High efficiency positive displacement thermodynamic system

• US 8,424,284 B2
• Filed: 10/30/2009
• Issued: 04/23/2013
• Est. Priority Date: 05/20/2004
• Status: Active Grant

• Current Assignee: Gilbert Staffend
• Original Assignee: Gilbert Staffend
• Inventors: Staffend, Gilbert, Staffend, Nancy A.
• Primary Examiner(s): NGUYEN, HOANG M
• Application Number:
  US12/609,876
• Publication Number:
  US 20100050628A1
• Time in Patent Office: 1,271 Days
• Field of Search: 60/396, 605/19, 606/50, 60682-683, 123/204, 123/221, 123/223, 123/224, 123/235, 123/236, 418/235, 418/241, 418/260
• US Class Current: 60/39.6
• CPC Class Codes: F01C 1/3441 the inner and outer member being in contact along one line or continuous surface substantially parallel to the axis of rotation
• CPC Class Codes: F01C 1/356 with vanes reciprocating with respect to the outer member
• CPC Class Codes: F01C 11/002 of similar working principle
• CPC Class Codes: F01C 20/24 characterised by using valves for controlling pressure or flow rate, e.g. discharge valves F01C20/10 takes precedence
• CPC Class Codes: F01K 27/00 Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
• CPC Class Codes: F01K 7/00 Steam engine plants characterised by the use of specific types of engine F01K3/02 takes precedence; Plants or engines characterised by their use of special steam systems, cycles or processes reciprocating-piston engines using uniflow principle F01B17/04; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
• CPC Class Codes: F02G 1/043 the engine being operated by expansion and contraction of a mass of working gas which is heated and cooled in one of a plurality of constantly communicating expansible chambers, e.g. Stirling cycle type engines
• CPC Class Codes: F02G 2270/10 Rotary pistons

Abstract

Devices and methods for moving a working fluid through a controlled thermodynamic cycle in a positive displacement fluid-handling device (20, 20′, 20″) with minimal energy input include continuously varying the relative compression and expansion ratios of the working fluid in respective compressor and expander sections without diminishing volumetric efficiency. In one embodiment, a rotating valve plate arrangement (40, 42, 44, 46) is provided with moveable apertures or windows (48, 50, 56, 58) for conducting the passage of the working fluid in a manner which enables on-the-fly management of the thermodynamic efficiency of the device (20) under varying conditions in order to maximize the amount of mechanical work needed to move the target quantity of heat absorbed and released by the working fluid. When operated in refrigeration modes, the work required to move the heat is minimized. In power modes, the work extracted for the given input heat is maximized.

Claims

1. A method for moving a working fluid through a controlled thermodynamic cycle in a positive displacement fluid-handling device, said method comprising the steps of:

providing a working fluid at an inlet pressure, the working fluid comprising a compressible substance capable of intermittently storing and releasing mechanical energy;

providing at least one compression chamber and at least one expansion chamber, each having a respective displacement volume and definable volumetric efficiency;

volumetrically compressing a fixed quantity of the working fluid in the compression chamber, and volumetrically expanding a fixed quantity of the working fluid in the expansion chamber;

creating a pressure differential in the working fluid relative to the inlet pressure during one of said compressing and expanding steps, then moving a variable amount of heat into or out of the working fluid, and then subsequently returning the working fluid to the inlet pressure during the other one of said compressing and expanding steps entirely within the respective compression or expansion chamber; and

said step of returning the working fluid to the inlet pressure including adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved during said moving step without decreasing the volumetric efficiency of the compression and expansion chambers.

2. The method of claim 1 wherein said step of providing at least one compression chamber and at least one expansion chamber includes calculating the volumetric efficiency for each of the compression and expansion chambers by mathematically dividing the mass of working fluid in each chamber during the respective one of said compressing and expanding steps by the product of the density of the working fluid and the displacement volume of the respective compression and expansion chamber.

3. The method of claim 1 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes controlling at least one of the following:

target temperatures, approach temperatures, relative pressure lift, corresponding pressures, and operating costs.

4. The method of claim 1 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes maintaining asymmetric compression and expansion volumes.

5. The method of claim 1 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes monitoring the pressure of the working fluid.

6. The method of claim 1 wherein said step of moving a variable amount of heat includes providing a high-side heat exchanger operatively disposed between an outlet from the compression chamber and an inlet to the expansion chamber;

providing a low-side heat exchanger operatively disposed between an outlet from the expansion chamber and an inlet to the compression chamber;

rejecting heat energy from the working fluid in the high-side heat exchanger; and

absorbing heat energy in the working fluid in the low-side heat exchanger.

7. The method of claim 6 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes dynamically changing the location of at least one of the compressor inlet and expander outlet to alter the thermodynamic efficiency.

8. The method of claim 7 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes shifting a pair of valve plates having overlapping apertures so that the degree of overlap changes.

9. The method of claim 7 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes providing at least one rotatable outlet valve plate having an aperture formed therein adjacent the expansion chamber outlet and at least one rotatable inlet valve plate having an aperture formed therein adjacent the compression chamber inlet, and further including the step of maintaining the apertures in the respective outlet and inlet valve plates in direct longitudinally opposed relation to one another.

10. The method of claim 6 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes manipulating at least one flow control valve operatively associated with the high-side heat exchanger.

11. The method of claim 6 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes operatively locating a check valve between the outlet from the compression chamber and the high-side heat exchanger, and operatively locating a flow control valve between the high-side heat exchanger and the inlet to the expansion chamber.

12. The method of claim 6 wherein one of said steps of rejecting heat energy and absorbing heat energy includes discharging the working fluid to ambient atmosphere.

13. The method of claim 6 wherein said step of rejecting heat energy includes discharging the working fluid to ambient atmosphere and said step of absorbing heat energy includes combusting the working fluid.

14. The method of claim 1 wherein said step of creating a pressure differential in the working fluid includes radially displacing at least one vane relative to a rotating hub.

15. The method of claim 14 further wherein said step of creating a pressure differential in the working fluid includes co-rotating a compression element and an expansion element within a common housing.

16. The method of claim 14 wherein said step of creating a pressure differential in the working fluid includes co-rotating a compression element and an expansion element within respective housings.

17. The method of claim 14 wherein said steps of volumetrically compressing and volumetrically expanding includes sweeping at least one lobe in a continuous rotational direction.

18. The method of claim 1 wherein said steps of volumetrically compressing and volumetrically expanding include sweeping at least one lobe in a continuous rotational direction while moving the working fluid through modes of intake, expansion, compression and exhaust.

19. A method for moving a working fluid through a controlled thermodynamic cycle in a positive displacement fluid-handling device in such a manner that, in the case of a refrigerator heat is moved with the minimum theoretical application of work and, in the case of a heat engine the maximum theoretical amount of work is extracted from a given movement of heat, said method comprising the steps of:

providing a working fluid at an inlet pressure, the working fluid comprising a compressible substance capable of intermittently storing and releasing mechanical energy;

providing at least one compression chamber and at least one expansion chamber, each having a respective displacement volume and definable volumetric efficiency;

volumetrically compressing a fixed quantity of the working fluid in the compression chamber, and volumetrically expanding a fixed quantity of the working fluid in the expansion chamber;

creating a pressure differential in the working fluid relative to the inlet pressure during one of said compressing and expanding steps, then moving a variable amount of heat into or out of the working fluid, and then subsequently returning the working fluid to the inlet pressure during the other one of said compressing and expanding steps entirely within the respective compression or expansion chamber;

said step of moving a variable amount of heat including providing a high-side heat exchanger operatively disposed between an outlet from the compression chamber and an inlet to the expansion chamber;

providing a low-side heat exchanger operatively disposed between an outlet from the expansion chamber and an inlet to the compression chamber;

rejecting heat energy from the working fluid in the high-side heat exchanger; and

absorbing heat energy in the working fluid in the low-side heat exchanger;

said step of returning the working fluid to the inlet pressure including adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved during said moving step without decreasing the volumetric efficiency of the compression and expansion chambers; and

said step of creating a pressure differential in the working fluid including radially displacing at least one vane relative to a rotating hub.

20. The method of claim 19 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes shifting a pair of valve plates having overlapping apertures so that the degree of overlap changes.

21. The method of claim 19 wherein said step of adjusting the displacement volume of the expansion chamber relative to the compression chamber based on the amount of heat moved includes providing at least one rotatable outlet valve plate having an aperture formed therein adjacent the expansion chamber outlet, and at least one rotatable inlet valve plate having an aperture formed therein adjacent the compression chamber inlet;

and further including the step of maintaining the apertures in the respective outlet and inlet valve plates in direct longitudinally opposed relation to one another.

22. The method of claim 19 wherein said steps of volumetrically compressing and volumetrically expanding include sweeping at least one lobe in a continuous rotational direction while moving the working fluid through modes of intake, expansion, compression and exhaust.

23. A positive displacement rotating vane-type device of the type operated in a thermodynamic cycle, said device comprising:

a generally cylindrical stator housing having a central axis and longitudinally spaced, opposite ends;

a rotor rotatably disposed within said stator housing and establishing an interstitial space therebetween;

a plurality of vanes operatively disposed between rotor and said stator housing for dividing said interstitial space into intermittent compression and expansion chambers;

a compression chamber outlet and an expansion chamber inlet respectively communicating with said interstitial space;

a high-pressure side heat exchanger fluidly adjoining said compressor outlet and said expander inlet;

an expansion chamber outlet and a compression chamber inlet respectively communicating with said interstitial space;

a low-pressure side heat exchanger fluidly adjoining said expansion chamber outlet and said compression chamber inlet; and

at least one rotatable outlet valve plate disposed adjacent said expansion chamber outlet with an aperture formed therein for conducting the passage of a working fluid, and at least one rotatable inlet valve plate disposed adjacent said compression chamber inlet with an aperture formed therein for conducting the passage of a working fluid, whereby said outlet and inlet valve plates can be rotated with respect to said stator housing so as to manage the thermodynamic efficiency of said device under varying conditions.

24. The device of claim 23 wherein said at least one rotating outlet valve plate comprises a pair of outlet valve plates having complementary overlapping apertures therein, and said at least one rotating inlet valve plate comprises a pair of inlet valve plates having complementary overlapping apertures therein.

25. The device of claim 23 wherein said aperture in said outlet valve plate is directly longitudinally opposed to said aperture in said inlet valve plate.

26. The device of claim 23 wherein one of said high-pressure side heat exchanger and said low-pressure side heat exchanger comprises ambient atmosphere.