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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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6.1 Modern views on kinetics <strong>of</strong> swelling 315<br />

Figure 6.1.3. Kinetic curves <strong>of</strong> plane layer swelling at different values <strong>of</strong> concentration dependence <strong>of</strong> diffusion<br />

coefficient (ε= 0.1, d = 2/9): a - power law mode (1-s=0;2-s=1;3-s=1.5; 4-s=2.5); b - exponential (5-s=5)<br />

and blow-up mode (6 -s=5.5). [Adapted, by permission, from E. Ya. Denisyuk, V. V. Tereshatov, Vysokomol.<br />

soed., A42, 74 (2000)].<br />

following from Eqs. [6.1.38] and [6.1.41] we can estimate the concentration dependence <strong>of</strong><br />

the diffusion coefficient <strong>of</strong> a liquid fraction in elastomer. According to Eq. [6.1.40] the parameter<br />

q is determined from the initial section <strong>of</strong> the kinetic swelling curve.<br />

Experimental estimates <strong>of</strong> the parameter r can be obtained from the strain curve l(t) using<br />

Eqs. [6.1.31] and [6.1.40]. Then by making use <strong>of</strong> the formula<br />

d =1-q/r [6.1.46]<br />

following from Eq. [6.1.41] we can evaluate the parameter d which characterizes the strain<br />

dependence <strong>of</strong> the equilibrium swelling ratio <strong>of</strong> elastomer under symmetric biaxial extension<br />

in Eq. [6.1.45]. Generally the estimation <strong>of</strong> this parameter in tests on equilibrium swelling<br />

<strong>of</strong> strained specimens proves to be a tedious experimental procedure.<br />

The value <strong>of</strong> diffusion coefficient in an equilibrium swelling state can be determined<br />

from the final section <strong>of</strong> kinetic swelling curve using Eq. [6.1.44], which is expressed in<br />

terms <strong>of</strong> dimensional variables as<br />

2<br />

2<br />

g ( t) = 1−Cexp(<br />

−α D t / h )<br />

[6.1.47]<br />

1 1<br />

0<br />

where α 1 is calculated from Eq. [6.1.43). For d = 2/9, α 1 ≈ 1.2220.<br />

Note that all these relations are valid only for sufficiently high values <strong>of</strong> elastomer<br />

swelling ratio.<br />

The obtained theoretical predictions have been verified in experiments on real elastomers.<br />

The elastomers tested in our experiments were amorphous polybutadiene urethanes<br />

(PBU) with polymer network <strong>of</strong> different density: 0.3 kmol/m 3 (PBU-1), 0.05 kmol/m 3<br />

(PBU-2), 0.2 kmol/m 3 (PBU-3), 0.1 kmol/m 3 (PBU-4). Oligooxypropylene triol - Laprol<br />

373 was used as a crosslinking agent at the curing <strong>of</strong> prepolymer <strong>of</strong> oligobutadiene diol. The<br />

elastomer specimens were manufactured in the form <strong>of</strong> disks, 35 mm in diameter and 2 mm<br />

thick. The kinetics <strong>of</strong> specimen swelling was determined in low-molecular liquids: toluene,<br />

dibutyl sebacate (DBS), dioctyl sebacate (DOS).<br />

The typical kinetic and strain curves <strong>of</strong> free swelling are given in Figure 6.1.4. 6 The<br />

S-shape <strong>of</strong> the kinetic swelling curves in terms <strong>of</strong> coordinates (t 1/2 ,g 1) is indicative <strong>of</strong>

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