Method and system for power production with improved efficiency
The present disclosure relates to systems and methods that provide power generation using predominantly CO 2 as a working fluid. In particular, the present disclosure provides for the use of a portion of the heat of compression from a CO 2 compressor as the additive heating necessary to increase the overall efficiency of a power production system and method.
1. A method for heating a recirculating gas stream comprising:
passing a heated exhaust gas stream through a recuperative heat exchanger to withdraw heat therefrom and form a cooled gas stream;
separating the cooled gas stream into at least a first fraction and a second fraction;
compressing the first fraction of the cooled gas stream to form a compressed first fraction gas stream;
compressing the second fraction of the gas stream so as to add heat to the second fraction of the gas stream and form a compressed second fraction gas stream;
combining the compressed first fraction gas stream and the compressed second fraction gas stream to form a combined recirculating gas stream; and
pumping the combined recirculating gas stream to a pressure that is greater than a pressure of the compressed first fraction gas stream and greater than a pressure of the compressed second fraction gas stream;
wherein the combined recirculating gas stream is heated using the heat withdrawn from the heated exhaust gas stream and the heat added to the second fraction of the gas stream.
2. The method according to claim 1 , wherein heat is added to the second fraction of the gas stream so that the compressed second fraction gas stream is at a temperature of 100° C. to 400° C.
3. The method according to claim 1 , wherein the combined recirculating gas stream is pumped to a pressure of 100 bar (10 MPa) to 500 bar (50 MPa).
4. The method according to claim 1 , wherein compressing the second fraction of the gas stream comprises multi-stage compression with no intercooling.
5. The method according to claim 1 , comprising withdrawing the heat that was added to the second fraction of the gas stream fraction and providing said heat to the combined recirculating gas stream after said pumping.
6. The method according to claim 1 , wherein the recuperative heat exchanger comprises at least two heat exchangers or at least two heat exchange sections in series.
7. The method according to claim 1 , further comprising adding heat to the combined recirculating gas stream after said pumping, wherein the heat added to the combined recirculating gas stream is derived from one or both of an air separation unit and a gas turbine.
8. The method according to claim 1 , wherein after heating the combined recirculating gas stream using the heat withdrawn from the heated exhaust gas stream and the heat added to the second fraction of the gas stream, the method further comprises passing the combined recirculating gas stream to a combustor that combusts a fuel with oxygen to form a combustion product stream.
9. A method of generating power, the method comprising:
expanding a compressed CO 2 containing stream through a turbine to expand the compressed CO 2 containing stream, generate power, and form a turbine exhaust stream;
withdrawing heat from the turbine exhaust stream;
dividing the turbine exhaust stream to form a first turbine exhaust portion and second turbine exhaust portion;
compressing the first turbine exhaust portion to form a main recycle CO 2 stream;
compressing the second turbine exhaust portion to add heat thereto and form a secondary recycle CO 2 stream;
combining the main recycle CO 2 stream and the secondary recycle CO 2 stream to form a combined recycle CO 2 stream; and
compressing the combined recycle CO 2 stream;
wherein the combined recycle CO 2 stream is heated using the heat withdrawn from the turbine exhaust stream and the heat added to the second turbine exhaust portion.
10. The method according to claim 9 , wherein the CO 2 containing stream has a temperature of 500° C. to 1,700° C. and a pressure of 100 bar (10 MPa) to 500 bar (50 MPa).
11. The method according to claim 9 , wherein a pressure ratio across the turbine is about 5 to 12.
12. The method according to claim 9 , wherein the heat from the turbine exhaust stream is withdrawn in a recuperative heat exchanger.
13. The method according to claim 9 , wherein the secondary recycle CO 2 stream when being combined with the main recycle CO 2 stream is at a temperature of 100° C. to 400° C.
14. The method according to claim 9 , wherein compressing the second turbine exhaust portion comprises multi-stage compression with no intercooling between compressor stages.