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    • 2. 发明授权
    • Method for producing perhalogenated cyclopentene
    • 生产全卤代环戊烯的方法
    • US06395940B1
    • 2002-05-28
    • US09486608
    • 2000-03-01
    • Takeo KomataTakayuki NishimiyaFuyuhiko SakyuHideaki ImuraMikio UjiieMasatomi Kanai
    • Takeo KomataTakayuki NishimiyaFuyuhiko SakyuHideaki ImuraMikio UjiieMasatomi Kanai
    • C07C1720
    • C07C23/08C07C17/206C07C17/208C07C17/21
    • The invention relates to a method for producing a first perhalogenated cyclopentene represented by the general formula: C5ClBF8−B where B is an integer of from 0 to 7. The method includes a step of (a) fluorinating a second perhalogenated cyclopentene by hydrogen fluoride in a gas phase in the presence of a fluorination catalyst. The second perhalogenated cyclopentene is represented by general formula: C5ClAF8−A where A is an integer of from 1 to 8, and A is not smaller than B. With this method, the first perhalogenated cyclopentene (e.g., 1,2-dichloro-3,3,4,4,5,5-hexafluorocyclopentene, another chlorofluorinated cyclopentene, or octafluorocyclopentene) can continuously easily be produced, for example, from octachlorocyclopentene obtained by chlorination of hexachlorocyclopentadiene that is easily available. Therefore, the above method is very useful as an industrial scale production method. In case that the first perhalogenated cyclopentene is octafluorocyclopentene, the method may further include a step of (b) fluorinating a reaction product of the step (a) in a way that is different from that of the step (a), thereby to convert said reaction product of the step (a) into octafluoropentene. The step (a) may be conducted by a multistep reaction wherein there are provided “m” of reaction zones in number where m is an integer of from 2 to 10. In this case, the reaction zones are arranged in series and such that a reaction temperature of each reaction zone is independently controllable.
    • 本发明涉及一种制备由通式C5ClBF8-B表示的第一全卤代环戊烯的方法,其中B为0-7的整数。该方法包括以下步骤:(a)通过氟化氢将第二全卤代环戊烯氟化 在氟化催化剂存在下的气相。 第二全卤代环戊烯由通式C5ClAF8-A表示,其中A为1至8的整数,A不小于B.使用该方法,将第一全卤代环戊烯(例如1,2-二氯-3 ,3,4,4,5,5-六氟环戊烯,另一种氯氟化环戊烯或八氟环戊烯)可以连续容易地制备,例如由可以容易获得的六氯环戊二烯氯化获得的八氯环戊烯。 因此,上述方法作为工业规模生产方法是非常有用的。 在第一全卤代环戊烯是八氟环戊烯的情况下,该方法还可以包括以下步骤:(b)以与步骤(a)不同的方式氟化步骤(a)的反应产物,从而将所述 步骤(a)的反应产物进入八氟戊烯。 步骤(a)可以通过多步反应进行,其中m为2〜10的整数的“m”个反应区。在这种情况下,反应区串联排列,使得 每个反应区的反应温度是独立可控的。