首页> 外国专利> process for the production of exo tetrahydrodicyclopentadien by hydrogenation of endo - dicyclopentadien and subsequent isomerisation of the endo - tetrahydrodicyclopentadiens

process for the production of exo tetrahydrodicyclopentadien by hydrogenation of endo - dicyclopentadien and subsequent isomerisation of the endo - tetrahydrodicyclopentadiens

机译:内二环戊二烯加氢及随后的内四氢二环戊二烯异构化制备外四氢二环戊二烯的方法。

摘要

Prepn. of oxo-tetrahydrodicyclopentadiene (I) is carried out by (a) hydrogenating endo-dicyclopentadiene (II) contg. a dispersed Ni catalyst to form crude endo-tetrahydrodicyclopentadiene (III) with a m.pt. of at least 70 deg.C; (b) contacting the crude (III) with AlCl3 at 100-150 deg.C; and (c) sepg. the liq. phase comprising from the sludge phase of the reaction mixt. Hydrogenation is pref. effected in 2 stages: (1) at 110-120 deg.C to effect hydrogenation of the 8 and 9 positions; (2) at 150-200 deg.C to complete the hydrogenation. Step (b) is pref. effected in the presence of an inert solvent, esp. added (I). The AlCl3- rich sludge from step (c) is pref. recycled to step (b). (I) is a high-energy fuel for use in jet engeins, e.g. in missiles. The presence of spent Ni catalyst in the crude (III) ensures high conversions in step (b) with high selectivity for (I); e.g. 81-99% yields can be obtd.
机译:准备氧-四氢二环戊二烯(I)的制备通过(a)将内二环戊二烯(II)加氢进行。用分散的镍催化剂形成熔点为四氢呋喃的粗制内四氢二环戊二烯(Ⅲ)。至少70摄氏度; (b)在100-150℃下使粗品(III)与AlCl 3接触;和(c)sepg。液体由反应混合物的污泥相组成的相。氢化是优选的。分两个阶段进行:(1)在110-120℃下进行8和9位加氢; (2)在150-200℃下完成氢化。步骤(b)是优选的。特别是在惰性溶剂存在下进行。添加(I)。来自步骤(c)的富含AlCl3的污泥是优选的。回收到步骤(b)。 (I)是用于喷气葛根素的高能燃料,例如在导弹中。粗制(III)中废镍催化剂的存在确保了步骤(b)中的高转化率和(I)的高选择性;例如可以达到81-99%的产率。

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