Transient Conduction: The Lumped Capacitance Method

Slides:



Advertisements
Similar presentations
Extended Surfaces Chapter Three Section 3.6 Lecture 6.
Advertisements

BESSEL’S EQUATION AND BESSEL FUNCTIONS:
Transient Conduction: The Lumped Capacitance Method
Chapter 5 : Transient Conduction
Fourier’s Law and the Heat Equation
Fourier’s Law and the Heat Equation
Transient Conduction: Spatial Effects and the Role of Analytical Solutions Chapter 5 Sections 5.4 to 5.7 Lecture 10.
Chapter 2 Introduction to Heat Transfer
Extended Surfaces Chapter Three Section 3.6.
Heat Transfer Chapter 2.
CHE/ME 109 Heat Transfer in Electronics LECTURE 12 – MULTI- DIMENSIONAL NUMERICAL MODELS.
Transient Conduction & Biot Number Calculator By: Matthew Hunter and Jared Oehring.
Solutions of the Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Idea Generates More Mathematics….
Conservation of Energy
CHAPTER 8 APPROXIMATE SOLUTIONS THE INTEGRAL METHOD
CHAP 5 FINITE ELEMENTS FOR HEAT TRANSFER PROBLEMS
Heat Transfer Rates Conduction: Fourier’s Law
UNSTEADY STATE HEAT TRANSFER. This case of heat transfer happens in different situations. It is complicated process occupies an important side in applied.
Heat Transfer: Physical Origins and Rate Equations
Two-Dimensional Conduction: Flux Plots and Shape Factors
Chapter 3: Unsteady State [ Transient ] Heat Conduction
Chapter 4 TRANSIENT HEAT CONDUCTION
Chapter 2 HEAT CONDUCTION EQUATION
CHE/ME 109 Heat Transfer in Electronics LECTURE 9 – GENERAL TRANSIENT CONDUCTION MODELS.
Introduction to Convection: Flow and Thermal Considerations
CHAPTER 7 NON-LINEAR CONDUCTION PROBLEMS
Heat Transfer in Structures
1 CHAPTER 5 POROUS MEDIA Examples of Conduction in Porous Media component electronic micro channels coolant (d) coolant porous material (e) Fig.
Chapter 2 HEAT CONDUCTION EQUATION
Transient Conduction: Spatial Effects and the Role of Analytical Solutions Chapter 5 Sections 5.4 to 5.8.
CHAPTER 5 MESB 374 System Modeling and Analysis Thermal Systems
Two-Dimensional Conduction: Finite-Difference Equations and Solutions
1 CHAPTER 9 PERTURBATION SOLUTIONS 9.1 Introduction Objective Definitions Perturbation quantity Basic Problem To construct an approximate solution to a.
1 CHAPTER 4 TRANSIENT CONDUCTION Neglect spatial variation: Criterion for Neglecting Spatial Temperature Variation Cooling of wire by surface convection:
Transient Conduction: Finite-Difference Equations and Solutions Chapter 5 Section 5.9  
TRANSIENT CONDUCTION Lumped Thermal Capacitance Method Analytical Method: Separation of Variables Semi-Infinite Solid: Similarity Solution Numerical Method:
HEAT CONDUCTION EQUATION
Heat flux through the wall
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.
One Dimensional Non-Homogeneous Conduction Equation P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Another simple Mathematical.
Chapter 2: Heat Conduction Equation
Chapter 3 Part 2 One-Dimensional, Steady-State Conduction.
Finite-Difference Solutions Part 2
External Flow: The Flat Plate in Parallel Flow Chapter 7 Section 7.1 through 7.3.
Chapter Three Sections 3.1 through 3.4
Introduction:- If the temperature of the body does not very with time it said to be in steady state. if there is an abrupt change in its surface temperature.
Chapter 1. Essential Concepts
Chapter 4: Transient Heat Conduction Yoav Peles Department of Mechanical, Aerospace and Nuclear Engineering Rensselaer Polytechnic Institute Copyright.
Thermal Considerations in a Pipe Flow (YAC: 10-1– 10-3; 10-6) Thermal conditions  Laminar or turbulent  Entrance flow and fully developed thermal condition.
Internal Flow: General Considerations. Entrance Conditions Must distinguish between entrance and fully developed regions. Hydrodynamic Effects: Assume.
Extended Surfaces (Fins) Bhagwat Singh Shishodia Associate Professor Manav Rachna International University.
Transient Conduction: The Lumped Capacitance Method
Heat Transfer: Physical Origins and Rate Equations
Lumped Capacitance Calculator
differential equations of heat transfer
Fourier’s Law and the Heat Equation
Fourier’s Law and the Heat Equation
Heat Transfer Transient Conduction.
Extended Surface Heat Transfer
SUBJECT : HEAT & MASS TRANSFER Date : 15/02/2013
Chapter Three Sections 3.1 through 3.4
Chapter Three Section 3.5, Appendix C
Spencer Ferguson and Natalie Siddoway April 7, 2014
Transient Heat Conduction
HEAT TRANSFER Transient Conduction.
Transient Heat Conduction
Internal Flow: General Considerations
Heat Transfer in common Configuration
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.
Presentation transcript:

Transient Conduction: The Lumped Capacitance Method Chapter Five Sections 5.1 thru 5.3

Transient Conduction Transient Conduction A heat transfer process for which the temperature varies with time, as well as location within a solid. It is initiated whenever a system experiences a change in operating conditions and proceeds until a new steady state (thermal equilibrium) is achieved. It can be induced by changes in: surface convection conditions ( ), surface radiation conditions ( ), a surface temperature or heat flux, and/or internal energy generation. Solution Techniques The Lumped Capacitance Method Exact Solutions The Finite-Difference Method

Lumped Capacitance Method The Lumped Capacitance Method Based on the assumption of a spatially uniform temperature distribution throughout the transient process. Hence . Why is the assumption never fully realized in practice? General Lumped Capacitance Analysis: Consider a general case, which includes convection, radiation and/or an applied heat flux at specified surfaces as well as internal energy generation

Lumped Capacitance Method (cont.) First Law: Assuming energy outflow due to convection and radiation and with inflow due to an applied heat flux Is this expression applicable in situations for which convection and/or radiation provide for energy inflow? May h and hr be assumed to be constant throughout the transient process? How must such an equation be solved?

Special Case (Negligible Radiation Special Cases (Exact Solutions, ) Negligible Radiation The non-homogeneous differential equation is transformed into a homogeneous equation of the form: Integrating from t=0 to any t and rearranging, (5.25) To what does the foregoing equation reduce as steady state is approached? How else may the steady-state solution be obtained?

Special Case (Convection) Negligible Radiation and Source Terms (5.2) The thermal time constant is defined as (5.7) Thermal Resistance, Rt Lumped Thermal Capacitance, Ct The change in thermal energy storage due to the transient process is (5.8)

Special Case (Radiation) Negligible Convection and Source Terms Assuming radiation exchange with large surroundings, (5.18) Result necessitates implicit evaluation of T(t).

The Biot Number and Validity of The Lumped Capacitance Method The Biot Number: The first of many dimensionless parameters to be considered. Definition: convection or radiation coefficient Physical Interpretation: Criterion for Applicability of Lumped Capacitance Method:

Problem: Thermal Energy Storage Problem 5.11: Charging a thermal energy storage system consisting of a packed bed of aluminum spheres. Schematic:

Problem: Thermal Energy Storage (cont.)

Problem: Furnace Start-up Problem 5.15: Heating of coated furnace wall during start-up. Schematic:

Problem: Furnace Start-up Hence, with

Problem: Furnace Start-up (cont.)