IP Library Granted Patent US 10,767,556
Granted Patent B2
US 10,767,556 · App. 15/999,280 · Granted Sep 8, 2020

Method and equipment for combustion of ammonia

Inventors: Ghenadie Bulat (Lincoln, GB); Timothy Hughes (Wantage, GB); Jonathan May (Lincoln, GB); Ian Wilkinson (Witney, GB)
Assignee: Siemens Aktiengesellschaft
F02C3/24F01K23/10F01K23/18F02C3/20F02C3/22F02C3/34F02C6/04F23C6/04F23C9/06F23C2900/9901F23J2215/10
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Quick Facts
Patent No.
US 10,767,556
App. No.
15/999,280
Granted
Sep 8, 2020
Kind
B2
Abstract

A method for the combustion of ammonia, wherein a first combustion chamber receives ammonia and hydrogen in controlled proportions, and an oxygen-containing gas. Combustion of the ammonia and hydrogen produces NH 2 ions among other combustion products. A second combustion chamber receives the combustion products from the first combustion chamber and receives further ammonia and further hydrogen in controlled proportions, wherein combustion produces nitrogen oxides among other combustion products. A third combustion chamber receives the nitrogen oxides along with further ammonia and further hydrogen in further controlled proportions along with further oxygen-containing gas, such that the nitrogen oxides are combusted into nitrogen and water.

Claims (20)

1. A method for the combustion of ammonia, wherein a first combustion chamber receives ammonia and hydrogen in controlled proportions, and an oxygen-containing gas, wherein combustion of the ammonia and hydrogen produces NH 2 ions among exhaust gases from the first combustion chamber, and wherein a second combustion chamber receives the exhaust oases from the first combustion chamber and receives further ammonia and further hydrogen in controlled proportions, wherein combustion in the second combustion chamber produces nitrogen oxides among exhaust gases from the second combustion chamber, and wherein a third combustion chamber receives the exhaust gases from the second combustion chamber including nitrogen oxides along with further ammonia and further hydrogen in further controlled proportions along with further oxygen-containing gas, such that the nitrogen oxides are combusted into nitrogen and water.

2. The method for the combustion of ammonia according to claim 1 wherein energy from the combustion in the second combustion chamber is recovered by operation of a first turbine by the exhaust gases from the second combustion chamber to convert energy from the combustion in the second combustion chamber into mechanical energy.

3. The method for the combustion of ammonia according to claim 2 wherein energy from the combustion in the first combustion chamber is recovered by operation of a second turbine by the exhaust gases from the first combustion chamber to convert the energy from the combustion in the first combustion chamber into mechanical energy.

4. The method for the combustion of ammonia according to claim 1 wherein energy from the combustion in the third combustion chamber is recovered by operation of a third turbine to convert the energy from the combustion in the third combustion chamber into mechanical energy.

5. The method for the combustion of ammonia according to claim 4 wherein operation of the third turbine is by heating of water in a heat exchanger to drive the third turbine by steam.

6. The method for the combustion of ammonia according to claim 1 wherein heat is recovered from the third combustion chamber by an integrated heat exchanger.

7. The method for the combustion of ammonia according to claim 1 wherein a proportion of exhaust gases from the third combustion chamber is recirculated into the first combustion chamber in order to provide combustion of ammonia remaining in the exhaust gases from the third combustion chamber.

8. A system for the combustion of ammonia, comprising:

a first combustion chamber connected to a source of ammonia, to receive ammonia, and connected to a source of hydrogen, to receive hydrogen, in controlled proportions, and connected to a source of oxygen-containing gas, to receive an oxygen-containing gas; a second combustion chamber connected to the first combustion chamber to receive exhaust gases from the first combustion chamber, and connected to the source of ammonia to receive further and connected to the source of hydrogen to receive further hydrogen in further controlled proportions; and a third combustion chamber connected to the second combustion chamber to receive exhaust gases from the second combustion chamber, and connected to the source of ammonia to receive further ammonia and, and connected to the source of hydrogen to receive further hydrogen in further controlled proportions, and connected to the source of oxygen-containing gas to receive further oxygen-containing gas.

9. The system according to claim 8 , further comprising a first turbine connected to receive the exhaust gases from the second combustion chamber, to generate a mechanical output and to provide the exhaust gases from the second combustion chamber to the third combustion chamber.

10. The system according to claim 3 further comprising a second turbine connected to receive the exhaust gases from the first combustion chamber and to provide the exhaust gases from the first combustion chamber to the second combustion chamber.

11. The system according to claim 10 further comprising a third turbine connected to a heat exchanger which is connected to receive exhaust gases from the third combustion chamber, whereby to heat water and generate steam to drive the third turbine.

12. The system according to claim 11 wherein the heat exchanger is integrated into the third combustion chamber.

13. The system for the combustion of, ammonia according to claim 8 , further comprising a recirculation line arranged to recirculate a portion of exhaust gas from the third combustion chamber back into the first combustion chamber.

14. The system for the combustion of ammonia according to claim 13 wherein the recirculation line is connected to a mixer to mix the proportion of the exhaust gas the third combustion chamber with the oxygen-containing gas.

15. The system for the combustion of ammonia according to claim 8 the source of hydrogen is a single source connected to any two of said first combustion chamber, said second combustion chamber, and said third combustion chamber.

16. The system for the combustion of ammonia according to claim 8 wherein, the source of hydrogen is a single source connected to all of said first combustion chamber, said second combustion chamber, and said third combustion chamber.

17. The system for the combustion of ammonia according to claim 8 wherein, the source of oxygen-containing gas is a single source connected to both of said first combustion chamber and said third combustion chamber.

18. The system for the combustion of ammonia according to claim 8 wherein, the source of ammonia is a single source connected to any two of said first combustion chamber, said second combustion chamber and said third combustion chamber.

19. The system for the combustion of ammonia, according to claim 8 wherein, the source of ammonia is a single source connected to all of said first combustion chamber, said second combustion chamber, and said third combustion chamber.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 5, 2021
From: SIEMENS AKTIENGESELLSCHAFT
To: SIEMENS ENERGY GLOBAL GMBH & CO. KG
Reel/Frame 056501/0020 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 22, 2019
From: BULAT, GHENADIE; MAY, JONATHAN
To: SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED
Reel/Frame 051089/0732 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 22, 2019
From: HUGHES, TIMOTHY; WILKINSON, IAN
To: SIEMENS PLC.
Reel/Frame 051089/0872 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 22, 2019
From: SIEMENS PLC.
To: SIEMENS AKTIENGESELLSCHAFT
Reel/Frame 051090/0325 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 22, 2019
From: SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED
To: SIEMENS AKTIENGESELLSCHAFT
Reel/Frame 051090/0387 →
Priority Claims (1)
GB 1602617.1 · Feb 15, 2016 · national
Continuity (1)
Related Publication 20190107048A1 · Apr 11, 2019
Cited By (1)
US 12,222,106