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Pilot scale evaluation on ferric floc sludge concentration with pelleting flocculation blanket process

机译:球团絮凝床工艺对铁絮凝污泥浓度的中试评价

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Pelleting flocculation blanket (PFB) process has been successfully applied to high turbidity suspensions for high efficient solid/liquid separation. In this paper, by using the PFB process, a dynamic experimental study was carried out on concentrating ferric flocs sludge with a scale of 1.3–5.4m~3/h. The pilot experiment aimed to optimize the conditioning system and determine the operational parameters. Under the raw sludge concentrations of 103–1,154 mg/L, the system could achieve ideal conditioning effect with polyacrylamide (PAM) dosages of 0.3–2.7 mg/L, agitation speed of 10 rpm, and water up-flow rates of 18–48 m/h. Under the experimental conditions, the increase of polymer dosage would improve effluent turbidity and pellets settling behaviour, the moderate up-flow rate had no marked effect on treatment results, while too large surface loading could worsen effluent turbidity. The experimental results also revealed that there existed an approximately linear relationship between the raw sludge concentration and optimum PAM dosage, that is, the optimum dosage of PAM increased synchronously as the raw sludge concentration increased. While the relationship between the raw sludge concentration and maximum up-flow rate reflected another linear dependence, namely, the maximum up-flow rate would decreased linearly as the raw sludge concentration increased.
机译:制粒絮凝毯(PFB)工艺已成功应用于高浊度悬浮液,以实现高效固/液分离。本文采用PFB工艺,对铁絮凝污泥进行了动态实验研究,污泥浓度为1.3-5.4m〜3 / h。该试验旨在优化空调系统并确定运行参数。在原始污泥浓度为103–1,154 mg / L的情况下,该系统可以以0.3–2.7 mg / L的聚丙烯酰胺(PAM)剂量,10 rpm的搅拌速度和18–48的上水流速实现理想的调节效果。米/小时在实验条件下,聚合物用量的增加会改善废水的浊度和颗粒沉降的行为,适度的上流速率对处理效果没有明显的影响,而太大的表面负荷会使废水的浊度恶化。实验结果还表明,原料污泥浓度与最佳PAM用量之间存在线性关系,即随着原料污泥浓度的增加,PAM的最佳用量同步增加。原污泥浓度和最大上流率之间的关系反映了另一个线性关系,即最大污泥上流率随着原污泥浓度的增加而线性下降。

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