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B Finite difference method

In the model equations, A represents the cross sectional area of reactor, a is the mole fraction of combustor fuel gas, C is the molar concentration of component gas, Cp the heat capacity of insulation and F is the molar flow rate of feed. The AH denotes the heat of reaction, L is the reactor length, P is the reactor pressure, R is the gas constant, T represents the temperature of gas, U is the overall heat transfer coefficient, v represents velocity of gas, W is the reactor width, and z denotes the reactor distance from the inlet. The Greek letters, e is the void fraction of catalyst bed, p the molar density of gas, and rj is the stoichiometric coefficient of reaction. The subscript, c, cat, r, b and a represent the combustor, catalyst, reformer, the insulation, and ambient, respectively. The obtained PDE model is solved using Finite Difference Method (FDM). [Pg.631]

In this work the electronic predissociation from the A,B and B states has been studied using a time dependent Golden rule approach in an adiabatic representation. The PES s previously reported[31 ] to simulate the experimental spectrum[22] were used. Non-adiabatic couplings between A-X and B-X were computed using highly correlated electroiric wavefunctions using a finite difference method, with the MOLPRO package[42]. [Pg.402]

Pergamon Press, NY(1962), Chapter 26 "Solution of Characteristics of the Equations of One Dimensional Unsteady Flow , by A.E. Glennie (Method of Characteristics is described) Chapter 27 "Finite Difference Methods for One-Dimensional Unsteady Flow , by N.E. Hoskin B.W. Pearson (Mesh Method is described) 9) H.D. Huskey G,A. Korn, "Computer Handbook , McGraw-Hill, NY(1962)... [Pg.183]

G.S- Telegin, DoklAkad N 147, 1122-25 (1962) CA 58, 7779 (1963) (Calculation of Parameters of Detonation Waves of Condensed Explosives) 77) H. Freiwald R. Schall, Explosivst 10, 1-5 (1962) (Detonation Waves) 77a) N.E. Hoskin B.W. Pearson, "Finite Difference Methods for One- Dimensional Unsteady Flow ... [Pg.728]

B. A. Luty, M. E. Davis, and J. A. McCammon,/. Comput. Chem.,13, 768 (1992). Electrostatic Energy Calculations by a Finite-Difference Method Rapid Calculation of Charge-Solvent Interaction Energies. [Pg.63]

B Solve transient one- or two-dimensional condudion problems using the finite difference method. [Pg.304]

Consider sleady two-dimensional heat transfer in a long solid bar of (a) square and (b) rectangular cross sections as shown in ihe figure. The measured lemperatuces at selecied points of the outer surfaces are as shown. The thermal conductivity of the body is k = 20 W/m °C, and there is no heat generation. Using the finite difference method with a mesh size of d-v = Ay = 1.0 cm, determine the tempeialures at the indicated points in the medium. [Pg.360]

There are many studies that imply numerical methods for the forward modelling of galvanic corrosion problem. These techniques are based mainly on boundary value problems (B VP) formulations in order to obtain or verify results, such as finite element method (FEM), finite difference method (FDM) or boundary element method (BEM). These methods are successfully used and showed to be very accurate to solve BVPs. Some of them are also implemented in commercial software. [Pg.174]

Figure 11.6 Comparison of profiles calculated with OCFE and a finite difference method. N = 1000 plates. Line 1, forward-backward finite difference algorithm, Courant number = 2 line 2, OCFE, fp = 5 s. (a) 1 9 mixture, a = 1.5. (b) 1 1 mixture, a. = 1.5. (c) 5 1 mixture, a = 1.2. Figure 11.6 Comparison of profiles calculated with OCFE and a finite difference method. N = 1000 plates. Line 1, forward-backward finite difference algorithm, Courant number = 2 line 2, OCFE, fp = 5 s. (a) 1 9 mixture, a = 1.5. (b) 1 1 mixture, a. = 1.5. (c) 5 1 mixture, a = 1.2.
Yu, B., and Kawaguchi, Y, Direct numerical simulation of viscoelastic drag-reducing flow a faithful finite difference method, J. Non-Newtonian Fluid Meek, 116, 431-466 (2004). [Pg.126]

FIGURE 6.3. (a) Equal and (b) unequal distance spacings used in the finite difference method. [Pg.83]

The motion of the polymeric network was obtained in numerical simulations by a multistep finite difference method from Eq. (9.26). In Figure 9.3(a), we show oscillations, obtained for appropriate parameters. In (b), we show the concentration distributions of the autocatalytic species for the same intermediate value of the sphere radius Rs = 5 taken, respectively, when the system is swelling (F state) or shrinking (FT state). [Pg.177]

Gourlay extended the slender body theory of Tuck with the unsteady slender body theory. This improvement allows one to consider a ship moving in a non-uniform depth since the coordinate system is now earth-flxed, whereas it is ship-fixed for classic numerical methods. The ID system still uses vertical cross-sections and decomposition into an inner and outer expansion. The pressure integration is only made on the ship length based on the ship section B(x) at each x along the hull. Resolution of the ID equation is made with the finite difference method. Comparison with experimental results for soft squat situations h/T > 4) showed good agreement with numerical results. No tests were made for hard squat conditions (i.e., shallow depths) where flow around the ship is affected. [Pg.757]

Then Cy b(z+ is estimated. Equation (14.3.1.A-g) yields Cj b z+ Az) and an analogous equation the concentration of the products. Numerical integration of (14.3.1.A-k) by means of a finite difference method with variable step size or by means of spline orthogonal collocation leads to in the liquid film and to NaIy yl. Alternatively, approximate analytical solutions may be used. Numerical integration of (14.3.1.A-f) then leads to Cj b z+ A., a value which is compared with the estimated value. If these values do not match, iteration is required. [Pg.796]


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