首页> 外国专利> Exo-tetra:hydro-dicyclopentadiene jet fuel prodn. - from endo-dicyclopentadiene by hydrogenation and isomerisation

Exo-tetra:hydro-dicyclopentadiene jet fuel prodn. - from endo-dicyclopentadiene by hydrogenation and isomerisation

机译:Exo-tetra:hydro-dicyclopentadiene喷气燃料产品-通过氢化和异构化从二环戊二烯内

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。

著录项

  • 公开/公告号DE3026587A1

    专利类型

  • 公开/公告日1982-02-04

    原文格式PDF

  • 申请/专利权人 ASHLAND OILINC.;

    申请/专利号DE19803026587

  • 发明设计人 C. HOWESTEVEN;V. NORTONRICHARD;

    申请日1980-07-14

  • 分类号C07C13/28;C07C5/22;

  • 国家 DE

  • 入库时间 2022-08-22 12:43:12

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号