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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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256 Nobuyuki Tanaka<br />

N66, -CH(CH 3)- for iPP, -CH(C 6H 5)- for iPS, and -C 6H 4- for PET, was used. 21 The predicted<br />

values <strong>of</strong> c 2 for PS and PET are close to the experimental values, 56.6K and 55.3K, respectively.<br />

20,22 The standard values <strong>of</strong> c 1 and c 2 in equation [5.2.13] are 17.44 and 51.6K, respectively.<br />

20,23<br />

Table 5.2.1<br />

Polymer<br />

Tg<br />

K<br />

hg int<br />

cal/mol<br />

hg conf<br />

cal/mol<br />

sg conf<br />

cal/(K mol)<br />

hg (=hg int +hg conf )<br />

cal/mol<br />

N6 313 8500 475 11.2 8980 21.7<br />

N66 323 17000 976 22.6 17980 11.5<br />

iPP 270 1360 180 0.98 1540 94.1<br />

iPS 359 16<br />

4300 520 2.03<br />

PET 342 3900 282 7.10<br />

4820<br />

(4520)<br />

4180<br />

(4200)<br />

c2<br />

K<br />

53.1<br />

(56.6)<br />

55.6<br />

(55.3)<br />

The numerical values in parentheses are the experimental values 20,22 <strong>of</strong> c2 and hg (from c2). N6: polycaproamide<br />

(nylon-6), N66: poly(hexamethylene adipamide) (nylon-6,6), iPP: isotactic polypropylene, iPS: isotactic polystyrene,<br />

PET: poly(ethylene terephthalate).<br />

5.2.2.2 Cp jump at the glass transition<br />

The mechanism <strong>of</strong> Cp jump at the glass transition could be illustrated by the melting <strong>of</strong> ordered<br />

parts released from the glassy states. 10 Figure 5.2.2 shows the state models for an<br />

amorphous polymer below and above Tg. The ordered parts are generated near Tg in the cooling process; in the glasses, the ordered<br />

parts are contained. In the heating process, right after the glassy state was removed at<br />

Tg, the melting <strong>of</strong> ordered parts starts and continues up to Te, keeping an equilibrium state<br />

between ordered parts and flow parts. In this temperature range, the free energy per molar<br />

structural unit for polymer liquids contained ordered parts, fm, is given by: 10<br />

( )<br />

f = f X + f 1 −X<br />

[5.2.14]<br />

m x x flow x<br />

where:<br />

fx the free energy per molar structural unit for ordered parts<br />

fflow the free energy per molar structural unit for flow parts<br />

Xx the mole fraction <strong>of</strong> ordered parts<br />

From (dfm/dXx) p = 0, an equilibrium relation is derived:<br />

fm = fx = fflow<br />

[5.2.15]<br />

Whereas, C p is defined as:<br />

( )<br />

C = dh / dT<br />

[5.2.16]<br />

p q p<br />

with h q =f q- T(df q/dT) p, q = m, x or flow

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