Catalyst regenerating methods and apparatuses and methods of inhibiting corrosion in catalyst regenerating apparatuses

Patent metadata

Field	Value
Publication number	US-10011791-B2
Application number	US-201414525755-A
Country	US
Kind code	B2
Filing date	Oct 28, 2014
Priority date	Oct 28, 2014
Publication date	Jul 3, 2018
Grant date	Jul 3, 2018

Abstract

Methods and apparatuses for regenerating catalysts and methods of inhibiting corrosion in catalyst regenerating apparatuses are provided. An exemplary apparatus includes: a metal vessel configured to receive a spent catalyst stream and contact at least a portion of the spent catalyst stream with an oxygen containing environment at a sufficiently high temperature to burn coke present in the spent catalyst stream; a refractory material overlying at least a portion of an inner surface of the metal vessel; and a corrosion inhibiting material in contact with at least a portion of the inner surface of the metal vessel and disposed between the inner surface and at least a portion of the refractory material, wherein the corrosion inhibiting material is heat stable at a temperature of at least up to about 400° F. (about 204° C.) and inhibits contact of an acid environment with the inner surface of the metal vessel.

First claim

What is claimed is:

1. A catalyst regenerating apparatus comprising:
a metal vessel having an inner surface and configured to receive a spent catalyst stream and an oxygen-containing gas, and to provide an oxygen containing environment at a sufficiently high temperature to burn coke present on the spent catalyst stream and generate regenerated catalyst, wherein the spent catalyst stream comprises catalyst having coke deposits;
a refractory material overlying at least a portion of the inner surface of the metal vessel; and
a corrosion inhibiting material overlying at least a portion of the inner surface of the metal vessel and disposed between the inner surface and at least a portion of the refractory material, wherein the corrosion inhibiting material is heat stable at a temperature of at least up to about 400° F. (about 204° C.) and inhibits contact of an acid environment with the inner surface of the metal vessel.

2. The catalyst regenerating apparatus of claim 1 , wherein at least a region of the metal vessel is configured to receive and accumulate regenerated catalyst.

3. The catalyst regenerating apparatus of claim 2 , wherein at least a portion of the inner surface coated with the corrosion inhibiting material faces the region of the metal vessel configured to receive and accumulate regenerated catalyst.

4. The catalyst regenerating apparatus of claim 1 , wherein the corrosion inhibiting material comprises a coal tar based formulation.

5. The catalyst regenerating apparatus of claim 1 , wherein the corrosion inhibiting material is a hydrophobic coating.

6. The catalyst regenerating apparatus of claim 1 , wherein the corrosion inhibiting material comprises asphalt.

7. The catalyst regenerating apparatus of claim 1 , wherein the corrosion inhibiting material comprises about 20 wt. % to about 60 wt. % asphalt.

8. A method of regenerating a fluid catalytic cracking catalyst, said method comprising the steps of:
introducing a spent catalyst stream into a catalyst regenerator, wherein the spent catalyst stream comprises spent catalyst having coke deposits, and wherein the catalyst regenerator comprises:
a metal vessel with an inner surface,
a refractory material overlying at least a portion of the inner surface of the metal vessel;
a corrosion inhibiting material disposed between at least a portion of the inner surface of the metal vessel and at least a portion of the refractory material, wherein the corrosion inhibiting material is heat stable at a temperature of at least up to about 400° F. (about 204° C.), and inhibits contact of an acid environment with the portion of the inner surface of the metal vessel contacted by the corrosion inhibiting material; and
contacting a portion of the spent catalyst stream with an oxygen containing environment at a sufficiently high temperature to burn coke present on the spent catalyst.

9. The method of claim 8 , wherein introducing the spent catalyst stream into the catalyst regenerator comprises introducing a spent catalyst stream from a fluid catalytic cracking reactor into the catalyst regenerator.

10. The method of claim 8 , wherein introducing the spent catalyst stream into the catalyst regenerator comprises introducing the spent catalyst stream into a catalyst regenerator comprising a metal vessel with at least a region of the metal vessel configured to receive and accumulate regenerated catalyst.

11. The method of claim 10 , wherein introducing the spent catalyst stream into the catalyst regenerator comprises introducing the spent catalyst stream into the catalyst regenerator, wherein at least a portion of the inner surface in contact with the corrosion inhibiting material faces the region of the metal vessel configured to receive and accumulate regenerated catalyst.

12. The method of claim 8 , wherein introducing the spent catalyst stream into the catalyst regenerator comprises introducing the spent catalyst stream into the catalyst regenerator comprising an inner surface, at least a portion of which is in contact with a corrosion inhibiting material comprising asphalt.

13. The method of claim 8 , wherein introducing the spent catalyst stream into the catalyst regenerator comprises introducing the spent catalyst stream into the catalyst regenerator comprising an inner surface, at least a portion of which is overlied with a corrosion inhibiting material comprising about 20 wt. % to about 60 wt. % asphalt.

Assignees

• Uop Llc

Inventors

• Palmas Paolo
• Althoff James W
• Victor Sanford Allan

Classifications

• B01J2208/00911

  Sparger-type feeding elements · CPC title

• B01J2219/0245

  of synthetic organic material · CPC title

• B01J8/26

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

• B01J8/003

  in a downward flow · CPC title

• B01J8/1863

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