12.07.2015 Views

Integrating Structure Control over Multiple Length Scales in Porous ...

Integrating Structure Control over Multiple Length Scales in Porous ...

Integrating Structure Control over Multiple Length Scales in Porous ...

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

diameter of 5 mm. The catalyst bed was fixed by quartz wool plugs. The quartz U-tube wasplaced <strong>in</strong> a tubular oven (Carbolite Furnaces) and connected to a mass flow controller(Brooks, 5895E) and gas chromatograph (Hewlett Packard 6890N, equipped with GS GasProcolumn and capable of automatic gas sampl<strong>in</strong>g) by Swagelok coupl<strong>in</strong>gs with Teflon O-r<strong>in</strong>gs.A manometer was used to monitor the pressure before the catalyst bed, which was constant at0 barg dur<strong>in</strong>g all experimental conditions.Each catalytic experiment consisted of two cycles from 200 to 600°C and back with aheat<strong>in</strong>g and cool<strong>in</strong>g ramp of 2.5 °C m<strong>in</strong> -1 . Prior to each run, the catalyst was pre-treated at 200°C <strong>in</strong> the reaction mixture of 1 vol% CH 4 , 4 vol% O 2 <strong>in</strong> balance He. The total flow dur<strong>in</strong>geach run was 130 mL m<strong>in</strong> -1 . The experimental conditions were set so that the conversionnever reached 100%. Carbon dioxide was the only reaction product detected. Blancexperiments demonstrated that the diluent, α-Al 2 O 3 was not active under the chosenconditions.

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!