Applied Mathematics and Modeling for Chemical Engineers - download pdf or read online

By Richard G. Rice

ISBN-10: 0471303771

ISBN-13: 9780471303770

Bridges the distance among classical research and smooth functions. Following the bankruptcy at the version construction level, it introduces conventional concepts for fixing usual differential equations, including new fabric on approximate resolution tools corresponding to perturbation innovations and ordinary numerical suggestions. additionally comprises analytical the way to care for very important sessions of finite-difference equations. The final part discusses numerical answer ideas and partial differential equations.

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Sample text

80« implies symmetry at the center of the rod, whereas at the curved outer surface of the rod the usual Newton cooling condition is applicable (Eq. 80ft). 8Od states that there is no heat flow across theflatend of the rod. This is tantamount to saying that either the flat end is insulated or the flat end area is so small compared to the curved surface of the rod that heat loss there is negligible. Solutions for various boundary conditions can be found in Carslaw and Jaeger (1959). When dealing with simple equations (as in the previous three models), the dimensional equations are solved without recourse to the process of nondimensionalisation.

Let T0 and T1 be the atmosphere and solvent temperatures, respectively. 52) where T is the temperature of the rod, and L 1 and L2 are lengths of rod exposed to solvent and to atmosphere, respectively. Obviously, the volume elements are finite (not differential), being composed of the volume above the liquid of length L 2 and the volume below of length L 1 . Solving for T from Eq. 53 gives us a very quick estimate of the rod temperature and how it varies with exposure length. , long L 1 section and high liquid heat transfer coefficient compared to gas coefficient), the rod temperature is then very near T1.

A) Derive the steady-state oxygen mole balance for an incremental volume of AAx (A being the column cross-sectional area) and show that the liquid phase balance is (1 - B)De^ - uOL§- + kca(C* - C) = 0 (b) Lump parameters by defining a new dimensionless length as z= kcax "^T and define the excess concentration as y = (C - C*), and so obtain the elementary, second order, ordinary differential equation d2y dy where ^—e a = c (dimensionless) Note, the usual conditions in practice are such that a < 1.

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Applied Mathematics and Modeling for Chemical Engineers by Richard G. Rice

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