首页> 外国专利> Plant for purifying waters and sludges includes main electron-beam reactor tank with air-cooled window from which ozone is fed to pre- and post-reaction stages to break contaminants down completely, with high energy efficiency

Plant for purifying waters and sludges includes main electron-beam reactor tank with air-cooled window from which ozone is fed to pre- and post-reaction stages to break contaminants down completely, with high energy efficiency

机译:净化水和污泥的工厂包括带风冷窗的主电子束反应器罐,臭氧从该罐进料至反应前和反应后阶段,以高效率地彻底分解污染物

摘要

Ozone-containing gas is supplied to each of: a pre-reactor (7), main electron beam irradiation reactor (11) and a post-reactor (14). The material for purification, passes through all three in sequence. An Independent claim is included for the corresponding process. Preferred features: Electrons enter the main reactor through a window (23). Flowing air (e.g.) cools the window. At the same time electrons generate ozone in the air. This is supplied to the pre- and/or post-treatment reactors. Volumetric rate of gas production from the window and volumetric rate of material supply into the main reactor, are in the ratio 0.1:1 to 10:1, preferably 5:1 to 7:1. Gas leaving pre- and post-reactors, and optionally some from the main reactor, is collected in a closed system. Fresh air is supplied to it via a controller (26), offsetting diverse process gas volume changes. Gas from the closed system is recycled for window cooling duty as before. Mixing of gas and material, takes place in the reactors. There is a set residence time for the material, in each reactor. This can be zero in the pre- and/or post-reactor, achieved by bypassing, should material supply condition permit. Oxidant chemicals are added into the pre-reactor. The material is sent from the post-reactor for a further stage of biological purification (17). From either of these two stages, it is re-cycled to the pre-reactor.
机译:将含臭氧的气体供应至以下各者:预反应器(7),主电子束辐射反应器(11)和后反应器(14)。用于纯化的材料依次通过所有三个。相应过程包括独立索赔。优选的特征:电子通过窗口(23)进入主反应器。流动的空气(例如)使窗户冷却。同时,电子在空气中产生臭氧。将其供应至预处理和/或后处理反应器。从窗口产生的气体的体积比和进入主反应器的材料的体积比为0.1∶1至10∶1,优选5∶1至7∶1。离开前置反应器和后反应器的气体,以及可选地从主反应器流出的气体,都被收集在一个密闭系统中。新鲜空气通过控制器(26)供应给它,从而抵消了各种工艺气体体积的变化。像以前一样,将封闭系统中的气体再循环用于车窗冷却。气体和材料的混合在反应器中进行。在每个反应器中,物料都有设定的停留时间。如果物料供应条件允许,则在旁路前和/或后反应器中可以为零。将氧化剂化学物质添加到预反应器中。物料从后反应器中送出,用于生物纯化的进一步阶段(17)。从这两个阶段中的任何一个阶段,将其再循环至预反应器。

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