Chemical Engineering, School of Engineering, RMIT University, Victoria, Australia.
Chemical Engineering, School of Engineering, RMIT University, Victoria, Australia.
Water Res. 2016 May 15;95:159-64. doi: 10.1016/j.watres.2016.03.002. Epub 2016 Mar 3.
The legal banning of conventional sludge disposal methods such as landfill has led to a global movement towards achieving a sustainable sludge management strategy. Reusing sludge for energy production (biogas production) through the anaerobic digestion of sludge can provide a sustainable solution. However, for the optimum performance of digesters with minimal use of energy input, operating conditions must be regulated in accordance with the rheological characteristics of the sludge. If it is assumed that only secondary sludge enters the anaerobic digesters, an impact of variations to the solids concentration and volume fraction of each sludge type must be investigated to understand how the apparent viscosity and yield stress of the secondary and digested sludge mixture inside the digesters changes. In this study, five different total solids concentration of secondary and digested sludge were mixed at different digested sludge volume fractions ranging from 0 to 1. It was found that if secondary sludge was mixed with digested sludge at the same total solids concentration, the apparent viscosity and the yield stress of the mixture increased exponentially by increasing the volume fraction of digested sludge. However, if secondary sludge was added to digested sludge with a different solids concentration, the apparent viscosity and yield stress of the resulting mixed sludge was controlled by the concentrated sludge regardless of its type. Semi - empirical correlations were proposed to predict the apparent viscosity and yield stress of the mixed digested and secondary sludge. A master curve was also developed to predict the flow behaviour of sludge mixtures regardless of the total solid concentration and volume fraction of each sludge type within the studied solids concentration range of 1.4 and 7%TS. This model can be used for digesters optimization and design by predicting the rheology of sludge mixture inside digester.
传统污泥处理方法(如填埋)的法律禁令促使全球努力实现可持续的污泥管理策略。通过污泥的厌氧消化来生产能源(沼气)可以提供一种可持续的解决方案。然而,为了使消化器以最小的能量输入达到最佳性能,必须根据污泥的流变特性来调节操作条件。如果假设只有二级污泥进入厌氧消化器,那么必须研究每种污泥类型的固体浓度和体积分数的变化对其的影响,以了解消化器内二级和消化污泥混合物的表观粘度和屈服应力如何变化。在这项研究中,将五种不同总固体浓度的二级和消化污泥以不同的消化污泥体积分数(从 0 到 1)混合。结果发现,如果二级污泥与消化污泥在相同的总固体浓度下混合,那么随着消化污泥体积分数的增加,混合物的表观粘度和屈服应力呈指数增长。然而,如果将二级污泥添加到具有不同固体浓度的消化污泥中,那么所得混合污泥的表观粘度和屈服应力将由浓缩污泥控制,而与其类型无关。提出了半经验相关性来预测混合消化和二级污泥的表观粘度和屈服应力。还开发了一条主曲线来预测污泥混合物的流动行为,而不管每种污泥类型的总固体浓度和体积分数如何,其研究的固体浓度范围为 1.4%和 7%TS。该模型可用于通过预测消化器内污泥混合物的流变性来优化和设计消化器。