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Optimum parameters

The most reliable estimates of the parameters are obtained from multiple measurements, usually a series of vapor-liquid equilibrium data (T, P, x and y). Because the number of data points exceeds the number of parameters to be estimated, the equilibrium equations are not exactly satisfied for all experimental measurements. Exact agreement between the model and experiment is not achieved due to random and systematic errors in the data and due to inadequacies of the model. The optimum parameters should, therefore, be found by satisfaction of some selected statistical criterion, as discussed in Chapter 6. However, regardless of statistical sophistication, there is no substitute for reliable experimental data. [Pg.44]

As indicated in Chapter 6, and discussed in detail by Anderson et al. (1978), optimum parameters, based on the maximum-likelihood principle, are those which minimize the objective function... [Pg.67]

The optimum parameters for furfural-benzene are chosen in the region of the overlapping 39% confidence ellipses. The ternary tie-line data were then refit with the optimum furfural-benzene parameters final values of binary parameters were thus obtained for benzene-cyclohexane and for benzene-2,2,4-trimethyl-pentane. Table 4 gives all optimum binary parameters for this quarternary system. [Pg.75]

Fig. 5.17. Time domain CARS of nitrogen under normal conditions. Points designate experimental data, solid line calculation with a = 6.0 A, b = 0.024, c = 0.0015. The insert depicts the dependences of the relative mean-square deviation on each of the parameters , b and c, the other two being fixed at their optimum values. The deviations are expressed as percentage of optimum parameters. Fig. 5.17. Time domain CARS of nitrogen under normal conditions. Points designate experimental data, solid line calculation with a = 6.0 A, b = 0.024, c = 0.0015. The insert depicts the dependences of the relative mean-square deviation on each of the parameters , b and c, the other two being fixed at their optimum values. The deviations are expressed as percentage of optimum parameters.
If we have very little information about the parameters, direct search methods, like the LJ optimization technique presented in Chapter 5, present an excellent way to generate very good initial estimates for the Gauss-Newton method. Actually, for algebraic equation models, direct search methods can be used to determine the optimum parameter estimates quite efficiently. However, if estimates of the uncertainty in the parameters are required, use of the Gauss-Newton method is strongly recommended, even if it is only for a couple of iterations. [Pg.139]

If we are certain that the optimum parameter estimates lie well within the constraint boundaries, the simplest way to ensure that the parameters stay within the boundaries is through the use of the bisection rule. Namely, during each iteration of the Gauss-Newton method, if anyone of the new parameter estimates lie beyond its boundaries, then vector Ak +I) is halved, until all the parameter constraints are satisfied. Once the constraints are satisfied, we proceed with the determination of the step-size that will yield a reduction in the objective function as already discussed in Chapters 4 and 6. [Pg.165]

In the first step, the adsorption isotherms of the compounds should be determined under non-linear chromatographic conditions, which can be done in several ways [11]. Afterwards, models should be implemented and used to simulate the chromatographic behavior and to find the optimum system parameters for a given separation problem. Different approaches for finding the optimum parameter are described in the literature [12-16] mainly for adsorption and ion exchange chromatography. [Pg.216]

Another way to produce biphenyl derivates using flow was described by Leeke et al. [34] where they performed a Pd catalyzed Suzuki-Miyaura synthesis in the presence of a base. First experiments were carried out in toluene/methanol solvent. A reaction mixture was passed through the encapsulated Pd filled column bed length 14.5 cm (some cases 10 cm) x 25.4 mm id. 45 g of PdEnCat. Base concentration, temperature and flow rate were optimized and at optimum parameters (0.05 M base concentration, 100°C and 9.9 mL/min) the conversion was 74%. Then the reaction was performed under supercritical conditions using supercritical CO2 at high pressure and temperature. After optimizing the concentration of base, flow rate, pressure and temperature, the highest conversion rate (81%) was observed at 166 bar and 100°C where the reactant mixture was monophasic in the supercritical state. This system is able to produce 0.06 g/min of the desired product. [Pg.409]

The influence of atmospheric air on the properties of mineral materials manufactured in thermal processes is generally known. An example of the nature of this phenomenon as regards hardness, is a series of Vickers hardness tests of a material made of sintered corundum modified with 0.6% MgO sintered at 1950-2050 K in various environments. The sintering process is accelerated in the presence of hydrogen and is slowest in air thus allowing a material with optimum parameters to be obtained at a significantly lower temperature. The results, specified in Table 6.2.4, show the gases used as... [Pg.116]

Theory of Programmed Temperature Gas Chromatography The Prediction of Optimum Parameters, J. C. Giddings, in Gas Chromatography, Academic Press, New York, 1962, Chapter V. [Pg.301]

Figures 6 and 7 present a comparison for six PS chains of various molecular weights (from 2.63X 104 to 3.75 X 105). For the PS-X (140 K)-toluene system which was selected to determine the optimum parameters in the models of Milner et al. and de Gennes, the present calculations and... Figures 6 and 7 present a comparison for six PS chains of various molecular weights (from 2.63X 104 to 3.75 X 105). For the PS-X (140 K)-toluene system which was selected to determine the optimum parameters in the models of Milner et al. and de Gennes, the present calculations and...
Based on the analysis of the optimum parameters for MR1 for large n-alkanes from n-Ci4H3o to n-C44Hgo, a linear function of... [Pg.238]

The relationship between the response and the variables is visualized by a response siuface or contour plot to see the relative influence of the parameters, to find an optimum parameter combination, and to predict experimental results for other parameter, for two variables, When k = 2 the empirical model from the general Eq. (2) becomes... [Pg.137]

Fig, 7 95% confidence region of transport parameters and qt for G43A catalyst, optimum parameter pair is shown as point... [Pg.482]

Determining the optimum parameters was a long process which required many hours of engineering and technician time and spanned a time period of over one year. In addition to these initial multivariant experiments, a large number of independent experiments were conducted to verify the predicted results. [Pg.206]


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See also in sourсe #XX -- [ Pg.101 , Pg.103 ]

See also in sourсe #XX -- [ Pg.51 ]




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