| 摘要 |
A process for the production of liquid hydrocarbon products by passing, at elevated temperature and pressure, synthesis gas and a fluidizing liquid through a fluidized catalytic bed within a reaction zone, characterized in that the fluidized catalytic bed is an aggregative fluidized catalytic bed comprising a particulate Fischer-Tropsch catalyst having a density of greater than 4,000 kg/m<3>.
|
