The classical description of diffusion, which is based on Fick's Law (the assumption. gradient), is justified only in mixtures in which one component

Size: px
Start display at page:

Download "The classical description of diffusion, which is based on Fick's Law (the assumption. gradient), is justified only in mixtures in which one component"

Transcription

1 Solution of the Maxwell-Stefan Equations Background The classical description of diffusion, which is based on Fick's Law (the assumption of a linear relationship between the flux of a species and its concentration gradient), is justified only in mixtures in which one component (usually referred to as the solvent) is present invery large excess. In this regard it is not well suited to the description of diffusion in multicomponent gaseous mixtures, which can assume the entire range of compositions. More specifically, analyses based on Fick's Law are fundamentally incapable of accounting for apparently unphysical phenomena that have been experimentally observed in multicomponent gaseous diffusion, such as a net flux of a species in the opposite direction to, or even in the absence of, a concentration gradient in that species. [See, for example, J.B. Duncan and H.L. Toor, An experimental study of three component gas diffusion,", AIChE Journal, 8(): 38-4 (96).] In contrast, counterintuitive phenomena such as these can be accounted for by the Maxwell-Stefan (M-S) equations, in which coupling between the fluxes N j of diffusing species is explicitly taken into account. For a gas of constant overall concentration c, the gradient rx i of the mole fraction of each species is related not only to its own flux, but to the fluxes of all the other species, according to rx i = X j6=i cd ij (x i N j x j N i ); where D ij = D ji is the binary diffusivity ofi in j (or j in i), which canin principle be estimated from the kinetic theory of gases. The reciprocal diffusivity that appears on the right-hand side of this equation has the physical significance of a drag coefficient, expressing the average force experienced by the two species as a result of their relative motion. The physical foundations and applications of the M-S equations are described thoroughly in a review by Krishna and Wesselingh [R. Krishna and J.A. Wesselingh, The Maxwell-Stefan approach to mass transfer,"chemical Engineering Science, 5(6): 86 9 (997)].

2 Dimensionless Form For numerical calculations, the equations can be conveniently be rewritten in terms of dimensionless variables. Thus, the length coordinates X; Y; Z can be replaced by thex = X=L; y = Y=L; z = Z=L, where L is a reference length, and the fluxes N i can be replaced with dimensionless fluxes n i defined as n i = L cd 0 N i ; where D 0 is a reference diffusivity, which can be assigned an arbitrary value. One plausible choice would be to set it equal to the smallest of the pairwise diffusivities obtained from the Chapman-Enskog formalism. Alternatively, one could simply set it equal to the diffusivity of the pure Nth component, corresponding to the dependent mole fraction x N = x ::: x N. In these terms, the transport equations rx i = X j6=i cd ij (x i N j x j N i ) in which the gradient is taken with respect to X; Y; Z, become L rx i = X j6=i cd ij cd 0 L (x in j x j n i ) in which the gradient is taken with respect to x; y; z, or rx i = X j6=i D ij (x i n j x j n i ); where D ij = D ij =D 0 is a dimensionless diffusivity. Application of the M-S equations to time-dependent phenomena requires introduction of further equations relating the time dependence of the mole fraction of each species to its rate of transport by diffusion and convection, and its consumption by homogeneous or heterogeneous reactions. In the absence of convection and reaction, accumulation or depletion of a species in an infinitesimal control volume arises from differences in the diffusive flux of that species across opposite faces of the volume. As the dimensions of the control volume are shrunk to zero, the conservation law = r N i:

3 is recovered. For a three-dimensional Cartesian coordinate system (X; Y; Z), the divergence (r ) term that appears on the right-hand side is r N i : When the dimensionless spatial coordinates and dimensionless fluxes are introduced, = L r (cd 0 L n i) and these equations become, after = r n i; where fi D 0 t=l is a dimensionless time. Nonlinearity The advantages of the more rigorous theory of diffusion expressed by the M-S equations are, unfortunately, offset to a large extent by the difficulties in the solution of these equations. The linear parabolic partial differential equation that results from Fick's Law is the subject of a vast literature, and many analytical solutions are available. In contrast, the nonlinear coupling of each concentration gradient to the fluxes of all the species has the practical effect of limiting analytical solutions to steady-state problems in which the fluxes can be independently specified, or most can be set equal to zero. The latter class of problems generally reduce to the solution of a transcendental equation for one or more of the nonvanishing fluxes, and includes several classical problems in chemical engineering, suchastheevaporation of a liquid through a gas film [see, for example, R.B. Bird, W.E. Stewart, and E.N. Lightfoot, Transport Phenomena," New York: Wiley (96), p. 539.] The theoretical analysis of the Duncan-Toor (96) experiments was based on an earlier method developed by Toor [H.L. Toor, Diffusion in three-component gas mixtures,", AIChE Journal, 3(): ((957))], in which the transport equations were reduced to a pair of nonlinear equations for the two independent fluxes, but this approach does not seem to be applicable to more complex cases. This paper contains references to other particular cases in which analytical solutions are possible. 3

4 A highly interesting paper by Baker [Daniel R. Baker, Reducing nonlinear systems of transport equations to Laplace's equation," SIAM Journal of Applied Mathematics, 53(): (993)] demonstrates how the nonlinearity can be removed by expressing the fluxes in terms of a scalar potential, Q viz., n i = ο i rq; where ο i is a constant, and the potential function satisfies Laplace's equation: r Q =0: A direct consequence of this representation is that the divergence of the fluxes vanishes identically: r n i =0: If the constants ο i are chosen so that ο = and ο i = M i =M,whereM i and M are the molar masses of species i and, respectively, the mass-average velocity of the fluid is ρv = M N + :::+ M m N m = 0; this situation is usually referred to as equimolar counterdiffusion. This transformation has the effect of reducing the transport equations to a system of linear differential equations for the mole fractions with independent variable Q, and the condition that all the mole fractions sum to unity yields a nonlinear boundary condition for Q. Nonlinear boundary value problems for Laplace's equation can be solved by using the appropriate Green function to set up a nonlinear integral equation, which can be solved by substitutioniteration. Subsequent literature references to this important work have been concerned with applications to the solution of the Nernst-Planck equations for combined ionic diffusion and migration in electrolyte solutions. No further work has been published on the application of this method to the M-S equations, or to unsteady conditions. Since the conservation law equates the rate of change of the mole fraction to the negative divergence of the species flux, the representation of the species fluxes in terms of a harmonic potential is fundamentally unsuited to analysis of transient diffusion phenomena. Furthermore, the flux and its divergence can be expected to vary with position as well as with time. These two observations suggest that it might be possible to generalize Baker's approach to unsteady problems by dividing the space into elements within which the 4

5 fluxes are again represented as n i = ο i rq, but the potential in the kth such element is instead a solution of the Poisson equation r Q = fl k ; where the constant fl k is not necessarily zero. The time-dependence of the each mole fraction is then expressed = r n i = ο i fl k ; in view of the definition of the constants ο i, these expressions clearly sum to zero, which indicates consistency with the equimolal diffusion assumption as well as the addition of the mole fractions to unity. When this scalar potential representation of the fluxes is substituted into the M-S equations, and the multi-variable chain rule is applied in the form rx i = dx i dq rq; the gradient ofq cancels, resulting in a system of linear differential equations for the vector x of mole fractions as a function of Q: dx X i dq = (x j ο i x i ο j ): D j6=i ij Collecting terms in each mole fraction, this can be written in the form d dq 6 4 x. x m = 6 4 P j6= οj D j ο ο D P j6=. οm Dm οm Dm D οj D j ο D m ο D m.... P j6=m οj Dmj x. x m : For example, for a three-component system, the matrix is A = 6 4 ο cd ο 3 cd 3 ο cd ο 3 cd 3 ο cd ο cd ο 3 cd 3 ο cd 3 ο 3 cd 3 ο 3 cd 3 ο cd ο 3 cd : 5

6 Thus, the system of differential equations for x can be written compactly as dx dq = Ax where the elements of the matrix A are A ij =( ffi ij ) ο j X ο j ffi ij ; cd ij cd ij and ffi ij is the Kronecker delta ( if i = j and 0 otherwise.) Integrating the differential equations for x from one boundary of the region at which the concentrations are fixed at x 0, and Q is zero, the solution is x = x 0 exp[aq]: To complete the solution, this expression is substituted into the boundary conditions to be satisfied by the mole fractions and/or the species fluxes. This typically results in a nonlinear boundary condition for the Laplace equation defining the potential. Some remarks on the practical implementation of this result might be helpful. The right-hand side of this result contains the exponential of a matrix times a scalar argument Q. Although this is to be interpreted as: j6=i exp[aq] =I + QA + Q! A + ::: where I is the identity matrix, this power series representation is never used in practice. Rather, the exponential is represented in the form exp[aq]= k= E k e kq ; where the scalars k are the eigenvalues of A. For symmetric matrices, the m m coefficient matrices E k can be constructed from the dyadic products of the corresponding eigenvectors. For unsymmetric matrices such asa defined above, the E k can be obtained from the first m powers of A, according to the procedure suggested by Harris et al. (00) [William A. Harris, Jr., Jay P. Fillmore, and Donald R. Smith, Matrix exponentials - another approach," SIAM Review, 43(4): (00)], which is based on the Cayley-Hamilton Theorem from linear algebra. 6

7 Construction of the Potential Function As shown by Baker, steady-state solutions of the M-S equations can be expressed in terms of a single solution of Laplace's equation subject to a nonlinear boundary condition, and the above analysis showed that a single solution of the Poisson equation can likewise be used to describe situations in which the flux divergences are constant. For unsteady problems the flux divergence can be expected to vary with position, the indicated solution is to divide the region of interest into elements that are small enough that the flux divergence is approximately constant. Since within each element, the potential is defined by a different function, additional conditions of continuity of the potential function and its derivative must be satisfied at the boundaries of adjacent elements. The piecewise definition of the potential function subject to continuity conditions is closely related to the problem of interpolation by polynomial spline functions. The process of constructing the potential function corresponding to the concentration profile existing at some instant of time is perhaps best illustrated by considering the simplest case of unsteady diffusion in a onedimensional region from z = 0 to z = L. The appropriate analytical form for the potential function within each element follows by integration of the Green function for the one-dimensional Poisson equation times a constant source density. For the equation d Q dz = f(z) over the interval [0,L], at the end points of which homogeneous Dirichlet conditions are satisfied, the Green function satisfies d g = ffi(z ) dz where is the coordinate of the source point, and is given by g(zj ) = 8 < : (L )z 0 L (L z) L Suppose that the source density is given by» z<» z<l f( ) =F; [z ;z ] 7

8 and is zero elsewhere in the interval. Then the potential is Q(z) = Z L 0 g(zj )f( )d ; and the case of interest here is when z [z ;z ]. Then Z z Z z Q = F (L )zd + F (L z) d L z L z = F ρ z[l(z z ) L (z z)] + (L z) (z z )] = Lz z(lz + z z )+ Lz : This shows that the required potential is a quadratic function of the coordinates. For the satisfation of the continuity and flux-matching conditions that apply at the boundaries between the adjoining elements, it proves more convenient to assume a more general form Taking the gradient of this function Q = ff k + fi k (z z k )+ fl k(z z k ) : dq dz = fi k + fl k (z z k ) shows that the fluxes vary linearly with z in each element, and that the flux divergences, which are proportional to d Q dz = fl k are constant. Continuity of the potential at the boundary between elements k and k + is expressed by ff k+ = ff k + fi k (z k+ z k )+ fl k(z k+ z k ) ; and the continuity of the derivative at the same point requires that fi k+ = fi k + fl k (z k+ z k ): 8 ff

9 If the elements are assumed to be of identical width, so that z k+ z k = h, k = ;:::;n, these equations can be solved recursively, as follows. Thus, for k =, the continuity and flux-matching conditions at the boundary are and for k =3, ff = ff + fi h + fl h fi = fi + fl h; ff 3 = ff + fi h + fl h fi 3 = fi + fl h: After performing the indicated substitutions, the latter two relations become ff 3 = ff +fi h +» 3 fl + fl h fi 3 = fi +(fl + fl )h: Proceeding similarly for higher values of k and in general, ff 4 = ff +3fi h + ff 5 = ff +3fi h +» 5 fl + 3 fl + fl 3 h fi 4 = fi +(fl + fl + fl 3 )h;» 7 fl + 5 fl + 3 fl 3 + fl 4 h fi 5 = fi +(fl + fl + fl 3 + fl 4 )h; ff k+ = ff + kfi h + h fi k+ = fi + h kx l= k l + fl k In this way, it is seen that for n such elements, the piecewise-defined potential function requires a total of n + coefficients: ff, fi,andfl fl n. In the special case when all fl = fl n =0,thePoisson equation reduces to Laplace's equation, for which the appropriate solution is a linear function of the single 9 kx l= fl k :

10 space coordinate z. The above result is clearly consistent with this, since in that limit fi k+ = fi for all k and ff k+ = ff + kfi h -thetwo parameters ff, fi are then determined by the values of the potential at each end. Thus, the potential function appropriate for an unsteady problem also includes the steady-state function. The above discussion demonstrates the crucial importance of the parameters fl k, but makes no mention of how these are derived. As discussed in detail in the next section, it is at this point that the nonlinearities enter the analysis. Determination of the Flux Divergences Of the total of n + constants included in the potential function for the one-dimensional diffusion problem presented in the preceding section, ff can in fact be set equal to zero, and fi can be determined to represent the steady state concentration profile. The remaining n parameters fl :::fl n, the values of which define the divergences of the species fluxes and the rate of change of the mole fractions within each element, need to be selected so that the vectors mole fractions at adjacent nodesk, k + are consistent with the analytical solution. This is somewhat less straightforward than other collocation problems, in that there are m components of each vector that must be equated, but only one adjustable parameter, fl k. The best that can be done under such conditions is to apply a least-squares criterion to the quantity i= jx k+ exp[aq(z k+ )]x k j = i= jx k+ exp[aq(z k + h)]x k j ; which should have a minimum value of zero. Now if the matrix exponential is represented in the form exp[aq(z k + h)] = l= E l exp[ l Q(z k + h)]; where the matrices E l are obtained as described by Harris et al. (00), the mole fractions at x k+ are x k+ = " l= E l exp[ l Q(z k + h)] # 0 x k = l= exp[ l Q(z k + h)]e l x k :

11 Since E l is m m and x k is m, each of the l products E l x k is seen to be a column vector with ith component so that x k+;i = (E l x k ) i = l= j= E ij;l x k;j ; exp[ l Q(z k + h)] j= E ij;l x k;j : The requirement that the mole fractions at successive nodesk, k + are consistent is therefore expressed by the system of nonlinear equations 0 3 X 4 xk+;i exp[ l Q(z k + m E ij;l x k;j A5 =0; i= l= which are to be solved for fl :::fl n. The computational overhead associated with the solution of a system of n nonlinear equations at each iteration in fact turns out to be less severe than might first be supposed. This is because once ff and fi have been determined from the steady state concentration profile, the appearance of only fl in the potential for the first element[z ;z ], only fl, fl in the second [z ;z 3 ], etc., allows fl :::fl n to be determined by a forward recursion. Each step in this process can be achieved by means of one-dimensional optimization algorithms, which are known to be inherently more robust than their multivariate counterparts. Time-Stepping Algorithm As mentioned earlier, the parameters fl :::fl n define the rate of change of each mole fraction with respect to time. Although in principle, the j= = r n i = ο i fl k leads directly to the Euler approximation scheme x k;i (fi + ffifi) =x k;i (fi)+ο i fl k ffifi; in practice, this method is very seldom used, since unreasonably small step sizes ffifi are required to achieve results of satisfactory accuracy. But if the

12 entire calculation described above were incorporated into a subroutine that returned fl :::fl n as the values of the time derivatives of a function, the time-stepping algorithm could be performed by a wide variety ofmuch more accurate subroutines for the numerical integration of systems of ordinary differential equations. One possible choice is the fourth-order Runge-Kutta method; since this estimates the variable increments as the average of four function values, each time step would require four `passes' through the recursion for the flux divergences. The computational cost associated with multiple passes is possibly significant for adjustable-order predictor-corrector schemes, which potentially require even more function evaluations for each step. Interestingly, this proposed scheme seems to allow considerably more flexibility than the well-known numerical methods for the integration of the heat equation, in which the temporal and spatial integrations are more intimately linked.

Differential equations of mass transfer

Differential equations of mass transfer Differential equations of mass transfer Definition: The differential equations of mass transfer are general equations describing mass transfer in all directions and at all conditions. How is the differential

More information

V. Electrostatics Lecture 24: Diffuse Charge in Electrolytes

V. Electrostatics Lecture 24: Diffuse Charge in Electrolytes V. Electrostatics Lecture 24: Diffuse Charge in Electrolytes MIT Student 1. Poisson-Nernst-Planck Equations The Nernst-Planck Equation is a conservation of mass equation that describes the influence of

More information

A Numerically Stable Method for Integration of the Multicomponent Species Diffusion Equations

A Numerically Stable Method for Integration of the Multicomponent Species Diffusion Equations Journal of Computational Physics 174, 460 472 (2001) doi:101006/jcph20016930, available online at http://wwwidealibrarycom on A Numerically Stable Method for Integration of the Multicomponent Species Diffusion

More information

An Overly Simplified and Brief Review of Differential Equation Solution Methods. 1. Some Common Exact Solution Methods for Differential Equations

An Overly Simplified and Brief Review of Differential Equation Solution Methods. 1. Some Common Exact Solution Methods for Differential Equations An Overly Simplified and Brief Review of Differential Equation Solution Methods We will be dealing with initial or boundary value problems. A typical initial value problem has the form y y 0 y(0) 1 A typical

More information

Addition of Angular Momenta

Addition of Angular Momenta Addition of Angular Momenta What we have so far considered to be an exact solution for the many electron problem, should really be called exact non-relativistic solution. A relativistic treatment is needed

More information

Mathematical Preliminaries

Mathematical Preliminaries Mathematical Preliminaries Introductory Course on Multiphysics Modelling TOMAZ G. ZIELIŃKI bluebox.ippt.pan.pl/ tzielins/ Table of Contents Vectors, tensors, and index notation. Generalization of the concept

More information

Conjugate Gradient (CG) Method

Conjugate Gradient (CG) Method Conjugate Gradient (CG) Method by K. Ozawa 1 Introduction In the series of this lecture, I will introduce the conjugate gradient method, which solves efficiently large scale sparse linear simultaneous

More information

Time-Dependent Statistical Mechanics 5. The classical atomic fluid, classical mechanics, and classical equilibrium statistical mechanics

Time-Dependent Statistical Mechanics 5. The classical atomic fluid, classical mechanics, and classical equilibrium statistical mechanics Time-Dependent Statistical Mechanics 5. The classical atomic fluid, classical mechanics, and classical equilibrium statistical mechanics c Hans C. Andersen October 1, 2009 While we know that in principle

More information

Part I.

Part I. Part I bblee@unimp . Introduction to Mass Transfer and Diffusion 2. Molecular Diffusion in Gasses 3. Molecular Diffusion in Liquids Part I 4. Molecular Diffusion in Biological Solutions and Gels 5. Molecular

More information

Integration of Ordinary Differential Equations

Integration of Ordinary Differential Equations Integration of Ordinary Differential Equations Com S 477/577 Nov 7, 00 1 Introduction The solution of differential equations is an important problem that arises in a host of areas. Many differential equations

More information

BAE 820 Physical Principles of Environmental Systems

BAE 820 Physical Principles of Environmental Systems BAE 820 Physical Principles of Environmental Systems Estimation of diffusion Coefficient Dr. Zifei Liu Diffusion mass transfer Diffusion mass transfer refers to mass in transit due to a species concentration

More information

HIGH ACCURACY NUMERICAL METHODS FOR THE SOLUTION OF NON-LINEAR BOUNDARY VALUE PROBLEMS

HIGH ACCURACY NUMERICAL METHODS FOR THE SOLUTION OF NON-LINEAR BOUNDARY VALUE PROBLEMS ABSTRACT Of The Thesis Entitled HIGH ACCURACY NUMERICAL METHODS FOR THE SOLUTION OF NON-LINEAR BOUNDARY VALUE PROBLEMS Submitted To The University of Delhi In Partial Fulfillment For The Award of The Degree

More information

Advection, Conservation, Conserved Physical Quantities, Wave Equations

Advection, Conservation, Conserved Physical Quantities, Wave Equations EP711 Supplementary Material Thursday, September 4, 2014 Advection, Conservation, Conserved Physical Quantities, Wave Equations Jonathan B. Snively!Embry-Riddle Aeronautical University Contents EP711 Supplementary

More information

ENGI 4430 PDEs - d Alembert Solutions Page 11.01

ENGI 4430 PDEs - d Alembert Solutions Page 11.01 ENGI 4430 PDEs - d Alembert Solutions Page 11.01 11. Partial Differential Equations Partial differential equations (PDEs) are equations involving functions of more than one variable and their partial derivatives

More information

ENGINEERING MATHEMATICS I. CODE: 10 MAT 11 IA Marks: 25 Hrs/Week: 04 Exam Hrs: 03 PART-A

ENGINEERING MATHEMATICS I. CODE: 10 MAT 11 IA Marks: 25 Hrs/Week: 04 Exam Hrs: 03 PART-A ENGINEERING MATHEMATICS I CODE: 10 MAT 11 IA Marks: 25 Hrs/Week: 04 Exam Hrs: 03 Total Hrs: 52 Exam Marks:100 PART-A Unit-I: DIFFERENTIAL CALCULUS - 1 Determination of n th derivative of standard functions-illustrative

More information

NUMERICAL COMPUTATION IN SCIENCE AND ENGINEERING

NUMERICAL COMPUTATION IN SCIENCE AND ENGINEERING NUMERICAL COMPUTATION IN SCIENCE AND ENGINEERING C. Pozrikidis University of California, San Diego New York Oxford OXFORD UNIVERSITY PRESS 1998 CONTENTS Preface ix Pseudocode Language Commands xi 1 Numerical

More information

INTRODUCTION TO FINITE ELEMENT METHODS ON ELLIPTIC EQUATIONS LONG CHEN

INTRODUCTION TO FINITE ELEMENT METHODS ON ELLIPTIC EQUATIONS LONG CHEN INTROUCTION TO FINITE ELEMENT METHOS ON ELLIPTIC EQUATIONS LONG CHEN CONTENTS 1. Poisson Equation 1 2. Outline of Topics 3 2.1. Finite ifference Method 3 2.2. Finite Element Method 3 2.3. Finite Volume

More information

Multicomponent diffusion in gases and plasma mixtures

Multicomponent diffusion in gases and plasma mixtures High Temperatures ^ High Pressures, 2002, volume 34, pages 109 ^ 116 15 ECTP Proceedings pages 1337 ^ 1344 DOI:10.1068/htwu73 Multicomponent diffusion in gases and plasma mixtures Irina A Sokolova Institute

More information

MATHEMATICAL METHODS INTERPOLATION

MATHEMATICAL METHODS INTERPOLATION MATHEMATICAL METHODS INTERPOLATION I YEAR BTech By Mr Y Prabhaker Reddy Asst Professor of Mathematics Guru Nanak Engineering College Ibrahimpatnam, Hyderabad SYLLABUS OF MATHEMATICAL METHODS (as per JNTU

More information

Mathematics for Engineers and Scientists

Mathematics for Engineers and Scientists Mathematics for Engineers and Scientists Fourth edition ALAN JEFFREY University of Newcastle-upon-Tyne B CHAPMAN & HALL University and Professional Division London New York Tokyo Melbourne Madras Contents

More information

A First Course on Kinetics and Reaction Engineering Unit 33. Axial Dispersion Model

A First Course on Kinetics and Reaction Engineering Unit 33. Axial Dispersion Model Unit 33. Axial Dispersion Model Overview In the plug flow reactor model, concentration only varies in the axial direction, and the sole causes of that variation are convection and reaction. Unit 33 describes

More information

Review of Vector Analysis in Cartesian Coordinates

Review of Vector Analysis in Cartesian Coordinates Review of Vector Analysis in Cartesian Coordinates 1 Scalar: A quantity that has magnitude, but no direction. Examples are mass, temperature, pressure, time, distance, and real numbers. Scalars are usually

More information

Numerical methods for the Navier- Stokes equations

Numerical methods for the Navier- Stokes equations Numerical methods for the Navier- Stokes equations Hans Petter Langtangen 1,2 1 Center for Biomedical Computing, Simula Research Laboratory 2 Department of Informatics, University of Oslo Dec 6, 2012 Note:

More information

Fluid Dynamics and Balance Equations for Reacting Flows

Fluid Dynamics and Balance Equations for Reacting Flows Fluid Dynamics and Balance Equations for Reacting Flows Combustion Summer School 2018 Prof. Dr.-Ing. Heinz Pitsch Balance Equations Basics: equations of continuum mechanics balance equations for mass and

More information

Basic Aspects of Discretization

Basic Aspects of Discretization Basic Aspects of Discretization Solution Methods Singularity Methods Panel method and VLM Simple, very powerful, can be used on PC Nonlinear flow effects were excluded Direct numerical Methods (Field Methods)

More information

FUNDAMENTALS OF CHEMISTRY Vol. II - Irreversible Processes: Phenomenological and Statistical Approach - Carlo Cercignani

FUNDAMENTALS OF CHEMISTRY Vol. II - Irreversible Processes: Phenomenological and Statistical Approach - Carlo Cercignani IRREVERSIBLE PROCESSES: PHENOMENOLOGICAL AND STATISTICAL APPROACH Carlo Dipartimento di Matematica, Politecnico di Milano, Milano, Italy Keywords: Kinetic theory, thermodynamics, Boltzmann equation, Macroscopic

More information

2. FLUID-FLOW EQUATIONS SPRING 2019

2. FLUID-FLOW EQUATIONS SPRING 2019 2. FLUID-FLOW EQUATIONS SPRING 2019 2.1 Introduction 2.2 Conservative differential equations 2.3 Non-conservative differential equations 2.4 Non-dimensionalisation Summary Examples 2.1 Introduction Fluid

More information

Introduction to Mass Transfer

Introduction to Mass Transfer Introduction to Mass Transfer Introduction Three fundamental transfer processes: i) Momentum transfer ii) iii) Heat transfer Mass transfer Mass transfer may occur in a gas mixture, a liquid solution or

More information

Lecture 4: Numerical solution of ordinary differential equations

Lecture 4: Numerical solution of ordinary differential equations Lecture 4: Numerical solution of ordinary differential equations Department of Mathematics, ETH Zürich General explicit one-step method: Consistency; Stability; Convergence. High-order methods: Taylor

More information

Alexander Ostrowski

Alexander Ostrowski Ostrowski p. 1/3 Alexander Ostrowski 1893 1986 Walter Gautschi wxg@cs.purdue.edu Purdue University Ostrowski p. 2/3 Collected Mathematical Papers Volume 1 Determinants Linear Algebra Algebraic Equations

More information

Contents. Part I Vector Analysis

Contents. Part I Vector Analysis Contents Part I Vector Analysis 1 Vectors... 3 1.1 BoundandFreeVectors... 4 1.2 Vector Operations....................................... 4 1.2.1 Multiplication by a Scalar.......................... 5 1.2.2

More information

Steady-State Molecular Diffusion

Steady-State Molecular Diffusion Steady-State Molecular Diffusion This part is an application to the general differential equation of mass transfer. The objective is to solve the differential equation of mass transfer under steady state

More information

Some Notes on Linear Algebra

Some Notes on Linear Algebra Some Notes on Linear Algebra prepared for a first course in differential equations Thomas L Scofield Department of Mathematics and Statistics Calvin College 1998 1 The purpose of these notes is to present

More information

14 Divergence, flux, Laplacian

14 Divergence, flux, Laplacian Tel Aviv University, 204/5 Analysis-III,IV 240 4 Divergence, flux, Laplacian 4a What is the problem................ 240 4b Integral of derivative (again)........... 242 4c Divergence and flux.................

More information

MATHEMATICS 217 NOTES

MATHEMATICS 217 NOTES MATHEMATICS 27 NOTES PART I THE JORDAN CANONICAL FORM The characteristic polynomial of an n n matrix A is the polynomial χ A (λ) = det(λi A), a monic polynomial of degree n; a monic polynomial in the variable

More information

NUMERICAL METHODS FOR ENGINEERING APPLICATION

NUMERICAL METHODS FOR ENGINEERING APPLICATION NUMERICAL METHODS FOR ENGINEERING APPLICATION Second Edition JOEL H. FERZIGER A Wiley-Interscience Publication JOHN WILEY & SONS, INC. New York / Chichester / Weinheim / Brisbane / Singapore / Toronto

More information

Foundations of Matrix Analysis

Foundations of Matrix Analysis 1 Foundations of Matrix Analysis In this chapter we recall the basic elements of linear algebra which will be employed in the remainder of the text For most of the proofs as well as for the details, the

More information

BEM for compressible fluid dynamics

BEM for compressible fluid dynamics BEM for compressible fluid dynamics L. gkerget & N. Samec Faculty of Mechanical Engineering, Institute of Power, Process and Environmental Engineering, University of Maribor, Slovenia Abstract The fully

More information

GAME PHYSICS SECOND EDITION. дяййтаййг 1 *

GAME PHYSICS SECOND EDITION. дяййтаййг 1 * GAME PHYSICS SECOND EDITION DAVID H. EBERLY дяййтаййг 1 * К AMSTERDAM BOSTON HEIDELBERG LONDON NEW YORK OXFORD PARIS SAN DIEGO SAN FRANCISCO SINGAPORE SYDNEY TOKYO MORGAN ELSEVIER Morgan Kaufmann Publishers

More information

1 Introduction. 2 Elements and Shape Functions in 1D

1 Introduction. 2 Elements and Shape Functions in 1D Introduction Introduction to the Finite Element Method James R Nagel Department of Electrical and Computer Engineering University of Utah, Salt Lake City, Utah April 4, 0 The finite element method (FEM)

More information

MASS TRANSPORT Macroscopic Balances for Multicomponent Systems

MASS TRANSPORT Macroscopic Balances for Multicomponent Systems TRANSPORT PHENOMENA MASS TRANSPORT Macroscopic Balances for Multicomponent Systems Macroscopic Balances for Multicomponent Systems 1. The Macroscopic Mass Balance 2. The Macroscopic Momentum and Angular

More information

Problem 1: Toolbox (25 pts) For all of the parts of this problem, you are limited to the following sets of tools:

Problem 1: Toolbox (25 pts) For all of the parts of this problem, you are limited to the following sets of tools: CS 322 Final Exam Friday 18 May 2007 150 minutes Problem 1: Toolbox (25 pts) For all of the parts of this problem, you are limited to the following sets of tools: (A) Runge-Kutta 4/5 Method (B) Condition

More information

KINGS COLLEGE OF ENGINEERING DEPARTMENT OF MATHEMATICS ACADEMIC YEAR / EVEN SEMESTER QUESTION BANK

KINGS COLLEGE OF ENGINEERING DEPARTMENT OF MATHEMATICS ACADEMIC YEAR / EVEN SEMESTER QUESTION BANK KINGS COLLEGE OF ENGINEERING MA5-NUMERICAL METHODS DEPARTMENT OF MATHEMATICS ACADEMIC YEAR 00-0 / EVEN SEMESTER QUESTION BANK SUBJECT NAME: NUMERICAL METHODS YEAR/SEM: II / IV UNIT - I SOLUTION OF EQUATIONS

More information

Nernst Equilibrium Potential. p. 1

Nernst Equilibrium Potential. p. 1 Nernst Equilibrium Potential p. 1 Diffusion The conservation law for a compound with concentration c: rate change of c = local production + accumulation due to transport. Model: d c dv = p dv J n da dt

More information

Navier-Stokes Equation: Principle of Conservation of Momentum

Navier-Stokes Equation: Principle of Conservation of Momentum Navier-tokes Equation: Principle of Conservation of Momentum R. hankar ubramanian Department of Chemical and Biomolecular Engineering Clarkson University Newton formulated the principle of conservation

More information

Module 2 : Convection. Lecture 12 : Derivation of conservation of energy

Module 2 : Convection. Lecture 12 : Derivation of conservation of energy Module 2 : Convection Lecture 12 : Derivation of conservation of energy Objectives In this class: Start the derivation of conservation of energy. Utilize earlier derived mass and momentum equations for

More information

CHAPTER 3 Further properties of splines and B-splines

CHAPTER 3 Further properties of splines and B-splines CHAPTER 3 Further properties of splines and B-splines In Chapter 2 we established some of the most elementary properties of B-splines. In this chapter our focus is on the question What kind of functions

More information

7 The Navier-Stokes Equations

7 The Navier-Stokes Equations 18.354/12.27 Spring 214 7 The Navier-Stokes Equations In the previous section, we have seen how one can deduce the general structure of hydrodynamic equations from purely macroscopic considerations and

More information

Lecture V: The game-engine loop & Time Integration

Lecture V: The game-engine loop & Time Integration Lecture V: The game-engine loop & Time Integration The Basic Game-Engine Loop Previous state: " #, %(#) ( #, )(#) Forces -(#) Integrate velocities and positions Resolve Interpenetrations Per-body change

More information

APPENDIX A. Background Mathematics. A.1 Linear Algebra. Vector algebra. Let x denote the n-dimensional column vector with components x 1 x 2.

APPENDIX A. Background Mathematics. A.1 Linear Algebra. Vector algebra. Let x denote the n-dimensional column vector with components x 1 x 2. APPENDIX A Background Mathematics A. Linear Algebra A.. Vector algebra Let x denote the n-dimensional column vector with components 0 x x 2 B C @. A x n Definition 6 (scalar product). The scalar product

More information

x x2 2 + x3 3 x4 3. Use the divided-difference method to find a polynomial of least degree that fits the values shown: (b)

x x2 2 + x3 3 x4 3. Use the divided-difference method to find a polynomial of least degree that fits the values shown: (b) Numerical Methods - PROBLEMS. The Taylor series, about the origin, for log( + x) is x x2 2 + x3 3 x4 4 + Find an upper bound on the magnitude of the truncation error on the interval x.5 when log( + x)

More information

PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS

PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS PRINCIPLES AND MODERN APPLICATIONS OF MASS TRANSFER OPERATIONS Jaime Benitez iwiley- INTERSCIENCE A JOHN WILEY & SONS, INC., PUBLICATION Preface Nomenclature xiii xv 1. FUNDAMENTALS OF MASS TRANSFER 1

More information

Classical Mechanics in Hamiltonian Form

Classical Mechanics in Hamiltonian Form Classical Mechanics in Hamiltonian Form We consider a point particle of mass m, position x moving in a potential V (x). It moves according to Newton s law, mẍ + V (x) = 0 (1) This is the usual and simplest

More information

Linear Algebra. The analysis of many models in the social sciences reduces to the study of systems of equations.

Linear Algebra. The analysis of many models in the social sciences reduces to the study of systems of equations. POLI 7 - Mathematical and Statistical Foundations Prof S Saiegh Fall Lecture Notes - Class 4 October 4, Linear Algebra The analysis of many models in the social sciences reduces to the study of systems

More information

Differential Equations 2280 Sample Midterm Exam 3 with Solutions Exam Date: 24 April 2015 at 12:50pm

Differential Equations 2280 Sample Midterm Exam 3 with Solutions Exam Date: 24 April 2015 at 12:50pm Differential Equations 228 Sample Midterm Exam 3 with Solutions Exam Date: 24 April 25 at 2:5pm Instructions: This in-class exam is 5 minutes. No calculators, notes, tables or books. No answer check is

More information

Modeling using conservation laws. Let u(x, t) = density (heat, momentum, probability,...) so that. u dx = amount in region R Ω. R

Modeling using conservation laws. Let u(x, t) = density (heat, momentum, probability,...) so that. u dx = amount in region R Ω. R Modeling using conservation laws Let u(x, t) = density (heat, momentum, probability,...) so that u dx = amount in region R Ω. R Modeling using conservation laws Let u(x, t) = density (heat, momentum, probability,...)

More information

1 Linear transformations; the basics

1 Linear transformations; the basics Linear Algebra Fall 2013 Linear Transformations 1 Linear transformations; the basics Definition 1 Let V, W be vector spaces over the same field F. A linear transformation (also known as linear map, or

More information

Cartesian Tensors. e 2. e 1. General vector (formal definition to follow) denoted by components

Cartesian Tensors. e 2. e 1. General vector (formal definition to follow) denoted by components Cartesian Tensors Reference: Jeffreys Cartesian Tensors 1 Coordinates and Vectors z x 3 e 3 y x 2 e 2 e 1 x x 1 Coordinates x i, i 123,, Unit vectors: e i, i 123,, General vector (formal definition to

More information

Notes on Entropy Production in Multicomponent Fluids

Notes on Entropy Production in Multicomponent Fluids Notes on Entropy Production in Multicomponent Fluids Robert F. Sekerka Updated January 2, 2001 from July 1993 Version Introduction We calculate the entropy production in a multicomponent fluid, allowing

More information

DS-GA 1002 Lecture notes 0 Fall Linear Algebra. These notes provide a review of basic concepts in linear algebra.

DS-GA 1002 Lecture notes 0 Fall Linear Algebra. These notes provide a review of basic concepts in linear algebra. DS-GA 1002 Lecture notes 0 Fall 2016 Linear Algebra These notes provide a review of basic concepts in linear algebra. 1 Vector spaces You are no doubt familiar with vectors in R 2 or R 3, i.e. [ ] 1.1

More information

Lecture 2 Constitutive Relations

Lecture 2 Constitutive Relations Lecture 2 Constitutive Relations Conservation equations Dv = @ + r v =0 @t rp + r + g DY i + r ( Y iv i )= i i =1, 2,...,N { De = pr v + r q Dh + r q Z Y i p = R h = Y i h o i + c p d o W i We already

More information

Numerical Methods for Engineers and Scientists

Numerical Methods for Engineers and Scientists Numerical Methods for Engineers and Scientists Second Edition Revised and Expanded Joe D. Hoffman Department of Mechanical Engineering Purdue University West Lafayette, Indiana m MARCEL D E К К E R MARCEL

More information

Electromagnetic Waves For fast-varying phenomena, the displacement current cannot be neglected, and the full set of Maxwell s equations must be used

Electromagnetic Waves For fast-varying phenomena, the displacement current cannot be neglected, and the full set of Maxwell s equations must be used Electromagnetic Waves For fast-varying phenomena, the displacement current cannot be neglected, and the full set of Maxwell s equations must be used B( t) E = dt D t H = J+ t D =ρ B = 0 D=εE B=µ H () F

More information

Outline. Definition and mechanism Theory of diffusion Molecular diffusion in gases Molecular diffusion in liquid Mass transfer

Outline. Definition and mechanism Theory of diffusion Molecular diffusion in gases Molecular diffusion in liquid Mass transfer Diffusion 051333 Unit operation in gro-industry III Department of Biotechnology, Faculty of gro-industry Kasetsart University Lecturer: Kittipong Rattanaporn 1 Outline Definition and mechanism Theory of

More information

PDE Solvers for Fluid Flow

PDE Solvers for Fluid Flow PDE Solvers for Fluid Flow issues and algorithms for the Streaming Supercomputer Eran Guendelman February 5, 2002 Topics Equations for incompressible fluid flow 3 model PDEs: Hyperbolic, Elliptic, Parabolic

More information

2. The Schrödinger equation for one-particle problems. 5. Atoms and the periodic table of chemical elements

2. The Schrödinger equation for one-particle problems. 5. Atoms and the periodic table of chemical elements 1 Historical introduction The Schrödinger equation for one-particle problems 3 Mathematical tools for quantum chemistry 4 The postulates of quantum mechanics 5 Atoms and the periodic table of chemical

More information

CHAPTER 7 SEVERAL FORMS OF THE EQUATIONS OF MOTION

CHAPTER 7 SEVERAL FORMS OF THE EQUATIONS OF MOTION CHAPTER 7 SEVERAL FORMS OF THE EQUATIONS OF MOTION 7.1 THE NAVIER-STOKES EQUATIONS Under the assumption of a Newtonian stress-rate-of-strain constitutive equation and a linear, thermally conductive medium,

More information

Index. C 2 ( ), 447 C k [a,b], 37 C0 ( ), 618 ( ), 447 CD 2 CN 2

Index. C 2 ( ), 447 C k [a,b], 37 C0 ( ), 618 ( ), 447 CD 2 CN 2 Index advection equation, 29 in three dimensions, 446 advection-diffusion equation, 31 aluminum, 200 angle between two vectors, 58 area integral, 439 automatic step control, 119 back substitution, 604

More information

ACM/CMS 107 Linear Analysis & Applications Fall 2016 Assignment 4: Linear ODEs and Control Theory Due: 5th December 2016

ACM/CMS 107 Linear Analysis & Applications Fall 2016 Assignment 4: Linear ODEs and Control Theory Due: 5th December 2016 ACM/CMS 17 Linear Analysis & Applications Fall 216 Assignment 4: Linear ODEs and Control Theory Due: 5th December 216 Introduction Systems of ordinary differential equations (ODEs) can be used to describe

More information

Numerical Methods for Partial Differential Equations: an Overview.

Numerical Methods for Partial Differential Equations: an Overview. Numerical Methods for Partial Differential Equations: an Overview math652_spring2009@colorstate PDEs are mathematical models of physical phenomena Heat conduction Wave motion PDEs are mathematical models

More information

Mathematical Notes for E&M Gradient, Divergence, and Curl

Mathematical Notes for E&M Gradient, Divergence, and Curl Mathematical Notes for E&M Gradient, Divergence, and Curl In these notes I explain the differential operators gradient, divergence, and curl (also known as rotor), the relations between them, the integral

More information

Combustion MATHEMATICAL MODEL FOR TRANSIENT. S. M. Frolov Λ,F.S.Frolov Λ, and B. Basara y

Combustion MATHEMATICAL MODEL FOR TRANSIENT. S. M. Frolov Λ,F.S.Frolov Λ, and B. Basara y Combustion MATHEMATICAL MODEL FOR TRANSIENT DROPLET VAPORIZATION S. M. Frolov Λ,F.S.Frolov Λ, and B. Basara y Λ N. N. Semenov Institute of Chemical Physics Russian Academy of Sciences Moscow, Russia y

More information

Introduction to Techniques for Counting

Introduction to Techniques for Counting Introduction to Techniques for Counting A generating function is a device somewhat similar to a bag. Instead of carrying many little objects detachedly, which could be embarrassing, we put them all in

More information

PARTIAL DIFFERENTIAL EQUATIONS

PARTIAL DIFFERENTIAL EQUATIONS MATHEMATICAL METHODS PARTIAL DIFFERENTIAL EQUATIONS I YEAR B.Tech By Mr. Y. Prabhaker Reddy Asst. Professor of Mathematics Guru Nanak Engineering College Ibrahimpatnam, Hyderabad. SYLLABUS OF MATHEMATICAL

More information

ENGI 9420 Lecture Notes 8 - PDEs Page 8.01

ENGI 9420 Lecture Notes 8 - PDEs Page 8.01 ENGI 940 ecture Notes 8 - PDEs Page 8.0 8. Partial Differential Equations Partial differential equations (PDEs) are equations involving functions of more than one variable and their partial derivatives

More information

Numerical Solutions to Partial Differential Equations

Numerical Solutions to Partial Differential Equations Numerical Solutions to Partial Differential Equations Zhiping Li LMAM and School of Mathematical Sciences Peking University Numerical Methods for Partial Differential Equations Finite Difference Methods

More information

Advanced. Engineering Mathematics

Advanced. Engineering Mathematics Advanced Engineering Mathematics A new edition of Further Engineering Mathematics K. A. Stroud Formerly Principal Lecturer Department of Mathematics, Coventry University with additions by Dexter j. Booth

More information

Final Exam May 4, 2016

Final Exam May 4, 2016 1 Math 425 / AMCS 525 Dr. DeTurck Final Exam May 4, 2016 You may use your book and notes on this exam. Show your work in the exam book. Work only the problems that correspond to the section that you prepared.

More information

SIMPLIFICATION OF LAMINAR BOUNDARY LAYER EQUATIONS. Karlo T. Raić. University of Belgrade, Faculty of Technology and Metallurgy

SIMPLIFICATION OF LAMINAR BOUNDARY LAYER EQUATIONS. Karlo T. Raić. University of Belgrade, Faculty of Technology and Metallurgy Metallurgical and Materials Engineering Association of Metallurgical Engineers of Serbia AMES Scientific paper https://doi.org/10.30544/347 SIMPLIFICATION OF LAMINAR BOUNDARY LAYER EQUATIONS Karlo T. Raić

More information

ENGI 9420 Lecture Notes 8 - PDEs Page 8.01

ENGI 9420 Lecture Notes 8 - PDEs Page 8.01 ENGI 940 Lecture Notes 8 - PDEs Page 8.01 8. Partial Differential Equations Partial differential equations (PDEs) are equations involving functions of more than one variable and their partial derivatives

More information

Introduction to Partial Differential Equations

Introduction to Partial Differential Equations Introduction to Partial Differential Equations Partial differential equations arise in a number of physical problems, such as fluid flow, heat transfer, solid mechanics and biological processes. These

More information

Diffusion and Adsorption in porous media. Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad

Diffusion and Adsorption in porous media. Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad Diffusion and Adsorption in porous media Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad Contents Introduction Devices used to Measure Diffusion in Porous Solids Modes of transport in

More information

Chapter 2 Mass Transfer Coefficient

Chapter 2 Mass Transfer Coefficient Chapter 2 Mass Transfer Coefficient 2.1 Introduction The analysis reported in the previous chapter allows to describe the concentration profile and the mass fluxes of components in a mixture by solving

More information

Introduction to Heat and Mass Transfer. Week 9

Introduction to Heat and Mass Transfer. Week 9 Introduction to Heat and Mass Transfer Week 9 補充! Multidimensional Effects Transient problems with heat transfer in two or three dimensions can be considered using the solutions obtained for one dimensional

More information

Classical Field Theory: Electrostatics-Magnetostatics

Classical Field Theory: Electrostatics-Magnetostatics Classical Field Theory: Electrostatics-Magnetostatics April 27, 2010 1 1 J.D.Jackson, Classical Electrodynamics, 2nd Edition, Section 1-5 Electrostatics The behavior of an electrostatic field can be described

More information

PH.D. PRELIMINARY EXAMINATION MATHEMATICS

PH.D. PRELIMINARY EXAMINATION MATHEMATICS UNIVERSITY OF CALIFORNIA, BERKELEY Dept. of Civil and Environmental Engineering FALL SEMESTER 2014 Structural Engineering, Mechanics and Materials NAME PH.D. PRELIMINARY EXAMINATION MATHEMATICS Problem

More information

Duality, Dual Variational Principles

Duality, Dual Variational Principles Duality, Dual Variational Principles April 5, 2013 Contents 1 Duality 1 1.1 Legendre and Young-Fenchel transforms.............. 1 1.2 Second conjugate and convexification................ 4 1.3 Hamiltonian

More information

Verification of the Maxwell Stefan theory for diffusion of three-component mixtures in zeolites

Verification of the Maxwell Stefan theory for diffusion of three-component mixtures in zeolites Chemical Engineering Journal 87 (2002) 1 9 Verification of the Maxwell Stefan theory for diffusion of three-component mixtures in zeolites R. Krishna, D. Paschek Department of Chemical Engineering, University

More information

Systems of Second Order Differential Equations Cayley-Hamilton-Ziebur

Systems of Second Order Differential Equations Cayley-Hamilton-Ziebur Systems of Second Order Differential Equations Cayley-Hamilton-Ziebur Characteristic Equation Cayley-Hamilton Cayley-Hamilton Theorem An Example Euler s Substitution for u = A u The Cayley-Hamilton-Ziebur

More information

Control, Stabilization and Numerics for Partial Differential Equations

Control, Stabilization and Numerics for Partial Differential Equations Paris-Sud, Orsay, December 06 Control, Stabilization and Numerics for Partial Differential Equations Enrique Zuazua Universidad Autónoma 28049 Madrid, Spain enrique.zuazua@uam.es http://www.uam.es/enrique.zuazua

More information

Solution of a System of ODEs with POLYMATH and MATLAB, Boundary Value Iterations with MATLAB

Solution of a System of ODEs with POLYMATH and MATLAB, Boundary Value Iterations with MATLAB dy Solution of a System of ODEs with POLYMATH and MATLAB, Boundary Value Iterations with MATLAB For a system of n simultaneous first-order ODEs: dy1 = f1( y1, y2, K yn, x) dx dy2 = f 2( y1, y2, K yn, x)

More information

CHEMICAL ENGINEERING

CHEMICAL ENGINEERING CHEMICAL ENGINEERING Subject Code: CH Course Structure Sections/Units Section A Unit 1 Unit 2 Unit 3 Unit 4 Unit 5 Unit 6 Section B Section C Section D Section E Section F Section G Section H Section I

More information

Development of Dynamic Models. Chapter 2. Illustrative Example: A Blending Process

Development of Dynamic Models. Chapter 2. Illustrative Example: A Blending Process Development of Dynamic Models Illustrative Example: A Blending Process An unsteady-state mass balance for the blending system: rate of accumulation rate of rate of = of mass in the tank mass in mass out

More information

Computational Fluid Dynamics Prof. Dr. Suman Chakraborty Department of Mechanical Engineering Indian Institute of Technology, Kharagpur

Computational Fluid Dynamics Prof. Dr. Suman Chakraborty Department of Mechanical Engineering Indian Institute of Technology, Kharagpur Computational Fluid Dynamics Prof. Dr. Suman Chakraborty Department of Mechanical Engineering Indian Institute of Technology, Kharagpur Lecture No. #12 Fundamentals of Discretization: Finite Volume Method

More information

Exact and Approximate Numbers:

Exact and Approximate Numbers: Eact and Approimate Numbers: The numbers that arise in technical applications are better described as eact numbers because there is not the sort of uncertainty in their values that was described above.

More information

Applied Numerical Analysis

Applied Numerical Analysis Applied Numerical Analysis Using MATLAB Second Edition Laurene V. Fausett Texas A&M University-Commerce PEARSON Prentice Hall Upper Saddle River, NJ 07458 Contents Preface xi 1 Foundations 1 1.1 Introductory

More information

Chapter 4 Copolymerization

Chapter 4 Copolymerization Chapter 4 Copolymerization 4.1 Kinetics of Copolymerization 4.1.1 Involved Chemical Reactions Initiation I 2 + M 2R 1 r = 2 fk d I 2 R I Propagation Chain Transfer Termination m,n + k p m+1,n m,n + B k

More information

Math 1060 Linear Algebra Homework Exercises 1 1. Find the complete solutions (if any!) to each of the following systems of simultaneous equations:

Math 1060 Linear Algebra Homework Exercises 1 1. Find the complete solutions (if any!) to each of the following systems of simultaneous equations: Homework Exercises 1 1 Find the complete solutions (if any!) to each of the following systems of simultaneous equations: (i) x 4y + 3z = 2 3x 11y + 13z = 3 2x 9y + 2z = 7 x 2y + 6z = 2 (ii) x 4y + 3z =

More information

Development of Dynamic Models. Chapter 2. Illustrative Example: A Blending Process

Development of Dynamic Models. Chapter 2. Illustrative Example: A Blending Process Development of Dynamic Models Illustrative Example: A Blending Process An unsteady-state mass balance for the blending system: rate of accumulation rate of rate of = of mass in the tank mass in mass out

More information

Econ Slides from Lecture 7

Econ Slides from Lecture 7 Econ 205 Sobel Econ 205 - Slides from Lecture 7 Joel Sobel August 31, 2010 Linear Algebra: Main Theory A linear combination of a collection of vectors {x 1,..., x k } is a vector of the form k λ ix i for

More information