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

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4 Results and discussion<br />

He Permeance (mol/s m 2 Pa)<br />

2.5E-08<br />

2.5�10 8<br />

2.0E-08<br />

2.0·10 8<br />

1.5E-08<br />

1.5·10 8<br />

1.0·10 8<br />

1.0E-08<br />

0.5·10 8<br />

5.0E-09<br />

0.0·10 8<br />

Helium Nitrogen<br />

0.0E+00<br />

0.0E+00<br />

-250 0 250 500 750 1000 1250<br />

Time after Steam (h)<br />

109<br />

5.0E-09<br />

5�10 -9<br />

4.0E-09<br />

4·10 -9<br />

3.0E-09<br />

3·10 -9<br />

2·10 -9<br />

2.0E-09<br />

1·10 -9<br />

1.0E-09<br />

0·10 -9<br />

Figure 76: He (♦) and N2 (■) permeance of a Ti0.5Zr0.5O2 membrane (#205) calc<strong>in</strong>ed at 600ºC be<strong>for</strong>e and<br />

after exposure to 3 bar of steam at 200ºC.<br />

N 2 Permeance (mol/s m 2 Pa)

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