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间歇曝气与好氧沉淀厌氧工艺组合用于脱氮及减少污水污泥的研究。

Investigation of intermittent aeration and oxic settling anaerobic process combination for nitrogen removal and sewage sludge reduction.

作者信息

Bosco Mofatto Paulo Marcelo, Cosenza Alida, Di Trapani Daniele, Mannina Giorgio

机构信息

Engineering Department, Palermo University, Viale delle Scienze, Ed. 8, 90128, Palermo, Italy.

Engineering Department, Palermo University, Viale delle Scienze, Ed. 8, 90128, Palermo, Italy.

出版信息

Chemosphere. 2024 Sep;363:142877. doi: 10.1016/j.chemosphere.2024.142877. Epub 2024 Jul 15.

Abstract

A pilot plant with a conventional activated sludge (CAS) system with intermittent aeration (IA) was monitored. The system was configured as an Oxic Settling Anaerobic (OSA) process with the insertion of one anaerobic side-stream reactor (ASSR). The pilot plant was fed with real wastewater and an intensive experimental campaign was carried out including sludge minimization, nitrogen and carbon removal, GHG emissions and biokinetic parameters. The experimental campaign was divided into periods: Period I, II, and III. In Periods I and II, the ASSR reactor was operated with two different hydraulic retention times (HRT), 4 and 6 h, with an aeration/non-aeration ratio of 30 min/30 min. In Period III, the HRT in the anaerobic reactor was the same as in Period II. In contrast, the biological reactor's aerated/non-aerated ratio was increased to 40 min/20 min. Results demonstrated that combining IA and OSA might be effective in the reduction of excess sludge production. The yield coefficient decreased from Period I to Period II (Y from 0.41 to 0.25 gTSS gCOD, in Period I and II, respectively). Nevertheless, the HRT increase in the ASSR compromised the system performance regarding nitrification and greenhouse gas emissions and worsened the sludge settleability. However, the increase in the aeration duration was beneficial in restoring the system's nitrification and denitrification ability and carbon footprint. The lowest carbon footprint was obtained during Period III (6.8 kgCO/d).

摘要

对一个采用间歇曝气(IA)的传统活性污泥(CAS)系统的中试装置进行了监测。该系统配置为缺氧沉淀厌氧(OSA)工艺,并插入了一个厌氧侧流反应器(ASSR)。中试装置采用实际废水进料,并开展了一项深入的实验活动,包括污泥最小化、氮和碳去除、温室气体排放以及生物动力学参数。实验活动分为三个阶段:第一阶段、第二阶段和第三阶段。在第一阶段和第二阶段,ASSR反应器以两种不同的水力停留时间(HRT)运行,即4小时和6小时,曝气/非曝气比为30分钟/30分钟。在第三阶段,厌氧反应器中的HRT与第二阶段相同。相比之下,生物反应器的曝气/非曝气比增加到40分钟/20分钟。结果表明,将IA和OSA相结合可能对减少剩余污泥产量有效。产率系数从第一阶段到第二阶段有所下降(第一阶段和第二阶段的Y分别从0.41降至0.25 gTSS/gCOD)。然而,ASSR中HRT的增加损害了系统在硝化和温室气体排放方面的性能,并使污泥沉降性能恶化。不过,曝气时间的增加有利于恢复系统的硝化和反硝化能力以及碳足迹。在第三阶段获得了最低的碳足迹(6.8 kgCO/d)。

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