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Then, the solubility parameter can be estimated from general equations:<br />

ΔHmix = Vs(δ1 – δ2) * φ1 φ2 .<br />

- This is one <strong>of</strong> the simple expressions <strong>of</strong> solubility parameter deduced for nonpolar<br />

systems. In practise, we have solvents and solutions with different polar forces such as<br />

dispersion, polar and hydrogen ones. Therefore the cohesive energy Ecoh is divided <strong>in</strong>to three<br />

parts, correspond<strong>in</strong>g to three types <strong>of</strong> <strong>in</strong>teraction forces Ecoh = Ed + Ep + Eh (contribution <strong>of</strong><br />

dispersion forces Ed, polar forces Ep and hydrogen-bond<strong>in</strong>g Eh). Then every substance could<br />

be characterized accord<strong>in</strong>g to free contributions <strong>of</strong> total solubility parameter<br />

2 2 2<br />

δtotal.= σ + σ + σ .<br />

disp.<br />

polar.<br />

hydrogen.<br />

By this is predicted that if δ1 = δ2 the ethalpy <strong>of</strong> mix<strong>in</strong>g is ΔHmix = 0 and ΔGmix = ΔHmix -<br />

TΔSmix < 0 and this is <strong>in</strong> accorrdance with the general rule for thermodynamic view <strong>of</strong><br />

solubility and mix<strong>in</strong>g. Then, the smaller is the difference <strong>of</strong> value δ <strong>of</strong> solvent and polymer,<br />

the better is possibility <strong>of</strong> its dissolv<strong>in</strong>g. The polymers should be mostly soluble <strong>in</strong> that<br />

solvents, which their < δ > correspond to the middle <strong>of</strong> the <strong>in</strong>terval <strong>of</strong> polymer solubility or<br />

approximately ± 2 units.<br />

AIM OF STUDY:<br />

The aim <strong>of</strong> conducted research is the evaluation <strong>of</strong> <strong>in</strong>fluence <strong>of</strong> several aspects – especially<br />

structure <strong>of</strong> samples – on the chemical resistance <strong>of</strong> PUR coat<strong>in</strong>gs and the value <strong>of</strong> their<br />

solubility parametr δ2. As far as these aspects are concerned, these <strong>in</strong>clude especially the type<br />

<strong>of</strong> used monomers (<strong>in</strong> case <strong>of</strong> PUR polymers for example like type and funcionality <strong>of</strong> used<br />

alcohols, acids and isocyanates, type <strong>of</strong> bonds, etc.), the weight, size and type <strong>of</strong> film form<strong>in</strong>g<br />

polymer and the type <strong>of</strong> <strong>in</strong>teractions between <strong>in</strong>dividual cha<strong>in</strong> parts.<br />

METHOLOGY:<br />

The solubility parameter δ2 <strong>of</strong> polymer could be determ<strong>in</strong>ed accord<strong>in</strong>g to its <strong>in</strong>teraction<br />

with solvents <strong>of</strong> known solubility parameter δ1. For example, the solubility parameter <strong>of</strong> a<br />

l<strong>in</strong>ear polymer can be determ<strong>in</strong>ed from its limit<strong>in</strong>g viscosity number and <strong>of</strong> a cross-l<strong>in</strong>ked<br />

one accord<strong>in</strong>g to the degree <strong>of</strong> swell<strong>in</strong>g, both <strong>of</strong> these values be<strong>in</strong>g the function <strong>of</strong> solubility<br />

parameter <strong>of</strong> used solvent δ1. In case <strong>of</strong> best solvent, is the value <strong>of</strong> [η] or Q <strong>of</strong> polymer the<br />

heights and solubility parameter <strong>of</strong> this solvent δ1 correspondents with solubility parameter <strong>of</strong><br />

polymer δ2<br />

As far as measur<strong>in</strong>g <strong>of</strong> viscosity is concenred, the samples were dissolved <strong>in</strong> <strong>selected</strong><br />

group <strong>of</strong> solvents whose solubility parameters δ1 varied from 18 to 24 (30). Then their<br />

dynamic viscosity η were masured. It was done us<strong>in</strong>g capillar or Ubelohde viscosimeter.<br />

η sp<br />

Subsequently, specific viscosity ηspec and the limit<strong>in</strong>g viscosity number [η] = lim were<br />

c→0<br />

c<br />

calculated.<br />

The degree <strong>of</strong> sample’s swell<strong>in</strong>g Q = (m-m0/m0)*1/ςsolv was calculated by weight<strong>in</strong>g<br />

samples after soak<strong>in</strong>g <strong>in</strong> chosen solvents for 5 days.<br />

Sborník soutěže Studentské tvůrčí č<strong>in</strong>nosti Student 2006 a doktorské soutěže O cenu děkana 2005 a 2006<br />

Sekce DSP 2006, strana 250

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