Lecture Objectives: Boundary Conditions Project 1 (software)

Slides:



Advertisements
Similar presentations
Simulation of Turbulent Flows in Channel with Obstructions. Golovnya B. P. ISMEL, Cherkassy, Ukraine.
Advertisements

1 Application of for Predicting Indoor Airflow and Thermal Comfort.
Outline Overview of Pipe Flow CFD Process ANSYS Workbench
Basic Governing Differential Equations
Turbulent Models.  DNS – Direct Numerical Simulation ◦ Solve the equations exactly ◦ Possible with today’s supercomputers ◦ Upside – very accurate if.
Lecture Objectives: Simple algorithm Boundary conditions.
External Convection: Laminar Flat Plate
Lecture Objectives -Finish with modeling of PM -Discuss -Advance discretization -Specific class of problems -Discuss the CFD software.
..perhaps the hardest place to use Bernoulli’s equation (so don’t)
Computer Aided Thermal Fluid Analysis Lecture 10
Announcement Course Exam October 11 th (Tuesday) In class: 90 minutes long Examples are posted on the course website.
0.1m 10 m 1 km Roughness Layer Surface Layer Planetary Boundary Layer Troposphere Stratosphere height The Atmospheric (or Planetary) Boundary Layer is.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
CHE/ME 109 Heat Transfer in Electronics
Lecture Objectives: Finish with Solar Radiation and Wind Define Boundary Conditions at Internal Surfaces.
Lecture Objectives: Review discretization methods for advection diffusion equation Accuracy Numerical Stability Unsteady-state CFD Explicit vs. Implicit.
Lecture Objectives: -Define turbulence –Solve turbulent flow example –Define average and instantaneous velocities -Define Reynolds Averaged Navier Stokes.
Lecture Objectives Discuss specific class of problems
Next Class Final Project and Presentation – Prepare and me the ppt files 5-7 slides Introduce your problem (1-2 slides) – Problem – Why CFD? Methods.
Boundary Layer Laminar Flow Re ‹ 2000 Turbulent Flow Re › 4000.
ASRAE Student Branch meeting Speaker: Kenneth Simpson USGBC – LEED rating system Today at 5 pm ECJ
Mass Transfer Coefficient
Student Chapter Meeting Thursday, Sept. 3 rd 7pm ECJ Interested in HVAC design, MEP, or building environmental systems? Come learn about all of the.
Chapter 6 Introduction to Forced Convection:
Lecture Objectives Ventilation Effectiveness Thermal Comfort Meshing.
© Fluent Inc. 12/18/2015 D1 Fluent Software Training TRN Modeling Turbulent Flows.
CEE 262A H YDRODYNAMICS Lecture 13 Wind-driven flow in a lake.
FREE CONVECTION 7.1 Introduction Solar collectors Pipes Ducts Electronic packages Walls and windows 7.2 Features and Parameters of Free Convection (1)
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Reynolds Analogy It can be shown that, under specific conditions (no external pressure gradient and Prandtle number equals to one), the momentum and heat.
INTRODUCTION TO CONVECTION
CFD Lab 1 Simulation of Turbulent Pipe Flow Seong Mo Yeon, Timur Dogan, and Michael Conger 10/07/2015.
Sarthit Toolthaisong FREE CONVECTION. Sarthit Toolthaisong 7.2 Features and Parameters of Free Convection 1) Driving Force In general, two conditions.
Turbulence Models Validation in a Ventilated Room by a Wall Jet Guangyu Cao Laboratory of Heating, Ventilating and Air-Conditioning,
Lecture Objectives: Review discretization methods for advection diffusion equation –Accuracy –Numerical Stability Unsteady-state CFD –Explicit vs. Implicit.
Boundary Layer on a Flat Plate: Blasius Solution H z from Kundu’s book Assuming displacement of streamlines is negligible →u = U = constant everywhere,
Lecture Objectives: Define 1) Reynolds stresses and
BOUNDARY LAYERS Zone of flow immediately in vicinity of boundary Motion of fluid is retarded by frictional resistance Boundary layer extends away from.
External Flow: The Flat Plate in Parallel Flow Chapter 7 Section 7.1 through 7.3.
Lecture Objectives: - Numerics. Finite Volume Method - Conservation of  for the finite volume w e w e l h n s P E W xx xx xx - Finite volume.
Lecture Objectives Review wall functions Discuss: Project 1, HW2, and HW3 Project topics.
Convection Heat Transfer in Manufacturing Processes P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Mode of Heat Transfer due to.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
CONVECTION : An Activity at Solid Boundary P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Identify and Compute Gradients.
© Copyright 2014 COMSOL. Any of the images, text, and equations here may be copied and modified for your own internal use. All trademarks are the property.
GOVERNMENT ENGINEERING COLLEGE-BHUJ LAMINAR FLOW IN PIPES 
Objective Introduce Reynolds Navier Stokes Equations (RANS)
Chapter 8: Internal Flow
Lecture Objectives: Discus HW 1 Finish with Solar Radiation Components
Lecture Objectives: Answer questions related to HW 1
Lecture Objectives Discuss: Project 1 Diffuser modeling
Lecture Objectives Learn about particle dynamics modeling
Lecture Objectives: Answer questions related to HW 1
Objective Review Reynolds Navier Stokes Equations (RANS)
Lecture Objectives Learn about Implementation of Boundary Conditions
Lecture Objectives Finish with boundary conditions Unsteady State Flow.
*supported by the Army Research Office
Fundamentals of Convection
Natural Convection New terms Volumetric thermal expansion coefficient
Heat Transfer Coefficient
Lecture Objectives Review for exam Discuss midterm project
Objective Discuss Energy and Concentration conservation equations
Lecture Objectives: Simple Algorithm vs. Direct Solvers Discuss HW 3
Lecture Objectives Ventilation Effectiveness, Thermal Comfort, and other CFD results representation Surface Radiation Models Particle modeling.
Objectives Duct Design AND Diffuser Selection.
Lecture Objectives: Start using CFD Software Class project 1
Objective Discus Turbulence
Convective Heat Transfer
Section 8, Lecture 1, Supplemental Effect of Pressure Gradients on Boundary layer • Not in Anderson.
Lecture 4 Dr. Dhafer A .Hamzah
Presentation transcript:

Lecture Objectives: Boundary Conditions Project 1 (software)

Surface boundaries wall functions Wall surface Introduce velocity temperature and concentration Use wall functions to model the micro-flow in the vicinity of surface Using relatively large mesh (cell) size.

Surface boundaries wall functions Course mesh distribution in the vicinity of surface Y Wall surface Velocity in the first cell will depend on the distance y.

Surface boundary conditions and log-wall functions E is the integration constant and y* is a length scale Friction velocity u+=V/Vt y*=(n/Vt) y+=y/y* k- von Karman's constant The assumption of ‘constant shear stress’ is used here. Constants k = 0.41 and E = 8.43 fit well to a range of boundary layer flows. Surface cells Turbulent profile Laminar sub-layer

K-e turbulence model in boundary layer Wall shear stress Eddy viscosity V Wall function for e Wall function for k

Modeling of Turbulent Viscosity in boundary layer forced convection natural convection

Temperature and concentration gradient in boundary layer Depend on velocity field Temperature q=h(Ts-Tair) Concentration F=hc(Cs-Cair/m) m=Dair/Ds m- segregation coefficient h = f(V) = f(k,e) Tair Ts Into source term of energy equation hC = f(V, material prop.) Cair Cs

Project 1 Pat a) Numerical diffusion The purpose of this project part is to analyze how mesh size and orientation affects the accuracy of result. outlet inlet T1 T2 T1=30C T2=20C outlet inlet Pat b) Learn how to: 1) Model: geometry, heat sources, concentration sources, diffusers, 2) Select important simulation parameters 3) Generate appropriate mesh 4) Check the results 5) Present the results

AIRPAK Software

Example Modeling Problem Office ventilation (tutorial 1 in handouts posted on the website) Boundaries: Geometry:

Temperature and concentration gradient in boundary layer Depend on velocity field Temperature q=h(Ts-Tair) Concentration F=hc(Cs-Cair/m) m=Dair/Ds m- segregation coefficient h = f(V) = f(k,e) Tair Ts Into source term of energy equation hC = f(V, material prop.) Cair Cs

Inlets Diffuser Types Valve diffuser swirl diffusers ceiling diffuser wall or ceiling floor

Diffuser Types Grill (side wall) diffusers Linear diffusers Vertical Horizontal one side

Displacement ventilation diffusers

Diffuser modeling Complex geometry - Δ~10-4m We can spend all our momentum sources Momentum method Complex geometry - Δ~10-4m We can spend all our computing power for one small detail

Diffuser Modeling Fine mesh or box method for diffuser modeling

Jet parameters A0 - effective area of the diffuser V0 – initial jet velocity X - distance from the diffuser Vm – maximum jet velocity at distance x from the diffuser K – property of diffuser

Diffuser properties (ASHRAE) Fig. 1 Airflow patterns of different diffusers

Project 1 http://www.costco.com/.product.100222479.html