Control schemes for thermal management of power production systems and methods

Patent metadata

Field	Value
Publication number	US-12480443-B2
Application number	US-202418796846-A
Country	US
Kind code	B2
Filing date	Aug 7, 2024
Priority date	Oct 22, 2019
Publication date	Nov 25, 2025
Grant date	Nov 25, 2025

Abstract

The present invention relates to systems and methods for controlling a power production plant and optionally providing a one or more product streams for an end use thereof. Control of a power production plant specifically can include executing one or more functions effective for adjusting a heat profile of a heat exchange unit (HEU) operating with a plurality of streams passing therethrough. This can include implementing a control function that alters a flow of one or more of the plurality of streams by adding flow to or withdrawing flow one or more of the plurality of streams at an intermediate temperature range within the HEU at a point that is positioned between a first end and a second end of the HEU.

First claim

The invention claimed is:

1 . A power production method comprising:
expanding a heated, pressurized stream in a turbine to generate power and form a turbine exhaust stream; passing the turbine exhaust stream through a heat exchange unit (HEU) from a first end of the HEU with a higher operational temperature toward a second end of the HEU with a lower operational temperature; processing the turbine exhaust stream downstream from the HEU to form a recycle stream; passing at least a portion of the recycle stream through the HEU toward the first end of the HEU; and implementing a control function whereby a bypass portion of the turbine exhaust stream passing through the HEU leaves the HEU at a position between the first end of the HEU and the second end of the HEU and rejoins the turbine exhaust stream downstream of the second end of the HEU so that mass flow of the turbine exhaust stream is reduced through a portion of the HEU without reducing total mass flow of the turbine exhaust stream that is processed to form the recycle stream.

2 . The power production method of claim 1 , wherein processing the turbine exhaust stream downstream from the HEU comprises processing through or more of a separator, a compressor, and a pump.

3 . The power production method of claim 1 , wherein the control function is responsive to one or both of the following signals received by a controller:
a signal indicating a change in power demand effective to cause an operational change of the turbine altering power generation; a signal indicating that a temperature within the HEU is within a defined threshold of a maximum operating temperature of the HEU.

4 . The power production method of claim 1 , further comprising causing the bypass portion of the turbine exhaust stream to be processed through a bypass heat exchanger effective to transfer heat from the bypass portion of the turbine exhaust stream to one or more further streams.

5 . The power production method of claim 1 , wherein the control function includes causing a valve to open or close to modify a mass flow of the bypass portion of the turbine exhaust stream that leaves the HEU at a position between the first end of the HEU and the second end of the HEU.

6 . The power production of claim 5 , wherein the valve is positioned in a bypass line in fluid connection with the HEU.

7 . A power production method comprising:
expanding a heated, pressurized stream in a turbine to generate power and form a turbine exhaust stream; passing the turbine exhaust stream through a heat exchange unit (HEU) from a first end of the HEU with a higher operational temperature toward a second end of the HEU with a lower operational temperature; and implementing a control function whereby a portion of the turbine exhaust stream passing through the HEU leaves the HEU at a position between the first end of the HEU and the second end of the HEU, is compressed in a recirculation compressor, and is introduced back in the HEU at a section of the HEU that is downstream from where the portion of the turbine exhaust stream leaves the HEU.

8 . The power production method of claim 7 , further comprising implementing a control function effective to reduce a flow rate through the recirculation compressor while maintaining a substantially constant outlet temperature from the recirculation compressor.

9 . The power production method of claim 7 , further comprising implementing a control function effective to close an inlet guide vane (IGV) of the recirculation compressor in response to a signal indicating that a temperature within the HEU is within a threshold value of a maximum operating temperature of the HEU.

10 . The power production method of claim 7 , further comprising one or both of the following:
passing a recycle stream through the HEU toward the first end of the HEU so that the recycle stream is heated in the HEU; passing an oxidant stream through the HEU toward the first end of the HEU so that the oxidant stream is heated in the HEU.

11 . A power production method comprising:
expanding a heated, pressurized stream in a turbine to generate power and form a turbine exhaust stream; passing the turbine exhaust stream through a heat exchange unit (HEU) from a first end of the HEU with a higher operational temperature toward a second end of the HEU with a lower operational temperature; processing the turbine exhaust stream downstream from the HEU to form a recycle stream; passing one or both of the recycle stream and an oxidant stream through the HEU toward the first end of the HEU; and implementing a control function effective to increase mass flow of the turbine exhaust stream through a portion of the HEU by addition of fluid to the turbine exhaust stream at one or more positions between the first end of the HEU and the second end of the HEU.

12 . The power production method of claim 11 , wherein the control function is effective to cause a portion of the recycle stream to be passed to the turbine exhaust stream.

13 . The power production method of claim 11 , wherein the control function is effective to cause a portion of the oxidant stream to be passed to the turbine exhaust stream.

14 . The power production method of claim 11 , wherein one or both of the following conditions is met:
implementing the control function is responsive to a signal indicating a change in power demand effective to cause an operational change of the turbine that alters power generation thereby; implementing the control function is responsive to a signal indicating that a temperature within the HEU is within a defined threshold of a maximum operating temperature of the HEU.

15 . The power production method of claim 11 , wherein the control function includes causing one or more valves to open or close to modify a mass flow of a stream passing to the turbine exhaust stream in the HEU.

16 . A power production method comprising:
expanding a heated, pressurized stream in a turbine to generate power and form a turbine exhaust stream; passing the turbine exhaust stream through a heat exchange unit (HEU) from a first end of the HEU with a higher operational temperature toward a second end of the HEU with a lower operational temperature; processing the turbine exhaust stream downstream from the HEU to form a recycle stream; passing one or both of the recycle stream and an oxidant stream through the HEU toward the first end of the HEU; implementing a control function that alters a mass flow of one or more of the turbine exhaust stream, the recycle stream, and the oxidant stream passing through a portion of the HEU by adding mass flow to or withdrawing mass flow from the one or more of the turbine exhaust stream, the recycle stream, and the oxidant stream at one or more positions between the first end of the HEU and the second end of the HEU; and adding heat to the HEU using a heater that is arranged to provide heat at a location in the HEU between the first end of the HEU and the second end of the HEU.

17 . The power production method of claim 16 , wherein the heater is an electric heater.

18 . The power production method of claim 16 , wherein the heater is a solar heater or a nuclear heater.

19 . The power production method of claim 16 , wherein the heater is an oxy-fired burner arranged on a line passing the turbine exhaust stream through the HEU.

20 . The power production method of claim 19 , wherein the oxy-fired burner is arranged so that emissions from the oxy-fired burner mix with t

Assignees

• 8 Rivers Capital Llc

Inventors

• Forrest Brock Alan
• Lu Xijia
• Fetvedt Jeremy Eron
• Rafati Navid

Classifications

• F05D2210/12

  gaseous, i.e. compressible · CPC title

• F02C6/18

  using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants (using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10) · CPC title

• B01D53/9445

  Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] · CPC title

• B01D53/58

  Ammonia · CPC title

• Y02E20/14

  Combined heat and power generation [CHP] · CPC title