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Selection of media for the design of ballasted flocculation processes

机译:选择用于压载絮凝工艺的介质

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Conventional clarification processes imply specific facility footprints that translate into important capital costs. Ballasted flocculation, consisting of injecting ballast medium to increase floc specific gravity and size, is being increasingly used in the water industry owing to its potential for design with very high superficial velocities. However, no systematic approach has yet been proposed to compare and select an appropriate ballast medium with respect to its specific gravity and size. In order to facilitate this procedure, this research project explores the hypothesis that flocculation performance is controlled by the surface area of the medium available for ballasted flocculation. This hypothesis was tested at laboratory scale by evaluating five ballast media with differing specific gravity and size: granular activated carbon, anthracite, silica sand, ilmenite, and magnetite sand having specific gravities of 1.24, 1.45, 2.62, 3.70, and 5.08, respectively. Flocculation kinetics were monitored by measuring floc size through microscopy and with a camera installed directly on the jar-test beaker. Settling performance was monitored using turbidity measurements. This study shows that all ballast media, when expressed as total surface available during flocculation, required similar surface concentrations to achieve settled water turbidity near 1 NTU and lower. In addition, the effects from the ballast media size and specific gravity were lowered for settling time longer than 3 min. Inversely, for settling time of 12 s, larger and denser media produced lower settled water turbidity. For certain applications, lighter ballast media may be more economical because they offer more available surface area for a given mass concentration, hence reducing the amount of ballast media required in the flocculation tank. Finally, the ballast media point of zero charge and shape were not identified as key criteria for ballasted flocculation. (C) 2018 Elsevier Ltd. All rights reserved.
机译:常规的澄清流程意味着特定的设施足迹会转化为重要的资本成本。压载絮凝包括注入压载介质以增加絮凝比重和尺寸,由于其具有很高的表观速度设计潜力,因此越来越多地用于水工业。但是,尚未提出系统的方法来针对其比重和尺寸比较和选择合适的压载介质。为了促进该程序,该研究项目探索了絮凝性能受可用于压载絮凝的介质表面积控制的假设。通过评估五个比重不同且比重不同的压载介质,在实验室规模上测试了该假设:粒状活性炭,无烟煤,硅砂,钛铁矿和比重分别为1.24、1.45、2.62、3.70和5.08的磁铁矿砂。通过显微镜测量絮凝物的大小并用直接安装在广口瓶试验烧杯上的照相机来监测絮凝动力学。使用浊度测量监测沉降性能。这项研究表明,所有压载介质以絮凝过程中可用的总表面表示时,都需要相似的表面浓度才能使沉降的水浊度接近1 NTU或更低。此外,镇流器介质尺寸和比重的影响降低了,沉降时间超过3分钟。相反,对于12 s的沉降时间,较大和较密的介质产生的沉降水浊度较低。对于某些应用,较轻的压载介质可能更经济,因为对于给定的质量浓度,它们会提供更多的可用表面积,因此减少了絮凝池中所需的压载介质的数量。最后,零电荷和形状的压载介质点未被确定为压载絮凝的关键标准。 (C)2018 Elsevier Ltd.保留所有权利。

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