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Evaporation time, effect

Additional Factors Affecting Evaporation Times. For liquid drops containing solids, which lower the normal vapor pressure of the liquid, the net effect of the solids is to increase the time for complete evaporation, Marshall (1954). The presence of solids introduces an additional complication associated with the changing droplet surface temperature during the evaporation process. This gives rise to longer evaporation times. [Pg.343]

UF test kit. The effect of parameters like polymer solution composition, evaporation time and shrinkage temperature were studied for the tailor making of the membranes. The commercial requirement for the concentration is hiking of concentration from 20 mg/1 to 10 g/l. The feasibility of the process was assessed by experiments in three stages (i) 19 mg/l to 122 mg/l... [Pg.299]

Unfortunately, the slmulational data " are neither conclusive, suggesting scaling exponents between 4 and 6. Obviously, finite-size and finite-time effects are important, giving rise to gradual crossovers (similar to what we observed in the evaporation case ). In addition, details of the dynamics, for instance, fast or slow terrace diffusion (as discussed above), should be viewed carefully. [Pg.154]

Drug release may be affected by a number of process parameters such as drug loading, polymer molecular weight, polymer composition, initial concentration of the polymer in the organic phase of the emulsion, amount of emulsifier, stirring speed, vacuum pressure, solvent evaporation time and temperature. These parameters were kept constant and only the amount of NaOH was varied. Therefore, changes in the in vitro release curves should reflect only the effect of NaOH in various concentrations. ... [Pg.217]

Figure 9. Effect of volatility on evaporation time for fuel droplet burning in oxygen-nitrogen atmosphere. Figure 9. Effect of volatility on evaporation time for fuel droplet burning in oxygen-nitrogen atmosphere.
The effect of Fuchs modification on Eq. 15.15 is to increase the lifetime of very small drops fairly significantly and to even have some effect on drops having diameters of 10 gm or more. Figure 15.1 shows a plot of the ratio of Eq. 15.16 to Eq. 15.15 for similar conditions as a function of d, the droplet diameter. As an example, for 1-gm-diameter droplets, evaporation times as estimated by using the Fuchs modification are about 20 times greater than those estimated with Langmuir s equation alone. [Pg.142]

Information on droplet characteristics in sprays and spray flames is presented. The distribution of OH and CH species in spray and gas-fueled flames is presented in order to decouple the effect of droplet vaporization. As the droplet size in the spray flame becomes smaller, its signature should begin to resemble that of the gas-fueled flame, due to the extremely short evaporation time of the droplets. [Pg.130]

The attractive features of splitless injection techniques are that they allow the analysis of dilute samples without preconcentration (trace analysis) and the analysis of dirty samples, since the injector is easily dismantled for cleaning. Success with individual samples, however, depends on the selection of experimental variables of which the most important sample size, sample solvent, syringe position, sampling time, initial column temperature, injection temperature and carrier gas flow rate, often must be optimized by trial and error. These conditions, once established, are not necessarily transferable to another splitless injector of a different design. Also, the absolute accuracy of retention times in splitless injection is generally less than that found for split injection. For splitless injection the reproducibility of retention times depends not only on chromatographic interactions but also on the reproducibility of the sampling period and the evaporation time of the solvent in the column inlet, if solvent effects (section 3.5.6.2) are employed. The choice of solvent, volume injected and the constancy of thermal zones will all influence retention time precision beyond those for split injection. For quantitative analysis the precision of repeated sample injections is normally acceptable but the method is subject to numerous systematic errors that may... [Pg.185]

The heated evaporation of graphite liquid marbles on a superheated substrate was investigated at various surface temperatures and compared with pure water droplets. It is found that if the temperature is above the Leidenfrost point, the evaporation time of liquid marbles and water droplets are almost the same, whereas if the temperature is below the Leidenfrost point, water droplets evaporate much faster and liquid marbles still exhibit the Leidenfrost-like effect. It is postulated that the prolonged evaporation time of... [Pg.1660]

Fang, Y., Pham, V.A., Matsuura, T., Santerre, J.P. and Narbaitz, R.M. 1994. Effect of surface-modifying macromolecules and solvent evaporation time on the performance of polyethersulfone membranes for the separation of chloroform/water mixtures by per-vaporation.. 7. Ami. Polvm. ScL 54 1937-1943. [Pg.177]

The liquid phase distribution over time obtained from the numerical simulation is shown in Fig. 11 At the onset of evaporation, a curved meniscus develops inside the cylinder and recedes. Upon further evaporation, capillary effects become clearly visible large pores dry out earlier, while small pores stay saturated for a longer time. In order to study the effect of wettability, another simulation with the same particle packing but with a different value of the equilibrium contact angle has been performed, see Fig. 12. By comparing these two figures, one can see that the capillary effects are clearly more pronounced for smaller equilibrium contact angle. [Pg.104]

Figure 33.11 UTDR amplitude as a function of arrival time for a portion of the reflected waveform during the evaporative casting of polymeric membranes from a casting solution initially at 23 °C and a composition of 10 65 25 wt% of cellulose-acetate, acetone, and water, respectively, showing the effect of evaporation time (a) 0 s, (b) 70 s, (c) 165 s, and (d) 450 s peaks A, B, and C correspond to reflections from the fixed support plate, phase separation boundary, and liquid-gas interface, respectively. Figure 33.11 UTDR amplitude as a function of arrival time for a portion of the reflected waveform during the evaporative casting of polymeric membranes from a casting solution initially at 23 °C and a composition of 10 65 25 wt% of cellulose-acetate, acetone, and water, respectively, showing the effect of evaporation time (a) 0 s, (b) 70 s, (c) 165 s, and (d) 450 s peaks A, B, and C correspond to reflections from the fixed support plate, phase separation boundary, and liquid-gas interface, respectively.

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See also in sourсe #XX -- [ Pg.460 , Pg.461 ]




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