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

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2 Theoretical background<br />

membranes (Figure 4). The supported zeolite membranes are by far the most extensively<br />

studied. The most <strong>in</strong>vestigated support material is α-alum<strong>in</strong>a. Sta<strong>in</strong>less Steel, γ-alum<strong>in</strong>a<br />

and titania are examples of other support materials suitable <strong>for</strong> zeolite membranes. 43,44<br />

A B C<br />

Figure 4 Schematic draw<strong>in</strong>g of polymer – zeolite composite membrane (A), self supported zeolite membrane<br />

(B) and a (α-Al2O3) supported zeolite membrane (C).<br />

Ideal zeolite membranes are gastight directly after the hydrothermal crystallisation. A<br />

common nitrogen permeation test is applied to test the gas tightness. Zeolite membranes<br />

must be activated, or <strong>in</strong> more detail, the water and organics, such as structure direct<strong>in</strong>g<br />

agents (SDA’s), must be removed <strong>in</strong> order to obta<strong>in</strong> an open and <strong>in</strong>terconnected<br />

microporous structure. Remov<strong>in</strong>g these SDA’s can be done via:<br />

o Chemical leach<strong>in</strong>g<br />

o Ion exchange techniques which is applicable <strong>for</strong> the larger pore zeolites (e.g. 12r<strong>in</strong>g)<br />

o Thermal treatment at specified temperatures, heat<strong>in</strong>g rate, atmosphere and<br />

duration. The heat<strong>in</strong>g rate and cool<strong>in</strong>g rate can be key factors <strong>for</strong> remov<strong>in</strong>g SDA<br />

without destroy<strong>in</strong>g the zeolite layers due to different expansion coefficient of<br />

templated and template free zeolite structures<br />

o Low temperature ozone treatment. 43<br />

The thermal expansion coefficient difference of the membrane layer and support can<br />

cause stress, undesired cracks and peel<strong>in</strong>g off. Porous <strong>in</strong>termediate layers or th<strong>in</strong> zeolite<br />

layers with randomly ordered crystals are recommended <strong>in</strong> order to reduce the thermal<br />

stresses.<br />

The preparation methods <strong>for</strong> different supported zeolite membranes are known and<br />

<strong>in</strong>clude (a) <strong>in</strong> situ hydrothermal synthesis <strong>in</strong> the presence of a substrate, (b) “dry or wet<br />

gel conversion method” and (c) the application of two stage (phase) secondary growth<br />

methods. The seeds <strong>in</strong> the secondary growth methods can be colloidal zeolites that are<br />

deposited by dip coat<strong>in</strong>g, sp<strong>in</strong> coat<strong>in</strong>g or sputter<strong>in</strong>g 38 .<br />

17

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