Two novel designs of FCC riser regeneration are proposed in this work.
To improve the regeneration performance of a single riser regenerator
, the first design allows the regenerating air to be separately suppli
ed at several different levels in the riser. Simulations based on the
riser regeneration model previously developed by us show that this met
hod provides good operation performance with improved flexibility and
stability, higher solids inventory, and longer solids residence time.
By properly adjusting the air flow rates and the regenerated catalyst
recycle ratio, this multiple air supply riser regenerator can meet the
specifications of most industrial units: reducing the carbon content
on the regenerated catalyst to less than 0.1 wt % and controlling the
riser temperature under 730 degrees C. The second design is a two-stag
e riser FCC regenerator, which connects two riser regenerators in seri
es. This novel design combines the advantages of both the riser regene
ration and the conventional two-stage turbulent bed regeneration. It a
lso provides significant advantages over the single riser regenerator:
operating the second riser at high temperature without catalyst hydro
thermal deactivation and greatly increased regeneration efficiency and
operation flexibility. Both novel regeneration technologies have now
been patented in China and are being incorporated in the design of the
FCCU of the SINOPEC Changling Refinery.