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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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7.1 Introduction to diffusion, swelling, and drying 353<br />

Initial evaporation rate, % s -1<br />

Table 7.1.1 shows the effect <strong>of</strong> cosolvent<br />

addition on the evaporation rate <strong>of</strong> solvent<br />

mixture.<br />

The initial rate <strong>of</strong> evaporation <strong>of</strong><br />

solvent depends on both relative humidity<br />

and cosolvent presence (Figure 7.1.25). As<br />

relative humidity increases the initial<br />

evaporation rate decreases. The addition<br />

<strong>of</strong> cosolvent doubles the initial evaporation rate.<br />

In convection drying, the rate <strong>of</strong> solvent evaporation depends on airflow, solvent partial<br />

pressure, and temperature. By increasing airflow or temperature, higher process rates<br />

can be achieved but the risk <strong>of</strong> skin and bubble formation is increased. As discussed above,<br />

Vrentas-Duda free-volume theory is the basis for predicting solvent diffusion, using a small<br />

number <strong>of</strong> experimental data to select process conditions. The design <strong>of</strong> a process and a<br />

dryer which uses a combination <strong>of</strong> convection heat and radiant energy is a more complex<br />

process. Absorption <strong>of</strong> radiant energy is estimated from the Beer’s Law, which, other than<br />

for the layers close to the substrate, predicts: 32<br />

where:<br />

0.12<br />

0.1<br />

0.08<br />

[ ( ) ]<br />

Q () ξ = I αexp−α βh −ξ<br />

r<br />

0<br />

H 2 O<br />

H 2 O+BuOH<br />

Table 7.1.1. Experimentally determined<br />

initial evaporation rates <strong>of</strong> waterborne<br />

coating containing a variety <strong>of</strong> solvents at<br />

5% level (evaporation at 25 o C and 50% RH)<br />

Co-solvent<br />

Qr radiant energy absorption<br />

ξ distance from substrate<br />

I0 intensity <strong>of</strong> incident radiation<br />

α volumetric absorption coefficient<br />

β fractional thickness <strong>of</strong> the absorbing layer next to the substrate<br />

h thickness<br />

Initial evaporation<br />

rate, μg cm -2 s -1<br />

0.06<br />

none 3.33<br />

methyl alcohol 4.44<br />

0.04<br />

ethyl alcohol 3.56<br />

0.02<br />

0 10 20 30 40 50 60 70<br />

n-propyl alcohol<br />

n-butyl alcohol<br />

4.00<br />

3.67<br />

Relative humidity, %<br />

i-butyl alcohol 3.67<br />

Figure 7.1.25. Initial evaporation rate from n-amyl alcohol 3.33<br />

waterborne coating vs. relative humidity for two<br />

solvent systems. [Data from S Kojima, T Moriga, n-hexyl alcohol 3.22<br />

Polym. Eng. Sci., 35, No.13, 1098-105 (1995).] ethylene glycol<br />

mono-butyl ester<br />

3.22<br />

ethylene glycol<br />

mono-hexyl ester<br />

3.33<br />

butyl carbinol 3.11<br />

methyl-i-butyl ketone 4.89<br />

[7.1.17]

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