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Optimization design variables

Process - spatial configuration - control structure and settings - operational parameters - disturbance scenario Continuous - optimal design variables - performance criteria - non-equilibrium thermodynamics - steady-state simulation - dynamic simulation - multiobjective optimization... [Pg.157]

Figure 8.12. Driving forces as a function of the MeOH feed flowrate. Remarks MeOH feed flowrate varies from the nominal value (168 mol xs ) to 150 mol xs the optimal design variables and sizing parameters corresponds to a /soon — /exergy design, with w =[0.3 0.7]. ... Figure 8.12. Driving forces as a function of the MeOH feed flowrate. Remarks MeOH feed flowrate varies from the nominal value (168 mol xs ) to 150 mol xs the optimal design variables and sizing parameters corresponds to a /soon — /exergy design, with w =[0.3 0.7]. ...
During the last few years process synthesis by algorithm methods have made considerable progress. The problem of chemical process synthesis can be stated as follows given a set of reactants with amounts specified, determine both the cost-optimal structure and the optimal design variables of each process unit that can produce a set of specified products. In general, the process synthesis problem can be expressed as a MINLP problem where the integer and continuous variables occur nonlinearly in the performance index. The mathematical form is ... [Pg.105]

After the optimal design variables for the extractive distillation column are determined, the total TAC can be calculated with the entrainer recovery column and the recycle stream included. Additional costs in the TAC include the annualized capital cost for the entrainer recovery column, the costs associated with the cooler from B2 on the entrainer feed, the operating costs of the steam and cooling water to operate the entrainer recovery column, and the entrainer makeup cost. As an example. Figure 10.13 shows the results of the optimization runs for Case 1 with N2 and Np2 as the design variables. The y axis is the TAC of the complete flowsheet. From the flgure, N2 should be 24 and Afe should be at Stage 9. [Pg.310]

Table 10.5 shows the optimal design variables and also the minimized TAC results for Cases 1, 2, and 3. The TAC of Case 1 is the lowest, which verifies the recommendation... [Pg.310]

Factorial design methods cannot always be applied to QSAR-type studies. For example, i may not be practically possible to make any compounds at all with certain combination of factor values (in contrast to the situation where the factojs are physical properties sucl as temperature or pH, which can be easily varied). Under these circumstances, one woul( like to know which compounds from those that are available should be chosen to give well-balanced set with a wide spread of values in the variable space. D-optimal design i one technique that can be used for such a selection. This technique chooses subsets o... [Pg.713]

Optimization. Optimi2ation of the design variables is an important yet often neglected step in the design of extractive distillation sequences. The cost of the solvent recovery (qv) step affects the optimi2ation and thus must also be included. Optimi2ation not only yields the most efficient extractive distillation design, it is also a prerequisite for vaUd comparisons with other separation sequences and methods. [Pg.187]

Extensive design and optimization studies have been carried out for this sequence (108). The principal optimization variables, ie, the design variables that have the largest impact on the economics of the process, are the redux ratio in the azeo-column the position of the tie-line for the mixture in the decanter, determined by the temperature and overall composition of the mixture in the decanter the position of the decanter composition on the decanter tie-line (see Reference 104 for a discussion of the importance of these variables) and the distillate composition from the entrainer recovery column. [Pg.196]

The varianee equation provides a valuable tool with whieh to draw sensitivity inferenees to give the eontribution of eaeh variable to the overall variability of the problem. Through its use, probabilistie methods provide a more effeetive way to determine key design parameters for an optimal solution (Comer and Kjerengtroen, 1996). From this and other information in Pareto Chart form, the designer ean quiekly foeus on the dominant variables. See Appendix XI for a worked example of sensitivity analysis in determining the varianee eontribution of eaeh of the design variables in a stress analysis problem. [Pg.152]

Catalytic crackings operations have been simulated by mathematical models, with the aid of computers. The computer programs are the end result of a very extensive research effort in pilot and bench scale units. Many sets of calculations are carried out to optimize design of new units, operation of existing plants, choice of feedstocks, and other variables subject to control. A background knowledge of the correlations used in the "black box" helps to make such studies more effective. [Pg.17]

The mathematical procedure for a single merit function optimization for many design variables involves derivatives of the merit function with respect to each of the design variables (as a generalization to multiple... [Pg.430]

For laminate optimization, which we examined in Section 7.7, we have some strong temptations. We could include many design variables. We could talk about which fibers we would deal with out of a collection of those offered by various manufacturers. In addition, we could consider which matrix materials, what percentage of fibers and matrix that we deal with, what orientation of each of the fiber directions, and the thicknesses of the various laminae. All of those various factors are potential design variables, and, in order to treat them, you must have a fairly complicated optimization scheme to be able to achieve the objective of actually tailoring a laminate for specific design requirements. [Pg.461]

Once a model has been fitted to the available data and parameter estimates have been obtained, two further possible questions that the experimenter may pose are How important is a single parameter in modifying the prediction of a model in a certain region of independent variable space, say at a certain point in time and, moreover. How important is the numerical value of a specific observation in determining the estimated value of a particular parameter Although both questions fall within the domain of sensitivity analysis, in the following we shall address the first. The second question is addressed in Section 3.6 on optimal design. [Pg.86]

An extreme case of these empirical models are black box models, predominantly polynomials, the application of which is strictly restricted to the range of operating conditions and design variables for which the models were developed. Even in this range, optimization using black box models can lead to operating conditions far from the real optimum. This is due to non-linearities of the real systems, which cannot be modelled by polynomials. Black box... [Pg.318]

Often, it is not quite feasible to control the calibration variables at will. When the process under study is complex, e.g. a sewage system, it is impossible to produce realistic samples that are representative of the process and at the same time optimally designed for calibration. Often, one may at best collect representative samples from the population of interest and measure both the dependent properties Y and the predictor variables X. In that case, both Y and X are random, and one may just as well model the concentrations X, given the observed Y. This case of natural calibration (also known as random calibration) is compatible with the linear regression model... [Pg.352]

In this case, there are n design variables, with p equality constraints and q inequality constraints. The existence of such constraints can simplify the optimization problem by reducing the size of the problem to be searched or avoiding problematic regions of the objective function. In general though, the existence of the constraints complicates the problem relative to the problem with no constraints. [Pg.42]

Continuous- Variable Optimal Design Standard integer sizes ... [Pg.429]

The estimation of operating and capital costs is an important facet of process design and optimization. In the absence of firm bids or valid historical records, you can locate charts, tables, and equations that provide cost estimates from a wide variety of sources based on given values of the design variables. [Pg.604]


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See also in sourсe #XX -- [ Pg.9 ]

See also in sourсe #XX -- [ Pg.42 ]




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Example D-optimal design for screening of variables in enamine synthesis

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