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Ozone catalytic oxidation capacity of Ti-Co@Al_2O_3 for the treatment of biochemical tailwater from the coal chemical industry

机译:臭氧催化氧化能力Ti-Co @ Al_2O_3从煤化工中处理生化尾水

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A Ti‐Co@γ‐Al_(2)O_(3)composite catalyst was prepared using impregnation and sol‐gel methods to degrade biochemical tailwater from the coal chemical industry, and its preparation conditions (active component doping ratio, load times, and calcination temperature) were optimized through single‐factor experiments. The surface properties of the Ti‐Co@γ‐Al_(2)O_(3)composite catalyst and the crystal structure characteristics of the catalytically active components were characterized via scanning electron microscopy–energy dispersive spectrometry, X‐ray diffraction, and X‐ray fluorescence. The effects of reaction time, initial pH, ozone aeration, and catalyst dosage on degradation performance were investigated through an experiment on the catalytic ozonation degradation of biochemical tail water. Results showed that the optimal conditions were as follows: reaction time of 30 min, pH of 8.2, ozone aeration of 30 mg/min, and catalyst dosage of 20 g/L. The total phenol and total organic carbon removal rates for biochemical tailwater were 66.1% and 57.6%, respectively, in the catalytic system. The mechanism of degradation of organic pollutants by catalytic ozonation was investigated by adding tert‐butanol to the catalytic ozone oxidation system. The degradation of chemical oxygen demand in biochemical tailwater was caused primarily by the synergy between the Ti‐Co@γ‐Al_(2)O_(3)catalyst and ozone. Practitioner points Ti‐Co/γ‐Al_(2)O_(3)catalyst was prepared for the catalytic oxidation of biochemical tail water. The optimal removal rates of total phenol and TOC were 67.7% and 58.8%, respectively. The organic matter was degraded rapidly and efficiently after 5 min of ozone catalytic oxidation reaction. It provides theoretical guidance for the practical application of ozone catalytic oxidation. Ozone catalytic oxidation capacity of Ti‐Co@Al2O3 for the treatment of biochemical tailwater from the coal chemical industry.
机译:使用浸渍和溶胶 - 凝胶方法制备Ti-Co@γ-Al_(2)O_(3)复合催化剂,以降解来自煤化工的生物化学尾水,其制备条件(活性成分掺杂比,负荷时间和通过单因素实验优化煅烧温度。通过扫描电子显微镜 - 能量分散光谱法,X射线衍射和X-表征催化活性组分的Ti-Co-γ-Al_(2)O_(3)复合催化剂的表面性质及催化活性组分的晶体结构特性射线荧光。通过实验研究了反应时间,初始pH,臭氧通气和催化剂剂量对降解性能的影响,研究了生物化学尾水的催化臭氧化降解。结果表明,最佳条件如下:30分钟的反应时间,pH为8.2,臭氧曝气30mg / min,催化剂剂量为20g / L.生化尾水的总苯酚和总有机碳除去率分别在催化系统中分别为66.1%和57.6%。通过将叔丁醇加入催化臭氧氧化体系,研究了通过催化臭氧溶解的有机污染物降解机制。生物化学尾水中化学氧需求的降解主要是由Ti-Coγ-Al_(2)O_(3)催化剂和臭氧之间的协同作用引起的。为催化氧化生物化学尾水制备从业者点Ti-Co /γ-Al_(2)O_(3)催化剂。总苯酚和TOC的最佳去除率分别为67.7%和58.8%。在臭氧催化氧化反应5分钟后,有机物在5分钟后快速有效地降解。它为臭氧催化氧化的实际应用提供了理论指导。 Ti-Co @ Al2O3臭氧催化氧化能力,用于治疗煤化工生物化学尾水。

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