Apparatus and process for heating catalyst from a reactor

Patent metadata

Field	Value
Publication number	US-9669373-B2
Application number	US-201414568258-A
Country	US
Kind code	B2
Filing date	Dec 12, 2014
Priority date	Dec 12, 2014
Publication date	Jun 6, 2017
Grant date	Jun 6, 2017

Abstract

A process and apparatus for heating catalyst is presented. Cooler catalyst is removed from a reactor and heated with a hot gas in a riser, heated in a heating tube or heated in a heating chamber. Heated catalyst is disengaged from the hot gas if necessary and returned to the reactor. The process and apparatus can be used for producing light olefins. The hot gas may be a flue gas from an FCC regenerator or a combustion gas from a heater.

First claim

The invention claimed is:

1. A reactor apparatus comprising:
a reactor vessel comprising a hydrocarbon feed inlet, a catalyst outlet in the reactor vessel, a product outlet in the reactor vessel and a catalyst inlet to the reactor vessel;
a heating chamber in direct communication with the catalyst outlet and a source of gas;
a riser in downstream communication with said catalyst outlet at a first end and said heating chamber in direct communication with a second end of said riser;
said catalyst inlet in downstream communication with said second end of said riser.

2. The reactor apparatus of claim 1 further comprising said reactor vessel above said heating chamber.

3. The reactor apparatus of claim 1 wherein said source of gas is an FCC regenerator.

4. The reactor apparatus of claim 1 wherein said source of gas is a hydrocarbon source.

5. The reactor apparatus of claim 1 wherein said feed inlet is above the catalyst outlet.

6. The reactor apparatus of claim 1 further comprising a stripping section below said feed inlet.

7. The reactor apparatus of claim 1 further comprising a disengaging section above said feed inlet in said reactor vessel.

8. The reactor apparatus of claim 1 further comprising a conduit for transferring catalyst to the catalyst regenerator.

9. The reactor apparatus of claim 1 further comprising:
an FCC regenerator comprising a spent catalyst inlet, a regenerated catalyst outlet, a flue gas outlet, the first end of said riser being in direct communication with the flue gas outlet, wherein said source of gas is the FCC regenerator.

10. The reactor apparatus of claim 9 further comprising:
a second reactor vessel comprising a hydrocarbon feed inlet, a catalyst outlet in the second reactor vessel, a product outlet in the second reactor vessel, and a catalyst inlet to the second reactor vessel;
wherein the spent catalyst inlet is in downstream communication with the catalyst outlet of the second reactor vessel, and the catalyst inlet of the second reactor vessel is in downstream communication with the regenerated catalyst outlet.

11. The reactor apparatus of claim 9 wherein the FCC regenerator further comprises a hot gas inlet and the heating chamber further comprises a hot gas outlet in communication, the hot gas inlet of the FCC regenerator being in downstream communication with the hot gas outlet of the heating chamber.

12. The reactor apparatus of claim 9 wherein the reactor vessel further comprises a second catalyst outlet and the FCC regenerator further comprises a second spent catalyst inlet, the second spent catalyst inlet of the FCC regenerator being in downstream communication with the second catalyst outlet of the reactor vessel.

13. A reactor apparatus comprising:
a reactor vessel comprising a feed inlet, a catalyst outlet in the reactor vessel, a product outlet in the reactor vessel and a catalyst inlet to the reactor vessel;
a heating chamber in direct communication with the catalyst outlet and a source of gas, said reactor vessel being disposed above said heating chamber;
a riser in downstream communication with said catalyst outlet at a first end and said heating chamber in direct communication with a second end of said riser;
a disengaging section above said feed inlet in said reactor vessel; and
said catalyst inlet in downstream communication with said second end of said riser.

14. The reactor apparatus of claim 13 further comprising a stripping section below said feed inlet.

15. The reactor apparatus of claim 13 wherein said source of gas is an FCC regenerator.

16. The reactor apparatus of claim 13 wherein said source of gas is a hydrocarbon source.

17. The reactor apparatus of claim 13 wherein said feed inlet is above the catalyst outlet.

18. The reactor apparatus of claim 13 further comprising:
an FCC regenerator comprising a spent catalyst inlet, a regenerated catalyst outlet, a flue gas outlet, the first end of said riser being in direct communication with the flue gas outlet, wherein said source of gas is the catalyst regenerator;
a second reactor vessel comprising a hydrocarbon feed inlet, a catalyst outlet in the second reactor vessel, a product outlet in the second reactor vessel, and a catalyst inlet to the second reactor vessel;
wherein the spent catalyst inlet is in downstream communication with the catalyst outlet of the second reactor vessel, and the catalyst inlet of the second reactor vessel is in downstream communication with the regenerated catalyst outlet.

19. The reactor apparatus of claim 18 wherein the FCC regenerator further comprises a hot gas inlet and the heating chamber further comprises a hot gas outlet in communication, the hot gas inlet of the FCC regenerator being in downstream communication with the hot gas outlet of the heating chamber;
or
wherein the reactor vessel further comprises a second catalyst outlet and the catalyst regenerator further comprises a second spent catalyst inlet, the second spent catalyst inlet of the FCC regenerator being in downstream communication with the second catalyst outlet of the reactor vessel;
or both.

20. A reactor apparatus comprising:
a reactor vessel comprising a hydrocarbon feed inlet, a catalyst outlet in the reactor vessel, a product outlet in the reactor vessel and a catalyst inlet to the reactor vessel;
a heating chamber in direct communication with the catalyst outlet and a source of gas, wherein said source of gas is a hydrocarbon source;
a riser in downstream communication with said heating chamber at a first end; and
said catalyst inlet in downstream communication with a second end of said riser.

Assignees

• Uop Llc

Inventors

• Mehlberg Robert L

Classifications

• B01J8/1836 Primary

  Heating and cooling the reactor (B01J8/42 takes precedence) · CPC title

• B01J8/30

  the edge of a lower bed projecting beyond the edge of the superjacent bed · CPC title

• C10G11/18

  according to the "fluidised-bed" technique · CPC title