Use of three-dimensional computational fluid dynamics model for a new configuration of circular primary settling tank

被引:8
作者
Griborio, A. G. [1 ]
Rodriguez, J. A. [2 ]
Enriquez, L. [2 ]
McCorquodale, J. A. [3 ]
机构
[1] Hazen & Sawyer PC, 4000 Hollywood Blvd 750N, Hollywood, FL 33021 USA
[2] Univ Valle, EIDENAR, Fac Engn, Cali, Colombia
[3] Univ New Orleans, Dept Civil Engn, New Orleans, LA 70122 USA
关键词
center well; circular primary settling tank; computational fluid dynamics; POTABLE WATER-TREATMENT; NUMERICAL-SIMULATION; WASTE-WATER; SECONDARY CLARIFIERS; SEDIMENTATION TANKS; FLOW; PERFORMANCE; CFD; FLOCCULATION; DESIGN;
D O I
10.2166/wst.2021.110
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Appropriately used, CFD models are powerful tools to design and optimize primary settling tanks (PSTs). This paper uses a Fluent-based 3D model to identify the possible causes for underperformance of the circular PSTs at the Cali WWTP, Colombia, and to propose design modifications to improve performance. A new configuration for the center well (CW) is proposed and evaluated. The influence of a rotational sludge scraper and of continuously sludge removal were considered in the numerical simulation. The new configuration included the modification of the current CW diameter and the location of a second baffle with the CW. The results suggest that the installation of the second baffle allows a more uniform flow distribution within the PST and consequently, the hydrodynamic problems associated with short-circuiting of the influent to the bottom of the tank are reduced. The second baffle suppresses the downward current, effectively dissipates the kinetic energy in the influent and forces the particles to move toward the bottom of the PST. In addition, the second CW baffle allows the formation in the inlet zone of a consistently more concentrated sludge blanket layer and thicker sludge, reducing the risk of solids leaving in the effluent of the PST.
引用
收藏
页码:333 / 348
页数:16
相关论文
共 97 条
[1]   SIMULATION OF PARTICLE CONCENTRATION DISTRIBUTION IN PRIMARY CLARIFIERS [J].
ABDELGAWAD, S ;
MCCORQUODALE, JA .
CANADIAN JOURNAL OF CIVIL ENGINEERING, 1985, 12 (03) :454-463
[2]   MODELING FLOW AND MIXING IN SEDIMENTATION TANKS [J].
ADAMS, EW ;
RODI, W .
JOURNAL OF HYDRAULIC ENGINEERING-ASCE, 1990, 116 (07) :895-913
[3]   Large-eddy simulations of particle sedimentation in a longitudinal sedimentation basin of a water treatment plant. Part I: Particle settling performance [J].
Al-Sammarraee, M. ;
Chan, A. ;
Salim, S. M. ;
Mahabaleswar, U. S. .
CHEMICAL ENGINEERING JOURNAL, 2009, 152 (2-3) :307-314
[4]  
ALARIE RL, 1980, J ENV ENG DIV-ASCE, V106, P293
[5]  
Amini, 2016, P 9 INT C MULT FLOW
[6]   Experimental Study and Computational Fluid Dynamics Simulation of a Full-Scale Membrane Bioreactor for Municipal Wastewater Treatment Application [J].
Amini, Ershad ;
Mehrnia, Mohammad Reza ;
Mousavi, Seyyed Mohammad ;
Mostoufi, Navid .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (29) :9930-9939
[7]  
Amini S., 2011, P 10 INT C CIRC FLUI
[8]  
ANSYS, 2016, ANSYS Fluent Theory Guide
[9]  
Applegate C.S., 2010, P WEFTEC 83 ANN TECH, DOI [10.2175/193864710798194201, DOI 10.2175/193864710798194201]
[10]   Experimental investigation of effects of baffle configurations on the performance of a secondary sedimentation tank [J].
Asgharzadeh, H. ;
Firoozabadi, B. ;
Afshin, H. .
SCIENTIA IRANICA, 2011, 18 (04) :938-949