Generating power using an ion transport membrane
View Patent ↗A system may include a compressor, a heat exchanger and an ITM. The compressor is configured to receive an air stream and compress the air stream to generate a pressurized stream. The heat exchanger is configured to receive the pressured stream and indirectly heat the pressurized stream using heat from an oxygen stream from an Ion Transport Membrane (ITM). The ITM is configured to receive the heated pressurized stream and generate an oxygen stream and the non-permeate stream, wherein the non-permeate stream is passed to a gas turbine burner and the oxygen stream is passed to the heat exchanger.
1. A method, comprising:
discharging, from a turbine compressor, an air stream in connection with compressing air used during combustion in a gas turbine;
compressing the air stream to generate a pressurized stream;
indirectly heating the pressurized stream using heat from an oxygen stream from an Ion Transport Membrane (ITM);
generating the oxygen stream and a non-permeate stream using the ITM, wherein the non-permeate stream is passed to a gas turbine burner and the oxygen stream is passed to a first heat exchanger;
combusting a fuel gas in combination with the non-permeate stream to generate a heated non-permeate stream, wherein a temperature of the combination of the fuel gas and the non-permeate stream is below a predefined threshold temperature for a gas turbine burner, and a concentration of oxygen in the heated non-permeate stream is such that when mixed with a fuel gas stream results in an oxygen concentration below a lower flammable limit of the mixture;
heating at least a portion of the pressurized stream using heat from the heated non-permeate stream, wherein the heated non-permeate stream is cooled during the indirect heating; and
mixing the cooled non-permeate stream with the fuel gas for the gas turbine or introducing the cooled non-permeate stream at a point between the turbine compressor and an expander.
2. A method of claim 1 , wherein 40% and 60% of the heated pressurized stream is received from an air compressor which is separate from the gas turbine.
3. The method of claim 1 , wherein the heated non-permeate stream is about 800° C. or higher.
4. The method of claim 1 , wherein an oxygen concentration of the heated non-permeate stream is about below 2.5% or less molar concentration.
5. The method of claim 1 , wherein the heated pressurized stream is a range from about 800° C. to about 900° C.
6. The method of claim 1 , wherein the heated pressurized stream is at a pressure in a range from about 2 bars to 10 bars.