CPC C10G 11/05 (2013.01) [B01J 29/005 (2013.01); B01J 29/06 (2013.01); B01J 29/061 (2013.01); B01J 29/084 (2013.01); B01J 29/085 (2013.01); B01J 29/088 (2013.01); B01J 29/40 (2013.01); B01J 29/70 (2013.01); B01J 29/7007 (2013.01); B01J 29/7038 (2013.01); B01J 29/7057 (2013.01); B01J 29/80 (2013.01); B01J 29/83 (2013.01); B01J 29/85 (2013.01); B01J 35/0013 (2013.01); B01J 37/0009 (2013.01); B01J 37/0045 (2013.01); B01J 37/036 (2013.01); B01J 37/038 (2013.01); B01J 37/10 (2013.01); B01J 37/28 (2013.01); B01J 37/30 (2013.01); C10G 11/18 (2013.01); B01J 2029/062 (2013.01); B01J 2029/081 (2013.01); B01J 2229/36 (2013.01); B01J 2229/42 (2013.01); C07C 2527/14 (2013.01); C07C 2527/16 (2013.01); C07C 2527/167 (2013.01); C07C 2527/18 (2013.01); C07C 2527/182 (2013.01); C07C 2529/06 (2013.01); C07C 2529/08 (2013.01); C07C 2529/40 (2013.01); C07C 2529/70 (2013.01); C07C 2529/83 (2013.01); C07C 2529/85 (2013.01)] | 3 Claims |
1. A process for manufacturing an FCC catalyst comprising:
a. Adding, clay, boehmite and sodium stabilized basic colloidal silica to form a slurry;
b. Digesting the slurry with a monoprotic acid to a pH of less than 4.0;
c. Adding one or more zeolites to the slurry;
d. Adding polysilicic acid made separately and added inline;
e. Mixing the slurry and then destabilizing the slurry by raising the pH to above 4.0
f. Shaping and collecting the resulting FCC Catalyst.
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