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    TUBE BUNDLE REACTOR FOR NON-CATALYZED OR HOMOGENOUSLY CATALYZED REACTIONS
    1.
    发明申请
    TUBE BUNDLE REACTOR FOR NON-CATALYZED OR HOMOGENOUSLY CATALYZED REACTIONS 审中-公开
    管式反应器非催化或均匀催化反应

    公开(公告)号：WO2010083978A3

    公开(公告)日：2011-01-06

    申请号：PCT/EP2010000280

    申请日：2010-01-19

    Applicant: BASF SE ,  TELES JOAQUIM HENRIQUE ,  RESCH PETER ,  RUPPEL WILHELM ,  WEGERLE ULRIKE ,  GERLINGER WOLFGANG ,  ROESSLER-FEIGEL BEATRICE ,  MEIER ANTON ,  MUELLER CHRISTIAN

    Inventor： TELES JOAQUIM HENRIQUE ,  RESCH PETER ,  RUPPEL WILHELM ,  WEGERLE ULRIKE ,  GERLINGER WOLFGANG ,  ROESSLER-FEIGEL BEATRICE ,  MEIER ANTON ,  MUELLER CHRISTIAN

    IPC: B01J19/24 ,  B01J19/00

    CPC classification number: B01J19/2425 ,  B01J4/001 ,  B01J19/006 ,  B01J2219/00085 ,  B01J2219/00166 ,  F28D7/16 ,  F28F9/0265 ,  F28F9/0275 ,  F28F9/0278 ,  Y02P20/582

    Abstract: The invention relates to a tube bundle reactor having a flat feed dome. Alternatively, the discharge dome can also be designed flat. The flat design reduces the reaction heat developing in the hood in reaction types that take place not only in the tube bundle (non-catalyzed reactions and reactions with homogenously distributed catalyst). Undesired reactions that already take place in the dome due to accumulated heat are thus heavily suppressed, whereby greater selectivity in temperature-sensitive reactions is achieved. Additionally, the temperature distribution within the domes can be precisely controlled. The tube bundle reactor comprises a tube bundle that has a feed end connected to a feed dome of the tube bundle reactor, wherein the feed dome is designed in a flat shape having a cross-sectional surface at the feed end and an inner volume, and the ratio of the inner volume to the cross-sectional surface is less than 0.35 m. The invention is furthermore implemented by a method for operating a tube bundle reactor, comprising: introducing a reactant mixture into a tube bundle and converting at least a portion of the reactant mixture into a product inside the tube bundle. The introduction step comprises: feeding the reactant mixture into an inner space of a feed dome of the tube bundle reactor and forwarding the reactant mixture into a feed end of the tube bundle in the form of a fluid flow. The fluid flow has a cross-sectional surface upon entering the feed end and the inner space of the feed dome through which the fluid flows has an inner volume; wherein the ratio of the inner volume to the cross-sectional surface is less than 0.35 m.

    Abstract translation: 本发明涉及一种具有平面供应罩管束反应器。 可替换地，放电罩可以制成平的。 扁平设计降低导致反应类型，发生不仅在Rohbündel（未催化的反应和反应以均匀地分布催化剂）罩反应热。 其特征在于，由此更高的选择性与对温度敏感的反应实现的是那些已经在罩发生不希望的反应，由于积热，强烈抑制。 此外，该罩内的温度分布可以被精确地控制。 包括具有进料端，其连接到所述管束反应器的供给罩管束管束反应器中，与在进料端的内部容积的横截面面积和扁平形状的供给罩构造，并且内部容积的横截面面积的比例为小于0， 35米。 引入在管束中的反应物混合物，并且至少在管束内的反应混合物的一部分反应，以一个产品：此外，本发明是通过一种用于操作管束反应器的方法，包括的手段来实现。 放电，其包括：供给所述反应物混合物进入管束反应器的供给罩的内和反应物混合物通入在流体流的形式管束的一个进给端。 流体流动的横截面面积，因为它进入的进料端和通过其流体流流，具有内部容积的供给机罩的内部; 其中内部体积与横截面面积的比例为小于0.35微米。

    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDROGENATION
    4.
    发明专利
    REACTOR FOR CARRYING OUT AUTOTHERMAL GAS-PHASE DEHYDROGENATION 未知

    公开(公告)号：CA2782417A1

    公开(公告)日：2011-06-09

    申请号：CA2782417

    申请日：2010-11-30

    Applicant: BASF SE

    Inventor： KOLIOS GRIGORIOS ,  RUPPEL WILHELM ,  WEGERLE ULRIKE ,  KESSEL JASMINA ,  GERLINGER WOLFGANG ,  MABANDE GODWIN TAFARA PETER ,  SCHINDLER GOETZ-PETER ,  KOSTOVA ALBENA ,  OLBERT GERHARD ,  PFAB PETER

    IPC: B01J19/24

    Abstract: The invention relates to a reactor (1) in the form of a horizontal cylinder for carrying out autothermal gas phase dehydrogenbation of a hydrocarbon-containing gas flow (2) by means of an oxygen-containing gas flow (3), with a reaction mixture being obtained, on a heterogeneous catalyst in the form of a monolith (4), characterized in that the interior of the reactor (1) is divided by a detachable cylindrical or prismatic housing G, which is disposed in the longitudinal direction of the reactor (1), gastight in the circumferential direction and open at both end faces thereof, into an inner area A, having one or a plurality of catalytically active zones (5), in which are provided a packing of monoliths (4) stacked on, adjacent, and above one another, and, in front of each catalytically active zone (5), a mixing zone (6) having fixed installations, and an outer area B disposed coaxially to the inner area A.

    7.
    发明专利
    未知

    公开(公告)号：AT389630T

    公开(公告)日：2008-04-15

    申请号：AT04722160

    申请日：2004-03-20

    Applicant: BASF SE

    Inventor： PETZOLDT JOCHEN ,  DIETERLE MARTIN ,  ARNOLD HEIKO ,  RUPPEL WILHELM ,  MUELLER-ENGEL KLAUS-JOACHIM

    IPC: C07C57/05 ,  C07C51/25

    Abstract: In a process for heterogeneously catalyzed partial gas phase oxidation of propene to acrylic acid, the propene-containing starting reaction gas mixture is oxidized in a first reaction stage using a fixed catalyst bed 1 which consists of a plurality of fixed catalyst bed zones and is accommodated in two successive temperature zones A, B, and the acrolein-containing product gas mixture of the first reaction stage is then oxidized in a second reaction stage using a fixed catalyst bed 2 which consists of a plurality of fixed catalyst bed zones and is accommodated in two successive temperature zones C, D, and the transition from one temperature zone to another temperature zone within one reaction stage does not spatially coincide with a transition from one fixed catalyst bed zone to another fixed catalyst bed zone.

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