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    VERFAHREN ZUR HERSTELLUNG VON CYCLOHEXAN MIT AUS EINEM STEAMCRACKVERFAHREN STAMMENDEN AUSGANGSMATERIALIEN
    13.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON CYCLOHEXAN MIT AUS EINEM STEAMCRACKVERFAHREN STAMMENDEN AUSGANGSMATERIALIEN 有权
    用于生产用蒸汽CYCLOHEXANE从裂缝过程中获得起始物

    公开(公告)号：EP2909159A2

    公开(公告)日：2015-08-26

    申请号：EP13776829.7

    申请日：2013-10-16

    Applicant: BASF SE

    Inventor： TSCHIRSCHWITZ, Steffen ,  WISSEL-STOLL, Kathrin ,  BÜRKLE, Jochen ,  KOSTOVA, Albena ,  SCHMITT, Markus ,  WLOKA, Veronika ,  DEUERLEIN, Stephan ,  BOSCH, Marco ,  OEHLENSCHLÄGER, Steffen ,  SCHREIBER, Michael ,  AVERLANT, Gauthier Luc Maurice ,  JONI, Joni ,  PROCHAZKA, Roman ,  BOCK, Martin ,  KINDLER, Alois ,  MALKOWSKY, Daniela ,  SPUHL, Katharina ,  BITTERLICH, Stefan ,  PFEIFFER, Daniel

    IPC: C07C5/29 ,  C07C13/18

    CPC classification number: C07C5/10 ,  C07C5/29 ,  C07C2523/755 ,  C07C2527/125 ,  C07C2601/14 ,  C07C13/18

    Abstract: The invention relates to a method for producing cyclohexane by isomerizing a hydrocarbon mixture (KG1) containing methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. A flow (S1) originating from a steam cracking process is used as a starting material. The hydrocarbon mixture (KG1) is obtained from said stream (S1) in a device for removing aromatics. The hydrocarbon mixture has a reduced aromatic content in comparison with the flow (S1). (KG1) can also be (nearly) free of aromatics. In dependence on the type and amount of the aromatics remaining in the hydrocarbon mixture (KG1), in particular if benzene is present, a hydrogenation of (KG1) additionally can be performed before the isomerization. Furthermore, additional purification steps can optionally be performed before or after the isomerization or hydrogenation in dependence on the presence of other components of (KG1). Preferably high-purity cyclohexane (in accordance with specifications) is isolated from the hydrocarbon mixture (KG2) arising during the isomerization, wherein the specifications are given, for example, by the use of the cyclohexane for the production of caprolactam known to the person skilled in the art.

    Abstract translation: 本发明涉及一种通过含异构化在催化剂的存在下的烃混合物（KG1）甲基环戊烷（MCP）生产环己烷。 催化剂较好是在酸性离子液体。 从蒸汽裂解过程的流程（S1）源自被用作起始材料。 烃混合物（KG1）从所述流（S1）在一个设备中获得用于除去芳族化合物。 烃混合物具有与所述流（S1）相比较减少的芳族含量。 因此（KG1）可以（几乎）不含芳香烃。 在剩余在烃混合物（KG1）的芳族化合物的类型和量的依赖性，特别是如果是苯存在的（KG1）氢化另外可在异构化之前进行。 进一步，另外的纯化步骤可任选的异构化或氢化之前或之后执行。在依赖（KG1）的其它组分的存在。 优选高纯度的环己烷（与规格雅舞蹈）从烃混合物（KG 2）的异构化，worin规格中给出，对于实施例中所产生，通过使用环己烷为已知的本领域技术人员生产己内酰胺的分离 的技术人员。

    VERFAHREN ZUR AUFARBEITUNG EINES BUTEN- UND/ODER BUTADIEN ENTHALTENDEN STOFFSTROMS
    15.
    发明公开
    VERFAHREN ZUR AUFARBEITUNG EINES BUTEN- UND/ODER BUTADIEN ENTHALTENDEN STOFFSTROMS 有权
    VERFAHREN ZUR AUFARBEITUNG EINES BUTEN - UND / ODER BUTADIEN ENTHALTENDEN STOFFSTROMS

    公开(公告)号：EP2681178A1

    公开(公告)日：2014-01-08

    申请号：EP12706605.8

    申请日：2012-03-02

    Applicant: BASF SE

    Inventor： KOSTOVA, Albena ,  BENFER, Regina ,  GÖTZ, Jochen ,  REZAI, Alireza ,  MORILLO, Aristides ,  OLBERT, Gerhard ,  PFAB, Peter ,  KOLIOS, Grigorios ,  WEBER, Markus ,  WECK, Alexander

    IPC: C07C7/04 ,  C07C7/08 ,  C07C7/11 ,  C07C11/08 ,  C07C11/167 ,  C07C9/10

    CPC classification number: B01D3/40 ,  C07C7/04 ,  C07C7/08 ,  C07C7/11 ,  C07C11/16 ,  C07C11/167

    Abstract: The invention relates to a process for workup of a stream (1) comprising butene and/or butadiene, butane, hydrogen and/or nitrogen and carbon dioxide, comprising the following steps: (a) absorption of the stream (1) comprising butene and/or butadiene, butane, hydrogen and/or nitrogen, with or without carbon dioxide, with a mixture (5) comprising 80 to 97% by weight of N-methylpyrrolidone and 3 to 20% by weight of water to obtain a stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, and a stream (7) comprising hydrogen and/or nitrogen and butane, (b) extractive distillation of the stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, with a stream (13) comprising 80 to 97% by weight of N-methylpyrrolidone and 3 to 20% by weight of water to separate the stream (9) comprising N-methylpyrrolidone, water, butene and/or butadiene, and butane, with or without carbon dioxide, into a stream (17) comprising N-methylpyrrolidone, water, butene and/or butadiene, and a stream (15) comprising essentially butane, with or without carbon dioxide, (c) distillation of the stream (17) comprising N-methylpyrrolidone, water, butene and/or butadiene into a stream (23) comprising essentially N-methylpyrrolidone and water, and a stream (21) comprising butene and/or butadiene.

    Abstract translation: 本发明涉及包含丁烯和/或丁二烯，丁烷，氢气和/或氮气和二氧化碳的物流（1）的处理方法，其包括以下步骤：（a）将包含丁烯和 （5）包含80-97重量％的N-甲基吡咯烷酮和3-20重量％的水以获得流（9），所述混合物（5）包含具有或不具有二氧化碳的丁二烯，丁烷，氢和/ ）包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷（含有或不含二氧化碳）以及包含氢和/或氮和丁烷的物流（7），（b）物流（9）的萃取蒸馏包含 （13）包含80-97重量％的N-甲基吡咯烷酮和3-20重量％的水以分离含有或不含二氧化碳的N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷， 包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯和丁烷的物流（9），有或没有汽车 （17），包含N-甲基吡咯烷酮，水，丁烯和/或丁二烯，以及基本上包含丁烷的物流（15），其中含有或不含有二氧化碳，（c）蒸馏包含N （23）和包含丁烯和/或丁二烯的物流（21），所述物流（23）基本上包含N-甲基吡咯烷酮和水。

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