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Modeling assumption

In either case, the structure of the solvation shell has to be calculated by otiier methods supplied or introduced ad hoc by some fiirther model assumptions, while charge distributions of the solute and within solvent molecules are obtained from quantum chemistry. [Pg.839]

Plant-specific features and modeling assumptions affecting risk, and Use of IPEs for risk-based regulation. [Pg.392]

PWR iriubiliiy riiiisily driven by plant operating characteristics, IPE modeling assumptions, and assessment n liic r tciinn of... [Pg.397]

In particular we would like to treat some essential effects of fluctuations where we assume that, for example, thermal fluctuations exist and are localized in space and time. The effects on large lengths and long times are then of interest where the results are independent of local details of the model assumptions and therefore will have some universal validity. In particular, the development of a rough surface during growth from an initially smooth surface, the so-called effect of kinetic roughening, can be understood on these scales [42,44]. [Pg.861]

Although the pzc contains all the essential structural information about the metal/solution interface, this information is not immediately apparent but must be appropriately decoded. This necessitates a description of (M - A) in microscopic terms that require a minimum of model assumptions.3 Another problem is that (0M - 0s)o is not directly accessible to experimental determination. What is actually measured, usually de-... [Pg.5]

Measured in water (ISEC characterization based on the Ogston s model assumption is not generally reliable in alcohols owing to the occurrence of enthalpic interactions [151]). [Pg.221]

The impedance data have been usually interpreted in terms of the Randles-type equivalent circuit, which consists of the parallel combination of the capacitance Zq of the ITIES and the faradaic impedances of the charge transfer reactions, with the solution resistance in series [15], cf. Fig. 6. While this is a convenient model in many cases, its limitations have to be always considered. First, it is necessary to justify the validity of the basic model assumption that the charging and faradaic currents are additive. Second, the conditions have to be analyzed, under which the measured impedance of the electrochemical cell can represent the impedance of the ITIES. [Pg.431]

Sensitivity studies allow estimation of the contribution of various parameters to the total uncertainty in the result of a QRA. Such studies can identify major contributors to overall risk for a list of incidents and can identify which models, assumptions, and data are important to the final risk estimate. [Pg.38]

The Wagner-Nelson method of calculation does not require a model assumption concerning the absorption process. It does require the assumption that (a) the body behaves as a single homogeneous compartment and (b) drug elimination obeys first-order kinetics. The working equations for this calculation are developed next. [Pg.91]

A great deal can be learned about the absorption process by applying Eqs. (40) and (41) to plasma concentration versus time data. Since there is no model assumption with regard to the absorption process, the calculated values of At/Vd can often be manipulated to determine the kinetic mechanism that controls absorption. This is best illustrated by an example. [Pg.92]

Under the applied QWASI model assumptions, the QWASI results are in the range of measured data reported in literature and thus support that the strongest impact to sediment and water concentrations of DeBDE are from direct emission to water as opposed to atmospheric concentrations. This result points out the high importance of DeBDE-leaching from deposited waste material and a lower meaning of the fraction that is transferred to the atmosphere. [Pg.370]

An example rather than linking average bubble size to just or essentially the (overall) power input of a particular vessel-impeller combination, dedicated CFD (preferably DNS and LES) allows for studying ( tracking ) the response of bubble size to local and spatial variations in the turbulence levels in a stirred vessel. In this way, the validity of certain modeling assumptions may be affirmed or disproved. Particularly, effects of spatial variations in e which... [Pg.217]

From a plot of the internalisation flux against the metal concentration in the bulk solution, it is possible to obtain a value of the Michaelis-Menten constant, Am and a maximum value of the internalisation flux, /max (equation (35)). Under the assumption that kd kml for a nonlimiting diffusive flux, the apparent stability constant for the adsorption at sensitive sites, As, can be calculated from the inverse of the Michaelis-Menten constant (i.e. A 1 = As = kf /kd). The use of thermodynamic constants from flux measurements can be problematic due to both practical and theoretical (see Chapter 4) limitations, including a bias in the values due to nonequilibrium conditions, difficulties in separating bound from free solute or the use of incorrect model assumptions [187,188],... [Pg.476]

In Fig. 5.5a a simple scheme of reaction steps is proposed. Some of the assumptions of our model are summarized in Table 5.1. The short-hand representation of a surface site is a simplification that does not take into account either detailed structural aspects of the oxide surface or the oxidation state of the metal ion and its coordination number. It implies (model assumption 2 in Table 5.1) that all functional surface groups, such as those in a cross-linked polyhydroxo-oxo acid, are treated as if they were identical. [Pg.166]

However, we have to reflect on one of our model assumptions (Table 5.1). It is certainly not justified to assume a completely uniform oxide surface. The dissolution is favored at a few localized (active) sites where the reactions have lower activation energy. The overall reaction rate is the sum of the rates of the various types of sites. The reactions occurring at differently active sites are parallel reaction steps occurring at different rates (Table 5.1). In parallel reactions the fast reaction is rate determining. We can assume that the ratio (mol fraction, %a) of active sites to total (active plus less active) sites remains constant during the dissolution that is the active sites are continuously regenerated after AI(III) detachment and thus steady state conditions are maintained, i.e., a mean field rate law can generalize the dissolution rate. The reaction constant k in Eq. (5.9) includes %a, which is a function of the particular material used (see remark 4 in Table 5.1). In the activated complex theory the surface complex is the precursor of the activated complex (Fig. 5.4) and is in local equilibrium with it. The detachment corresponds to the desorption of the activated surface complex. [Pg.169]

In contrast to PCA which can be considered as a method for basis rotation, factor analysis is based on a statistical model with certain model assumptions. Like PCA, factor analysis also results in dimension reduction, but while the PCs are just derived by optimizing a statistical criterion (spread, variance), the factors are aimed at having a real meaning and an interpretation. Only a very brief introduction is given here a classical book about factor analysis in chemistry is from Malinowski (2002) many other books on factor analysis are available (Basilevsky 1994 Harman 1976 Johnson and Wichem 2002). [Pg.96]

The following criteria are usually directly applied to the calibration set to enable a fast comparison of many models as it is necessary in variable selection. The criteria characterize the fit and therefore the (usually only few) resulting models have to be tested carefully for their prediction performance for new cases. The measures are reliable only if the model assumptions are fulfilled (independent normally distributed errors). They can be used to select an appropriate model by comparing the measures for models with various values of in. [Pg.128]

The denominator n 2 is used here because two parameters are necessary for a fitted straight line, and this makes s2 an unbiased estimator for a2. The estimated residual variance is necessary for constructing confidence intervals and tests. Here the above model assumptions are required, and confidence intervals for intercept, b0, and slope, b, can be derived as follows ... [Pg.136]


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See also in sourсe #XX -- [ Pg.1054 ]




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Associated-solution model assumptions

Assumptions made in the calculation of model ages

Assumptions of model

Assumptions of the Standard Model

Assumptions on Model

Basic assumptions of the model

Black-Scholes option model assumptions

Black-Scholes option model options assumption

Born model, assumptions

Comments about Model Assumptions

Degradation modelling assumptions

Dispersion model assumptions

Distillation columns model assumptions

Equilibrium model assumptions

Evaporator model assumptions

Experimental Support of Model Assumptions

Finite element modelling assumptions

First-order absorption models assumptions

Flame model, assumptions made

General Assumptions and Attributes of Three Models

Instantaneous absorption models assumptions

Ionic model assumptions

Linear adsorption isotherm, assumption model

Logistic regression model assumptions

Microscopic Description and Model Assumptions

Misspecification and Violation of the Model Assumptions

Mixing process model assumptions

Model Assumptions for Fixed-Bed Reactor

Model Assumptions in Light of CFD and Experiment

Model assumption misspecification

Model assumptions

Model description and assumptions

Modeling Assumptions and Simplification

Modeling plasma processes assumptions

Multiple dosing models assumptions

Possible model assumptions for two-phase flow in relief systems

Separator model assumptions

Solution diffusion model assumptions

Spin-line models assumptions

Testing the Model Assumptions

The modeling assumptions

Theoretical models development basic assumptions

Tubular reactor model assumptions

Zero-order absorption models assumptions

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