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Idealized models

With all QSPR studies it is not possible to separate the influence of the data used to train the model and the computational approach used to derive the model from the final model. Ideally, the QSPR should be sufficiently general to be applied to any compound that is reasonably represented by the data used to derive the model. [Pg.303]

However, any kinetics may be inserted as required. The RTD function E(t) may be known either from a flow model (ideal or nonideal) or from experimental tracer data. [Pg.501]

In this model, idealized skeletons are assumed, deformations of the skeleton by ligands being neglected. The ligands have a static or dynamic symmetry about their skeletal bond axes which is compatible with the skeletal symmetry. Here it should be noted that the conceptual dissection of molecules into skeleton and ligands has been a standard procedure developed by stereochemists quite some time ago. [Pg.13]

After examining tiie training set classes with PCA, the next step is to construct and validate the SIMCA models. Ideally, tlie SIMCA models are constructed using the training set and validated using a completely separate test set. Tliis separate test set is usually not available and therefore it is necessary to use a cross-validation scheme. There are many procedures for splitting the data set and a few are discussed below. Keep in mind that the training set must be carefully... [Pg.257]

In order for a process to be controllable by machine, it must represented by a mathematical model. Ideally, each element of a dynamic process, for example, a reflux drum or an individual tray of a fractionator, is represented by differential equations based on material and energy balances, transfer rates, stage efficiencies, phase equilibrium relations, etc., as well as the parameters of sensing devices, control valves, and control instruments. The process as a whole then is equivalent to a system of ordinary and partial differential equations involving certain independent and dependent variables. When the values of the independent variables are specified or measured, corresponding values of the others are found by computation, and the information is transmitted to the control instruments. For example, if the temperature, composition, and flow rate of the feed to a fractionator are perturbed, the computer will determine the other flows and the heat balance required to maintain constant overhead purity. Economic factors also can be incorporated in process models then the computer can be made to optimize the operation continually. [Pg.39]

Integration of a time-dependent thermal-capillary model for CZ growth (150, 152) also has illuminated the idea of dynamic stability. Derby and Brown (150) first constructed a time-dependent TCM that included the transients associated with conduction in each phase, the evolution of the crystal shape in time, and the decrease in the melt level caused by the conservation of volume. However, the model idealized radiation to be to a uniform ambient. The technique for implicit numerical integration of the transient model was built around the finite-element-Newton method used for the QSSM. Linear and nonlinear stability calculations for the solutions of the QSSM (if the batchwise transient is neglected) showed that the CZ method is dynamically stable small perturbations in the system at fixed operating parameters decayed with time, and changes in the parameters caused the process to evolve to the expected new solutions of the QSSM. The stability of the CZ process has been verified experimentally, at least... [Pg.99]

In the pseudo-phase model, ideal solutions are assumed2 so that 72 = 1 and 02 — am. (18.71)... [Pg.345]

Atomic level simulations and electronic structure calculations are necessary to understand the mechanisms and physical properties for these molecule/bulk interfacial CTs. However, unfortunately, a simple extension of standard theoretical models for homogeneous CTs is not always useful. While there are several difficulties in developing theoretical models (ideally possible to combine ah initio techniques) for interfacial CTs, the fundamental difficulties result from (i) the total system size often being (semi-) infinite (ii) the coexistence of locality and nonlocality in excited electron... [Pg.75]

It is important in any prediction to know whether the query compounds fall within the AD of the model. Ideally, the AD should cover the structural, physicochemical and response space (e.g. mode of action) of the model. The distance-to-model measure can be used as a measure for the AD (see Section III.B.4.). " ... [Pg.506]

Often the kinetics of the chemical reaction and whether or not the reaction rate is affected by transport limitation are not known a priori. Lab-scale experimental reactors are structured such that they are operated isothermally and can be described by one of three ideal reactor models (ideal batch, CSTR, and plug flow). Isothermal operation is achieved by providing a large beat-transfer surface and maintaing the reactor in a constant-temperature bath. Experiments are conducted at different initial (or inlet) reactant proportions (to determine the form of the rate expression) and at different temperatures (to determine the activation energy). [Pg.16]

We derived the species-based design equations for three ideal reactor models ideal batch reactor, plug-flow reactor, and CSTR. [Pg.126]

At this point it is appropriate to turn to the model of the AU55 cluster/ recalling the Chini magic numbers .f The number of Pd atoms found in cluster 6 matches this well, within experimental error. The number of metal atoms in the five-layer 12-vertex solid, icosahedron or cuboctahedron is 1 -I- 12-I-42-I-92-t- 162-I-252 = 561 atoms (see Schemes 1 and 2). Therefore, molecule 6 can be represented by the model (idealized) formula Pd56iphen6o(OAc)i8o (Fig. 3). [Pg.1375]

The appropriate SVD-derived spectral and temporal eigenvectors were selected and the temporal vectors were modeled. Ideally, the temporal vectors are the kinetic traces of individual components, each one being associated with a spectrum of a pure component Le., the spectral vector). Once the temporal vectors had been modeled the pure component spectra were reconstructed as a function of the pre-exponential multiplier obtained from the analysis, SVD determined spectral eigenvectors, and the corresponding eigenvalues. After the spectra of the component species were determined, the extinction profile was calculated and used along with the calculated decay times to construct a linear combination of the pure component species contributions to the observed... [Pg.201]


See other pages where Idealized models is mentioned: [Pg.287]    [Pg.333]    [Pg.953]    [Pg.13]    [Pg.13]    [Pg.464]    [Pg.23]    [Pg.3]    [Pg.18]    [Pg.93]    [Pg.69]    [Pg.103]    [Pg.198]    [Pg.1036]    [Pg.269]    [Pg.267]    [Pg.383]    [Pg.124]    [Pg.154]    [Pg.195]    [Pg.432]    [Pg.571]    [Pg.141]    [Pg.353]    [Pg.163]    [Pg.3661]    [Pg.526]    [Pg.4]    [Pg.398]    [Pg.130]    [Pg.817]    [Pg.42]   
See also in sourсe #XX -- [ Pg.85 , Pg.88 , Pg.152 ]




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Adsorption ideal Langmuir model

An Incremental Model of the Non-ideal Switch

An ideal gas model

Analytical Solutions of the Ideal Model

Applications of Ideal Reactor Models

As ideal model system

Band Profiles in Displacement Chromatography with the Ideal Model

Band Profiles of Single-Components with the Ideal Model

Band Profiles of Two Components with the Ideal Model

Choice of Idealized Reactor Model

Chromatography ideal model

Components of the Ideal GIT Model

Constructing Reference Models with Idealized Symmetry

Crystallization ideal stirred tank model

Debye Models, Three Ideal Components

Definition of the ideal solution model

Equilibrium ideal Langmuir model

Equilibrium model, ideal

Ideal Langmuir Model

Ideal Mixing Model Comparison with the Yalkowsky and Bolton Approach

Ideal Model Summary

Ideal adsorbed layer model

Ideal adsorbed phase model

Ideal analytical model, deviations

Ideal crystal models

Ideal cylinder models

Ideal gas model

Ideal kinetic model

Ideal kinetic model equilibrium approximations

Ideal kinetic model interpretations

Ideal kinetic model mathematical relations

Ideal kinetic model thermodynamic modeling

Ideal model

Ideal model

Ideal model of chromatography

Ideal model, nonlinear chromatography

Ideal proton transport modeling

Ideal reactor models

Ideal surface layers and model isotherms

Ideal two-dimensional models

Ideal two-phase model

Ideal-chain model

Idealized HMO (pd) Model

Idealized flow models

Idealized machine model

Idealized reactor models (

KINETICS AND IDEAL REACTOR MODELS

Kinetic Data Analysis and Evaluation of Model Parameters for Uniform (Ideal) Surfaces

Lattice model for ideal and regular solutions

Liquid lattice model ideal solution

Mass Balances According to Ideal Models

Mixing Models Reactors with Ideal Flows

Model 1 The Ideal Discontinuous Stirred Tank Reactor (DCSTR)

Model 2 The Ideal Continuous Stirred Tank Reactor (CSTR) with V Constant

Model 3 The Ideal Semicontinuous Stirred Tank Reactor (SCSTR) with V Variable

Model Solutions for the Motion of a Hypothetical Economy in Ideal Time

Model catalysts ideal crystals

Model ideal adsorbed solution

Model of non-ideal lattice gas

Models allowing for the deviations from ideality

Models ideal plug flow

Modifications of the Ideal Rubber Model

Non-ideal model

Nonlinear, Ideal Model of SMB

Optimization ideal model

Polymer ideal chain model

Polymers, kinetic modeling from ideality

Practical Relevance of the Ideal Model

Reaction cavity idealized model

Reactor models ideal batch

Solution models ideal

Solution phase models ideal solutions

Sphere Sources, Ideal Three-Dimensional Models

TUBEMIX - Non-Ideal Tube-Tank Mixing Model

The Fixed Junction Model of Ideal Rubbers

The Ideal Gas Model

The Ideal Model in Gas Chromatography

The Ideal in vitro Artificial Membrane Permeability Model

The ideal solution model

Thermodynamic model ideal solution

Vibrational idealized models

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