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Comparison to Other Models

250 °C) was adopted from Samanta et al. [4] and proportionally adjusted to match the measured ambient temperature value. In [4], the conductivity of a similar material was reported as a hnear function of temperature, while no experimental proof was given. The curve above Tj gg, in Keller et al. [1] presented a rapid decrease of [Pg.59]

In order to further validate the modeling approach, the hot disk method with transient thermal analysis was used to measure the temperature-dependent effective thermal conductivity [21]. This experimental technique is based on the concept of the transient hot strip (THS) technique, first introduced by Gustafsson [22] and currently accepted as one of the most convenient techniques for studying effective thermal conductivity [23, 24]. One advantage is that the apparatus employs a comparatively large specimen that allows analyzing the material in its proper structure rather than a small nonrepresentative coupon. [Pg.60]

The pultruded GFRP material investigated in [21] was produced by Fiberline Denmark and composed of E-glass fibers embedded in an isophthalic polyester resin (fiber weight fraction 57.6%). Two specimens were prepared as 100 mm square plates with 6 mm thickness. Only the through-thickness thermal conductivity was measured. The hot plate sensor was placed between the two plates and was then heated by an electrical current for a short period of time. The dissipated heat caused [Pg.60]

In the following text we compare and contrast the recoupled pair bond model with three models that have also been proposed to rationaHze the existence and stability [Pg.64]


CO3 species was formed and the X-ray structure solved. It is thought that the carbonate species forms on reaction with water, which was problematic in the selected strategy, as water was produced in the formation of the dialkyl carbonates. Other problems included compound solubility and the stability of the monoalkyl carbonate complex. Van Eldik and co-workers also carried out a detailed kinetic study of the hydration of carbon dioxide and the dehydration of bicarbonate both in the presence and absence of the zinc complex of 1,5,9-triazacyclododecane (12[ane]N3). The zinc hydroxo form is shown to catalyze the hydration reaction and only the aquo complex catalyzes the dehydration of bicarbonate. Kinetic data including second order rate constants were discussed in reference to other model systems and the enzyme carbonic anhy-drase.459 The zinc complex of the tetraamine 1,4,7,10-tetraazacyclododecane (cyclen) was also studied as a catalyst for these reactions in aqueous solution and comparison of activity suggests formation of a bidentate bicarbonate intermediate inhibits the catalytic activity. Van Eldik concludes that a unidentate bicarbonate intermediate is most likely to the active species in the enzyme carbonic anhydrase.460... [Pg.1185]

According to the creators, USEtox provides a parsimonious and transparent tool for human health and ecosystem characterization factor (CF) estimates. It has been carefully constructed as well as evaluated via comparison with other models and falls within the range of their results while being less complex. [Pg.101]

First, the simplest model which includes the minimum number of compartments and model parameters must be defined. For this model, the parameters are estimated from a set of measurements obtained by non-linear regression or curve-fitting (Section 13.2.8.3).The purpose of this process is to find a set of model parameters which best fits the measurements (Section 13.2.8.2). If the goodness-of-fit is acceptable (Section 13.2.8.5), the model can be evaluated by comparison with other models (Section 13.2.8.6). [Pg.345]

Physically, this closure attempts to model the effect of SGS fluctuations on the filtered reaction rate by assuming that the largest of the SGS are dynamically similar to the smallest of the resolved scales. The influence of the smallest eddies, in particular Kolmogorov eddies, on the filtered reaction rate is assumed negligible because the large viscosity in the flame tends to rapidly dissipate these scales [19]. Further discussion and assessment of this model with comparisons to other SGS combustion closures and DNS results can be found in [17]. [Pg.162]

Most of biological chemistry can be understood in terms of simple ball and stick models. The chemistry of nitric oxide and related oxides is more intimidating because its patterns of bonding depend strongly on quantum mechanics and molecular orbital theory. But the basics can be grasped by comparison to other molecules and a simple consideration of where nitrogen sits in the periodic table. [Pg.18]

Finally, some attention has been paid to the quality of the complete electrostatic potential about the molecule at the NDDO level. This topic is discussed in Chapter 9, as are additional details associated with the performance of semiempirical models in comparison to other levels of electronic structure theory for a variety of more specialized properties. [Pg.152]

Measurements of deviation of the standard adsorption entropy at graphitized carbon black have been carried out for thietane and other heterocyclic molecules. The theoretical standard entropy for the thietane molecule shows a greater deviation from the experimental value in comparison to others, which seems to indicate that for thietane a simple model of an adsorbed molecule with 2° of freedom is not accurate <1997ZP1333>. [Pg.396]

The above results are summarized in a proposed molecular structure and proposed description for the origin of thermal decomposition products. The purpose of presenting molecular structures is to summarize research results in a concise form which will allow a convenient comparison to other work. For example, the proposed structure is similar to those of Wiser (6) and of Heredy and Wender ( 7). But these structures only represent aspects of the structure which are constrained by available data, and are not unique. They may be wrong in details for which data is missing. Care should therefore be exercised in the way such models are interpreted. [Pg.68]

Satisfactory agreement with experimental data was obtained for Cu-SiC composite deposition in a channel flow. Because of the limited range of experimental data it is not clear if the model is also able to describe important features, like the peak in the particle composite content versus current density curve. In comparison to Valdes model, the particle mass transfer is poorly taken into account by using the Reynolds number. The particle-electrode interaction on the other hand is treated much more adequately by the balance between particle adsorption (Co, Sx and Dm) and particle ejection due to hydrodynamics (Gq). For example, a small value for d is obtained, indicating that, in accordance with experimental data (Section III), electro-osmotic interactions between particles and the cathode (Dm) are negligible. [Pg.520]

This combination of Equations [5] and [16] is called the Generalized Born/Surface Area model (GB/SA), and it is currently available in the Macro-ModeP computer package. The speed of the molecular mechanics calculations is not significantly decreased by comparison to the gas phase situation, making this model well suited to large systems. Moreover, the model takes account of some first-hydration-shell effects through the positive surface tension as well as the volume polarization effects. A selection of data for aqueous solution is provided later (Table 2), and the model is compared to experiment and to other models. Nonaqueous solvents have been simulated by changing the dielectric constant in the appropriate equations, 8 but to take the surface tension to be independent of solvent does not seem well justified. [Pg.17]

In the Sumi-Marcus (SM) model 13a], the perspective is changed, with a TST rate constant based on a low-frequency molecular mode (m) as the reaction coordinate, and with G dependent on a diffusive solvent coordinate X. For ease of comparison with other models, we transform X (relative to its definition in [13a]) so as to correspond to a continuous charging parameter (X = 0 for the bottom of the reactant well, and X = 1 for the bottom of the product well for the case of parabolic free energy profiles the transformation is linear the more general situation is dealt with in [98]). Also, 7.ci = A + z , and /.d = a, , where 7, , is the reorganization energy associated with the low-frequency mode m. These definitions lead to the following equation ... [Pg.103]

The preparation of a series of dipeptide-derived a-keto-amide compounds, including among others derivatives 358 and 359, with an incorporated lipoyl residue, has been described <2005BMCL5176>. These substrates, tested in an animal model, exhibit the potential to be effective for treatment of a specific form of muscular dystrophy, known as Duchenne muscular dystrophy. While the type of substituents in 358 and 359 and related compounds is of interest regarding the biological activity, the presence of a nonpolar lipophilic lipoyl group is an important advantage in comparison to other lipophilic moieties due to the increase of the permeability into the muscle cell. [Pg.942]

Our discussion of pathway design in the context of catalytic reaction mechanisms will summarize the treatment presented by Mavrovouniotis (1992) and Mavrovouniotis and Stephanopoulos (1992). The interested reader may refer to these for mathematical details, analysis of computational complexity, and comparison to other approaches in the context of model reaction systems. [Pg.151]

Thus, the surface of this amorphous carbon (which is a model of the surfaces of non-graphitized carbon blacks [23]) differs considerably from the surface of amorphous oxide and the main structural characteristics such as the C-C and 0-0 coordination numbers are also drastically different. Nevertheless, the adsorption properties of heterogeneous surfaces of various nongraphitized carbon blacks with respect to an inert adsorbate such as argon are not that drastically different and actually have many common features. We discuss these properties in the next section. Here we only use this fact to show that subtle structural differences of various models of amorphous oxide surfaces discussed above may be not that important for their adsorption properties in comparison to other factors such as indefiniteness of adsorption potential on oxide surfaces (see below). Because of its generality and in spite of its approximate character, the BS appears to be a convenient model for the computer simulation of adsorption on amorphous, and even more general (see Introduction) heterogeneous oxide surfaces. [Pg.343]

In a previous study [39] various ion models were tested and a new model was proposed, which was called the Moliere-ion potential . Due to its simplicity and good comparison with other models (including Dedkov s model for ions [43] and Moliere and Thomas-Fermi models for neutral atoms [44]) we have used this model throughout this study. [Pg.58]

Originally, the UNIFAC-FV model has been developed for solvent activities in polymers. It can be assumed that the model (Equations 16.48 through 16.50) is also valid for estimating the polymer activities. However, such an application of UNIFAC-FV is rather problematic. It has been shown that the performance of UNIFAC-FV in predicting the activities of heavy alkanes in shorter ones is not very good. Sample results are shown in Tables 16.5 and 16.6 for the activities of both the solvent and the heavy compound where comparison with other models is also provided. Such problems restrict the applicability of UNIFAC-FV to cases where only the solvent activity is needed. To our knowledge, UNIFAC-FV has not been tested for LEE in polymer solutions, where both the solvent and polymer activities are required. [Pg.707]

The scope of this chapter is, therefore, (i) to review the Bell-Limbach tunneling model in comparison with other models and its use for describing single steps of multiple hydrogen transfer networks and (ii) to review applications of this approach in a number of cases which have been studied mainly by NMR. A description of the techniques used for the determination of rate constants of Id-transfer will not be included in this chapter readers interested in this problem are referred to a recent review [4]. [Pg.138]


See other pages where Comparison to Other Models is mentioned: [Pg.114]    [Pg.64]    [Pg.65]    [Pg.46]    [Pg.59]    [Pg.114]    [Pg.64]    [Pg.65]    [Pg.46]    [Pg.59]    [Pg.109]    [Pg.1218]    [Pg.138]    [Pg.139]    [Pg.65]    [Pg.172]    [Pg.22]    [Pg.89]    [Pg.412]    [Pg.23]    [Pg.24]    [Pg.320]    [Pg.291]    [Pg.36]    [Pg.1218]    [Pg.194]    [Pg.109]    [Pg.443]    [Pg.1274]    [Pg.78]    [Pg.33]    [Pg.161]   


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