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    • 94. 发明申请
    • Method of vapor phase catalytic oxidation using multitubular reactor
    • 使用多管反应器的气相催化氧化方法
    • US20050148793A1
    • 2005-07-07
    • US11064020
    • 2005-02-23
    • Shuhei YadaHirochika HosakaJinno Kimikatsu
    • Shuhei YadaHirochika HosakaJinno Kimikatsu
    • B01J23/88B01J8/06C07B61/00C07C27/14C07C45/28C07C45/33C07C45/35C07C47/22C07C51/00C07C51/21C07C51/215C07C51/235C07C51/25C07C57/05
    • C07C51/215B01J8/067B01J2208/00212B01J2208/00221B01J2208/0023C07C45/33C07C45/35C07C51/00C07C51/252C07C47/22C07C57/04
    • An object of the present invention is to provide a method of vapor phase catalytic oxidation which is capable of: efficiently removing heat of reaction; preventing the formation of hot spots; and efficiently providing a desired product. Provided is a method of vapor phase catalytic oxidation of a substance to be oxidized with a gas containing molecular oxygen by means of a multitubular reactor, the multitubular reactor comprising: a cylindrical reactor shell fitted with a raw material supply port and a product outlet; multiple circular conduits disposed around the cylindrical reactor shell and used to introduce a heat medium into the cylindrical reactor shell or to lead the heat medium out therefrom; a circulation device for connecting the multiple circular conduits to each other; multiple reaction tubes restrained by means of multiple tube plates of the reactor and having a catalyst accommodated therein; and multiple baffles arranged in a longitudinal direction of the reaction tube and used to change a direction of the heat medium introduced into the reactor shell, wherein the method comprises: performing a reaction of vapor phase catalytic oxidation under such conditions that a heat transfer coefficient of the heat medium is 1,000 W/(m2·K) or higher.
    • 本发明的目的是提供一种气相催化氧化方法,其能够有效地除去反应热; 防止热点形成; 并有效地提供期望的产品。 提供了一种通过多管反应器的含有分子氧的气体进行气相催化氧化的方法,所述多管反应器包括:装有原料供应口和产品出口的圆柱形反应器壳; 多个圆形管道设置在圆柱形反应器壳体周围,用于将热介质引入圆柱形反应器壳体中或将热介质从其中引出; 用于将多个圆形导管彼此连接的循环装置; 多个反应管通过反应器的多个管板约束并具有容纳在其中的催化剂; 以及沿反应管的纵向布置的多个挡板,用于改变引入反应器壳体的热介质的方向,其中所述方法包括:在以下条件下进行气相催化氧化反应:在 热介质为1,000W /(m 2·2K)以上。