Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
number 3 • 99<br />
METHODS<br />
The study <strong>of</strong> <strong>the</strong> effect <strong>of</strong> solvent mixtures on commercial<br />
oil and alkyd paints focused on <strong>the</strong> behavior <strong>of</strong> <strong>the</strong> crosslinked<br />
matrix upon solvation, <strong>the</strong> solubility, and leachability <strong>of</strong><br />
low molecular weight compounds. Paint products used were<br />
Schmincke Norma Pr<strong>of</strong>essional- Ölfarbe 11704, PBk 9, 37 mL<br />
and Winsor & <strong>New</strong>ton Griffin alkyd paint 1302340, PBk 9, 37<br />
mL at a film thickness <strong>of</strong> 300 mm. The alkyd tested is a long- oil<br />
o- phthalic acid polyester derivative <strong>of</strong>ten used in oxidative drying<br />
<strong>of</strong> alkyd paints (Ploeger, 2009). The paint films were aged<br />
over 12 months while applying True- Lite 5500 K daylight under<br />
window glass at 35°C–40°C. Because <strong>of</strong> <strong>the</strong> similarity <strong>of</strong> <strong>the</strong><br />
chemical nature <strong>of</strong> <strong>the</strong> binders in <strong>the</strong>se paints it was possible to<br />
compare selective solvation effects. The experiments were run<br />
with six solvents exhibiting characteristic interactive properties,<br />
n- hexane, toluene, chlor<strong>of</strong>orm, diethyl e<strong>the</strong>r, acetone, and<br />
ethanol (pure, Merck), as well as binary mixtures <strong>the</strong>re<strong>of</strong> at five<br />
different molar mixing ratios, 0.15:0.85, 0.35:0.65, 0.50:0.50,<br />
0.65:0.35, and 0.85:0.15, in correspondence to data collected<br />
by Marcus (2002). Swelling tests were performed after Zumbühl<br />
(2005). The swelling capacity upon immersion was used<br />
to quantify solvation effects on <strong>the</strong> binder matrix and explore<br />
its relation to <strong>the</strong> parameters <strong>of</strong> <strong>the</strong> solvent mixtures. The linear<br />
solvation energy relationship based on <strong>the</strong> solvatochromic system<br />
developed by Catalán (2001) was applied to characterize<br />
<strong>the</strong> solvent mixtures. A PerkinElmer LAMBDA 750 UV/Vis/NIR<br />
spectrometer was used at a spectral resolution <strong>of</strong> 1 nm to quantify<br />
<strong>the</strong> extraction <strong>of</strong> binding media components from leachates<br />
<strong>of</strong> alkyd paint films immersed in 25 binary ethanol mixtures for<br />
1 and 10 minutes (maximum swelling). Extracts <strong>of</strong> 2 g <strong>of</strong> paint<br />
sample in 50 mL <strong>of</strong> solvent were gravimetrically quantified and<br />
characterized using Fourier transform infrared spectroscopy<br />
(FTIR), direct temperature resolved mass spectrometry, and gas<br />
chromatography mass spectroscopy. The FTIR measurements<br />
were performed on a PerkinElmer System 2000 and a Bruker<br />
HYPERION 3000/Tensor 27 at 4 cm –1 spectral resolution and<br />
32 scans. For spectroscopic distinction <strong>of</strong> <strong>the</strong> carboxylic acid<br />
groups from o<strong>the</strong>r oxidation products, samples were rolled out<br />
on CVD diamond windows and exposed to sulfur tetrafluoride<br />
(SF 4<br />
) for 16 hours in a Teflon chamber (Mallégol et al., 2000).<br />
Direct temperature- resolved mass spectrometry (DTMS) measurements<br />
were carried out on a Thermo DSQ II quadrupole<br />
instrument equipped with a direct probe module. The sample<br />
was homogenized in methanol (2 mL to 1 mg <strong>of</strong> sample). Approximately<br />
0.5 mL <strong>of</strong> <strong>the</strong> suspension (equivalent to 0.25 mg<br />
sample) was applied to <strong>the</strong> rhenium filament, and <strong>the</strong> solvent<br />
was allowed to evaporate. The filament was <strong>the</strong>n introduced<br />
<strong>into</strong> <strong>the</strong> ion source and resistively heated by ramping <strong>the</strong> applied<br />
current. (Probe experimental parameters were as follows:<br />
5 s at 0 mA, ramp 10 mA/s to 1000 mA, and 20 s at 1000 mA.<br />
Mass spectrometer parameters were as follows: ion source temperature,<br />
220°C; electron lens, 100 V; electron energy, –16 eV;<br />
emission current, 45 mV; lens 1, –25 V; lens 2, –8 V; lens 3, –25<br />
V; prefilter –12.5 V; full scan mode mass to charge ratio m/z,<br />
42–1050; scan rate, 9700 amu/s.) Analyses were carried out in<br />
triplicate.<br />
RESULTS AND DISCUSSION<br />
The solvation properties were characterized by analyzing<br />
<strong>the</strong> swelling behavior <strong>of</strong> free paint film, expressed in volume<br />
change DV/V 0<br />
(Zumbühl, 2005). The absolute swelling values<br />
are different for oil and alkyd paint. This is due to distinct densities<br />
within <strong>the</strong> cross- linked system and variable mobility <strong>of</strong> <strong>the</strong><br />
polymer chains. All 75 binary solvent mixtures within <strong>the</strong> 15<br />
experimental series exhibited nonideal properties (Figure 3).<br />
Nonideal swelling properties <strong>of</strong> ethanol mixtures were<br />
similarly documented by Phenix (2002). In order to qualify <strong>the</strong><br />
selective solvation, <strong>the</strong> parametrization <strong>of</strong> <strong>the</strong> solvent mixtures<br />
was carried out using <strong>the</strong> Catalán (2001) solvatochromic linear<br />
solvation energy relationship system. Results show that solvation<br />
<strong>of</strong> oil paint systems is dominated by dispersive interactions,<br />
whereas dipole- dipole interactions as well as specific protic and<br />
aprotic interactions are <strong>of</strong> negligible importance. The solvation<br />
<strong>of</strong> <strong>the</strong> oxidative functional groups is only <strong>of</strong> minor influence.<br />
This is also true for mature oil paint films, where <strong>the</strong> absolute<br />
swelling capacity decreases with age while <strong>the</strong> relative solvent<br />
sensitivity remains nearly unchanged (Stolow, 1978). Cosolvation<br />
was observed in alkyd paint systems exhibiting a very distinct<br />
swelling sensitivity when compared to oil paint. This can<br />
be explained through dipolar solvents, e.g., acetone, showing a<br />
dipole- induced interaction with polarizable functional groups,<br />
such as aromatic rings and ester groups within <strong>the</strong> phthalic acid<br />
polyester structure <strong>of</strong> <strong>the</strong> alkyd. The nonideal swelling properties,<br />
however, cannot be due to selective solvation because no<br />
relation between <strong>the</strong>se two factors was observed.<br />
Nonideal Action <strong>of</strong> Solvent Mixtures<br />
The swelling data reveal almost equivalent swelling anomalies<br />
within oil and alkyd paints. In extremis, <strong>the</strong> swelling volume<br />
can reach several times <strong>the</strong> ideal value, as shown in Figure 3. It<br />
seems obvious that this effect is not influenced by <strong>the</strong> liquid- solid<br />
interactions but is unambiguously caused by liquid- liquid interactions.<br />
As a general rule, <strong>the</strong> larger <strong>the</strong> difference in polarity is<br />
between <strong>the</strong> mixed solvents, <strong>the</strong> greater <strong>the</strong> observed deviation is<br />
from <strong>the</strong> ideal behavior. In apolar mixtures this deviation from<br />
ideal behavior is generally small. In contrast, mixtures containing<br />
a polar solvent deviate significantly and may exhibit strong<br />
anomalies in <strong>the</strong> swelling behavior (Figure 4).<br />
As a consequence, all ethanol mixtures induce very strong<br />
swelling anomalies in oil and alkyd paints, with an increase in<br />
volume <strong>of</strong> up to 200%. This effect is particularly pronounced<br />
with ethanol mixtures forming azeotropes, an observation that is<br />
consistent with <strong>the</strong> findings for different polymers: here <strong>the</strong> solubility<br />
increases if at least one <strong>of</strong> <strong>the</strong> components strongly interacts