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Use of Integrated Equations

An alternative to a graphical display is to calculate the rate constant for each data point using the integrated rate equation, seeking constancy in the calculated k values. [Pg.24]

A reaction order determined by plotting the integrated rate equation is sometimes called the order with respect to time f this order has an unambiguous meaning only if the order is independent of time, which means that the plotted function is linear [Pg.24]


Making use of integral equation (4) again this beeomes ... [Pg.127]

In fact, during the last 30 years the use of integral equations has allowed us to move significantly forward in the theory and interpretation of induction logging. This is the main reason why we will describe here only this numerical method. At the same time it is reasonable to point out that both methods have been used, provided that a model of the medium and a field have cylindrical symmetry with the common axis. Until now this restriction has not permitted us to investigate a field behavior in the case when the boundaries between a formation and a surrounding medium are not perpendicular to the borehole axis. [Pg.159]

Computer simulations are not the only methods which can be used to calculate the dielectric constant of pure liquids. Other approaches are given by the use of integral equations, in particular, the hypemetted chain (HNC) molecular integral equation and the molecular Omstein-Zemike (OZ) theory (see Section 8.7.1 for details on such methodologies). [Pg.488]

As already said, the use of integral equation methodologies is not the only possible way of obtaining thermodynamical properties for liquids. Computer simulations are also widely used, and it is then possible to obtain equilibrium properties by mean of both Monte Carlo and Molecular Dynamics simulations. [Pg.490]

Because of the work involved in solving large systems of simultaneous linear equations it is desirable that only a small number of us be computed. Thus the gaussian integration formulas are useful because of the economy they offer. See references on numerical solutions of integral equations. [Pg.478]

One important class of integral equation theories is based on the reference interaction site model (RISM) proposed by Chandler [77]. These RISM theories have been used to smdy the confonnation of small peptides in liquid water [78-80]. However, the approach is not appropriate for large molecular solutes such as proteins and nucleic acids. Because RISM is based on a reduction to site-site, solute-solvent radially symmetrical distribution functions, there is a loss of infonnation about the tliree-dimensional spatial organization of the solvent density around a macromolecular solute of irregular shape. To circumvent this limitation, extensions of RISM-like theories for tliree-dimensional space (3d-RISM) have been proposed [81,82],... [Pg.144]

Now, we would like to comment on some general features of the solutions of integral equations for the local density. We use superscripts H and P to abbreviate the solutions of the HNCl and PYl equations (6) and (7), respectively. By considering the limiting behavior of the cavity functions inside the solid one obtains... [Pg.175]

The above-quoted integral equation has been widely used over the last 50 years and to give a detailed aeeount of all its divergent appheations would require a whole book. The interested reader is advised to eonsult several already available review artieles [8-10] as well as a number of exeellent monographs [4-6,11,12]. Here we only mention some direetions of researeh that use the integral equation approaeh and will shortly point some of its advantages as well as limitations and drawbaeks it suffers from. [Pg.246]

Integral equation theories are widely used in the theoretical study of liquids. There are two broad classes of integral equation theories those based on the Bom-Green-Yvon (BGY) hierarchy and those based on the Omstein-Zemike (OZ) equation [88]. Although the formalism is exact in both classes, it is generally easier to fashion approximations in the case of the OZ-equation-based approach, and this type of theory has therefore been more popular. Surprisingly, the BGY approach has never been implemented for nonuniform polymers, and this section is therefore restricted to a discussion of the OZ-equation-based approach. [Pg.109]

Ideal reactors can be classified in various ways, but for our purposes the most convenient method uses the mathematical description of the reactor, as listed in Table 14.1. Each of the reactor types in Table 14.1 can be expressed in terms of integral equations, differential equations, or difference equations. Not all real reactors can fit neatly into the classification in Table 14.1, however. The accuracy and precision of the mathematical description rest not only on the character of the mixing and the heat and mass transfer coefficients in the reactor, but also on the validity and analysis of the experimental data used to model the chemical reactions involved. [Pg.481]

AG is the free energy change of a process with AS and AV as the accompanying changes in entropy and volume. As a first approximation, one can assume AS and AV to be nearly constant within a limited p and T range, and use the integrated equation... [Pg.127]

Tbe results for water are mainly available from computer simulations, although some results of integral equation theories have been reported in recent years. Despite the varied nature of the intermolecular potential energy functions used, most of these studies give a qualitatively similar picture. As an example, we consida in some detail the results obtained for the potential energy function given above (for the interface between water and Pt). [Pg.128]

The purpose of this example is to show how to design the control system by using the pole-placement technique and the use of integrators. The integrators can be represented by introducing a new set of state variables u(t), so the equations of the global system are the following ... [Pg.26]

Our problem has four parts. First, we must determine the rate law for an infinitesimal length of catalyst bed. Second, the resulting equation must be integrated over the length of the bed. Third, the values of certain of the system parameters must be determined using the integrated equation and experimental conversions. Finally, the site density is determined from the values of these parameters. [Pg.114]

Liu,Y., Safavi-Naeini, S., Chaudhuri, S.K., and Sabry, R., 2004, On the determination of resonant modes of dielectric objects using surface integral equations, IEEE Trans. Antennas Propagat. 52(4) 1062-1069. [Pg.67]

We cannot evaluate the constant of integration in Equation (15.27) as easily as we did with Equation (15.24), because in the limit of X2 = 0, where Henry s law is followed. In X2 would approach negative infinity. (As X2 0, p,2 also tends toward negative infinity.) Instead, let us make use of the equation for the chemical potential of component 2 in the gas phase in equilibrium with the solution. That is [from Equation (10.23)],... [Pg.344]

These equations are the standard form of a well-studied class of integral equations, the Volterra equation of the second kind (see, for example, Brunner and van der Houwen, 1986). Before discussing the numerical method, we draw a few simple conclusions from those equations. Using a free-electron-metal tip (that is, if in the entire energy range of interest). [Pg.310]

Rather than solving the master equation and subsequently taking the Laplace transform, it is often easier to make use of the equation for pB>IB(A) itself. Multiply (VI.1.2) with e-A, integrate over t from 0 to oo, and use partial integration in the left-hand member,... [Pg.309]

A detailed treatment of the theoretical approach used in treating LSV and CV boundary value problems can be found in the monograph by MacDonald [23], More specific information on the numerical solution of integral equations common to electrochemical methods is available in the chapter by Nicholson [30]. The most commonly used method for the calculation of the theoretical electrochemical response, at the present time, is digital simulation which has been well reviewed by Feldberg [31, 32], Prater [33], Maloy [34], and Britz [35]. [Pg.156]

Equation 8-16 can be integrated under the assumption that c0 remains constant as pressure changes. Our future use of this equation will be related to bubble-point pressure, so we will use a lower limit of... [Pg.234]

If the measuring (transmitting) circuit of an instrument has linear characteristics (which requires separate experimental validation), the output signal of a linear instrument y(t) is expressed in terms of the input signal x(t) using the integral equation ... [Pg.107]

One problem for kineticists is that only a relatively slight increase in complexity of the kinetic scheme results in differential equations which cannot be integrated in a straightforward manner to give a manageable analytical expression. When this happens the differential equations have to be solved by either numerical integration or computer simulation. This is a mathematical limitation of the use of integrated rate expressions which is not apparent in the kinetic scheme. Typical schemes which are mathematically complex are... [Pg.81]


See other pages where Use of Integrated Equations is mentioned: [Pg.126]    [Pg.24]    [Pg.473]    [Pg.20]    [Pg.177]    [Pg.417]    [Pg.79]    [Pg.1243]    [Pg.126]    [Pg.24]    [Pg.473]    [Pg.20]    [Pg.177]    [Pg.417]    [Pg.79]    [Pg.1243]    [Pg.328]    [Pg.79]    [Pg.151]    [Pg.322]    [Pg.2]    [Pg.91]    [Pg.79]    [Pg.71]    [Pg.164]    [Pg.170]    [Pg.192]    [Pg.465]    [Pg.16]    [Pg.130]    [Pg.209]   


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