Sulfated nanozirconia: an investigation on acid-base properties and n-butane isomerization activity.

Hydrated zirconia was synthesized by an organo-inorganic route employing surfactant and was sulfated using aqueous ammonium persulfate, followed by drying at 110 degrees C. The sample thus obtained was calcined at 600 degrees C to obtain sulfated zirconia and was characterized by several physicochemical methods. Crystallite sizes of sulfated zirconia were calculated from X-ray line broadening using the Debye-Scherer equation and were found to be in the range of 25 nm. When pretreated in air, the catalyst was found to exhibit butane isomerization activity at a temperature as low as 35 degrees C under atmospheric pressure. It showed conversion as high as 37% at 100 degrees C under normal pressure when pretreated in air, whereas nitrogen-pretreated catalyst showed zero activity under similar conditions. NH(3) and CO(2) temperature-programmed desorption studies on air- and helium-pretreated samples indicated that the catalyst surface changes appreciably during air pretreatment. Results on butane isomerization in conjunction with TPD studies suggest that zirconium-oxy sites play an important role in butane activation during the reaction.

Studies on platinum-promoted sulfated zirconia alumina: effects of pretreatment environment and carrier gas on n-butane isomerization and benzene alkylation activities.

A series of platinum-promoted sulfated zirconia alumina catalysts (SZA) with different amounts of platinum (0.5, 1, and 2 wt%) were synthesized. Two other catalysts were prepared by mechanically mixing different proportions of the Al-promoted sulfated zirconia with Pt/Al(2)O(3). The 650 degrees C calcined catalysts were characterized by N(2) adsorption/desorption (BET), TPR, and TPD analysis. Butane isomerization activity of the catalysts was studied at 270 degrees C, varying the pretreatment environment and carrier gases. Though the textural properties of the catalysts did not change significantly with platinum loading, the maximum surface area of 116 m(2)/g was exhibited by the catalyst with 1 wt% Pt loading. Under the studied reaction conditions, the air-pretreated catalysts (sulfated zirconia alumina (SZA) and platinated SZA) showed higher n-butane conversion than the N(2)-pretreated catalyst. However, nitrogen was a better carrier gas than H(2), CO(2) or air, and CO(2) and air deactivated the catalyst very fast. Unlike the platinated SZA catalysts, the mechanically mixed catalysts showed an induction phenomenon. A redox mechanism is suggested for butane isomerization over these catalysts. The catalyst SZA was also found to be active for alkylation of benzene with isopropanol, which gave 93% selectivity toward cumene.