Process and apparatus for producing and recycling cracked hydrocarbons

Patent metadata

Field	Value
Publication number	US-9567537-B2
Application number	US-201514642990-A
Country	US
Kind code	B2
Filing date	Mar 10, 2015
Priority date	Mar 10, 2015
Publication date	Feb 14, 2017
Grant date	Feb 14, 2017

Abstract

A process and apparatus is for recycling LCO and/or HCO to an FCC unit to recover additional distillate. Spent catalyst recycle in the FCC unit may be used to improve distillate yield. A hydroprocessing zone may saturate cycle oil aromatics for cracking in an FCC unit. The recycle cracked stream may be recycled to a downstream hydroprocessing zone to avoid a first hydroprocessing zone for hydrotreating feed to the FCC unit. Additional recovery of cycle oil for recycle is obtained by heating slurry oil prior to vacuum separation.

First claim

The invention claimed is:

1. An apparatus for catalytically cracking hydrocarbons comprising:
an FCC reactor for contacting a hydrocarbon feed stream with catalyst to provide a cracked stream;
a main fractionation column in downstream communication with said FCC reactor for fractionating said cracked stream into products including a slurry oil stream;
a slurry heater in downstream communication with a main outlet in a bottom of said main fractionation column for heating said slurry oil stream;
a vacuum separator in downstream communication with said slurry heater for separating said heated slurry oil stream into a cycle oil stream and a heavy stream under vacuum pressure;
a receiver in communication with a separator overhead line of said vacuum separator;
a vacuum generation device in communication with a receiver overhead line of said receiver; and
a receiver bottoms line of said receiver for providing a recycle stream.

2. The apparatus of claim 1 wherein said slurry heater is a heat exchanger.

3. The apparatus of claim 2 further comprising a loop heater in communication with said slurry heater for heating a heat exchange fluid for said slurry heater.

4. The apparatus of claim 3 wherein said loop heater is a fired heater or an electric heater.

5. The apparatus of claim 2 wherein said slurry heater is a shell and tube heat exchanger and said tube is in communication with said bottom outlet.

6. The apparatus of claim 1 wherein said FCC reactor is in downstream communication with said receiver bottoms line.

7. The apparatus of claim 6 wherein a hydroprocessing unit is in downstream communication with said receiver bottoms line.

8. The apparatus of claim 7 wherein said FCC reactor is in downstream communication with said hydroprocessing unit.

9. The apparatus of claim 1 wherein said vacuum separator is a vacuum fractionation column.

10. An apparatus for catalytically cracking hydrocarbons comprising:
an FCC reactor for contacting a hydrocarbon feed stream with catalyst to provide a cracked stream;
a main fractionation column in downstream communication with said FCC reactor for fractionating said cracked stream into products including a slurry oil stream;
a slurry heater comprising a heat exchanger in downstream communication with a main outlet in a bottom of said main fractionation column for heating said slurry oil stream;
a vacuum separator in downstream communication with said slurry heater for separating said heated slurry oil stream into a cycle oil stream and a heavy stream under vacuum pressure;
a loop heater in communication with said slurry heater for heating a heat exchange fluid for said slurry heater;
a receiver in communication with a separator overhead line of said vacuum separator;
a vacuum generation device in communication with a receiver overhead line of said receiver; and
a receiver bottoms line of said receiver for providing a recycle stream.

11. The apparatus of claim 10 wherein said loop heater is a fired heater or an electric heater.

12. The apparatus of claim 10 wherein said slurry is a shell and tube heat exchanger and said tube is in communication with said bottom outlet.

13. The apparatus of claim 10 wherein said FCC reactor is in downstream communication with said receiver bottoms line.

14. The apparatus of claim 13 wherein a hydroprocessing unit is in downstream communication with said receiver bottoms line.

15. The apparatus of claim 14 wherein said FCC reactor is in downstream communication with said hydroprocessing unit.

16. An apparatus for catalytically cracking hydrocarbons comprising:
an FCC reactor for contacting a hydrocarbon feed stream with catalyst to provide a cracked stream;
a main fractionation column in downstream communication with said FCC reactor for fractionating said cracked stream into products including a slurry oil stream;
a slurry heater in downstream communication with a main outlet in a bottom of said main fractionation column for heating said slurry oil stream;
a vacuum fractionation column in downstream communication with said slurry heater for separating said heated slurry oil stream into a cycle oil stream and a heavy stream under vacuum pressure;
a receiver in communication with an overhead line of said vacuum fractionation column;
a receiver bottoms line of said receiver for providing a recycle stream; and
said FCC reactor in downstream communication with said receiver bottoms line.

17. The apparatus of claim 16 further comprising a hydroprocessing unit in downstream communication with said receiver bottoms line and said FCC reactor in downstream communication with said hydroprocessing unit.

18. The apparatus of claim 16 further comprising a vacuum generation device in communication with a receiver overhead line of said receiver.

Assignees

• Uop Llc

Inventors

• Qafisheh Jibreel A

Classifications

• B01J8/1863

  followed by a downward movement outside the reactor and subsequently re-entering it · CPC title

• B01J8/26

  with two or more fluidised beds, e.g. reactor and regeneration installations · CPC title

• B01J8/1845

  with particles moving upwards while fluidised · CPC title

• B01J8/0055

  using cyclones · CPC title

• B01J8/003

  in a downward flow · CPC title