Solution to More Thermo-Mechanical Problems using Laplace Equations

Slides:



Advertisements
Similar presentations
Fourier’s Law and the Heat Equation
Advertisements

Basic law of heat conduction --Fourier’s Law Degree Celsius.
Navier-Stokes Equation
Heat Transfer Chapter 2.
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
One Dimensional Polar Geometries For Conduction with Heat Generation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A.
The Heat Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Easy Solution to Industrial Heat Transfer.
Solutions of the Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Idea Generates More Mathematics….
LINEAR SECOND ORDER ORDINARY DIFFERENTIAL EQUATIONS
CHAPTER 8 APPROXIMATE SOLUTIONS THE INTEGRAL METHOD
CHAPTER 7 NON-LINEAR CONDUCTION PROBLEMS
Scientific Computing Partial Differential Equations Introduction and
CHAPTER 2 ONE-DIMENSIONAL STEADY STATE CONDUCTION
1 CHAPTER 5 POROUS MEDIA Examples of Conduction in Porous Media component electronic micro channels coolant (d) coolant porous material (e) Fig.
Bessel Functions  Bessel functions, are canonical solutions y(x) of Bessel's differential equation: α (the order of the Bessel function) Bessel functions.
Boundary-Value Problems in Other Coordinates CHAPTER 14.
Biosystems engineering
CHAPTER 3 TWO-DIMENSIONAL STEADY STATE CONDUCTION
3. 3 Separation of Variables We seek a solution of the form Cartesian coordinatesCylindrical coordinates Spherical coordinates Not always possible! Usually.
Industrial Calculations For Transient Heat Conduction
Chapter 8 Partial Differential Equation. 8.1 Introduction Independent variables Formulation Boundary conditions Compounding & Method of Image Separation.
Two Dimensional Steady State Heat Conduction
One Dimensional Non-Homogeneous Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A truly non-homogeneous.
1 CHAPTER 9 PERTURBATION SOLUTIONS 9.1 Introduction Objective Definitions Perturbation quantity Basic Problem To construct an approximate solution to a.
One-Dimensional Steady-State Conduction
CHAPTER 3 EXACT ONE-DIMENSIONAL SOLUTIONS 3.1 Introduction  Temperature solution depends on velocity  Velocity is governed by non-linear Navier-Stokes.
1 CHAPTER 4 TRANSIENT CONDUCTION Neglect spatial variation: Criterion for Neglecting Spatial Temperature Variation Cooling of wire by surface convection:
Chapter 2 Introduction to Conduction. Conduction Rate Equation Cartesian Cylindrical Spherical Isotherm: The direction of heat flow will always be normal.
HEAT TRANSFER FINITE ELEMENT FORMULATION
Chapter 4 : Solution of Electrostatic ProblemsLecture 8-1 Static Electromagnetics, 2007 SpringProf. Chang-Wook Baek Chapter 4. Solution of Electrostatic.
FREE CONVECTION 7.1 Introduction Solar collectors Pipes Ducts Electronic packages Walls and windows 7.2 Features and Parameters of Free Convection (1)
One Dimensional Models for Conduction Heat Transfer in Manufacturing Processes P M V Subbarao Professor Mechanical Engineering Department I I T Delhi.
Chapter 2: Heat Conduction Equation
Boundary-Value Problems in Rectangular Coordinates
3.3 Separation of Variables 3.4 Multipole Expansion
1 Teaching Innovation - Entrepreneurial - Global The Centre for Technology enabled Teaching & Learning D M I E T R, Wardha DTEL DTEL (Department for Technology.
ERT 216 HEAT & MASS TRANSFER Sem 2/ Dr Akmal Hadi Ma’ Radzi School of Bioprocess Engineering University Malaysia Perlis.
HEAT TRANSFER Problems with FEM solution
Date of download: 7/9/2016 Copyright © ASME. All rights reserved. From: Convective Motion and Heat Transfer in a Slowly Rotating Fluid Quasi-Sphere With.
§ Separation of spherical variables: zonal harmonics Christopher Crawford PHY
AFE BABALOLA UNIVERSITY
One-Dimensional Steady-State Conduction
UNSTEADY-STATE HEAT CONDUCTION - II
Chapter 2: Introduction to Conduction
differential equations of heat transfer
Boundary-Value Problems in Rectangular Coordinates
Fourier’s Law and the Heat Equation
Chapter 3: One-Dimensional Steady-State Conduction
Fourier’s Law and the Heat Equation
Lecture 13 Contents Partial Differential Equations
Heat Diffusion Equation, Boundary Conditions and Initial Conditions
Ch9.8 (Ch16.2e) Heat Flow, or Diffusion, PDE
First order non linear pde’s
Ch 11.5: Further Remarks on Separation of Variables: A Bessel Series Expansion In this chapter we are interested in extending the method of separation.
Extended Surface Heat Transfer
Introduction to Partial Differential Equations
Chapter Three Section 3.5, Appendix C
More Non-Dimensional Models for Simple Heat Exchangers
§3.3.1 Separation of Cartesian variables: Orthogonal functions
ME/AE 339 Computational Fluid Dynamics K. M. Isaac Topic2_PDE
Simple ODEs to Study Thermofluids
Partial Differential Equations
Characteristics of Sturm-Liouville Problems
Step change in the boundary condition of conduction problems
P M V Subbarao Professor Mechanical Engineering Department I I T Delhi
Second Order-Partial Differential Equations
What are Fins ? Fins are extended surfaces used to increase the rate of heat transfer. It is made of highly conductive materials such as aluminum.
Solving Systems of Equations by Elimination Part 2
Example-cylindrical coordinates
Lecture 13 Contents Partial Differential Equations
Presentation transcript:

Solution to More Thermo-Mechanical Problems using Laplace Equations P M V Subbarao Professor Mechanical Engineering Department I I T Delhi A Rosetta Stone of Thermofluids …..

The Laplacian Operator In Cartesian Coordinates In Cylindrical Coordinates In Spherical Coordinates

Laplace Equations & Principle of Superposition : Laplace Equation

True 2D Problems : Steady Conduction in Plate Boundary conditions: x = 0 & 0 < y < H : T(0,y)= 0 x = W & 0 < y < H : T(W,y)= f1(y) y = 0 & 0 < x < W : T(x,0)= 0 y = H & 0 < x < W : T(x,H)= f2(x)

Principle of Superposition Let The Temperatures are determined by Boundary conditions: x = 0 & 0 < y < H :  (0,y)= 0 x = W & 0 < y < H :  (W,y)= 0 y = 0 & 0 < x < W :  (x,0)= 0 y = H & 0 < x < W :  (x,H)= f2(x) x = 0 & 0 < y < H :  (0,y)= 0 x = W & 0 < y < H :  (W,y)= f1(y) y = 0 & 0 < x < W :  (x,0)= 0 y = H & 0 < x < W :  (x,H)= 0

General Solutions :  Function Unused Boundary conditions: y = H & 0 < x < W :  (x,H)= f2(x)

General Solutions :  Function Unused Boundary conditions: x = W & 0 < y < H :  (W,y)= f1(y))

True 2D Problems : Steady Conduction in Plate Boundary conditions: x = 0 & 0 < y < H : T(0,y)= 0 x = W & 0 < y < H : T(W,y)= f1(y) y = 0 & 0 < x < W : T(x,0)= 0 y = H & 0 < x < W : T(x,H)= f2(x)

Simple Harmonic Functions as Solutions W Unused Boundary condition-1: x = W & 0 < y < H : T(W,y)= siny

Simple Harmonic Functions as Solutions W Unused Boundary condition -2: y = H & 0 < x < W : T(x,H)= sinx

Non-homogeneous Boundary Conditions for 2D Laplace Equation Method of Superposition: Decomposes the real problem ) ( y g x f L W o q ¢ ¥ T h , Example: Problem with 4 NHBC is decomposed into 4 problems each having one NHBC PDE

= + The Solution 3 2 4 ) ( y g x f L W q ¢ T h , x y L W T h , ) ( f g ¥ T h , = x y L W ¥ T h , 4 + ) ( f 3 g 2

Friction Welding of Two Solid Cylinders Radial and Axial Conduction in a Cylinder Two solid cylinders are pressed coaxially with a force F and rotated in opposite directions. Coefficient of friction is o r z ¥ T h , L w Convection at the outer surfaces. How to Achieve the Strong Weld?

Governing PDE in Cylindrical Coordinates Boundary conditions or finite

Separation of Variables Selecting the sign of the as positive.

The SO-ODE for Radial Distribution of Temperature  The General form of Bessel equation is This is a Bessel equation with m2=0 Solution to Bessel’s ODE

The SO-ODE for Axial Distribution of Temperature Complete solution

Application of Boundary Conditions or finite

Boundary Condition - 2 Define

Boundary Condition - 3

The Series Solution for Temperature

are orthogonal with respect to Boundary Condition - 4 Orthogonality Condition and are orthogonal with respect to Applying orthogonality gives the values of aj

Computation of Coefficients

The Final Equation for Temperature Disribution z ¥ T h , L w

Non-homogeneous Laplace Equations Example : Thermal Analysis of Nuclear Rods L a T o r q ¢ z Fig. 3.6 Solid cylinder generates heat at a rate One end is at while the other is insulated. Cylindrical surface is at Find the steady state temperature distribution.

Formulation of Problem Important Observations L a T o r q ¢ z Fig. 3.6 • Energy generation leads to NHDE • Define to make BC at surface homogeneous • Use cylindrical coordinates

Non-homogeneous Laplace Equation r q ¢ z Fig. 3.6 Boundary conditions (1) finite (2) (3) (4)

Solution to

The Solution Let: Split above equation: Let

Therefore • Guideline for splitting PDE and BC: should be governed by HPDE and three HBC. Let take care of the NH terms in PDE and BC

BC (1) finite (c-1) BC (2) (c-2) BC (3) Let (c-3)

Thus (d-1) BC (4) Let (c-4) Thus (d-2) Solution to (d)

(e) (i) Assumed Product Solution (f) (f) into (c), separating variables (g) (h)

(ii) Selecting the sign of the terms (i) (j) For (k)

(l) (iii) Solutions to the ODE (m) (j) is a Bessel equation with (n)

Solution to (k) and (l) (o) (p) Complete Solution: (q) (iv) Application of Boundary Conditions BC (c-1) to (n) and (p)

BC (c-4) to (m) and (o) BC (c-3) to (m) and (o) Equation for or (r) With The solutions to become

(s) BC (d-1) and (d-2) and (t) BC (c-2) (u)

(v) Orthogonality are solutions to equation (i). and Comparing (i) with eq. (3.5a) shows that it is a Sturm- Liouville equation with Eq. (3.6) gives and and 2 HBC at are orthogonal with respect to

Evaluating the integrals and solving for

Solution to (w) (5) Checking Dimensional check: Units of and of in solution (s) are in °C Limiting check: and