Balanced adsorbent refrigerator

• US 5,813,248 A
• Filed: 11/01/1996
• Issued: 09/29/1998
• Est. Priority Date: 11/01/1995
• Status: Expired due to Fees

• Current Assignee: David A. Zornes, John J. Bauer
• Original Assignee: David A. Zornes, John J. Bauer
• Inventors: Zornes, David A., Bauer, John J.
• Primary Examiner(s): DOERRLER, WILLIAM CHARLES
• Application Number:
  US08/742,387
• Time in Patent Office: 697 Days
• Field of Search: 62/480, 62/476, 62/101, 62/102, 62/106, 62/112, 62/477, 252/69, 165/81
• US Class Current: 62/480
• CPC Class Codes: C09K 5/047 for absorption-type refrigeration systems
• CPC Class Codes: F25B 17/08 the absorbent or adsorbent being a solid, e.g. salt F25B17/12 takes precedence
• CPC Class Codes: F25B 27/02 using waste heat, e.g. from internal-combustion engines
• CPC Class Codes: F25B 35/04 using a solid as sorbent
• CPC Class Codes: F28D 20/003 using thermochemical reactions
• CPC Class Codes: F28F 19/006 Preventing deposits of ice
• CPC Class Codes: F28F 2265/14 for preventing damage by freezing, e.g. for accommodating volume expansion
• CPC Class Codes: Y02A 30/27 Relating to heating, ventilation or air conditioning [HVAC] technologies
• CPC Class Codes: Y02A 30/274 using waste energy, e.g. from internal combustion engine
• CPC Class Codes: Y02B 30/00 Energy efficient heating, ventilation or air conditioning [HVAC]
• CPC Class Codes: Y02E 60/14 Thermal energy storage
• CPC Class Codes: Y02P 20/10 Process efficiency

Abstract

A heat transfer apparatus that uses an adsorbent material to generate a cooling effect. The heat transfer apparatus includes a first vessel containing adsorbent material and a second vessel interconnected to the first. A working substance is contained within the two interconnected vessels. The adsorbent material and working substance are sized such that the working substance is completely adsorbed in both liquid and solid states by the adsorbent material from the second vessel into the first, cooling the second vessel and heating the first. Complete adsorption includes adsorption of the working substance by vaporization when the working substance is in a liquid phase and adsorption by sublimation when the working substance is in a solid phase. The second vessel contains a compressible foam which accommodates the expansion of the working substance when it changes phase from a liquid to a solid and prevents the second vessel from breaking.

Claims

1. A heat transfer apparatus which uses a heat source to generate a cooling effect, the apparatus comprising:

a first vessel having a first aperture and containing an adsorbent material having an adsorbing capacity;

a second vessel having a second aperture, the second aperture connected to the first aperture of the first vessel with a conduit, the conduit providing a fluid passage between the vessels, the vessels and the conduit forming a sealed volume capable of maintaining less than atmospheric pressure therein; and

a quantity of working substance within the scaled volume, the quantity including a portion of working substance in the second vessel, the working substance being capable of being strongly adsorbed by the absorbent material, the adsorbing capacity of the adsorbent material being sufficient to adsorb by sublimation at least part of the portion of working substance in the second vessel when substantially the entire portion of working substance in the second vessel is in a solid state.

2. The heat transfer apparatus of claim 1, further comprising a valve positioned in the conduit and moveable between an open position with the working substance free to move between the first and second vessels and closed position with the working substance constrained from movement between the vessels.

3. The heat transfer apparatus of claim 2 wherein the valve is in the closed position and substantially all the working substance is retained by the adsorbent material.

4. The heat transfer apparatus of claim 1 wherein the second vessel has a third aperture therein, further comprising a third vessel connected to the third aperture, the third vessel having an adsorbent material and an adsorbent capacity, wherein the third vessel is capable of being heated by a heat source while the first vessel is adsorbing the working substance, and the first vessel is capable of being heated by the heat source while the third vessel is adsorbing the working substance.

5. The heat transfer apparatus of claim 1 wherein the second vessel is a refrigeration element for cooling a volume surrounding the second vessel.

6. The heat transfer apparatus of claim 1 wherein the quantity of working substance is not greater than the adsorbing capacity of the adsorbent material at a selected temperature and pressure of the sealed volume such that the working substance is capable of being substantially completely adsorbed by the adsorbent material.

7. The heat transfer apparatus of claim 1 wherein the sealed unit has an internal absolute pressure of 4 mm of mercury.

8. The heat transfer apparatus of claim 1 wherein the adsorbent material has a weight and the working substance has a weight that is 28.5% of the adsorbent material weight.

9. The heat transfer apparatus of claim 1, further comprising a heat source positioned proximate to the adsorbent material for heating the adsorbent material and evaporating the working substance therefrom, the heat source being controllable between an active state wherein the heat source heats the adsorbent material and an inactive state.

10. The heat transfer apparatus of claim 9 wherein the heat source is positioned external to the first vessel.

11. The heat transfer apparatus of claim 9 wherein the heat source is positioned within the first vessel.

12. The heat transfer apparatus of claim 11 wherein the heat source is thermally coupled to the adsorbent material.

13. The heat transfer apparatus of claim 11 wherein the heat source is bonded to the adsorbent material.

14. The heat transfer apparatus of claim 9 wherein the first vessel is capable of achieving a temperature of approximately 70°

F. when the heat source is in its inactive state.

15. The heat transfer apparatus of claim 9 wherein the heat source is heated by solar energy.

16. The heat transfer apparatus of claim 1 wherein the adsorbent material is a zeolite.

17. The heat transfer apparatus of claim 1 wherein the working substance is water.

18. The heat transfer apparatus of claim 1 wherein the working substance is a first adsorbate, further comprising a second adsorbate, the first adsorbate being adsorbed by the adsorbent at a slower rate than a rate at which the second adsorbate is adsorbed by the adsorbent.

19. The heat transfer apparatus of claim 18 wherein the first adsorbate is water and the second adsorbate is carbon dioxide.

20. The heat transfer apparatus of claim 1 wherein the adsorbent is a first adsorbent and the working substance is a first adsorbate, further comprising a second adsorbent and a second adsorbate, the first adsorbate being adsorbed by the first adsorbent at a rate different than a rate at which the second adsorbate is adsorbed by the second adsorbent.

21. The heat transfer apparatus of claim 1 wherein the second vessel has a burst pressure limit, further comprising compressible material positioned within the second vessel, the compressible material compressible by the working substance as it changes from a liquid state to a solid state between an uncompressed volume and a smaller compressed volume, the compressible material and working substance exerting a selected pressure on the container which is less than the burst pressure limit.

22. The heat transfer apparatus of claim 1 wherein the first vessel has a vacuum aperture therethrough and an internal pressure, further comprising a vacuum valve connected to the vacuum aperture, the vacuum valve connectable to a vacuum source and moveable between an open position with the vacuum source in fluid communication with the first vessel for reducing the internal pressure of the first vessel and a closed position with the first vessel sealed from the vacuum source.

23. The heat transfer apparatus of claim 1, further comprising a Stirling engine having an engine efficiency and operating between a hot reservoir and a cold reservoir wherein the second vessel is positioned to cool the cold reservoir, lowering a temperature at which the cold reservoir removes heat from the Stirling engine, and the first vessel is positioned to heat the hot reservoir, thereby increasing the engine efficiency relative to a Stirling engine lacking the heat transfer apparatus.

24. The heat transfer apparatus of claim 1, further comprising a thermal voltaic device having a hot side and a cold side and a voltage output wherein the second vessel is positioned to cool the cold side, and the first vessel is positioned to heat the hot side thereby increasing the voltage output relative to a voltage device lacking the heat transfer apparatus.

25. The heat transfer apparatus of claim 1, further comprising a turbine device positioned in the conduit between the first and second vessels, the turbine device having a turbine rotor capable of converting linear motion of the working substance as it is adsorbed by the adsorbent material from the second vessel to the first vessel to rotational motion and transferring energy associated with the rotational motion outside the conduit.

26. The heat transfer apparatus of claim 1 wherein the first and second vessels, conduit and working substance define a first refrigeration unit, further comprising at least a second refrigeration unit, the second vessels of the refrigeration units being contained within a refrigeration chamber defining a refrigerated volume, the refrigeration units being controllable to maintain the refrigerated volume at a selected temperature.

27. The heat transfer apparatus of claim 1 wherein the first vessel has an interior area and the conduit has a perforated portion projecting into the interior area, the perforated portion having a plurality of perforations of a selected size, for passage of the working substance between the adsorbent and the conduit.

28. The heat transfer apparatus of claim 27, further comprising a mesh layer positioned between the perforated portion and the adsorbent, the mesh layer having a plurality of openings, the openings having a size that is smaller than the selected size of the perforations of the perforated portion of the conduit to prevent the adsorbent material from entering the perforations.

29. The heat transfer apparatus of claim 1, further comprising a refrigerator chamber defining an interior area having a temperature, wherein the second vessel is positioned within the interior area of the refrigerator chamber, the conduit passes through an aperture in the refrigerator chamber, and the first vessel is positioned outside the interior area, the heat transfer apparatus capable of lowering the temperature of the interior area below a temperature outside the interior area.

30. The heat transfer apparatus of claim 1 wherein the second vessel is a length of tubing.

31. The heat transfer apparatus of claim 1, further comprising a plurality of fins projecting outwardly from an exterior surface of the second vessel.

32. The heat transfer apparatus of claim 1 wherein the quantity of working substance is approximately equal to the adsorbing capacity of the adsorbent material.

33. The heat transfer apparatus of claim 1, further comprising a heat transfer source for transferring heat between the adsorbent material and a region outside the first vessel, the heat transfer source being in thermal contact with the adsorbent material.

34. The heat transfer apparatus of claim 33 wherein the heat transfer source is a water jacket surrounding the adsorbent material.

35. The heat transfer apparatus of claim 33 wherein the heat transfer source is positioned within the first vessel.

36. The heat transfer apparatus of claim 33 wherein the heat transfer source is capable of cooling the adsorbent material.

37. The heat transfer apparatus of claim 33 wherein the heat transfer source is capable of heating the adsorbent material.

38. A method for transferring heat and a working substance between a first vessel containing an adsorbent material and a second vessel connected to the first vessel, the two vessels defining a sealed volume containing a working substance in a liquid phase, the method comprising:

allowing a portion of the working substance to vaporize by adsorption and transfer from the second vessel to the adsorptive material in the first vessel, thereby causing a remaining portion of the working substance to freeze, creating a frozen working substance; and

continuing to adsorb the frozen working substance by sublimation from the second vessel to the adsorptive material in the first vessel.

39. The method of claim 38, further comprising continuing to adsorb the frozen working substance by sublimation from the second vessel to the adsorptive material in the first vessel until the frozen working substance is substantially completely adsorbed by the adsorbent material.

40. The method of claim 38, further comprising:

heating the adsorbent to drive the working substance in a vapor state from the adsorbent to the second vessel; and

condensing the working substance from a vapor state to a liquid state in the second vessel.