High temperature thermochemical energy storage system
US-2017362090-A1 · Dec 21, 2017 · US
US12188380B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12188380-B2 |
| Application number | US-202418403991-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 4, 2024 |
| Priority date | Nov 30, 2020 |
| Publication date | Jan 7, 2025 |
| Grant date | Jan 7, 2025 |
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An energy storage system converts variable renewable electricity (VRE) to continuous heat at over 1000° C. Intermittent electrical energy heats a solid medium. Heat from the solid medium is delivered continuously on demand. An array of bricks incorporating internal radiation cavities is directly heated by thermal radiation. The cavities facilitate rapid, uniform heating via reradiation. Heat delivery via flowing gas establishes a thermocline which maintains high outlet temperature throughout discharge. Gas flows through structured pathways within the array, delivering heat which may be used for processes including calcination, hydrogen electrolysis, steam generation, and thermal power generation and cogeneration. Groups of thermal storage arrays may be controlled and operated at high temperatures without thermal runaway via deep-discharge sequencing. Forecast-based control enables continuous, year-round heat supply using current and advance information of weather and VRE availability. High-voltage DC power conversion and distribution circuitry improves the efficiency of VRE power transfer into the system.
Opening claim text (preview).
What is claimed is: 1. A calcination system, including: a thermal energy storage (TES) system configured to store thermal energy derived from a renewable energy source, wherein the TES system includes: a thermal energy storage medium; a heating element configured to heat the storage medium using electricity from the renewable energy source; and a heat transfer system configured to transfer thermal energy from the heated storage medium to the calcination system; the calcination system being configured to remove carbon dioxide from a supply of calcium carbonate by: receiving the thermal energy from the heat transfer system; and applying the received thermal energy to the calcium carbonate. 2. The calcination system of claim 1 , further including a recirculation system configured to recirculate an exhaust fluid output to the TES system as an input. 3. The calcination system of claim 2 , wherein the TES system is configured to recover thermal energy from the recirculated exhaust fluid output. 4. The calcination system of claim 2 , further including a cooling cyclone configured to: receive calcium carbonate; and reduce a temperature of the calcium carbonate, wherein the recirculation system is configured to collect, from the cooling cyclone, the exhaust fluid for recirculation. 5. The calcination system of claim 2 , wherein the recirculation system includes a filter coupled to the TES system, wherein the filter is configured to remove particulate matter from the exhaust fluid prior to the exhaust fluid being provided to the TES system. 6. The calcination system of claim 1 , wherein the storage medium includes refractory material. 7. The calcination system of claim 1 , further configured to generate calcium oxide by application of the received thermal energy to the calcium carbonate. 8. The calcination system of claim 7 , further configured to provide the calcium oxide to a cement production system. 9. The calcination system of claim 1 , wherein the heat transfer system is configured to radiatively extract heat from the heated storage medium. 10. The calcination system of claim 1 , further including a thermophotovoltaic cogeneration system configured to convert at least some radiative heat from the heated storage medium to electricity. 11. The calcination system of claim 1 , further including one or more ceramic resistive heaters configured to provide additional heat to the calcium carbonate. 12. The calcination system of claim 1 , further including a burner configured to supply combustion energy in addition to the thermal energy supplied by the TES system. 13. The calcination system of claim 1 , further including a heat exchanger configured to produce steam using thermal energy recovered from an exhaust fluid output of the calcination system. 14. The calcination system of claim 13 , further including a steam turbine configured to generate electricity using the produced steam. 15. The calcination system of claim 1 , wherein the storage medium includes alumina, magnetite, olivine, or a combination thereof. 16. The calcination system of claim 1 , wherein the heating element includes a conductive ceramic material. 17. The calcination system of claim 1 , wherein the storage medium includes a conductive ceramic material. 18. A method for calcination, including: receiving, by a thermal energy storage (TES) system, energy supplied by an energy source; storing, by the TES system, the received energy as thermal energy by heating a storage medium with the received energy; transferring, by a heat transfer system, thermal energy from the heated storage medium to a calcination system; receiving, at the calcination system, the transferred thermal energy; and applying, by the calcination system, the received thermal energy to calcium carbonate. 19. The method of claim 18 , further including recirculating an exhaust fluid output to the TES system as an input. 20. The method of claim 19 , further including recovering thermal energy from the recirculated exhaust fluid output. 21. The method of claim 19 , further including: receiving calcium carbonate in a cooling cyclone; reducing a temperature of the calcium carbonate; and collecting, from the cooling cyclone, the exhaust fluid for recirculation. 22. The method of claim 19 , further including remove particulate matter from the exhaust fluid using a filter prior to the exhaust fluid being provided to the TES system. 23. The method of claim 18 , further including generating calcium oxide by application of the received thermal energy to the calcium carbonate. 24. The method of claim 23 , further including providing the calcium oxide to a cement production system. 25. The method of claim 18 , further including producing steam using thermal energy recovered from an exhaust fluid output of the calcination system. 26. The method of claim 18 , further including radiatively extracting, at the heat transfer system, heat from the heated storage medium. 27. The method of claim 18 , further including converting, by a thermophotovoltaic cogeneration system, at least some radiative heat from the heated storage medium to electricity. 28. A calcination system, including: a thermal energy storage (TES) system configured to store thermal energy derived from a renewable energy source, wherein the TES system includes: a heating element configured to heat a storage medium using electricity from the renewable energy source; and a fluid heating system configured to heat a non-combustive fluid including carbon dioxide with the thermal energy from the heated storage medium; the calcination system being configured to remove carbon dioxide from a supply of calcium carbonate by: receiving thermal energy obtained from the non-combustive fluid; and applying the received thermal energy to the calcium carbonate. 29. The calcination system of claim 28 , wherein the fluid heating system is configured to radiatively extract heat from the heated storage medium to heat the non-combustive fluid. 30. The calcination system of claim 28 , further including a thermophotovoltaic cogeneration system configured to convert at least some radiative heat from the heated storage medium to electricity. 31. The method of claim 18 , wherein the heat transfer system includes a fluid heating system, and wherein transferring thermal energy from the heated storage medium to the calcination system includes: heating, by the fluid heating system, a non-combustive fluid including carbon dioxide with the thermal energy from the heated storage medium; receiving, at the calcination system, thermal energy obtained from the non-combustive fluid; and applying, by the calcination system, the received thermal energy to the calcium carbonate to remove carbon dioxide from the calcium carbonate. 32. The method of claim 31 , further including radiatively extracting, at the fluid heating system, heat from the heated storage medium. 33. The method of claim 31 , further including converting, by a thermophotovoltaic cogeneration system, at least some radiative heat from the heated storage medium to electricity. 34. A calcination system, including: a thermal energy storage (TES) system configured to store thermal energy derived from a renewable e
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