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Handbook of Solvents - George Wypych - ChemTech - Ventech!

Handbook of Solvents - George Wypych - ChemTech - Ventech!

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7.3 Drying <strong>of</strong> coated film 397<br />

Figure 7.3.10. Schematic diagram <strong>of</strong> drying experiment apparatus.<br />

ducts. To make the laminar airflow over the balance, the length <strong>of</strong> ducts and sizes are determined.<br />

The experiment is usually conducted in a low air velocity so as the air not to disturb<br />

the balance. Honeycomb style mesh is <strong>of</strong>ten helpful to filter the air and make the airflow a<br />

laminar one. It enabled us to do the drying experiment at a higher velocity <strong>of</strong> air. The air velocity<br />

can be as high as 1 ~ 2m/sec.<br />

Actually the air velocity <strong>of</strong> industrial dryer is much higher than the experimental conditions<br />

and the directions <strong>of</strong> flow are normally perpendicular to the coating surface, not parallel<br />

with coating surface. Thus we can hardly expect to conduct a quantitative simulation<br />

from this experiment, but we can find the characteristic drying curve and mechanisms <strong>of</strong><br />

drying <strong>of</strong> the given materials.<br />

The drying rate <strong>of</strong> coating is the weight <strong>of</strong> solvent loss per time divided by the area <strong>of</strong><br />

evaporation.<br />

where:<br />

R<br />

mass<br />

R mass<br />

dW W +Δ −W<br />

=− ≈−<br />

Adt AΔt t t t<br />

evaporation rate<br />

W weight <strong>of</strong> sample at a specific time<br />

t time<br />

Δt time interval between measurements<br />

A evaporation area<br />

[7.3.9]

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