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Purification of wastewater contaminated with organic substances, by catalytic wet oxidation with hydrogen peroxide, comprises treating the wastewater at temperature and pressure in reactor and in catalytic reactor

机译:通过用过氧化氢催化湿式氧化来净化被有机物污染的废水,包括在反应器和催化反应器中在温度和压力下处理废水

摘要

The purification of wastewater contaminated with organic substances by catalytic wet oxidation with hydrogen peroxide, comprises treating the wastewater at 60-210[deg]C, a pressure of up to 30 bar and a retention time of 20-300 minutes in reactor (R01A, R02A, R03A) and in a catalytic reactor (R01B, R02B, R03B). The reactors are connected in a closed circuit. The ratio of the volumes of the reactor to the catalytic reactor is 30-200:1. Solid catalysts are used in the catalytic reactor and are seventh and eighth group metals, which are assigned as a subgroup or as noble metals in the periodic system. The purification of wastewater contaminated with organic substances by catalytic wet oxidation with hydrogen peroxide, comprises treating the wastewater at 60-210[deg]C, a pressure of up to 30 bar and retention time of 20-300 minutes in reactor (R01A, R02A, R03A) and in a catalytic reactor (R01B, R02B, R03B). The reactors are connected in a closed circuit. The ratio of the volumes of the reactor to the catalytic reactor is 30-200:1. Solid catalysts are used in the catalytic reactor and are seventh and eighth group metals, which are assigned as a subgroup or as noble metals in the periodic system. The hydrogen peroxide is dosed before supplying the water into the reactor. The added quantity of the hydrogen peroxide depends on the required oxidation potential. The PH value is adjusted from 7-9 in a reservoir for the wastewater. The purified water is stored in a buffer tank (P4) before entry into heat exchangers (W0, W1).
机译:通过过氧化氢催化湿式氧化净化被有机物污染的废水,包括在60-210℃,压力高达30 bar和在反应器(R01A, R02A,R03A)和催化反应器(R01B,R02B,R03B)中。电抗器以闭合回路连接。反应器与催化反应器的体积比为30-200∶1。固体催化剂用于催化反应器中,并且是第七和第八族金属,它们在周期系统中被指定为亚组或贵金属。通过用过氧化氢催化湿式氧化净化被有机物污染的废水,包括在60-210℃,压力高达30 bar和在反应器中保留20-300分钟的时间(R01A,R02A)处理废水。 ,R03A)和催化反应器(R01B,R02B,R03B)中。电抗器以闭合回路连接。反应器与催化反应器的体积比为30-200∶1。固体催化剂用于催化反应器中,并且是第七和第八族金属,它们在周期系统中被指定为亚组或贵金属。在将水供应到反应器中之前计量加入过氧化氢。过氧化氢的添加量取决于所需的氧化电位。在用于废水的水库中,将PH值从7-9进行调整。净化水在进入热交换器(W0,W1)之前先储存在缓冲罐(P4)中。

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