| CPC F01K 3/02 (2013.01) [B63H 11/00 (2013.01); F01K 3/08 (2013.01); F01K 3/186 (2013.01); F01K 13/02 (2013.01); F01K 15/00 (2013.01); F03G 6/071 (2021.08); F22B 29/06 (2013.01); F22B 35/10 (2013.01); F28D 20/00 (2013.01); H01M 8/04014 (2013.01); H01M 8/04029 (2013.01); H01M 8/04037 (2013.01); H01M 8/04052 (2013.01); H01M 8/04074 (2013.01); H02J 1/102 (2013.01); H02J 3/00 (2013.01); H02J 3/04 (2013.01); H02M 1/0003 (2021.05); H02M 1/007 (2021.05); B63H 11/12 (2013.01); B63H 11/14 (2013.01); B63H 11/16 (2013.01); F01K 11/02 (2013.01); F01K 19/04 (2013.01); F03D 9/18 (2016.05); F28D 2020/0004 (2013.01); Y02E 60/14 (2013.01)] | 64 Claims |

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1. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, including:
a convection section configured to preheat a hydrocarbon feedstock and/or dilution steam and to mix the hydrocarbon feedstock with the dilution steam to provide a preheated mixture;
a radiant section configured to be heated and 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 TES 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 to one or both of the convection section and the radiant section; and
one or more fuel burners configured to burn a fuel source that includes greater than about 0.5% molecular hydrogen, wherein the fluid movement system is further configured to stabilize a burner flame by supplying the heated fluid directly to the one or more fuel burners.
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