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上流式厌氧污泥床反应器处理甘蔗制糖厂废水

Treatment of cane sugar mill wastewater in an upflow anaerobic sludge bed reactor.

作者信息

Nacheva P Mijaylova, Chávez G Moeller, Chacón J Matías, Chuil A Canul

机构信息

Mexican Institute of Water Technology, Paseo Cuauhnáhuac 8532, Col. Progreso, Jiutepec Morelos, 62550, México.

出版信息

Water Sci Technol. 2009;60(5):1347-52. doi: 10.2166/wst.2009.402.

Abstract

The performance of a mesophilic UASB reactor was studied for the treatment of sugar cane mill wastewater previously pre-treated for solid separation. The experimental work was carried out in a reactor with 80 L total volume. Four organic loads were applied and the process performance was evaluated during two months for each experimental stage. Removal efficiencies higher than 90% were obtained with organic loads up to 16 kg COD m(-3) d(-1). Stable process performance and high biogas production were obtained. The COD removal rate increased substantially with the load increase to 24 kg COD m(-3) d(-1). However, the obtained removal was of only 78-82%, which can be attributed to the accumulation of volatile organic acids. The kinetic coefficients were obtained using first order model for the substrate removal rate and Monod's equation for bacteria specific growth rate. The UASB reactor is a good option for the biological treatment of pre-treated sugar cane mill wastewaters. The discharge requirements for COD concentration can be accomplished if the reactor is operated at a low organic load of 4 kg COD m(-3) d(-1). At higher loads, an additional biological treatment stage is needed.

摘要

研究了中温上流式厌氧污泥床(UASB)反应器处理经预处理以实现固液分离的甘蔗制糖厂废水的性能。实验工作在一个总体积为80升的反应器中进行。施加了四种有机负荷,并在每个实验阶段的两个月内评估了工艺性能。在有机负荷高达16 kg COD m(-3) d(-1)时,去除效率高于90%。获得了稳定的工艺性能和高沼气产量。当负荷增加到24 kg COD m(-3) d(-1)时,化学需氧量(COD)去除率大幅提高。然而,获得的去除率仅为78 - 82%,这可归因于挥发性有机酸的积累。使用底物去除率的一级模型和细菌比生长速率的莫诺德方程获得了动力学系数。UASB反应器是预处理甘蔗制糖厂废水生物处理的一个良好选择。如果反应器在4 kg COD m(-3) d(-1)的低有机负荷下运行,则可以满足COD浓度的排放要求。在较高负荷下,需要额外的生物处理阶段。

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