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Dipl. Ing. Matthias Mayerhofer Technische Universität München ...

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48 Experiments<br />

12<br />

10<br />

8<br />

6<br />

4<br />

2<br />

0<br />

H_2<br />

0 200 400 600 800 1000<br />

Temperature (°C)<br />

Figure 21: Reduction of Nickel based catalyst<br />

The reactor was loaded with biomass and it started being heated up at 450°C under N2 flow, while<br />

good fluidization of the bed material with steam was achieved. Prior to the catalyst tests the gasifier<br />

was operated for ~2 hours to ensure stable operating conditions. In the beginning the product gas<br />

bypassed the catalytic test rig and was driven directly in the combustion chamber until steady state<br />

gas composition was reached. For the experiments of the iron based catalysts the temperature was<br />

raised at 750°C with dp=0.9 mbar and after an hour at these conditions with the gas passing<br />

through the catalyst, two tar samples were taken before and after the catalyst test rig. This procedure<br />

was repeated for all the different operating conditions that were about to be tested. The set<br />

point of dp=0.9 mbar and 800°C was tested twice to compare the tar measurements to the values<br />

obtained at the same point about two hours earlier. Finally, the pressure drop reached the lowest<br />

point dp=0.45 mbar. The effectiveness of the catalysts was tested in sulfur and chlorine containing<br />

environment. The operating conditions at which the samples were taken are presented in the following<br />

Table 5.<br />

The two additional gas compositions sampling points for the nickel based catalysts were ~12500<br />

1/h for dp=3 mbar and ~14500 1/h for dp=4 mbar.<br />

All the calculations were made for 40mL amount of catalyst. However, after the experiments with<br />

the iron based catalysts. A protective grid was placed on top of the catalyst amount inside the bed,<br />

to prevent the larger particles to be blown away, but for the finer ones it was impossible to avoid it.<br />

It is not known if the particles were blown away all at once in the beginning of the experiment or<br />

they were linearly decreased.<br />

Table 5: Different operating conditions of sampling points for iron based catalysts<br />

Sampling Points Temperature (°C) Pressure Drop (mbar) Space Velocity (1/h)<br />

1 750 0,9 6500<br />

2 800 0,9 6500<br />

3 860 0,9 6500<br />

4 800 0,45 4500<br />

5 800 1,5 8500<br />

6 800 2 10000

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