IP Library › Granted Patent US 11,478,784
Granted Patent B2
US 11,478,784 · App. 16/781,843 · Granted Oct 25, 2022

Catalyst compositions for ammonia decomposition

Inventors: Jorge Gascon (Thuwal, SA); Salvador Sayas (Thuwal, SA); Natalia Morlanes (Thuwal, SA); Sai Katikaneni (Dhahran, SA); Aadesh Harale (Dhahran, SA); Bandar Solami (Dhahran, SA)
Assignees: Saudi Arabian Oil Company; King Abdullah University of Science and Technology
B01J37/031B01J23/10B01J23/78B01J35/023B01J37/009B01J37/0201B01J37/0236B01J37/04B01J37/06B01J37/088C01B3/047
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Quick Facts
Patent No.
US 11,478,784
App. No.
16/781,843
Granted
Oct 25, 2022
Kind
B2
Abstract

A method for ammonia decomposition to produce hydrogen, the method comprising the steps of introducing an ammonia stream to a reactor, wherein the ammonia stream comprises ammonia, wherein the reactor comprises a cobalt-based catalyst, the cobalt-based catalyst comprising 15 wt % and 70 wt % of cobalt, 5 wt % and 45 wt % of cerium, and 0.4 wt % and 0.5 wt % barium, wherein a remainder of weight of the cobalt-based catalyst is oxygen; contacting the ammonia in the ammonia stream with the cobalt-based catalyst, wherein the cobalt-based catalyst is operable to catalyze an ammonia decomposition reaction; catalyzing the ammonia decomposition reaction to cause the ammonia decomposition in the presence of the cobalt-based catalyst to produce hydrogen; and withdrawing a product stream from the reactor, the product stream comprising hydrogen.

Claims (14)

1. A method for ammonia decomposition to produce hydrogen, the method comprising the steps of:

introducing a flow of hydrogen gas to the reactor;

increasing a temperature in the reactor to 500° C. at a rate of 2° C. per minute, wherein the reactor comprises a cobalt-based catalyst, the cobalt-based catalyst comprising:

15 wt % and 70 wt % of cobalt,

5 wt % and 45 wt % of cerium, and

0.4 wt % and 0.5 wt % barium, wherein a remainder of weight of the cobalt-based catalyst is oxygen;

maintaining the temperature in the reactor at 500° C. for at least 3 hours to activate metal sites on the cobalt-based catalyst;

introducing an ammonia stream to the reactor, wherein the ammonia stream comprises ammonia;

contacting the ammonia in the ammonia stream with the cobalt-based catalyst at temperature in a range between 250-700° C. to decompose the ammonia, wherein the cobalt-based catalyst is operable to catalyze an ammonia decomposition reaction;

catalyzing the ammonia decomposition reaction to cause the ammonia decomposition in the presence of the cobalt-based catalyst to produce hydrogen; and

withdrawing a product stream from the reactor, the product stream comprising hydrogen.

2. The method of claim 1 , wherein a pressure in the reactor is in a range between 1 bar and 40 bar.

3. The method of claim 1 , wherein the product stream further comprises nitrogen.

4. The method of claim 1 , wherein the conversion of ammonia is greater than 95%.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 4, 2020
From: KATIKANENI, SAI; HARALE, AADESH; SOLAMI, BANDAR
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 051717/0687 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 4, 2020
From: GASCON, JORGE; SAYAS, SALVADOR; MORLANES, NATALIA
To: KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY
Reel/Frame 051717/0753 →
Continuity (1)
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