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Microaerophilic-aerobic sequential batch reactor for treatment of azo dyes containing simulated wastewater

机译:需氧好氧顺序分批反应器用于处理含模拟废水的偶氮染料

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摘要

Azo dyes are considered to be resistant to attack by aerobic microorganisms and not amenable to aerobic effluent treatment process. Azo dyes are decolorized under anaerobic or microaerophilic condition by the enzyme azoreductase secreted by microorganisms. The present study is a new approach to decolorization and biodegradation of azo dyes from simulated wastewater in an aerobic sequencing batch reactor. Facultative microorganisms under microaerophilic conditions decolorize azo dyes and total biodegradation occurs under aerated conditions. Laboratory flask experiments with various combination modes of aeration and static have shown 92.84% initial COD reduction along with 99.0% decolorization. Accordingly, an investigation was made on a laboratory scale to assess the feasibility of microaerophilic fixed film bed reactor system to decolorize simulated textile wastewater including the influence of operating conditions. Work was carried out with a laboratory scale down flow reactor, equipped with beads used in insulation as support. A continuous reactor for decolorization/biodegradation of azo dyes in aerobic sequencing reactor needs an understanding of a sequence. The first reactor was always operated under microaerophilic down flow fixed film fixed bed conditions, where the azo dyes from simulated wastewater were decolorized at 7.72 h hydraulic retention time with 2.2392 kg/m~3 per day loading rate. COD reduction of 74.67% was achieved. The second reactor operated in a down flow fixed bed, and shows a significant decrease in COD along with ammonia, nitrite and nitrate.
机译:偶氮染料被认为对需氧微生物具有抵抗力,并且不适合需氧废水处理过程。厌氧或微需氧条件下,偶氮染料会被微生物分泌的偶氮还原酶脱色。本研究是一种新方法,可在好氧排序批处理反应器中从模拟废水中脱色和生物降解偶氮染料。在微需氧条件下的兼性微生物使偶氮染料脱色,并且在曝气条件下发生总生物降解。带有不同曝气和静态混合模式的实验室烧瓶实验显示,初始COD减少量为92.84%,脱色率为99.0%。因此,在实验室规模上进行了研究以评估微需氧固定膜床反应器系统对包括操作条件的影响的模拟纺织品废水进行脱色的可行性。用实验室规模的向下流动反应器进行工作,该反应器配备有用于绝缘的珠粒作为载体。在好氧测序反应器中用于偶氮染料脱色/生物降解的连续反应器需要了解序列。第一个反应器始终在微需氧的固定膜固定床条件下运行,其中模拟废水中的偶氮染料在7.72 h水力停留时间下以2.2392 kg / m〜3的日载量脱色。 COD减少了74.67%。第二个反应器在下流式固定床中运行,并且COD以及氨,亚硝酸盐和硝酸盐显着降低。

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