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    • 2. 发明申请
    • Process and Plant for Ammonia-Urea Production
    • 氨 - 尿素生产过程和工厂
    • US20140018575A1
    • 2014-01-16
    • US14007100
    • 2012-02-10
    • Ermanno FilippiMarco BadanoFrederico ZardiAndrea Scotto
    • Ermanno FilippiMarco BadanoFrederico ZardiAndrea Scotto
    • C07C273/10
    • C07C273/10C01C1/0488Y02P20/52C07C275/02
    • A process for ammonia -urea production where: liquid ammonia produced in an ammonia section is fed to a urea section directly at the ammonia synthesis pressure, and where the liquid ammonia is purified at high pressure with the steps of: cooling the liquid ammonia (20) obtaining a cooled liquid ammonia stream (21), separating a gaseous fraction (22) comprising hydrogen and nitrogen from said cooled liquid ammonia, obtaining purified liquid ammonia (23) at a high pressure, and reheating said purified liquid ammonia (23) after separation of said gaseous fraction, obtaining a reheated purified ammonia (24) having a temperature suitable for feeding to the urea synthesis process. The application also deals with an ammonia -urea plant comprising an ammonia cooler, a liquid-gas separator and an ammonia re-heater and with a method for revamping existing ammonia -urea plants.
    • 一种氨 - 脲生产方法,其中在氨段产生的液氨直接以氨合成压力供给到尿素部分,并且液氨在高压下被纯化,其步骤是:冷却液氨(20 获得冷却的液氨流(21),从所述冷却的液氨中分离包含氢和氮的气态馏分(22),在高压下获得纯化液氨(23),并在 分离所述气态馏分,获得具有适于供给到尿素合成方法的温度的再加热的纯化氨(24)。 本申请还涉及一种氨脲装置,其包括氨冷却器,液气分离器和氨再加热器以及用于改造现有氨 - 脲装置的方法。
    • 4. 发明授权
    • Vertical isothermal shell-and-tube reactor
    • 垂直等温壳管反应堆
    • US08414840B2
    • 2013-04-09
    • US13320410
    • 2010-08-06
    • Ermanno FilippiEnrico RizziMirco Tarozzo
    • Ermanno FilippiEnrico RizziMirco Tarozzo
    • B01J8/02
    • B01J8/0285B01J8/0221B01J8/0278B01J2208/00132B01J2208/00884F28D7/06
    • Isothermal vertical reactor (1) for a chemical reaction, comprising a shell (2) with internal gas-permeable walls (16, 18) defining an inlet distribution chamber (17) and a product collecting chamber (19), an open-top catalytic bed between said gas-permeable walls, and a tube heat exchanger (5) embedded in said catalytic bed, the tube heat exchanger (5) comprising a bundle of U-tubes, where an inlet (14) is disposed to direct a fresh charge in an upper chamber (21) over the catalytic bed and the U-shaped top portion of the tube bundle; a portion (F1) of the fresh charge passes through the catalytic bed with a mixed axial-transversal flow, and another portion (F2) of the fresh charge enters the inlet gas-distribution chamber (17) and passes through the catalytic bed with a substantially transversal flow.
    • 用于化学反应的等温立式反应器(1),包括具有限定入口分配室(17)和产品收集室(19)的内部气体可渗透壁(16,18)的壳体(2),开放顶部催化剂 在所述气体可渗透壁之间的床和嵌入所述催化床中的管式热交换器(5)之间,所述管式热交换器(5)包括一束U形管,其中设置入口(14)以引导新鲜的电荷 在催化床上的上室(21)和管束的U形顶部; 新鲜电荷的一部分(F1)以混合的轴向横向流动通过催​​化床,新鲜电荷的另一部分(F2)进入入口气体分配室(17)并通过催化床 基本上横向流动。