Improving the performance of industrial clarifiers using three-dimensional computational fluid dynamics

被引:30
|
作者
Das, Shankhadeep [1 ]
Bai, Hua [1 ]
Wu, Chunliang [2 ]
Kao, Jen-Hsiang [3 ]
Barney, Bryon [3 ]
Kidd, Mike [4 ]
Kuettel, Mark [4 ]
机构
[1] Dow Chem Co USA, Engn & Proc Sci, Freeport, TX USA
[2] Ansys Inc, Tech serv, Houston, TX 77094 USA
[3] Dow Chem Co USA, Environm Technol Ctr, Freeport, TX USA
[4] Dow Chem Co USA, Envinronm Operat, Freeport, TX USA
关键词
Clarifier; wastewater treatment; feedwell; energy dissipating inlet; total suspended solids; RECTANGULAR SETTLING TANKS; WATER TREATMENT PLANTS; SEDIMENTATION BASINS; CIRCULAR CLARIFIER; SEWAGE SLUDGES; FLOW; MODEL; SIMULATION; CLOSURE; DESIGN;
D O I
10.1080/19942060.2015.1121518
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Sedimentation is one of the most popular wastewater treatment processes, and is used to separate solid particles from carrier fluid in settling tanks known as clarifiers. The clarifier, as the last major facility in wastewater treatment plants (WWTPs), can limit or define the performance of the overall WWTP. This paper presents a novel three-dimensional unsteady computational fluid dynamics (CFD) model to improve the efficiency of an industrial clarifier that had been experiencing underperformance and reduction in wastewater handling capacity. We propose a numerical technique to address the transient process of removing sludge from the floor of clarifiers by using rotating rakes. The CFD model was first applied to analyzing the ramifications of the current clarifier geometry on performance. The results show that the root causes for underperformance are related to the unconventional top side feed design of the clarifier, which leads to significant asymmetry in the flow distribution. The CFD model was next used to investigate various design modifications with the goal of improving the clarifier performance. A few geometry modification ideas such as an inward baffle, dissipating inlets, and a submerged skirt were found to create a more uniform flow distribution in the clarifier, significantly reducing the backflow into the feedwell and the velocity of the flow exiting the feedwell, which helps the solid particles to settle in the clarifier. These three designs were found to reduce the effluent total suspended solids (TSS) by more than 80% and thus significantly improve clarifier performance. It is believed that the CFD model developed in this study can become a computationally efficient tool for investigating the performance of industrial clarifiers with complex geometries and rotating rakes.
引用
收藏
页码:130 / 144
页数:15
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