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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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350 <strong>George</strong> <strong>Wypych</strong><br />

• evaporation-induced self association <strong>of</strong> the polymer with progressive entrapment <strong>of</strong><br />

adsorbed volatile molecules in the glassy microdomains (during transition from a<br />

rubbery to a glassy state)<br />

• elimination <strong>of</strong> residual molecules entrapped in the polymer.<br />

The last two stages are discussed in Chapter 16 which deals with residual solvent. This<br />

discussion concentrates on the effect <strong>of</strong> components on the drying process and the effect <strong>of</strong><br />

the drying process on the properties <strong>of</strong> the product.<br />

A schematic <strong>of</strong> the drying process is<br />

represented in Figure 7.1.18. The material<br />

to be dried is placed on an impermeable<br />

substrate. The material consists <strong>of</strong> solvent<br />

and semicrystalline polymer which contains<br />

a certain initial fraction <strong>of</strong> amorphous<br />

and crystalline domains. The presence <strong>of</strong><br />

Figure 7.1.18. Schematic representation <strong>of</strong> drying a<br />

polymer slab. [Adapted, by permission, from M O Ngui,<br />

S K Mallapragada, J. Polym. Sci.: Polym. Phys. Ed., 36,<br />

No.15, 2771-80 (1998).]<br />

crystalline domains complicates the process<br />

<strong>of</strong> drying because <strong>of</strong> the reduction in<br />

diffusion rate <strong>of</strong> the solvent. Evaporation<br />

<strong>of</strong> solvent causes an inward movement <strong>of</strong><br />

material at the surface and the drying pro-<br />

cess may change the relative proportions <strong>of</strong> amorphous and crystalline domains. 29<br />

Equations for the change in thickness <strong>of</strong> the material and kinetic equations which relate<br />

composition <strong>of</strong> amorphous and crystalline domains to solvent concentration are needed to<br />

quantify the rate <strong>of</strong> drying.<br />

The thickness change <strong>of</strong> the material during drying is given by the equation:<br />

v dL<br />

D<br />

dt<br />

v<br />

1 = ⎛ ∂<br />

⎜<br />

⎝ ∂<br />

⎞<br />

⎟<br />

1<br />

x ⎠x=<br />

L<br />

[7.1.13]<br />

where:<br />

v1 volume fraction <strong>of</strong> solvent<br />

L thickness <strong>of</strong> slab as in Figure 7.1.18<br />

t time<br />

D diffusion coefficient<br />

x coordinate <strong>of</strong> thickness<br />

The rate <strong>of</strong> change <strong>of</strong> crystalline volume fraction is given by the equation:<br />

∂v<br />

2<br />

∂t<br />

c<br />

= kv<br />

[7.1.14]<br />

1 1<br />

where:<br />

v2c volume fraction <strong>of</strong> crystalline phase<br />

k1 rate change <strong>of</strong> crystalline phase proportional to folding rate<br />

The rate <strong>of</strong> change <strong>of</strong> amorphous volume fraction is given by the equation:<br />

∂v<br />

2a∂⎛ ∂v1<br />

⎞<br />

= ⎜D<br />

⎟− kv 1 1<br />

[7.1.15]<br />

∂t<br />

∂x<br />

⎝ ∂x<br />

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