Material activation system with thermal energy storage system
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.
1. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium; and
a material heating system configured to:
receive thermal energy derived from the circulated non-combustive fluid by receiving the circulated non-combustive fluid at a first inlet in the material heating system; and
apply the received thermal energy to a raw material to produce an activated material, by injecting the raw material via a second inlet positioned above the first inlet in the material heating system and directing the fluid in an up-flow configuration such that the raw material is suspended in the material heating system.
2. The material activation system of claim 1 , further comprising:
a recirculation system configured to:
recirculate an exhaust fluid output from the material heating system to the TES system as an input.
3. The material activation system of claim 2 , further comprising:
a cooling cyclone configured to:
receive the activated material from the material heating system; and
reduce a temperature of the activated material; and
wherein the recirculation system is configured to:
collect, from the cooling cyclone, the exhaust fluid for recirculation.
4. The material activation system of claim 3 , wherein the recirculation system includes:
a filter coupled between the material heating system and the TES system, wherein the filter is configured to remove particulate from the exhaust fluid prior to the exhaust fluid being provided to the TES system.
5. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium;
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material; and
a heat exchanger configured to:
receive the circulated non-combustive fluid from the TES system;
transfer heat from the circulated non-combustive fluid into a second fluid; and
provide the second fluid to the material heating system for applying the thermal energy to the raw material.
6. The material activation system of claim 5 , further comprising:
a bypass configured to inject a portion of the circulated non-combustive fluid received from the TES system into the second fluid provided to the material heating system.
7. The material activation system of claim 5 , wherein the TES system is configured to:
provide the circulated non-combustive fluid to the material heating system at a temperature within a range of from 600° C. to 1100° C.
8. The material activation system of claim 5 , wherein the non-combustive fluid is carbon dioxide.
9. The material activation system of claim 5 , wherein the storage medium includes brick.
10. The material activation system of claim 5 , wherein the material heating system includes one or more ceramic resistive heaters configured to provide additional heat to the raw material.
11. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium;
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material; and
a pre-heater configured to:
apply thermal energy derived from the circulated non-combustive fluid to heat the raw material to a first temperature; and
provide the heated raw material as an input to the material heating system for heating to a second temperature.
12. The material activation system of claim 11 , further comprising:
a burner configured to supply combustion energy to the material heating system in addition to the thermal energy supplied by the TES system.
13. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium;
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material, wherein the material heating system is configured to perform a calcination process that transforms calcium carbonate as the raw material into calcium oxide as the activated material for cement production; and
a recirculation system configured to recirculate carbon dioxide produced by the calcination process to the TES system for use as the non-combustive fluid.
14. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium; and
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material, wherein the material heating system is configured to perform a dehydroxylation process that removes hydroxide from clay minerals as the raw material to produce activated clay as the activated material.
15. The material activation system of claim 14 , further comprising:
an atmosphere reduction system coupled to the material heating system and configured to reduce an amount of oxygen in contact with the activated clay.
16. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium; and
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material, wherein the material heating system is configured to implement a Bayer process that transforms bauxite as the raw material to produce aluminum oxide as the activated material.
17. The material activation system of claim 16 , wherein the material heating system is configured to:
implement a first stage of the Bayer process that includes heating the bauxite to a temperature within a range from 300° C. to 480° C. and at a first pressure within a range of 6 bar to 8 bar;
implement a second stage of the Bayer process that includes elevating a temperature of the bauxite within a temperature range from 750° C. to 950° C. and a second pressure lower than the first pressure; and
recirculate, from the second stage to the first stage, the thermal energy derived from the circulated non-combustive fluid.
18. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium;
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material; and
a steam cycle system that includes:
a heat exchanger configured to produce steam from thermal energy recovered from the material heating system; and
a steam turbine configured to generate electricity from the produced steam.
19. A material activation system, comprising:
a thermal energy storage (TES) system configured to store thermal energy derived from an energy source by heating a storage medium using energy from the energy source and circulating a non-combustive fluid through the heated storage medium;
a material heating system configured to receive thermal energy derived from the circulated non-combustive fluid and apply the received thermal energy to a raw material to produce an activated material;
a blower configured to heat the non-combustive fluid including carbon dioxide by circulating the non-combustive fluid through the heated storage medium; and
a calciner configured to removed carbon dioxide from a supply of calcium carbonate within the material activation system, by receiving thermal energy obtained from the heated non-combustive fluid and applying the received thermal energy to the calcium carbonate.
20. The material activation system of claim 19 , wherein the calciner is configured to apply the received thermal energy by:
injecting calcium carbonate via a first inlet of the calciner; and
injecting, via a second inlet underneath the first inlet, the heated non-combustive fluid in an up-flow configuration that suspends the injected calcium carbonate within the calciner.
21. The material activation system of claim 19 , further comprising:
a heat exchanger configured to heat a second fluid by transferring thermal energy from the heated non-combustive fluid into the second fluid;
wherein the calciner is configured to apply the received thermal energy by injecting the heated second fluid into the calciner to heat the calcium carbonate.
22. The material activation system of claim 19 , further comprising:
a recirculation system configured to:
recover, from the calciner, carbon dioxide produced by the material activation system; and
recirculate the recovered carbon dioxide to the TES system for inclusion in the non-combustive fluid.
23. The material activation system of claim 19 , further comprising:
a pre-heater configured to:
receive additional thermal energy obtained from the heated non-combustive fluid;
apply the additional thermal energy to heat calcium carbonate to a first temperature; and
provide the heated calcium carbonate to the calciner for heating to a second temperature that is higher than the first temperature.