Petroleum Processing and Petrochemicals ›› 2020, Vol. 51 ›› Issue (12): 33-40.
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Abstract: ZrO2-Al2O3 was prepared by co-precipitation method, SO42-/ZrO2-Al2O3 was prepared by impregnating ZrO2-Al2O3 with sulfuric acid solution, and Pt-SO42-/ZrO2-Al2O3 solid superacid catalyst was prepared by impregnating platinum chloride solution by equal volume method. BET, XRF, XRD, NH3-TPD, Py-IR techniques were used to characterize the pore structure, crystal phase structure, and acid properties of different Pt- SO42-/ZrO2-Al2O3 catalysts. The n-hexane was used as the probe material to evaluate the conversion and isomerization activity of Pt-SO42-/ZrO2-Al2O3 catalysts. The results showed that when the content of Al2O3 was 5%, the roasting temperature of SO42-/ZrO2-Al2O3 was 650 ℃, and the sulfuric acid added was 15%, the tetragonal phase zirconia content of Pt- SO42-/ZrO2-Al2O3 catalyst was the highest, the total acid content and the amount of B acid were the most, and both the conversion and isomerization rate of n-hexane were the highest. At 2.0 MPa, 240 ℃, volumetric space velocity of 1.0 h-1, and hydrogen-to-oil volume ratio of 700, the conversion of n-hexane on Pt-SO42-/ZrO2-Al2O3 catalyst was 88.72%, the isomerization rate was 80.07%.
Key words: platinum, zirconia, alumina, solid superacid, isomerization, n-hexane
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