Methane partial oxidation by unsupported and silica supported iron phosphate catalysts - Influence of reaction conditions and co-feeding of water on activity and selectivity

Citation
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
Citations number
34
Categorie Soggetti
Physical Chemistry/Chemical Physics","Chemical Engineering
Journal title
JOURNAL OF CATALYSIS
ISSN journal
00219517 → ACNP
Volume
181
Issue
1
Year of publication
1999
Pages
104 - 112
Database
ISI
SICI code
0021-9517(19990101)181:1<104:MPOBUA>2.0.ZU;2-E
Abstract
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.