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Inorganic Microporous Membranes for Gas Separation in Fossil Fuel ...

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3 Experimental<br />

Another solution was prepared compris<strong>in</strong>g H2O and yttrium nitrate (Treibacher) <strong>in</strong> 2propanol<br />

to prepare YSZ sols. This hydrolysis solution was added drop wise at 0ºC to the<br />

Zr-solution, and the hydrolysis molar ratio (W) was water/Zr ~4. The f<strong>in</strong>al sol conta<strong>in</strong>ed<br />

variable contents of solids with a nom<strong>in</strong>al molar ratio Zr/Y ~ 85/15. The carboxylic acids<br />

used as catalysts <strong>in</strong>clude acetic, propionic, caproic (Ca) and nanonic acid, all of which<br />

were supplied by Aldrich. The different solid contents were obta<strong>in</strong>ed by adjust<strong>in</strong>g the<br />

amount of 2-propanol used as solvent. S<strong>in</strong>gle oxide titania sols are synthesised us<strong>in</strong>g<br />

titanium isopropoxide (Alfa Aesar) <strong>in</strong>stead of zirconium n-propoxide. No b<strong>in</strong>ders are<br />

used <strong>in</strong> order to avoid large pores <strong>in</strong> the s<strong>in</strong>ter<strong>in</strong>g steps.<br />

The structure direct<strong>in</strong>g agents (SDA’s) such as, decylam<strong>in</strong>e (C10), cetylam<strong>in</strong>e (C16),<br />

cetyltrimethylammonium (CTA+) and Pluronic F127 are added to zirconia sols with<br />

weight ratios of 0.32, 0.48, 0.73 and 1.2 <strong>for</strong> C10, C16, CTA+ and F127, respectively.<br />

3.3.1.2 Am<strong>in</strong>e route<br />

Polymeric sols were prepared by mix<strong>in</strong>g a precursor solution and a hydrolysis solution.<br />

The alkoxide (zirconium n-propoxide or titanium n-propoxide Aldrich) was mixed with<br />

with diethanolam<strong>in</strong>e (hereafter referred as DEA) and n-propanol (ACS Reagents Aldrich)<br />

with a molar ratio 1:2:72.6 under argon atmosphere, <strong>for</strong>m<strong>in</strong>g the precursor solution. TiO2<br />

and ZrO2 mixture sols were prepared by mix<strong>in</strong>g the alkoxide precursors, via mix<strong>in</strong>g 10,<br />

25, 50, 66, 75 or 90% of titanium n-propoxide to zirconium n-propoxide. The hydrolysis<br />

solution, consist<strong>in</strong>g of 7-10 mol equivalents (with respect to the alkoxide) of 1.0 M HNO3<br />

(Aldrich) and n-propanol (volume ratio 1.8:50), was added slowly (1.5 mL/m<strong>in</strong>) to the<br />

precursor solution under vigorous stirr<strong>in</strong>g <strong>in</strong> an argon atmosphere. The molar ratio of the<br />

f<strong>in</strong>al sol was 1:2:7:120 <strong>for</strong> respectively the alkoxide, diethanolam<strong>in</strong>e, H2O and<br />

n-propanol.<br />

The effect of acidification on hydrolysis and condensation was <strong>in</strong>vestigated by select<strong>in</strong>g<br />

1.0 M HNO3, 0.1 M HNO3 or H2O. The effect of DEA to stabilise the precursors is<br />

compared to the longer cha<strong>in</strong> diisopropanolam<strong>in</strong>e (hereafter referred as DIPA).<br />

n-Propanol (Reagent plus, 99.7%), DEA and DIPA were purchased from Aldrich and<br />

used as received.<br />

43

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