FLOW REACTOR OF NONEQUILIBRIUM OPEN TYPE
    242.
    发明公开
    FLOW REACTOR OF NONEQUILIBRIUM OPEN TYPE 审中-公开
    NICHT EKILIBRIERTER DURCHFLUSSREAKTOR OFFENEN TYPS

    公开(公告)号:EP1161982A4

    公开(公告)日:2004-12-29

    申请号:EP00902066

    申请日:2000-02-03

    Inventor: MATSUNO KOICHIRO

    Abstract: A flow reactor for liquid-phase polymerization reactions. A liquid reaction mixture containing organic reactant molecules to be polymerized is jetted into a low-temperature high-pressure part (B) from a high-temperature high-pressure part (A) through a circulation line (C) to inhibit the polymer yielded in the part (A) from decomposing in the part (B). The polymer is sent to the part (A) through a circulation line (C) to further cause polymerization. This cycle is repeated. Thus, a reaction such as amino acid polymerization can be conducted in a nonequilibrium open system while regulating the degree of polymerization by controlling polymerization and decomposition.

    Abstract translation: 用于液相聚合反应的流动反应器。 将含有待聚合的有机反应物分子的液体反应混合物从高温高压部分(A)通过循环管线(C)喷射到低温高压部分(B)中以抑制在高温高压部分 部分(A)在部分(B)中分解。 聚合物通过循环管线(C)送入部分(A)以进一步引起聚合。 这个循环重复进行。 因此,可以在非平衡开放系统中进行氨基酸聚合等反应,同时通过控制聚合和分解来调节聚合度。

    VERFAHREN ZUR CHEMOTHERMISCHEN UMSETZUNG FLIESSFÄHIGER VERBINDUNGEN UND KONVERTER ZUR DURCHFÜHRUNG DES VERFAHRENS
    249.
    发明公开
    VERFAHREN ZUR CHEMOTHERMISCHEN UMSETZUNG FLIESSFÄHIGER VERBINDUNGEN UND KONVERTER ZUR DURCHFÜHRUNG DES VERFAHRENS 失效
    对于热CHEMO实施FLOWABLE化合物和转炉方法用于执行该方法

    公开(公告)号:EP0814901A1

    公开(公告)日:1998-01-07

    申请号:EP95912255.0

    申请日:1995-03-20

    CPC classification number: B01J12/005 B01J3/00 F23G7/008 F23G7/065

    Abstract: A process for thermochemically converting fluid or fluidisable compounds (charge), in particular organic or complex toxic compounds, into low-molecular organic or inorganic compounds, has a preliminary step, during which the energy required for the conversion reaction is generated, and at least one subsequent main step during which the conversion reaction takes place. In the preliminary step, the reaction partners that are subjected to an overpressure and form an exothermic mixture are completely mixed during a mixing phase without being able to react during the mixing phase. Only at the end of the mixing phase both reaction partners react with a high reaction speed and energy density that depend on the overpressure. During the main step of the process, a second mixture to be reacted that consists of the charge and of a reactive receives the energy required for the reaction by being mixed with the reaction products from the first partial reaction that are in a high temperature and pressure state.

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