首页> 外国专利> Preparation of propene from 2-butene and isobutene rich feed stream comprises contacting 4 carbon hydrocarbon stream with ethene in a metathesis step, and separating the streams

Preparation of propene from 2-butene and isobutene rich feed stream comprises contacting 4 carbon hydrocarbon stream with ethene in a metathesis step, and separating the streams

机译:由富含2-丁烯和异丁烯的进料流制备丙烯的步骤包括在复分解步骤中使4碳氢化合物流与乙烯接触,并分离这些流

摘要

Preparation of an ethene stream (C 2), a propene stream (C 3), an isobutene and optionally a 4C-olefin stream (C 4), a 2-methyl-2-butene and optionally 2-butene stream (C 5), and optionally other hydrocarbons containing stream (C x), optionally several separate components containing streams, comprises contacting a C4-hydrocarbon stream with ethene in a metathesis step; and separating the streams. Preparation of an ethene stream (C 2), a propene stream (C 3), an isobutene and optionally 4C olefin stream (C 4), a 2-methyl-2-butene and optionally 2-butene stream (C 5), and optionally other hydrocarbons containing stream (C x), optionally several separate components containing streams, comprises: (A) a metathesis step, in which a C4-hydrocarbon stream, containing at least 2-butene (15 wt.%), at least isobutene (5 wt.%) and 1-butene (less than 5 wt.%) (feed stream), is contacted with ethene in the presence of usual metathesis catalysts; and (B) separation of the streams (C2, C3, C4 and optionally Cx) from the obtained hydrocarbon stream, with the stream (C5) completely or partially led back to the metathesis step. Independent claims are included for methods for preparing feed stream, comprising subjecting naphtha or other hydrocarbon compounds to steam cracking or fluid catalytic cracking (FCC)-process, or dehydrating butane containing hydrocarbon stream and followed by purifying the obtained C4-olefin-mixture containing isobutene, 2-butene, butadiene, optionally butyne and optionally 1-butene, and removing the obtained stream of C4-olefin-mixture; and removing butadiene and butyne by means of selective hydrogenation to butene or butane hydride, or butadiene and butyne by extractive distillation of the obtained C4-olefin-mixture (raffinate I), where the content of 1,3-butadiene is at a maximum of 1000 wt. ppm.
机译:制备乙烯料流(C 2),丙烯料流(C 3),异丁烯和任选的4C-烯烃料流(C 4),2-甲基-2-丁烯和任选的2-丁烯料流(C 5)以及任选地包含其它烃的物流(C x),任选地包含几个单独的组分的物流,包括在复分解步骤中使C 4-烃物流与乙烯接触;并分开溪流。制备乙烯料流(C 2),丙烯料流(C 3),异丁烯和任选的4C烯烃料流(C 4),2-甲基-2-丁烯和任选的2-丁烯料流(C 5),和任选地包含其他烃的物流(C x),任选地包含物流的几个单独的组分包括:(A)复分解步骤,其中C 4烃物流包含至少2-丁烯(15重量%),至少异丁烯在通常的复分解催化剂的存在下,将5重量%的1-丁烯和小于5重量%的1-丁烯(进料流)与乙烯接触; (B)从获得的烃物流中分离出物流(C2,C3,C4和任选的Cx),其中物流(C5)完全或部分地回到复分解步骤。对于制备进料流的方法包括独立权利要求,所述方法包括使石脑油或其他烃化合物经受蒸汽裂化或流化催化裂化(FCC)过程,或使含丁烷的烃流脱水,然后纯化所获得的含异丁烯的C4-烯烃混合物。 ,2-丁烯,丁二烯,任选的丁炔和任选的1-丁烯,并除去所得的C 4-烯烃混合物流;并通过将所获得的C4-烯烃混合物(萃余液I)进行萃取蒸馏,选择性地氢化成丁烯或氢化丁烷,或丁二烯和丁炔,来除去丁二烯和丁炔,其中1,3-丁二烯的含量最大为1000重量ppm。

著录项

  • 公开/公告号DE102005009665A1

    专利类型

  • 公开/公告日2006-08-31

    原文格式PDF

  • 申请/专利权人 BASF AG;

    申请/专利号DE20051009665

  • 申请日2005-02-28

  • 分类号C07C6/04;C07C11/06;C07C7/12;C07C7/08;

  • 国家 DE

  • 入库时间 2022-08-21 21:20:23

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