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

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4 Results and discussion<br />

The coupled loss of SDA and crystall<strong>in</strong>ity dur<strong>in</strong>g calc<strong>in</strong>ation might be expla<strong>in</strong>ed by the<br />

collapse of the DOH surface structure. While the <strong>in</strong>ner part of the DOH crystals<br />

ma<strong>in</strong>ta<strong>in</strong>s their crystal structure <strong>in</strong>clud<strong>in</strong>g the trapp<strong>in</strong>g of some of the template and the<br />

outer part of the DOH crystals collapses. In pr<strong>in</strong>ciple, O2 with a k<strong>in</strong>etic diameter of 3.46<br />

Å, CO of 3.70 Å and CO2 of 3.30 Å are <strong>in</strong>accessible to the DOH structure due to the<br />

smaller w<strong>in</strong>dow open<strong>in</strong>g compared to the k<strong>in</strong>etic diameter of these gasses. However, the<br />

DOH structure might ‘breathe’ (elastic vibration) at elevated temperatures allow<strong>in</strong>g the<br />

transport of these gasses. This behaviour has been observed <strong>for</strong> other zeolites. 134<br />

The rema<strong>in</strong>s of the burned out ADA might react with the oxygen from the silica<br />

framework at elevated temperatures. This could expla<strong>in</strong> the decrease <strong>in</strong> cage occupancy<br />

coupled with the DOH structure loss. This might occur preferentially at the outer surface<br />

of the DOH crystals. SDA combustion is studied by DTA/TG measurements <strong>in</strong> air and <strong>in</strong><br />

nitrogen. DTA/TG plots show similar behaviour <strong>for</strong> both gasses <strong>in</strong>dicat<strong>in</strong>g that the<br />

weight loss is <strong>in</strong>dependent of the atmosphere and could expla<strong>in</strong> the <strong>in</strong>ternal combustion.<br />

In a nut shell, conventional calc<strong>in</strong>ation at ambient pressure removes only a part of the<br />

organic SDAs.<br />

2) Catalytic oxidation by titanium <strong>in</strong>corporation <strong>in</strong> the DOH framework<br />

Titanium was <strong>in</strong>corporated <strong>in</strong>to the DOH framework <strong>in</strong> order to enhance the conventional<br />

calc<strong>in</strong>ation by means of catalytic oxidation. Small amounts of titanium isopropoxide or<br />

titanium n-propoxide were added to the silica source or to the f<strong>in</strong>al sol composition.<br />

Similar attempts have been per<strong>for</strong>med to <strong>in</strong>corporate iron or alum<strong>in</strong>ium and have resulted<br />

<strong>in</strong> multi phase zeolite products.<br />

Highly crystall<strong>in</strong>e Ti-DOH products are obta<strong>in</strong>ed after ~27 days of crystallisation at<br />

200ºC <strong>in</strong> the presence of a small amount of titanium <strong>in</strong> the gel (molar ratio Si/Ti 10-∞,<br />

see Table 17). Electron energy dispersive X-ray analysis and Inductively Coupled Plasma<br />

analysis confirm the presence of titanium <strong>in</strong> the samples. Raman spectroscopy presents<br />

bands at 960 cm -1 <strong>in</strong>dicat<strong>in</strong>g the presence of Ti-O-Si bonds.<br />

Table 17 Cage occupancy of as-made and after calc<strong>in</strong>ation <strong>for</strong> samples with different Si/Ti molar ratios<br />

Sample # Crystal size Si/Ti Cage occupancy<br />

As-made Calc<strong>in</strong>ed at 900ºC<br />

Ti-1 Ca. 100 µm ∞ 91% 31%<br />

Ti-2 100 76% 24%<br />

Ti-3 Ca. 40 µm ∞ - 11%<br />

Ti-4 100 - 4%<br />

60

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