Patent Number: 
Section: claims

1. A method of producing hydrogen, the method comprising:heating a feed stream comprising water with a high-temperature heat source to form a heated feed stream;directing the heated feed stream into a splitting device to convert the heated feed stream into a first stream comprising hydrogen and a second stream comprising oxygen; andcombusting a portion of the first stream to further heat the heated feed stream before directing the heated feed stream into the splitting device. 2. The method according to claim 1, further comprising:cooling a remaining portion of the first stream; andremoving water from the remaining portion of the first stream. 3. The method according to claim 2, further comprising combining the water with the feed stream. 4. The method according to claim 3, further comprising:cooling at least a portion of the second stream;removing water from the at least a portion of the second stream to form a third stream comprising a relatively increased fraction of oxygen; andexpanding the third stream. 5. The method according to claim 4, further comprising removing water from the expanded third stream. 6. The method according to claim 1, wherein heating the feed stream with the high-temperature heat source comprises indirectly thermally coupling a nuclear reactor with a hydrogen production facility receiving the feed stream. 7. The method according to claim 6, wherein indirectly thermally coupling the nuclear reactor with the hydrogen production facility comprises:heating a first fluid comprising a molten salt or helium with the nuclear reactor and passing the first fluid through a first heat exchanger;directly thermally coupling an intermediate heat exchange loop with the first heat exchanger; anddirectly thermally coupling the intermediate heat exchange loop with the feed stream. 8. The method according to claim 7, wherein directly thermally coupling the intermediate heat exchange loop with the first heat exchanger comprises heating a second fluid comprising a molten salt with the first heat exchanger, and wherein directly thermally coupling the intermediate heat exchange loop with the feed stream comprises passing the second fluid through a second heat exchanger and heating the feed stream with the second heat exchanger. 9. The method according to claim 7, further comprising:passing the first fluid through a second heat exchanger;heating supercritical carbon dioxide with the second heat exchanger;directing the supercritical carbon dioxide through an expansion turbine; anddriving a generator with the expansion turbine. 10. The method according to claim 1, further comprising combusting a portion of the second stream with the portion of the first stream. 11. A system for producing hydrogen comprising:a high-temperature heat source configured to heat a first coolant fluid;a hydrogen production facility configured to split molecules in a mass of water into a first stream comprising hydrogen and a second stream comprising oxygen;a water flow path configured to deliver water from a water source to the hydrogen production facility;a hydrogen flow path configured to direct produced hydrogen from the hydrogen production facility;an oxygen flow path configured to direct produced oxygen from the hydrogen production facility;at least two heat exchangers configured to thermally couple the high-temperature heat source and the water flow path;a combustor thermally coupled with the water flow path and configured to heat the water of the water flow path before the hydrogen production facility receives the water; anda diversion flow path configured to divert a portion of the produced hydrogen from the hydrogen flow path to the combustor. 12. The system of claim 11, wherein the high-temperature heat source includes a nuclear reactor. 13. The system of claim 12, wherein the at least two heat exchangers comprise:a first heat exchanger configured to exchange heat between the first coolant fluid and a second coolant fluid; anda second heat exchanger configured to exchange heat between the second coolant fluid and the water of the water flow path. 14. The system of claim 13, further comprising:a third heat exchanger configured to exchange heat between the first coolant fluid and another fluid;a expansion turbine configured to expand the another fluid; anda generator operably coupled to the expansion turbine. 15. The system of claim 14, wherein the another fluid comprises supercritical carbon dioxide. 16. The system of claim 15, wherein the first coolant fluid comprises a molten salt or helium fluid. 17. The system of claim 16, wherein the second coolant fluid comprises a molten salt or helium fluid. 18. The system of claim 11, further comprising another diversion flow path configured to divert a portion of the produced oxygen from the oxygen flow path to the combustor. 19. A plant comprising:a primary heat loop comprising:a first coolant fluid;a nuclear reactor configured to heat the first coolant fluid;a first heat exchanger positioned downstream of the nuclear reactor and configured to transfer heat from the first coolant fluid to a second coolant fluid; anda second heat exchanger positioned downstream of the first heat exchanger and configured to transfer heat from the first coolant fluid to a third coolant fluid comprising supercritical carbon dioxide;an intermediate heat exchange loop comprising:the second coolant fluid; anda third heat exchanger positioned downstream of the first heat exchanger and configured to transfer heat from the second coolant fluid to a first fluid comprising water;a power generation loop comprising:the third coolant fluid; andan expansion turbine positioned downstream of the second heat exchanger and configured to expand the third coolant fluid; andat least one hydrogen production facility thermally coupled to the third heat exchanger and configured to produce hydrogen gas and oxygen gas from the first fluid. 20. The plant of claim 19, further comprising:a fourth heat exchanger positioned upstream of the third heat exchanger and configured to heat the first fluid;a combustor positioned downstream of the third heat exchanger and configured to heat the first fluid; andan electrolyzer positioned downstream of the combustor and configured to split the first fluid into a third fluid comprising hydrogen and a fourth fluid comprising oxygen. 21. The plant of claim 20, further comprising a first gas-liquid separator positioned downstream of the electrolyzer and configured to remove a fifth fluid comprising water from the third fluid. 22. The plant of claim 21, further comprising a mixer positioned downstream of the gas-liquid separator and configured to combine the fifth fluid with the first fluid. 23. The plant of claim 21, further comprising a second gas-liquid separator positioned downstream of the electrolyzer, in parallel with the first gas-liquid separator, and configured to remove a sixth fluid comprising water from the fourth fluid. 24. The plant of claim 19, wherein the intermediate heat exchange loop further comprises a fourth heat exchanger positioned downstream of the first heat exchanger, in parallel with the third heat exchanger, and configured to transfer heat from the second coolant fluid to a third fluid comprising water.