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

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2 Theoretical background<br />

2.3.3.2 <strong>Microporous</strong> transition metal oxide membranes<br />

In contrast to sol-gel derived non-transition silica membranes, the <strong>for</strong>mation of<br />

microporous transition titania or (yttria stabilized) zirconia is difficult due to the fast and<br />

hard to control hydrolysis and condensation reactions of Ti or Zr-precursors. 81 The fast<br />

reactivity can be a result of the larger charge density of Zr or Ti compared with Si 76 or<br />

by the heterogeneousity of the commercially purchased alkoxide precursors. 80,81 Several<br />

groups have reported the synthesis of microporous YSZ (yttria doped zirconia) 78,81,83,104-<br />

111 or titania 78,82,83,100-102,104,112,113 materials, however they were not successful <strong>in</strong><br />

produc<strong>in</strong>g membranes with a significantly larger permselectivity than the Knudsen factor<br />

<strong>for</strong> the gasses H2, N2, CO2 and CH4 as a result of the pore sizes of ~0.9 nm and larger. 114<br />

2.3.4 Selection of Sol-Gel derived membrane material<br />

<strong>Microporous</strong> sol-gel derived silica membranes are found nowadays <strong>in</strong>dustrial <strong>in</strong><br />

pervaporation applications. Lab scale sol-gel derived membranes offer good gas<br />

separation factors which is ma<strong>in</strong>ly based on the molecular siev<strong>in</strong>g compared with<br />

sorption properties. Good prospects are there<strong>for</strong>e envisaged <strong>for</strong> applications such as<br />

dehydrogenation of hydrocarbons, coal gasification, the postcombustion concept and the<br />

water-gas shift process <strong>in</strong> the precombustion concept.<br />

Modified sol-gel derived non-transition metal oxide silica membranes have not found<br />

their way <strong>in</strong>to the large scale gas separation. An alternative method to obta<strong>in</strong><br />

hydrothermal stable microporous membranes is to develop non-silica sol-gel derived<br />

materials with the follow<strong>in</strong>g requirements:<br />

o Separative to H2 from CO2 or CO2 from N2 by means of molecular siev<strong>in</strong>g<br />

o Defect free microporous layers<br />

o Comparable permeabilities to silica membranes<br />

o Stable <strong>in</strong> hydrothermal conditions<br />

2.3.4.1 <strong>Microporous</strong> transition metal oxide membranes<br />

Sol-gel derived microporous crystall<strong>in</strong>e titania membranes are commercially today<br />

available with a pore size of 0.9 nm. 101 Sol-gel derived microporous crystall<strong>in</strong>e (yttria<br />

doped) zirconia material is prepared at lab scale. Both, titania and zirconia, sol-gel<br />

derived transition metal oxide materials are be<strong>in</strong>g <strong>in</strong>creas<strong>in</strong>gly studied due to a more<br />

controllable sol-gel synthesis us<strong>in</strong>g precursor modifiers. 78-80,82,83,110,115<br />

Crystall<strong>in</strong>e materials are desirable due to their expected thermal and chemical stability.<br />

However, state of the art silica layers are amorphous and conta<strong>in</strong> pore sizes <strong>in</strong> the range<br />

of 0.5 nm, whereas the titania and zirconia materials tend to crystallise at lower<br />

temperatures and might have larger particles than their silica counterparts, result<strong>in</strong>g <strong>in</strong><br />

larger pores. It is known that a mixture of titania and zirconia has a higher crystallisation<br />

29

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