Process for fluid catalytic cracking and hydrocracking hydrocarbons

Patent metadata

Field	Value
Publication number	US-9394496-B2
Application number	US-201414248985-A
Country	US
Kind code	B2
Filing date	Apr 9, 2014
Priority date	Apr 9, 2014
Publication date	Jul 19, 2016
Grant date	Jul 19, 2016

Abstract

A process and apparatus for recovering cycle oil from FCC CSO is described. By feeding the additional cycle oil to a hydrocracking unit additional diesel, naphtha and petrochemical feedstock may be obtained. The additional cycle oil is obtained by vacuum separation of the CSO. The described process and apparatus can provide additional recovery for a refiner.

First claim

The invention claimed is:

1. A process for catalytically cracking hydrocarbons comprising:
feeding a hydrocarbon feed stream to an FCC reactor and contacting said hydrocarbon feed stream with catalyst to catalytically crack said hydrocarbon feed stream to provide a cracked stream;
disengaging said catalyst from said cracked stream;
fractionating said cracked stream into products including a slurry oil stream from a bottom of a main fractionation column;
separating said slurry oil stream into a cycle oil process stream and a heavy stream under vacuum pressure in a separator, comprising condensing a separator overhead stream from an overhead of said separator, separating said condensed overhead stream in a receiver; and taking said cycle oil process stream from a bottom of said receiver; and
refluxing said cycle oil process stream to said main fractionation column.

2. The process of claim 1 further comprising hydrocracking a cycle oil stream from said main fractionation column.

3. The process of claim 1 further comprising heating said slurry oil stream before the separation step.

4. The process of claim 1 further comprising pulling a vacuum on a receiver overhead stream from said receiver and feeding it to a drain drum.

5. The process of claim 2 further comprising withdrawing a cycle oil stream from said main fractionation column, hydrocracking a portion of said cycle oil stream and returning another portion of said cycle oil stream to main fractionation column.

6. The process of claim 5 further comprising withdrawing said cycle oil stream from said main fractionation column from an outlet that is at a higher elevation than an inlet of said cycle oil process stream refluxed to said main fractionation column.

7. The process of claim 5 further comprising cooling said another portion of said cycle oil stream before it is returned to said main fractionation column.

8. The process of claim 2 further comprising recovering a diesel stream and/or an aromatics stream from said hydrocracked cycle oil stream.

9. A process for catalytically cracking hydrocarbons comprising:
feeding a hydrocarbon feed stream to an FCC reactor and contacting said hydrocarbon feed stream with catalyst to catalytically crack said hydrocarbon feed stream to provide a cracked stream;
disengaging said catalyst from said cracked stream;
fractionating said cracked stream into products including a slurry oil stream from a bottom of a main fractionation column;
separating said slurry oil stream into a cycle oil process stream and a heavy stream under vacuum pressure in a separator, comprising condensing a separator overhead stream from an overhead of said separator; separating said condensed overhead stream in a receiver and taking said cycle oil process stream from a bottom of said receiver; and
refluxing said cycle oil process stream to said main fractionation column; and
hydrocracking a cycle oil stream from said main fractionation column.

10. The process of claim 9 further comprising pulling a vacuum on a receiver overhead stream from said receiver and feeding it to a drain drum.

11. The process of claim 9 further comprising withdrawing a cycle oil stream from said main fractionation column, hydrocracking a portion of said cycle oil stream and returning another portion of said cycle oil stream to main fractionation column.

12. The process of claim 11 further comprising withdrawing said cycle oil stream from said main fractionation column from an outlet that is at a higher elevation than an inlet of said cycle oil process stream refluxed to said main fractionation column.

13. The process of claim 9 further comprising recovering a diesel stream and/or an aromatics stream from said hydrocracked cycle oil stream.

14. A process for catalytically cracking hydrocarbons comprising:
feeding a hydrocarbon feed stream to an FCC reactor and contacting said hydrocarbon feed stream with catalyst to catalytically crack said hydrocarbon feed stream to provide a cracked stream;
disengaging said catalyst from said cracked stream;
fractionating said cracked stream into products including a slurry oil stream from a bottom of a main fractionation column;
separating said slurry oil stream into a cycle oil process stream and a heavy stream under vacuum pressure in a separator, comprising condensing a separator overhead stream from an overhead of said separator, separating said condensed overhead stream in a receiver and taking said cycle oil process stream from a bottom of said receiver;
refluxing said cycle oil process stream to said main fractionation column;
hydrocracking a cycle oil stream from said main fractionation column; and
recovering a diesel stream and/or an aromatics stream from said hydrocracked cycle oil stream.

15. The process of claim 14 further comprising withdrawing said cycle oil stream from said main fractionation column, hydrocracking a portion of said cycle oil stream and returning another portion of said cycle oil stream to main fractionation column.

Assignees

• Uop Llc

Inventors

• Qafisheh Jibreel A
• Cabanaw Boyd E
• Zhu Xin X

Classifications

• C10G2400/04

  Diesel oil · CPC title

• C10G2300/4081

  Recycling aspects · CPC title

• C10G2400/30

  Aromatics · CPC title

• C10G69/04 Primary

  including at least one step of catalytic cracking in the absence of hydrogen · CPC title