The methane oxidation by oxygen is carried out on catalytic systems Mo
-V-Cu-P-O, W-Pb-B-O and V-Zn-Bi-B-O containing 1% Pt or Pd. The design
of reactor makes possible to decrease the deep oxidation rate and lea
ds to increase of oxygenates yield. Thermodynamic analysis of methane
and sulphur interaction with calculation of all product concentrations
at molar relationship S-2:CH4 from 0 to 5, temperatures in the range
from 750 to 1500 K and pressures from 1 to 100 atm has been carried ou
t. The possibility of interaction between methane and sulphur forming
products of partial oxidation and condensation was confirmed experimen
tally. (C) 1998 Elsevier Science B.V. All rights reserved.