• Title of article

    p-Xylene yield in fluid catalytic cracking products Original Research Article

  • Author/Authors

    Xinjin Zhao، نويسنده , , Terry G. Roberie، نويسنده , , K. Raj Rajagopalan، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 1996
  • Pages
    12
  • From page
    407
  • To page
    418
  • Abstract
    Both direct dealkylation of feed aromatics and hydrogen transfer chemistry contribute to the production of para-xylene in fluid catalytic cracking gasoline products. Based on laboratory scale FCC riser testing, it was found that catalysts containing high rare earth and low matrix activity are the preferred catalysts for high p-xylene yields in fluid catalytic cracking products. Aromatic feedstocks yield higher p-xylene than paraffinic feeds. Catalyst or feed change did not alter the distribution among the three xylene isomers. p-Xylene yield increases with conversion, but the o,m,p distribution does not change much with conversion.
  • Keywords
    FCC catalyst , para-Xylene , ZSM-5 , Rare earth , Equilibrium , Matrix effect , Riser
  • Journal title
    Applied Catalysis A:General
  • Serial Year
    1996
  • Journal title
    Applied Catalysis A:General
  • Record number

    1148543