Exhaust after-treatment system including electrolysis generated H2 and NH3
View Patent ↗An exhaust after-treatment system including an exhaust passage, a lean-NOx trap (LNT) provided in the exhaust passage, a tank carrying an aqueous reagent, an electrochemical cell in communication with the tank and configured to receive the aqueous reagent therefrom, the electrochemical cell configured to convert the aqueous reagent into a hydrogen exhaust treatment fluid for purging the LNT, and a controller in communication with the electrochemical cell, wherein the controller is configured to vary an amount of the hydrogen exhaust treatment fluid produced by the electrochemical cell.
1. An exhaust after-treatment system comprising:
an exhaust passage;
a lean-NOx trap (LNT) provided in the exhaust passage;
an exhaust treatment component provided in the exhaust passage;
a tank carrying an aqueous reagent;
an electrochemical cell in communication with the tank and configured to receive the aqueous reagent therefrom, the electrochemical cell configured to convert the aqueous reagent into a hydrogen exhaust treatment fluid for purging the LNT and another exhaust treatment fluid for treating an exhaust in the exhaust treatment component; and
a controller in communication with the electrochemical cell, the controller being configured to vary an amount of the hydrogen exhaust treatment fluid produced by the electrochemical cell.
2. The exhaust after-treatment system according to claim 1 , further comprising an injector in communication with the electrochemical cell and the exhaust passage, the injector being configured to receive the hydrogen exhaust treatment fluid from the electrochemical cell, and dose the hydrogen exhaust treatment fluid into the exhaust passage at a location upstream from the LNT.
3. The exhaust after-treatment system according to claim 2 , wherein the aqueous reagent comprises urea.
4. The exhaust after-treatment system according to claim 3 , wherein the another exhaust treatment fluid includes an ammonia exhaust treatment fluid, and the injector is configured to receive the hydrogen and ammonia exhaust treatment fluids from the electrochemical cell, and dose the hydrogen and ammonia exhaust treatment fluids into the exhaust passage at a location upstream from the LNT.
5. The exhaust after-treatment system according to claim 4 , wherein the exhaust treatment component includes an SCR exhaust treatment component that is located in the exhaust passage downstream from the LNT; and
the exhaust after-treatment system further comprises a second injector in communication with the electrochemical cell and the exhaust passage, the second injector being configured to receive the ammonia exhaust treatment fluid from the electrochemical cell and/or the aqueous reagent from the tank, and dose the ammonia exhaust treatment fluid and/or the aqueous reagent into the exhaust passage at a location upstream from the SCR exhaust treatment component.
6. The exhaust after-treatment system according to claim 1 , wherein the electrochemical cell includes an anode and a cathode, each of the anode and the cathode being in communication with a power source.
7. The exhaust after-treatment system according to claim 6 , wherein the power source is in communication with the controller.
8. The exhaust after-treatment system according to claim 7 , wherein power source is configured to apply a voltage to each of the anode and the cathode based on an instruction received from the controller.
9. The exhaust after-treatment system according to claim 1 , further comprising a plurality of the electrochemical cells.
10. The exhaust after-treatment system according to claim 4 , further comprising a first accumulator and a second accumulator in communication with the electrochemical cell, the first accumulator configured to store the hydrogen exhaust treatment fluid produced by the electrochemical cell, and the second accumulator configured to store the ammonia exhaust treatment fluid.
11. An exhaust after-treatment system comprising:
an exhaust passage;
a lean-NOx trap (LNT) provided in the exhaust passage;
an SCR exhaust treatment component provided in the exhaust passage;
a tank carrying an aqueous urea reagent;
a plurality of electrochemical cells in communication with the tank and configured to receive the aqueous urea reagent therefrom, the electrochemical cells each configured to convert the aqueous reagent into ammonia exhaust treatment fluid and a hydrogen exhaust treatment fluid;
a controller in communication with each of the electrochemical cells, the controller being configured to vary amounts of each of the hydrogen exhaust treatment fluid and the ammonia exhaust treatment fluid produced by the electrochemical cells;
a first injector in communication with each of the electrochemical cells and the exhaust passage, the first injector being configured to receive the hydrogen exhaust treatment fluid from the electrochemical cells, and dose the hydrogen exhaust treatment fluid into the exhaust passage at a location upstream from the LNT to purge the LNT; and
a second injector in communication with each of the electrochemical cells and the exhaust passage, the second injector being configured to receive the ammonia exhaust treatment fluid from the electrochemical cells, and dose the ammonia exhaust treatment fluid into the exhaust passage at a location upstream from the SCR exhaust treatment component.
12. The exhaust after-treatment system according to claim 11 , wherein the electrochemical cells each include an anode, a cathode, and a power source, each of the anode and the cathode being in communication with the power source.
13. The exhaust after-treatment system according to claim 12 , wherein each of the power sources are in communication with the controller.
14. The exhaust after-treatment system according to claim 13 , wherein the power source of each cell is configured to apply a voltage to each of the anode and the cathode of each cell based on an instruction received from the controller.
15. The exhaust after-treatment system according to claim 14 , wherein the voltage applied to the anode and cathode of each cell is independently selected by the controller to vary the amounts of each of the ammonia exhaust treatment fluid and the hydrogen exhaust treatment fluid produced by each of the electrochemical cells.
16. The exhaust after-treatment system according to claim 11 , further comprising a pump between the tank and each of the electrochemical cells for providing the aqueous urea reagent from the tank to the each of the electrochemical cells, the pumps each being in communication with the controller.
17. The exhaust after-treatment system according to claim 16 , wherein a flow rate of the aqueous urea reagent to each of the electrochemical cells provided by each of the pumps is independently selected by the controller to vary a concentration of the aqueous reagent in each of the electrochemical cell.
18. The exhaust after-treatment system according to claim 17 , wherein varying the concentration of the aqueous urea reagent in each of the electrochemical cells varies a current applied to the anode and the cathode of each of the electrochemical cells to vary the amounts of each of the ammonia exhaust treatment fluid and the hydrogen exhaust treatment fluid produced by each of the electrochemical cells.
19. The exhaust after-treatment system according to claim 11 , wherein each of the electrochemical cells are in communication with a first feed line that is configured to provide the hydrogen exhaust treatment fluid produced by each of the electrochemical cells to the first injector, and each of the electrochemical cells are in communication with a second feed line that is configured to provide the ammonia exhaust treatment fluid produced by each of the electrochemical cells to the second injector.
20. An exhaust after-treatment system comprising:
an exhaust passage;
a lean-NOx trap (LNT) provided in the exhaust passage;
an SCR exhaust treatment component provided in the exhaust passage;
a tank carrying an aqueous urea reagent;
a plurality of electrochemical cells in communication with the tank and configured to receive the aqueous urea reagent therefrom, the electrochemical cells each configured to convert the aqueous reagent into a hydrogen exhaust treatment fluid and an ammonia exhaust treatment fluid;
a controller in communication with each of the electrochemical cells, the controller being configured to vary amounts of each of the hydrogen exhaust treatment fluid and the ammonia exhaust treatment fluid produced by the electrochemical cells;
a first feed line in communication with and configured to receive the hydrogen exhaust treatment fluid from each of the electrochemical cells;
a second feed line in communication with and configured to receive the ammonia exhaust treatment fluid from each of the electrochemical cells;
a plurality of first injectors in communication with the first feed line, the first injectors each being configured to dose the hydrogen exhaust treatment fluid into the exhaust passage at a location upstream from the LNT; and
a plurality of second injectors in communication with the second feed line, the second injectors each being configured to dose the ammonia exhaust treatment fluid into the exhaust passage at a location upstream from the SCR exhaust treatment component,
wherein a plurality of first valves are located between the first injectors and the first feed line, and a plurality of second valves are located between the second injectors and the second feed line.
21. The exhaust after-treatment system according to claim 20 , wherein each of the first valves and each of the second valves are in communication with the controller.
22. The exhaust after-treatment system according to claim 21 , wherein each of the first valves and each of the second valves are independently actuated by the controller to vary amounts of the ammonia exhaust treatment fluid and hydrogen exhaust treatment fluid doses into the exhaust passage.
23. The exhaust after-treatment system according to claim 20 , wherein the electrochemical cells each include an anode, a cathode, and a power source, each of the anode and the cathode being in communication with the power source.
24. The exhaust after-treatment system according to claim 23 , wherein each of the power sources are in communication with the controller.
25. The exhaust after-treatment system according to claim 24 , wherein the power source of each cell is configured to apply a voltage to each of the anode and the cathode of each cell based on an instruction received from the controller.
26. The exhaust after-treatment system according to claim 23 , wherein the voltage applied to the anode and cathode of each cell is independently selected by the controller to vary the amounts of each of the hydrogen exhaust treatment fluid and the ammonia exhaust treatment fluid produced by each of the electrochemical cells.
27. The exhaust after-treatment system according to claim 20 , further comprising a pump between the tank and each of the electrochemical cells for providing the aqueous urea reagent from the tank to the each of the electrochemical cells, the pumps each being in communication with the controller.
28. The exhaust after-treatment system according to claim 27 , wherein a flow rate of the aqueous urea reagent to each of the electrochemical cells provided by each of the pumps is independently selected by the controller to vary a concentration of the aqueous reagent in each of the electrochemical cell.
29. The exhaust after-treatment system according to claim 28 , wherein varying the concentration of the aqueous urea reagent in each of the electrochemical cells varies a current applied to the anode and the cathode of each of the electrochemical cells to vary the amounts of each of the hydrogen exhaust treatment fluid and the ammonia exhaust treatment fluid produced by each of the electrochemical cells.