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

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Results and Discussion 57<br />

er, the value of CH4 stabilized after a while, which indicated efficient steam reforming. It is probable<br />

that the catalyst is semi- deactivated very fast but then it becomes stable and it can work long-term.<br />

Either way the value of the methane at dp=0.9 and T=800°C is significantly lower than the value<br />

obtained from the iron based catalysts at the same conditions.<br />

Wet CH₄ composition Vol (%)<br />

4,0<br />

3,5<br />

3,0<br />

2,5<br />

2,0<br />

1,5<br />

1,0<br />

0,5<br />

0,0<br />

-0,5<br />

14:35 14:51 15:08 15:25 15:42 15:59<br />

-1,0<br />

7.3 Tar Analysis<br />

Figure 27: Change of wet gas composition of CH4 with time<br />

The Table 9 presents the classification of tars. Class 1 one tars can’t be detected by the GC/FID.<br />

Table 9: Classification of tars<br />

Class 2 Class 3 Class 4 Class 5<br />

Phenol toluene napthalene Fluoranthen<br />

o-Kresol o-Xyl/Styr Biphenyl Pyren<br />

m-Kresol Inden Fluoren<br />

Anthracen<br />

Time<br />

Iron based catalysts:<br />

It is expected that as the char is built up inside the gasifier during the experiment it acts as an in<br />

situ catalyst, so as time passed the tar produced decreased. In the following<br />

Figure 28, it is seen that as the sampling was made as the time passed there is a clear decrease in<br />

for different higher hydrocarbon molecules. The following figure is referred to each tar class compound<br />

that was detected by the GC/FID, an unknown compound that is likely benzene is not included<br />

in the graph, and the total amount of unknown compounds produced by the gasifier.

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