Computer Aided Thermal Fluid Analysis Lecture 10

Slides:



Advertisements
Similar presentations
Lecture 15: Capillary motion
Advertisements

Direct Forcing Immersed Boundary (DFIB) Method for Mixed Heat Transfer
Convection.
Turbulent Models.  DNS – Direct Numerical Simulation ◦ Solve the equations exactly ◦ Possible with today’s supercomputers ◦ Upside – very accurate if.
Estimation of Convective Heat Transfer Coefficient
Computer Aided Thermal Fluid Analysis Lecture 2 Dr. Ming-Jyh Chern ME NTUST.
An Analysis of Hiemenz Flow E. Kaufman and E. Gutierrez-Miravete Department of Engineering and Science Rensselaer at Hartford.
1 “CFD Analysis of Inlet and Outlet Regions of Coolant Channels in an Advanced Hydrocarbon Engine Nozzle” Dr. Kevin R. Anderson Associate Professor California.
Transport phenomena in chemical processes part III Michał Araszkiewicz PhD.
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.
Convection Convection Matt Penrice Astronomy 501 University of Victoria.
Internal Flow: Heat Transfer Correlations
Flow over an Obstruction MECH 523 Applied Computational Fluid Dynamics Presented by Srinivasan C Rasipuram.
Computer Aided Thermal Fluid Analysis Lecture 7 Dr. Ming-Jyh Chern ME NTUST.
Sensible heat flux Latent heat flux Radiation Ground heat flux Surface Energy Budget The exchanges of heat, moisture and momentum between the air and the.
Engineering H191 - Drafting / CAD The Ohio State University Gateway Engineering Education Coalition Lab 4P. 1Autumn Quarter Transport Phenomena Lab 4.
1 B. Frohnapfel, Jordanian German Winter Academy 2006 Turbulence modeling II: Anisotropy Considerations Bettina Frohnapfel LSTM - Chair of Fluid Dynamics.
CHE/ME 109 Heat Transfer in Electronics LECTURE 18 – FLOW IN TUBES.
Why Laminar Flow in Narrow Channels (Heat Transfer Analysis)
Reynolds Experiment Laminar Turbulent Reynolds Number
CHE/ME 109 Heat Transfer in Electronics
Fluid Dynamics: Boundary Layers
Flow and Thermal Considerations
FUNDAMENTAL EQUATIONS, CONCEPTS AND IMPLEMENTATION
Computer Aided Thermal Fluid Analysis Lecture 11 Dr. Ming-Jyh Chern ME NTUST.
ERT 209 HEAT & MASS TRANSFER Sem 2/ Prepared by; Miss Mismisuraya Meor Ahmad School of Bioprocess Engineering University Malaysia Perlis 17 February.
Lecture Objectives: -Define turbulence –Solve turbulent flow example –Define average and instantaneous velocities -Define Reynolds Averaged Navier Stokes.
Governing equations: Navier-Stokes equations, Two-dimensional shallow-water equations, Saint-Venant equations, compressible water hammer flow equations.
1 CHAPTER 6 HEAT TRANSFER IN CHANNEL FLOW 6.1 Introduction (1) Laminar vs. turbulent flow transition Reynolds number is where  D tube diameter  u mean.
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
Lesson 13 CONVECTION HEAT TRANSFER Given the formula for heat transfer and the operating conditions of the system, CALCULATE the rate of heat transfer.
Chapter 6 Introduction to Forced Convection:
Nazaruddin Sinaga Laboratorium Efisiensi dan Konservasi Energi Fakultas Teknik Universitas Diponegoro.
Laminar Natural Convection in 2D Glazing Cavities
HEAT TRANSFER FINITE ELEMENT FORMULATION
FREE CONVECTION 7.1 Introduction Solar collectors Pipes Ducts Electronic packages Walls and windows 7.2 Features and Parameters of Free Convection (1)
Quantification of the Infection & its Effect on Mean Fow.... P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Modeling of Turbulent.
Reynolds Analogy It can be shown that, under specific conditions (no external pressure gradient and Prandtle number equals to one), the momentum and heat.
Compressibility and Heat Transfer Effects on Boundary Layers L. Sankar November 30, 2004.
INTRODUCTION TO CONVECTION
Sarthit Toolthaisong FREE CONVECTION. Sarthit Toolthaisong 7.2 Features and Parameters of Free Convection 1) Driving Force In general, two conditions.
MULTLAB FEM-UNICAMP UNICAMP Workshop on Thermal Boundary Conditions Several thermal boundary conditions will be explored in this workshop modifying the.
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.

ARSM -ASFM reduction RANSLESDNS 2-eqn. RANS Averaging Invariance Application DNS 7-eqn. RANS Body force effects Linear Theories: RDT Realizability, Consistency.
APPLICATION TO EXTERNAL FLOW
Pipe flow analysis.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
University of Wisconsin -- Engine Research Center slide 1 Flamelet Modeling for the Diffusion Combustion in OpenFOAM ME 769 Final Project Presentation.
Turbulent Fluid Flow daVinci [1510].
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
Objective Introduce Reynolds Navier Stokes Equations (RANS)
Introduction to the Turbulence Models
Chapter 8: Internal Flow
Chamber Dynamic Response Modeling
Penetration Buoyant flow inside cavity Conference paper UKHTC 2011
Lecture Objectives Learn about Implementation of Boundary Conditions
Viscous Flow in Pipes.
Fundamentals of Convection
9th Lecture : Turbulence (II)
Heat Transfer Coefficient
Thermal behavior of the LHCb PS VFE Board
Lecture Objectives: Boundary Conditions Project 1 (software)
Heat Transfer In Channels Flow
Lecture Objectives: Start using CFD Software Class project 1
Convective Heat Transfer
14. Computational Fluid Dynamics
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Presentation transcript:

Computer Aided Thermal Fluid Analysis Lecture 10 Dr. Ming-Jyh Chern ME NTUST

Road Map for Today What is turbulence? Reynolds Averaged Navier-Stokes (RANS) equations Turbulence models Boundary conditions for turbulence models

What is turbulence? Part I

What is turbulence? Part II Let us see a movie regarding a turbulent flow in a valve.

What is turbulence? Part III – Its nature Random Effective Mixing High Reynolds number 3-D Energy Dissipation Eddy Motions

What is turbulence? Energy Cascade

Reynolds Decomposition

Reynolds Averaged Navier-Stokes (RANS) equations is the so-called Reynolds stress.

Boussinesq’s Assumption How to determine eddy viscosity nt?

Zero equation model nt is assumed to be a constant and depends on various flow fields.

One equation model

Two equations model

K-e turbulence model

K-e turbulence model

Boundary conditions Inlet Conditions

Boundary conditions for a solid wall 1. Wall function

Boundary conditions for a solid wall 1. Wall function

Boundary conditions for a solid wall 2. Two Layer Method

Boundary conditions for a solid wall 2. Two Layer Method

Example – Sudden Expansion Flow ui 0.1 m 0.13 m 1 m 2.5 m

Example – Sudden Expansion Flow – establish mesh

Example – Sudden Expansion Flow – Laminar Flow Case Working fluids – air Density = 1.205 m3/s Dynamics viscosity = 1.81e-5 kg/ms Characteristic length = 0.1 m If we consider a laminar channel flow at Re = 100, then the magnitude of inlet velocity must be 0.015 m/s.

Example – Sudden Expansion Flow – Boundary setup Outlet or constant pressure boundary Symmetry boundary Symmetry boundary Inlet boundary

Example – Sudden Expansion Flow – Results of laminar Flow

Example – Sudden Expansion Flow – Turbulent Flow Case Working fluids – air Density = 1.205 m3/s Dynamics viscosity = 1.81e-5 kg/ms Characteristic length = 0.1 m If we consider a turbulent channel flow at Re = 30,000, then the magnitude of inlet velocity must be 4.5 m/s. k and e at the inlet boundary (k = 0.30375, e = 7.859).

Example – Sudden Expansion Flow – Results of Turbulent Flow Contours of k

Simulation of Heat Transfer Forced convection or natural convection? Boundary conditions, a. isothermal boundary, b. constant heat flux. Conjugate heat transfer? Heat sources should be imposed inside solids.

Example – Forced convection with isothermal boundary ui 0.1 m 0.13 m 1 m 2.5 m T = 313 K The constant wall temperature is 293 K, except for the orange region at which the temperature is 313 K.

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary

Example – Forced convection with isothermal boundary Isothermal contours

Example – Natural convection with isothermal boundary T = 293 K g 0.01 m Adiabatic boundary Adiabatic boundary 0.01 m T = 294 K

Example – Natural convection with isothermal boundary

Example – Natural convection with isothermal boundary Boussinesq’s approximation: assume the buoyant force f in N-S equations is

Example – Natural convection with isothermal boundary

Example – Natural convection with isothermal boundary

Example – Natural convection with isothermal boundary

Example – Natural convection with isothermal boundary Isothermal contours

Example – Conjugate Heat Transfer Heat conduction in a solid and convection in a fluid are considered in conjugate heat transfer. At least, two materials shall be defined as a fluid and a solid in the model, respectively.

Example – Conjugate Heat Transfer .

Example – Conjugate Heat Transfer T = 293 K air g 0.01 m Adiabatic boundary Adiabatic boundary 0.01 m Al T = 294 K

Example – Conjugate Heat Transfer 1 3 2

Example – Conjugate Heat Transfer 4. Choose a solid material from the table or creat a new one. Do not forget to click apply.

Example – Conjugate Heat Transfer 5. Use C> /NEW / Zone to select cells into cset.

Example – Conjugate Heat Transfer 6. Click Tools/Cell Tools to set Type 2 Solid to Material 2

Example – Conjugate Heat Transfer 7. Use cell list to change cells in cset to the type 2 solid

Example – Conjugate Heat Transfer 8. Check if there are two different kinds of cells. Red one is fluid 1. Green one is solid 2.

Example – Conjugate Heat Transfer Go back to STAR Guide. Click Thermal Options. Click Heat Transfer ON. The rest procedures for simulation of natural convection are as same as the previous example.

Example – Conjugate Heat Transfer Iosthermal contours + Velocity vectors