Architectures for electrochemical systems
View Patent ↗The present invention generally relates to electrochemical systems for producing hydrogen and/or power. Various aspects of the invention are directed to reactor designs for producing hydrogen and/or power from a fuel and water, conducting ceramics and other materials for such systems, including mixed ionically and electrically conducting ceramics which can be used for hydrogen gas generation, control systems for such systems, and methods of operating such systems.
1. A system, comprising:
a source of fuel;
a source of water;
a housing;
an oxidation chamber in fluidic communication with the source of fuel and a source of oxidant, the oxidation chamber operative to produce an output product stream including oxidized fuel;
a reaction chamber downstream from and in fluidic communication with the oxidation chamber and configured to receive a single fuel input stream consisting of the output product stream including oxidized fuel from the oxidation chamber, the reaction chamber operative to produce a further output stream including further oxidized fuel;
a cleanup chamber downstream from and in fluidic communication with the reaction chamber and the source of oxidant, the cleanup chamber operative to further oxidize any unoxidized products present in the further output stream from the reaction chamber; and
a water conversion chamber, contained within but fluidically separate from the reaction chamber at least in part by a mixed ionically and electronically conductive material to supply ions to the reaction chamber for reaction within the reaction chamber to produce the further output stream, the water conversion chamber in fluidic communication with the source of water, the water conversion chamber operative to produce a hydrogen output product stream fluidically separate from the reaction chamber and the further output stream;
wherein water from the source of water enters the water conversion chamber through a water input port;
wherein the hydrogen output product stream exits the water conversion chamber through a hydrogen output port;
wherein each of the oxidation chamber, the reaction chamber, the water conversion chamber within the reaction chamber, and the cleanup chamber are contained within the housing;
wherein the hydrogen output product stream is substantially pure and free of contaminants;
wherein the cleanup chamber is configured to receive a single input stream from the reaction chamber consisting of the further output stream of the reaction chamber; and
wherein the water conversion chamber, the water input port and the hydrogen output port are all disposed within the reaction chamber.
2. The system of claim 1 , wherein the mixed ionically and electronically conductive material comprises a ceramic.
3. The system of claim 2 , wherein the mixed ionically and electronically conductive material is substantially gas impermeable.
4. The system of claim 2 , further comprising a porous substrate in physical contact with the mixed ionically and electronically conductive material.
5. The system of claim 2 , wherein the material comprises YSZ.
6. The system of claim 2 , wherein the material comprises YST.
7. The system of claim 2 , wherein the material comprises YLST.
8. The system of claim 2 , wherein the material comprises ScCeST.
9. The system of claim 2 , wherein the mixed ionically and electronically conductive material comprises a first phase comprising a ceramic ionic conductor and a second phase comprising a ceramic electrical conductor.
10. The system of claim 9 , wherein the first phase comprises YSZ.
11. The system of claim 9 , wherein the first phase comprises zirconia.
12. The system of claim 11 , wherein the zirconia is stabilized in a cubic structure using one or more dopants.
13. The system of claim 11 , wherein the zirconia is stabilized using Y.
14. The system of claim 13 , wherein Y is present in a mole ratio of between about 5 mol % and about 10 mol %.
15. The system of claim 11 , wherein the zirconia is stabilized using Sc.
16. The system of claim 15 , wherein Sc is present in a mole ratio of between about 5 mol % and about 15 mol %.
17. The system of claim 9 , wherein the first phase comprises an oxide including at least cerium oxide and gadolinium oxide.
18. The system of claim 9 , wherein the first phase comprises a La-ferrite material.
19. The system of claim 9 , wherein the first phase comprises Gd 2 O 3 doped with Ce.
20. The system of claim 9 , wherein the first phase comprises a doped LaFeO 3 .
21. The system of claim 20 , wherein the doped LaFe03 is doped with one or more of Sr, Ca, Ga, or Fe.
22. The system of claim 9 , wherein the second phase comprises a LST material.
23. The system of claim 9 , wherein the second phase comprises a YST material.
24. The system of claim 9 , wherein the second phase comprises a LCC material.
25. The system of claim 9 , wherein the second phase comprises a YLST material.
26. The system of claim 9 , wherein the second phase comprises a ScCeST material.
27. The system of claim 9 , wherein the first phase is interconnected throughout the mixed ionically and electronically conductive material such that the material is ionically conductive, and the second phase is interconnected throughout the mixed ionically and electronically conductive material such that the material is electronically conductive.
28. The system of claim 2 , further comprising at least one electrode positioned adjacent the mixed ionically and electronically conductive material.
29. The system of claim 28 , wherein the electrode is porous.
30. The system of claim 28 , wherein the electrode has a composition similar to the composition of the mixed ionically and electronically conductive material.
31. The system of claim 28 , comprising at least two electrodes positioned adjacent the mixed ionically and electronically conductive material.
32. The system of claim 1 , further comprising a polishing chamber in fluidic communication with the water conversion chamber.
33. The system of claim 32 , wherein the polishing chamber comprises a catalyst for catalyzing a reaction of CO and H 2 to CH 4 and H 2 O.
34. The system of claim 33 , wherein the polishing chamber comprises ruthenium.
35. The system of claim 33 , wherein the polishing chamber comprises platinum.
36. The system of claim 1 , further comprising a fuel cell in fluidic communication with the water conversion chamber.
37. The system of claim 36 , wherein the fuel cell is a solid oxide fuel cell.
38. The system of claim 1 , further comprising a power-generating device, able to produce power by consuming H 2 , in fluidic communication with the water conversion chamber.
39. The system of claim 1 , further comprising a hydrogen collection chamber in fluidic communication with the water conversion chamber.
40. The system of claim 39 , wherein the hydrogen collection chamber is in fluidic communication with a water inlet to the water conversion chamber via a gas conduit.
41. The system of claim 40 , further comprising a gas pump able to pump gas within the gas conduit.
42. The system of claim 1 , wherein the source of fuel comprises a carbonaceous fuel.
43. The system of claim 1 , wherein the source of fuel comprises an oxidizable fuel.
44. The system of claim 1 , wherein the source of fuel comprises a gasified fuel.
45. The system of claim 44 , wherein the source of fuel comprises gasified coal.
46. The system of claim 44 , wherein the source of fuel comprises a gasified hydrocarbon.
47. The system of claim 1 , further comprising a fluidic connection such that at least a portion of hydrogen generated in the water conversion chamber is captured downstream of the water conversion chamber and mixed with the water upstream of the water conversion chamber.
48. The system of claim 47 , wherein the fluidic connection comprises a pump.
49. The system of claim 1 , wherein the source of oxidant provides an oxidant consisting of air.