Methane was oxyhydrochlorinated over a promoted copper catalyst at tot
al pressures of up to 930 kPa. The catalyst yield increased three-fold
as pressure increased from 130 to 930 kPa for relative inlet concentr
ations of CH4:HCl:O-2 of 5:2:1. Selectivity to CH3Cl decreased as temp
erature and pressure increased; a higher percentage of polychlorinated
methanes and carbon oxides were produced at higher temperature and pr
essure. The pressure effect on CH3Cl selectivity remained even when co
rrected for the higher CH4 conversions at higher pressures. Decreasing
O-2 concentration in the inlet stream had no major effect on CH3Cl yi
eld, although less CO and CO2 were produced at higher temperatures. De
creasing HCL concentration increased CO2 selectivity at the expense of
chloromethane products.