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Analytical and Numerical Methods

2 Analytical and Numerical Methods. - Modeling deactivation at the particle and reactor levels involves solution of boundary value problems that result [Pg.242]

They used this model to predict the effective diffusivity in the partially impervious deposit (zone 4). They developed and solved the coupled mass balance equations for spherical pellets in a fixed bed reactor. To compare the model with experimental data, they measured the conversion of propane and propylene over partially poisoned pellets in a small isothermal packed bed reactor. For intrinsic kinetic rates of propane and propylene they employed the empirical rate equations proposed by Volts et al. and Hiam et al. The Hegedus model is briefly described below  [Pg.243]

The mass balance of reactive species in the catalyst pellet is described by  [Pg.243]

The integral fixed bed reactor is simulated by a cascade of cells. Each cell contains N catalyst pellets. Usually Vceu is selected such that its dimension in the flow direction is comparable to the diameter of catalyst pellet. N is calculated as following  [Pg.244]

They solved these equations using a finite element method (Ritz-Galerkin [Pg.244]


Linz, P. Analytical and Numerical Methods for Volterra Equations, SIAM Publications, Philadelphia (1985). [Pg.423]

References Courant, R., and D. Hilbert, Methods of Mathematical Physics, vol. I, Interscience, New York (1953) Linz, P., Analytical and Numerical Methods for Volterra Equations, SIAM Publications, Philadelphia (1985) Porter, D., and D. S. G. Stirling, Integral Equations A Practical Treatment from Spectral Theory to Applications, Cambridge University Press (1990) Statgold, I., Greens Functions and Boundary Value Problems, 2d ed., Interscience, New York (1997). [Pg.36]

Solutions for Volterra equations are done in a similar fashion, except that the solution can proceed point by point, or in small groups of points depending on the quadrature scheme. See Linz, P., Analytical and Numerical Methods for Volterra Equations, SIAM, Philadelphia (1985). There are methods that are analogous to the usual methods for... [Pg.54]

The uniform density limit has been well-studied by a combination of analytic and numerical methods. This section will review some (but not all) of what is known about it. [Pg.16]

In general it is desirable to solve the non-linear models by an approximate analysis to give analytical solutions that can be used for checking the numerical procedures and for evaluating the numerical results. A role of ADM is to take a place just in between the roles of analytical and numerical methods. [Pg.287]

Analytical and numerical methods are described in more detail below. [Pg.53]

A large part of the present book will be concerned with a discussion of some of the analytical and numerical methods that can be used to try to predict h for various flow situations. Basically, these methods involve the simultaneous application of the principles governing viscous fluid flow, i.e., the principles of conservation of mass and momentum and the principle of conservation of energy. Although considerable success has been achieved with these methods, there still remain many cases in which experimental results have to be used to arrive at working relations for the prediction of h. [Pg.6]

The basic aim of the book is to present a discussion of some currently available methods for predicting convective heat transfer rates. The main emphasis is, therefore, on the prediction of heat transfer rates rather than on the presentation of large amounts of experimental data. Attention is given to both analytical and numerical methods of analysis. Another aim of the book is to present a thorough discussion of the foundations of the subject in a clear, easy to follow, student-oriented style. [Pg.630]

A combined analytical and numerical method is employed to optimize process conditions for composites fiber coating by chemical vapor infiltration (CVI). For a first-order deposition reaction, the optimum pressure yielding the maximum deposition rate at a preform center is obtained in closed form and is found to depend only on the activation energy of the deposition reaction, the characteristic pore size, and properties of the reactant and product gases. It does not depend on the preform specific surface area, effective diffusivity or preform thickness, nor on the gas-phase yield of the deposition reaction. Further, this optimum pressure is unaltered by the additional constraint of prescribed deposition uniformity. Optimum temperatures are obtained using an analytical expression for the optimum value along with numerical... [Pg.183]

F. A. Williams, A Review of Some Theoretical Considerations of Turbulent Flame Structure, in AGARD Conference Proceedings No. 164, Analytical and Numerical Methods for Investigation of Flow Fields with Chemical Reactions, Especially Related to Combustion, M. Barrere, ed., AGARD, NATO, Paris (1975), II 11 to II 1-25. [Pg.180]

In the second chapter we consider steady-state and transient heat conduction and mass diffusion in quiescent media. The fundamental differential equations for the calculation of temperature fields are derived here. We show how analytical and numerical methods are used in the solution of practical cases. Alongside the Laplace transformation and the classical method of separating the variables, we have also presented an extensive discussion of finite difference methods which are very important in practice. Many of the results found for heat conduction can be transferred to the analogous process of mass diffusion. The mathematical solution formulations are the same for both fields. [Pg.693]

The combination of analytical and numerical methods ensured the reliability of the algorithm, the results obtained, and the conclusions drawn. This is not possible in the case of a quadratic EPR (1.7), (1.8). First of all, condition (3.46), (3.47) was crucial for... [Pg.111]

Both analytical and numerical methods of lines are presented in this chapter for elliptic partial differential equations. Semianalytical method, presented in this chapter is very powerful technique, and is valid for elliptic Partial differential equations with mixed boundaries also (Subramanian and White, 1999). Numerical method of lines presented in this chapter should be used with precaution, as it may not work for stiff problems. A total of seven examples were presented in this chapter. [Pg.581]

Chow and Yovanovich [15] showed, by analytical and numerical methods, that the capacitance is a slowly changing function of the conductor shape and aspect ratio provided the total area of the conductor is held constant. [Pg.132]

A check on the foregoing formulas is provided by a comparison with computations that have been laboriously (and carefully) carried out by six-dimensional numerical integration (A.V. Turbiner, private communication). The analytical and numerical methods are in agreement within the precision of the latter. [Pg.68]

The determination of the thermal conductivity of grain is based on the comparison of the temperature history data obtained by using the line heat source probe with the approximate analytical and numerical methods [35,54]. The analytical method has the advantage of being quick in calculating thermal conductivity. This method, however, requires a perfect line source and a small diameter tube holding the line heat source. In reality, this requirement is difficult to meet. Therefore, a time-correction procedure has been introduced [52,54,56]. Another objection to the analytical method is that it cannot easily be used to calculate the temperature distribution in the heated grain and to compare it with the measured one. Such a comparison can be easily accomplished by a numerical method, where the estimated accuracy for thermal conductivity is determined and the thermal conductivity of the device is taken into account [54]. [Pg.578]

See Gerald and Wheatley (2003), and Rice and Do (2012) for details and applications of analytical and numerical methods for solving model equations. [Pg.104]

Naphadzokova, L. Kh. Kozlov, G. V. Synergetics of metal oxides solubility in trans-esterification reaction process. Proceedings of I-th International Sci.-Techn. Conf. "Analytical and Numerical Methods of Natural Scientific and Social Problems Simulation Penza, PSU, 2006, 190-193. [Pg.335]

M-CGl. Have adequate knowledge of the scientific and technological aspects mathematical, analytical and numerical methods... [Pg.191]

Advection and dispersion of contaminants can be modeled using analytical and numerical methods. Advancement of computer technology now permits the use of complex numerical computational methods on portable computers. Modeling is helpful in evaluating factors that control contaminant migration, assessing the extent of contamination, and evaluating the effectiveness of remedial measures. [Pg.237]

The above-mentioned complexity of the relationships between the structure and properties of textiles is further complicated by the non-linear mechanical properties of individual fibres caused by their visco-elastic behaviour, friction between fibres and threads, anisotropy, and statistical distribution of all properties. Modelling such complex materials requires application of a combination of experimental, analytical, and numerical methods, which will be considered in this chapter. [Pg.3]

In Section 4.4 we discussed methods for solving two-dimensional heat-conduction problems using grap]iical procedures and shape factors. In this section we consider analytical and numerical methods. [Pg.310]

Werner, D.H. 1995. Analytical and numerical methods for evaluating the electromagnetic field integrals associated with current-carrying wire antennas. In Advanced Electromagnetism Foundations, Theory and Applications. World Scientific, Ltd. [Pg.1515]

The first possibility is considered in the quasibinary system A—(Bi xCx) with limited solubility, but without intermediate phases. Analytical and numerical methods were used to find the solutions, which correspond to the case of a diffusion path going through the conode (at the interphase boundary, the concentrations jump between two edge points of the conode). At that the inter-diffusion in the couple A, solid solution (BC) was treated in the approximation of parabolic movement of the boundary. On the basis of diffusion equations for a and /3 phases and two equations for flux balance (for A and B components), one has... [Pg.348]

Although there are some additional terms and factors due to random surface roughness and its orientation in equation (2-h), the terms occured are local mean pressure p and expectations of function of actual film thickness only. Therefore, on the meaning of statistical average the hydrodynamic lubrication according to this equation is the same as the smooth form. All the analytical and numerical methods used to evaluate the full film Reynold s equation are still applicable. [Pg.263]


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