Parallel cycle heat engines

• US 9,284,855 B2
• Filed: 08/18/2011
• Issued: 03/15/2016
• Est. Priority Date: 11/29/2010
• Status: Active Grant

• Current Assignee: Echogen Power Systems, LLC
• Original Assignee: Echogen Power Systems, LLC
• Inventors: Held, Timothy James, Xie, Tao, Miller, Jason, Vermeersch, Michael Louis
• Primary Examiner(s): Pereiro, Jorge
• Assistant Examiner(s): Wan, Deming
• Application Number:
  US13/212,631
• Publication Number:
  US 20120131920A1
• Time in Patent Office: 1,671 Days
• Field of Search: 606/50, 606/417, 606/73, 606/49
• US Class Current: 1/1
• CPC Class Codes: F01K 13/02 Controlling, e.g. stopping or starting
• CPC Class Codes: F01K 23/04 condensation heat from one cycle heating the fluid in another cycle
• CPC Class Codes: F01K 25/10 the vapours being cold, e.g. ammonia, carbon dioxide, ether
• CPC Class Codes: F01K 25/103 Carbon dioxide F01K25/065 takes precedence
• CPC Class Codes: F22B 35/086 operating at critical or supercritical pressure

Abstract

Waste heat energy conversion cycles, systems and devices use multiple waste heat exchangers arranged in series in a waste heat stream, and multiple thermodynamic cycles run in parallel with the waste heat exchangers in order to maximize thermal energy extraction from the waste heat stream by a working fluid. The parallel cycles operate in different temperature ranges with a lower temperature work output used to drive a working fluid pump. A working fluid mass management system is integrated into or connected to the cycles.

Claims

1. A method for converting thermal energy to work, comprising:

circulating a working fluid comprising carbon dioxide with a pump throughout a working fluid circuit;

separating the working fluid into a first mass flow and a second mass flow within the working fluid circuit;

transferring thermal energy in a first heat exchanger from a heat source to the first mass flow, the first heat exchanger being in thermal communication with the heat source;

expanding the first mass flow in a first turbine fluidly coupled to the first heat exchanger via the working fluid circuit;

transferring residual thermal energy in a first recuperator from the first mass flow discharged from the first turbine to the first mass flow directed to the first heat exchanger, the first recuperator being fluidly coupled to the first turbine via the working fluid circuit;

transferring thermal energy in a second heat exchanger from the heat source to the second mass flow, the second heat exchanger being in thermal communication with the heat source;

transferring thermal energy in a third heat exchanger from the heat source to the first mass flow prior to passing through the first heat exchanger, the third heat exchanger being in thermal communication with the heat source and fluidly arranged between the pump and the first heat exchanger via the working fluid circuit;

expanding the second mass flow in a second turbine fluidly coupled to the second heat exchanger; and

transferring residual thermal energy in a second recuperator from a combined first and second mass flow to the first mass flow directed to the first heat exchanger, the second recuperator being fluidly coupled to the second turbine via the working fluid circuit.

2. The method of claim 1, further comprising transferring residual thermal energy in the second recuperator from the second mass flow discharged from the second turbine to the second mass flow directed to the second heat exchanger.

3. The method of claim 2, further comprising transferring residual heat in a third recuperator from the combined first and second mass flow discharged from the second recuperator to the first mass flow before the first mass flow is introduced into the third heat exchanger, the third recuperator being fluidly arranged between the pump and the third heat exchanger via the working fluid circuit.

4. A system for converting thermal energy to work, comprising:

a working fluid comprising carbon dioxide;

a working fluid circuit containing the working fluid;

one pump fluidly coupled to the working fluid circuit and configured to circulate the working fluid throughout the working fluid circuit, the working fluid circuit separating the working fluid into a first mass flow and a second mass flow downstream of the one pump, and wherein an inlet of the one pump receives both the first mass flow and the second mass flow;

a first heat exchanger in fluid communication with the one pump via the working fluid circuit and configured to be in thermal communication with a heat source, the first heat exchanger receiving the first mass flow and configured to transfer thermal energy from the heat source to the first mass flow;

a first turbine fluidly coupled to the first heat exchanger via the working fluid circuit and configured to expand the first mass flow;

a first recuperator fluidly coupled to the first turbine via the working fluid circuit and configured to transfer residual thermal energy from the first mass flow discharged from the first turbine to the first mass flow directed to the first heat exchanger;

a second heat exchanger in fluid communication with the one pump via the working fluid circuit and configured to be in thermal communication with the heat source, the second heat exchanger receiving the second mass flow and configured to transfer thermal energy from the heat source to the second mass flow;

a second turbine fluidly coupled to the second heat exchanger via the working fluid circuit and configured to expand the second mass flow; and

a second recuperator fluidly coupled to the second turbine via the working fluid circuit and configured to transfer residual thermal enemy from a combined first and second mass flow to the first mass flow directed to the first heat exchanger.

5. The system of claim 4, wherein the heat source is a waste heat stream.

6. The system of claim 4, wherein the working fluid is at a supercritical state at the inlet to the one pump.

7. The system of claim 4, wherein the first heat exchanger and the second heat exchanger are fluidly arranged in series with the heat source.

8. The system of claim 4, wherein the first mass flow circulates in parallel with the second mass flow.

9. The system of claim 4, wherein the second recuperator is configured to transfer residual thermal energy from the second mass flow discharged from the second turbine to the second mass flow directed to the second heat exchanger.

10. The system of claim 9, wherein the first recuperator and the second recuperator are fluidly arranged in parallel on a low temperature side of the working fluid circuit, and the first recuperator and the second recuperator are fluidly arranged in parallel on a high temperature side of the working fluid circuit.

11. The system of claim 4, wherein an inlet pressure at the first turbine is substantially equal to an inlet pressure at the second turbine.

12. The system of claim 11, wherein a discharge pressure at the first turbine is different than a discharge pressure at the second turbine.

13. The system of claim 4, further comprising a mass management system being operatively connected to the working fluid circuit via at least one tie-in point and including a working fluid storage tank, wherein the mass management system is configured to transfer working fluid between the working fluid circuit and the working fluid storage tank.

14. A system for converting thermal energy to work, comprising:

a working fluid comprising carbon dioxide;

a working fluid circuit containing the working fluid;

a pump fluidly coupled to the working fluid circuit and configured to circulate the working fluid throughout the working fluid circuit, the working fluid circuit separating the working fluid into a first mass flow and a second mass flow downstream of the pump;

a first heat exchanger in fluid communication with the pump via the working fluid circuit and configured to be in thermal communication with a heat source, the first heat exchanger receiving the first mass flow and configured to transfer thermal energy from the heat source to the first mass flow;

a first turbine fluidly coupled to the first heat exchanger via the working fluid circuit and configured to expand the first mass flow;

a first recuperator fluidly coupled to the first turbine via the working fluid circuit and configured to transfer residual thermal energy from the first mass flow discharged from the first turbine to the first mass flow directed to the first heat exchanger;

a second heat exchanger in fluid communication with the pump via the working fluid circuit and configured to be in thermal communication with the heat source, the second heat exchanger being configured to receive the second mass flow and transfer thermal energy from the heat source to the second mass flow;

a second turbine fluidly coupled to the second heat exchanger via the working fluid circuit and configured to expand the second mass flow, the second mass flow being discharged from the second turbine and re-combined with the first mass flow to generate a combined mass flow;

a second recuperator fluidly coupled to the second turbine via the working fluid circuit and configured to transfer residual thermal energy from the combined mass flow to the second mass flow directed to the second heat exchanger; and

a third heat exchanger configured to be in thermal communication with the heat source and fluidly arranged between the pump and the first heat exchanger via the working fluid circuit, the third heat exchanger being configured to receive and transfer thermal energy to the first mass flow upstream of the first heat exchanger, and wherein the first heat exchanger, the second heat exchanger, and the third heat exchanger are fluidly arranged in series in the heat source.

15. The system of claim 14, wherein the heat source is a waste heat stream.

16. The system of claim 14, wherein the working fluid is at a supercritical state at an inlet to the pump.

17. The system of claim 14, wherein the first mass flow circulates in parallel with the second mass flow.

18. The system of claim 14, wherein the first and second recuperators form a single recuperator component.

19. The system of claim 14, wherein the first recuperator and the second recuperator are fluidly arranged in series within a low temperature side of the working fluid circuit, and the first recuperator and the second recuperator are fluidly arranged in parallel within a high temperature side of the working fluid circuit.

20. The system of claim 14, further comprising a third recuperator fluidly arranged between the pump and the third heat exchanger via the working fluid circuit.

21. The system of claim 20, wherein the third recuperator is configured to transfer residual heat from the combined mass flow discharged from the second recuperator to the first mass flow before the first mass flow is introduced into the third heat exchanger.

22. The system of claim 21, wherein the first recuperator, the second recuperator, and the third recuperator are fluidly arranged in series within a low temperature side of the working fluid circuit.

23. The system of claim 20, wherein the first recuperator, the second recuperator, and the third recuperator form a single recuperator component.

24. The system of claim 23, wherein the single recuperator component is configured to receive the first mass flow discharged from the third heat exchanger and configured to transfer additional residual thermal energy from the combined mass flow to the first mass flow prior to the first mass flow passing through the first heat exchanger.

25. The system of claim 14, wherein an inlet pressure at the first turbine is substantially equal to an inlet pressure at the second turbine.

26. The system of claim 25, wherein a discharge pressure at the first turbine is different than a discharge pressure at the second turbine.