11.07.2015 Views

Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

SHOW MORE
SHOW LESS

Create successful ePaper yourself

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

OP-I-11KINETIC ASPECTS OF METHANE OXIDATION BY O 2 AND N 2 OOVER V 2 O 5 /SiO 2Yu.I. Pyatntsky, L.N. Raevskaya, A.I. BostanL.V. Pisarzhevsky <strong>Institute</strong> <strong>of</strong> Physical Chemistry, National Academy <strong>of</strong> Sciences <strong>of</strong> Ukraine,pr. Nauki, 31, 03087 Kiev, Ukraine, e-mail: yupyat@ukr.netNitrous oxide has been explored as an oxidant in <strong>the</strong> different catalytic reactions [1]including methane partial oxidation [2-4]. According to [4], <strong>the</strong> relationship between <strong>the</strong> rates<strong>of</strong> methane oxidation by O 2 and N 2 O over V 2 O 5 /SiO 2 depends on <strong>the</strong> reaction temperature.The aim <strong>of</strong> <strong>the</strong> present work is to study <strong>the</strong> mechanistic causes <strong>of</strong> <strong>the</strong> temperature affect on<strong>the</strong> relative rates <strong>of</strong> methane oxidation by oxygen and N 2 O.Steady-state catalytic runs were performed in fixed-bed quartz reactor (11 mm i.d.) over1.4%V 2 O 5 /SiO 2 prepared with chemical vapour deposition method and 3.6%V 2 O 5 /SiO 2prepared with <strong>the</strong> impregnation. The support was fumed silica A-380 (380 m 2 /g). The catalystgranules (0.5-1mm) were diluted with quartz granules to improve a temperature control. Inletconcentration <strong>of</strong> methane was 30 vol.%, N 2 O 30 vol.%, O 2 15 vol.%.Figs. 1a and 1b show <strong>the</strong> dependence <strong>of</strong> reaction selectivity on methane conversion over1.4%V 2 O 5 /SiO 2 catalyst. As seen, <strong>the</strong> selectivity dependencies for <strong>the</strong> main reaction products(formaldehyde and CO) on methane conversion are similar; <strong>the</strong> CH 2 O/CO ratio is in a littledependence on <strong>the</strong> oxidant.Fig.1a. 550 o CFig.1b. 575 o C100100Selectivity, %80604020CO(O2)CO2(O2)CH2O(O2)CH3OH(O2)CO(N2O)CO2(N2O)CH2O(N2O)CH3OH(N2O)Selectivity, %80604020CO(O2)CO2(O2)CH2O(O2)CH3OH(O2)CO(N2O)CO2(N2O)CH2O(N2O)CH3OH(N2O)00 2 4 6 8Conversion, %00 2 4 6 8 10 12 14Conversion, %The temperature increasing leads to inversion <strong>of</strong> <strong>the</strong> levels <strong>of</strong> <strong>the</strong> reaction rates (Fig. 2a).The obtained activation energies for N 2 O and O 2 are equal to 116 and 232 kJ/mole,correspondingly. The qualitatively same result was obtained for 3.6%V 2 O 5 /SiO 2 catalyst wi<strong>the</strong>nergy activation 158 kJ/mole for N 2 O and 227 kJ/mole for O 2 .Attempts to explain <strong>the</strong> different action <strong>of</strong> N 2 O and О 2 using different versions <strong>of</strong> <strong>the</strong>«two-step» mechanism <strong>of</strong> <strong>the</strong> Mars-van Krevelen type had no success. Quite satisfactoryexplanation can be made using <strong>the</strong> following scheme <strong>of</strong> <strong>the</strong> surface chain reaction mechanismlike mechanism proposed by Kazansky for CO oxidation over V 2 O 5 /SiO 2 catalyst [5]:46

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

Saved successfully!

Ooh no, something went wrong!