Thermal energy storage system coupled with steam cracking system
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 energy storage system provides higher-temperature heat to a steam cracking furnace system for converting a hydrocarbon feedstock into cracked gas, thereby increasing the efficiency of the temperature control.
1. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a convection section configured to preheat a hydrocarbon feedstock and dilution steam and to mix the preheated hydrocarbon feedstock with the dilution steam to provide a preheated mixture;
a radiant section configured to convert the preheated mixture into a cracked gas at high temperature;
a cooling section including at least one quench exchanger configured to quench the cracked gas;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to heat a fluid to a temperature in a target range;
a fluid movement system configured to direct the heated fluid into the steam cracking system at a high temperature as either a sole heat source or a supplementary heat source in combination with a primary heat source;
an electric booster heater configured to increase the temperature of the heated fluid prior to reaching the radiant section; and
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
2. The steam cracking system of claim 1 , wherein the energy source is a variable renewable energy source having intermittent availability.
3. The steam cracking system of claim 1 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric booster.
4. The steam cracking system of claim 1 , wherein the convection section is configured to exhaust and direct at least a portion of the heated fluid back as an input to the TES system for reheating.
5. The steam cracking system of claim 4 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
6. The steam cracking system of claim 1 , wherein the thermal energy storage medium further includes refractory material.
7. The steam cracking system of claim 1 , wherein:
the primary heat source further includes at least one fuel burner configured to produce a flame from combustion of hydrocarbon and/or hydrogen fuel with combustion air; and
the fluid movement system is further configured to inject the heated fluid along furnace refractory linings of the radiant section for radiant heat transfer from the flame to the preheated mixture.
8. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a convection section configured to preheat a hydrocarbon feedstock and dilution steam and to mix the preheated hydrocarbon feedstock with the dilution steam to provide a preheated mixture;
a radiant section configured to convert the preheated mixture into a cracked gas at high temperature;
a cooling section including at least one quench exchanger configured to quench the cracked gas;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to heat a fluid to a temperature in a target range; and
a fluid movement system configured to direct the heated fluid into the steam cracking system at a high temperature as either a sole heat source or a supplementary heat source in combination with a primary heat source,
wherein the convection section is configured to exhaust and direct at least a portion of the heated fluid back as an input to the TES system for reheating.
9. The steam cracking system of claim 8 , wherein the energy source is a variable renewable energy source having intermittent availability.
10. The steam cracking system of claim 8 , further including an electric booster heater configured to increase the temperature of the heated fluid prior to reaching the radiant section.
11. The steam cracking system of claim 10 , further including:
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system; and
a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric booster.
12. The steam cracking system of claim 8 , further configured to cool the heated fluid to remove to remove water vapor via condensation prior to input to the TES system.
13. The steam cracking system of claim 8 , wherein the thermal energy storage medium further includes refractory material.
14. The steam cracking system of claim 8 , wherein:
the primary heat source further includes at least one fuel burner configured to produce a flame from combustion of hydrocarbon and/or hydrogen fuel with combustion air; and
the fluid movement system is further configured to inject the heated fluid along furnace refractory linings of the radiant section for radiant heat transfer from the flame to the preheated mixture.
15. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a convection section configured to preheat a hydrocarbon feedstock and dilution steam and to mix the preheated hydrocarbon feedstock with the dilution steam to provide a preheated mixture;
a radiant section configured to convert the preheated mixture into a cracked gas at high temperature;
a cooling section including at least one quench exchanger configured to quench the cracked gas;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to heat a fluid to a temperature in a target range; and
a fluid movement system configured to direct the heated fluid into the steam cracking system at a high temperature as either a sole heat source or a supplementary heat source in combination with a primary heat source,
wherein the primary heat source further includes at least one fuel burner configured to produce a flame from combustion of hydrocarbon and/or hydrogen fuel with combustion air.
16. The steam cracking system of claim 15 , wherein the energy source is a variable renewable energy source having intermittent availability.
17. The steam cracking system of claim 15 , further including an electric booster heater configured to increase the temperature of the heated fluid prior to reaching the radiant section.
18. The steam cracking system of claim 17 , further including an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
19. The steam cracking system of claim 18 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric booster.
20. The steam cracking system of claim 15 , wherein the convection section is configured to exhaust and direct at least a portion of the heated fluid back as an input to the TES system for reheating.
21. The steam cracking system of claim 20 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
22. The steam cracking system of claim 15 , wherein the thermal energy storage medium further includes refractory material.
23. The steam cracking system of claim 15 , wherein the fluid movement system is further configured to inject the heated fluid along furnace refractory linings of the radiant section for radiant heat transfer from the flame to the preheated mixture.
24. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a convection section configured to preheat a hydrocarbon feedstock and dilution steam and to mix the preheated hydrocarbon feedstock with the dilution steam to provide a preheated mixture;
a radiant section configured to convert the preheated mixture into a cracked gas at high temperature;
a cooling section including at least one quench exchanger configured to quench the cracked gas;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to heat a fluid to a temperature in a target range; and
a fluid movement system configured to direct the heated fluid into the steam cracking system at a high temperature as either a sole heat source or a supplementary heat source in combination with a primary heat source,
wherein the fluid movement system is further configured to inject the heated fluid along furnace refractory linings of the radiant section for radiant heat transfer from a flame produced by combustion of hydrocarbon and/or hydrogen fuel with combustion air to the preheated mixture.
25. The steam cracking system of claim 24 , wherein the energy source is a variable renewable energy source having intermittent availability.
26. The steam cracking system of claim 24 , further including an electric booster heater configured to increase the temperature of the heated fluid prior to reaching the radiant section.
27. The steam cracking system of claim 26 , further including an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
28. The steam cracking system of claim 27 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric booster.
29. The steam cracking system of claim 24 , wherein the convection section is configured to exhaust and direct at least a portion of the heated fluid back as an input to the TES system for reheating.
30. The steam cracking system of claim 29 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
31. The steam cracking system of claim 24 , wherein the thermal energy storage medium further includes refractory material.