Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Rate equations estimation, 85,86 relaxation

Experimentally the single relaxation observed was attributed to step 3 in the mechanism because (a) theoretical calculation of k 2 and k2 predicted an estimated relaxation frequency inaccessible to the equipment used and (b) step 2 is excluded since the rate of displacement of water from the primary hydration sphere of an anion is independent of the cation. The relaxation data were analyzed by the equation... [Pg.509]

Equation (4-14) shows that the relaxation is first-order according to Eq. (4-15), measurements of t at several values of reactant concentrations allow the rate constants to be estimated. [Pg.139]

The simulations can be made to reproduce the initial ratio of fits in Equation 9.27 using the measured 7j (ps) and fitting the distance r (nm), which is the only adjustable parameter. For canthaxan-thin and BI the experimental fits and the integrated values showed the best match in a very narrow temperature range ( 10 K) in the vicinity of the maximum enhancement in the relaxation rate. The distances obtained from the curve fits were similar to those determined from l/rM - 1/7 M0 difference, namely, 13.0 2.0 A for canthaxanthin and 10.0 2.0 A for BI. It was found for canthaxanthin, which shows no prominent peak in the relaxation rate, that the distance does not depend on l/rM -l/rM0. Using the ratio of curve fits, we can estimate the value of r for canthaxanthin as 9. 0+3.0 A in TiMCM-41 in the temperature range of 110-130K. [Pg.184]

Using the case of S = 5/2 as an illustrative example, he demonstrated that it was possible to derive closed-form analytical expressions for the PRE of the form of the SBM equations times (1 + correction term). For typical parameter values, the effect of the correction term was to increase the prediction of the SBM theory by 5-7%. A similar approach was also applied to the S = 7/2 system, such as Gd(III) (101), where the correction terms could be larger. For that case, the estimations of the electron spin relaxations rates, obtained in the solution for PRE, were also used for simulations of ESR lineshapes. [Pg.74]

The rate of a nonradiative relaxation such as the km process of equation (7) can be estimated from t° values measured at a sufficiently low temperature such that ka and kbisc are likely to be unimportant because of their higher activation energy. Under such a condition, 1/t° = (kr + knT), and kT can be estimated from the low temperature limit to t°, or from equation (25). For coordination compounds, knT is usually not very temperature dependent, act typically being 8-12 kJ mol-1. [Pg.396]

Petrie and Ito (84) used numerical methods to analyze the dynamic deformation of axisymmetric cylindrical HDPE parisons and estimate final thickness. One of the early and important contributions to parison inflation simulation came from DeLorenzi et al. (85-89), who studied thermoforming and isothermal and nonisothermal parison inflation with both two- and three-dimensional formulation, using FEM with a hyperelastic, solidlike constitutive model. Hyperelastic constitutive models (i.e., models that account for the strains that go beyond the linear elastic into the nonlinear elastic region) were also used, among others, by Charrier (90) and by Marckmann et al. (91), who developed a three-dimensional dynamic FEM procedure using a nonlinear hyperelastic Mooney-Rivlin membrane, and who also used a viscoelastic model (92). However, as was pointed out by Laroche et al. (93), hyperelastic constitutive equations do not allow for time dependence and strain-rate dependence. Thus, their assumption of quasi-static equilibrium during parison inflation, and overpredicts stresses because they cannot account for stress relaxation furthermore, the solutions are prone to numerical instabilities. Hyperelastic models like viscoplastic models do allow for strain hardening, however, which is a very important element of the actual inflation process. [Pg.854]

In Fig. 15.27, the transient extensional viscosity of a low-density polyethylene, measured at 150 °C for various extensional rates of strain, is plotted against time (Munstedt and Laun, 1979). Qualitatively this figure resembles the results of the Lodge model for a Maxwell model in Fig. 15.26. For small extensional rates of strain (qe < 0.001 s ) 77+(f) is almost three times rj+ t). For qe > 0. 01 s 1 r/+ (f) increases fast, but not to infinite values, as is the case in the Lodge model. The drawn line was estimated by substitution of a spectrum of relaxation times of the polymer (calculated from the dynamic shear moduli, G and G") in Lodge s constitutive equation. The resulting viscosities are shown in Fig. 15.28 after a constant value at small extensional rates of strain the viscosity increases to a maximum value, followed by a decrease to values below the zero extension viscosity. [Pg.570]

The observed relaxation time is time-averaged value of s e and Sj. The fraction of Na ion under the slow-motion condition is expected small, but the transverse relaxation rate constants (s ) are expected larger than Sfr j by 10 to 100 times. Therefore, we applied this equation to the observed relaxation rate constants to estimate the 2 compartments. One problem is accurate knowledge of the value of s for 23Na+ in the agar gel. [Pg.435]

Values of the coefficients for the set of differential equations were chosen to give cool flames at realistic initial pressures and temperatures. Further restrictions on the choice of coefficients were imposed by requiring that the fuel conversion should not exceed 25 % at the maximum of the temperature pulse, that the induction period should be between 15 and 20 sec, and that the thermal relaxation time should be 0,25 sec. To achieve this the rate coefficients of reactions (d), (f), (h) and (g) were varied about reasonable estimates of their likely values. The parameters chosen for the model are given in Table 24. The computer was used in a conversational mode to map out an ignition diagram (Fig. 26) which compares favourably with that found experimentally [191] (Fig. 27). [Pg.347]

Relaxation of dilute spedes (star or linear) in monodisperse matrices (star or linear) can also be worked out with Eq. 98, using F(t) appropriate to the dilute spedes and R(t) for the matrix. Preluninary results indicate that long-arm molecule relaxations can be controUed over wide ranges by the choice of chain length for a linear polymer matrix. On the other hand, relaxations of linear chains in a star matrix should be less affected by matrix chain structure. Their behavior should move from the homologous linear melt behavior when in the matrix is of the order of ra for the linear chains to behavior as unattached linear chains in a network when r , > ra. The latter prediction seems inconsistent with recent experimental lesults where linear chain relaxation rates were found to be the same in the homologous melt and in a star matrix with > Ta. This may indicate some fundamental problem with the equation suggeted to estimate (Eq. 85). [Pg.103]


See other pages where Rate equations estimation, 85,86 relaxation is mentioned: [Pg.214]    [Pg.182]    [Pg.108]    [Pg.237]    [Pg.293]    [Pg.131]    [Pg.158]    [Pg.516]    [Pg.497]    [Pg.109]    [Pg.79]    [Pg.242]    [Pg.65]    [Pg.254]    [Pg.200]    [Pg.112]    [Pg.118]    [Pg.851]    [Pg.170]    [Pg.97]    [Pg.59]    [Pg.291]    [Pg.211]    [Pg.222]    [Pg.4]    [Pg.360]    [Pg.72]    [Pg.171]    [Pg.75]    [Pg.538]    [Pg.165]    [Pg.29]    [Pg.406]    [Pg.867]    [Pg.867]    [Pg.85]    [Pg.170]    [Pg.192]    [Pg.186]   


SEARCH



Relaxation equation

Relaxation rates

© 2024 chempedia.info