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Isothermal decay method

O Brien. 1235 Ohmic drop, 811, 1089, 1108 Ohmic resistance, 1175 Ohm s law, 1127. 1172 Open circuit cell, 1350 Open circuit decay method, 1412 Order of electrodic reaction, definition 1187. 1188 cathodic reaction, 1188 anodic reaction, 1188 Organic adsorption. 968. 978. 1339 additives, electrodeposition, 1339 aliphatic molecules, 978, 979 and the almost-null current test. 971 aromatic compounds, 979 charge transfer reaction, 969, 970 chemical potential, 975 as corrosion inhibitors, 968, 1192 electrode properties and, 979 electrolyte properties and, 979 forces involved in, 971, 972 977, 978 free energy, 971 functional groups in, 979 heterogeneity of the electrode, 983, 1195 hydrocarbon chains, 978, 979 hydrogen coadsorption and, 1340 hydrophilicity and, 982 importance, 968 and industrial processes, 968 irreversible. 969. 970 isotherms and, 982, 983... [Pg.45]

Choubey A., Das S., Sharma S. K. and Manam J. 2010.Calculation for the trapping parameters of K3Na(S04)2 phosphor hy isothermal luminescence decay method. Mater. Chem. Phys. 120 472-475. [Pg.189]

In order to illustrate the method, we can refer to the measurements of the isothermal decay of nonlinear d33 proportional to the square root of the SHG intensity, of DR19 in a polyimide films [71]. Polyimides are good candidates for NLO devices since they offer high thermal and good chemical stability. The second order nonlinear coefficient d33 have been fitted with a double exponential function ... [Pg.137]

With the pVT techniques based on the pressure decay method [12,13], a polymer sample is seated in a container of known volume acting as equilibrium cell the quantity of gas initially introduced in this cell is evaluated by pVT measurements in a calibrated cell from which the gas is transferred into the equilibrium cell in a series of isothermal expansions. The pressure decay in the equilibrium cell during sorption permits evaluation of the amount of gas penetrating into the polymer. The pressure decay principle allows a sensitivity of few hundredths of milligram of absorbed gas per gram of polymer [14]. [Pg.84]

Except for radioactive decays, other reaction rate coefficients depend on temperature. Hence, for nonisothermal reaction with temperature history of T(t), the reaction rate coefficient is a function of time k(T(t)) = k(t). The concentration evolution as a function of time would differ from that of isothermal reactions. For unidirectional elementary reactions, it is not difficult to find how the concentration would evolve with time as long as the temperature history and hence the function of k(t) is known. To illustrate the method of treatment, use Reaction 2A C as an example. The reaction rate law is (Equation 1-51)... [Pg.29]

Thus, for the temperature-dependent electron tunneling reactions, the mismatch of the decay curves for the samples kept at different temperatures all the time can be observed only with large observation time intervals. In contrast to this, the presence or absence of the acceleration of the reaction with the rapid increase in temperature at a certain instant t0 can be easily noticed even with a very short observation time interval. Consequently, the method based on registering the change in kinetics with a jumpwise variation in temperature, is a more sensitive test for the presence or absence of the activation energy for the electron tunneling reaction than the method based on comparing the isothermic kinetic curves. [Pg.160]

On-line isothermal chromatography is ideally suited to rapidly and continuously separate short-lived radionuclides in the form of volatile species from less volatile ones. Since volatile species rapidly emerge at the exit of the column, they can be condensed and assayed with nuclear spectroscopic methods. Less volatile species are retained much longer and the radionuclides eventually decay inside the column. [Pg.138]

The theory of simple waves applies to large-volume injections, i.e., to the profiles obtained upon injection of rectangular profiles which are so wide that the injection plateau has not been entirely eroded when the band elutes. Then, simplifications of the solution occur because there is a constant state, the concentration plateau. This solution is not valid in overloaded elution chromatography when the injection volume is sufficiently small that the injection plateau has eroded and disappeared by the time the band elutes from the column. It is important to discuss this solution, however, because it takes a finite time for the profile of even a narrow rectangular injection to decay, and the band profile during that period is given by the simple wave solution. Also, this solution is the basis for a method of determination of competitive equilibrium isotherms (Chapter 4, Section 4.2.4). [Pg.389]

Some essential discoveries concerning the organization of the adsorbed layer derive from the various spectroscopic measurements [38-46]. Here considerable experimental evidence is consistent with the postulate that ionic surfactants form localized aggregates on the solid surface. Microscopic properties like polarity and viscosity as well as aggregation number of such adsorbate microstructures for different regions in the adsorption isotherm of the sodium dedecyl sulfate/water/alumina system were determined by fluorescence decay (FDS) and electron spin resonance (ESR) spectroscopic methods. Two types of molecular probes incorporated in the solid-liquid interface under in situ equilibrium conditions... [Pg.799]

Other recent work in the field of optimization of catalytic reactors experiencing catalyst decay includes the work of Romero e/ n/. (1981 a) who carried out an analysis of the temperature-time sequence for deactivating isothermal catalyst bed. Sandana (1982) investigated the optimum temperature policy for a deactivating catalytic packed bed reactor which is operated isothermally. Promanik and Kunzru (1984) obtained the optimal policy for a consecutive reaction in a CSTR with concentration dependent catalyst deactivation. Ferraris ei al. (1984) suggested an approximate method to obtain the optimal control policy for tubular catalytic reactors with catalyst decay. [Pg.220]

Rates of this kind are of relatively little use, as it is impossible to sieve out isothermal sets of rates at constant activity. It would take many experiments at different conditions to make available a sufficient data set to allow the sieving out of isothermal data at constant activity. Such data would, however, allow us to compare sets of isothermal rates at a variety of activities and from this determine the parameters of the deactivation equation. Unfortunately, the number of experiments required for this procedure to be applied presents a serious handicap. The method cannot be made compatible with rapid data acquisition. Fortunately, there is a way out of the dilemma. It is possible to unravel decay properties by other much simpler and less laborious means. The method described below (see also Grenier, (1997)) requires as few as two experiments using the decaying catalyst. [Pg.136]

It is difficult to infer a reasonable trap parameter from isothermal photocurrent decay measurements, particularly in this case, where the traps are created at random in the material by ion irradiation. The parameters might be determined directly with sufficient knowledge of the ion beam and its effect on the irradiated material. We also assume that the solid is optically excited so that a portion of the traps above the equilibrium Fermi level contains electrons and a portion of those below the Fermi level contains holes. In the method of Simmons and Tam [182], a current is induced (/ ) in the external circuit given by... [Pg.283]

The above theory was applied for the interpretation of dynamic surface-tension data obtained with solutions of sodium dodecyl sulfate (SDS) by means of the MBP method. The empirical adsorption isotherm, Ci (F), of SDS due to Tajima [29] was used with a value m 77 of the mean aggregation number of the micelles. The best numerical fits of the data are shown in Fig. 7. Curves a and b correspond to surfactant concentrations below CMC that is the reason why the respective data are processed by means of Eqs. (41) and (42). The diffusion coefficient of the SDS monomers calculated from the curves is Dj => 5 X 10 cmVs, which is close to the value determined by other authors [135]. This value of Di has been further used to fit the data for concentrations above CMC by means of Eqs. (76)-(79) see curves c and d in Fig. 7. Thus, from the latter two curves, one determines 70 s for the rate constant of micelle decay, which in view of Eq. (69) yields kf 1400 s for the characteristic time of the fast relaxation process of micellization. [Pg.326]

Albers et al. (1975) added excess N2O to H/He mixtures which were passed through an isothermal flow reactor in the temperature range 720-1110 K. ESR and mass spectrometry methods were used to measure H, OH, and N2O. The rate constant k was inferred from the decay of H radicals. Since measurable NO concentrations were not detected in the mass spectrometer, it was concluded that reaction (1) is dominant over reaction (2). [Pg.403]


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