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Differential operations time derivatives

A differential equation for the time evolution of the density operator may be derived by taking the time derivative of equation (Al.6.49) and using the TDSE to replace the time derivative of the wavefiinction with the Hamiltonian operating on the wavefiinction. The result is called the Liouville equation, that is. [Pg.230]

The result is the most useful of all the Laplace transformations. It says that the operation of differentiation in the time domain is replaced by multiplication by s in the Laplace domain, minus an initial condition. This is where perturbation variables become so useful. If the initial condition is the steadystate operating level, all the initial conditions like are equal to zero. Then simple multiplication by s is equivalent to differentiation. An ideal derivative unit or a perfect differentiator can be represented in block-diagram form as shown in Fig. 9.3. [Pg.313]

Equation (3.133) can be applied to a fluid element moving with the mass average velocity v. After replacing the differential operators with substantial time derivative operators inEq. (3.133), we have... [Pg.121]

To derive the overall kinetics of a gas/liquid-phase reaction it is required to consider a volume element at the gas/liquid interface and to set up mass balances including the mass transport processes and the catalytic reaction. These balances are either differential in time (batch reactor) or in location (continuous operation). By making suitable assumptions on the hydrodynamics and, hence, the interfacial mass transfer rates, in both phases the concentration of the reactants and products can be calculated by integration of the respective differential equations either as a function of reaction time (batch reactor) or of location (continuously operated reactor). In continuous operation, certain simplifications in setting up the balances are possible if one or all of the phases are well mixed, as in continuously stirred tank reactor, hereby the mathematical treatment is significantly simplified. [Pg.751]

Equation 5.2.18 is the dimensionless, differential energy balance equation of ideal batch reactors, relating the reactor dimensionless temperature, 0(t), to the dimensionless extents of the independent reactions, Z (t), at dimensionless operating time T. Note that individual dZ /dfr s are expressed by the reaction-based design equations derived in Chapter 4. [Pg.139]

The modeling of stationarily operating enzyme electrodes is a special case of nonstationary modeling. In this context, stationary means the consideration of the behaviour after infinite time (steady state), i.e., solutions have to be found for which the time derivative has to be zero. For all models considered, the existence of a unique and stable mathematical solution is assumed. Since the respective partial differential equations are linear initial boundary problems, known existence and uniqueness theorems may be used (Kamke, 1956 Fife, 1979 Ozisik, 1980). [Pg.68]

Since the time derivative operator is mathematically well defined, and the operator d is not, it is important to remember in using Eqs. 3.1-9 that they are abbreviations of Eq. 3.1-8. It is part of the traditional notation of thermodynamics to use cW to indicate a differential change in the property 6. rather than the mathematically more correct ddldt. [Pg.54]

From (10.55) we see that the tensors gij,g and behave as though they were constants in material differentiation with respect to t. However, this is not the case with surface metric tensor ttap as can be seen from (10.56), and it is the consequence of its explicit dependence of time. Then the operation of raising and lowering of indices of tensor fields with respect to aap is not, generally, commutative with material time derivative. Particularly, this is tme for Indeed, it is easy to show that... [Pg.247]

It is noted that the momentum derivatives of the coupling elements (51) represent one of the main obstacles of a practical trajectory-based evaluation of the QCL equation, because these terms require the knowledge of the function in question not only at a particular point in phase space but at the same time also at nearby points. As a remedy, we may restrict ourselves to the limit of small momentum changes Snm/P At 1 and approximate 1 - - SnmP exp(S m5/dP). Since eP / Pf p) = /(p + S ), the approximation reduces the action of the differential operator to a simple shift of momenta. We note that this approximation resembles the usual momentum-jump ansatz employed in various surface-hopping methods. ... [Pg.654]

If the reactor is not operating at steady state, the calculation of the multiplication constant is more difficult, since, in the differential equation, there is now a time-derivative term to be considered. A convenient method for treating this case involves the use of the quantity Ve (introduced in Sec. 4.6d), a fictitious number of neutrons per fission, which may be adjusted so that for any composition and configuration the fission sources can be made just to balance the losses. Thus we choose as the applicable differential equation for the nonstationary system... [Pg.210]

Another requirement in satisfying the special theory of relativity is to have the spatial and temporal variables being treated on the same footing. The differential operators in Lorentz invariant form are QIQx, 6/0y, didz, and (l/ic)0/0t, giving the magnitude for spatial and temporal dimensions as x + y + z — c t. This means that the order of the differentials for the coordinate and time in the equation of motion must be the same. The time-dependent Schrodinger equation exhibits time derivatives in the first order and coordinate derivatives in the second order therefore it is not Lorentz invariant. [Pg.114]

In dealing with fields that vary over time and space, we will need various differential operators. In the nonrelativistic theory of electrodynamics the gradient operator, V, and the time derivative, d/dr, are used. From our experience in the previous chapter with mixing of space and time coordinates under Lorentz transformations, we might expect these to combine in a four-space differential operator also. Indeed, in our notation. [Pg.17]

Note that this Four-Parameter Fluid model is composed of a Kelvin element (subscripts 1) and a Maxwell element (subscripts 0). Thus, the constitutive laws (differential equations) for the Kelvin and Maxwell elements need to be used in conjunction with the kinematic and equilibrium constraints of the system to provide the governing differential equation. Again, treating the time derivatives as differential operators will allow the simplest derivation of Eq. 5.12. The derivation is left as an exercise for the reader as well as the determination of the relations between the pi and q, coefficients and the spring moduli and damper viscosities (see problem 5.1). [Pg.164]

We have obtained the recursive expressions and the formal operators to calculate the high order time derivatives of the absolute angular velocities and of the mass center positions. The differentiation of the mechanical tensor terms with respect to the generalized coordinates is given in the Appendix. In the following section, we will give a summary of our programming. [Pg.72]

The terms in brackets equal an operator analogous to the substantial time derivative known from the transport phenomena literature. The total differential of / (r, c, t) is given by ... [Pg.212]

When an agitated bateh eontaining M of fluid with speeifie heat e and initial temperature t is heated using an isothermal eondensing heating medium Tj, the bateh temperature tj at any time 6 ean be derived by the differential heat balanee. For an unsteady state operation as shown in Figure 7-27, the total number of heat transferred is q, and per unit time 6 is ... [Pg.637]

In this equation, H, the Hamiltonian operator, is defined by H = — (h2/8mir2)V2 + V, where h is Planck s constant (6.6 10 34 Joules), m is the particle s mass, V2 is the sum of the partial second derivative with x,y, and z, and V is the potential energy of the system. As such, the Hamiltonian operator is the sum of the kinetic energy operator and the potential energy operator. (Recall that an operator is a mathematical expression which manipulates the function that follows it in a certain way. For example, the operator d/dx placed before a function differentiates that function with respect to x.) E represents the total energy of the system and is a number, not an operator. It contains all the information within the limits of the Heisenberg uncertainty principle, which states that the exact position and velocity of a microscopic particle cannot be determined simultaneously. Therefore, the information provided by Tint) is in terms of probability I/2 () is the probability of finding the particle between x and x + dx, at time t. [Pg.3]


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See also in sourсe #XX -- [ Pg.165 ]




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