首页> 外国专利> Method for Obtaining a Flow of Hydrocarbons Containing Between 4 and 12 Carbon Atoms Per Molecule, with an Increased Quantity of Linear Alpha-Olefins

Method for Obtaining a Flow of Hydrocarbons Containing Between 4 and 12 Carbon Atoms Per Molecule, with an Increased Quantity of Linear Alpha-Olefins

机译:获得每分子含4到12个碳原子的碳氢化合物并增加线性α-烯烃数量的方法

摘要

A process is proposed for obtaining a stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with an increased proportion of linear α-olefins compared to a feed stream of aliphatic hydrocarbons comprising from 4 to 12 carbon atoms per molecule, with a content of linear α-olefins, linear internal olefins and dienes, whereinthe feed stream is fed to a first distillation zone D1 having at least 5 theoretical plates,in which the linear α-olefins are removed partly or fully as a component of a vapor stream which additionally also comprises the dienes,and at whose lower end a liquid stream is obtained which has been depleted partly or fully of linear α-olefins,the liquid stream from the lower end of the first distillation zone D1 is introduced into a isomerization unit which is equipped with an isomerization catalyst over which the linear internal olefins are isomerized partly or fully to linear α-olefins, and the linear α-olefins formed in this way are removed as a component of a vapor stream ascending into the first distillation zone D1, the vapor stream ascending out of the first distillation zone D1 enters a selective hydrogenation unit comprising a second reactive distillation zone RD2 in which at least a portion of the dienes are hydrogenated selectively to olefins over a low-isomerization selective hydrogenation catalyst to obtain a vapor stream which is drawn off, condensed fully or partly and drawn off as a product stream with an increased proportion of linear α-olefins compared to the feed stream,the distillation zone D1 and the reactive distillation zone RD2 being integrated in a single reactive distillation column RDK.
机译:提出了一种用于获得每分子包含4至12个碳原子的脂族烃料流的方法,与每分子包含4至12个碳原子的脂族烃进料料流相比,该方法增加了线性α-烯烃的比例。线性α-烯烃,线性内部烯烃和二烯的含量,其中 将进料流进料到具有至少5个理论塔板的第一蒸馏区D 1 其中直链α-烯烃作为蒸气物流的一部分被部分或全部除去,该蒸气物流还另外包含二烯, ,其下限末端获得的液体物流已部分或全部被线性α-烯烃耗尽, 来自第一蒸馏区下端的液体物流将D 1 引入配备有异构化催化剂的异构化单元,在该异构化催化剂上,直链内烯烃部分或全部异构化为直链α-烯烃,并且以这种方式形成的直链α-烯烃为作为组件删除上升到第一蒸馏区D 1的蒸汽流, 上升到第一蒸馏区D的蒸汽流 1 进入包含第二反应蒸馏区RD 2 的选择性加氢装置,其中至少一部分二烯通过低异构化选择性加氢催化剂选择性加氢成烯烃获得与原料流相比,以线性α-烯烃比例增加的形式被抽出,全部或部分冷凝并作为产物流排出的蒸气流, 蒸馏区D 1 和反应蒸馏区RD 2 集成在单个反应蒸馏塔RDK中。 < / ListItem>

著录项

  • 公开/公告号US2008164138A1

    专利类型

  • 公开/公告日2008-07-10

    原文格式PDF

  • 申请/专利权人 THOMAS HILL;CHRISTIAN MILLER;

    申请/专利号US20060910028

  • 发明设计人 THOMAS HILL;CHRISTIAN MILLER;

    申请日2006-03-22

  • 分类号B01D3/34;

  • 国家 US

  • 入库时间 2022-08-21 20:12:14

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