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    • 5. 发明申请
    • TUBE BUNDLE REACTOR FOR NON-CATALYZED OR HOMOGENOUSLY CATALYZED REACTIONS
    • 管式反应器非催化或均匀催化反应
    • WO2010083978A3
    • 2011-01-06
    • PCT/EP2010000280
    • 2010-01-19
    • BASF SETELES JOAQUIM HENRIQUERESCH PETERRUPPEL WILHELMWEGERLE ULRIKEGERLINGER WOLFGANGROESSLER-FEIGEL BEATRICEMEIER ANTONMUELLER CHRISTIAN
    • TELES JOAQUIM HENRIQUERESCH PETERRUPPEL WILHELMWEGERLE ULRIKEGERLINGER WOLFGANGROESSLER-FEIGEL BEATRICEMEIER ANTONMUELLER CHRISTIAN
    • B01J19/24B01J19/00
    • B01J19/2425B01J4/001B01J19/006B01J2219/00085B01J2219/00166F28D7/16F28F9/0265F28F9/0275F28F9/0278Y02P20/582
    • 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.
    • 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。