Energy storage system and alumina calcination applications
An energy storage system (TES) 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. Heat delivery via flowing gas establishes a thermocline which maintains high outlet temperature throughout discharge. The delivered heat which may be used for processes including power generation and cogeneration. In one application, the TES provides higher-temperature heat through non-combustible fluid to an alumina calcination system used to remove impurities or volatile substances and/or to incur thermal decomposition to a desired product.
1. A calcination system, including:
a thermal energy storage (TES) system configured to store thermal energy derived from a variable renewable energy source having intermittent availability, wherein the TES system is configured to deliver heat to a use in the form of a heated fluid; and
a calciner configured to receive and heat a material stream with thermal energy provided by a heated fluid source and generate a calcined product;
wherein the heated fluid source includes a primary fuel burner configured to provide a first portion of the thermal energy required by the calciner to generate the calcined product and wherein the TES system provides a second portion of the thermal energy to the calciner to generate the calcined product, and
wherein the calcination system is configured to recirculate a portion of exhaust gas from the calciner into the TES system for reheating.
2. The calcination system of claim 1 , wherein the second portion of the thermal energy provided by the TES system is heated fluid.
3. The calcination system of claim 1 , wherein the TES system is configured to provide the heated fluid to the calciner as direct heated fluid.
4. The calcination system of claim 1 , wherein the TES system is configured to provide the heated fluid to a steam generator to generate steam for use in steam partial calcination.
5. The calcination system of claim 1 , wherein the primary fuel burner is configured to operate with combustion air having a higher oxygen composition by volume than in ambient air.
6. The calcination system of claim 1 , wherein the TES system is configured to provide the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature.
7. The calcination system of claim 1 , wherein the primary fuel burner is configured to burn a fuel source that includes greater than 0.5% molecular hydrogen.
8. The calcination system of claim 1 , further including:
a heat exchanger configured to produce steam from exhaust gas exiting the calciner; and
a turbine configured to generate electricity using the produced steam.
9. A method for using a calcination system, the method including:
storing thermal energy in a thermal energy storage (TES) system, wherein the thermal energy is derived from a variable renewable energy source having intermittent availability;
receiving a material stream at a calciner;
extracting a first portion of thermal energy from a primary fuel burner;
extracting a second portion of thermal energy from the TES system; and
providing the first and second portions of thermal energy to the calciner to generate a calcined product from the material stream; and
recirculating a portion of exhaust gas from the calciner back into the TES system for reheating.
10. The method of claim 9 , wherein the second portion of thermal energy includes a heated fluid.
11. The method of claim 10 , further including the step of providing the heated fluid to the calciner as direct heated fluid.
12. The method of claim 10 , further including the step of providing the heated fluid to generate steam for use in steam partial calcination.
13. The method of claim 9 , further including the step of operating the primary fuel burner with combustion air having a higher oxygen composition by volume than in ambient air.
14. The method of claim 9 , further including the step of providing the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature so that the calciner receives higher-temperature heat.
15. The method of claim 9 , further including the step of burning a fuel source at the primary fuel burner, wherein the fuel source includes greater than 0.5% molecular hydrogen.
16. The method of claim 9 , further including the step of using a heat exchanger to produce steam from exhaust gas exiting the calciner; and using a turbine to generate electricity using the produced steam.
17. A calcination system, including:
a thermal energy storage (TES) system configured to store thermal energy derived from a variable renewable energy source having intermittent availability, wherein the TES system is configured to deliver heat to a use in the form of a heated fluid; and
a calciner configured to receive and heat a material stream with thermal energy provided by a heated fluid source and generate a calcined product;
wherein the heated fluid source includes a primary fuel burner configured to provide a first portion of the thermal energy required by the calciner to generate the calcined product and wherein the TES system provides a second portion of the thermal energy to the calciner to generate the calcined product, and
wherein the TES system is configured to provide the heated fluid to the calciner as direct heated fluid.
18. The calcination system of claim 17 , wherein the second portion of the thermal energy provided by the TES system is heated fluid.
19. The calcination system of claim 17 , wherein the TES system is configured to provide the heated fluid to the calciner as direct heated fluid.
20. The calcination system of claim 17 , wherein the primary fuel burner is configured to operate with combustion air having a higher oxygen composition by volume than in ambient air.
21. The calcination system of claim 17 , configured to provide the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature.
22. The calcination system of claim 17 , wherein the primary fuel burner is configured to burn a fuel source that includes greater than 0.5% molecular hydrogen.
23. The calcination system of claim 17 , further including:
a heat exchanger configured to produce steam from exhaust gas exiting the calciner; and
a turbine configured to generate electricity using the produced steam.
24. A method for using a calcination system, the method including:
storing thermal energy in a thermal energy storage (TES) system, wherein the thermal energy is derived from a variable renewable energy source having intermittent availability;
receiving a material stream at a calciner;
extracting a first portion of thermal energy from a primary fuel burner;
extracting a second portion of thermal energy from the TES system;
providing the first and second portions of thermal energy to the calciner to generate a calcined product from the material stream; and
providing the heated fluid to generate steam for use in steam partial calcination.
25. The method of claim 24 , wherein the second portion of thermal energy includes a heated fluid.
26. The method of claim 24 , further including the step of providing the heated fluid to the calciner as direct heated fluid.
27. The method of claim 24 , further including the step of operating the primary fuel burner with combustion air having a higher oxygen composition by volume than in ambient air.
28. The method of claim 24 , further including the step of providing the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature so that the calciner receives higher-temperature heat.
29. The method of claim 24 , further including the step of burning a fuel source at the primary fuel burner, wherein the fuel source includes greater than 0.5% molecular hydrogen.
30. The method of claim 24 , further including the step of using a heat exchanger to produce steam from exhaust gas exiting the calciner; and using a turbine to generate electricity using the produced steam.
31. A calcination system, including:
a thermal energy storage (TES) system configured to store thermal energy derived from a variable renewable energy source having intermittent availability, wherein the TES system is configured to deliver heat to a use in the form of a heated fluid; and
a calciner configured to receive and heat a material stream with thermal energy provided by a heated fluid source and generate a calcined product;
wherein the heated fluid source includes a primary fuel burner configured to provide a first portion of the thermal energy required by the calciner to generate the calcined product and wherein the TES system provides a second portion of the thermal energy to the calciner to generate the calcined product, and
wherein the TES system is configured to provide the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature.
32. The calcination system of claim 31 , wherein the second portion of the thermal energy provided by the TES system is heated fluid.
33. The calcination system of claim 31 , wherein the TES system is configured to provide the heated fluid to the calciner as direct heated fluid.
34. The calcination system of claim 31 , wherein the primary fuel burner is configured to operate with combustion air having a higher oxygen composition by volume than in ambient air.
35. The calcination system of claim 31 , wherein the primary fuel burner is configured to burn a fuel source that includes greater than 0.5% molecular hydrogen.
36. The calcination system of claim 31 , further including:
a heat exchanger configured to produce steam from exhaust gas exiting the calciner; and
a turbine configured to generate electricity using the produced steam.
37. A calcination system, including:
a thermal energy storage (TES) system configured to store thermal energy derived from a variable renewable energy source having intermittent availability, wherein the TES system is configured to deliver heat to a use in the form of a heated fluid; and
a calciner configured to receive and heat a material stream with thermal energy provided by a heated fluid source and generate a calcined product;
wherein the heated fluid source includes a primary fuel burner configured to provide a first portion of the thermal energy required by the calciner to generate the calcined product and wherein the TES system provides a second portion of the thermal energy to the calciner to generate the calcined product;
a heat exchanger configured to produce steam from exhaust gas exiting the calciner; and
a turbine configured to generate electricity using the produced steam.
38. The calcination system of claim 37 , wherein the second portion of the thermal energy provided by the TES system is heated fluid.
39. The calcination system of claim 37 , wherein the TES system is configured to provide the heated fluid to the calciner as direct heated fluid.
40. The calcination system of claim 37 , wherein the primary fuel burner is configured to operate with combustion air having a higher oxygen composition by volume than in ambient air.
41. The calcination system of claim 37 , wherein the primary fuel burner is configured to burn a fuel source that includes greater than 0.5% molecular hydrogen.
42. A method for using a calcination system, the method including:
storing thermal energy in a thermal energy storage (TES) system, wherein the thermal energy is derived from a variable renewable energy source having intermittent availability;
receiving a material stream at a calciner;
extracting a first portion of thermal energy from a primary fuel burner;
extracting a second portion of thermal energy from the TES system;
providing the first and second portions of thermal energy to the calciner to generate a calcined product from the material stream; and
providing the second portion of thermal energy to one or more burner inputs of the primary fuel burner to increase flame temperature so that the calciner receives higher-temperature heat.
43. The method of claim 42 , wherein the second portion of thermal energy includes a heated fluid.
44. The method of claim 42 , further including the step of providing the heated fluid to the calciner as direct heated fluid.
45. The method of claim 42 , further including the step of operating the primary fuel burner with combustion air having a higher oxygen composition by volume than in ambient air.
46. The method of claim 42 , further including the step of burning a fuel source at the primary fuel burner, wherein the fuel source includes greater than 0.5% molecular hydrogen.
47. The method of claim 42 , further including the step of using a heat exchanger to produce steam from exhaust gas exiting the calciner; and using a turbine to generate electricity using the produced steam.
48. A method for using a calcination system, the method including:
storing thermal energy in a thermal energy storage (TES) system, wherein the thermal energy is derived from a variable renewable energy source having intermittent availability;
receiving a material stream at a calciner;
extracting a first portion of thermal energy from a primary fuel burner;
extracting a second portion of thermal energy from the TES system;
providing the first and second portions of thermal energy to the calciner to generate a calcined product from the material stream;
using a heat exchanger to produce steam from exhaust gas exiting the calciner; and
using a turbine to generate electricity using the produced steam.
49. The method of claim 48 , wherein the second portion of thermal energy includes a heated fluid.
50. The method of claim 48 , further including the step of providing the heated fluid to the calciner as direct heated fluid.
51. The method of claim 48 , further including the step of operating the primary fuel burner with combustion air having a higher oxygen composition by volume than in ambient air.
52. The method of claim 48 , further including the step of burning a fuel source at the primary fuel burner, wherein the fuel source includes greater than 0.5% molecular hydrogen.