• Title of article

    Isopentane dehydrogenation on Pt-Sn catalysts supported on Al-Mg-O mixed oxides: effect of Al/Mg atomic ratio Original Research Article

  • Author/Authors

    H Armend?riz، نويسنده , , A Guzm?n، نويسنده , , J.A Toledo، نويسنده , , M.E Llanos، نويسنده , , A V?zquez، نويسنده , , G Aguilar-R??os، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2001
  • Pages
    12
  • From page
    69
  • To page
    80
  • Abstract
    A series of Mg-Al-O supports was prepared by the coprecipitation method at constant pH. The Al/Mg atomic ratio ranged from 2.06 to 4.9. The physico-chemical, as well as the surface and structural properties of the synthesized materials were strongly dependent on the Al/Mg atomic ratio. In solids with an Al/Mg atomic ratio higher than 2, a support with a mixture of Al2O3 and MgAl2O4 phases was obtained. In all the supports a non stoichiometric magnesium aluminate spinel structure (MgAl2+xO4+(3/2)x) was not detected. The supports were impregnated with Pt and Sn (0.6 and 1.2 wt.%, respectively). The resulting catalysts were evaluated in the isopentane dehydrogenation reaction at 550°C and atmospheric pressure. On the Pt-Sn catalysts which were prepared with aluminum rich supports (Al/Mg=2.4 and 4.9), TPD-H2 results showed the presence of Pt particles (unalloyed and tin alloyed) deposited in both Al2O3 and MgAl2O4 phases. A stronger Pt-support interaction on MgAl2O4 phase than on Al2O3 phase was observed. The Pt-Sn catalyst impregnated on pure MgAl2O4 showed the maximum selectivity to isoamilenes. The high Al2O3 content supports (Al/Mg>3) bring about a higher light olefins (C2–C4) production, which promotes the coke formation. This process finally accelerated the catalyst deactivation. This is explained by the higher acidity of alumina compared with magnesium aluminate.
  • Keywords
    Platinum , TIN , Magnesium aluminate , Isopentane dehydrogenation , Alumina
  • Journal title
    Applied Catalysis A:General
  • Serial Year
    2001
  • Journal title
    Applied Catalysis A:General
  • Record number

    1150658