Department of Civil, Geological and Mining Engineering, Polytechnique Montreal, Quebec, H3C 3A7, Canada.
Department of Civil, Geological and Mining Engineering, Polytechnique Montreal, Quebec, H3C 3A7, Canada.
Water Res. 2018 Dec 15;147:25-32. doi: 10.1016/j.watres.2018.09.041. Epub 2018 Sep 27.
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.
传统的澄清工艺需要特定的设施占地面积,这会转化为重要的资本成本。由于具有设计非常高的表面流速的潜力,加重絮凝,包括注入加重介质以增加絮体的比重和尺寸,在水行业中越来越多地被使用。然而,尚未提出系统的方法来比较和选择适当的加重介质,以考虑其比重和尺寸。为了便于进行此程序,本研究项目探讨了以下假设:絮凝性能受可用于加重絮凝的介质表面积控制。通过评估五种具有不同比重和尺寸的加重介质,在实验室规模上对该假设进行了测试:颗粒活性炭、无烟煤、硅砂、钛铁矿和磁铁矿砂,其比重分别为 1.24、1.45、2.62、3.70 和 5.08。通过显微镜和直接安装在 jar 测试烧杯上的相机测量絮体尺寸来监测絮凝动力学。使用浊度测量来监测沉降性能。本研究表明,所有加重介质,当以絮凝过程中总表面积的形式表示时,都需要类似的表面浓度来实现接近 1 NTU 且更低的沉淀水浊度。此外,对于大于 3 分钟的沉降时间,加重介质的尺寸和比重的影响降低。相反,对于 12 秒的沉降时间,更大和更密的介质会产生更低的沉淀水浊度。对于某些应用,较轻的加重介质可能更经济,因为它们在给定的质量浓度下提供更多的可用表面积,从而减少絮凝罐中所需的加重介质的量。最后,加重介质的零电荷点和形状未被确定为加重絮凝的关键标准。