Process for making ammonia

Patent metadata

Field	Value
Publication number	US-9914645-B2
Application number	US-201414535491-A
Country	US
Kind code	B2
Filing date	Nov 7, 2014
Priority date	Nov 7, 2013
Publication date	Mar 13, 2018
Grant date	Mar 13, 2018

Abstract

A system for producing ammonia comprises a reactor configured for receiving nitrogen feed gas and hydrogen feed gas, the reactor comprising a catalyst configured to convert at least a portion of the nitrogen gas and at least a portion of the hydrogen feed gas to ammonia to form a reactant mixture comprising the ammonia and unreacted nitrogen feed gas and unreacted hydrogen feed gas, an adsorbent configured to selective adsorb at least a portion of the ammonia from the reactant mixture, and a recycle line to recycle the unreacted nitrogen feed gas, the unreacted hydrogen feed gas, and unabsorbed ammonia to the reactor.

First claim

What is claimed is:

1. A system for producing ammonia, the system comprising:
a reactor configured for receiving nitrogen feed gas (N 2 ) and hydrogen feed gas (H 2 ), the reactor comprising a catalyst configured to convert at least a portion of the nitrogen gas and at least a portion of the hydrogen feed gas to ammonia (NH 3 ) to form a reactant mixture comprising the ammonia and unreacted nitrogen feed gas and unreacted hydrogen feed gas;
an absorbent configured to selective absorb at least a portion of the ammonia from the reactant mixture;
one or more control systems configured to control a reaction temperature and a reaction pressure in the reactor during conversion of the portion of the nitrogen feed gas and the portion of the hydrogen feed gas to ammonia, and to control an absorption temperature and an absorption pressure at the absorbent during selective absorption of at least the portion of the ammonia from the reactant mixture, wherein the one or more control systems are configured to control the reaction temperature to 350° C. or greater and to control the absorption temperature to from about 170° C. to about 200° C.; and
a recycle line to recycle the unreacted nitrogen feed gas, the unreacted hydrogen feed gas, and unabsorbed ammonia to the reactor.

2. The system of claim 1 , wherein the absorbent has a selective affinity for absorbing ammonia that is higher than its affinity for absorbing nitrogen gas or hydrogen gas.

3. The system of claim 1 , wherein the absorbent comprises magnesium chloride (MgCl 2 ).

4. The system of claim 1 , wherein the one or more control systems are configured to control the temperature of the absorbent to a desorption temperature configured to provide for desorption of absorbed ammonia from the absorbent.

5. The system of claim 1 , wherein the one or more control system systems are configured to control pressure applied to the absorbent to a desorption pressure configured to provide for desorption of absorbed ammonia from the absorbent.

6. The system of claim 1 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia for the system is at least about 50%.

7. The system of claim 1 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia for the system is at least about 70%.

8. The system of claim 1 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia for the system is at least about 80%.

9. The system of claim 1 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia for the system is at least about 90%.

10. A method for producing ammonia, the method comprising:
reacting at least a portion of a nitrogen feed gas (N 2 ) and at least a portion of a hydrogen feed gas (H 2 ) in the presence of a catalyst in a reactor to form ammonia (NH 3 ), wherein unreacted nitrogen gas (N 2 ), unreacted hydrogen gas (H 2 ), and the ammonia (NH 3 ) form a reactant mixture;
controlling a temperature in the reactor to a reaction temperature;
controlling a pressure in the reactor to a reaction pressure;
selectively absorbing at least a portion of the ammonia from the reactant mixture with an absorbent;
controlling a temperature at the absorbent to an absorption temperature of from about 170° C. to about 200° C.;
controlling a pressure at the absorbent to an absorption pressure; and
following the selective absorbing, recycling the unreacted nitrogen gas, the unreacted hydrogen, and unabsorbed ammonia to the reactor.

11. The method of claim 10 , wherein the absorbent has a selective affinity for absorbing ammonia that is higher than its affinity for absorbing nitrogen gas or hydrogen gas.

12. The method of claim 10 , wherein the absorbent comprises magnesium chloride (MgCl 2 ).

13. The method of claim 10 , wherein the absorption pressure at the absorbent is from about 50 bar to about 100 bar.

14. The method of claim 10 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia from the method is at least about 50%.

15. The method of claim 10 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia from the method is at least about 70%.

16. The method of claim 10 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia from the method is at least about 80%.

17. The method of claim 10 , wherein overall conversion of the nitrogen feed gas and the hydrogen feed gas to ammonia from the method is at least about 90%.

Assignees

• Univ Minnesota

Inventors

• Himstedt Heath H
• Huberty Mark S
• Mccormick Alon V
• Schmidt Lanny D
• Cussler Edward L

Classifications

• B01J8/0005

  Catalytic processes under superatmospheric pressure (non-catalytic processes B01J3/00) · CPC title

• Y02P20/52

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

• C01C1/006

  making use of solid ammonia storage materials, e.g. complex ammine salts · CPC title

• B01D53/047

  Pressure swing adsorption · CPC title

• C01C1/0458 Primary

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