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上流式厌氧污泥床(UASB)反应器处理黑水:一项初步研究。

Black water treatment by an upflow anaerobic sludge blanket (UASB) reactor: a pilot study.

机构信息

Department of Hydraulics and Sanitation, University of São Paulo (EESC-USP), 400 Trabalhador São Carlense Avenue, São Carlos, São Paulo 13566-590, Brazil E-mail:

Department of Environmental and Civil Engineering, University of São Paulo State (FEB-UNESP), 14-01 'Engenheiro Luiz Edmundo Carrijo Coube' Avenue, Bauru, São Paulo 17033-360, Brazil.

出版信息

Water Sci Technol. 2019 Oct;80(8):1505-1511. doi: 10.2166/wst.2019.402.

Abstract

Decentralized sanitary wastewater treatment has become a viable and sustainable alternative, especially for developing countries and small communities. Besides, effluents may present variations in chemical oxygen demand (COD), biochemical oxygen demand (BOD) and total nitrogen values. This study describes the feasibility of using a pilot upflow anaerobic sludge blanket (UASB) reactor to treat wastewater with different organic loads (COD), using black water (BW) and sanitary wastewater, in addition to its potential for preserving nutrients for later recovery and/or reuse. The UASB reactor was operated continuously for 95 weeks, with a hydraulic retention time of 3 days. In Phase 1, the reactor treated simulated BW and achieved 77% COD removal. In Phase 2, treating only sanitary wastewater, the COD removal efficiency was 60%. Phase 3 treated simulated BW again, and COD removal efficiency was somewhat higher than in Phase 1, reaching 81%. In Phase 3, the removal of pathogens was also evaluated: the efficiency was 1.96 log for Escherichia coli and 2.13 log for total coliforms. The UASB reactor was able to withstand large variations in the organic loading rate (0.09-1.49 kg COD m d), in continuous operation mode, maintaining a stable organic matter removal.

摘要

分散式卫生废水处理已成为一种可行且可持续的替代方案,特别是对于发展中国家和小型社区而言。此外,废水的化学需氧量(COD)、生化需氧量(BOD)和总氮值可能会有所变化。本研究描述了使用中试上流式厌氧污泥床(UASB)反应器处理具有不同有机负荷(COD)的废水的可行性,使用黑水(BW)和卫生废水,以及保留养分以备将来回收和/或再利用的潜力。UASB 反应器连续运行了 95 周,水力停留时间为 3 天。在第 1 阶段,反应器处理模拟 BW,COD 去除率达到 77%。在第 2 阶段,仅处理卫生废水时,COD 去除效率为 60%。第 3 阶段再次处理模拟 BW,COD 去除效率略高于第 1 阶段,达到 81%。在第 3 阶段,还评估了病原体的去除效果:大肠杆菌的去除效率为 1.96 log,总大肠菌群的去除效率为 2.13 log。UASB 反应器能够在连续运行模式下承受有机负荷率(0.09-1.49 kg COD m d)的大幅波动,保持稳定的有机物去除。

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