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用于亚热带条件下污水处理的两步上流式厌氧污泥床系统及在稳定塘中的后处理。

Two-step upflow anaerobic sludge bed system for sewage treatment under subtropical conditions with posttreatment in waste stabilization ponds.

作者信息

Seghezzo Lucas, Trupiano Aníbal P, Liberal Viviana, Todd Patrick G, Figueroa María E, Gutiérrez Marcelo A, Da Silva Wilches Ana C, Iribarnegaray Martín, Guerra Raquel G, Arena Angélica, Cuevas Carlos M, Zeeman Grietje, Lettinga Gatze

机构信息

Universidad Nacional de Salta, Laboratorio de Estudios Ambientales (CIUNSa-INENCO), Buenos Aires 177, A4402FDC Salta, Argentina.

出版信息

Appl Biochem Biotechnol. 2003 Apr-Jun;109(1-3):167-80. doi: 10.1385/abab:109:1-3:167.

DOI:10.1385/abab:109:1-3:167
PMID:12794292
Abstract

A pilot-scale sewage treatment system consisting of two upflow anaerobic sludge bed (UASB) reactors followed by five waste stabilization ponds (WSPs) in series was studied under subtropical conditions. The first UASB reactor started up in only 1 mo (stable operation, high chemical oxygen demand [COD] removal efficiency, low volatile fatty acids concentration in the effluent, alkalinity ratio above 0.7, biogas production above 0.1 Nm3/kg of CODremoved). Removal efficiencies up to 90% were obtained in the anaerobic steps at a hydraulic retention time of 6 + 4 h (80% removal in the first step). Fecal coliform removal in the whole system was 99.9999% (99.94% in anaerobic steps and 99.98% in WSPs). COD balances over UASB reactors are provided. A minimum set of data necessary to build COD balances is proposed. Intermittent sludge washout was detected in the reactors with the COD balances. Sludge washout from single-step UASB reactors should be monitored and minimized in order to ensure constant compliance with discharge standards, especially when no posttreatment is provided. The system combined high COD and fecal coliform removal efficiency with an extremely low effluent concentration, complying with discharge standards, and making it an attractive option for sewage treatment in subtropical regions.

摘要

在亚热带条件下,对一个中试规模的污水处理系统进行了研究,该系统由两个上流式厌氧污泥床(UASB)反应器和随后串联的五个稳定塘(WSP)组成。第一个UASB反应器仅用1个月就启动成功(运行稳定,化学需氧量[COD]去除效率高,出水挥发性脂肪酸浓度低,碱度比高于0.7,沼气产量高于0.1 Nm3/kg去除的COD)。在水力停留时间为6 + 4小时的厌氧步骤中,去除效率高达90%(第一步去除80%)。整个系统中粪大肠菌群的去除率为99.9999%(厌氧步骤中为99.94%,稳定塘中为99.98%)。提供了UASB反应器的COD平衡情况。提出了建立COD平衡所需的最少数据集。在进行COD平衡的反应器中检测到间歇性污泥流失。应监测并尽量减少单步UASB反应器的污泥流失,以确保始终符合排放标准,特别是在没有后续处理的情况下。该系统结合了高COD和粪大肠菌群去除效率以及极低的出水浓度,符合排放标准,使其成为亚热带地区污水处理的一个有吸引力的选择。

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