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Simplex process

We note that the simplex process is currently used to solve linear programs far more frequently than any other method. Briefly, this method of solution begins by choosing basis vectors in m-dimensions where m is the number of inequalities. (The latter are reduced to equalities by introducing slack variables.) For brevity we omit discussion of the case where it is not possible to form such a basis. The components of each vector comprise the coefficients of one of the variables, the first component being the coefficient of the variable in the first inequality, the second component is the coefficient of the same... [Pg.292]

This problem can readily be solved geometrically. However, we present it as an exercise and obtain the solution by the simplex process, using the maximization version. The process applies to large-scale problems, to which some of the most modem computers are applied. [Pg.294]

This problem can be cast in linear programming form in which the coefficients are functions of time. In fact, many linear programming problems occurring in applications may be cast in this parametric form. For example, in the petroleum industry it has been found useful to parameterize the outputs as functions of time. In Leontieff models, this dependence of the coefficients on time is an essential part of the problem. Of special interest is the general case where the inputs, the outputs, and the costs all vary with time. When the variation of the coefficients with time is known, it is then desirable to obtain the solution as a function of time, avoiding repetitions for specific values. Here, we give by means of an example, a method of evaluating the extreme value of the parameterized problem based on the simplex process. We show how to set up a correspondence between intervals of parameter values and solutions. In that case the solution, which is a function of time, would apply to the values of the parameter in an interval. For each value in an interval, the solution vector and the extreme value may be evaluated as functions of the parameter. [Pg.298]

We add a non-negative slack variable x2 to the first of these inequalities and subtract a non-negative slack variable xt from the second, thus obtaining equations. We then set up the matrix of coefficients and proceed to solve the problem by the simplex process to show clearly the operations involved. We have ... [Pg.298]

Now x°(t) as given by the simplex process is extended to include the slack variables. These are of course ignored in the final answer. The correspondence for our example is as follows with aP given in the extended form. [Pg.301]

Automatic optimization requires an efficient computer system to establish whether one separation is better than another. A so-called resolution function , for which various dihnitions have been proposed, is used as an objective criterion, covering resolution between neighbouring peaks and the analysis time involved. Identihcation by the computer of individual peaks, whether by the injection of standards or by spectroscopic means, is a distinct advantage. The simplex process may be used to optimize automatically the separation of complex acid-base mixtures by simultaneous variation of pH, ion pair reagent concentration, composition of ternary mobile phase, flow rate and temperature. Some automatic optimization systems are available commercially and, although they do leave some room for improvement, there is no doubt that they provide satisfactory answers to a great many problems. [Pg.280]

Fig. 2.6. Illustration of the sequential simplex process of compound selection (after Darvas 1974, copyright (1974) American Chemical Society). Fig. 2.6. Illustration of the sequential simplex process of compound selection (after Darvas 1974, copyright (1974) American Chemical Society).
The molten ferroalloy is regularly tapped by tilting the arc furnace and pouring it into ladles while the silicate slag is also tapped but on the other side and disposed of in landfill. The sili-cothermic process yields a low-carbon ferrochrome or LC ferrochrome (0.05 to 0.50 wt.% C) but with a silicon content of 8 to 12 wt.% Si. Further purification of ferrochrome can be performed by the Simplex process, which consists in reacting, in the solid state, high-carbon with oxidized ferrochromium to produce the extra-low-carbon grade (0.01 wt% C). [Pg.370]

In multiple determinations, the median is calculated for each calibration point (Fig. 12). The margins of error correspond to simple standard deviations. The medians, or the singly determined values, are fitted to a four-parameter function by a simplex process each curve has seven calibration points. The zero value is not included in the mathematical evaluation, but is used only for control purposes ... [Pg.168]

The method considers only two factors, only three initial experiments are required to perform the simplex process and obtain the maximum A/ /. ,i , which can be selected from the nine preliminary experiments. [Pg.85]

Finally, in a recent paper Maru and coworkers [9] reported on the reaction between chromiun oxide and chromium carbide, which forms the basis of the Simplex process [14]. [Pg.181]

Multichannel time-resolved spectral data are best analysed in a global fashion using nonlinear least squares algoritlims, e.g., a simplex search, to fit multiple first order processes to all wavelengtli data simultaneously. The goal in tliis case is to find tire time-dependent spectral contributions of all reactant, intennediate and final product species present. In matrix fonn tliis is A(X, t) = BC, where A is tire data matrix, rows indexed by wavelengtli and columns by time, B contains spectra as columns and C contains time-dependent concentrations of all species arranged in rows. [Pg.2967]

There are two basic types of unconstrained optimization algorithms (I) those reqmring function derivatives and (2) those that do not. The nonderivative methods are of interest in optimization applications because these methods can be readily adapted to the case in which experiments are carried out directly on the process. In such cases, an ac tual process measurement (such as yield) can be the objec tive function, and no mathematical model for the process is required. Methods that do not reqmre derivatives are called direc t methods and include sequential simplex (Nelder-Meade) and Powell s method. The sequential simplex method is quite satisfac tory for optimization with two or three independent variables, is simple to understand, and is fairly easy to execute. Powell s method is more efficient than the simplex method and is based on the concept of conjugate search directions. [Pg.744]

Shannon, C. E., 190,195,219,220,242 Shapley, L. S316 Skirokovski, V. P., 768 Shortley, O. H., 404 Shot noise process, 169 Shubnikov, A. V., 726 Shubnikov groups, 726 Shubnikov notation for magnetic point groups, 739 Siebert, W. M., 170 Signum function, 313 Similar matrices, 68 Simon, A408 Simplex method, 292 Simulation, 317... [Pg.783]

A family of computer programs has been rritten for this procedure called MIXCO. The algorithm used for the iteration and optimization processes is the simplex routine and was adapted... [Pg.176]

The simplex approach to the optimum is also an experimental method and has been applied more widely to pharmaceutical systems. Originally proposed by Spendley et al. [9], the technique has even wider appeal in areas other than formulation and processing. A particularly good example to illustrate the principle is the application to the development of an analytical method (a continuous flow analyzer) by Deming and King [6]. [Pg.611]

The most effective spectrophotometric procedures for pKa determination are based on the processing of whole absorption curves over a broad range of wavelengths, with data collected over a suitable range of pH. Most of the approaches are based on mass balance equations incorporating absorbance data (of solutions adjusted to various pH values) as dependent variables and equilibrium constants as parameters, refined by nonlinear least-squares refinement, using Gauss-Newton, Marquardt, or Simplex procedures [120-126,226],... [Pg.31]

Carpenter, B.H., Sweeney, H.C. Process Improvement with Simplex Self Directing Evolutionary Operation, Chemical Engineering, July 5, 1965, P- D7. [Pg.414]


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See also in sourсe #XX -- [ Pg.162 ]

See also in sourсe #XX -- [ Pg.370 ]

See also in sourсe #XX -- [ Pg.181 ]




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