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2007_6_Nr6_EEMJ

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Chirila et al /Environmental Engineering and Management Journal 6 (<strong>2007</strong>), 6, 549-553<br />

Conversia NO x<br />

[%]<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

600 °C<br />

800 °C<br />

1000 °C<br />

150 200 250 300 350 400 450 500 550 600 650<br />

Oxygen lack in synthetic gas mixture leaded to<br />

important changes of conversion curves for both<br />

propane oxidation and nitrogen oxides reduction.<br />

Fig.6 displays, reduction reaction was favored, while<br />

oxidation reaction has kept constant values in whole<br />

temperature range in which tests were performed. The<br />

higher values for oxidation reaction belong to<br />

perovskite sample calcined at 600 o C which proves to<br />

be again the most efficient perovskite in propane<br />

oxidation while LaMnO 3 sample calcined at 800°C<br />

presented lower values, almost negligible.<br />

Temperatura [°C]<br />

100<br />

100<br />

90<br />

90<br />

80<br />

Conversia C 3<br />

H 6<br />

[%]<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

600<br />

800<br />

1000<br />

150 200 250 300 350 400 450 500 550 600 650<br />

Temperatura [°C]<br />

Conversiea NO x<br />

[%]<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

600<br />

800<br />

1000<br />

150 200 250 300 350 400 450<br />

Temperature [°C]<br />

Fig. 4. Nitrogen oxides (a) and propene (b) conversion for<br />

the LaMnO 3 perovskite samples (propene 600 ppm, NOx<br />

600 ppm)<br />

Conversia NO x<br />

[%]<br />

Conversia C 6<br />

H 8<br />

[%]<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

600 °C<br />

800 °C<br />

1000 °C<br />

150 200 250 300 350 400 450<br />

Temperatura [°C]<br />

600 °C<br />

800 °C<br />

1000 °C<br />

150 200 250 300 350 400 450<br />

Temperatura [°C]<br />

Fig. 5. Nitrogen oxides (a) and propane (b) conversion for<br />

the LaMnO 3 perovskite samples (propane 400 ppm, NOx<br />

600 ppm, 5% O 2 )<br />

Conversia C 6<br />

H 8<br />

[%]<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

600 °C<br />

800 °C<br />

1000 °C<br />

150 200 250 300 350 400 450<br />

Temperatura [°C]<br />

Fig. 6. Nitrogen oxides (a) and propane (b) conversion for<br />

the LaMnO 3 perovskite samples (propane 400 ppm, NOx<br />

600 ppm)<br />

4. Conclusions<br />

The characterization by presented physicochemical<br />

methods confirmed that the synthesized<br />

samples are perovskite structures with a high<br />

homogeneity and crystallinity. The calcination<br />

process has leaded to three different symmetry of<br />

LaMnO 3 perovskite due to octahedral distortion.<br />

It is well known that perovskites present a<br />

certain small surface comparing with other catalysts.<br />

The BET specific surface of LaMnO 3 perovskite was<br />

found 24m 2 /g corresponding to the sample obtained at<br />

600 o C and decreases once with the calcinations<br />

temperature rising up to 2.5m 2 /g in the case of<br />

calcinations sample at 800 o C. The oxidation state of<br />

the manganese from the LaMnO 3 perovskite leaded to<br />

552

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