Efficient conversion of heat to useful energy

• US 7,516,619 B2
• Filed: 07/14/2005
• Issued: 04/14/2009
• Est. Priority Date: 07/19/2004
• Status: Active Grant

• Current Assignee: Recurrent Engineering, LLC (Kalina Power Limited)
• Original Assignee: Recurrent Engineering, LLC (Kalina Power Limited)
• Inventors: Pelletier, Richard I.
• Primary Examiner(s): Nguyen; Hoang M
• Application Number:
  US11/182,603
• Publication Number:
  US 20060010870A1
• Time in Patent Office: 1,370 Days
• Field of Search: 606/49, 606/51, 606/71
• US Class Current: 60/649
• CPC Class Codes: F01K 25/065 with an absorption fluid remaining at least partly in the liquid state, e.g. water for ammonia F01K5/00 takes precedence

Abstract

A heat transfer system includes a power sub-system configured to receive a heat source stream, and one or more heat exchangers configured to transfer heat from the heat source stream to a working stream. The working stream is ultimately heated to a point where it can be passed through one or more turbines, to generate power, while the heat source stream is cooled to a low temperature tail. A distillation condensation sub-system cools the spent stream to generate an intermediate stream and a working stream. The working stream can be variably heated by the intermediate stream so that it is at a sufficient temperature to make efficient use of the low temperature tail. The working stream is then heated by the low temperature tail, and subsequently passed on for use in the power sub-system.

Claims

1. A heat transfer system for converting heat into energy, comprising:

a power sub-system communicatively coupled to a heat source stream, said power sub-system comprising;

a first heat exchanger adapted to heat a multi-component working stream with heat from said heat source stream thereby producing a heated working stream;

a turbine adapted to expand said heated working stream thereby producing a spent stream;

a stream splitter adapted to split a partially heated working stream into a first substream and a second substream prior to being heated in said first heat exchanger, and

a second heat exchanger adapted to heat said first substream with heat from said spent stream thereby producing a cooled spent stream having a first set of thermodynamic characteristics;

a distillation condensation sub-system adapted to receive said cooled spent stream having substantially the same thermodynamic characteristics as said first set of thermodynamic characteristics, thereby producing a condensed working stream; and

a residual heat exchanger adapted to heat said condensed working stream with heat from a low temperature tail of said heat source stream thereby producing said partially heated working stream.

2. The heat transfer system as recited in claim 1, wherein said working stream comprises a mixture of components that each have a different boiling point.

3. The heat transfer system as recited in claim 1, wherein said heat source stream is a fluid material comprising brine arising from a geothermal vent.

4. The heat transfer system as recited in claim 1, wherein said distillation condensation sub-system further comprises a separator configured to substantially separate a vapor component of an intermediate stream from a liquid component.

5. The heat transfer system as recited in claim 4, wherein said distillation condensation sub-system is configured to optionally recombine said vapor component with the said liquid component in order to obtain an appropriate temperature for said intermediate stream.

6. The heat transfer system as recited in claim 5, wherein said distillation condensation sub-system further comprises a heat exchanger that transfers heat from said intermediate stream to said working stream after said intermediate stream has passed said separator, such that said intermediate stream heats said working stream to a temperature that is appropriate for use with said low temperature tail.

7. The heat transfer system as recited in claim 1, wherein said power sub-system comprises a second turbine configured to generate electricity from said working stream.

11. The heat transfer system as recited in claim 1, further comprising a second heat exchanger communicatively coupled to heat the second substream with heat from the heat source stream.

12. The heat transfer system as recited in claim 1, wherein the second substream is heated by heat from the heat source stream.

8. A method for implementing a thermodynamic cycle comprising:

expanding a multi-component gaseous working stream transforming its energy into a usable form and producing a spent stream;

cooling the spent stream producing a cooled spent stream having a first set of thermodynamic characteristics;

condensing the cooled spent stream having substantially the same thermodynamic characteristics as said first set of thermodynamic characteristics in a distillation condensation sub-system and producing a condensed stream;

pressurizing the condensed stream and producing a multi-component stream;

heating the multi-component stream with fluid from the distillation condensation subsystem;

subsequent to heating the multi-component stream with fluid from the distillation condensation subsystem, heating the working stream with the low temperature tail of a heat source stream at a residual heat exchanger;

splitting the multi-component stream heated at the residual heat exchanger to form a first substream and a second substream;

heating the first substream with heat from the spent stream at a first heat exchanger, thereby forming said cooled spent stream;

recombining the first substream and the second substream to form a recombined multi-component stream; and

heating the recombined multi-component stream with heat from the heat source stream at a second heat exchanger to form the multi-component gaseous working stream.

9. The method as recited in claim 8, further comprising heating the second substream with heat from the heat source stream.

10. The method as recited in claim 9, wherein the second substream is heated in a third heat exchanger.

13. A method for implementing a thermodynamic cycle comprising:

expanding a multi-component gaseous working stream transforming its energy into a usable form and producing a spent stream;

cooling the spent stream and producing a cooled spent stream having a first set of thermodynamic characteristics;

condensing the cooled spent stream having substantially the same thermodynamic characteristics as said first set of thermodynamic characteristics in a distillation condensation sub-system and producing a condensed stream;

pressurizing the condensed stream and producing a multi-component stream;

heating the multi-component stream with the low temperature tail of a heat source stream at a residual heat exchanger;

splitting the multi-component stream heated at the residual heat exchanger to form a first substream and a second substream;

heating the first substream with heat from the spent stream at a first heat exchanger, thereby producing the cooled spent stream; and

heating the second substream with heat from the heat source stream at a second heat exchanger.

14. The method of claim 13, wherein the working stream has a temperature at or near its boiling point after being heated with the low temperature tail of the heat source stream.

15. The method of claim 13, wherein the distillation condensation sub-system comprises:

distillation and condensation of the spent stream, the spent steam comprising a multi-component working fluid having a lower boiling point component and a higher boiling point component,

mixing a lean stream having a reduced amount of lower boiling point component compared to higher boiling point component with a rich stream having a greater amount of lower boiling point component when compared to higher boiling point component, and

mixing of a very lean stream with the spent working stream.

16. The method of claim 15, wherein the spent working stream passes in heat exchange relationship with an intermediate lean stream in the distillation condensation sub-stream prior to mixing with a very lean stream.

17. The method of claim 16, wherein the spent working stream is mixed with the very lean stream thereby forming an intermediate lean stream which passes through a low pressure condenser of the distillation condensation sub-system.