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Slope balance

Because a material balance on water must be satisfied during the drydown as well as afterward, the path from the initial concentration to equihbrium can be represented graphically by a material balance line and an equihbrium curve. The coordinates of the starting point on the material balance line are the initial water contents of the fluid to be dried and the desiccant. The slope of the line is the ratio of fluid mass to desiccant mass. The line terminates at its intersection with the equihbrium curve (Eig. 4). [Pg.509]

In case A the solvents are immiscible, so the rate of feed solvent alone in the feed stream F is the same as the rate of feed solvent alone in the raffinate stream R. In like manner, the rate of extraction solvent alone is the same in the stream entering S as in the extract stream leaving E (Fig. 15-12). The ratio of extraction-solvent to feed-solvent flow rates is therefore S /F = E /R. A material balance can be written around the feed end of the extrac tor down to any stage n (see Fig. 15-12) and then rearranged to a McCabe-Thiele type of operating line with a slope of F /S [Eq. (15-11)]. [Pg.1461]

Operating lines can be found in the ual way from material balances. The slope of each such line is AC/AC = L/U, where L is the downflow rate in the particular column section and C is now the concentration in the descending stream. [Pg.2019]

Figure 1.9 The balance of endothermic surface energy and the exothermic formation of the stable condensed phase during nucleation from the vapour phase. The critical radius, above which the nuclei become stable, is where the resultant Gibbs energy change has zero slope... Figure 1.9 The balance of endothermic surface energy and the exothermic formation of the stable condensed phase during nucleation from the vapour phase. The critical radius, above which the nuclei become stable, is where the resultant Gibbs energy change has zero slope...
Aris and Amundson (1958) solved the coupled, time-dependent material and energy balances, linearizing the equations about the operating point by a Taylor series expansion. This made the solution possible by the method of characteristic equations. The solution yielded two equations, one the slope condition and the other recognized by Gilles and Hofmann (1961) as the condition that sets the limits to avoid rate oscillation. This is called the... [Pg.187]

This is accomplished by measuring the rate at constant temperature and at various concentrations by varying the feed rate. Calculating 0, multiplying by the measured slope at the calculated 0, and then adding one gives the derivative of the mass balance rate with regard to concentration. [Pg.191]

The initial moisture content is a determinant factor in the rate of heat transfer to the center of the core mat [226,227]. At short press closing times the rapid temperature rise occurs at the same time for both lower and higher moisture content percentages indicating that the steam condensation front reaches the core at the same rate and that this is then determined more by local permeability rather than local moisture content. The slope of the rise is similar as it is the balance of horizontal and vertical permeability which controls the rate of steam flow to the core layer. Furthermore, water remains in the surface layer in a quantity such as... [Pg.1095]

It also follows that, when three (or more) oxidation states lie approximately on a straight line in the volt-equivalent diagram, they tend to form an equilibrium mixture rather than a reaction going to completion (provided that the attainment of thermodynamic equilibrium is not hindered kinetically). This is because the slopes joining the several points are almost the same, so that E° for the various couples (and hence AG°) are the same there is consequently approximately zero change in free energy and a balanced... [Pg.436]

Vmin = Minimum fresh air flow based on slope of operating line, L/V, on x-y diagram V = Vapor flowrate, mols/hr or molar volume W = Bottoms product, or still bottoms, or ketde bottoms, mols also see B or mols/hr bottoms product or mols of residue or bottoms/unit time (Ponchon heat balance)... [Pg.106]

Once there is an appreciable amount of cells and they are growing very rapidly, the cell number exponentially increases. The optical cell density of a culture can then be easily detected that phase is known as the exponential growth phase. The rate of cell synthesis sharply increases the linear increase is shown in the semi-log graph with a constant slope representing a constant rate of cell population. At this stage carbon sources are utilised and products are formed. Finally, rapid utilisation of substrate and accumulation of products may lead to stationary phase where the cell density remains constant. In this phase, cell may start to die as the cell growth rate balances the death rate. It is well known that the biocatalytic activities of the cell may gradually decrease as they age, and finally autolysis may take place. The dead cells and cell metabolites in the fermentation broth may create... [Pg.82]

If pe lies below the pes line then only H2S is stable for pa values between the pe3 line and the p 4 line, is stable for pa lying above the pa4 line, HSOT is stable. At a pH of 1.9, the dominant S(VI) species changes to. The slope of the pa4 curve changes slightly at pH = 1.9 reflecting a change in the number of protons in the balanced reaction ... [Pg.95]

Nyhan, J.W., A seven-year water balance study of an evapotranspiration landfill cover varying in slope for semiarid regions, Vadose Zone Journal, 4, 466-480, 2005. [Pg.1089]

Solution First, the balanced composite curves must be constructed using the complete set of data from Table 17.1. Figure 17.5 shows the balanced composite curves. Note that the steam has been incorporated within the construction of the hot composite curve to maintain the monotonic nature of composite curves. The same is true of the cooling water in the cold composite curve. Figure 17.5 also shows the curves divided into enthalpy intervals where there is a change of slope either on the hot composite curve or on the cold composite curve. [Pg.390]

Figure 26.28a shows the limiting composite curve for the three operations from Table 26.5 (i.e. excluding the flowrate loss). Matched against the limiting composite curve is a water supply line that shows a change in slope where the flowrate loss occurs. The target flowrate can be determined by a mass balance below the pinch. [Pg.601]


See other pages where Slope balance is mentioned: [Pg.415]    [Pg.637]    [Pg.33]    [Pg.89]    [Pg.34]    [Pg.92]    [Pg.436]    [Pg.248]    [Pg.252]    [Pg.1141]    [Pg.1272]    [Pg.1465]    [Pg.1658]    [Pg.2028]    [Pg.79]    [Pg.175]    [Pg.177]    [Pg.415]    [Pg.1116]    [Pg.361]    [Pg.214]    [Pg.48]    [Pg.175]    [Pg.245]    [Pg.336]    [Pg.69]    [Pg.278]    [Pg.507]    [Pg.365]    [Pg.600]    [Pg.608]    [Pg.131]    [Pg.383]   
See also in sourсe #XX -- [ Pg.367 , Pg.368 , Pg.369 , Pg.370 , Pg.371 , Pg.372 , Pg.373 , Pg.394 , Pg.516 , Pg.517 , Pg.525 , Pg.529 ]

See also in sourсe #XX -- [ Pg.367 , Pg.368 , Pg.369 , Pg.370 , Pg.371 , Pg.372 , Pg.373 , Pg.394 , Pg.516 , Pg.517 , Pg.525 , Pg.529 ]




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