Method of optimizing performance of Rankine cycle power plants

• US 4,358,930 A
• Filed: 06/23/1980
• Issued: 11/16/1982
• Est. Priority Date: 06/23/1980
• Status: Expired due to Term

• Current Assignee: The United States of America As Represented By The Secretary of Agriculture
• Original Assignee: United States Department of Energy
• Inventors: Pope, William L., Pines, Howard S., Silvester, Lenard F., Doyle, Padraic A.
• Primary Examiner(s): Ostrager, Allen M.
• Assistant Examiner(s): Husar, Stephen F.
• Application Number:
  US06/162,345
• Time in Patent Office: 876 Days
• Field of Search: 60/647, 60/651, 60/655, 60/671, 60/641.2
• US Class Current: 60/647
• CPC Class Codes: F01K 25/06 using mixtures of different fluids plants using mixtures of steam and gas F01K21/04
• CPC Class Codes: F01K 25/08 using special vapours
• CPC Class Codes: F03G 7/04 using pressure differences or thermal differences occurring in nature F03G7/06 takes precedence
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

A method for efficiently operating a Rankine cycle power plant (10) to maximize fuel utilization efficiency or energy conversion efficiency or minimize costs by selecting a turbine (22) fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line (46).

Claims

1. A method for operating a turbine to maximize energy conversion and/or fuel utilization efficiency including the step of:

expanding working fluid in a turbine with a turbine fluid inlet state which is substantially in the supercritical vapor region and substantially where the specific heat of the working fluid is a maximum.

2. A method for operating a turbine to maximize energy conversion and/or fuel utilization efficiency including the step of:

expanding working fluid in a turbine with a turbine fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line of the fluid.

3. A method for operating a binary Rankine cycle power plant to maximize energy conversion and/or fuel utilization efficiency including the steps of:

vaporizing a working fluid in a supercritical heat exchanger; and

expanding the working fluid in a turbine with a turbine fluid inlet state which is substantially in the supercritical vapor region and substantially where the specific heat of the working fluid is a maximum.

4. A method for operating a power plant to maximize energy conversion and/or fuel utilization efficiency including the steps of:

vaporizing a working fluid in a heat exchanger to supercritical exit conditions; and

expanding the working fluid in a turbine with a turbine fluid inlet state which is substantially in the supercritical vapor region and substantially where the specific heat of the working fluid is a maximum.

5. A method for operating a power plant to maximize energy conversion and/or fuel utilization efficiency, including the steps of:

vaporizing a fluid in a heat exchanger; and

expanding the fluid in a turbine with a turbine fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line of the fluid.

6. The method of claim 5 wherein the step of expanding the fluid in a turbine with a turbine fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line of the fluid includes the step of expanding the fluid in a turbine with the turbine fluid inlet state such that the turbine inlet state on a pressure-enthalpy graph has substantially the following boundaries;

(1) the constant critical temperature line;

(2) the critical pressure line;

(3) the line of constant specific volume extending from the intersection of the critical pressure line and the maximum constant specific enthalpy line tangent to the vapor saturation boundary;

(4) the constant temperature line which is 20% above the critical temperature line; and

(5) the line of constant specific volume which is 20% below the critical specific volume.

7. A method for operating a Rankine cycle power plant to maximize thermodynamic and economic performance including the steps of:

vaporizing a fluid in a supercritical primary heater;

expanding the fluid in a turbine with a turbine fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line of the fluid; and

condensing the fluid exhausted from the turbine;

returning the condensed fluid to the heater.

8. The method of claim 7 wherein the step of expanding the fluid in a turbine with a turbine fluid inlet state which is substantially in the area adjacent and including the transposed critical temperature line of the fluid includes the step of expanding the fluid in a turbine with the turbine fluid inlet state such that the turbine inlet state on a pressure-enthalpy graph has substantially the following boundaries:

(1) the constant critical temperature line;

(2) the critical pressure line;

(3) the line of constant specific volume extending from the intersection of the critical pressure line and the maximum constant specific enthalpy line tangent to the vapor saturation boundary;

(4) the constant temperature line which is 20% above the critical temperature line; and

(5) the line of constant specific volume which is 20% below the critical specific volume.

9. The method of claim 7, wherein the fluid has a vapor saturation boundary as defined on a pressure-enthalpy diagram, including the step of selecting the fluid to have a vapor saturation boundary which is at least in part parallel to the condition, as represented on the pressure-enthalpy diagram, of fluid expanding in the turbine.

10. The method of claim 7 including the step of selecting the fluid so that there is substantially dry expansion of fluid in the turbine.

11. The method of claim 7 including the step of selecting the working fluid so that particular chemical reactions can be avoided that would accelerate fouling in the primary heater.

12. The method of claim 7, wherein the Rankine cycle power plant uses geothermal brine and has a brine disposal system, including the steps of heating the working fluid with geothermal brine and selecting the working fluid so that particular chemical reactions can be avoided that could cause clogging in the brine disposal system.

13. The method of claim 7 including the step of:

using a working fluid composed of a mixture of isobutane and isopentane.

14. The method of claim 7 including the step of:

using a working fluid selected from the group consisting of methane, ethane, propane, n-butane, isobutane, n-pentane, isopentane, and neopentane and mixtures thereof.

15. The method of claim 7 including the step of:

using a working fluid composed of a mixture of Pyridine and water.

16. The method of claim 7 including the step of:

using a working fluid composed of an azeotrope.

17. The method of claim 7 including the step of:

vaporizing the fluid in the heater with heat rejected from a higher temperature process.

18. The method of claim 7 including the step of:

using the vaporizing, selecting, expanding, condensing and returning steps as a bottoming cycle for efficiently using waste heat rejected from a higher temperature process.

19. The method of claim 7 including the step of:

using the vaporizing, selecting, expanding, condensing and returning steps as a topping cycle rejecting heat to a lower temperature cycle to increase overall power output and process efficiency.

20. The method of claim 7 wherein the vaporized fluid is a working fluid and including the steps of:

vaporizing the working fluid in the heater with a source fluid; and

changing the composition of the working fluid responsive to a declining temperature of the source fluid.

21. The method of claim 20 including the step of:

using a working fluid composed of a mixture of isobutane and isopentane.

22. The method of claim 20 including the step of:

using a working fluid selected from the group consisting of methane, ethane, propane, n-butane, isobutane, n-pentane, isopentane, and neopentane and mixtures thereof.

23. The method of claim 20 including the step of using a working fluid composed of a mixture of Pyridine and water.

24. The method of claim 7 including the step of:

changing the composition of the fluid to maintain a desired turbine inlet state as the primary heater degrades due to fouling.

25. The method of claim 7 wherein the Rankine cycle power plant uses geothermal brine and has geothermal brine injection wells including the step of:

changing the composition of the fluid to maintain a desired turbine inlet state as clogging increases in the injection wells.

26. The method of claim 7 wherein the Rankine cycle power plant uses geothermal brine and has geothermal brine injection wells including the step of changing the turbine inlet operating conditions to another point in the area adjacent and including the transposed critical temperature line as brine injection characteristics change.

27. The method of claim 7 including the step of:

co-generating electric power and mechanical work or process heat from the step of expanding fluid in the turbine.

28. The method of claim 7, wherein the environment is used as a heat sink, including the step of:

selecting turbine characteristics to minimize efficiency degradation in response to heat sink variations.

29. The method of claim 7 including the step of:

selecting turbine characteristics to minimize efficiency degradation as the power output requirements of the power plant are reduced.

30. The method of claim 7, wherein the Rankine cycle power plant uses geothermal brine from a geothermal brine source including the step of:

selecting turbine characteristics to minimize efficiency degradation in response to a temperature decline in the geothermal brine source.

31. The method of claim 7 including the step of:

using a working fluid comprising an olefin.

32. The method of claim 7 including the step of:

using a working fluid comprising a saturated light hydrocarbon.

33. The method of claim 7 including the step of:

using a working fluid comprising hydrocarbons and mixtures thereof.