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PDF file - Facultatea de Chimie şi Inginerie Chimică

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IRON DOPED CARBON AEROGEL AS CATALYST FOR PHENOL TOTAL OXIDATION<br />

We also studied the influence of the catalyst quantity and phenol initial<br />

concentration over the overall efficiency in the CWAO process. Results obtained<br />

in these cases are presented in figures 5 and 6. If we used a double catalyst<br />

quantity (0.2 g instead of 0.1 g) an increase with only 11% of the overall<br />

efficiency was observed, figure 5. Also a 10 times <strong>de</strong>crease of the phenol<br />

solution concentration led to an increase of 28% in overall efficiency value<br />

(figure 6).<br />

0.2 g<br />

0.1 g<br />

68.85<br />

In the same working conditions, on the Fe<br />

121<br />

(2+) -DCA catalyst we obtained<br />

overall efficiency values with 20% smaller than in case of Fe (3+) -DCA, fact<br />

that can be explained by its smaller surface area and partial coverage of<br />

iron/iron oxi<strong>de</strong> particles by graphitic clouds. The blank carbon aerogel sample<br />

had no activity in phenol oxidation process.<br />

76.39<br />

64 66 68 70 72 74 76 78<br />

Efficiency, (%)<br />

Figure 5. Catalyst quantity influence over the maximum overall efficiencies obtained<br />

in the phenol CWAO process, at constant air flow and constant temperature, 60 L/h,<br />

80°C, for Fe (3+) -DCA catalyst (Ci = 1000 mg phenol/dm 3 ).<br />

100 mg/L<br />

1 000 mg/L<br />

68.85<br />

88.39<br />

0 20 40 60 80 100<br />

Efficiency, (%)<br />

Figure 6. Phenol initial concentration influence over the overall efficiencies in the<br />

phenol CWAO process, at constant air flow and constant temperature, 60 L/h, 80°C,<br />

for Fe (3+) -DCA catalyst (0.1 g catalyst).

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