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首页> 外文期刊>Chemical engineering journal >The coupling use of advanced oxidation processes and sequencing batch reactor to reduce nitrification inhibition of industry wastewater: Characterization and optimization
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The coupling use of advanced oxidation processes and sequencing batch reactor to reduce nitrification inhibition of industry wastewater: Characterization and optimization

机译:晚期氧化方法和测序批量反应器的偶联用途降低产业废水硝化抑制作用:表征和优化

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摘要

The excess emission of ammonia nitrogen is a common issue encountered by many industry wastewater treatment plants, due to the elevated concentrations and toxicities of compounds released from a large number of industries which might inhibit the growth of nitrifying bacteria. In this work, we are aiming at addressing the above issue raised by an industry wastewater treatment plant and elucidating the nitrification inhibitory mechanisms. A straight-forward and reliable method i.e., respirometry, was developed for the characterisation of nitrification inhibition. The pretreatment methods of Fenton and ozone oxidations and iron carbon micro electrolysis have been attempted to reduce the nitrification inhibition and the former two turned out to be effective. The nitrification inhibition rate (NIR) of the wastewater after Fenton oxidation was reduced from 87% to 13.6% with the optimized condition (pH= 3.0, H2O2 dosage of 14.7 mM, Fe2+ dosage of 4.90 mM, and reaction time of 20 min). The optimal parameters for ozonation were: pH = similar to 8.2 (original pH of wastewater), reaction time of 25 min (equivalent to an ozone dosage of 381 mg/L), under which the NIR was declined to 12.7%. The nitrification inhibition might be attributed to the presence of compounds with hydrophobic properties, high molecular weight, and aromatic and unsaturated structures in industry wastewater. The coupling use of Fenton-SBR and ozone-SBR achieved NH3-N removal efficiency of 98% and 93%, respectively. The effluent NH3-N finally met with the Integrated Wastewater Discharge Standard (DB31/199-2009).
机译:由于从可能抑制硝化细菌的生长的大量行业释放的化合物的浓度和毒性升高,许多行业废水处理厂的过量排放是许多行业废水处理厂的常见问题。在这项工作中,我们旨在解决由行业废水处理厂提出的上述问题,并阐明硝化抑制机制。用于表征硝化抑制的直接和可靠的方法,即呼吸方法。芬顿和臭氧氧化和铁碳微电解的预处理方法已经尝试降低硝化抑制,前两个结果是有效的。芬顿氧化后废水的硝化抑制率(NIR)从87%降低至13.6%,优化条件(pH = 3.0,H 2 O 2剂量为14.7mm,Fe2 +剂量为4.90mm,反应时间为20分钟)。臭氧化的最佳参数是:pH =类似于8.2(废水的原始pH),反应时间25分钟(相当于臭氧剂量为381mg / L),其中NIR下降至12.7%。硝化抑制可能归因于工业废水中具有疏水性质,高分子量和芳族和不饱和结构的化合物的存在。 FENTON-SBR和臭氧-SBR的偶联使用分别获得98%和93%的NH 3-N去除效率。流出物NH3-N最后与集成的废水排放标准(DB31 / 199-2009)达到了。

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