2009 January 10-12 www.kostic.niu.edu 1 Computational Fluid Dynamics Simulation of Open-Channel Flows Over Bridge-Decks Under Various Flooding Conditions.

Slides:



Advertisements
Similar presentations
Fluid Mechanics Research Group Two phase modelling for industrial applications Prof A.E.Holdø & R.K.Calay.
Advertisements

SolidWorks Flow Simulation
Lecture 15: Capillary motion
Convection.
The analysis of the two dimensional subsonic flow over a NACA 0012 airfoil using OpenFoam is presented. 1) Create the geometry and the flap Sequence of.
University of Western Ontario
Boundary Layer Flow Describes the transport phenomena near the surface for the case of fluid flowing past a solid object.
2003 International Congress of Refrigeration, Washington, D.C., August 17-22, 2003 CFD Modeling of Heat and Moisture Transfer on a 2-D Model of a Beef.
Computational Modeling of Flow over a Spillway In Vatnsfellsstífla Dam in Iceland Master’s Thesis Presentation Chalmers University of Technology 2007.
1 “CFD Analysis of Inlet and Outlet Regions of Coolant Channels in an Advanced Hydrocarbon Engine Nozzle” Dr. Kevin R. Anderson Associate Professor California.
Project #4: Simulation of Fluid Flow in the Screen-Bounded Channel in a Fiber Separator Lana Sneath and Sandra Hernandez 4 th year - Biomedical Engineering.
Who Wants to Be a CFD Expert? In the ME 566 course title, CFD for Engineering Design, what does the acronym CFD stand for? A.Car Free Day B.Cash Flow Diagram.
Adam Koenig, Wichita State University Mentors: Dr. Ron Riggs, University of Hawai’i, Manoa Dr. Sungsu Lee, Chungbuk National University Krystian Paczkowski,
UNICAMP THE HEIGHT OF LIQUID METHOD FOR FREE SURFACE FLOWS Flow simulations of real processes often involve fluids that are separated by a sharp interface.
Experimental and Numerical Study of the Effect of Geometric Parameters on Liquid Single-Phase Pressure Drop in Micro- Scale Pin-Fin Arrays Valerie Pezzullo,
Flow over an Obstruction MECH 523 Applied Computational Fluid Dynamics Presented by Srinivasan C Rasipuram.
Engineering H191 - Drafting / CAD The Ohio State University Gateway Engineering Education Coalition Lab 4P. 1Autumn Quarter Transport Phenomena Lab 4.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
D A C B z = 20m z=4m Homework Problem A cylindrical vessel of height H = 20 m is filled with water of density to a height of 4m. What is the pressure at:
2009 January 10-12www.kostic.niu.edu CFD Simulation of Open Channel Flooding Flows and Scouring Around Bridge Structures The 6th WSEAS International Conference.
2009 January 10-12© M. Kostic Prof. M. Kostic Mechanical Engineering NORTHERN ILLINOIS UNIVERSITY The CFD Simulation of Flooding Flows and Scouring Around.
University of South Carolina FCR Laboratory Dept. of Chemical Engineering By W. K. Lee, S. Shimpalee, J. Glandt and J. W. Van Zee Fuel Cell Research Laboratory.
Image courtesy of National Optical Astronomy Observatory, operated by the Association of Universities for Research in Astronomy, under cooperative agreement.
Fluid Mechanics Wrap Up CEE 331 June 27, 2015 CEE 331 June 27, 2015 
California State University, Chico
Introduction to Convection: Flow and Thermal Considerations
DETAILED TURBULENCE CALCULATIONS FOR OPEN CHANNEL FLOW
Fluid mechanics 3.1 – key points
LAMINAR PLANE COUETTE AND OPEN CHANNEL FLOW
FUNDAMENTAL EQUATIONS, CONCEPTS AND IMPLEMENTATION
Introduction to Convection: Flow and Thermal Considerations
Introduction to COMSOL Travis Campbell Developed for CHE 331 – Fall 2012 Oregon State University School of Chemical, Biological and Environmental Engineering.
CFD Modeling of Turbulent Flows
Introduction Aerodynamic Performance Analysis of A Non Planar C Wing using Experimental and Numerical Tools Mano Prakash R., Manoj Kumar B., Lakshmi Narayanan.
In-term project presentation by Kanish Jindal Modeling of chlorine contact chamber at West Lafayette treatment plant.
Governing equations: Navier-Stokes equations, Two-dimensional shallow-water equations, Saint-Venant equations, compressible water hammer flow equations.
Mathematical Equations of CFD
Momentum Equations in a Fluid (PD) Pressure difference (Co) Coriolis Force (Fr) Friction Total Force acting on a body = mass times its acceleration (W)
Mass Transfer Coefficient
1 MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 6: DIMENTIONAL ANALYSIS Instructor: Professor C. T. HSU.
Chapter 6 Introduction to Forced Convection:
A canopy model of mean winds through urban areas O. COCEAL and S. E. BELCHER University of Reading, UK.
Order of Magnitude Scaling of Complex Engineering Problems Patricio F. Mendez Thomas W. Eagar May 14 th, 1999.
Unit 1: Fluid Dynamics An Introduction to Mechanical Engineering: Part Two Fluid dynamics Learning summary By the end of this chapter you should have learnt.
Chapter 8: Flow in Pipes.
Fluid Dynamics Stream Ecosystems. Fluid Dynamics Lecture Plan First consider fluids, stress relationships and fluid types Then consider factors affecting.
ME 101: Fluids Engineering Chapter 6 ME Two Areas for Mechanical Engineers Fluid Statics –Deals with stationary objects Ships, Tanks, Dams –Common.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 8: BOUNDARY LAYER FLOWS
INTRODUCTION TO CONVECTION

Turbulence Models Validation in a Ventilated Room by a Wall Jet Guangyu Cao Laboratory of Heating, Ventilating and Air-Conditioning,
Lecture Objectives: Define 1) Reynolds stresses and
Viscous Flow in Pipes: Overview
Pipe flow analysis.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
Indian Institute of Space Science and Technology STUDY OF EFFECT OF GAS INJECTION OVER A TORPEDO ON FLOW-FIELD USING CFD.
CFD Simulation Investigation of Natural Gas Components through a Drilling Pipe RASEL A SULTAN HOUSSEMEDDINE LEULMI.
Chapter 1: Basic Concepts
Chapter 8: Internal Forced Convection
The Standard, RNG, and Realizable k- Models. The major differences in the models are as follows: the method of calculating turbulent viscosity the turbulent.
Hamdache Abderrazaq 1*, Belkacem Mohamed 1, Hannoun Nourredine 2
Numerical Investigation of Turbulent Flows Using k-epsilon
The inner flow analysis of the model
Fluid Flow Regularization of Navier-Stokes Equations
Subject Name: FLUID MECHANICS
22nd hydrotech conference, 2015 Characteristics of siphon spillways R
The application of an atmospheric boundary layer to evaluate truck aerodynamics in CFD “A solution for a real-world engineering problem” Ir. Niek van.
FLUID MECHANICS REVIEW
Part VI:Viscous flows, Re<<1
Presentation transcript:

2009 January Computational Fluid Dynamics Simulation of Open-Channel Flows Over Bridge-Decks Under Various Flooding Conditions The 6th WSEAS International Conference on FLUID MECHANICS ( WSEAS - FLUIDS'09 ) Ningbo, China, January 10-12, 2009 S. Patil, M. Kostic and P. Majumdar Department of Mechanical Engineering NORTHERN ILLINOIS UNIVERSITY

2009 January Motivation :  Bridges are crucial constituents of the nation’s transportation systems  Bridge construction is critical issue as it involves great amount of money and risk  Bridge structures under various flood conditions are studied for bridge stability analysis  Such analyses are carried out by scaled experiments to calculate drag and lift coefficients on the bridge  Scaled experiments are limited to few design variations and flooded conditions due to high cost and time associated with them  Advanced commercial Computational Fluid Dynamics (CFD) software and parallel computers can be used to overcome such limitations

2009 January  CFD is the branch of fluid mechanics which uses numerical methods to solve fluid flow problems  In spite of having simplified equations and high speed computers, CFD can achieve only approximate solutions  CFD is a versatile tool having flexibility is design with an ability to impose and simulate real time phenomena  CFD simulations if properly integrated can complement real time scaled experiments  Available CFD features and powerful parallel computers allow to study wide range of design variations and flooding conditions with different flow characteristics and different flow rates  CFD simulation is a tool for through analysis by providing better insight of what is virtually happening inside the particular design

2009 January Literature Review:  Ramamurthy, Qu and Vo, conducted simulation of three dimensional free surface flows using VOF method and found good agreement between simulation and experimental results  Maronnier, Picasso and Rappaz, conducted simulation of 3D and 2D free surface flows using VOF method and found close agreement between simulation and experimental results.  Harlow, and Welch, wrote Navier stokes equations in finite difference forms with fine step advancement to simulate transient viscous incompressible flow with free surface. This technique is successfully applicable to wide variety of two and three dimensional applications for free surface  Koshizuka, Tamako and Oka, presented particle method for transient incompressible viscous flow with fluid fragmentation of free surfaces. Simulation of fluid fragmentation for collapse of liquid column against an obstacle was carried. A good agreement was found between numerical simulation and experimental data

2009 January Objectives:  The objective of the present study is to validate commercial code STAR-CD for hydraulic research  The experimental data conducted by Turner Fairbank Highway Research Center (TFHRC) at their own laboratories will be simulated using STAR-CD  The base case of Fr = 0.22 and flooding height ratio, h*=1.5 is simulated with appropriate boundary conditions corresponding to experimental testing  The open channel turbulent flow will be simulated using two different methods  First by transient Volume of Fluid (VOF) methodology and other as a steady state closed channel flow with top surface as slip wall  Drag and lift coefficients on the bridge is calculated using six linear eddy viscosity turbulence model and simulation outcome will be compared with experimental results

2009 January  The suitable turbulence model will be identified which predicts close to drag and lift coefficients  The parametric study will be performed for time step, mesh density and convergence criteria to identify optimum computational parameters  The suitable turbulence model will be used to simulate 13 different flooding height ratio from h*=0.3 to 3 for Fr =0.22

2009 January Experimental Data:  Experiments are conducted for open channel turbulent flow over six girder bridge deck for different flooding height ratios (h*) and with various flow conditions (Fr) L Bridge =0.34 m S=0.058 m ΔW Simulation = L Flow = 0.26 m Flow Direction Schematic of experimental six girder bridge deck model

2009 January Dimensions of experimental six girder bridge deck model L Flow X Y Nomenclature for bridge dimensions and flooding ratios Theory Flooding Ratio Froude Number

2009 January  Experimental data consists of drag and lift coefficients as the function of Froude number, Fr and dimensionless flooding height ratio h*  Experimental data consists of five different sets of experiments for Froude numbers from Fr =0.12 to 0.40 and upstream average velocity 0.20 m/s to 0.65 m/s  The experiments for the Froude number, Fr=0.22 are repeated four times with an average velocity of 0.35 m/s for h*=0.3 to 3  The lift coefficient is calculated by excluding buoyancy forces in Y (vertical) direction

2009 January

2009 January

2009 January Governing Equations for fluid flow:  Mass conservation equation  Momentum conservation equation  Energy conservation equation

2009 January Dimensionless parameters for open channel flow:  Reynolds Number y b For 2D open channel flow,

2009 January Froude Number:  Froude number is dimensionless number which governs character of open channel flow The flow is classified on Froude number Subcritical or tranquil flow Critical Flow Supercritical or rapid flow Open channel flow is dominated by inertial forces for rapid flow and by gravity forces for tranquil flow

2009 January Froude number is also given by Where Wave speed (m/s) = Flow depth (m)

2009 January Force Coefficients:  The component of resultant pressure and shear forces in direction of flow is called drag force and component that acts normal to flow direction is called lift force  Drag force coefficient is  Lift force coefficient is  In the experimental testing, the drag reference area is the frontal area normal to the flow direction. The lift reference area is the bridge area perpendicular to Y direction.

2009 January Drag and lift reference areas for experimental data: For drag, if,then drag area is if,then drag area is For lift, for all,lift area is

2009 January Turbulent Flow:  Turbulent flow is complex phenomena dominated by rapid and random fluctuations  Turbulent flow is highly unsteady and all the formulae for the turbulent flow are based on experiments or empirical and semi – empirical correlations  Turbulent Intensity  Turbulence mixing length (m)  Turbulent kinetic energy (m 2 /s 2 )

2009 January  Turbulence dissipation rate (m 2 /s 3 )  Specific dissipation rate (1/s)

2009 January Turbulence Models:  Six eddy viscosity turbulence models are studied from STAR-CD turbulence options  Two major groups of turbulence models k-ε and k-ω are studied  The k- ε turbulence model The k-ω turbulence models a. Standard High Reynolds a. Standard High Reynolds b. Renormalization Group b. Standard Low Reynolds c. SST High Reynolds d. SST Low Reynolds

2009 January The k-ε High Reynolds turbulence model:  Most widely used turbulent transport model  First two equation model to be used in CFD  This model uses transport equations for k and ε in conjunction with the law-of-the wall representation of the boundary layer The k-ε RNG turbulence model:  This turbulence model is obtained after modifying k-ε standard turbulence model using normalization group method to renormalize Navier Stokes equations  This model takes into account effects of different scales of motions on turbulent diffusion

2009 January k-ω turbulence model:  The k-ω turbulence models are obtained as an alternative to the k-ε model which have some difficulty for near wall treatment  The k-ω turbulence models Standard k-ω model Shear stress transport (SST) model High Reynolds Low Reynolds High ReynoldsLow Reynolds

2009 January SST k-ω turbulence model:  SST turbulence model is obtained after combining best features of k-ε and k-ω turbulence model  SST turbulence model is the result of blending of k-ω model near the wall and k-ε model near the wall

2009 January Computational Model:  STAR-CD (Simulation of Turbulent flow in Arbitrary Regions Computational Dynamics) is CFD analysis software  STAR-CD is finite volume code which solves governing equations for steady state or transient problem  The first method used in STAR-CD to simulate open channel turbulent flow is free surface method which makes use of Volume of Fluid (VOF) methodology  VOF methodology simulates air and water domain  VOF methodology uses volume of fraction variable to capture air- water interface

2009 January VOF technique:  VOF technique is a transient scheme which captures free surface.  VOF deals with light and heavy fluids  VOF is the ratio of volume of heavy fluid to the total control volume  Volume of fraction is given by  Transport equation for volume of fraction  Volume fraction of the remaining component is given by

2009 January  The properties at the free surface vary according to volume fraction of each component

2009 January Free Surface method: Dimensions for computational model h*=1.5 generated in STAR-CD (Dimensions not to scale and in SI units) 0 Y X Z

2009 January Computational Mesh: Full computational domain with non uniform mesh and 2 cells thick in Z direction for =1.5 Y X Y

2009 January Boundary Conditions: Bottom Wall (No Slip) Top wall (slip) Water Inlet Air Inlet Outlet Symmetry Plane X Y Z Y

2009 January Computational parameters for VOF methodology: Inlet velocity, U0.35 m/s Turbulent kinetic energy, k m 2 /s 2 Turbulent Dissipation Rate, ε m 2 /s 3 Solution methodTransient Solver methodAlgebraic Multigrid approach (AMG) Solution algorithmSIMPLE Relaxation factorPressure Momentum, Turbulence, Viscosity Differencing schemeMARS Convergence Criteria10 -2 Time Step (Δt)0.01 s

2009 January Water slip top wall method: Y X Z Dimensions for computational model h*=1.5 for water slip –top-wall method (Dimensions not to scale and in SI units)

2009 January Boundary conditions: Top wall (slip) Bottom wall (No slip) Outlet (Standard) Symmetry Plane X Y X Y Water Inlet Computational domain with boundary surfaces and boundary conditions for water slip-top-wall method

2009 January Computational parameters for water slip-top-wall method: Inlet velocity, Turbulent kinetic energy, Turbulent Dissipation Rate, 0.35 m/s m 2 /s m 2 /s 3 Solution MethodSteady State Solver MethodAlgebraic Multigrid approach (AMG) Solution AlgorithmSIMPLE Relaxation factorPressure Momentum, turbulence, Viscosity Differencing schemeUD Convergence Criteria10 -6

2009 January STAR-CD simulation Validation with basics of fluid mechanics : Fully developed velocity profile for laminar pipe flow after STAR-CD simulation

2009 January Fully developed velocity profile for the turbulent pipe flow after STAR-CD simulation

2009 January Flow typeWall Roughness (m) Theoretical friction factor (Reference) Simulation friction factor Absolute Difference Percentage Difference LaminarSmooth TurbulentSmooth Turbulent Turbulent Turbulent Comparison between theoretical and simulated friction factor :

2009 January Calculation of entrance length: Continued on next page

2009 January

2009 January Verification of power law velocity profile:

2009 January Comparison between Fluent and STAR-CD for same geometry: X Y Operating ConditionVariables Inlet VelocityU = 2 m/s Inlet turbulence intensity10 % Inlet turbulence mixing length0.1 m Outlet gauge pressure0 Pa WallsNo Slip Convergence0.001

2009 January Comparison for velocity contours between STAR-CD and Fluent

2009 January Comparison for velocity vectors between STAR-CD and Fluent

2009 January Comparison for X velocities between Fluent and STAR-CD

2009 January ParameterFluentSTAR-CD (Reference Data) Absolute Difference Percentage Difference ΔP STAT % ΔP TOT % Pressure difference ( Pa ) 3.97 % CLCL 5.5 % CDCD Percentage Difference Absolute Difference STAR-CD (Reference Data) FluentForce Coefficients Force Coefficients

2009 January VOF simulation of experimental data: Effect of time steps on drag coefficients

2009 January Effect of time steps on lift coefficients:

2009 January Effect of decreased downstream length on force coefficients

2009 January Effect of decrease in under bridge water depth

2009 January Effect of top boundary condition at top as slip wall and symmetry

2009 January Free Surface Development: Nomenclature for VOF contour plot Free surface, Volume fraction for water

2009 January t=10sec t=30sec t=50 sec t=150 sec t=200 sec sec t=300 sec t =250 sec t=100se c Effect of k-ε standard turbulence model on free surface development:

2009 January Effect of different turbulence models on drag coefficients:

2009 January Effect of different turbulence models on lift coefficients:

2009 January Turbulence Models h* up h* dw h* avg C D avg C D exp C L avg C L exp k-ε High Re k-ε RNG k-ω STD High Re k-ω STD Low Re k-ω SST High Re k-ω SST Low Re h* up h* dw h* avg C D avg C D exp C L avg C L exp Count6.00 Maximum Average Std. Dev Minimum Comparison between simulation results for different turbulence model and experimental results:

2009 January Water slip-top-wall method: (a) Basic Coarse mesh (b) Refined near bridge (c) Fully refined model 0 % (Ref) % (Ref) Fully refined model 0.08 % % Refined near bridge 0.54% % Basic coarse grid % DifferenceCLCL CDCD Mesh Density

2009 January % % % % % (ref) % (ref) % differenceCLCL CDCD Convergence criteria Effect of convergence criteria on final solution:

2009 January Comparison between VOF and Water slip-top-wall method with experimental results:

2009 January Drag coefficient, C D Lift Coefficient, C L Turbulence modelVOFExp.Water slip-top- wall VOFExp. Water slip- top-wall k-ε High Re k-ε RNG k-ω STD High Re k-ω STD Low Re k-ω SST High Re k-ω SST Low Re The k-ε RNG predicts closet drag and lift coefficients

2009 January Effect of inlet turbulence on drag and lift coefficients:

2009 January Fully developed velocity profile after selected runs:

2009 January Fully developed turbulence kinetic energy after selected runs:

2009 January Fully developed turbulence dissipation rate after selected runs:

2009 January h *CFD Simulation Experimental (Reference) Absolute Difference Percentage Difference Comparison between CFD simulations and experimental data for Fr=0.22 for drag coefficients:

2009 January h *CFD Simulation Experimental (Reference) Absolute Difference Percentage Difference Comparison between CFD simulation and experimental data for Fr=0.22 for lift coefficients:

2009 January

2009 January

2009 January Conclusion:  CFD simulations by STAR-CD for Fr=0.22 case, predicts more drag than experimental drag except for h*=0.289  The percentage difference if the experimental data is taken as reference, is maximum of 67% for h*=0.972 and minimum of 15% for h* =0.289  For lift predictions, for cases of h* 1, CFD simulations predict lower lift than experimental

2009 January Recommendations for future work:  VOF simulations are run for convergence criterion of VOF should be run for more convergence criterion and that is only available with large computing power.  VOF simulations should be run for lower time step than 0.01 sec and for longer simulation time up to 500 sec.  In this study only linear eddy viscosity turbulence models are used. The effect of Large Eddy Simulation, Reynolds stress models and non linear eddy viscosity turbulence models should be tested on force coefficients

2009 January Acknowledgments: The authors like to acknowledge support by Dean Promod Vohra, College of Engineering and Engineering Technology of Northern Illinois University (NIU), and Dr. David P. Weber of Argonne National Laboratory (ANL); and especially the contributions by Dr. Tanju Sofu, and Dr. Steven A. Lottes of ANL, as well as financial support by U.S. Department of Transportation (USDOT) and computational support by ANL’s Transportation Research and Analysis Computing Center (TRACC).

2009 January QUESTIONS ??? More information at: