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Elements Equations

The exponential of a diagonal matrix is again a diagonal matrix with exponentials of the diagonal elements, equation (B2.4.17)). [Pg.2097]

Note that in equation system (2.64) the coefficients matrix is symmetric, sparse (i.e. a significant number of its members are zero) and banded. The symmetry of the coefficients matrix in the global finite element equations is not guaranteed for all applications (in particular, in most fluid flow problems this matrix will not be symmetric). However, the finite element method always yields sparse and banded sets of equations. This property should be utilized to minimize computing costs in complex problems. [Pg.48]

After the aussembly of elemental equations into a global set and imposition of the boundary conditions the final solution of the original differential equation with respect to various values of upwinding parameter jS can be found. The analytical solution of Equation (2.80) with a = 50 is found as... [Pg.61]

The Galerldn finite element method results when the Galerldn method is combined with a finite element trial function. The domain is divided into elements separated by nodes, as in the finite difference method. The solution is approximated by a linear (or sometimes quadratic) function of position within the element. These approximations are substituted into Eq. (3-76) to provide the Galerldn finite element equations. The element integrals are defined as... [Pg.477]

Lagranglan codes are characterized by moving the mesh with the material motion, u = y, in (9.1)-(9.4), [24]. The convection terms drop out of (9.1)-(9.4) simplifying all the equations. The convection terms are the first terms on the right-hand side of the conservation equations that give rise to fluxes between the elements. Equations (9.1)-(9.2) are satisfied automatically, since the computational mesh moves with the material and, hence, no volume or mass flux occurs across element boundaries. Momentum and energy still flow through the mesh and, therefore, (9.3)-(9.4) must be solved. [Pg.331]

Introducing a concept of gradient diffusion for particles and employing a mixture fraction for the non-reacting fluid originating upstream, / = c Vc O) and a probability density function for the statistics of the fluid elements, /(/), equation (2.100) becomes... [Pg.56]

In general, the equations for the density operator should be solved to describe the kinetics of the process. However, if the nondiagonal matrix elements of the density operator (with respect to electron states) do not play an essential role (or if they may be expressed through the diagonal matrix elements), the problem is reduced to the solution of the master equations for the diagonal matrix elements. Equations of two types may be considered. One of them is the equation for the reduced density matrix which is obtained after the calculation of the trace over the states of the nuclear subsystem. We will consider the other type of equation, which describes the change with time of the densities of the probability to find the system in a given electron state as a function of the coordinates of heavy particles Pt(R, q, Q, s,...) and Pf(R, q, ( , s,... ).74,77 80... [Pg.160]

If FA represents the molal flow rate of reactant A into the volume element and FA + dFA represents the molal flow rate out of the volume element, equation 8.2.1 becomes... [Pg.263]

In order to calculate eigenvalues of energy use is made of the corresponding Boundary Element Equation (BEE) of this BIE. And for matrix elements of BEE we have ... [Pg.174]

The total volumetric flow rate through the pipe is obtained by integrating the element equation over the whole cross section of the pipe, that is from r = 0 to r = r, ... [Pg.45]

For very small partition coefficients (incompatible elements), equation (9.3.13) becomes... [Pg.497]

For kinetic disequilibrium partitioning of trace elements, equation (9.6.6) after Burton et al. (1953) is commonly presented as an alternative to equation (9.6.5) due to Tiller et al. (1953) (e.g., Magaritz and Hofmann, 1978 Lasaga, 1981 Walker and Agee, 1989 Shimizu, 1981). However, the relative values of viscosity and chemical diffusivity in common liquids and silicate melts make the momentum boundary-layer (i.e., the liquid film which sticks to the solid) orders of magnitude thicker than the chemical boundary layer. It is therefore quite unlikely that, except for rare cases of transient state, liquid from outside the momentum boundary-layer may encroach on the chemical boundary-layer, i.e., <5 may actually be taken as infinite. As a simple description of steady-state disequilibrium fractionation, the model of Tiller et al. (1953) has a much better physical rationale. A more elaborate discussion of these processes may be found in Tiller (1991a, b). [Pg.525]

The matrix element < [Equation (7.9)] is zero unless the direct product... [Pg.252]

Let us now consider a galvanic cell with the redox couples of equation 8.164. This cell may be composed of a Cu electrode immersed in a one-molal solution of CUSO4 and a Zn electrode immersed in a one-molal solution of ZnS04 ( Dan-iell cell or Daniell element ). Equation 8.170 shows that the galvanic potential is positive the AG of the reaction is negative and the reaction proceeds toward the right. If we short-circuit the cell to annul the potential, we observe dissolution of the Zn electrode and deposition of metallic Cu at the opposite electrode. The flow of electrons is from left to right thus, the Zn electrode is the anode (metallic Zn is oxidized to Zn cf eq. 8.167), and the Cu electrode is the cathode (Cu ions are reduced to metallic Cu eq. 8.168) ... [Pg.543]

As indicated earlier, a difficulty immediately arises the evaluation of the parts of the matrix elements (equation 4) involving terms containing r using free-ion d wave functions gives results which are obviously grossly in error. Consequently, there is not likely to be any relationship between the parameters such as developed in cubic symmetry the low symmetry cases involve (at least) three parameters to describe the d-orbital splitting pattern. [Pg.220]

The use of alkoxides to synthesize new alkoxides by the process of alcohol interchange has been widely applied for a large number of elements (equation 15). [Pg.339]

Normally we would choose to do the sum over classes rather than over group elements. Equation (20) is an extremely useful relation, and is used frequently in many practical applications of group theory. [Pg.79]

Recommended analytical masses, elemental equations, interference effects, and internal standards are summarized below in the following tables. [Pg.434]

Table 4 Recommended Elemental Equations for Calculations (Continued)... [Pg.437]

With these relationships for off-diagonal matrix elements, equation (3) can be written in the following general form ... [Pg.65]

Once a finite element formulation has been implemented in conjunction with a specific element type — either 1D, 2D or 3D — the task left is to numerically implement the technique and develop the computer program to solve for the unknown primary variables — in this case temperature. Equation (9.19) is a form that becomes very familiar to the person developing finite element models. In fact, for most problems that are governed by Poisson s equation, problems solving displacement fields in stress-strain problems and flow problems such as those encountered in polymer processing, the finite element equation system takes the form presented in eqn. (9.19). This equation is always re-written in the form... [Pg.458]

Before we proceed to our discussion of global stiffness matrix storage schemes, we will discuss the last aspect of the finite element implementation, namely, the application of the boundary conditions. As discussed earlier, the natural boundary conditions are imbedded in the finite element equation system - it is implied that every boundary node without an... [Pg.461]

Following the procedure used with the one-dimensional FEM model and using the constant strain triangle element developed in the previous section, we can now formulate the finite element equations for a transient conduction problem with internal heat generation rate per unit volume of Q. The governing equation is given by... [Pg.474]


See other pages where Elements Equations is mentioned: [Pg.121]    [Pg.781]    [Pg.1391]    [Pg.22]    [Pg.40]    [Pg.75]    [Pg.94]    [Pg.95]    [Pg.10]    [Pg.177]    [Pg.221]    [Pg.141]    [Pg.183]    [Pg.407]    [Pg.205]    [Pg.81]    [Pg.189]    [Pg.208]    [Pg.229]    [Pg.18]    [Pg.434]    [Pg.436]    [Pg.436]    [Pg.437]    [Pg.99]    [Pg.457]   
See also in sourсe #XX -- [ Pg.277 , Pg.306 , Pg.308 ]




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