Hydrocracking process utilizing aqueous ammonia

Patent metadata

Field	Value
Publication number	US-10119082-B2
Application number	US-201414568854-A
Country	US
Kind code	B2
Filing date	Dec 12, 2014
Priority date	Dec 12, 2014
Publication date	Nov 6, 2018
Grant date	Nov 6, 2018

Abstract

A process for controlling hydrocracking reactions in a hydrocracking reactor by passing aqueous ammonia to the hydrocracking reactor. The aqueous ammonia is injected into the process at various locations at a low pressure, typically between approximately 0.17 to approximately 2.07 MPa (25 to 300 psi). A wash fluid can be used to lower the concentration of ammonia in the hydrocracking reactor, and thus, increase the catalytic activity of the hydrocracking catalyst.

First claim

What is claimed is:

1. A process for controlling an activity of a hydrocracking catalyst in a hydrocracking reaction zone, the process comprising:
passing an aqueous ammonia stream into a hydrocracking reaction zone having an acidic hydrocracking catalyst, wherein a pressure of the aqueous ammonia stream when injected is between approximately 0.17 to approximately 2.07 MPa (25 to 300 psi) and reducing an ammonia concentration in the hydrocracking reaction zone with a wash fluid.

2. The process of claim 1 , wherein the aqueous ammonia stream is mixed with a feed stream to form a combined stream, wherein the combined stream is passed into the hydrocracking reaction zone.

3. The process of claim 1 wherein a pressure of the aqueous ammonia stream is between approximately 0.34 to approximately 1.7 MPa (50 to 250 psi).

4. The process of claim 1 wherein the aqueous ammonia stream comprises between 15 to 25 wt % of ammonia.

5. The process of claim 1 further comprising:
passing a feed stream into the hydrocracking reaction zone; and,
operating the hydrocracking reaction zone under hydrocracking conditions.

6. The process of claim 1 further comprising:
monitoring for ammonia in an effluent from the hydrocracking reaction zone; and,
reducing an amount of the ammonia passed to the hydrocracking reaction zone upon a detection of ammonia in the effluent.

7. The process of claim 6 further comprising:
increasing a temperature in the hydrocracking reaction zone after the amount of ammonia passed to the hydrocracking reaction zone is reduced.

8. The process of claim 7 wherein the wash fluid comprises water.

9. A process for maintaining a temperature of a hydrocracking reaction zone, the process comprising:
hydrocracking hydrocarbons in the presence of hydrogen and an acidic hydrocracking catalyst in a hydrocracking reaction zone;
inhibiting the hydrocracking of the hydrocracking reaction zone by inhibiting acid sites on the acidic hydrocracking catalyst with ammonia,
wherein the ammonia is an aqueous ammonia having an initial pressure of between approximately 0.17 to approximately 2.07 MPa (25 to 300 psi); and
reducing an ammonia concentration in the hydrocracking reaction zone with a wash fluid.

10. The process of claim 9 further comprising:
passing a stream of the aqueous ammonia to the hydrocracking reaction zone.

11. The process of claim 10 wherein the initial pressure of the aqueous ammonia is between approximately 0.34 to approximately 1.7 MPa (50 to 250 psi).

12. The process of claim 9 further comprising:
mixing a feed stream with the aqueous ammonia to form a combined stream; and,
passing the combined stream to the hydrocracking reaction zone.

13. The process of claim 9 wherein the catalyst comprises a fresh catalyst.

14. The process of claim 9 wherein the wash fluid is water.

15. The process of claim 9 further comprising:
increasing the hydrocracking catalytic activity in the hydrocracking reaction zone by reducing an ammonia concentration in the hydrocracking reaction zone.

16. A process for hydrocracking hydrocarbons, the process comprising: hydrocracking a portion of hydrocarbons in a feed stream in the presence of hydrogen and an acidic hydrocracking catalyst in a hydrocracking reaction zone; passing a stream of aqueous ammonia having an initial pressure between approximately 0.17 to approximately 2.07 MPa (25 to 300 psi) to the hydrocracking reaction zone; and decreasing an amount of aqueous ammonia passed to the hydrocracking reaction zone to increase the hydrocracking reactions by reducing an ammonia concentration to the hydrocracking reaction zone with a wash fluid.

17. The process of claim 16 further comprising:
mixing the aqueous ammonia with the feed stream upstream of the hydrocracking reaction zone.

18. The process of claim 16 further comprising:
vaporizing the aqueous ammonia within the hydrocracking reactor.

Assignees

• Uop Llc

Inventors

• Mallett Vernon L

Classifications

• C10G47/12

  Inorganic carriers · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• B01J8/0453

  the beds being superimposed one above the other · CPC title

• C10G47/16

  Crystalline alumino-silicate carriers · CPC title

• C10G47/36 Primary

  Controlling or regulating · CPC title