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[低溶解氧条件下通过有限丝状菌膨胀实现节能:A/O工艺的实验验证]

[Energy saving achieved by limited filamentous bulking under low dissolved oxygen: experimental validation in A/O process].

作者信息

Guo Jian-hua, Wang Shu-ying, Peng Yong-zhen, Zheng Ya-nan, Huang Hui-jun, Ge Shi-jian, Sun Zhi-rong

机构信息

School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin 150090, China.

出版信息

Huan Jing Ke Xue. 2008 Dec;29(12):3348-52.

Abstract

Preliminary studies had been conducted to determine the correctness of the theory and technique of energy saving achieved by limited filamentous bulking under low DO using a lab-scale A/O reactor with real domestic wastewater as the influent. The results showed that SVI could be maintained 150-230 mL/g and sludge settleability would not become very poor under the condition of low DO. During the period of limited filamentous bulking, COD and total nitrogen removal efficiencies were improved, and distinct simultaneous nitrification and denitrification (SND) was achieved, while ammonia removal efficiency would slightly decline with decreasing of DO, compared with the period of good settleability sludge under high DO. COD, ammonia and total nitrogen removal efficiencies were 86%, 70% and 63%, respectively. It was found that about 10%-25% nitrogen would be removed by SND based on the mass balance of nitrogen. Besides, SS in the effluent was almost negligible and the effluent turbidity was lower than 3 NTU. Significantly, aeration consumptions would be decreased by 17% under the condition with DO of 0.5 mg/L compared with 2.0 mg/L according to theoretical calculation of air requirements to keep different DO levels, which was about 57% in lab-scale reactor correspondingly.

摘要

利用以实际生活污水为进水的实验室规模A/O反应器,进行了初步研究,以确定在低溶解氧(DO)条件下通过有限丝状膨胀实现节能的理论和技术的正确性。结果表明,在低DO条件下,污泥体积指数(SVI)可维持在150 - 230 mL/g,污泥沉降性能不会变得很差。在有限丝状膨胀期间,化学需氧量(COD)和总氮去除效率提高,实现了明显的同步硝化反硝化(SND),而与高DO下沉降性能良好的污泥时期相比,随着DO的降低,氨氮去除效率会略有下降。COD、氨氮和总氮去除效率分别为86%、70%和63%。基于氮的质量平衡发现,约10% - 25%的氮将通过SND去除。此外,出水的悬浮物(SS)几乎可以忽略不计,出水浊度低于3 NTU。值得注意的是,根据保持不同DO水平所需空气量的理论计算,与2.0 mg/L的DO条件相比,在0.5 mg/L的DO条件下曝气消耗量可降低17%,在实验室规模的反应器中相应降低约57%。

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