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Number of Free Variables

The performance of a given column or the equipment requirements for a given separation are established by solution of certain mathematical relations. These relations comprise, at every tray, heat and material balances, vapor-liquid equilibrium relations, and mol fraction constraints. In a later section, these equations will be stated in detail. For now, it can be said that for a separation of C components in a column of n trays, there stiU remain a number, C + 6, of variables besides those involved in the cited equations. These must be fixed in order to define the separation problem completely. Several different combinations of these C + 6 variables may be feasible, but the ones commonly fixed in column operation are the following  [Pg.395]

A common alternate specification is of the overhead and bottoms compositions expressed through distribution of the keys (two variables) as a replacement of items 4 and 7. [Pg.395]

ESTIMATION OF REFLUX AND NUMBER OF TRAYS (FENSKE-UNDERWOOD-GILLILAND METHOD) [Pg.395]


Fig. 5 A significant difference between the various approaches is only visible for Bq < 100. At higher values of Bo the number of free variables plays no noticeable role and the critical values follow a master curve. The solid lines show results including the velocity field, the dashed lines correspond to the minimal set of variables. At low Bo in the upper curves we used X = 2... Fig. 5 A significant difference between the various approaches is only visible for Bq < 100. At higher values of Bo the number of free variables plays no noticeable role and the critical values follow a master curve. The solid lines show results including the velocity field, the dashed lines correspond to the minimal set of variables. At low Bo in the upper curves we used X = 2...
Considerations 393 Sequencing of Columns 393 Number of Free Variables 3P5... [Pg.770]

If the selected space group of the starting structure has high symmetry, the number of free parameters will be smaller than the number of constraints and it is not possible for all the predicted distances to be realized. If the deviations are small, the structure may be stable, but if they are large, the structure will relax or, in extreme cases, be so unstable that it cannot be prepared. Relaxation may involve only a small adjustment to the bond lengths so that the valence sum rule continues to be obeyed (at the expense of the equal valence rule), or it may involve a reduction in the symmetry as is found in the case of CaCrF5 described above. If the symmetry is reduced, the number of free variables is increased and the atomic coordinates may be under-determined. In this case, the constraints on the sizes of non-bonding distances become important. [Pg.39]

If there are more than one independent disorders in a stmcture, one also has to use more then one additional free variable. Accordingly, the sof instructions are to be changed to 21.0000 and- 21.0000, 31.0000 and- 31.0000, 41.0000 and -41.0000, and so forth. For each disorder one uses part 1, PART 2, and PART 0. Higher part numbers are only used to formulate disorders with more than one component. The format of the. ins file limits the number of free variables to 99, which should be enough to describe even very complicated structures. [Pg.63]

A rule called the Gibbs phase rule tells us how many phases can be in coexistence for a given substance or mixture. The rule arises from the fact that, to be in coexistence, a constraint exists that the chemical potentials of each component in each phase must be equal. After some math, one can find a relationship between the number of components of a system, the number of free variables (such as temperature, pressure, or the fraction of a given component present in a mixture), and the number of phases that can be in coexistence. This relationship is ... [Pg.35]

The Dortmund Data Bank is still growing and currently contains about 4.78 million data points. Models with a high number of free variables fitted to a limited number of experimental data points, such as a kinetic model for methanol steam reforming with 13 parameters determined by 43 experiments [45], must be evaluated critically. [Pg.639]

Remember that the variance is the number of free variables in the system, among the p external intensive physical variables and the molar fractions. This number gives us the maximum number of degrees of freedom of the system that maximum number of degrees of freedoms may be reduced by the imposition of specific constraints. Gibbs phase mle applies equally to open systems and closed systems, and pertains solely to the intensive variables. [Pg.42]

Duhem s phase rule enables us to define a Duhem variance, which applies only to closed systems and pertains to the external intensive variables, the composition variables and the quantities of matter. The goal is always to determine the number of free variables. [Pg.42]


See other pages where Number of Free Variables is mentioned: [Pg.310]    [Pg.310]    [Pg.48]    [Pg.395]    [Pg.395]    [Pg.420]    [Pg.395]    [Pg.395]    [Pg.184]    [Pg.437]    [Pg.642]    [Pg.269]    [Pg.352]    [Pg.266]    [Pg.310]   


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