Steam use and safety systems
A solid oxide electrolyzer cell (SOEC) system including a stack of electrolyzer cells configured to receive water or steam in combination with hydrogen, and a steam recycle outlet configured to recycle a portion of the water or steam.
1. A solid oxide electrolyzer cell (SOEC) system comprising:
a stack of electrolyzer cells configured to receive water or steam in combination with hydrogen;
a hydrogen conduit fluidly connected to the stack of electrolyzer cells and configured to provide external hydrogen to the stack of electrolyzer cells when the SOEC system is in startup, and to cease providing the external hydrogen to the stack of electrolyzer cells when the SOEC system is operating at steady state;
a recycle steam inlet;
a hydrogen product outlet fluidly connected to the recycle steam inlet, and configured to recycle a portion of a hydrogen and steam exhaust from the hydrogen product outlet into the recycle steam inlet when the SOEC system is operating at the steady state;
a hotbox that encloses the stack of electrolyzer cells;
an enriched air blower; and
an enriched air conduit fluidly connecting an enriched air outlet of the hotbox to the enriched air blower;
an air blower;
an air conduit fluidly connecting the air blower to an air inlet of the hotbox; and
wherein the stack of electrolyzer cells is configured to cease receiving hydrogen when the SOEC system detects a safety event, and the enriched air blower continues to operate and ventilate a cabinet of the hotbox during the safety event.
2. The SOEC of claim 1 , further comprising a steam recycle outlet configured to recycle a portion of the water or steam.
3. The SOEC system of claim 2 , wherein steam output by the recycle steam outlet is configured to be mixed with hydrogen and a combination of steam and hydrogen is configured to be supplied to the recycle steam inlet.
4. The SOEC system of claim 2 , wherein steam output by the recycle steam outlet is configured to be vaporized, mixed with hydrogen, and supplied to the recycle steam inlet.
5. The SOEC system of claim 2 , wherein steam output by the recycle steam outlet is configured to be regulated by a water management system, mixed with hydrogen, and supplied to the recycle steam inlet.
6. The SOEC system of claim 1 , further comprising a splitter that supplies a portion of the hydrogen and steam exhaust to a steam recycle blower.
7. The SOEC system of claim 6 , wherein a recycled portion of the hydrogen and steam exhaust includes steam and does not include hydrogen.
8. The SOEC system of claim 1 , wherein the stack of electrolyzer cells is further configured to receive the external hydrogen when the SOEC system is in shutdown, or when the SOEC system is not producing hydrogen.
9. The SOEC system of claim 1 , wherein the safety event is detected by a pressure detector or a thermal detector.
10. The SOEC system of claim 1 , wherein a combination of steam, hydrogen, and heated deionized water is configured to be supplied to the recycle steam inlet.
11. The SOEC system of claim 1 , wherein the air blower and the enriched air blower are each located outside of the hotbox.
12. A method of operating a solid oxide electrolyzer cell (SOEC) system comprising:
receiving, at a stack of electrolyzer cells, water or steam in combination with hydrogen, wherein the stack of electrolyzer cells is located in a hotbox;
providing air to the stack of electrolyzer cells using an air blower;
providing external hydrogen to the stack of electrolyzer cells at startup of the SOEC system;
ceasing providing the external hydrogen to the stack of electrolyzer cells during steady state operation of the SOEC system; and
recycling a portion of a hydrogen and steam exhaust from the stack of electrolyzer cells into the stack of electrolyzer cells during the steady state operation of the SOEC system;
removing enriched air from the hotbox during the steady state operation of the SOEC system using an enriched air blower; and
ventilating a cabinet of the hotbox during a safety event using the enriched air blower.
13. The method of claim 12 , wherein the enriched air has a temperature between 120 degrees C. and 300 C and a pressure between 0.05 psig and 0.5 psig.
14. The method of claim 12 , wherein the air blower and the enriched air blower are each located outside of the hotbox.