IP Library › Granted Patent US 11,174,759
Granted Patent B2
US 11,174,759 · App. 16/547,210 · Granted Nov 16, 2021

Systems and methods for power production using nested CO

Inventors: Rodney John Allam (Wiltshire, GB); Brock Alan Forrest (Durham, NC)
Assignee: 8 Rivers Capital, LLC
F01K23/04F01K7/16F01K23/10F01K25/08F01K25/103F02C1/007F02C1/06F02C1/08F02C3/34F02C6/18F25J3/04018F25J3/04024F25J3/04133F25J3/04145F25J3/04533F25J3/04618F05D2260/61F25J2230/06F25J2240/70F25J2260/80Y02E20/16Y02E20/34
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Quick Facts
Patent No.
US 11,174,759
App. No.
16/547,210
Granted
Nov 16, 2021
Kind
B2
Abstract

The present disclosure relates to systems and methods useful for power production. In particular, a power production cycle utilizing CO 2 as a working fluid may be combined with a second cycle wherein a compressed CO 2 stream from the power production cycle can be heated and expanded to produce additional power and to provide additional heating to the power production cycle.

Claims (16)

1. A method of power production comprising:

carrying out a first cycle that includes:

expanding a work stream comprising recycled CO 2 across a first turbine to produce a first quantity of power;

withdrawing heat from the work stream in a recuperative heat exchanger;

compressing the work stream;

reheating the work stream using withdrawn heat in the recuperative heat exchanger; and

superheating the compressed work stream in a combustor; and

carrying out a nested cycle wherein compressed work stream from the first cycle is heated with a heat source that is independent of the combustor and the recuperative heat exchanger and is expanded across a second turbine to produce a second quantity of power.

2. The method of power production of claim 1 , wherein the expanded work stream from the nested cycle is used to add heat to the work stream in the first cycle after the compressing and before the superheating.

3. The power production method of claim 1 , wherein the heat source in the nested cycle is one or more of a combustion heat source, a solar heat source, a nuclear heat source, a geothermal heat source, and an industrial waste heat source.

4. A method for improving the efficiency of a power production cycle, the method comprising:

operating the power production cycle so that compressed, recycled CO 2 is passed through a combustor wherein a carbonaceous fuel is combusted with an oxidant to produce an exhaust stream comprising the compressed, recycled CO 2 ; the exhaust stream is expanded across a turbine to produce power and form a turbine exhaust stream comprising the recycled CO 2 ; the turbine exhaust stream is cooled in a recuperative heat exchanger; the cooled turbine exhaust stream is passed through a separator to separate the recycled CO 2 ; the recycled CO 2 is compressed; and the compressed recycled CO 2 is split into a first portion and a second portion with the first portion being heated by passage through the recuperative heat exchanger against the turbine exhaust stream; and

adding further heating to the compressed recycled CO 2 above the level of heating that is available from the turbine exhaust stream, the further heating being provided by heating the second portion of the compressed recycled CO 2 with a heat source that is independent of the power production cycle and expanding across a second turbine to produce a second quantity of power, and transferring heat from the heated, second portion of the compressed recycled CO 2 to the first portion of the compressed recycled CO 2 in the power production cycle.

5. The method of claim 4 , comprising passing the heated, second portion of the compressed recycled CO 2 through the recuperative heat exchanger so as to transfer heat to the first portion of the compressed recycled CO 2 therein.

6. The method of claim 4 , comprising passing the heated, second portion of the compressed recycled CO 2 through a secondary heat exchanger to add the further heating thereto.

7. The method of claim 6 , wherein after passage through the secondary heat exchanger, the heated, second portion of the compressed recycled CO 2 is combined with the first portion of the compressed recycled CO 2 in the recuperative heat exchanger.

Continuity (3)
Division 15252798 · Aug 31, 2016
Provisional Application 62212749 · Sep 1, 2015
Related Publication 20190376419A1 · Dec 12, 2019
Cited By (9)
US 12,240,758 US 12,251,658 US 12,270,320 US 12,358,792 US 12,358,793 US 12,358,794 US 12,359,613 US 12,459,813 US 12,723,540