System to convert coke in fluid catalytic cracking process by utilizing metal oxides with in-situ CO2 capture
AssigneeExxonMobil Technology and Engineering Company
InventorsHyung Rae Kim, Arun K. Sharma, Bing Du
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Abstract
This disclosure relates to methods for reducing CO2 emissions from a fluid catalytic cracking process by providing a chemical looping system comprising a regenerator and reducer reactor, an oxidizer reactor, and a combustor reactor, and by sequestering the carbon dioxide of a CO2 and H2O stream. Also, this disclosure relates to methods for reducing CO2 emissions from a fluid catalytic cracking process by partially oxidizing catalyst coke particles in a fluid catalytic cracking regenerator reactor to produce synthesis gas, and by providing a chemical looping system comprising a reducer reactor, an oxidizer reactor, and a combustor reactor.
Claims17
A method for reducing CO2 emissions from a fluid catalytic cracking process by
- a) providing a chemical looping system comprising a regenerator and reducer reactor, an oxidizer reactor and a combustor reactor;
- i) feeding catalyst coke particles and metal oxide particles into the regenerator and reducer reactor of the chemical looping system to produce a plurality of streams comprising a regenerated catalyst stream, a CO2 and H2O stream and a reduced metal oxide particle stream;
- ii) feeding the stream of reduced metal oxide particles and a stream of water vapor into the oxidizer reactor of the chemical looping system to produce a plurality of streams comprising a hydrogen stream and a stream of oxidized metal oxide particles;
- and
- iii) feeding the stream of oxidized metal oxide particles and a stream of air into the combustor reactor of the chemical looping system to produce heat and a stream of metal oxide particles;
- and
- b) sequestering the carbon dioxide of the CO2 and H2O stream of step (a)(i) to reduce the CO2 emissions from the regenerator and reducer reactor.
Dependencies are inferred from the claim text.