Page 91 - Fluid Catalytic Cracking Handbook
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68  Fluid Catalytic Cracking Handbook

    desalter and carry over salts with the desalted crude. Slop can be
    fed to the coker or FCC main fractionator with the same result,
  « Purchased FCC feedstock can be exposed to salt water as ballast,
  * The me of atomizing steam and/or water that contain sodium. Just
    about every refiner practices some type of feed atomization using
    either steam or water. The steam or water can contain varying
    amounts of sodium depending on the quality of water treatment
    used in the refinery.

  Another problem associated with sodium appears in the form of
 sodium chloride. Chlorides tend to reactivate aged metals by redis-
 tributing the metals on the equilibrium catalyst and allowing them to
 cause more damage.

 Other Metals
  Iron is usually present in FCC feed as tramp iron and is not cata-
 lytically active. Tramp iron refers to various corrosion by-products
 from upstream processing and handling.
  Copper is as active as nickel, but the feed contains much less of it.

 Summary
  The metals in the FCC feed have many deleterious effects. Nickel
 causes excess hydrogen production, forcing eventual loss in the con-
 version or thruput. Both vanadium and sodium destroy catalyst struc-
 ture, causing losses in activity and selectivity. Solving the undesirable
 effects of metal poisoning involves several approaches:
  * Increasing the makeup rate of fresh catalyst
  * Employing some type of metal passivation
  * Adding good quality equilibrium catalysts to flush the metals
  * Employing demetalization technology to remove metals from the
    equilibrium catalyst
  Both demetalization and passivation technology are addressed in
 Chapter 3.




  The typical refinery laboratory is not equipped to conduct PONA
 and other chemical analyses of the FCC feed on a routine basis.
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