利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

73 条记录 (耗时 0.028 秒)

    Process for preparing acetylene by the Sachsse-Bartholomé process
    6.
    发明授权
    Process for preparing acetylene by the Sachsse-Bartholomé process 有权
    通过Sachsse-Bartholomé工艺制备乙炔的方法

    公开(公告)号：US08975460B2

    公开(公告)日：2015-03-10

    申请号：US13183683

    申请日：2011-07-15

    申请人： Lucia Königsmann ,  Maximilian Vicari ,  Thomas Heidemann ,  Dirk Groβschmidt ,  Jürgen Michel

    发明人： Lucia Königsmann ,  Maximilian Vicari ,  Thomas Heidemann ,  Dirk Groβschmidt ,  Jürgen Michel

    IPC分类号： C07C5/02 ,  C07C5/03 ,  C07C2/78

    CPC分类号： C07C2/78 ,  C07C11/24

    摘要： A process is proposed for preparing acetylene by the Sachsse-Bartholomé process by combustion of a natural gas/oxygen mixture in one or more burners to obtain a cracking gas which is cooled in two or more stages in burner columns, each burner having one or more burner columns assigned thereto, and said cracking gas being quenched with pyrolysis oil in the first cooling stage, to obtain a low boiler fraction comprising benzene, toluene and xylene from the one or more burner columns, which is cooled with direct cooling water and separated in a phase separator into an aqueous phase and an organic phase which comprises benzene, toluene and xylene and is fully or partly introduced to the top of the one or more burner columns as a return stream, wherein the organic phase comprising benzene, toluene and xylene from the phase separator, prior to full or partial recycling to the top of the one or more burner columns, is supplied to a selective hydrogenation over a catalyst which comprises at least one platinum group metal on an inorganic metal oxide as support, comprising 0.05 to 5% by weight of platinum group metal, based on the total weight of the catalyst, and wherein the selective hydrogenation is performed at a pressure in the range from 10 to 70 bar gauge and a temperature in the range from 0 to 100° C.

    摘要翻译： 提出了一种通过Sachsse-Bartholomé方法通过在一个或多个燃烧器中燃烧天然气/氧气混合物来制备乙炔的方法，以获得在燃烧器柱中两级或更多级冷却的裂化气体，每个燃烧器具有一个或多个 燃烧器列，并且在第一冷却阶段，所述裂解气体用热解油淬火，以从一个或多个燃烧器柱获得包含苯，甲苯和二甲苯的低沸点馏分，其用直接冷却水冷却并分离 相分离器进入水相和有机相，其包含苯，甲苯和二甲苯，并作为回流完全或部分地引入到一个或多个燃烧器塔的顶部，其中有机相包含苯，甲苯和二甲苯 在完全或部分再循环到一个或多个燃烧器塔的顶部之前，将相分离器供应到催化剂上的选择性氢化，所述催化剂包括在l 在一个无机金属氧化物上的一个铂族金属作为载体，包含0.05-5重量％的铂族金属，基于催化剂的总重量，其中选择性氢化在10〜 70巴规，温度范围为0至100℃。

    PROCESS FOR HYDROGENATING NITRILES
    7.
    发明申请
    PROCESS FOR HYDROGENATING NITRILES 审中-公开
    加氢处理方法

    公开(公告)号：US20120245389A1

    公开(公告)日：2012-09-27

    申请号：US13427308

    申请日：2012-03-22

    申请人： Christof Wilhelm Wigbers ,  Christoph Müller ,  Wolfgang Mägerlein ,  Martin Ernst ,  Thomas Heidemann ,  Johann-Peter Melder ,  Lucia Königsmann ,  Milind Joshi ,  Oliver Bey ,  Bernd Stein

    发明人： Christof Wilhelm Wigbers ,  Christoph Müller ,  Wolfgang Mägerlein ,  Martin Ernst ,  Thomas Heidemann ,  Johann-Peter Melder ,  Lucia Königsmann ,  Milind Joshi ,  Oliver Bey ,  Bernd Stein

    IPC分类号： C07C209/48

    CPC分类号： C07C209/48 ,  C07C2601/14 ,  C07C211/36 ,  C07C211/09

    摘要： The present invention relates to a process for hydrogenating organic nitriles by means of hydrogen in the presence of a catalyst in a reactor, where the shaped body catalyst is arranged in a fixed bed, wherein the shaped body in the shape of spheres or rods has in each case a diameter 3 mm or less, in the shape of tablets a height of 4 mm or less, and in the case of all other geometries in each case has an equivalent diameter L=1/a′ of 0.70 mm or less, where a′ is the external surface area per unit volume (mms2/mmp3), where: a ′ = A p V p , where Ap is the external surface area of the catalyst particle (mms2) and Vp is the volume of the catalyst particle (mmp3). The present invention further relates to a process for preparing downstream products of isophoronediamine (IPDA) or N,N-dimethylaminopropylamine (DMAPA) from amines prepared according to the invention.

    摘要翻译： 本发明涉及一种在反应器中催化剂存在下通过氢气氢化有机腈的方法，其中成形体催化剂布置在固定床中，其中球体或棒状的成形体具有 每个壳体的直径为3mm以下，片状形状为4mm以下，在各种情况下，所有其他几何形状的等效直径L = 1 / a'为0.70mm以下，其中 a'是每单位体积的外表面积（mms2 / mmp3），其中：a'= A p V p，其中Ap是催化剂颗粒的外表面积（mms2），Vp是催化剂颗粒的体积 mmp3）。 本发明还涉及由根据本发明制备的胺制备异佛尔酮二胺（IPDA）或N，N-二甲基氨基丙胺（DMAPA）的下游产物的方法。

    PROCESS FOR PREPARING ACETYLENE BY THE SACHSSE-BARTHOLOME PROCESS
    8.
    发明申请
    PROCESS FOR PREPARING ACETYLENE BY THE SACHSSE-BARTHOLOME PROCESS 有权
    通过SACHSSE-BARTHOLOME工艺制备乙烯的方法

    公开(公告)号：US20120022308A1

    公开(公告)日：2012-01-26

    申请号：US13183683

    申请日：2011-07-15

    申请人： Lucia Königsmann ,  Maximilian Vicari ,  Thomas Heidemann ,  Dirk Großschmidt ,  Jürgen Michel

    发明人： Lucia Königsmann ,  Maximilian Vicari ,  Thomas Heidemann ,  Dirk Großschmidt ,  Jürgen Michel

    IPC分类号： C07C4/22

    CPC分类号： C07C2/78 ,  C07C11/24

    摘要： A process is proposed for preparing acetylene by the Sachsse-Bartholomé process by combustion of a natural gas/oxygen mixture in one or more burners to obtain a cracking gas which is cooled in two or more stages in burner columns, each burner having one or more burner columns assigned thereto, and said cracking gas being quenched with pyrolysis oil in the first cooling stage, to obtain a low boiler fraction comprising benzene, toluene and xylene from the one or more burner columns, which is cooled with direct cooling water and separated in a phase separator into an aqueous phase and an organic phase which comprises benzene, toluene and xylene and is fully or partly introduced to the top of the one or more burner columns as a return stream, wherein the organic phase comprising benzene, toluene and xylene from the phase separator, prior to full or partial recycling to the top of the one or more burner columns, is supplied to a selective hydrogenation over a catalyst which comprises at least one platinum group metal on an inorganic metal oxide as support, comprising 0.05 to 5% by weight of platinum group metal, based on the total weight of the catalyst, and wherein the selective hydrogenation is performed at a pressure in the range from 10 to 70 bar gauge and a temperature in the range from 0 to 100° C.

    摘要翻译： 提出了一种通过Sachsse-Bartholomé方法通过在一个或多个燃烧器中燃烧天然气/氧气混合物来制备乙炔的方法，以获得在燃烧器柱中两级或更多级冷却的裂化气体，每个燃烧器具有一个或多个 燃烧器列，并且在第一冷却阶段，所述裂解气体用热解油淬火，以从一个或多个燃烧器柱获得包含苯，甲苯和二甲苯的低沸点馏分，其用直接冷却水冷却并分离 相分离器进入水相和有机相，其包含苯，甲苯和二甲苯，并作为回流完全或部分地引入到一个或多个燃烧器塔的顶部，其中有机相包含苯，甲苯和二甲苯 在完全或部分再循环到一个或多个燃烧器塔的顶部之前，将相分离器供应到催化剂上的选择性氢化，所述催化剂包括在l 在一个无机金属氧化物上的一个铂族金属作为载体，包含0.05-5重量％的铂族金属，基于催化剂的总重量，其中选择性氢化在10〜 70巴规，温度范围为0至100℃。

    Catalysts and method for the hydroamination of olefins
    10.
    发明授权
    Catalysts and method for the hydroamination of olefins 有权
    烯烃水解催化剂和方法

    公开(公告)号：US08529869B2

    公开(公告)日：2013-09-10

    申请号：US13265457

    申请日：2010-04-19

    申请人： Thomas Heidemann ,  Jens Kehrer

    发明人： Thomas Heidemann ,  Jens Kehrer

    IPC分类号： C01B39/46 ,  C07C209/60

    CPC分类号： B01J29/7057 ,  B01J29/7007 ,  B01J37/0201 ,  B01J2229/186 ,  C07C209/60 ,  C07C211/07

    摘要： The present invention relates to a hydroamination catalyst comprising boron beta zeolites, wherein the hydroamination catalyst is doped with lithium, and also a process for producing it. The present patent application further relates to a process for preparing amines by reaction of ammonia or primary or secondary amines with olefins at elevated temperatures and pressures in the presence of the hydroamination catalyst of the invention.

    摘要翻译： 本发明涉及包含硼沸石的水解催化剂，其中所述水化催化剂掺杂有锂，并且还涉及其生产方法。 本专利申请还涉及在本发明的水解催化剂存在下，在升高的温度和压力下，通过氨或伯胺或仲胺与烯烃的反应来制备胺的方法。