On sulfated titania prepared by gelling titanium alkoxide with sulfuric acid, isobutene oligomerization was carried out under different operating conditions. Under severe conditions [temperature 140 °C, pressure 600 psi and weight hourly space velocity (WHSV) of 2.5 h −1], the catalyst reached 100% isobutene conversion and selectivity for C 12 = and C 18 = olefins of 54 and 39%, respectively. Meanwhile, under soft conditions (28 °C, 100 psi and 10 h −1), conversion decreased from an initial value of 55–25% after 30 h on stream, while the selectivity for C 8 = increased from 42 to 60%. After 90 h on stream, catalyst activity was recovered by introducing nitrogen into the feed and the conversion then reached 90%. These results show that by varying the operating conditions over a sulfated titania catalyst, isobutene oligomerization can be controlled to the desired C 8 = or C 12 = olefin yield.