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Modelling polynomial state

Table 5.1 Number of coefficients to be identified for the polynomial state of a statistical model. Table 5.1 Number of coefficients to be identified for the polynomial state of a statistical model.
Number of factors of the process Statistical model with polynomial state (polynomial degree) ... [Pg.329]

In Table 5.1, where the statistical model is presented in a polynomial state, a rapid increase in the number of identifiable coefficients can be observed as the number of factors and the degree of the polynomial also increase. Each process output results in a new identification problem of the parameters because the complete model process must contain a relationship of the type shown in Eq. (5.3) for each output (dependent variable). Therefore, selecting the Ne volume and particularizing relation (5.5), allows one to rapidly identify the regression coefficients. When Eq. (5.5) is particularized to a single algebraic system we take only one input and one output into consideration. With such a condition, relations (5.3) and (5.5) can be written as ... [Pg.329]

We do not need to carry the algebra further. The points that we want to make are clear. First, even the first vessel has a second order transfer function it arises from the interaction with the second tank. Second, if we expand Eq. (3-46), we should see that the interaction introduces an extra term in the characteristic polynomial, but the poles should remain real and negative.1 That is, the tank responses remain overdamped. Finally, we may be afraid( ) that the algebra might become hopelessly tangled with more complex models. Indeed, we d prefer to use state space representation based on Eqs. (3-41) and (3-42). After Chapters 4 and 9, you can try this problem in Homework Problem 11.39. [Pg.59]

If the transfer functions GL and Gp are based on a simple process model, we know quite well that they should have the same characteristic polynomial. Thus the term -GL/Gp is nothing but a ratio of the steady state gains, -KL/Kp. [Pg.194]

Continuous Transfer functions in polynomial or pole-zero form state-space models transport delay... [Pg.240]

For self-associating protein systems, third-order polynomial functions provided a good fit over the accessible range The data on AG° must show the direction of the chemical change, toward the minimum in the Gibbs function. If this proves true, the equation can be applied in the standard or nonstandard state. For protein unfolding or DNA unwinding, nonlinear models are needed Consistent with Occam s razor, the simplest description is used to describe the system, and complexity is increased only if warranted by the experimental results. [Pg.367]

Reduced concentrations are also useful in the Monod-Wyman-Changeux cooperativity model, where a = [F]/ Kj and ca = [F]/X t. This makes polynomial functions simpler to handle. For example, if ligand F binds exclusively to the R-state, then the ligand F saturation function, Tf, for an n-site protein equals (1 + +... [Pg.614]

A different approach in the use of orthogonal polynomials as a transformation method for the population balance is discussed in (8 2.) Here the error in Equation 11 is minimized by the Method of Weighted Residuals. This approach releases the restrictions on the growth rate and MSMPR operation, however, at the cost of the introduction of numerical integration of the integrals involved, which makes the method computationally unattractive. The applicability in determining state space models is presently investigated and results will be published elsewere. [Pg.148]

L. Kauffman, State models and the Jones polynomial. Topology, 1987, 26, 395-407. [Pg.34]

The obtained steady-state kinetic equations (46) are the kinetic model required for both studies of the process and calculations of chemical reactors. The parameters of eqns. (46) are determined on the basis of experimental data. It is this problem that is difficult. The fact is that, in the general case, eqns. (46) are fractions whose numerator and denominator are the polynomials with respect to the concentrations of observed substances (concentration polynomials). Coefficients of these polynomials can be cumbersome complexes of the initial model parameters. These complexes can also be related. [Pg.229]

Finally, it appears that the kinetic models of complex reactions contain two types of components independent of and dependent on the complex mechanism structure [4—7]. Hence the thermodynamic correctness of these models is ensured. The analysis of simple classes indicates that an unusual analog arises for the equation of state relating the observed characteristics of the open chemical system, i.e. a kinetic polynomial [7]. This polynomial distinctly shows how a complex kinetic relationship is assembled from simple reaction equations. [Pg.384]

A i cation state via a y-polarized transition (also of Bi symmetry) means that the free electron must have A symmetry in order to satisfy the requirement in Eq. (35). This significantly restricts the allowed free electron states. Since the fit to Legendre polynomials required L < 8, partial waves with 1 = 0... 4 are required to model the data. The At symmetry partial waves with l < 4 are... [Pg.565]

Orthogonal collocation on two finite elements is used in the radial direction, as in the steady-state model (1), with Jacobi and shifted Legendre polynomials as the approximating functions on the inner and outer elements, respectively. Exponential collocation is used in the infinite time domain (4, 5). The approximating functions in time have the form... [Pg.362]

The state model and bracket polynomials introduced by L.H. Kauffman seem to be very special because they explore only the peculiar geometrical rules such as summation over all possible knot (link) splittings with simple defined weights. But L.H. Kauffman also showed that bracket polynomials are strongly connected with the Jones polynomials [38]. The substitution A —1 1/4 converts... [Pg.18]

When the preliminary steps of the statistical model have been accomplished, the researchers must focus their attention on the problem of correlation between dependent and independent variables (see Fig. 5.1). At this stage, they must use the description and the statistical selections of the process, so as to propose a model state with a mathematical expression showing the relation between each of the dependent variables and all independent variables (relation (5.3)). During this selection, the researchers might erroneously use two restrictions Firstly, they may tend to introduce a limitation concerning the degree of the polynomial that describes the relation between the dependent variable y( and the independent variables Xj, j = l,n Secondly, they may tend to extract some independent variables or terms which show the effect of the interactions between two or more independent variables on the dependent variable from the above mentioned relationship. [Pg.350]

There is an inherent coupling of the behavior of the micro-scale variables to the behavior of macro-scale variables. This in itself presents complications when simrrlating these models. A few researchers have tried to address this problem of couphng of scales in these models. The solid state concentration term defined by the micro scale diffusion equation need to be coupled with the governing equations for the macro-scale to predict electrochemical behavior. Wang and co-workers used volume averaged equations and a parabolic profile approximation for solid-phase concentration. Subramanian et al. developed approximations assuming that the solid-state concentration inside the spherical electrode particle can be expressed as a polynomial in the spatial direction. [Pg.324]

In the above paragraphs, we have already introduced several approximations in the description of the shift and relaxation rates in transition metals, the most severe being the introduction of the three densities of states Dsp E ),Dt2g(E ), and Deg E ). The advantage is that these values can be supplied by band structure calculations and that the J-like hyperfine field can sometimes be found from experiment. We have no reliable means to calculate the effective Stoner factors ai that appear in Eq. (2), and the disenhancement factors ki in the expression for the relaxation rate, Eq. (4), are also unknown. It is often assumed that k/ can be calculated from some /-independent function of the Stoner parameter k (x), thus k/ = k((X/). A few models exist to derive the relation k((x), all of them for simple metals [62-65]. For want of something better they have sometimes been applied to transition metals as well [66-69]. We have used the Shaw-Warren result [64], which can be fitted to a simple polynomial in rx. There is little fundamental justification for doing so, but it leads to a satisfactory description of, e.g., the data for bulk Pt and Pd. [Pg.492]


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