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Outer Loop Property Models

These are rigorous, composition-dependent methods, generally based on equations of state and liquid activity coefficients (Chapter 1). The /f-values and enthalpies are ultimately functions of temperature, pressure, and composition  [Pg.457]


For each outer loop function and gradient evaluation 4 and 14 inner loop problems were solved respectively (a total of 124 inner loop problems). For the inner loop problems 12-14 iterations for Tasks 1 and 3 and 5-7 iterations for Tasks 2 and 4 were usually required. For this problem size and detail of dynamic and physical properties models the computation time of slightly over 5 hrs (using SPARC-1 Workstation) is acceptable. It is to note that the optimum number of plates and optimum recovery for Task 1 (Table 7.2) are very close to initial number of plates and recovery (Table 7.1). This is merely a coincidence. However, during function evaluation step the optimisation algorithm hit lower and upper bounds of the variables (shown in Table 7.1) a number of times. Note that the choices of variable bounds were done through physical reasoning as explained in detail in Chapter 6 and Mujtaba and Macchietto (1993). [Pg.213]

These are methods for calculating A -values and enthalpies in the inner loop. They are simple functions that use parameters derived from the rigorous property models. The parameters are updated at each outer loop iteration. [Pg.456]

Cj, dj, ej,fj, Kj, and from property values computed by the rigorous thermodynamic property model. This step marks the beginning of the outer loop. [Pg.457]


See other pages where Outer Loop Property Models is mentioned: [Pg.457]    [Pg.336]    [Pg.457]    [Pg.336]    [Pg.8]    [Pg.520]    [Pg.10]   


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