Use of catalysts, method and apparatus for selective oxidation of ammonia in a gas containing hydrogen

Patent metadata

Field	Value
Publication number	US-10005067-B2
Application number	US-201515310264-A
Country	US
Kind code	B2
Filing date	May 26, 2015
Priority date	May 27, 2014
Publication date	Jun 26, 2018
Grant date	Jun 26, 2018

Abstract

The invention contributes to a cost effective way to solve the problem of trace ammonia removal from a hydrogen and nitrogen containing gas. The set of catalysts of the invention selectively oxidized ammonia in ppm concentration even in gas mixtures containing hydrogen gas in concentrations of three orders of magnitude higher than the concentration of ammonia.

First claim

The invention claimed is:

1. An apparatus for producing a gas mixture comprising hydrogen and nitrogen gas, said apparatus comprising:
an ammonia decomposition unit comprising a catalyst for decomposing ammonia;
an ammonia oxidizing unit comprising a selective catalyst oxidizing ammonia, wherein said catalyst oxidizing ammonia is a catalyst comprising at least one transition metal element configured to selectively remove ammonia from gas mixtures comprising hydrogen and ammonia gas, wherein the gas mixtures comprise ammonia at a concentration lower than 1000 ppm, wherein said at least one transition metal element is supported on a support; wherein said at least one transition metal element is Cr, Mo, W, or V or a combination thereof further comprising a feed to said ammonia oxidizing unit configured to introduce oxygen gas or an oxidant.

2. The apparatus for producing a gas mixture according to claim 1 , wherein said ammonia oxidizing unit is located downstream of the ammonia decomposition unit.

3. A method of using a catalyst to oxidize ammonia comprising:
selectively removing ammonia from a gas mixture comprising hydrogen and ammonia gases with a catalyst comprising at least one transition metal element supported on a support, wherein said at least one transition metal element is Cr, Mo, W, or V or a combination thereof, and wherein said catalyst is incorporated in an ammonia oxidizing unit present in an apparatus further comprising an ammonia decomposition unit, and a feed to said ammonia oxidizing unit configured to introduce oxygen gas or an oxidant.

4. The method of claim 3 , comprising selectively removing ammonia from a gas mixture comprising hydrogen and ammonia gases below the equilibrium concentration of ammonia at any given temperature.

5. The method of claim 3 , comprising selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and wherein the concentration of ammonia is lower than 1000 ppm.

6. The method of claim 5 , comprising selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and containing ammonia in ppm concentration, wherein the concentration of ammonia is lower than 500 ppm.

7. The method of claim 5 , comprising selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and containing ammonia in ppm concentration, wherein the concentration of ammonia is between 10 and 500 ppm.

8. A method of using the apparatus for producing a gas mixture according to claim 1 , comprising selectively removing ammonia from a gas mixture comprising hydrogen and ammonia gases in the apparatus of claim 1 .

9. The method of claim 8 comprising, selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and wherein the concentration of ammonia is lower than 1000 ppm.

10. The method of claim 8 comprising, selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and containing ammonia in ppm concentration, wherein the concentration of ammonia is lower than 500 ppm.

11. The method of claim 8 comprising, selectively removing ammonia from a gas mixture having a composition of 3:1 hydrogen to nitrogen ratio and containing ammonia in ppm concentration, wherein the concentration of ammonia is between 10 and 500 ppm.

12. A method for selectively removing ammonia from gas mixtures, the method comprising:
providing a flow of a gas mixture comprising hydrogen, nitrogen and ammonia gases over a catalyst, wherein said catalyst comprises at least one transition metal element comprising hydrogen and ammonia gas in ppm concentration, wherein said at least one transition metal element is supported on a support; and wherein said at least one transition metal element is Cr, Mo, W, or V or a combination thereof, thereby selectively removing said ammonia from said gas mixture, said ammonia being present in ppm concentration.

13. The method for selectively removing ammonia from gas mixtures according to claim 12 , wherein said gas mixture has a composition of at least 75 vol % of hydrogen gas and ammonia in ppm concentration.

14. The method for selectively removing ammonia from gas mixtures according to claim 12 , wherein the concentration of ammonia is lower than 1000 ppm.

15. The method for selectively removing ammonia from gas mixtures according to claim 12 , wherein the concentration of ammonia is lower than 500 ppm.

16. The method for selectively removing ammonia from gas mixtures according to claim 12 , wherein the concentration of ammonia is between 10 and 500 ppm.

Assignees

• Univ Danmarks Tekniske

Inventors

• Chakraborty Debasish
• Chorkendorff Ib
• Olsen Jakob Lind
• Lopes Silva Hugo José
• Nielsen Morten Godtfred

Classifications

• B01J37/0201

  Impregnation · CPC title

• B01J23/30 Primary

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• B01J2219/00002

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• B01J23/22

  Vanadium · CPC title

• B01D2255/20769

  Molybdenum · CPC title