Numerical Simulation of Horizontal Sedimentation Tanks

卧式沉淀池数值模拟

基本信息

  • 批准号:
    10650545
  • 负责人:
  • 金额:
    $ 1.22万
  • 依托单位:
  • 依托单位国家:
    日本
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
  • 财政年份:
    1998
  • 资助国家:
    日本
  • 起止时间:
    1998 至 1999
  • 项目状态:
    已结题

项目摘要

A sedimentation tank is the most basic unit operation in water and wastewater treatment, however its design and operation are mostly done by experiences, as its behaviors are very complicated and hard to study. Introduction of numerical simulations instead of expensive pilot plant studies gave better insights of characteristics of sedimentation tanks. The flow in forizontal sedimentation tanks was simplified as two dimensions un-compressive unsteady flow, uniform settling velocity of particles, no scoring of settled particles, and constant temperature. Numerical Methos was SMAC, finite elements method, and Crank-Nicholson method. The influent flow went down rapidly forming density current along the bottom. If settling velocity was fast, the current climbed up from the bottom after the particles had settled and went along the surface to the outlet. There was a dead current zone at the upper part near to the inlet and another one at the lower part near to the outlet. Simulated tracer studies showed the actual detention time was only 10% of the nominal one. When the particles were hard to settle, the density current reached to the end of the tank. The settled flows separated from the current and rose to the surface and went along the surface to the outlet. Detention time was about 50%. The density current was considered as hinder sedimentation efficiency, however it seemed to help sedimentation very much as its depth was small and the travel distance of particles to the bottom became very short. If there was a mean to strengthen the current, the efficiency should improved. Small inlet opening, that created strong influent flow, generated a stronger doenward flow and improved the settling efficiency considerably. Numerical simulations were very effective tools for the study of sedimentation tanks.
沉淀池是水和废水处理中最基本的单元操作,但由于其行为非常复杂,难以研究,因此其设计和操作大多依靠经验。引入数值模拟而不是昂贵的试点工厂的研究提供了更好的见解沉淀池的特点。将强化沉淀池内的流动简化为二维无压非定常流动,颗粒沉降速度均匀,沉降颗粒无划痕,温度恒定。数值方法采用SMAC、有限元法和Crank-Nicholson法。进水流量迅速下降,沿着底部形成异重流。如果沉降速度快,则颗粒沉降后水流从底部向上爬升,并沿着表面到达出口。在靠近进口的上部存在一个死流区,在靠近出口的下部也存在一个死流区。模拟示踪剂研究表明,实际滞留时间仅为标称滞留时间的10%。当颗粒难以沉降时,异重流到达槽底。沉淀下来的水流从水流中分离出来,上升到水面,然后沿着水面流向出水口。滞留时间约为50%。异重流被认为是一种阻碍沉降的因素,但由于异重流的深度很小,颗粒到达底部的距离也很短,因此异重流似乎对沉降有很大的帮助。如果有一种方法来加强电流,效率应该提高。小的入口开口,创造了强大的进水流量,产生了更强的向下流动,并大大提高了沉降效率。数值模拟是研究沉淀池的有效工具。

项目成果

期刊论文数量(15)
专著数量(0)
科研奖励数量(0)
会议论文数量(0)
专利数量(0)
荒川 潤一郎: "横流式沈殿池の数値シミュレーション、沈降が悪い粒子が流況に及ぼす影響"第50回全国水道研究発表会講演集. 50. 36-87 (1999)
荒川纯一郎:“错流沉积池的数值模拟,难沉降颗粒对流态的影响”第50届全国供水研究会议论文集50. 36-87(1999)。
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    0
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荒川潤一郎: "横流式沈殿池の数値シミュレーション、沈降か悪い粒子が流況に及ぼす影響"第50回全国水道研究発表会講演集. 50. 86-87 (1999)
荒川纯一郎:“错流沉降池的数值模拟,沉积或不良颗粒对流动条件的影响”第50届全国供水研究会议论文集50. 86-87(1999)。
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    0
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Ryosuke Ishizuka: "Numerical Simulation of Horizontal Sedimentation Tanks, Change of Current by Settling Velocity and Shape of Inlet"51st Annual Conference of JWWA. 51. (2000)
Ryosuke Ishizuka:“卧式沉淀池的数值模拟,通过沉降速度和入口形状改变水流”JWWA 第 51 届年会。
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    0
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Junichiro, Arakawa: "Numerical Simulation of Horizontal Sedimentation Tanks, Effects of Poor Settling Particles"50th Annual Conference of JWWA. 50. 86-87 (2000)
Junichiro, Arakawa:“卧式沉淀池的数值模拟,不良沉降颗粒的影响”JWWA 第 50 届年会。
  • DOI:
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  • 影响因子:
    0
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大沢 延実: "沈殿池の数値シミュレーション、横流式沈殿池と放射流沈殿池の比較"第49回全国水道研究発表会講演集. 49. 88-89 (1998)
大泽伸美:《沉积盆地的数值模拟、水平流沉积盆地与径向流沉积盆地的比较》第49届全国供水研究会议论文集49. 88-89(1998)。
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AYA Hidenori其他文献

AYA Hidenori的其他文献

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{{ truncateString('AYA Hidenori', 18)}}的其他基金

Water Treatment by Submerged Membrane Separation in Sedimentation Tank with Powdered Activated Carbon Dosage
粉状活性炭投加沉淀池浸没式膜分离水处理
  • 批准号:
    07650644
  • 财政年份:
    1995
  • 资助金额:
    $ 1.22万
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
Reaction Kinetics of Membrane Separation Anaerobic Digestion
膜分离厌氧消化的反应动力学
  • 批准号:
    04650500
  • 财政年份:
    1992
  • 资助金额:
    $ 1.22万
  • 项目类别:
    Grant-in-Aid for General Scientific Research (C)
Two Phase Anaerobic Digestion in Membrane Separated Bio-Reactor
膜分离生物反应器中的两相厌氧消化
  • 批准号:
    63550400
  • 财政年份:
    1988
  • 资助金额:
    $ 1.22万
  • 项目类别:
    Grant-in-Aid for General Scientific Research (C)

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