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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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7.3 Drying <strong>of</strong> coated film 401<br />

Figure 7.3.16. Phase diagram <strong>of</strong> MEK-toluene-VAGH system with the different initial solvent compositions. The<br />

concentration is measured by rapid scanning FT-IR method. [Adapted, by permission, Suzuki et al., Proceedings<br />

<strong>of</strong> 9th International Coating Science and Technology Symposium, Delaware, USA, May 17 - 20, 1998, pp. 21-24].<br />

example <strong>of</strong> PVAc-methanol system is suitable for the FT-IR spectroscopy because <strong>of</strong> their<br />

separated bands, it is difficult to extend FT-IR technique to the other solvent systems.<br />

7.3.3.3 High-airflow drying experiment using flame ionization detector (FID)<br />

total hydrocarbon analyzer<br />

The gravimetric method is limited to a certain air velocity level due to the oscillation <strong>of</strong> balance<br />

in the high airflow stream. However most <strong>of</strong> the industrial drying process accomplished<br />

by passing the coating under high air velocity jet <strong>of</strong> hot air. Thus to simulate the<br />

industrial drying conditions and according drying phenomena better, high airflow drying<br />

experiment setup (HADES) was suggested by Cairncross et al. 52,57<br />

Low air velocity results in low heat transfer coefficient, the heat transfer coefficient <strong>of</strong><br />

conventional laboratory drying experiments ranges from 1 to 10 J/m 2 s o C, while that <strong>of</strong> industrial<br />

dryer is ranges about 20 to 200 J/m 2 s o C. The high heat and mass transfer at the evaporation<br />

surface may result in ‘trapping skinning’ because the surface evaporation is too high<br />

in compared with the rate <strong>of</strong> diffusion <strong>of</strong> solvent within the coating. The heat transfer coefficient<br />

<strong>of</strong> HADES is up to 26.4 J/m 2 s o C which is equivalent with that <strong>of</strong> usual single-side impingement<br />

dryers, 52 and it was reported that the HADES successfully simulates the skinning<br />

phenomena with the solution <strong>of</strong> PMMA-toluene. 52<br />

HADES measures solvent concentration <strong>of</strong> exhaust gas from the sample chamber<br />

where the solvent is evaporated from the coating. Then the rate <strong>of</strong> evaporation is equal to the

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