Page 218 - Fluid Catalytic Cracking Handbook
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186   Fluid Catalytic Cracking Handbook

    is particularly useful where the reactor temperature is already
    maximized due to a metallurgy constraint.
  » Increasing catalyst to oil ratio. The catalyst to oil ratio can be
    increased through several knobs including: reducing the FCC feed
    preheat temperature, optimizing the stripping and dispersion steam
    rate, and using a catalyst that deposits less coke on the catalyst,
  Reduction of the catalyst/hydrocarbon time in the riser, coupled with
 the elimination of post-riser cracking, reduces the saturation of the
 "already produced olefins" and allows the refiner to increase the
 reaction severity. The actions enhance the olefin yields and still operate
 within the wet gas compressor constraints. Elimination of post-riser
 residence time (direct connection of the reactor cyclones to the riser)
 or reducing the temperature in the dilute phase virtually eliminates
 undesired thermal and nonselective cracking. This reduces dry gas and
 diolefin yields.
  Adding ZSM-5 catalyst additive is another process available to the
 refiner to boost production of light olefins. ZSM-5 at a typical con-
 centration of 0.5 to 3.0 wt% is used in a number of FCC units to
 increase the gasoline octane and light olefins. As part of the cracking
 of low octane components in the gasoline, ZSM-5 also makes C 3, C 4,
 and C 5 olefins (see Figure 6-2). Paraffinic feedstocks respond the most
 to ZSM-5 catalyst additive.

 Gasoline

  FCC gasoline has always been the most valuable product of a cat
 cracker unit. FCC gasoline accounts for about 35 vol% of the total
 U.S. gasoline pool. Historically, the FCC has been run for maximum
 gasoline yield with the highest octane.

 Gasoline Yield
  For a given feedstock, gasoline yield can be increased by:

  • Increasing catalyst-to-oil ratio by decreasing the feed preheat
    temperature
  • Increasing catalyst activity by increasing fresh catalyst addition
    or fresh catalyst activity
  • Increasing gasoline end point by reducing the main column top
    pumparound rate
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