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Difference quotient second

The truncation error ex is estimated as the contribution of the second-derivative term in Eq. (6.B-2) to the difference quotient in Eq. (6.B-3). Show that this gives... [Pg.128]

The second derivative in the -direction at position xf at time tk is replaced by the central second difference quotient... [Pg.194]

The second derivative (<92 d/<9x2)f+1 2 at time tk + At/2 is replaced by the arithmetic mean of the second central difference quotients at times tk and tk+l. This produces... [Pg.203]

The two second derivatives in the x- or y-directions are approximated by the central difference quotient, so that... [Pg.212]

Flip Rule Cross relations can be found in two ways. First, by using energy balances for appropriate cyclic processes and second as a direct result of a mathematical operation we call flipping. Naturally, the flip rule can be derived mathematically (see end of the Chapter), but we will give instructions here in the form of a kind of recipe Take the differential quotient in question (or difference quotient) you wish to transform and... [Pg.257]

Second, the balance is taken over an incremental space element, Ac, Ar, or AV. The mass balance equation is then divided by these quantities and the increments allowed to go to zero. This reduces e difference quotients to derivatives and the mass balance now applies to an infinitesimal point in space. We speak in this case of a "difference" or "differential" balance, or alternatively of a "microscopic" or "shell" balance. Such balances arise whenever a variable such as concentration undergoes changes in space. They occur in all systems that fall in the category of the device we termed a 1-D pipe (Figure 2.1b). When the system does not vary with time, i.e., is at steady state, we obtain an ODE. When variations with time do occur, the result is a partial differential equation (PDE) because we are now dealing with two independent variables. Finally, if we discard the simple 1-D pipe for a multidimensional model, the result is again a PDE. [Pg.50]

R is the ideal gas constant, T is the Kelvin temperature, n is the number of electrons transferred, F is Faraday s constant, and Q is the activity quotient. The second form, involving the log Q, is the more useful form. If you know the cell reaction, the concentrations of ions, and the E°ell, then you can calculate the actual cell potential. Another useful application of the Nernst equation is in the calculation of the concentration of one of the reactants from cell potential measurements. Knowing the actual cell potential and the E°ell, allows you to calculate Q, the activity quotient. Knowing Q and all but one of the concentrations, allows you to calculate the unknown concentration. Another application of the Nernst equation is concentration cells. A concentration cell is an electrochemical cell in which the same chemical species are used in both cell compartments, but differing in concentration. Because the half reactions are the same, the E°ell = 0.00 V. Then simply substituting the appropriate concentrations into the activity quotient allows calculation of the actual cell potential. [Pg.272]

By comparing Eqs. (54)-(56) a few differences are evident. Compared to Eqs. (55) and (56) the numerator of the last quotient in Eq. (54) is unsquared. In the publication of Balinov et al the sign of the second term in Eq. (54) was negative, but in a later publication the sign has been changed into +, as we already have written. Further, the first term of the Balinov equation (55) seems to be missing in the other two equations. [Pg.213]

The growth rate, characterized by the change of the radius with time, is proportional to the driving force for the phase separation, given by the differences between 2 > the chemical composition of the second phase in the continuous phase at any time, and, its equihbrium composition given by the binodal line. The proportionahty factor, given by the quotient of the diffusion constant, D, and the radius, r, is called mass transfer coefficient. Furthermore the difference between the initial amount of solvent, (])o, and c]) must be considered. The growth rate is mathematically expressed by [101]... [Pg.204]

Quotient of the second normal stress difference Nt) and the square of the shear rate (y) in the limit of zero shear rate... [Pg.162]

As shown by TalkneP there is a direct connection between the Rayleigh quotient method and the reactive flux method. Two conditions must be met. The first is that phase space regions of products must be absorbing. In different terms, the trial function must decay to zero in the products region. The second condition is that the reduced barrier height pyl" 1. As already mentioned above, differences between the two methods will be of the order e P. ... [Pg.10]

In a second study, intellectual functioning at 6-9 years was measured in 88 cocaine-exposed children and 96 unexposed children in New York City (273). The participants were interviewed and underwent medical and neurological examination and psychological assessment. Child intelligence was measured with the Wechsler Intelligence Scale for Children-III (WISC-III). Intelligence quotient scores did not differ between the two groups of children, even when adjustments for covariables were made. [Pg.514]

The first HTU term contains the physical and fluid-dynamic parameter and the second NTU term expresses the number of theoretical stages as function of the solute concentration difference. The extractor-specific HTU value is, on the one hand, described by the quotient of flow rate and cross-sectional area of the column, and, on the other hand, it is characterised by the interfacial area per unit volume and the mass transfer coefficient. The former is mainly influenced by drop size and phase hold-up, the latter by the relative movement of the dispersed phase. These characteristic HTU values can be experimentally measured for a certain extractor type and are used for comparison with other extractors or for the projection of larger units. [Pg.34]

This consideration leads to a common scheme in which delays of the order of 7xT are used between the n/2-n/2 clusters with the first and the second FID s (which are proportional to Mq and M(t), respectively) recorded and the quotient or the difference calculated, according to whether the first or the second of the above equations are being used. Thus, Mq is determined each time M(t) is determined and the above requirement is satisfied. This scheme has the added advantage that slowly drifting electronics do not affect the accuracy of T because the drift should contribute nearly equally to Mq and to M(t). An obvious extension is to use clusters of more than two pulses and use the 1st and the last FID s. Such a sequence (discussed later) can be quite in-... [Pg.167]

Michaelis-Menten parameters and determined for isolated enzymes for transforming different substrates. The value corresponds to the natural substrate [e.g. MejNO, MeaSO) while refers to the Michaelis-Menten constant for the second substrate (see also eqn (4.11)). The quotient of represents the catalytic specificity. ... [Pg.120]

Let s now consider a scenario where the same number of reactants are used as in the above example, but a different sequence is involved. Here the intermediate is formed in a second order reaction, and the intermediate converts to product in a first order reaction (Eq. 7.48). Eq. 7.49 expresses the rate of the reaction, and Eq. 7.50 expresses the SSA. Solving Eq. 7.50 for [I] leads to Eq. 7.51, which upon substitution into Eq. 7.49 gives Eq. 7.52. Eq. 7.52 has several rate constants incorporated into a product and quotient, which taken together is a constant that we call fcobs- This mechanistic scenario predicts that the reaction is first order in A and B, distinctly different than that presented in the last mechanistic scenario. This comparison reveals the power of a kinetic analysis when deciphering complex reaction mechanisms, because we are able to predict the order of the reaction with respect to different reactants for different possible mechanisms. However, this analysis also shows that we could not distinguish the mechanism of Eq. 7.48 from a simple elementary second order reaction of A and B, because both rate laws have a single rate constant, k or We cannot decipher whether a rate constant represents a single elementary step or a combination of several rate constants for individual elementary steps. [Pg.391]

Figure 19 Compression characteristics of recipe I. The second v-axis shows the influence of the nitrogen pressure on the porosity. Porosity was calculated by the quotient of upward pressure of the coated granules in silicon oil as a measure of the apparent density and the true density. The three different charts display the compression characteristics for three compression forces (5-15 kN). Figure 19 Compression characteristics of recipe I. The second v-axis shows the influence of the nitrogen pressure on the porosity. Porosity was calculated by the quotient of upward pressure of the coated granules in silicon oil as a measure of the apparent density and the true density. The three different charts display the compression characteristics for three compression forces (5-15 kN).
K2)jK2 is greater or lesser than the value AHyAHl, then the degree of conversion will rise or decrease with the rising temperature, respectively. When, in a point To the value of (1 + 2)/ 2 is equal to the quotient of heats of reaction, the degree of conversion will achieve an extreme value at this temperature (we assume that the second derivation differs from zero). [Pg.76]


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See also in sourсe #XX -- [ Pg.194 ]




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