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Non-equilibrium evaporation

Figure 9.6 The theoretical effect of non-equilibrium evaporation of lead on the isotopic ratio of a typical sample from the Laurion field. The shaded area shows the extent of the Laurion field as commonly defined, and the diagonal line shows the effect of increasing non-equilibrium losses on the isotopic ratio of a sample from the centre of the field. (From Scaife, 1993, with permission of the author and the University of Bradford.)... Figure 9.6 The theoretical effect of non-equilibrium evaporation of lead on the isotopic ratio of a typical sample from the Laurion field. The shaded area shows the extent of the Laurion field as commonly defined, and the diagonal line shows the effect of increasing non-equilibrium losses on the isotopic ratio of a sample from the centre of the field. (From Scaife, 1993, with permission of the author and the University of Bradford.)...
The variation of efficiencies is due to interaction phenomena caused by the simultaneous diffusional transport of several components. From a fundamental point of view one should therefore take these interaction phenomena explicitly into account in the description of the elementary processes (i.e. mass and heat transfer with chemical reaction). In literature this approach has been used within the non-equilibrium stage model (Sivasubramanian and Boston, 1990). Sawistowski (1983) and Sawistowski and Pilavakis (1979) have developed a model describing reactive distillation in a packed column. Their model incorporates a simple representation of the prevailing mass and heat transfer processes supplemented with a rate equation for chemical reaction, allowing chemical enhancement of mass transfer. They assumed elementary reaction kinetics, equal binary diffusion coefficients and equal molar latent heat of evaporation for each component. [Pg.2]

The surface of bulk block copolymer samples has been studied using TEM by Turturro et al. (1995). They report that non-equilibrium structures with lamellar and cylindrical microdomains oriented normal to the free surface can result from solvent casting, with a high evaporation rate. However, slower evaporation of solvent from their PS-PB diblocks resulted in the equilibrium conformation with domains parallel to the free surface. Perpendicular orientation of PS-PB lamellae at the free surface was observed earlier by Henkee et al. (1988) who studied thin films prepared by solvent casting. They observed that a reduction of this orientation occurs in favour of the parallel one on annealing the sample. [Pg.114]

This finding demonstrated that the presence of segregated stacks is a necessary condition for electrical conductivity. Reflecting the relative stabilities for the two stacking modes noted above, crystals of the red semiconductor form are obtained from a thermodynamic or equilibrium crystallization equimolar solutions of the donor and acceptor in accetonitrile are mixed and allowed to evaporate slowly. On the other hand, crystals of the black form are obtained from a kinetic or non-equilibrium crystallization hot equimolar solutions of the donor and acceptor in (the same) acetonitrile solvent are mixed and cooled rapidly. Some microcrystals of the resulting black powder are then used as seeds to obtain larger crystals of the segregated stack black form. [Pg.190]

Vaues of a may be very much less than unity and be temperature dependent. Somoijai and Lester [40] comment that "all the kinetic information is contained in the evaporation coefficient and its variation with conditions of vaporization", and they recommend the avoidance of the use of ot, in describing the rates of evaporation of solids under non-equilibrium conditions. The rate of sublimation is dependent on the attaimnent of sufficient energy by suitably disposed siuface molecules (possibly accompanied by electron or proton transfer in ionic solids). The overall rate of reactant removal is sensitive to the presence of impurities at the surface. The reverse reaction may be significant if the volatile material is not immediately removed from the vicinity of the reactant particles. Arrhenius parameters measured for sublimation processes may include a term which represents a temperature dependent concentration of surface intermediates [42]. The observation that measured evaporation rates are lower than those estimated from equilibrium vapour pressures suggests that the kinetics may be determined by a surface dissociation that precedes evaporation. This view is supported by evidence that, in selected systems, specific additives can considerably promote evaporation rates. For example [40], the evaporation rate of red phosphorous between 550 and 675 K was found to be increased by three orders of magnitude by the presence of thallium. [Pg.42]

WET-BULB TEMPERATURE. The wet-bulb temperature is the steady-state, non-equilibrium temperature reached by a small mass of liquid immersed under adiabatic conditions in a continuous stream of gas. The mass of the liquid is so small in comparison with the gas phase that there is only a negligible change in the properties of the gas, and the effect of the process is confined to the liquid. The method of measuring the wet-bulb temperature is shown in Fig. 23.4. A thermometer, or an equivalent temperature-measuring device such as a thermocouple, is covered by a wick, which is saturated with pure liquid and immersed in a stream of gas having a definite temperature T and humidity ff. Assume that initially the temperature of the liquid is about that of the gas. Since the gas is not saturated, liquid evaporates, and because the process is adiabatic, the latent heat is supplied at first by cooling the liquid. As the temperature of the liquid decreases below that of the gas, sensible heat is transferred to the liquid. Ultimately a steady... [Pg.747]

Non-Equilibrium Surface Heating and Evaporation Effect In Heterogeneous Plasma-Chemical Processes in Non-Thermal Discharges... [Pg.426]

Non-Equilibrium Surface Heating and Evaporation in Plasma Treatment of Thin Layers of Flat Surfaces Effect of Short Pulses... [Pg.427]

In summary, the process occurring in the early-time domain is regarded to be non-equilibrium. When the IR laser illuminates a surface of the liquid beam, C6H4(0H)2(H20), (m 0) is released from it by a compression wave caused by vibrational excitation of solvent molecules before the establishment of thermal equilibrium. As a result, a solute molecule embedded in a cold solvent cluster is isolated in the gas phase at a super thermal velocity of 1300 m s In the late-time domain, only a bare solute molecule having a thermal velocity of 400 m s is present because solute molecules are isolated after the evaporation of solvent by the IR-laser heating. [Pg.274]

Related to the generation of nanocapsules discussed above, is the appearance of rings or particles with single holes in hybrid system consisting of hydrophobic iron oxide, organic solvent, and polymer, probably in combination with KPS as initiator (see anchoring effect, Sect. 3.2). The emergence of these non-equilibrium structures is attributed to a delicate interplay of phase separation, viscosity, and solvent evaporation [191,192]. [Pg.226]

If two immiscible polymers are dissolved in a common solvent, which is then removed by evaporation, phase sep ation will occur. If the solvent is removed rapidly, non-equilibrium patterns may result (52). [Pg.11]


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See also in sourсe #XX -- [ Pg.426 ]




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Non-equilibrium

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