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

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5 Conclusions and recommendations<br />

5 Conclusions and recommendations<br />

First, this chapter <strong>in</strong>cludes the conclusions of the studied zeolite materials. The basic aim<br />

was to prepare zeolite material that could separate gasses by molecular siev<strong>in</strong>g.<br />

Recommendations on the zeolite materials are discussed to achieve this goal.<br />

Second, the results on sol-gel derived TiO2-ZrO2 sols, bulk materials, layers and<br />

membranes are summarised and related to the preparation of the TiO2-ZrO2 gas<br />

separation membrane goal. Additionally, suggestions <strong>for</strong> further research are outl<strong>in</strong>ed to<br />

achieve <strong>in</strong>dustrial goals.<br />

8-r<strong>in</strong>g Deca-dodecasil 3R and 6-r<strong>in</strong>g Dodecasil 1H zeolite materials<br />

Deca-dodecasil 3R (DDR) hydrothermal synthesis is complex and <strong>for</strong>med zeolite<br />

mixtures of DDR with DOH or SGT (Dodecasil 1H or Sigma 2). The synthesis of DDR<br />

as a potential CO2/N2 separation membrane material was unsuccessful. Further syntheses<br />

with vary<strong>in</strong>g gel compositions of nutrients from several suppliers and reaction conditions<br />

should be per<strong>for</strong>med <strong>in</strong> order to understand how to prepare s<strong>in</strong>gle phase DDR.<br />

Dodecasil 1H (DOH) crystal synthesis, structure direct<strong>in</strong>g agent (SDA) free synthesis and<br />

SDA-free DOH by means of post synthesis treatments were per<strong>for</strong>med to prepare allsilica<br />

zeolite material with pores <strong>in</strong>accessible to gasses with the exception of gasses with<br />

a k<strong>in</strong>etic diameter of H2 or smaller.<br />

DOH can be synthesised under standard conditions (Teflon l<strong>in</strong>ed autoclave heated<br />

under static conditions, 200°C, gel composition: 100SiO2:9-11ADA:70-270EN:3000-<br />

7400H2O <strong>for</strong>m<strong>in</strong>g crystals >100 µm). Chang<strong>in</strong>g the synthesis conditions from static to<br />

dynamic by means of autoclave rotation or stirr<strong>in</strong>g the gel <strong>in</strong> situ to obta<strong>in</strong> a more<br />

homogeneous gel mixture reduces the DOH crystallisation time from 21 days to 4 days<br />

coupled with a decrease <strong>in</strong> crystal size. The DOH crystal size can also be reduced by<br />

ag<strong>in</strong>g the gel at 80ºC <strong>for</strong> several hours be<strong>for</strong>e hydrothermal crystallisation at 200ºC. The<br />

DOH nucleation and growth can be decoupled.<br />

The DOH crystal size can be reduced to th<strong>in</strong> hexagonal plates with sizes <strong>in</strong> the order of<br />

10 µm be<strong>in</strong>g too large <strong>for</strong> membrane <strong>for</strong>mation or to act as seeds <strong>for</strong> the layer <strong>for</strong>mation<br />

by means of the secondary growth of DOH nuclei. The DOH crystal size might be<br />

synthesised smaller by means of further crystallisation optimisation. This might be<br />

accomplished by chang<strong>in</strong>g the gel composition, ag<strong>in</strong>g of the gel and reaction condition<br />

such as the heat<strong>in</strong>g ramp and stirr<strong>in</strong>g/rotat<strong>in</strong>g conditions.<br />

Secondary growth of DOH crystals <strong>in</strong> gel composition with the absence of SDA<br />

was unsuccessful. Low DOH yield was obta<strong>in</strong>ed us<strong>in</strong>g a small amount of SDA <strong>in</strong> the gel<br />

composition. These synthesised DOH crystals have a ~75% SDA cage occupancy. SDAfree<br />

DOH synthesis by means of seeded synthesis was not obta<strong>in</strong>ed. This proposed<br />

110

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