PATENTS
Gases, such as water gas, containing CO and H2 in proportion of 1:1 to 1:1.25 are first converted over Fe catalyst (Fe + Cu) at 225°-250° to olefin-rich hydrocarbons according to 2 CO + H2=CO2 + (CH2)x. The residual gas rich in H2, after separation of the liquid hydrocarbons and CO2 and correction of the gas composition to CO:H2=1:2, is used for the production of more liquid hydrocarbons at 185°-200° over a Co or Ni catalyst according to CO + 2 H2=H2O + (CH2)x. The Fe catalyst is put into operation with a S-free gas: after reaching its highest efficiency (after about 5 days) the Fe catalyst has become insensitive to S and can then be further operated with a S-containing gas. |