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Generalized Models

The considered constitutive laws for elastoplastic models generalize ones used in elasticity. The main peculiarity of elastoplastic models consists in an existence of inequality type restrictions imposed upon the stresses. Omitting the mentioned restrictions, elastoplastic models turn into elastic ones. [Pg.5]

The next part of the procedure involves risk assessment. This includes a deterrnination of the accident probabiUty and the consequence of the accident and is done for each of the scenarios identified in the previous step. The probabiUty is deterrnined using a number of statistical models generally used to represent failures. The consequence is deterrnined using mostiy fundamentally based models, called source models, to describe how material is ejected from process equipment. These source models are coupled with a suitable dispersion model and/or an explosion model to estimate the area affected and predict the damage. The consequence is thus determined. [Pg.469]

The urban RAM model was evaluated (52) using 1976 sulfur dioxide data from 13 monitoring locations in St. Louis on the basis of their second-highest once-a-year concentrations. The ratio of estimated to measured 3-h average concentrations was from 0.28 to 2.07, with a median of 0.74. Half of the values were between 0.61 and 1.11. For the 24-h average concentrations the ratios ranged from 0.18 to 2.31, with a median of 0.70. Half of the values were between 0.66 and 1.21. Thus, the urban RAM model generally underestimates concentrations by about 25%. [Pg.336]

Blast effects can be represented by a number of blast models. Generally, blast effects from vapor cloud explosions are directional. Such effects, however, cannot be modeled without conducting detailed numerical simulations of phenomena. If simplifying assumptions are made, that is, the idealized, symmetrical representation of blast effects, the computational burden is eased. An idealized gas-explosion blast model was generated by computation results are represented in Figure 4.24. Steady flame-speed gas explosions were numerically simulated with the BLAST-code (Van den Berg 1980), and their blast effects were calculated. [Pg.129]

Engineering models of tractive effort calculation derive from a basic model, generally called the Davis formula (after its initial formulator, W. J. Davis). The Davis formula calculates the resistance (Rt, in pounds per ton of weight being pulled) as ... [Pg.971]

Tire simplest model for describing binary copolyinerization of two monomers, Ma and Mr, is the terminal model. The model has been applied to a vast number of systems and, in most cases, appears to give an adequate description of the overall copolymer composition at least for low conversions. The limitations of the terminal model generally only become obvious when attempting to describe the monomer sequence distribution or the polymerization kinetics. Even though the terminal model does not always provide an accurate description of the copolymerization process, it remains useful for making qualitative predictions, as a starting point for parameter estimation and it is simple to apply. [Pg.337]

Values of 0 required to fit the rate of copolymerization by the chemical control model were typically in the range 5-50 though values <1 are also known. In the case of S-MMA copolymerization, the model requires 0 to be in the range 5-14 depending on the monomer feed ratio. This "chemical control" model generally fell from favor wfith the recognition that chain diffusion should be the rate determining step in termination. [Pg.368]

The distinctive properties of densely tethered chains were first noted by Alexander [7] in 1977. His theoretical analysis concerned the end-adsorption of terminally functionalized polymers on a flat surface. Further elaboration by de Gennes [8] and by Cantor [9] stressed the utility of tethered chains to the description of self-assembled block copolymers. The next important step was taken by Daoud and Cotton [10] in 1982 in a model for star polymers. This model generalizes the... [Pg.33]

Gel filtration chromatography has been extensively used to determine pore-size distributions of polymeric gels (in particle form). These models generally do not consider details of the shape of the pores, but rather they may consider a distribution of effective average pore sizes. Rodbard [326,327] reviews the various models for pore-size distributions. These include the uniform-pore models of Porath, Squire, and Ostrowski discussed earlier, the Gaussian pore distribution and its approximation developed by Ackers and Henn [3,155,156], the log-normal distribution, and the logistic distribution. [Pg.549]

Miniaturization and parallelization key approaches for drug development apparatus for combinatorial chemistry UHTS 1536 titer-plate format modular construction of apparatus applications of UHTS fine-chemical synthesis by micro reactors numbering-up nature as model general advantages of micro flow vision of plants-on-a-desk [233]. [Pg.90]

Permeability-pH profiles, log Pe - pH curves in arhficial membrane models (log Pjpp - pH in cehular models), generally have sigmoidal shape, similar to that of log Dod - pH cf. Fig. 3.1). However, one feature is unique to permeabihty profiles the upper horizontal part of the sigmoidal curves may be verhcally depressed, due to the drug transport resistance arising from the aqueous boundary layer (ABL) adjacent to the two sides of the membrane barrier. Hence, the true membrane contribution to transport may be obscured when water is the rate-limiting resistance to transport. This is especially true if sparingly soluble molecules are considered and if the solutions on either or both sides of the membrane barrier are poorly stirred (often a problem with 96-well microhter plate formats). [Pg.74]

Model components. Models generally consider 3 populations of radionuclides ... [Pg.321]

It is presumed that the effect of carcinogenic materials is to produce critical cell damage. Thus, carcinogenic health effects models generally are dose (i.e., integrated exposure) models, not exposure models. The lack of firm statistical bases often leads to the adoption of nonthreshold, linear models, even though thresholds and nonlinear effects might be expected. [Pg.71]

To address media-specific problems, single-media models for air, surface water, groundwater and soil pollution have been developed and used by different disciplines. Although these models generally provide detailed description of the pollutant distribution in space and time and incorporate mass transfer from other media as boundary conditions, they are not capable of characterizing the total environmental impact of a pollutant release. Multimedia models have been, therefore, developed to predict the concentration of chemicals in multiple environmental media simultaneously with consideration of chemical transport and transformation within and among media [1],... [Pg.48]

As the network learns, connection weights are adjusted so that the network can model general rules that underlie the data. If there are some general rules that apply to a large proportion of the patterns in the dataset, the network will repeatedly see examples of these rules and they will be the first to be learned. Subsequently, it will turn its attention to more specialized rules of which there are fewer examples in the dataset. Once it has learned these rules as well, if training is allowed to continue, the network may start to learn specific samples within the data. This is undesirable for two reasons. Firstly, since these particular patterns may never be seen when the trained network is put to use, any time spent learning them is wasted. Secondly,... [Pg.38]

The proposed model generally describes the electrochemical process, when the solid reagent and the product have precise phase borders and the electrochemical reaction taking place on the surface, which does not vary essentially with the time. [Pg.477]

Reaction paths can be traced at steady or varying temperature the latter case is known as a polythermal path. Strictly speaking, heat transfer occurs even at constant temperature, albeit commonly in small amounts, to offset reaction enthalpies. For convenience, modelers generally define polythermal paths in terms of changes in temperature rather than heat fluxes. [Pg.12]

Some examples of micellar rate enhancements of bimolecular reactions of electrophiles are shown in Table 5. Generally the surfactant was SDS with added electrophile, e.g. H30+ or a metal ion, but sulfonic acids were also used so that HaO+ was the counterion and there was no interionic competition. The maximum rate enhancements, knl, depend upon the specific conditions of the experiment, and, as predicted by the pseudophase ion-exchange model, generally decrease with increasing concentration of the electrophilic ion. In some cases the reactions were too fast for measurement... [Pg.234]

A preliminary structural model of a protein is arrived at using one of the methods described above. Calculated structure factors based on the model generally are in poor agreement with the observed structure factors. The agreement is represented by an R-factor defined as found in equation 3.9 where k is a scale factor ... [Pg.82]

Atmospheric Dispersion Models Atmospheric dispersion models generally fall into the categories discussed below. Regardless of the modeling approach, models should be verified that the appropriate physical phenomena are being modeled and validated by comparison with relevant data (at field and laboratory scale). The choice of modeling techniques may be influenced by the expected distance to the level of concern. [Pg.64]

An action specification generalizes all occurrences of the action in other words, it should hold tme for every snapshot pair (Figure 3.16), much as a type model generalizes all snapshots in Figure 3.11. Given a type T with operation M whose operation spec has a precondition P and postcondition Q, we interpret this operation spec as follows ... [Pg.134]

The chemical industry is the application field for the study and the development of a global value chain planning model. General characteristics of the chemical industry as application field are described in this chapter. Particularities of chemical commodities are described in more detail being relevant for the considered case. [Pg.75]

Quality, in terms of the validity of the acceleration, becomes interwoven with the validity of the model. Generally, it is not unreasonable to argue that if the data shows a good fit to the model it is valid. However, this provides absolutely no evidence that the model itself is valid, nor that the data is valid or even relevant when applied to the intended service conditions. [Pg.134]


See other pages where Generalized Models is mentioned: [Pg.337]    [Pg.512]    [Pg.515]    [Pg.381]    [Pg.11]    [Pg.720]    [Pg.2555]    [Pg.542]    [Pg.156]    [Pg.357]    [Pg.172]    [Pg.76]    [Pg.544]    [Pg.537]    [Pg.201]    [Pg.175]    [Pg.143]    [Pg.32]    [Pg.797]    [Pg.105]    [Pg.340]    [Pg.569]    [Pg.33]    [Pg.510]    [Pg.170]   
See also in sourсe #XX -- [ Pg.29 ]




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A General Theorem for Simple, Linear Reactor Models

A Generalized Model for Heterogeneous Reactions

A More General Rate Model for LTL Service

A general model of gas—solid reactions

A general model of human behaviour

A general stochastic model

A general stochastic model of surface reactions

A pseudo-Jahn-Teller system modeled through generalized spin Hamiltonian the C4H4 molecule

A simple general model

Adsorption model, generalized

Application of the Modeling and General Guidelines

Atmospheric Oceanic General Circulation Models

Atmospheric general circulation model

Atmospheric general circulation model AGCM)

Boolean network modeling generally

Calibration model general three-dimensional

Chemical model determination general regression

Chromatographic determination model, general

Combined models, mixing general

Complex Crystallization Conditions General Models

Computable general equilibrium model

Computable general equilibrium model PACE

Configuration mixing model: a general

Configuration mixing model: a general approach to organic reactivity

Convected Maxwell model generalized

Creep and the Retardation Spectra Generalized Kelvin-Voigt Model

Development of a Generalized Kinetic Model for One-Substrate Reactions Under Inhibition

Examples for General and Local ADME Models

Extended (lattice) generalized Jahn-Teller model

Flory-Huggins model generalized

Fundamental model equations general formulation

General - the Smoluchowski model

General Acid-Base Catalysis in Model Systems

General Aspects of the Modelling Approach

General Assumptions and Attributes of Three Models

General Closed Solution by Combined Model (Approximation)

General Collision Models

General Description of the Model Systems

General Design of Chronic Toxicity Studies Carcinogenesis as a Model

General Features of the Model

General Framework of Performance Modeling

General Goal Programming Model

General Inflammation Models

General Model Characteristics

General Model Fitting

General Model for a Single Vessel

General Model of Nonequilibrium Photodetectors with Auger Suppression

General Model with Interfacial and Intraparticle Gradients

General Modelling Procedure

General Molecular Modeling

General Observations on Forming the Model

General Performance Overview of Basic NDDO Models

General Process Modeling and Simulation (gPROMs)

General Rate-Based Model

General Remarks on Renormalized Rouse Models

General Rheological model modified

General Risk Pooling Model

General Rouse model

General Statistical Model

General Strategy for Modeling Two-Phase Phenomena

General Structure of the Model

General Structured Model

General additive modeling

General algebraic modeling system

General arrangement drawings and models

General aspects of modelling

General circulation model, GCM

General circulation models

General circulation models carbon cycle

General concepts for the development of a model

General dispersion model

General impedance models for distributed electrode processes

General input data for the MOREHyS model

General joint model

General kinetic model

General kinetic model and prediction of critical effects

General linear model

General linear model approach

General methodology for multiscale analysis, modeling, and optimization

General micromixing model

General model control

General model space

General models for adsorption kinetics and relaxations of surfactants

General nonlinear models

General purpose molecular modeling

General random flight models

General rate model

General rate model numerical solution

General rate model with pore diffusion

General renewal models

General viscous model

General-equilibrium model

Generalities on Modeling Problems Involving Multiple Scales

Generalization model

Generalization model

Generalization of the macro monetary model

Generalization of the model

Generalization to ODE Models with Nonlinear Dependence on the Parameters

Generalization to any mixture model of water

Generalized Bom model

Generalized Born method/electrostatic model

Generalized Born model

Generalized Born solvation model

Generalized Born/Surface Area Model

Generalized Collins-Kimball model

Generalized Gaussian model

Generalized Ising model

Generalized Kirkwood model

Generalized Kolmogorov Model

Generalized Maxwell and Kelvin Models

Generalized Maxwell-Stefan Model (GMS)

Generalized Mulliken-Hush model

Generalized Newtonian constitutive models

Generalized Rouse model

Generalized Shell Model and Phonon Dispersions

Generalized additive model

Generalized additive model procedure

Generalized additive modeling ,

Generalized conductor-like screening model

Generalized conductor-like screening model GCOSMO)

Generalized covariance models

Generalized covariance models estimation

Generalized curve-crossing model

Generalized electronic polaron model

Generalized hidden Markov model

Generalized linear Maxwell model

Generalized linear model

Generalized linear viscoelastic model

Generalized local Darcys model of Teorells oscillations (PDEs)

Generalized logistic model

Generalized mass action model

Generalized microkinetic model

Generalized multicompartment models

Generalized newtonian models

Generalized nonlinear models

Generalized susceptibility models

Generalized tiling model

Generalized tiling model models

Generalized tiling model properties

Generalized valence bond model

Herschel-Bulkley general model

Individual-based models general problems

Kelvin model generalized

Kelvin-Voigt generalized model

Linear Isotherm Systems—Solution to the General Model

Linear mixed effects model general

Major Conclusions and General Guidelines for Applying the Modeling

Mathematical modeling general considerations

Mathematical models general problems

Maxwell generalized model

Mechanical models generalized Kelvin

Mechanical models generalized Maxwell

Mode Analysis and Generalized Rouse Model

Model general

Model generalized pseudopotential theory

Modeling of Processes in Microreactors Based on General Balance Equation

Modelling general

Models general classifications

Molecular modelling general methods

Monte Carlo simulations generalized tiling model

More General Models of Freight Rates

Nonspherical Disturbances - The Generalized Regression Model

Observations on Some General Aspects of Modelling Methodology

Ocean general circulation models

On more general copolymer models and the Brownian scaling

Ordering models general principles

Overview of Distance Geometry as a General Model Builder

Perimeter model generalization

Perturbation theory, general methods for two-group model

Pharmacokinetic models general

Quantum optics generalized model

Reaction general model

Reactivity, organic, a general approach to: the configuration mixing model

Reactor Models General Considerations

Regular solution model general

Relaxation time generalized Maxwell model

Retention mechanisms general model

Rheological models general

Risk assessment general model

Schrodinger equation generalized model

Sequential interaction model generalized

Signal transduction mechanisms model generality

Simplification of the Generalized Mass Transfer Equation for a One-Dimensional Plug Flow Model

Sorption in membranes generalized model

The General Linear Mixed Effects Model

The General Model Framework

The General Rate Model of Chromatography

The General Three-Dimensional Calibration Model

The Mixture-Model (MM) Approach General Considerations

The Valence Bond State Correlation Diagram Model and Its General Outlook on Reactivity

The general box model with forcing terms

The general model

Transformational model general separation structure

Unit models general

Viscoelastic model, general

Viscoelasticity general models

Wigner function generalized model

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