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Computer simulation coefficients

The themiodynamic properties calculated by different routes are different, since the MS solution is an approximation. The osmotic coefficient from the virial pressure, compressibility and energy equations are not the same. Of these, the energy equation is the most accurate by comparison with computer simulations of Card and Valleau [ ]. The osmotic coefficients from the virial and compressibility equations are... [Pg.495]

Computer simulations act as a bridge between microscopic length and time scales and tlie macroscopic world of the laboratory (see figure B3.3.1. We provide a guess at the interactions between molecules, and obtain exact predictions of bulk properties. The predictions are exact in the sense that they can be made as accurate as we like, subject to the limitations imposed by our computer budget. At the same time, the hidden detail behind bulk measurements can be revealed. Examples are the link between the diffiision coefficient and... [Pg.2239]

Otlier expressions for tire diffusion coefficient are based on tire concept of free volume [57], i.e. tire amount of volume in tire sample tliat is not occupied by tire polymer molecules. Computer simulations have also been used to quantify tire mobility of small molecules in polymers [58]. In a first approach, tire partition functions of tire ground... [Pg.2536]

Figure 3. Conversion-jacket temperature relation (computer simulation). Heat transfer coefficient 75 cal/m sec °C... Figure 3. Conversion-jacket temperature relation (computer simulation). Heat transfer coefficient 75 cal/m sec °C...
Figure 14, Molecular weight-conversion relationship (computer simulation— reactor of a fixed geometry for a given initiator system) (h) heat transfer coefficient... Figure 14, Molecular weight-conversion relationship (computer simulation— reactor of a fixed geometry for a given initiator system) (h) heat transfer coefficient...
The attractive feature of LADM Is that once the fluid structure Is known (e.g., by solution of the YBG equations given In the previous section or by a computer simulation) then theoretical or empirical formulas for the transport coefficients of homogeneous fluids can be used to predict flow and transport In Inhomogeneous fluid. For diffusion and Couette flow In planar pores LADM turns out to be a surprisingly good approximation, as will be shown In a later section. [Pg.262]

Figure 2. MSssbauer Spectrum and Corresponding Computer Simulation for Sample 2 Under Water-Gas Shift Reaction Conditions at 613 K. A) situ MSssbauer spectrum of sample 2 at 613 K B) Computer-simulated spectrum C) Distribution of particle radii D) Relative volume fractions as a function of radius (A). For the computer simulation, the following pareimeters were used 0-1.25, mean radius = 65A, k-8 x 10 ergs/cm3. The Klebsch-Gordon coefficients used were 3 3 1. Figure 2. MSssbauer Spectrum and Corresponding Computer Simulation for Sample 2 Under Water-Gas Shift Reaction Conditions at 613 K. A) situ MSssbauer spectrum of sample 2 at 613 K B) Computer-simulated spectrum C) Distribution of particle radii D) Relative volume fractions as a function of radius (A). For the computer simulation, the following pareimeters were used 0-1.25, mean radius = 65A, k-8 x 10 ergs/cm3. The Klebsch-Gordon coefficients used were 3 3 1.
So far, Santos has been able to express the relation between a set of coefficients af, aj J 6 / describing a vector field and the overall curvature of the stream lines of this vector field. Based on the curvature field, they constructed the measure E of the curvature distribution in the simulation box. Provided that the homogeneous curvature field of curvature c0 is the one that minimizes E, the problem of packing has been recast as a minimization problem. However, the lack of information about the gradient of the error function to be minimized does not facilitate the search. Fortunately, appropriate computer simulation schemes for similar minimization problems have been proposed in the literature [105-109]. [Pg.62]

MJ Pikal. Use of laboratory data in freeze drying process design Heat and mass transfer coefficients and the computer simulation of freeze drying. J Parenter Sci Tech-nol 39 115-138, 1985. [Pg.697]

Carrying out a number of co-oxidation experiments with various hydrocarbon mixtures, one compares the results of experiment with that of computer simulations and step by step estimates of the parameters rl5 r2, Sl5 S2, and (/>. This technique is an effective qualitative method for estimating these coefficients. This technique is described in monographs and papers [5-9],... [Pg.215]

Whilst this Chapter is primarily concerned with the methods of determining the free energies of tautomeric or ionisation equilibria via computer simulation of free energy differences, many of the issues raised relate also to the determination of other molecular properties upon which behaviour of the molecule within the body may depend, such as the redox potential or the partition coefficient.6 In the next section, we shall give a brief explanation of the methods used to calculate these free energy differences -namely the use of a thermodynamic cycle in conjunction with ab initio and free energy perturbation (FEP) methods. This enables an explicit representation of the solvent environment to be used. In depth descriptions of the various simulation protocols, or the accuracy limiting factors of the simulations and methods of validation, have not been included. These are... [Pg.120]

Bonifacio, R.P., Padua, A.A.H., and Costa Gomes, M.F. Perfluoroalkanes in water experimental Henry slaw coefficients for hexafluoroethane and computer simulations for tetrafluoromethane and hexafluoroethane, J. Phys. Chem. A, 105 (35) 8403-8409, 2001. [Pg.1634]

For a theta solvent (V2 = 0) the relevant interaction is described by the third virial coefficient using a simple Alexander approach similar to the one leading to Eq. 13, the brush height is predicted to vary with the grafting density as h pa in agreement with computer simulations [65]. [Pg.169]

For the first sample in the computer simulation the 99 per cent confidence interval is (78.64, 81.80). This is a wider interval than the 95 per cent interval the more confidence we require the more we have to hedge our bets. It is fairly standard to use 95 per cent confidence intervals and this links with the conventional use of 0.05 (or 5 per cent) for the cut-off for statistical significance. Under some circumstances we also use 90 per cent confidence intervals and we will mention one such situation later. In multiple testing it is also sometimes the case that we use confidence coefficients larger than 95 per cent, again we will discuss the circumstances where this might happen in a later chapter. [Pg.41]

Whereas, the theoretical values for the reflection coefficients shown in Figs. 14-16 are reasonable estimates for light ions and for heavy ions in the keV range, there is no adequate theory for ions in the eV range. There have, however, been some computer simulations which seem to correctly predict trends . Moreover, excellent experimental work has been reported by Kornelsen and co-workers for ions in this energy range. [Pg.90]

Diffusion Coefficients from Computer Simulation and Experiment. .. 131... [Pg.86]

Fig. 16a, b. Computer simulation results for rodlike polymers in solution a the translational diffusion coefficients [122,123] b the rotational diffusion coefficient [119,122,123]... [Pg.132]

In principle, the expressions for pair potentials, osmotic pressure and second virial coefficients could be used as input parameters in computer simulations. The objective of performing such simulations is to clarify physical mechanisms and to provide a deeper insight into phenomena of interest, especially under those conditions where structural or thermodynamic parameters of the studied system cannot be accessed easily by experiment. The nature of the intermolecular forces responsible for protein self-assembly and phase behaviour under variation of solution conditions, including temperature, pH and ionic strength, has been explored using this kind of modelling approach (Dickinson and Krishna, 2001 Rosch and Errington, 2007 Blanch et al., 2002). [Pg.106]

It shows the clear link between the change of motion of the particle and its diffusion coefficient. In Fig. 50, the velocity autocorrelation function of liquid argon at 90 K (calculated by computer simulation) is shown [451], The velocity becomes effectively randomised within a time less than lps. Further comments on the velocity autocorrelation functions obtained by computer simulation are reserved until the next sub-section. Because the velocity autocorrelation function of molecular liquids is small for times of a picosecond or more, the diffusion coefficient defined in the limit above is effectively established and constant. Consequently, the diffusion equation becomes a reasonable description of molecular motion over times comparable with or greater than the time over which the velocity autocorrelation function had decayed effectively to zero. Under... [Pg.321]

Expressions for the transport coefficients suitable for use in computational simulations of chemically reacting flows are usually based on the Chapman-Enskog theory. The theory has been extended to address in detail transport properties in multicomponent systems [103,178]. [Pg.515]

In computer simulations a discrete lattice of sites is considered, each site is occupied by not more than one particle. Particles A are localized in their sites for r seconds and then possess hops. Thus, the mean diffusion coefficient Da = a2/(2dr) could be introduced. We assume that particles B are immobile, Dq = 0, since it permits to reduce greatly simulation time. Moreover, for Da = Dq and d = 1,2 the kinetics turn out to be quite similar. A hop of particle A into the site occupied by particle B results in their instant recombination. [Pg.267]


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