Methane partial oxidation by unsupported and silica supported iron phosphate catalysts - Influence of reaction conditions and co-feeding of water on activity and selectivity
Go. Alptekin et al., Methane partial oxidation by unsupported and silica supported iron phosphate catalysts - Influence of reaction conditions and co-feeding of water on activity and selectivity, J CATALYSIS, 181(1), 1999, pp. 104-112
The partial oxidation of methane to methanol and formaldehyde by molecular
oxygen has been investigated over crystalline and silica supported FePO4 at
a pressure of 1 atm and in the temperature range of 723-973 K. The quartz
phase of FePO4, as well as silica supported FePO4 prepared by impregnation
(5 wt%), were examined in a continuous how reactor, Experiments carried out
over FePO4 show high selectivity to formaldehyde at low conversion and sug
gest that formaldehyde is the primary reaction product, but selectivity dec
reased rapidly as conversion was increased. The highest space-time yield of
formaldehyde observed for this catalyst was 59 g/kg(cat)-h. Above 5% metha
ne conversion,carbon oxides were the only products. For silica-supported Fe
PO4, formaldehyde selectivity did not fall off rapidly, exhibiting a formal
dehyde selectivity of 12% Bt about 10% conversion (STY = 285 g/kg(cat)-h).
Quantifiable yields of methanol were observed at very low conversion levels
, i.e. below 3% (STY = 11 g/kg(cat)-h). Addition of steam (up to 0.1 atm pa
rtial pressure) into the feed stream increased the selectivity to methanol
( similar to 25 g/kg cat/h with up to 3% selectivity) and formaldehyde (sim
ilar to 487 g/kg cat/h with up to 94% selectivity) for the silica-supported
FePO4 catalyst. Steam addition had little effect on catalyst: activity. Ch
aracterization results indicate the presence of FePO4, as well as fivefold
coordinate Fe3+ in silica supported catalyst samples, and this species is p
roposed to be responsible for methane activation. After catalysis in the pr
esence of steam, the fivefold coordinate iron is present, but a significant
fraction of the FePO4 has been reduced to Fe2P2O7. Enhanced selectivity in
the presence of steam is attributed in part to the ease of the reversible
formation of surface hydroxyl groups (P-OH) from pyrophosphate (P-O-P) grou
ps. (C) 1999 Academic Press.