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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front Envir Sci Eng    2012, Vol. 6 Issue (5) : 638-648    https://doi.org/10.1007/s11783-012-0442-7
RESEARCH ARTICLE
Stormwater treatment: examples of computational fluid dynamics modeling
Gaoxiang YING1, John SANSALONE1(), Srikanth PATHAPATI1, Giuseppina GAROFALO1, Marco MAGLIONICO2, Andrea BOLOGNESI2, Alessandro ARTINA2
1. Engineering School of Sustainable Infrastructure and Environment, University of Florida, Gainesville, FL 32611-6450, USA; 2. DISTART, Universita di Bologna, Viale del Risorgimento 2, 40136 Bologna, Italia
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Abstract

Control of rainfall-runoff particulate matter (PM) and PM-bound chemical loads is challenging; in part due to the wide gradation of PM complex geometries of many unit operations and variable flow rates. Such challenges and the expense associated with resolving such challenges have led to the relatively common examination of a spectrum of unit operations and processes. This study applies the principles of computational fluid dynamics (CFD) to predict the particle and pollutant clarification behavior of these systems subject to dilute multiphase flows, typical of rainfall-runoff, within computationally reasonable limits, to a scientifically acceptable degree of accuracy. The Navier-Stokes (NS) system of nonlinear partial differential equations for multi-phase hydrodynamics and separation of entrained particles are solved numerically over the unit operation control volume with the boundary and initial conditions defined and then solved numerically until the desired convergence criteria are met. Flow rates examined are scaled based on sizing of common unit operations such as hydrodynamic separators (HS), wet basins, or filters, and are examined from 1 to 100 percent of the system maximum hydraulic operating flow rate. A standard turbulence model is used to resolve flow, and a discrete phase model (DPM) is utilized to examine the particle clarification response. CFD results closely follow physical model results across the entire range of flow rates. Post-processing the CFD predictions provides an in-depth insight into the mechanistic behavior of unit operations by means of three dimensional (3-D) hydraulic profiles and particle trajectories. Results demonstrate the role of scour in the rapid degradation of unit operations that are not maintained. Comparisons are provided between measured and CFD modeled results and a mass balance error is identified. CFD is arguably the most powerful tool available for our profession since continuous simulation modeling.

Keywords stormwater      unit operations and processes (UOPs)      hydrodynamic separation      filtration      adsorption      computational fluid dynamics (CFD)      turbulence modeling      discrete phase model      particle separation      detention/retention basins      clarification     
Corresponding Author(s): SANSALONE John,Email:jsansal@ufl.edu   
Issue Date: 01 October 2012
 Cite this article:   
Gaoxiang YING,John SANSALONE,Srikanth PATHAPATI, et al. Stormwater treatment: examples of computational fluid dynamics modeling[J]. Front Envir Sci Eng, 2012, 6(5): 638-648.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-012-0442-7
https://academic.hep.com.cn/fese/EN/Y2012/V6/I5/638
Fig.1  Isometric view of the screened HS
Fig.2  Profile view of the RCF apparatus.
Fig.3  Measured and modeled effluent concentrations measured as SSC for controlled prototype testing of the screened HS and RCF
Fig.4  Measured and modeled effluent PSD for controlled prototype testing of the screened HS and RCF
run #Q/(L·s-1)duration/mineffluent mass loadeffluent concentration
sump/cmmeasured/gmodeled/gRPD/%measured/(mg·L-1)modeled/(mg·L-1)RPD/%
138.81223321530604.81171124.3
231.11523276026902.5103993.9
331.11546451043234.11741655.2
438.81246548254211.11971922.5
Tab.1  Measured and modeled effluent mass loads and concentrations as a function of flow rate and depth of pre-loaded sediment in the screened HS; of the poorly-graded non-cohesive gradation with a of 110 μm
Fig.5  Measured and modeled pre-deposited PSDs and scoured effluent PSD for real-time testing of a screened HS
Fig.6  Influent hydrology for real-time testing of a screened HS
Fig.7  Measured and modeled influent PSD and separated PSD for real-time testing of a screened HS
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