CONSERVATION LAWS. See Figures 2 and 1.



Similar documents
Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows

An Introduction to Partial Differential Equations

Basic Equations, Boundary Conditions and Dimensionless Parameters

Electromagnetism - Lecture 2. Electric Fields

Differential Balance Equations (DBE)

Mechanics 1: Conservation of Energy and Momentum

- momentum conservation equation ρ = ρf. These are equivalent to four scalar equations with four unknowns: - pressure p - velocity components

Scalars, Vectors and Tensors

Differential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation

Fundamental Theorems of Vector Calculus

LECTURE 2: Stress Conditions at a Fluid-fluid Interface

RAJALAKSHMI ENGINEERING COLLEGE MA 2161 UNIT I - ORDINARY DIFFERENTIAL EQUATIONS PART A

Elasticity Theory Basics

Gauss Formulation of the gravitational forces

4. Introduction to Heat & Mass Transfer

Heat Transfer From A Heated Vertical Plate

Electrostatic Fields: Coulomb s Law & the Electric Field Intensity

Vector surface area Differentials in an OCS

1 The basic equations of fluid dynamics

Lecture L2 - Degrees of Freedom and Constraints, Rectilinear Motion

Chapter 9 Partial Differential Equations

Review of Vector Analysis in Cartesian Coordinates

A Resource for Free-standing Mathematics Qualifications

1 The Diffusion Equation

Physics of the Atmosphere I

Heat Transfer by Free Convection

ATM 316: Dynamic Meteorology I Final Review, December 2014

Heat equation examples

Energy Transport. Focus on heat transfer. Heat Transfer Mechanisms: Conduction Radiation Convection (mass movement of fluids)

Physics 235 Chapter 1. Chapter 1 Matrices, Vectors, and Vector Calculus

Creating a Crust on Bread.

FLUID DYNAMICS. Intrinsic properties of fluids. Fluids behavior under various conditions

CBE 6333, R. Levicky 1 Differential Balance Equations

Chapter 4. Electrostatic Fields in Matter

If Σ is an oriented surface bounded by a curve C, then the orientation of Σ induces an orientation for C, based on the Right-Hand-Rule.

This makes sense. t /t 2 dt = 1. t t 2 + 1dt = 2 du = 1 3 u3/2 u=5

FINAL EXAM SOLUTIONS Math 21a, Spring 03

Sound. References: L.D. Landau & E.M. Lifshitz: Fluid Mechanics, Chapter VIII F. Shu: The Physics of Astrophysics, Vol. 2, Gas Dynamics, Chapter 8

A QUICK GUIDE TO THE FORMULAS OF MULTIVARIABLE CALCULUS

3. Diffusion of an Instantaneous Point Source

arxiv: v2 [physics.acc-ph] 27 Oct 2014

Recall that two vectors in are perpendicular or orthogonal provided that their dot

Introduction to COMSOL. The Navier-Stokes Equations

PHY 301: Mathematical Methods I Curvilinear Coordinate System (10-12 Lectures)

ENERGY TRANSFER SYSTEMS AND THEIR DYNAMIC ANALYSIS

Lecture 17: Conformal Invariance

Module 1 : Conduction. Lecture 5 : 1D conduction example problems. 2D conduction

When the fluid velocity is zero, called the hydrostatic condition, the pressure variation is due only to the weight of the fluid.

A Primer on Index Notation

Parabolic Equations. Chapter 5. Contents Well-Posed Initial-Boundary Value Problem Time Irreversibility of the Heat Equation

Geometric evolution equations with triple junctions. junctions in higher dimensions

Chapter 7: Polarization

The potential (or voltage) will be introduced through the concept of a gradient. The gradient is another sort of 3-dimensional derivative involving

Introduction to the Finite Element Method

The Navier Stokes Equations

Performance Estimation of Water Thermal Energy Storage Tank by Using Simplified Simulation

Steady Heat Conduction

Convection in water (an almost-incompressible fluid)

Vacuum Technology. Kinetic Theory of Gas. Dr. Philip D. Rack

3 Vorticity, Circulation and Potential Vorticity.

3. Reaction Diffusion Equations Consider the following ODE model for population growth

Heating & Cooling in Molecular Clouds

Vanier College Differential Equations Section ESP Project Tumor Modeling

Chapter 28 Fluid Dynamics

Dynamic Process Modeling. Process Dynamics and Control

LECTURE 6: Fluid Sheets

Express Introductory Training in ANSYS Fluent Lecture 1 Introduction to the CFD Methodology

High Speed Aerodynamics Prof. K. P. Sinhamahapatra Department of Aerospace Engineering Indian Institute of Technology, Kharagpur

Part A Electromagnetism

Governing Equations of Fluid Dynamics

F = 0. x ψ = y + z (1) y ψ = x + z (2) z ψ = x + y (3)

HEAT AND MASS TRANSFER

State of Stress at Point

6 J - vector electric current density (A/m2 )

Section 13.5 Equations of Lines and Planes

Solutions for Review Problems

1 Error in Euler s Method

vector calculus 2 Learning outcomes

Statistical Mechanics, Kinetic Theory Ideal Gas. 8.01t Nov 22, 2004

M PROOF OF THE DIVERGENCE THEOREM AND STOKES THEOREM

ON CERTAIN DOUBLY INFINITE SYSTEMS OF CURVES ON A SURFACE

Heat Transfer Prof. Dr. Ale Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati

Exergy: the quality of energy N. Woudstra

Kinetic Theory of Gases. Chapter 33. Kinetic Theory of Gases

a) Use the following equation from the lecture notes: = ( J K 1 mol 1) ( ) 10 L

Heat Transfer and Energy

Class Meeting # 1: Introduction to PDEs

A LAMINAR FLOW ELEMENT WITH A LINEAR PRESSURE DROP VERSUS VOLUMETRIC FLOW ASME Fluids Engineering Division Summer Meeting

Differentiation of vectors

Statistical Physics, Part 2 by E. M. Lifshitz and L. P. Pitaevskii (volume 9 of Landau and Lifshitz, Course of Theoretical Physics).

Numerical Solution of Differential Equations

Scalar Valued Functions of Several Variables; the Gradient Vector

MATH 10550, EXAM 2 SOLUTIONS. x 2 + 2xy y 2 + x = 2

Elastic Wave Propagation

Solutions to Homework 10

Divergence and Curl of the Magnetic Field

Current, Resistance and Electromotive Force. Young and Freedman Chapter 25

A Survival Guide to Vector Calculus

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena.

Chapter 2. Parameterized Curves in R 3

Transcription:

CONSERVATION LAWS 1. Multivariable calculus 1.1. Divergence theorem (of Gauss). This states that the volume integral in of the divergence of the vector-valued function F is equal to the total flux of F through the surface (ˆn is the unit outer normal to the surface): F dv = F ˆn ds. See Figures 2 and 1. Figure 1. Divergence theorem: the total flux of F through the surface is equal to the volume integral in of the divergence of F. Here ˆn is the unit outer normal to the surface. Date: 12th November 2004 (Simon J.A. Malham). 1

2 Figure 2. Flux: for example, for a fluid the amount of material passing through/across the small area patch ds in the surface per unit time, is roughly the density of the material times the volume of the cylinder shown (v ˆn) ds, where v is the local velocity of the fluid.

1.2. Stokes theorem. This states that the integral of the flux of the curl of F through the surface S shown in Figure 3 is equal to the path integral of F round the bounding contour C: ( F ) ˆn ds = F dr. S C 3 Figure 3. Stokes theorem: the integral of the flux of F through the surface S shown is equal to the path integral of F round the bounding contour C shown.

4 1.3. Stokes theorem in the plane. If the vector-valued function F is conservative in some simply connected domain D, i.e. in D there exists a scalar potential function Φ such that F = Φ, then (see Figure 4) F dr = F dr = Φ(B) Φ(A), C 1 C 2 for any two contours C 1 and C 2 lying in D, with starting point A and end point B. In other words, the contour integral of F in such a case is independent of the path chosen and depends only on the endpoints A and B. In particular for a closed contour C lying in D, Stokes theorem in the plane says: F dr = 0. C Recall Cauchy s theorem from complex analysis: if f(z) is analytic in a closed simply connected domain D, then for every simple closed path C in D, f(z)dz = 0. C Figure 4. Stokes theorem in the plane: for any conservative function F (r) in the simply connected domain D, the path integral between any two points A, B D is independent of the path chosen. This is also known as the path independence property for conservative functions.

2. Heat equation 2.1. Physics. Suppose we have a large slab of material that has been heated. We would like to model how the temperature profile within the material will evolve in time. Let be an arbitrary closed subregion of the material slab then we have the following physical definitions: If ρ is the density (mass per unit volume) and H is the heat content per unit mass, then the total heat content in the region is ρh dv. The heat content per unit mass H can be expressed in the form T H = C(τ) dτ, (1) T 0 where C(T ) is the specific heat capacity at temperature T and T 0 is a reference temperature. The flow of heat energy out of the region is q n ds, where q is the flux of heat energy (measures the amount and direction of energy transport per unit time) and n is the unit outer normal to the bounding surface of, denoted by. Also suppose that heat is being generated internally (from some source) within the material. This could be due to a chemical reaction taking place internally or due to an external electric magnetic field acting on the slab that is heating it up internally due to hysteresis effects. If heat is being generated at the rate Q per unit volume (assume we know what Q is) then the total heat generated within is Q dv. 5 2.2. Conservation of energy. Conservation of heat energy implies that d ρh dv = q n ds + Q dv. (2) dt

6 Provided ρ and H are nice smooth functions then for the left hand side we can write d ρh dv = (ρh) dv, dt t while for the surface integral on the right hand side we can use the divergence theorem giving q n ds = q dv. Substituting these last two expressions back into the conservation relation (2) we get ( ) (ρh) + q Q dv = 0. t Now recall that our subregion was chosen completely arbitrarily and so could have been any closed subregion of the material of any size and so we must have that (ρh) + q Q = 0. t 2.3. Simplifying assumptions. If we assume that the density ρ is time independent and also that specific heat capacity C in (1) is constant, then this last equation reduces to ρc T t + q Q = 0. (3) Recall that we assume we know what Q is, but we do not as yet have an appropriate expression for the heat flux q. However Fourier s Law for heat conduction (in a stationary material) says that q = κ T, where κ = κ(t ) is the thermal conductivity which often depends on the temperature T. Basically Fourier s Law says that heat will flow in the direction of the largest negative temperature gradient (i.e. from hot to cold down the steepest temperature gradient). Substituting this expression for q into (3) we get the general nonlinear heat equation ρc T t = (κ(t ) T ) + Q. (4) If κ is constant and Q 0 this reduces to the famous linear heat equation T t = D 2 T, (5) where the constant D = κ is known as the thermal diffusivity. ρc

2.4. Nonlinear heat equation and rescaling. Depending on the material, the thermal conductivity κ(t ) is also often proportional to a power of the temperature T, i.e. κ(t ) = kt n, where k is a constant of proportionality and n the power growth. In such cases the nonlinear heat equation becomes (with Q 0) where K = T t = K (T n T ). (6) k. If we rescale T by setting ρc and substitute this into (6) we get u = K 1/n T, u t = (un u), (7) i.e. we have non-dimensionalized the nonlinear heat equation. 7