US2015065774A1PendingUtilityA1

Fluid catalytic cracking system and process

Assignee: UOP LLCPriority: Dec 29, 2008Filed: Nov 6, 2014Published: Mar 5, 2015
Est. expiryDec 29, 2028(~2.4 yrs left)· nominal 20-yr term from priority
C10G 2400/20B01J 29/084C10G 51/026B01J 29/80B01J 2208/025C10G 2300/301C07C 4/06B01J 38/30B01J 29/40C10G 51/06C10G 2300/107C07C 2529/48C10G 2300/1074B01J 8/26B01J 29/90C10G 51/00
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Claims

Abstract

One exemplary embodiment can be a fluid catalytic cracking system. Generally, the fluid catalytic cracking system includes a first reaction vessel and a second reaction vessel. The first reaction vessel may contain a first catalyst having pores with openings greater than about 0.7 nm and a second catalyst having pores with smaller openings than the first catalyst. What is more, the second reaction vessel may contain the second catalyst. Generally, at least a portion of the second catalyst is directly communicated with the first reaction vessel.

Claims

exact text as granted — not AI-modified
1 . A process for generating propylene in a system, comprising:
 A) communicating a first reaction vessel with a regeneration zone and a second reaction vessel wherein the first reaction vessel contains a first catalyst having pores with openings greater than about 0.7 nm and a second catalyst having pores with smaller openings than the first catalyst, and the second reaction vessel contains only the second catalyst for catalyzing at least one reaction.   
     
     
         2 . The process according to  claim 1 , wherein the second reaction vessel is at a temperature of about 550° to about 680° C. 
     
     
         3 . The process according to  claim 1 , further comprising communicating a spent second catalyst from the second reaction vessel to the first reaction vessel which, in turn, communicates the spent second catalyst with the regeneration zone.

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