Heat pump energized by low-grade heat source

• US 4,637,218 A
• Filed: 11/18/1985
• Issued: 01/20/1987
• Est. Priority Date: 11/04/1974
• Status: Expired due to Term

• Current Assignee: Dimiter I. Tchernev
• Original Assignee: Dimiter I. Tchernev
• Inventors: Tchernev, Dimiter I.
• Primary Examiner(s): NOT, DEFINED
• Application Number:
  US06/801,491
• Time in Patent Office: 428 Days
• Field of Search: 62/106, 62/235.1, 62/476, 62/480, 62/490, 126/428
• US Class Current: 62/106
• CPC Class Codes: F24S 10/80 comprising porous material or permeable masses directly contacting the working fluids for conveying liquefied working fluid from evaporator sections to condenser sections with capillary force F24S10/95
• CPC Class Codes: F24S 10/95 having evaporator sections and condenser sections, e.g. heat pipes
• CPC Class Codes: F25B 17/08 the absorbent or adsorbent being a solid, e.g. salt F25B17/12 takes precedence
• CPC Class Codes: F25B 27/002 using solar energy
• CPC Class Codes: F25B 27/007 in sorption type systems
• CPC Class Codes: F25B 29/006 of the sorption type system
• CPC Class Codes: F28D 20/003 using thermochemical reactions
• CPC Class Codes: Y02A 30/27 Relating to heating, ventilation or air conditioning [HVAC] technologies
• CPC Class Codes: Y02A 30/272 Solar heating or cooling
• CPC Class Codes: Y02B 10/20 Solar thermal
• CPC Class Codes: Y02B 30/00 Energy efficient heating, ventilation or air conditioning [HVAC]
• CPC Class Codes: Y02E 10/44 Heat exchange systems
• CPC Class Codes: Y02E 60/14 Thermal energy storage

Abstract

A heat pump using zeolite as an adsorbent wherein thermal energy from adsorbing zeolite in a one hermetically sealed space is used to heat desorbing zeolite located in another hermetically sealed space, such heat being conveyed by heat exchanger conduits containing a fluid which, before heating the desorbing zeolite, has its temperature increased to about 400° F. by a gas flame, the adsorption and desorption phases being changed between the zeolites in each cycle by reversing the fluid flow in the conduits. Cooling and heating for a building or other purposes are provided through the condenser and evaporator respectively for the working gas (water) which is desorbed and adsorbed into the zeolites. A propagating temperature front is established through the fluid-to-zeolite heat exchanger conduits to provide utilization of as much as ninety percent of thermal energy available during the desorption/adsorption phases.

Claims

1. An efficient system for heat utilization which comprises:

a container defining an hermetically sealed space which contains heat exchange means, a refrigerant, an adsorbent material in thermal communication with said heat exchange means adapted to adsorb and desorb said refrigerant in response to temperature changes of said heat exchange means, condenser means for condensing said refrigerant and evaporator means for evaporating said refrigerant;

said heat exchange means comprising conduit means extending through said container and defining a passageway therethrough hermetically separate from said space;

circulation means operatively associated with said heat exchange means for selectively causing a first fluid to flow through said conduit means, said first fluid being sufficiently hot that said refrigerant is desorbed from said material, the pressure of vapor of said refrigerant in said space is increased, said vapor received by said condenser means is condensed into liquid and collected in said evaporator means and further selectively and successively causing a second fluid to flow through said conduit means, said second fluid being sufficiently cool that said refrigerant is readsorbed by said material from said evaporator means and pressure of said vapor in said space is lowered; and

means for extracting energy from a third fluid which functions to cool or heat said condenser and said evaporator means respectively.

2. A system in accordance with claim 1 wherein said adsorbent is zeolite.

3. A system in accordance with claim 2 wherein said refrigerant is water.

4. A system in accordance with claim 2 wherein said second fluid after passing through said conduit means and having its temperature increased thereby is thereafter utilized as said first fluid and is heated by a low-grade heat source before being caused to flow through a further like heat exchange means in a further like container.

5. A system in accordance with claim 4 wherein said low-grade heat source is a mixture of air and combustion products.

6. A system in accordance with claim 4 wherein said low-grade heat source is waste heat.

7. A system in accordance with claim 4 wherein said low-grade heat source is solar energy.

8. A system in accordance with claim 2 wherein said material is in an immediate thermal conduction arrangement with said conduit means and such components perform the function of causing a temperature front to be propagated through said material in the direction of movement of said first and second fluids when flowing therethrough.

29. A system in accordance with claim 2 wherein said refrigerant comprises a polar fluid.

30. A system in accordance with claim 2 wherein said refrigerant is H₂ O, NH₃, CO₂, a fluorocarbon, a chlorocarbon or a hydrocarbon.

31. A system in accordance with claim 2 wherein said low-grade heat source is a gas flame.

32. A system in accordance with claim 2 wherein said adsorbent comprises natural zeolite having a thickness of not more than about ten millimeters.

9. Apparatus which receives its energy from a lowgrade heat source and provides heating and cooling for the interior of a building, said apparatus being operable to execute an intermittent adsorption heat pump cycle, said apparatus comprising:

1. two hermetically sealed spaces, each space defined by;

(a) a first chamber containing an adsorbent material and a refrigerant, said first chamber being in thermal communication with a first heat exchanger operative in a desorption mode to exchange heat with said low-grade heat source and in an adsorption mode to exchange heat with air from the atmosphere;

(b) a second chamber for condensing and vaporizing said refrigerant, said second chamber being in thermal communication with a second heat exchanger operative to exchange heat with said interior selectively to heat or cool same; and

2. conduit means for conveying said fluid which has been heated in said adsorption mode in one said space to be further heated by said low-grade heat source and received by said first heat exchange in said other space to heat said adsorbent in its desorption mode.

10. Apparatus in accordance with claim 9 wherein said adsorbent material is zeolite.

11. Apparatus in accordance with claim 10 wherein said refrigerant is water.

12. Apparatus in accordance with claim 11 wherein said low-grade heat source is a gas flame.

13. Apparatus in accordance with claim 10 wherein the longitudinal thermal conduction of said heat exchangers is relatively low and their thermal communication with said material is sufficiently efficient so that the temperature front is propagated through said heat exchanger when said fluid is conveyed therethrough by said conduit means.

14. Apparatus in accordance with claim 13 wherein said heat exchangers are composed of an alloy metal having a thermal conductivity in quantity of heat in calories transmitted per second through a plate one centimeter across in an area of one square centimeter with a temperature difference of 1°

C. which is not more than about 0.10.

15. Apparatus in accordance with claim 14 wherein said heat exchangers comprise tubes having a thickness of about one millimeter or less.

16. Apparatus in accordance with claim 15 wherein said material comprises sliced natural zeolite having thicknesses not more than ten millimeters.

33. Apparatus in accordance with claim 10 wherein said refrigerant comprises a polar fluid.

34. Apparatus in accordance with claim 10 wherein said refrigerant is H₂ O, NH₃, CO₂, a fluorocarbon, a chlorocarbon or a hydrocarbon.

35. Apparatus in accordance with claim 10 wherein said low-grade heat source comprises gases of combustion.

36. Apparatus in accordance with claim 10 wherein said adsorbent comprises natural zeolite.

17. A process for heating and cooling an interior space by using a low-grade heat source, the process comprising the steps of:

1. providing first and second pressure tight enclosures, each enclosure having a working refrigerant, an adsorbent material, a condenser and an evaporator therein, said adsorbent material being in thermal communication with a conduit which is provided for its respective enclosure, said adsorbent material being capable of adsorbing said refrigerant exothermically;

2. providing a low-grade heat source and means for it to be alternatively in thermal communication with said conduit for each said enclosure;

3. raising the vapor pressure of said refrigerant in said first enclosure and desorbing the refrigerant from said adsorbent material using said low-grade heat source;

4. allowing refrigerant vapor in said first enclosure to be received by said condenser therein, condensing said refrigerant vapor, and transferring said refrigerant'"'"'s heat of condensation to said internal space or to the atmosphere;

5. lowering the vapor pressure of said refrigerant in said second enclosure by adsorbing said refrigerant by said adsorbent, and transferring the heat of adsorption thereby generated to said first enclosure via said conduits; and

6. repeating steps 3, 4 and 5 in the opposite of said enclosures.

18. A process in accordance with claim 17 wherein said adsorbent material is zeolite.

19. A process in accordance with claim 18 wherein said working refrigerant is water.

20. A process in accordance with claim 18 wherein said low-grade heat source is a gas flame.

21. A process in accordance with claim 20 wherein said vapor pressure in step 3 is increased to about fifty millimeters of mercury.

22. A process in accordance with claim 21 wherein said refrigerant vapor in step 4 is condensed by said condenser at a temperature of about 100°

F.

23. A process in accordance with claim 22 wherein said vapor pressure in step 5 is reduced to at least ten millimeters of mercury.

37. A process in accordance with claim 18 wherein said refrigerant comprises a polar fluid.

38. A process in accordance with claim 18 wherein said refrigerant is H₂ O, NH₃, CO₂, a fluorocarbon, a chlorocarbon or a hydrocarbon.

39. A process in accordance with claim 18 wherein said low-grade heat source comprises gases of combustion.

40. A process in accordance with claim 18 wherein said adsorbent comprises natural zeolite.

24. Apparatus for exchanging heat between a fluid and a solid adsorbent which comprises a conduit for said fluid which is composed of metal having a thermal conductivity measured in quantity of heat in calories which is transmitted per second through a plate one centimeter thick across an area one square centimeter when the temperature difference is 1°

C. which is in the range of about 0.05 to 0.1, said conduit having an effective thickness of about 0.5 millimeters or less, the thermal conductivity of said solid adsorbent being substantially less than said conduit, said solid adsorbent mounted on said conduit in immediate thermal communication therewith and having a thickness of not more than about ten millimeters, said conduit and said solid adsorbent thereon being so arranged that a heat transfer takes place between a fluid flowing in said conduit and said solid adsorbent wherein said fluid and said solid adsorbent have different initial temperatures along a temperature front which moves along said solid adsorbed in the direction of said fluid'"'"'s movement, the temperature of said solid behind said front being about the same as said fluid behind said front and remaining at about its initial temperature forward of said front.

25. Apparatus in accordance with claim 24 wherein said solid absorbent is zeolite.

26. Apparatus in accordance with claim 25 wherein said initial temperature is about 100°

F.

27. Apparatus in accordance with claim 26 wherein said temperature of said zeolite at said front is about 300°

F.

28. Apparatus in accordance with claim 27 wherein said fluid is substantially air at substantially atmospheric pressure.

41. Apparatus in accordance with claim 25 wherein said fluid comprises a polar fluid.

42. Apparatus in accordance with claim 41 wherein said fluid is H₂ O, NH₃, CO₂, a fluorocarbon, a chlorocarbon or a hydrocarbon.

43. Apparatus in accordance with claim 24 wherein said solid adsorbent comprises natural zeolite.