Production of C-4 hydrocarbons from Fischer-Tropsch synthesis in a follow bed reactor consisting of Co-Ni-ZrO2 and sulfated-ZrO2 catalyst beds

Fischer-Tropsch synthesis was performed in a fixed-bed microreactor over a single bed consisting of Co-Ni-ZrO2 catalyst as well as over a follow bed c onfiguration consisting of Co-Ni-ZrO2 and sulfated-ZrO2 catalyst beds for t he selective production of C-4 hydrocarbons. A maximum C-4 hydrocarbon sele ctivity of 14.6 wt.% was obtained using the single bed approach at 250 degr eesC and weight hourly space velocities (WHSV) of 15 h(-1). When a follow b ed approach was used, there was an impressive increase in the selectivity f or C-4 hydrocarbons to a maximum of 24 wt.% and that for iso-C-4 hydrocarbo ns to a maximum of 13.8 wt.% from 14.6 and 5.5 wt.%, respectively. However, there was a rapid deactivation of the sulfated-ZrO2 catalyst due to coking and sulfate reduction. (C) 2001 Elsevier Science B.V. All rights reserved.