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Relation between saturation parameters

Under subsaturation conditions, variation of monomer concentration also influences other parameters such as the volume fraction of polymer in particles, rate constants and saturation of reaction media. Kinetic studies are more complicated and call for knowledge of the relations between different parameters or constants and the monomer concentration. [Pg.184]

The Kolmogorov Smirnov test Closely related to the visual approach employed in Fig. 42, the KS test evaluates the equality of two distributions. Under the assumption that a saturation parameter has no impact on stability, its distribution within the stable subset is identical (in a statistical sense) to its initial distribution. Deviations between the two distributions, such as those shown in Fig. 42, thus indicate a dependency between the parameter and dynamic stability. [Pg.226]

Particle shape is also an important parameter for the shear strength depending on the saturation of the filter cakes. For the fully dried filter cakes, shear strength is independent of the shape factor. The relation between the shear strength and the particle size and the other related parameters for the saturation region S=0% can be written as ... [Pg.322]

In phase II, liquid bridges are formed between the powder particles this results in a steep increase in power consumption. Phase II is defined by the two saturation parameters 52 and 53 which are related to the amount of moisture added to the system. Parameters 5 are determined as a function of time, 5(0, in the energy consumption versus operating time curve (Figure 146). They are associated with those points in time at which the curve for a specific particulate mass to be agglomerated changes its character as shown. From the time necessary to reach these points the amount of moisture which was added can be calculated. [Pg.191]

Criteria for the validity of the steady state assumption can be obtained operationally by consideration of how to obtain correct values for initial rates and their use in the evaluation of the Michaelis parameters. Before going into these practical considerations some reference should be made to theoretical treatments of steady state conditions (see Segel, 1975 Wong, 1975). We use the simple form, equation (3.3.19), for saturation kinetics, differentiating to obtain a relation between the change in the steady state intermediate Ce (0 and in Cs(0 with time. [Pg.84]

Soil mechanics is the application of the laws of Mechanics and Hydraulics to problems dealing with soiKref. 1). The seepage flow through the unsaturated soil is an important problem because the soil mass behavior depends on the interactions between the soil grains and pore water. The parameters for the seepage analysis require moisture retention as well as hydraulic conductivity, since hydraulic conductivity depends on water saturation which also relates to capillary suction. The moisture retention is usually described by the relation between the water saturation and capillary potential. [Pg.283]

You will recognize Equation (8.3) as Raoult s law, which you have undoubtedly seen before. It directly results from the criteria for equilibrium [Equation (8.1)] under the special circumstances described above (ideal gas, ideal solution, Lewis/Randall reference state). This equation is convenient, since the saturation pressure of species i depends only on the temperature of the system. The relation between Pf and T is commonly fit to the Antoine equation. Appendix A.l provides Antoine equation parameters for several species. [Pg.468]

Figure 35. The scaling relations (4)—(7) do not hold in the intermediate regime of the phase separation. The crossover between early and intermediate regime occurs when the order parameter saturates inside the domains (the order parameter is nonconserved). Figure 35. The scaling relations (4)—(7) do not hold in the intermediate regime of the phase separation. The crossover between early and intermediate regime occurs when the order parameter saturates inside the domains (the order parameter is nonconserved).
The assumption that AOM parameters are transferable from one system to another is one which deserves close scrutiny. For example, the negative value of for pyridine found in [Cr(py)4X2]+ depends on the assumption that the ex parameters for the halides are the same as in [Cr(NH3)4X2 ]+ (58). However, there is some reason to believe that the AOM parameters for halides may differ considerably from one compound to another in Cr(III)N4X2 chromophores, even when the equatorial ligands are closely related. Thus Barton and Slade (57) found ea for F to range between 7.2 kK and 9.0 kK, and ew between 1.7 kK and 2.5 kK, in a series of CrN4Xj systems where the equatorial ligands were saturated amines. This could account for the negative value of en obtained for pyridine, which seems inconsistent with the positive values found for Fe(II), Co(II) and Ni(II) complexes (48, 66,153,154). [Pg.114]

By the above definition, b is positive for crystal dissolution, and negative for crystal growth. During convective crystal dissolution, the dissolution rate u is directly proportional to b. During diffusive crystal dissolution, the dissolution rate is proportional to parameter a, which is positively related to b. Hence, for the dissolution of a given mineral in a melt, the size of parameter b is important. The numerator of b is proportional to the degree of undersaturation. If the initial melt is saturated, b = 0 and there is no crystal dissolution or growth. The denominator characterizes the concentration difference between the crystal and the saturated... [Pg.404]


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