摘要 |
<p>A process for converting synthesis gas to higher hydrocarbons, at an elevated temperature and pressure, comprising continuously introducing a synthesis gas feed stream comprising 0.1 to 50 % by volume of carbon dioxide into a continuous stirred reactor system comprising a reactor vessel containing a suspension of a solid particulate Fischer-Tropsch catalyst suspended in a liquid medium wherein the solid particulate Fischer-Tropsch catalyst is stable in the presence of carbon dioxide.</p> |