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Mesophilic anaerobic digestion of waste activated sludge: influence of the solid retention time in the wastewater treatment process

机译:废活性污泥的中温厌氧消化:废水处理过程中固体保留时间的影响

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摘要

The performance of mesophilic anaerobic digesters of four large Italian wastewater treatment plants without primary sedimentation were studied. Only the waste activated sludge is stabilised by means of the mesophilic (35-37℃) anaerobic digestion process. The anaerobic digesters generally worked with a hydraulic retention time in a range of 20-40 days and an organic loading rate of some 1 kg VS/m_(reactor)~3 day. The solids content of the sludge fed to the digesters was in the range 2.6-3.9% and the gas produced per kilogram of volatile solids added was in the range 0.07-0.18 m~3/kg VS_(fed). The specific gas production per kilogram of volatile solids destroyed was in the range 0.5-0.9 m~3/kg VS_(destroyed) and the reduction of the volatile solids concentration was in the range 13-27% (average 18%). These figures are particularly significant when designing anaerobic digesters for the treatment of waste activated sludge as single substrate. Moreover, it was observed that the higher the applied solid retention time in the activated sludge process for wastewater treatment, the lower the gas production. In particular, the specific gas production decreased from 0.18 to 0.07 m~3/kg VS_(fed) when increasing the solid retention time in the wastewater treatment line from 8 to 35 days. Finally, a mathematical model for the prediction of biogas production on the solid retention time applied in the wastewater treatment process was developed.
机译:研究了意大利四个大型废水处理厂中无初级沉淀的嗜温厌氧消化池的性能。只有废活性污泥通过中温(35-37℃)厌氧消化过程才能稳定。厌氧消化池的水力停留时间通常为20-40天,有机负荷率为1 kg V​​S / m_(反应器)〜3天。供入消化池的污泥的固体含量在2.6-3.9%的范围内,每千克添加的挥发性固体产生的气体在0.07-0.18m〜3 / kg V​​S_(进料)的范围内。每千克被破坏的挥发性固体的比气产量在0.5-0.9 m〜3 / kg V​​S_(被破坏)的范围内,挥发性固体浓度的降低在13-27%的范围内(平均18%)。当设计厌氧消化池作为单一底物处理废活性污泥时,这些数字特别重要。此外,已观察到在用于废水处理的活性污泥工艺中施加的固体保留时间越高,产气量越低。特别地,当将废水处理管线中的固体停留时间从8天增加到35天时,比气产量从0.18降至0.07 m3 / kg V​​S_(fed)。最后,建立了用于预测废水处理过程中固体停留时间的沼气产量的数学模型。

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