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    PROCESS FOR PREPARING POROUS METAL ORGANIC FRAMEWORKS
    1.
    发明申请
    PROCESS FOR PREPARING POROUS METAL ORGANIC FRAMEWORKS 审中-公开
    用于生产多孔金属有机骨架

    公开(公告)号：WO2007131948A3

    公开(公告)日：2008-02-07

    申请号：PCT/EP2007054554

    申请日：2007-05-11

    Applicant: BASF AG ,  PUETTER HERMANN ,  SCHUBERT MARKUS ,  RICHTER INGO ,  MUELLER ULRICH ,  TRUKHAN NATALIA

    Inventor： PUETTER HERMANN ,  SCHUBERT MARKUS ,  RICHTER INGO ,  MUELLER ULRICH ,  TRUKHAN NATALIA

    IPC: C25B3/12

    CPC classification number: C25B3/12

    Abstract: The present invention relates to a process for preparing a porous metal organic framework comprising at least two organic compounds coordinated to at least one metal ion, which comprises the steps (a) oxidation of at least one anode containing metal corresponding to the at least one metal ion in a reaction medium in the presence of at least a first organic compound, where the first organic compound is an optionally substituted monocyclic, bicyclic or polycyclic saturated or unsaturated hydrocarbon in which at least two ring carbons are replaced by heteroatoms selected from the group consisting of N, O and S, to form a reaction intermediate containing at least one metal ion and the first organic compound; and (b) reaction of the reaction intermediate at a prescribed temperature with an at least second organic compound which coordinates to the at least one metal ion, where the second organic compound is derived from a dicarboxylic, tricarboxylic or tetracarboxylic acid.

    Abstract translation: 本发明涉及一种用于制备包含配位的至少两个的至少一种金属有机化合物，包括（a）氧化中的至少一种的存在下相应的含有金属的阳极中的反应介质中的至少一种金属离子的至少之一中的步骤的多孔金属有机骨架 第一有机化合物，其中所述第一有机化合物和任选取代的单 - ，双 - 或多环饱和或未饱和烃基，其中至少两个环碳原子被选自下组的杂原子取代由选自N，O和S的取代， 形成所述至少一个金属离子和第一含有机化合物的中间体反应产物; 和（b）反应，该反应与至少其协调结合到所述至少一种金属离子，其中，二，三或四羧酸的第二有机化合物导出的第二有机化合物中间体在设定温度。

    SUPPORTED CATALYST COMPRISING DELTA- OR THETA-MODIFIED ALUMINIUM OXIDE SUPPORTS
    3.
    发明申请
    SUPPORTED CATALYST COMPRISING DELTA- OR THETA-MODIFIED ALUMINIUM OXIDE SUPPORTS 审中-公开
    在DELTA THETA或修改铝承运商的支持催化剂

    公开(公告)号：WO2005082526A2

    公开(公告)日：2005-09-09

    申请号：PCT/EP2005001914

    申请日：2005-02-24

    Applicant: BASF AG ,  SCHUBERT MARKUS ,  STEPHAN JUERGEN ,  BOEHM VOLKER ,  BRODHAGEN ANDREAS ,  POPLOW FRANK

    Inventor： SCHUBERT MARKUS ,  STEPHAN JUERGEN ,  BOEHM VOLKER ,  BRODHAGEN ANDREAS ,  POPLOW FRANK

    IPC: B01J21/04 ,  B01J23/36 ,  B01J32/00 ,  B01J35/00 ,  B01J35/10 ,  B01J37/08 ,  C07C5/333 ,  C10G45/00

    CPC classification number: B01J21/04 ,  B01J23/36 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1042 ,  B01J35/1061 ,  B01J37/08 ,  C07C5/333 ,  C10G45/00 ,  C07C11/08 ,  C07C11/02

    Abstract: The invention relates to a method for producing a supported catalyst, consisting of at least 75 wt. % Al2O3, whose delta- or theta-modified fraction of Al2O3 is at least 1 % of the total Al2O3 fraction and which contains a rhenium compound and optionally a promoter as the active component (A). According to the invention: a) a modified support (T) is produced from a conventional support (T) consisting of at least 75 wt. % of Al2O3, to which a promoter is optionally applied, the delta- or theta-modified fraction of the Al2O3 being at least 1 % of the total Al2O3 fraction, by the calcination of the conventional support (T) at a temperature of between 750 and 1100 DEG C; b) a supported catalyst precursor is produced from the modified support (T) by the application of the active component comprising the rhenium compound (A) to the modified support (T); and c) the supported catalyst precursor is calcinated at a temperature of between 500 and 750 DEG C.

    Abstract translation: 一种用于制备包括至少75重量％的担载催化剂过程.-氧化铝，氧化铝中的δ或θ修改的内容，的％，基于对Al2O3的量为至少1％，和铼化合物，和任选的 启动子含有作为活性成分（a），该方法包括从一个共同的载体（T），其由至少75重量的Al2O3％和在其上任选地施加的启动子制备），得到一种改性载体（T），其 在δ或θ变形例中，基于对Al2O3的量的Al2O3含量为至少1％的在750〜1100℃的温度下从改性载体T（b）煅烧所述载体通常（T）， ）在500〜750℃的温度下的改性载体（T）的活性成分（a），包括在施加所述铼化合物和c）负载催化剂前体上制备由煅烧的载体催化剂前体。

    STORAGE OF ACETYLENE-CONTAINING GASES BY MEANS OF METAL-ORGANIC FRAMEWORK MATERIALS
    5.
    发明申请
    STORAGE OF ACETYLENE-CONTAINING GASES BY MEANS OF METAL-ORGANIC FRAMEWORK MATERIALS 审中-公开
    乙炔气体的STORAGE使用金属有机骨架

    公开(公告)号：WO2008000694A3

    公开(公告)日：2008-02-28

    申请号：PCT/EP2007056231

    申请日：2007-06-22

    Applicant: BASF AG ,  SCHUBERT MARKUS ,  MUELLER ULRICH ,  PASTRE JOERG ,  SCHIERLE-ARNDT KERSTIN ,  TRILLER MICHAEL

    Inventor： SCHUBERT MARKUS ,  MUELLER ULRICH ,  PASTRE JOERG ,  SCHIERLE-ARNDT KERSTIN ,  TRILLER MICHAEL

    IPC: B01J20/22 ,  B01J20/28 ,  B01J31/16 ,  F17C11/00

    CPC classification number: F17C11/002 ,  B01J20/226

    Abstract: The invention relates to methods for storing an acetylene-containing gas in a porous metal-organic framework material, said metal-organic framework material containing at least one, at least bidentate compound that is coordinately bound to at least one metal ion. The method according to the invention comprises the step of contacting the acetylene-containing gas with the metal-organic framework material, the metal-organic framework material being copper-free. The invention also relates to a porous metal-organic framework material which contains the acetylene-containing gas and to a corresponding acetylene gas-pressure container and the use thereof.

    Abstract translation: 本发明涉及到用于存储含乙炔的气体到多孔金属 - 有机骨架材料的方法中，有机金属骨架材料含有至少一种配位到至少一种金属，至少双齿有机化合物，含所述含乙炔气体与金属 - 有机骨架材料相接触的步骤， 其中所述金属 - 有机骨架材料是不含铜。 此外，本发明涉及一种多孔金属有机骨架材料，含乙炔的含有和相应的乙炔气体的压力容器，以及它们的用途的气体。

    METHOD FOR PRODUCING PROPENE FROM PROPANE
    6.
    发明申请
    METHOD FOR PRODUCING PROPENE FROM PROPANE 审中-公开
    用于生产丙烯丙烷

    公开(公告)号：WO2007113085A3

    公开(公告)日：2008-03-13

    申请号：PCT/EP2007052354

    申请日：2007-03-13

    Applicant: BASF AG ,  SCHUBERT MARKUS ,  MUELLER ULRICH ,  KIENER CHRISTOPH ,  TEICH FRIEDHELM ,  CRONE SVEN ,  SIMON FALK ,  PASTRE JOERG

    Inventor： SCHUBERT MARKUS ,  MUELLER ULRICH ,  KIENER CHRISTOPH ,  TEICH FRIEDHELM ,  CRONE SVEN ,  SIMON FALK ,  PASTRE JOERG

    IPC: C07C7/12 ,  C07C7/13

    CPC classification number: C07C5/333 ,  C07C7/12 ,  C07C7/13 ,  C07C11/06

    Abstract: The invention relates to a method for producing propene from propane. Said method comprises the following steps: A) a feed gas stream (a) containing propane is prepared; B) the feed gas stream (a) containing propane, is introduced with optionally water vapour and optionally, an oxygen-containing gas stream into a dehydrogenation zone and then the propane is dehydrogenated to form propene, and a product gas stream (b) containing propane, propene, methane, ethane, ethene, hydrogen, optionally carbon monoxide, carbon dioxide, water vapour and oxygen, is obtained; C) the product gas stream (b) is cooled, optionally compressed and then water vapour is separated by condensation and a product gas stream (c) depleted in water vapour is obtained; D) the product gas stream (c) is brought into contact with a selectively active adsorber which selectively adsorbs propene in the selected adsorption conditions, and an adsorber charged with propene and a gas stream (d2) depleted in propene and containing propane, methane, ethane, ethene and hydrogen, carbon monoxide and carbon dioxide are obtained; E) a gas stream (e1) containing propene is released from the adsorber charged with propene by reducing the pressure and/or heat of the adsorber.

    Abstract translation: 本发明涉及用于由丙烷制备丙烯的方法，包括步骤：A）（a）中，提供了一种含丙烷的原料气流; B）包含（a），任选的蒸汽和任选的含氧气体流中的丙烷进料气流被送入脱氢区和丙烷经受脱氢成丙烯，得到产物气流b包括丙烷，丙烯，甲烷，乙烷，乙烯，氢气，任选的一氧化碳 ，二氧化碳，获得水蒸汽和氧气; C）的产物气流（B）被冷却，冷凝，任选地，这将允许水蒸气通过冷凝分离，得到一个蒸汽贫化产物气流（获得的C）; D）的产物气流（c）的具有选择性作用的吸附剂选择性吸附所选择的吸附条件下丙烯，与一个装有丙烯吸附剂和贫丙烯气流（D2）的包含丙烷，甲烷，乙烷，乙烯接触接触 和氢，得到一氧化碳和二氧化碳; E）从载有丙烯吸附剂通过减压和/或吸附剂的加热，气体流包含丙烯（E1）释放。

    TWO-STAGE METHOD FOR PRODUCING BUTANDIOL IN TWO REACTORS
    8.
    发明申请
    TWO-STAGE METHOD FOR PRODUCING BUTANDIOL IN TWO REACTORS 审中-公开
    两步反应器制备丁醇的两步法

    公开(公告)号：WO03104214A8

    公开(公告)日：2004-05-13

    申请号：PCT/EP0306060

    申请日：2003-06-10

    Applicant: BASF AG ,  HESSE MICHAEL ,  SCHLITTER STEPHAN ,  BORCHERT HOLGER ,  SCHUBERT MARKUS ,  ROESCH MARKUS ,  BOTTKE NILS ,  FISCHER ROLF-HARTMUTH ,  WECK ALEXANDER ,  WINDECKER GUNTHER ,  HEYDRICH GUNNAR

    Inventor： HESSE MICHAEL ,  SCHLITTER STEPHAN ,  BORCHERT HOLGER ,  SCHUBERT MARKUS ,  ROESCH MARKUS ,  BOTTKE NILS ,  FISCHER ROLF-HARTMUTH ,  WECK ALEXANDER ,  WINDECKER GUNTHER ,  HEYDRICH GUNNAR

    IPC: C07C29/149 ,  C07D315/00 ,  C07C31/20 ,  C07D307/20

    CPC classification number: C07D315/00 ,  C07C29/149 ,  C07C31/207

    Abstract: The invention relates to a method for producing optionally akyl-substituted 1,4-butandiol by two-stage catalytic hydration in the gaseous phase of C4 dicarboxylic acids and/or the derivatives thereof with the steps of: a) introducing a gaseous flow of a C4 dicarboxylic acid or a derivative thereof at 200 to 300 °C and 2 to 60 bar in a first reactor and catalytic gas phase hydration to a mainly optionally alkyl-substituted gamma-butyrolactone containing product; b) introducing the product flow so obtained into a second reactor at a temperature of from 150 °C to 240 °C and a pressure of from 15 to 100 bar and catalytic gas phase hydration to optionally alkyl-substituted 1,4-butandiol; c) removing the desired product from the intermediates, byproducts and possibly not reacted educt; d) optionally returning non-reacted intermediates to one or both hydration stages, whereby in both hydration stages one catalyst each is used which comprises = 5 % by weight, preferably 5 to 95 % by weight, especially 20 to 90 % by weight of an oxidic carrier, the pressure prevailing in the second reactor is higher than in the first reactor, and the product mixture removed from the first reactor is introduced into the second reactor without further purifying it.

    Abstract translation: 本发明涉及一种用于在C4二羧酸和/或其衍生物，包括以下步骤的气相制备任选被烷基取代的1,4-丁二醇，通过两阶段催化氢化：a）将C4二羧酸的气体流或它们的衍生物 在200〜300℃和2至在第一反应器和催化气相加氢在含有产物主要为任选被烷基取代的γ-丁内酯60巴; b）将由此获得进入第二反应器在150℃的温度至240℃的产品流和15至100巴和催化气相任选烷基取代的1,4-丁二醇的压力; c）从中间体，副产物和任选未反应的离析物中分离所需产物; d）任选地回收未转化的中间体在一个或两个氢化阶段，其中，在每种情况下，催化剂在两个氢化中使用的<= 95重量％，优选为5〜95重量％，特别是10至80重量％的CuO 和> = 5具有重量％，优选为5〜95重量％，特别是20至90重量的氧化载体的％，在第二反应器更高的压力占优势比在第一反应器和与第一反应器的产物混合物将取出的 不经进一步纯化而引入第二反应器中。

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