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Decolorizing dye wastewater with low temperature catalytic oxidation

机译:低温催化氧化脱色染料废水

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Novel oxidation technology to decolorize dye wastewater was discussed and the feasibility of color removal with Fe/MgO catalyst fluidizing in a reactor under continuous flow was demonstrated at room temperature. In batch tests, the oxidation reaction of reactive and disperse dye with an oxidizing agent, hydrogen peroxide, in the presence of Fe/MgO catalyst was performed. Through the catalytic oxidation, dyes were oxidized to molecules with lower molecular weight and then mineralized based on TOC analysis. The influence of hydrogen peroxide and catalyst dosage on the catalytic oxidation rate was verified. The catalytic oxidation rate increased with increasing hydrogen peroxide and catalyst dosage. Fe/MgO catalyst fluidizing in the reactor operated at room temperature was tested to decolorize the wastewater form a dye manufacturing industry. In the fluidized bed reactor, the wastewater was completely decolorized and about 30% of COD removal was obtained during 30 days of operation. Organic matters were degraded and part of them mineralized by the catalytic oxidation. BOD/COD ratio of the effluent from the fludized bed reactor was increased compared to that of the influent. After 30 days of operation, the effluent from the fluidized bed reactor started becoming yellowish. COD and residual hydrogen peroxide concentration in the effluent started to increase due to the catalyst losing its activity.
机译:讨论了将染料废水脱色的新型氧化技术,并证明了在室温下连续流动的反应器中流化Fe / MgO催化剂脱色的可行性。在分批测试中,在Fe / MgO催化剂的存在下,进行了活性染料和分散染料与氧化剂过氧化氢的氧化反应。通过催化氧化,染料被氧化为分子量较低的分子,然后根据TOC分析矿化。验证了过氧化氢和催化剂用量对催化氧化速率的影响。催化氧化速率随过氧化氢和催化剂用量的增加而增加。测试了在室温下运行的反应器中流化的Fe / MgO催化剂,以使染料制造行业的废水脱色。在流化床反应器中,废水已完全脱色,并且在运行30天期间获得了约30%的COD去除率。有机物质被降解,一部分被催化氧化矿化。与流化床相比,流化床反应器出水的BOD / COD比有所增加。运行30天后,流化床反应器的流出物开始变黄。由于催化剂失去活性,废水中的COD和残留的过氧化氢浓度开始增加。

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