利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

66 条记录 (耗时 0.033 秒)

    Fluid mixing device
    1.
    发明授权
    Fluid mixing device 失效
    流体混合装置

    公开(公告)号：US4019719A

    公开(公告)日：1977-04-26

    申请号：US672612

    申请日：1976-04-01

    申请人： Hans H. Schuster ,  Peter Zehner

    发明人： Hans H. Schuster ,  Peter Zehner

    IPC分类号： B01F5/00 ,  B01F5/06

    CPC分类号： B01F5/0619 ,  B01F5/0617

    摘要： An apparatus for thoroughly mixing components of fluid material and, more particularly, for combining and homogenizing streams of gaseous, liquid and/or granular material by passage through a tube-like conduit which contains a plurality of consecutive mixing elements comprising a set of stationary, angularly disposed flow-deflecting baffles of particular form and configuration which cause a repeated dividing, displacement and recombining of the fluid stream and thereby provide improved radial mixing and approximation of ideal plug flow.

    摘要翻译： 一种用于充分混合流体材料的组分的装置，更具体地说，用于通过穿过包含多个连续混合元件的管状导管来混合和均匀气态，液体和/或颗粒材料流，该装置包括一组静止的， 具有特定形式和构造的角度设置的流动偏转挡板，其导致流体流的重复分割，移位和复合，从而提供理想的塞流量的改进的径向混合和近似。

    PROCESS FOR PREPARING ISOCYANATES
    3.
    发明申请
    PROCESS FOR PREPARING ISOCYANATES 有权
    制备异氰酸酯的方法

    公开(公告)号：US20120172621A1

    公开(公告)日：2012-07-05

    申请号：US13394647

    申请日：2010-09-09

    申请人： Torsten Mattke ,  Matthias Kloetzer ,  Eckhard Stroefer ,  Bernhard Geissler ,  Peter Zehner

    发明人： Torsten Mattke ,  Matthias Kloetzer ,  Eckhard Stroefer ,  Bernhard Geissler ,  Peter Zehner

    IPC分类号： C07C263/06

    CPC分类号： C07C263/04 ,  C07C263/06 ,  C07C265/14

    摘要： The invention relates to a multistage process for the continuous preparation of organic, distillable polyisocyanates, preferably diisocyanates, particularly preferably aliphatic or cycloaliphatic diisocyanates, by reaction of the corresponding organic polyamines with carbonic acid derivatives and alcohols to form low molecular weight monomeric polyurethanes and thermal dissociation of the latter, in which the polyisocyanates produced and unusable residues are separated off at particular stages of the reaction and reusable by-products and intermediates are recirculated to preceding stages.

    摘要翻译： 本发明涉及通过相应的有机多胺与碳酸衍生物和醇的反应连续制备有机，可蒸馏的多异氰酸酯，优选二异氰酸酯，特别优选脂族或脂环族二异氰酸酯的多级方法，以形成低分子量单体聚氨酯和热解离 其中多异氰酸酯产生和不可用的残余物在反应的特定阶段被分离，并且可重复使用的副产物和中间体再循环到前面的阶段。

    Hydroformylation
    7.
    发明授权
    Hydroformylation 有权
    加氢甲酰化

    公开(公告)号：US07351384B2

    公开(公告)日：2008-04-01

    申请号：US11218532

    申请日：2005-09-06

    申请人： Peter Zehner ,  Michael Nilles

    发明人： Peter Zehner ,  Michael Nilles

    IPC分类号： B01J10/00 ,  B01J19/00

    CPC分类号： C07C45/50 ,  B01J19/006 ,  B01J19/2435 ,  B01J19/246 ,  B01J2219/00033 ,  B01J2219/00083 ,  B01J2219/00108 ,  B01J2219/0011 ,  B01J2219/00182 ,  B01J2219/00777 ,  C07C47/12

    摘要： Olefins having at least 6 carbon atoms are bydroformylated in the presence of a homogenous catalyst in a continuous process in which a) a vertical tall cylindrical reactor (1) whose interior space is divided by means of internals (2). into at least two reaction chambers which extend essentially in the longitudinal direction of the reactor is used, b) at least one olefin is introduced into the reactor together with synthesis gas at the lower end of the first reaction chamber, c) a partially reacted reaction mixture is conveyed from the upper end of a reaction chamber to the lower end of a next reaction chamber; and d) the hydroformylated olefin is taken off at the upper end of the last reaction chamber. The process allows a high conversion at a given reactor volume.

    摘要翻译： 具有至少6个碳原子的烯烃在连续过程中在均匀催化剂存在下加氢甲酰化，其中a）垂直的高柱形反应器（1），其内部空间通过内件（2）分成至少两个反应室 使用基本上在反应器的纵向延伸的方法，b）至少一种烯烃与第一反应室下端的合成气一起引入反应器，c）部分反应的反应混合物从上部 反应室的末端到下一个反应室的下端; 和d）加氢甲酰化烯烃在最后反应室的上端取出。 该方法允许在给定反应器体积下的高转化率。

    Method for producing oligomers
    8.
    发明授权
    Method for producing oligomers 失效
    生产低聚物的方法

    公开(公告)号：US06852898B2

    公开(公告)日：2005-02-08

    申请号：US10221168

    申请日：2001-03-22

    申请人： Ralf Schulz ,  Thomas Heidemann ,  Peter Schwab ,  Peter Zehner

    发明人： Ralf Schulz ,  Thomas Heidemann ,  Peter Schwab ,  Peter Zehner

    IPC分类号： B01J19/24 ,  C07B61/00 ,  C07C2/08 ,  C07C2/10 ,  C07C2/24 ,  C07C11/02 ,  C07C2/06

    CPC分类号： C07C2/10 ,  B01J19/2465 ,  C07C2/08

    摘要： In a process for preparing essentially unbranched oligomers of alkenes having from 4 to 6 carbon atoms starting from the alkenes or a hydrocarbon stream comprising such alkenes over a nickel-containing heterogeneous catalyst in an adiabatically operated reactor at from 20 to 300° C. and pressures of from 1 to 100 bar, a first substream of the output from the reactor is worked up to isolate the oligomers and the second substream is recirculated together with fresh alkene or a fresh hydrocarbon stream comprising such alkenes to the reactor.

    摘要翻译： 在从20-300℃绝热操作的反应器中，在烯烃或含有这种烯烃的含烃非均相催化剂的基础上制备基本上未分支的具有4-6个碳原子的烯烃低聚物的方法， 1至100巴，将来自反应器的输出的第一子流排除以分离低聚物，并将第二子流与新鲜的烯烃或包含这种烯烃的新鲜烃物流一起再循环到反应器中。

    Reactor for carrying out gas-liquid, liquid, liquid-liquid or gas-liquid-solid chemical reactions
    9.
    发明授权
    Reactor for carrying out gas-liquid, liquid, liquid-liquid or gas-liquid-solid chemical reactions 失效
    用于进行气液，液体，液体或液体 - 液体 - 固体化学反应的反应器

    公开(公告)号：US06838061B1

    公开(公告)日：2005-01-04

    申请号：US09831402

    申请日：1999-11-23

    申请人： Stefan Berg ,  Peter Zehner ,  Regina Benfer ,  Jörn Müller ,  Michael Nilles ,  Ralf Schulz ,  Dieter Stützer

    发明人： Stefan Berg ,  Peter Zehner ,  Regina Benfer ,  Jörn Müller ,  Michael Nilles ,  Ralf Schulz ,  Dieter Stützer

    IPC分类号： B01J8/22 ,  B01J10/00 ,  B01J19/00 ,  B01J19/24 ,  B01J19/26 ,  C07B61/00 ,  C07C45/72 ,  C07C51/235 ,  C07C53/122 ,  F28D7/00

    CPC分类号： C07C45/72 ,  B01J8/226 ,  B01J8/228 ,  B01J10/002 ,  B01J19/006 ,  B01J19/246 ,  B01J19/2465 ,  B01J2208/00123 ,  B01J2219/00078 ,  B01J2219/00777

    摘要： A reactor (1) of high cylindrical construction for continuously carrying out gas-liquid, liquid-liquid or gas-liquid-solid reactions, provided with a downward-directed jet nozzle (2) via which the starting materials and the reaction mixture are fed in and which is located in the upper region of the reactor, and provided with an offtake (3), preferably in the lower region of the reactor, via which the reaction mixture is conveyed via an external circuit back to the jet nozzle (2) by means of a pump (P), wherein a guide tube (4) which extends essentially over the total length of the reactor (1) with the exception of the reactor ends and has a cross-sectional area in the range from one tenth to one half of the cross-sectional area of the reactor (1) is located concentrically in the reactor (1), and the jet nozzle (2) is located above the upper end of the guide tube (4), preferably at a distance of from one eighth of the guide tube diameter to one guide tube diameter, or projects into the guide tube (4) to a depth up to a plurality of guide tube diameters is proposed. A heat exchanger, in particular a heat exchanger having heat exchange tubes (6), preferably running parallel to the guide tube, welded in between plates (5), is integrated into the annular space.

    摘要翻译： 一种高筒形结构的反应器（1），用于连续地进行气液，液 - 液或气 - 液 - 固反应，设有向下的喷射喷嘴（2），原料和反应混合物通过该喷嘴 并且其位于反应器的上部区域中，并且优选地在反应器的下部区域中设置有出料口（3），经由该反应混合物经由外部回路将反应混合物输送回到喷嘴（2） 通过泵（P），其中除了反应器端部之外基本上延伸到反应器（1）的总长度上的导管（4），并且横截面积在十分之一到 反应器（1）的横截面积的一半是同心地位于反应器（1）中，并且喷嘴（2）位于导管（4）的上端之上，优选距离 从引导管直径的八分之一到一个导管直径，或投入到 引导管（4）的深度达到多个导管直径。 热交换器，特别是具有焊接在板（5）之间的平行于引导管的热交换管（6）的换热器（6）整合到环形空间中。