Oxygen-enriched combustion for natural gas combined cycle operation
AssigneeExxonMobil Technology and Engineering Company
InventorsDavid C. Calabro, Edward W. Corcoran, Jr., Neel Rangnekar, Yu Wang
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Abstract
Systems and methods are provided for operating a combined cycle power plant while enhancing the CO2 content of the flue gas generated by the power plant. The CO2 content is enhanced by using a combination of exhaust gas recycle and oxygen-enriched combustion. The oxygen-containing flow for performing the oxygen-enriched combustion can be generated by an integrated pressure swing adsorption process that allows for production of a commercial grade nitrogen stream (95 vol % or more of N2) while also providing an oxygen-containing stream with an oxygen content between 25 vol % and 48 vol % with high O2 recovery.
Claims20
A method for operating a power generation process, comprising:
- separating air using a pressure swing adsorption process to form a nitrogen-containing stream comprising 95 vol % or more of N2 and an oxygen-containing stream comprising 25 vol % to 48 vol % of O2;
- combusting a fuel with O2 from at least a portion of the oxygen-containing stream in the presence of a recycle stream in a combustion chamber of a turbine to form a flue gas, the O2 from the at least a portion of the oxygen-containing stream comprising 16 vol % to 35 vol % of a combined volume of i) the fuel, ii) the at least a portion of the oxygen-containing stream, and iii) the recycle stream, the flue gas comprising 12 vol % or more of CO2;
- forming the recycle stream from one or more first portions of the flue gas;
- and
- performing post-combustion capture on at least a second portion of the flue gas to form a CO2-containing product stream and one or more CO2-depleted flue gas streams, the one or more CO2-depleted flue gas streams comprising 30 vol % or less of the CO2 from the at least a second portion of the flue gas,
- wherein the pressure swing adsorption process comprises:
- exposing air to a sorbent having kinetic selectivity for O2 relative to N2 in a sorbent environment at a pressure of 200 kPa-a to 800 kPa-a to form an adsorption effluent comprising the nitrogen-containing stream;
- exhausting a blowdown effluent from the sorbent environment;
- purging the sorbent environment with at least a portion of the blowdown effluent to form the oxygen-containing stream;
- and
- purging the sorbent environment with a portion of the adsorption effluent.
Dependencies are inferred from the claim text.