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PROCESS FOR THE DISPOSAL OF INTRACTABLE NON-BIODEGRADABLE WASTE MATERIAL FLOWS FROM OIL REFINERIES

机译:处置炼油厂难处理的不可生物分解的废物流的过程

摘要

The invention provides a process for the disposal treatment of persistent, oil refinery waste material flows, which are difficult to degrade under oxidative conditions, by way of performing a continuous, cyclic oxidation disposal treatment in air or oxygen atmosphere in the presence of known oxidation catalysts and known adsorbent, characterized in that the disposal treatment is carried out in at least two degradation stages, wherein the catalyst/adsorbent volumetric ratio (v/v) in an isolated or separate first reactor is between 0:1 and 1:1 in the first degradation stage and the catalyst/adsorbent volumetric ratio (v/v) in an isolated or separate second reactor is between 1:0 and 1:02 in the second degradation stage; and wherein the surface of the adsorbent : catalyst mixture is modified with a 3-50 fold amount of a 0.1-10 N inorganic acid prior to degradation; and wherein degradation is carried out at a pressure of 10-80 bar, at a temperature of 150-280°C, with a space velocity of 0.4-3.6 1/h and at a waste/oxygen ratio (v/v) of 5-500; and wherein optionally the material effluent of the acidic modification is reintroduced into the material flow to be treated.
机译:通过在已知的氧化催化剂存在下在空气或氧气气氛中进行连续,循环的氧化处理方法,本发明提供了一种处理方法,该方法用于处理在氧化条件下难以降解的持久的炼油厂废料流。已知的吸附剂,其特征在于,所述处置处理至少在两个降解阶段中进行,其中在分离或分离的第一反应器中,催化剂/吸附剂的体积比(v / v)在0:1至1:1之间。第一降解阶段,并且在第二降解阶段中,分离的或分离的第二反应器中的催化剂/吸附剂的体积比(v / v)在1:0至1:02之间;以及其中的吸附剂:催化剂混合物的表面在降解之前用3-50倍量的0.1-10N无机酸改性;其中降解是在10-80 bar的压力,150-280°C的温度,空速0.4-3.6 1 / h和废物/氧气比(v / v)为5的条件下进行的-500;其中任选地将酸性改性的物料流出物重新引入待处理的物料流中。

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