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Evaporation time

Fig. 9. SEM photographs of cellulose acetate membranes cast from a solution of acetone (volatile solvent) and 2-meth5l-2,4-pentanediol (nonvolatile solvent). The evaporation time before the stmcture is fixed by immersion ia water is shown (24). Fig. 9. SEM photographs of cellulose acetate membranes cast from a solution of acetone (volatile solvent) and 2-meth5l-2,4-pentanediol (nonvolatile solvent). The evaporation time before the stmcture is fixed by immersion ia water is shown (24).
Membrane stmcture is a function of the materials used (polymer composition, molecular weight distribution, solvent system, etc) and the mode of preparation (solution viscosity, evaporation time, humidity, etc). Commonly used polymers include cellulose acetates, polyamides, polysulfones, dynels (vinyl chloride-acrylonitrile copolymers) and poly(vinyhdene fluoride). [Pg.294]

Evaporation times in seconds, 1st entry in a cell is for water, 2nd is for ethanol and 3rd is for acetone... [Pg.342]

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]

It is evident from the discussion above that the time for complete evaporation of a drop in a spray depends on many factors in a complicated way and will be longer than that predicted by the single drop expressions given in Eqs. (l)and(2). Nevertheless, data such as that given in Table land Eqs. (1) and (2) gives valuable information on the order of magnitude ofthe evaporation time and the role of process variables. [Pg.343]

To calculate an evaporation rate, you would divide the evaporation time by the quantity of liquid used. Explain why it is possible to use the evaporation times from this lab as evaporation rates. [Pg.51]

Liquid Evaporation time (s) Shape of liquid drop... [Pg.51]

There are two main periods of evaporation. When a drop is ejected from an atomiser its initial velocity relative to the surrounding gas is generally high and very high rates of transfer are achieved. The drop is rapidly decelerated to its terminal velocity, however, and the larger proportion of mass transfer takes place during the free-fall period. Little error is therefore incurred in basing the total evaporation time on this period. [Pg.941]

An expression for the evaporation time for a pure liquid drop falling freely in air has been presented by Marshall(38,39). For drop diameters less than 100 im this may be simplified to give ... [Pg.941]

In order to obtain the solution desired, a value of Ts is assumed, the vapor pressure of A is determined from tables, and mAs is calculated from Eq. (6.98). This value of mAs and the assumed value of Ts are inserted in Eq. (6.97). If this equation is satisfied, the correct Ts is chosen. If not, one must reiterate. When the correct value of Ts and mAs are found, BT or BM are determined for the given initial conditions Tx or mAco. For fuel combustion problems, mAcc is usually zero however, for evaporation, say of water, there is humidity in the atmosphere and this humidity must be represented as mAco. Once BT and BM are determined, the mass evaporation rate is determined from Eq. (6.87) for a fixed droplet size. It is, of course, much preferable to know the evaporation coefficient (5 from which the total evaporation time can be determined. Once B is known, the evaporation coefficient can be determined readily, as will be shown later. [Pg.346]

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]

In order for the yttrium elution to work properly, the pH must be maintained at greater than pH 4. This is accomplished by converting the column to the ammonium form. Otherwise, the pH of the a-HIB will decrease on the column and yttrium will not elute. After yttrium is eluted, the ammonium ion must be displaced from the column to prevent excessive salts in the final product. This is the reason for the 0.5 M HC1 wash of the column after the a-HIB has been removed. The strontium product is obtained in 6 M HC1. Using a 40-50 ml resin bed, the strontium is obtained in a volume of approximately 100 ml. Some yield is sacrificed to keep this volume as small as possible to reduce the evaporation time. [Pg.130]

The evaporating flask should be less than one-half full for efficient solvent removal. Generally, the flask volume should be four to five times that of the solvent volume. Prolonged evaporation time should be avoided to minimize pigment degradation. Evaporation should be complete in 5 to 10 min. [Pg.777]

For later references, we want to keep in mind that, at 15°C and in the presence of lower atmospheric humidity, approximately 10% of the hydrogen cyanide used at Auschwitz have left the carrier material during the first five minutes, and approximately 50% after half an hour. In cool cellar areas with a relative humidity of approximately 100%, the evaporation times would have been seriously delayed . [Pg.195]

Split injection wide-bore inserts (3-5 mm ID) reduce deviations between the preset and the true split ratio and improve evaporation (prolonged evaporation time). [Pg.50]

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.

See other pages where Evaporation time is mentioned: [Pg.84]    [Pg.62]    [Pg.65]    [Pg.71]    [Pg.278]    [Pg.525]    [Pg.264]    [Pg.131]    [Pg.343]    [Pg.343]    [Pg.22]    [Pg.124]    [Pg.228]    [Pg.253]    [Pg.445]    [Pg.161]    [Pg.190]    [Pg.155]    [Pg.145]    [Pg.267]    [Pg.90]    [Pg.113]    [Pg.136]    [Pg.165]    [Pg.245]    [Pg.58]    [Pg.233]    [Pg.375]   
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See also in sourсe #XX -- [ Pg.49 ]

See also in sourсe #XX -- [ Pg.741 ]

See also in sourсe #XX -- [ Pg.124 ]




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