System and method to synthesize ammonia

Patent metadata

Field	Value
Publication number	US-10974970-B2
Application number	US-201815876259-A
Country	US
Kind code	B2
Filing date	Jan 22, 2018
Priority date	Jan 20, 2017
Publication date	Apr 13, 2021
Grant date	Apr 13, 2021

Abstract

A system and method for producing ammonia at high conversion rates. The system having a fluidized bed reactor with a fluidized zone with catalyst particles. The fluidized bed reactor is preferably configured to receive a continuous flow of solid sorbent particles, nitrogen, and hydrogen, with the catalyst particles being at least ten times larger than the sorbent particles. The method allows for the nitrogen and hydrogen react on a surface of the catalyst in order to generate ammonia that is adsorbed by the sorbent particles. The method extracts the adsorbed ammonia from the sorbent particles with a sorbent regenerator to product a pure ammonia product.

First claim

What is claimed is:

1. A method of producing ammonia, the method comprising the following steps:
flowing a stream of solid sorbent particles, hydrogen, and nitrogen into a reactor, wherein the reactor includes a fluidized bed of catalyst particles;
generating ammonia by reacting the hydrogen and the nitrogen on a surface of the catalyst particles; and
adsorbing the ammonia with the solid sorbent particles, wherein the catalyst particles are at least 10 times larger than the solid sorbent particles.

2. The method of claim 1 , wherein the catalyst particles comprise a mean diameter ranging from 1.0 mm to 6.0 mm and the solid sorbent particles include a mean diameter ranging from 0.1 mm to 0.6 mm.

3. The method of claim 1 , wherein the catalyst particles comprise a mean diameter ranging from 1.0 mm to 6.0 mm and the solid sorbent particles include a mean diameter ranging from 0.01 mm to 0.6 mm.

4. The method of claim 1 , wherein the solid sorbent particles comprise at least one of MgCl 2 , MgBr 2 , and CaCl 2 ).

5. The method of claim 1 , wherein the reactor operates at a pressure ranging from about 800 psig to 1500 psig and a temperature ranging from about 200° C. to 500° C.

6. The method of claim 1 , wherein the reactor operates at a pressure ranging from about 900 psig to 1100 psig and a temperature ranging from about 200° C. to 500° C.

7. The method of claim 1 , wherein a flowrate of hydrogen and nitrogen entering the reactor is controlled to fluidize the catalyst particles and the solid sorbent particles sufficiently such that lighter solid sorbent particles are elutriated out of the reactor with unreacted hydrogen, unreacted nitrogen and unadsorbed ammonia, while larger and heavier catalyst particles remain in the reactor.

8. The method of claim 7 , wherein the unreacted hydrogen, the unreacted nitrogen and the unadsorbed ammonia and the solid sorbent particles are fed to one of a cyclone or a filter to separate the solid sorbent particles from the unreacted hydrogen, the unreacted nitrogen and the unadsorbed ammonia.

9. The method of claim 8 , wherein the unreacted hydrogen, the unreacted nitrogen and the unadsorbed ammonia are recycled back to the reactor.

10. The method of claim 8 , wherein the solid sorbent particles pass to a sorbent regenerator, wherein the sorbent regenerator releases the adsorbed ammonia.

11. The method of claim 10 , wherein the sorbent regenerator operates by at least one of lowering the pressure and increasing the temperature, and the regenerated solid sorbent particles are reintroduced to the reactor.

12. The method of claim 1 , wherein overall conversion of nitrogen and hydrogen to ammonia ranges from 70% to 95%.

13. A system for producing ammonia according to the method of claim 1 , the system comprising:
a fluidized bed reactor configured to receive a flow of solid sorbent particles, nitrogen gas, and hydrogen gas, the fluidized bed reactor including a fluidized bed of catalyst particles, wherein the nitrogen gas and hydrogen gas react on a surface of the catalyst particles generating ammonia, and wherein at least a portion of the generated ammonia is adsorbed by the sorbent particles;
at least one of a cyclone or a filter to separate the solid sorbent particles from an unreacted nitrogen gas, an unreacted hydrogen gas and an unadsorbed ammonia; and
a sorbent regenerator to release an adsorbed ammonia from the solid sorbent particles.

14. The method of claim 1 , further comprising:
providing a continuous flow of the stream of the solid sorbent particles, nitrogen gas, and hydrogen gas into a fluidized bed reactor, wherein the fluidized bed reactor includes the fluidized bed of catalyst particles;
reacting the nitrogen gas and the hydrogen gas in the presence of the catalyst particles in the fluidized bed reactor to form the ammonia;
elutriating an adsorbed ammonia out of the fluidized bed reactor along with unreacted nitrogen gas, unreacted hydrogen gas, and unabsorbed ammonia;
separating the solid sorbent particles from the unreacted nitrogen gas, the unreacted hydrogen, and the unabsorbed ammonia;
releasing the adsorbed ammonia from the solid sorbent particles to produce a pure ammonia product; and
reintroducing regenerated sorbent particles into the reactor.

15. The method of claim 14 , further comprising recycling the unreacted nitrogen gas, the unreacted hydrogen, and unabsorbed ammonia to the reactor.

16. The method of claim 14 , wherein the catalyst particles comprise a mean diameter ranging from 1.0 mm to 6.0 mm and the solid sorbent particles comprise a mean diameter ranging from 0.01 mm to 0.6 mm.

17. The method of claim 14 , wherein the fluidized bed reactor is maintained at a temperature of 350° C. and a pressure of the fluidized bed reactor is maintained in a range of 900 psig to 1,100 psig.

18. The method of claim 14 , wherein the fluidized bed reactor comprises a cylindrical shape with a height to diameter ratio of at least ten to one.

19. The method of claim 14 , wherein an overall conversion of the nitrogen gas and the hydrogen gas to ammonia is greater than 70%.

20. The method of claim 1 , wherein a fluidized bed reactor is configured to receive a flow of the solid sorbent particles, nitrogen gas, and hydrogen gas, the fluidized bed reactor including the fluidized bed of catalyst particles, and further comprising:
at least one of a cyclone or a filter separating the solid sorbent particles from an unreacted nitrogen gas, an unreacted hydrogen gas and an unadsorbed ammonia; and
a sorbent regenerator releasing an adsorbed ammonia from the solid sorbent particles.

21. The method of claim 20 , further including a recycle line recycling the unreacted nitrogen gas, the unreacted hydrogen gas, and the unabsorbed ammonia to the reactor.

22. The method of claim 20 , wherein the method operates with a continuous flow of the solid sorbent particles, the nitrogen gas, and the hydrogen gas.

23. The method of claim 20 , further comprising at least one of a temperature control system controlling a temperature of the fluidized bed reactor or a pressure control system controlling a pressure of the fluidized bed reactor.

24. The method of claim 20 , wherein the fluidized bed reactor operates at a pressure ranging from 300 psig to 4,000 psig and a temperature ranging from 200° C. to 500° C.

25. The method of claim 20 , wherein the fluidized bed reactor operates at a pressure of about 1,000 psig and a temperature of about 350° C.

26. The method of claim 20 , wherein the fluidized bed reactor comprises a cylindrical shape with a height to diameter ratio ranging from 10:1 to 20:1.

27. The method of claim 26 , wherein the fluidized bed reactor includes a tapered section.

Assignees

• Gas Technology Inst

Inventors

• Stanis Ronald J
• Mays Jeffrey A

Classifications

• C01C1/0458 Primary

  Separation of NH3 (during purge gas treatment C01C1/0476) · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C01C1/0429 Primary

  Fluidized or moving bed reactors · CPC title

• C01C1/0476

  Purge gas treatment, e.g. for removal of inert gases or recovery of H2 · CPC title