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Mixing, energy volume

From equation (7) is also clear that the volume of the reactor V has only an effect on the ozone loss with the effluent. An increase in reactor volume results in an increase in residence time 6 and therefore in a decrease of the ozone loss. This means that large reactors are favourable. Also with respect to ozone supply a large reactor has advantages. However it has to be noted that large reactors require more mixing energy and are also more expensive. [Pg.260]

Each experiment in this part requires mixing equal volumes of two solutions in a test tube (100 X 13 mm). Use about 10 drops of each solution. Record your observation at the time of mixing (10). When there appears to be no evidence of a reaction, feel the test tube for an energy change (exothermic or endothermic). The solutions to be mixed are outlined in the table below. [Pg.78]

An ideal mixture of molten salts is a mixture for which the heat of mixing, energy of mixing and variation of volume of mixing have the value zero. Certainly, in practice there are no such ideal mixtures. The Gibbs energy of mixing... [Pg.471]

In a system with only one type of segment, the volume fraction is unity in every layer (p lz) = =1. Mixing energy is absent. Only in the surface layer is... [Pg.654]

The equilibrium constants are related to the thermodynamic Gibb s free energy in the regular manner ksTlnKn = AG ° = Af/ - TASj, where kg is Boltzmann s constant and T is the temperature, and ideal mixing (no volume change) is assumed. The chemical equilibrium constants can also be written in terms of the activities of the different species, defined in terms of the chemical potential, of specie k, as a/ expi/hJkgT). Thus, at equilibrium... [Pg.44]

A suspended liquid drop forms a sphere, because this shape has minimum surface area (hence minimum interfacial free energy) for a given volume area is related to the cube of droplet radius. Distortion is a flow shear effect, depending on droplet cross-section, related to the square of the radius. At large diameters, shear forces are greater than interfacial tension forces, droplets are distorted into cylinders, and subdivision occurs. Droplet radius decreases, until the interfacial tension forces balance (or exceed) shear forces, and further division stops. In emulsification experiments in which the amount of mixing energy is constant and y... [Pg.2209]

Within mean field theory, for a symmetric blend the excess free energy of mixing per volume is given by the Flory-Huggins expression ... [Pg.101]

Figure 8 shows the curves at different superficial linear velocities and the relationship ofhorsepower to height of liquid in a fermenter. These curves are the mixing energy (power per unit volume) released by rising bubbles to the liquid. [Pg.101]

Mixtures of polymer chain belonging to the same chemical species but with different isotopic compositions (deuterated and non-deuterated) have been widely used for experimental studies of polymer structures, since good neutron beams became available. This technique, combining the preparation of adequate samples and neutron scattering experiments, enabled the experimentalists to determine the size of polymer chains (polystyrene or polydimethylsiloxane), in all kinds of polymer mixtures or concentrated polymer solutions. However, the technique relies on the fact that the deuterated and non-deuterated isotopic varieties of a same polymer are compatible with one another. It is admitted that under the experimental conditions described above, the mixture constitutes a unique phase. In fact, the mixing energy of deuterated and non-deuterated chains is probably very small. However, it is non-zero, in particular, because of differences in atomic volumes and polarizabilities. Thus, there is no doubt that demixtion may occur in mixtures of deuterated and undeuterated chains of very high molecular masses. [Pg.834]

Using the energy, volume, and entropy changes on mixing given here, one can easily compute the other thermodynamic properties of an ideal gas mixture (Problem 9.1). The results are given in Table 9.1-1. Of particular interest are the expressions for... [Pg.402]

Fig. 11. Gibbs free energy of mixing against volume fraction of polymer for various values of y and n. Fig. 11. Gibbs free energy of mixing against volume fraction of polymer for various values of y and n.
AG the Gibbs free mixing energy (Pi volume fraction of a component of a solvent. [Pg.131]


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See also in sourсe #XX -- [ Pg.314 ]




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