,其中X独立地为氟或氯原子,在氟化催化剂存在下,在温度为320至420℃之间,与气相中的HF反应,氧气摩尔比 至大于1但不超过2.5的2-氯-3,3,3-三氟-1-丙烯,HF与要反应的有机化合物的总量的摩尔比为5至40。