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The State Equations

Equation (8.2) is generally ealled the state equation(s), where lower-ease boldfaee represents veetors and upper-ease boldfaee represents matriees. Thus... [Pg.233]

Write down the state equation and output equation for the spring-mass-damper system shown in Figure 8.1(a). [Pg.234]

For the RCL network shown in Figure 8.2, write down the state equations when... [Pg.235]

For the spring-mass-damper system given in Example 8.1, Figure 8.1, the state equations are shown in equation (8.13)... [Pg.241]

The discrete-time solution of the state equation may be considered to be the vector equivalent of the scalar difference equation method developed from a z-transform approach in Chapter 7. [Pg.244]

The continuous-time solution of the state equation is given in equation (8.47). If the time interval t — to) in this equation is T, the sampling time of a discrete-time system, then the discrete-time solution of the state equation can be written as... [Pg.245]

Wlienxi =yandx2 = Li, express the state equation in the eontrollable eanonieal form. Evaluate the eoeffieients of the state feedbaek gain matrix using ... [Pg.251]

Equation (8.106) provides the output equation and (8.107) the state equation... [Pg.252]

Using the state veetors x(t) and x(t) the state equations for the elosed-loop system are... [Pg.261]

Equation (10.57) is in the same form as the discrete-time solution of the state equation (8.76). [Pg.350]

This is the state equation of an ideal gas, where p is pressure, v is specific volume, p is density, R is the gas constant, and T is absolute temperature. In an airflow there is a transfer of heat from one layer to another. This change of... [Pg.49]

According to the state equation of ideal gas, the partial density of dry air in humid air is... [Pg.65]

Minimization of S(k) can be accomplished by using almost any technique available from optimization theory, however since each objective function evaluation requires the integration of the state equations, the use of quadratically convergent algorithms is highly recommended. The Gauss-Newton method is the most appropriate one for ODE models (Bard, 1970) and it presented in detail below. [Pg.85]

In the case of ODE models, the sensitivity matrix G(t() = (3xT/3k)T cannot be obtained by a simple differentiation. However, we can find a differential equation that G(t) satisfies and hence, the sensitivity matrix G(t) can be determined as a function of time by solving simultaneously with the state ODEs another set of differential equations. This set of ODEs is obtained by differentiating both sides of Equation 6.1 (the state equations) with respect to k, namely... [Pg.86]

Equations 6.47a and 6.47b should be solved simultaneously with the state equation (Equation 6.45). The three ODEs are put into the standard form (dz/dt = differential equation solvers by setting... [Pg.98]

If we wish to avoid the additional objective function evaluation at p=qa/2, we can use the extra information that is available at p=0. This approach is preferable for differential equation models where evaluation of the objective function requires the integration of the state equations. It is presented later in Section 8.7 where we discuss the implementation of Gauss-Newton method for ODE models. [Pg.141]

It should be emphasized here that it is unnecessary to integrate the state equations for the entire data length for each value of u. Once the objective function becomes greater than S(k0)). a smaller value for p can be chosen. By this procedure, besides the savings in computation time, numerical instability is also avoided since the objective function often becomes large very quickly and integration is stopped well before computer overflow is threatened. [Pg.150]

The main difference with differential equation systems is that every evaluation of the objective function requires the integration of the state equations, In this section we present an optimal step size policy proposed by Kalogerakis and Luus (1983b) which uses information only at g=0 (i.e., at k ) and at p=pa (i.e., at... [Pg.150]

The integration of the state equations (Equation 10.21) by the fully implicit Euler s method is based on the iterative determination of x(t1+i). Thus, having x(t,) we solve the following difference equation for x(t, i). [Pg.174]

The solution of Equation 10.28 is obtained in one step by performing a simple matrix multiplication since the inverse of the matrix on the left hand side of Equation 10.28 is already available from the integration of the state equations. Equation 10.28 is solved for r=l,...,p and thus the whole sensitivity matrix G(tr,) is obtained as [gi(tHt), g2(t,+1),- - , gP(t,+i)]. The computational savings that are realized by the above procedure are substantial, especially when the number of unknown parameters is large (Tan and Kalogerakis, 1991). With this modification the computational requirements of the Gauss-Newton method for PDE models become reasonable and hence, the estimation method becomes implementable. [Pg.176]

Here the B-spline Bim(zf, Xj) is the ith B-spline basis function on the extended partition Xj (which contains locations of the knots in the Zj direction), and is a coefficient. We use cubic splines and sufficient numbers of uniformly spaced knots so that the estimation problem is not affected by the partition. The estimation problem now involves determining the set of B-spline coefficients that minimizes Eq. (4.1.26), subject to the state equations [Eqs. (4.1.24 and 4.1.25)], for a suitable value of the regularization parameter. At this point, the minimization problem corresponds to a nonlinear programming problem. [Pg.374]

The fluid properties and porosity and permeability are determined independently. Boundary and initial conditions are specified for the particular experiment to be considered. With specified multiphase flow functions, the state equations, Eqs. (4.1.28, 4.1.5 and 4.1.6), can be solved for the transient pressure and saturation distributions, p (z,t) and s,(z,t), t= 1, 2. The values for F can then be calculated, which correspond to the measured data Y. [Pg.376]

Since its potential is positive, the first equation states that Agf tends to react with Cu. Since its potential is negative, the second equation states that Ag+ tends to react with Cu. (The reverse of the stated equation tends to proceed.) The same conclusion is drawn with either equation. You can always get a positive cell potential if you reverse the lower of the two half-cells from Table 14-2. [Pg.236]

The basic idea of DCGT is to replace the density in the state equation of a gas by the dielectric constant e. [Pg.212]

This paper is organized as follows. Section 2 presents non-trivial properties of the velocity distribution functions for RIG for quasi and ordinary particles in one dimensions. In section 3 we find the state equation for relativistic ideal gas of both types. Section 4 presents the distribution function for the observed frequency radiation generated for quasi and ordinary particles of the relativistic ideal gas, for fluxons under transfer radiation and radiative atoms of the relativistic ideal gas. Section 5 presents a generalization of the theory of the relativistic ideal gas in three dimensions and the distribution function for particles... [Pg.161]

Because A is negative and the overall term must be positive since there is heat release, the third term has a negative sign. The state equation is written as... [Pg.163]


See other pages where The State Equations is mentioned: [Pg.235]    [Pg.236]    [Pg.236]    [Pg.237]    [Pg.238]    [Pg.239]    [Pg.257]    [Pg.262]    [Pg.276]    [Pg.291]    [Pg.339]    [Pg.369]    [Pg.369]    [Pg.46]    [Pg.50]    [Pg.526]    [Pg.526]    [Pg.531]    [Pg.91]    [Pg.91]    [Pg.91]    [Pg.148]    [Pg.362]    [Pg.373]   


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Application of the Arrhenius equation to solid state reactions

Corresponding States Using The Lee-Kesler Equation of State

Dimensionless Form of the Generalized Mass Transfer Equation with Unsteady-State Convection, Diffusion, and Chemical Reaction

Discrete-time solution of the state vector differential equation

Equation of state near the critical point

Integral equation for the box-normalised collision state

Isotherms Derived from the Equation of State

Liquid Equilibrium Using the Equations of State Method

Modeling Phase Behavior with the Peng-Robinson Equation of State

Solution of the Steady-State Equations

Solution of the state vector differential equation

Solutions of the Steady-State Atmospheric Diffusion Equation

Some simple solutions to the diffusion equation at steady state

Specific heats and the equation of state

State Transition Diagrams from the Nonlinear Equations

States of Matter and the van der Waals Equation

The Bender Equation of State

The Benedict-Webb-Rubin (BWR) Equation of State

The Benedict-Webb-Rubin Equation of State

The Compressibility Factor Equation of State

The Equation of State

The Equation of State Approach

The MCTDH Equations of Motion for Several Electronic States

The Patel-Teja Equation of State

The Redlich-Kwong equation of state

The Schrodinger equation and stationary states

The Steady State Equations

The Trebble-Bishnoi Equation of State

The Virial Equation of State

The energy equation for general steady-state flow

The equation of state Extensive and intensive properties

The reduced equation-of-state

The state vector differential equation

The thermodynamic equation of state

The van der Waals equation and cubic equations of state

The van der Waals equation of state

Thermodynamics The equations of state

Thermodynamics and the Equation of State

Vapor-Liquid Equilibrium Modeling with Two-Parameter Cubic Equations of State and the van der Waals Mixing Rules

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