Systems and methods of processing ammonia
The present disclosure provides systems and methods for processing ammonia. A heater may heat reformers, where the reformers comprise ammonia (NH 3 ) reforming catalysts in thermal communication with the heater. NH 3 may be directed to the reformers from storage tanks, and the NH 3 may be decomposed to generate a reformate stream comprising hydrogen (H 2 ) and nitrogen (N 2 ). At least part of the reformate stream can be used to heat reformers. Additionally, the reformate stream can be directed to a hydrogen processing module such as a fuel cell.
1. A method for reforming ammonia, comprising:
a. directing ammonia to a reformer at an ammonia flow rate to produce a reformate stream comprising hydrogen and nitrogen;
b. combusting a first portion of the reformate stream with oxygen at an oxygen flow rate in a combustion heater to heat the reformer;
c. processing a second portion of the reformate stream in a hydrogen processing module;
d. measuring a temperature in the reformer or the combustion heater;
e. performing one or more of the following steps in response to the measured temperature being outside of a target temperature range of the reformer or the combustion heater to adjust the measured temperature to be within the target temperature range:
i. changing the ammonia flow rate;
ii. changing the oxygen flow rate;
iii. changing a percentage of the reformate stream that is the second portion of the reformate stream;
iv. changing a percentage of the reformate stream that is the first portion of the reformate stream; or
v. changing a percentage of the reformate stream that is vented or flared out of the combustion heater; and
f. repeatedly performing one or more of (i)-(v) by an amount that is based at least in part on a temperature difference, wherein the temperature difference is between a temperature measured in the reformer or the combustion heater and a set point temperature within the target temperature range.
2. The method of claim 1 , wherein the hydrogen processing module is a fuel cell.
3. The method of claim 1 , wherein the reformer comprises an ammonia reforming catalyst.
4. The method of claim 1 , wherein at least two of (i)-(v) are performed.
5. The method of claim 1 , wherein at least three of (i)-(v) are performed.
6. The method of claim 1 , wherein all of (i)-(v) are performed.
7. The method of claim 1 , wherein the temperature is measured using a temperature sensor.
8. The method of claim 1 , wherein the measured temperature is communicated to a controller.
9. The method of claim 1 , wherein one or more of (i)-(v) are performed with the aid of a controller.
10. The method of claim 1 , wherein at least one of (iii)-(v) are performed using a flow control module.
11. The method of claim 1 , wherein at least one of (iii)-(v) are performed by changing the second portion of the reformate stream processed in the hydrogen processing module.
12. The method of claim 1 , comprising:
based at least in part on the measured temperature being greater than the target temperature range, performing one or more of:
a. increasing the ammonia flow rate;
b. decreasing the oxygen flow rate;
a. increasing the percentage of the reformate stream that is the second portion of the reformate stream that is processed by the hydrogen processing module;
b. decreasing the percentage of the reformate stream that is the first portion of the reformate stream; or
c. increasing the percentage of the reformate stream that is vented or flared out of the combustion heater.
13. The method of claim 12 , wherein increasing the percentage of the reformate stream that is the second portion of the reformate stream decreases the first portion of the reformate stream that is combusted.
14. The method of claim 13 , wherein the hydrogen processing module is a fuel cell, and the first portion of the reformate stream comprises an anode off-gas that is directed from the fuel cell to the combustion heater.
15. The method of claim 12 , wherein decreasing the percentage of the reformate stream that is the first portion comprises decreasing the ammonia flow rate to the reformer to produce less hydrogen in the reformate stream.
16. The method of claim 12 , wherein the hydrogen processing module is a fuel cell, and increasing the percentage of the reformate stream that is the second portion that is processed by the hydrogen processing module increases an amount of power output by the fuel cell.
17. The method of claim 1 , comprising:
based at least in part on the measured temperature being less than the target temperature range, performing one or more of:
a. decreasing the ammonia flow rate
b. increasing the oxygen flow rate;
a. decreasing the percentage of the reformate stream that is the second portion of the reformate stream that is processed by the hydrogen processing module;
b. increasing the percentage of the reformate stream that is the first portion of the reformate stream; or
c. decreasing the percentage of the reformate stream that is vented or flared out of the combustion heater.
18. The method of claim 17 , wherein decreasing the percentage of the reformate stream that is the second portion increases the first portion of the reformate stream that is combusted.
19. The method of claim 18 , wherein the hydrogen processing module is a fuel cell, and the first portion of the reformate stream comprises an anode off-gas that is directed from the fuel cell to the combustion heater.
20. The method of claim 17 , wherein increasing the percentage of the reformate stream that is the first portion comprises increasing the ammonia flow rate to the reformer to produce more hydrogen in the reformate stream.
21. The method of claim 17 , wherein the hydrogen processing module is a fuel cell, and decreasing the percentage of the reformate stream that is the second portion processed by the hydrogen processing module decreases an amount of power output by the fuel cell.
22. The method of claim 1 , wherein one or more of (i)-(v) are changed by a proportional factor.
23. The method of claim 22 , wherein the proportional factor is different for each of (i)-(v).
24. The method of claim 1 , wherein (f) is repeated until the measured temperature is within the target temperature range.
25. The method of claim 1 , wherein at least part of the first portion is directed from the reformer to the combustion heater without being directed to the hydrogen processing module.
26. A method for reforming ammonia, comprising:
a. directing ammonia to a reformer at an ammonia flow rate to produce a reformate stream comprising hydrogen and nitrogen;
b. combusting a first portion of the reformate stream with oxygen at an oxygen flow rate in a combustion heater to heat the reformer;
c. processing a second portion of the reformate stream in a hydrogen processing module;
d. measuring a temperature in the reformer or the combustion heater;
e. performing one or more of the following steps in response to the measured temperature being outside of a target temperature range of the reformer or the combustion heater to adjust the measured temperature to be within the target temperature range:
i. changing the ammonia flow rate;
ii. changing the oxygen flow rate;
iii. changing a percentage of the reformate stream that is the second portion of the reformate stream;
iv. changing a percentage of the reformate stream that is the first portion of the reformate stream; or
v. changing a percentage of the reformate stream that is vented or flared out of the combustion heater;
wherein the temperature measured in the reformer or the combustion heater is a first temperature that is measured at a first time point;
f. at second time point subsequent to the first time point, measuring a second temperature of the reformer or the combustion heater;
g. calculating a time period between the first time point and the second time point;
h. calculating a temperature difference between the first temperature and the second temperature; and
j. changing one or more of (i)-(v) by an amount that is based at least in part on the time period and the temperature difference.
27. The method of claim 26 , wherein the hydrogen processing module is a fuel cell.
28. The method of claim 26 , wherein the reformer comprises an ammonia reforming catalyst.
29. The method of claim 26 , wherein at least two of (i)-(v) are performed.
30. The method of claim 26 , wherein at least three of (i)-(v) are performed.
31. The method of claim 26 , wherein all of (i)-(v) are performed.
32. The method of claim 26 , wherein the temperature is measured using a temperature sensor.
33. The method of claim 26 , wherein the measured temperature is communicated to a controller.
34. The method of claim 26 , wherein one or more of (i)-(v) are performed with the aid of a controller.
35. The method of claim 26 , wherein at least one of (iii)-(v) are performed using a flow control module.
36. The method of claim 26 , wherein at least one of (iii)-(v) are performed by changing the second portion of the reformate stream processed in the hydrogen processing module.
37. The method of claim 26 , comprising:
based at least in part on the measured temperature being greater than the target temperature range, performing one or more of:
a. increasing the ammonia flow rate;
b. decreasing the oxygen flow rate;
c. increasing the percentage of the reformate stream that is the second portion of the reformate stream that is processed by the hydrogen processing module;
d. decreasing the percentage of the reformate stream that is the first portion of the reformate stream; or
e. increasing the percentage of the reformate stream that is vented or flared out of the combustion heater.
38. The method of claim 37 , wherein increasing the percentage of the reformate stream that is the second portion of the reformate stream decreases the first portion of the reformate stream that is combusted.
39. The method of claim 38 , wherein the hydrogen processing module is a fuel cell, and the first portion of the reformate stream comprises an anode off-gas that is directed from the fuel cell to the combustion heater.
40. The method of claim 37 , wherein decreasing the percentage of the reformate stream that is the first portion comprises decreasing the ammonia flow rate to the reformer to produce less hydrogen in the reformate stream.
41. The method of claim 37 , wherein the hydrogen processing module is a fuel cell, and increasing the percentage of the reformate stream that is the second portion that is processed by the hydrogen processing module increases an amount of power output by the fuel cell.
42. The method of claim 26 , comprising:
based at least in part on the measured temperature being less than the target temperature range, performing one or more of:
a. decreasing the ammonia flow rate
b. increasing the oxygen flow rate;
c. decreasing the percentage of the reformate stream that is the second portion of the reformate stream that is processed by the hydrogen processing module;
d. increasing the percentage of the reformate stream that is the first portion of the reformate stream; or
e. decreasing the percentage of the reformate stream that is vented or flared out of the combustion heater.
43. The method of claim 42 , wherein decreasing the percentage of the reformate stream that is the second portion increases the first portion of the reformate stream that is combusted.
44. The method of claim 43 , wherein the hydrogen processing module is a fuel cell, and the first portion of the reformate stream comprises an anode off-gas that is directed from the fuel cell to the combustion heater.
45. The method of claim 42 , wherein increasing the percentage of the reformate stream that is the first portion comprises increasing the ammonia flow rate to the reformer to produce more hydrogen in the reformate stream.
46. The method of claim 42 , wherein the hydrogen processing module is a fuel cell, and decreasing the percentage of the reformate stream that is the second portion processed by the hydrogen processing module decreases an amount of power output by the fuel cell.
47. The method of claim 26 , further comprising repeating (f)-(j) until the measured temperature is within the target temperature range.
48. The method of claim 26 , wherein at least part of the first portion is directed from the reformer to the combustion heater without being directed to the hydrogen processing module.