Modeling with Differential Equations in Chemical Engineering'Modelling with Differential Equations in Chemical Engineering' covers the modelling of rate processes of engineering in terms of differential equations. While it includes the purely mathematical aspects of the solution of differential equations, the main emphasis is on the derivation and solution of major equations of engineering and applied science. Methods of solving differential equations by analytical and numerical means are presented in detail with many solved examples, and problems for solution by the reader. Emphasis is placed on numerical and computer methods of solution. A key chapter in the book is devoted to the principles of mathematical modelling. These principles are applied to the equations in important engineering areas. The major disciplines covered are thermodynamics, diffusion and mass transfer, heat transfer, fluid dynamics, chemical reactions, and automatic control. These topics are of particular value to chemical engineers, but also are of interest to mechanical, civil, and environmental engineers, as well as applied scientists. The material is also suitable for undergraduate and beginning graduate students, as well as for review by practising engineers. |
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Page 22
... shown in Table 2.4 . However , representation of the solutions in terms of a parameter ↑ has the advantage of ready visualization of stability of a dynamic system when t is regarded as time . As will be shown later , second - order ...
... shown in Table 2.4 . However , representation of the solutions in terms of a parameter ↑ has the advantage of ready visualization of stability of a dynamic system when t is regarded as time . As will be shown later , second - order ...
Page 177
... shown by the Runge - Kutta method with 50 intervals . ( b ) The reaction is reversible , 2A B , with rate equation FCo = raV + dna dt The concentration is ra = 2 nb VKe = 2 Ft - na 2K V The corresponding material balance is C = V = na ...
... shown by the Runge - Kutta method with 50 intervals . ( b ) The reaction is reversible , 2A B , with rate equation FCo = raV + dna dt The concentration is ra = 2 nb VKe = 2 Ft - na 2K V The corresponding material balance is C = V = na ...
Page 197
... shown . The temperatures are specified on the four boundaries . Since the grid is sym- metric , balances need be written for only some of the nodes . The balances are written for the necessary nodes in the form Tm , n = 0.25 ( Tm , n ...
... shown . The temperatures are specified on the four boundaries . Since the grid is sym- metric , balances need be written for only some of the nodes . The balances are written for the necessary nodes in the form Tm , n = 0.25 ( Tm , n ...
Common terms and phrases
a₁ a²u applied arctan auxiliary conditions ax² ay² b₁ becomes Bessel equation Bessel functions boundary conditions C₁ C₂ chemical coefficients convergence coordinates curve d²y derivative diffusion diskette dx dy dx/dt dx² dy/dx eigenvalues equa Example Figure finite first-order flow fluid formulas Gaussian elimination heat equation heat transfer homogeneous independent variables initial conditions input integral equation inverse k₁ Laplace equation Laplace transform linear differential equations linear equations mathematical method nodes nonhomogeneous nonlinear numerical ODEs orthogonal parameters Partial Differential Equations phase plane plane polynomials problem reaction reactor region result roots second-order separation of variables sinh solution solved substitution T₁ Table temperature tion u₁ V₁ values vector velocity x₁ x²y y₁ zero ди др ду дх