Using a two reactor system the direct catalytic conversion of methane to me
thyl formate is achieved. The two-step reaction sequence consists of the pa
rtial oxidation of methane to HCHO at 600-700 degrees C on a SiO2-based cat
alyst and the dimerisation of HCHO to methyl formate at 130-170 degrees C o
n amphoteric oxides such as TiO2, ZrO2 and Al2O3. By adopting a continuous
flow recycle reactor mode methyl formate yield up to 12% has been attained.
A preliminary analysis of the factors controlling activity and reaction pa
ttern of oxide catalysts in the dimerisation of formaldehyde is given. (C)
1998 Elsevier Science B.V. All rights reserved.