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Uncovering the Mysteries of the Floc Blanket: An Exploration with Inlet Jets, Flocculators, and Polyaluminum Chloride Precipitates

机译:揭开絮状物毯子的奥秘:入口喷气机,絮凝器和聚氯化铝沉淀物的探索

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摘要

Floc blankets are used in water treatment plants to improve plant performance and aid in sludge removal and consolidation. Maintaining a fully functioning floc blanket in sedimentation tanks requires that the floc blanket remain fluidized and sludge prevented from building up on the bottom of the tank. A laboratory water treatment system was used to evaluate the range of energy dissipation rates (EDR) of the inlet to the sedimentation tank to determine when the settled effluent turbidity of the system would exceed drinking water quality standards.. Increasing the inlet jet EDR up to approximately 300 mW/kg did not increase effluent turbidity of the system. Small inlet jets with high EDR can be used to ensure resuspension of the floc density current without adversely affecting water treatment plant performance.;The design of flocculators is based on mean shear (G) and hydraulic residence time (theta) and the product (Gtheta). Guidelines for these values are conservative and designs outside the suggested range could lower plant capital costs. The following flocculator parameters were evaluated: 1) increasing G (range of 74-251 s-1) while decreasing theta from 269 to 80 s (maintaining a constant Gtheta) and 2) maintaining a constant G (72 s-1) and varying theta (24 to 1425 s). Flocculator theta below recommended design guidelines performed well indicating that shorter flocculators could be used in the presence of floc blankets.;Three potential hypotheses by which residual particles aggregate with other flocs in the floc blanket were considered: residual particles aggregate with 1) other residual particles, 2) small flocs (transitional), or 3) large flocs (hindered). Three coagulant doses (0.625, 1.25, and 2.5 mg/L) were tested with four hydraulic flocculators with constant Gtheta but varying G (72, 126, 251, and 340 s-1) and theta (269, 159, 102, and 59 s) on the combined system. A classification system of flocs in the floc blanket was defined based on floc size and time-scale. Results strongly suggest that hypothesis 2 is valid, however, research is needed on floc sizes at specific locations within the system.
机译:絮凝毯用于水处理厂,以改善工厂的性能并帮助去除污泥和固结。要在沉淀池中保持功能完备的絮凝毯,必须使絮凝毯保持流化状态,并防止污泥积聚在沉淀池的底部。使用实验室水处理系统评估沉淀池入口的能量耗散率(EDR)范围,以确定系统的沉降出水浊度何时超过饮用水质量标准。.将入口射流EDR增加至大约300 mW / kg不会增加系统的污水浊度。可以使用具有高EDR的小型进口射流来确保重悬絮凝物密度流,而不会不利地影响水处理厂的性能。;絮凝器的设计基于平均剪切力(G)和水力停留时间(θ)和产品(Gtheta) )。这些值的指导原则是保守的,超出建议范围的设计可能会降低工厂的资本成本。对以下絮凝器参数进行了评估:1)增加G(74-251 s-1的范围),同时将θ从269降低到80 s(保持恒定的Gtheta); 2)维持恒定的G(72 s-1)并变化θ(24至1425 s)。低于推荐设计指南的絮凝器theta表现良好,表明在絮凝毯存在的情况下可以使用较短的絮凝器。;三个潜在的假设考虑了残留颗粒与絮凝毯中其他絮凝物的聚集:残留微粒与1)其他残留微粒凝结,2)小絮状物(过渡性)或3)大絮状物(受阻)。使用四台Gtheta恒定但G(72、126、251和340 s-1)和theta(269、159、102和59)变化的液压絮凝器测试了三种凝结剂剂量(0.625、1.25和2.5 mg / L) s)在组合系统上。基于絮状物的大小和时间尺度,定义了絮状物毯中的絮状物分类系统。结果强烈表明假设2是有效的,但是,需要对系统内特定位置的絮状物尺寸进行研究。

著录项

  • 作者

    Garland, Casey Ann.;

  • 作者单位

    Cornell University.;

  • 授予单位 Cornell University.;
  • 学科 Environmental engineering.
  • 学位 Ph.D.
  • 年度 2017
  • 页码 115 p.
  • 总页数 115
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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