Solar refrigeration and heating system usable with alternative heat sources

Information

  • Patent Grant
  • 6260370
  • Patent Number
    6,260,370
  • Date Filed
    Friday, August 27, 1999
    25 years ago
  • Date Issued
    Tuesday, July 17, 2001
    23 years ago
Abstract
An apparatus for heating and cooling includes a solar collector for transferring heat energy from incident solar rays to a liquid refrigerant material thereby changing a first portion to a gaseous state. An eductor-venturi reduces a pressure of the gaseous refrigerant material and a condenser removes the heat energy thereby changing the refrigerant material back to the liquid state. A heat exchanger associated with the condenser receives the heat energy removed from the refrigerant material. A float evaporator mounted in a cold chamber transfers heat energy from the atmosphere to the liquid refrigerant material thereby changing a second portion to the gaseous state and cooling the cold chamber atmosphere. A float actuated valve connected to the float evaporator is responsive to a level of the liquid refrigerant material in the evaporator for regulating a flow of the liquid refrigerant material into the evaporator.
Description




BACKGROUND OF THE INVENTION




The present invention relates generally to a system for cooling and heating and, in particular, to an apparatus and method for both heating and cooling powered by a solar heat source.




The U.S. Pat. No. 4,120,289, issued on Oct. 17, 1978 to Edward W. Bottum, shows a solar water heating system including a solar collector connected to a heat exchanger in a closed loop charged with refrigerant. The refrigerant is boiled in the collector and condensed in the heat exchanger to give off heat to water passing through the heat exchanger.




It is known that a heat pump system can be utilized to make ice. The U.S. Pat. No. 4,142,678, issued on Mar. 6, 1979 to Edward W. Bottum, shows a heat pump system having a compressor, evaporator and condenser connected together for the circulation of fluid refrigerant. The evaporator is a plate element that collects heat from the sun's rays. During cooler periods or when there is no sunlight, water is sprayed on the underside of the evaporator plate. This water freezes and forms a layer of ice that can be removed and used. The formation of ice also generates heat that is available to the heat pump thereby increasing the efficiency of the system.




U.S. Pat. No. 4,383,419, issued on May 17, 1983 to Edward W. Bottum, shows a heating system employing a heat pump that is provided with heat by a second system employing refrigerant as a heat transfer medium. The refrigerant is boiled using heat energy from the ground or a body of water, for example.




SUMMARY OF THE INVENTION




The present invention concerns an apparatus for heating and cooling including a heat source for transferring incident heat energy to a liquid refrigerant material thereby changing the refrigerant material from the liquid state to a gaseous state. The heat source has an inlet for receiving the refrigerant material in the liquid state and an outlet for discharging the refrigerant material in the gaseous state.




A venturi reduces the pressure of the refrigerant material. A “venturi”, as used herein, refers to a component having an inlet receiving higher-pressure gas and discharging it at a somewhat lower pressure through an outlet. It also has a second inlet capable of receiving gas at a considerably lower pressure (or vacuum) from an evaporator and discharging it through the same outlet Such a device is sometimes called an “eductor”.




The venturi has a first inlet connected to the heat source outlet for receiving the gaseous refrigerant material and an outlet for discharging the reduced pressure gaseous refrigerant material. A condenser means removes heat energy from the refrigerant material, thereby changing the refrigerant material from the gaseous state to the liquid state. The condenser means has an inlet connected to the venturi outlet for receiving the reduced pressure gaseous refrigerant material and an outlet for discharging the refrigerant material in the liquid state. The condenser means outlet is connected to the heat source inlet to return the liquid refrigerant material to the heat source. A heat exchange means is associated with the condenser means for receiving the heat energy removed from the refrigerant material by the condenser means.




A cold chamber containing an atmosphere has an evaporator means mounted in it to transfer heat energy from the cold chamber atmosphere to the liquid refrigerant material thereby changing the refrigerant material from the liquid state to the gaseous state and cooling the cold chamber atmosphere. The evaporator means has an inlet connected to the condenser means outlet for receiving the liquid refrigerant material and an outlet connected to a second inlet of the venturi for discharging the gaseous refrigerant material to the venturi. A valve is connected to the evaporator means inlet and is responsive to a level of the liquid refrigerant material in the evaporator means to regulate a flow of the liquid refrigerant material into the evaporator means. As liquid refrigerant boils due to its reduced pressure, heat is absorbed.




The expansion means for the evaporator can be an expansion valve, a “low side float”, or a capillary and a sight glass can be connected between the heat source and the venturi.




The invention also includes a method for simultaneously heating and cooling from a source of heat energy comprising the steps of: providing a source of liquid refrigerant material and transferring incident heat energy from a source of the heat energy to the liquid refrigerant material thereby changing a first portion of the refrigerant material from the liquid state to a gaseous state; reducing a pressure of the gaseous refrigerant material; removing the heat energy from the refrigerant material thereby condensing the reduced pressure gaseous refrigerant material to change the refrigerant material from the gaseous state to the liquid state; providing a heat exchange means for receiving the heat energy removed from the reduced pressure gaseous refrigerant material; evaporating a second portion of the liquid refrigerant material condensed from the reduced pressure gaseous refrigerant material by transferring heat energy from an atmosphere to the second portion of the liquid refrigerant material thereby changing the refrigerant material from the liquid state to the gaseous state and cooling the atmosphere; and returning the first portion of the liquid refrigerant material to the source of the liquid refrigerant material whereby the incident heat energy simultaneously produces heat energy in the heat exchange means and cools the atmosphere.











BRIEF DESCRIPTION OF THE DRAWINGS




The above, as well as other advantages of the present invention, will become readily apparent to those skilled in the art from the following detailed description of a preferred embodiment when considered in the light of the accompanying drawings in which:





FIG. 1

is a schematic view of a solar powered cooling and heating apparatus in accordance with the present invention; and





FIG. 2

is a schematic block diagram of a heating and cooling system in accordance with the present invention.











DESCRIPTION OF THE PREFERRED EMBODIMENT




The present invention concerns a heating and cooling method and apparatus powered by a heating source. There is shown in the

FIG. 1

a solar energy source powered system


10


for cooling and heating in accordance with a preferred embodiment of the present invention. The solar energy source includes a conventional solar collector


12


positioned at an angle such that it is exposed to the incident rays


14


of the sun (not shown). An inlet at a lower end of the solar connector


12


is connected to one end of a liquid line


16


and an outlet at an upper end of the solar collector is connected to one end of a vapor line


18


. The liquid line


16


includes a generally horizontally extending first portion


16




a


connected between the solar collector


12


and a generally vertically extending second portion


16




b.






The vapor line


18


includes a generally vertically extending first portion


18




a


connected between the solar collector


12


and a generally horizontally extending second portion


18




b


. As described below, the solar collector


12


, the liquid line


16


and the vapor line


18


form a closed circulation path for the refrigerant material wherein the refrigerant material is in a liquid state below a generally horizontally extending liquid level


20


. The liquid level


20


is shown as a broken line which intersects the solar collector


12


adjacent the upper end thereof and also intersects the second portion


16




b


of the liquid line


16


below an upper end thereof. The refrigerant material above the liquid level


20


is in a vapor or gaseous state.




A “low side” float evaporator


22


is mounted in a cold chamber


24


. A first connecting tube


26


extends from the first portion


16




a


of the liquid line


16


to an inlet port of the float evaporator


22


. A second connecting tube


28


extends from an outlet of the float evaporator


22


to a suction inlet of an expansion means such as a jet or venturi


30


. The venturi


30


is inserted into the vapor line second portion


18




b


with a first inlet for receiving refrigerant from the solar collector


12


and an outlet. An optional sight glass


32


can be connected in the vapor line second portion


18




b


between the solar collector


12


and the inlet of the venturi


30


. The ends of the lines


16


and


18


opposite the ends connected to the solar collector


12


are connected to a condenser


34


. The vapor line second portion


18




b


is connected to an inlet of the condenser


34


and the liquid line second portion


16




b


is connected to an outlet of the condenser. A heat exchange means


36


, such as a coil, is mounted inside the condenser and is connected between a cold water inlet line


38


and a hot water outlet line


40


.




In operation, the solar collector


12


is exposed to the rays


14


of the sun which causes a first portion of the liquid refrigerant below the liquid level


20


to boil into a vapor. The vaporized refrigerant rises through the vapor line first portion


18




a


and flows through the sight glass


32


and the venturi


30


to the interior of the condenser


34


. As the gaseous refrigerant flows through the venturi


30


, a low pressure or vacuum is produced in the second connecting tube


28


. The connecting tube


28


communicates the low pressure or vacuum to the interior of the float evaporator


22


. A quantity of the liquid refrigerant is present in the evaporator


22


below a liquid level


42


. The liquid refrigerant in the evaporator


22


will boil at the lower pressure communicated through the second connecting tube


28


and absorb heat from the surrounding atmosphere in the cold chamber


24


. The absorption process can be aided by providing fins


22




b


on the exterior of the float evaporator


22


to expose more surface area to the atmosphere in the cold chamber


24


. A vaporized second portion of the refrigerant material exits the evaporator


22


through the tube


28


and joins the vaporized first portion of the refrigerant material from the solar collector


12


in the venturi


30


. As the liquid level in the evaporator


22


falls due to evaporation, a float valve


22




a


at the inlet opens to allow liquid refrigerant from the first connecting tube


26


to flow in and replace the evaporated liquid. When sufficient liquid refrigerant has entered the evaporator


22


, the float valve


22




a


closes.




The heated gaseous refrigerant from the solar collector


12


and from the evaporator


22


enters the condenser


34


. Cold water flowing into the coil


36


from the line


38


absorbs heat from the vaporized refrigerant and this hot water exits the condenser


34


through the hot water line


40


. The refrigerant in the condenser


34


is cooled by this heat loss to the liquid state and flows into the liquid line second portion


16




b


to return to the solar collector


12


. The vapor pressure in the condenser


34


will be slightly lower than the vapor pressure in upper end of the solar collector


12


, but the liquid head in the liquid line second portion


16




b


is adequate to return the liquid refrigerant to the solar collector and to the inlet of the float evaporator


22


.




There is shown in the

FIG. 2

a block diagram representation of the present invention wherein a heat source powered system


50


for cooling and heating includes a heat source


52


which can be the conventional solar collector


12


shown in the

FIG. 1

or any other source of heat including electric, fossil fuel, fuel cell, the ground, a body of water, etc. An inlet at a lower end of the heat source


52


is connected to one end of a liquid line


54


and an outlet at an upper end of the heat source is connected to one end of a vapor line


56


. The liquid line


54


includes a generally horizontally extending first portion


54




a


connected between the heat source


52


and a generally vertically extending second portion


54




b


. The vapor line


56


includes a generally vertically extending first portion


56




a


connected between the heat source


52


and a generally horizontally extending second portion


56




b.






As described below, the heat source


52


, the liquid line


54


and the vapor line


56


form a closed circulation path for the refrigerant material wherein the refrigerant material is in a liquid state below a generally horizontally extending liquid level


58


. The liquid level


58


is shown as a broken line which intersects the heat source


52


and the second portion


54




b


of the liquid line


54


below an upper end thereof. The refrigerant material above the liquid level


58


is in a vapor or gaseous state.




A float evaporator


60


is mounted in a cold chamber


62


. A first connecting tube


64


extends from the liquid line first portion


54




a


to an inlet port of the float evaporator


60


. A second connecting tube


66


extends from an outlet of the float evaporator


60


to a


10


suction inlet of a venturi


68


such as the venturi


30


shown in the FIG.


1


. The expansion means


60


also can be an expansion valve or a capillary inserted into the tube


64


with an inlet for receiving refrigerant from a condenser


70


and an outlet. The ends of the lines


54


and


56


opposite the ends connected to the heat source


52


are connected to the condenser


70


. The vapor line second portion


56




b


is connected to an inlet of the condenser


70


and the liquid line second portion


54




b


is connected to an outlet of the condenser. A heat exchange means


70




a


, such as the coil


36


shown in the

FIG. 1

, is mounted inside the condenser


70


and is connected between an inlet line


72


and an outlet line


74


.




The operation of the system


50


is similar to the operation of the system


10


shown in the FIG.


1


. The heat source


52


heats the liquid refrigerant below the liquid level


58


to create a vapor. The vaporized refrigerant rises through the vapor line first portion


56




a


and flows through the venturi


68


to the interior of the condenser


70


. As the gaseous refrigerant flows through the venturi


68


, a low pressure or vacuum is produced in the second connecting tube


66


which low pressure or vacuum is communicated to the interior of the float evaporator


60


. A quantity of the liquid refrigerant is present in the evaporator


60


below a liquid level


76


. The liquid refrigerant in the evaporator


60


will boil at the lower pressure communicated through the second connecting tube


66


and absorb heat from the surrounding atmosphere in the cold chamber


62


. The vaporized refrigerant exits the evaporator


60


through the tube


66


and joins the vaporized refrigerant from the heat source


52


in the venturi


68


. As the liquid level in the evaporator


60


falls due to evaporation, a valve means


60




a


, such as the float valve


22




a


shown in the

FIG. 1

, opens to allow liquid refrigerant from the first connecting tube


64


to flow in and replace the evaporated liquid. When sufficient liquid refrigerant has entered the evaporator


60


, the float valve


60




a


closes.




The heated gaseous refrigerant from the heat source


52


and from the evaporator


60


enters the condenser


70


. A cold transfer medium, liquid or gas, flowing into the condenser


70


from the inlet line


72


absorbs heat from the vaporized refrigerant and this hot transfer medium exits the condenser through the outlet line


74


. The gaseous refrigerant in the condenser


70


is cooled by this heat loss to the liquid state and flows into the liquid line second portion


54




b


to return to the heat source


52


. The vapor pressure in the condenser


70


will be slightly lower than the vapor pressure in upper end of the heat source


52


, but the liquid head in the liquid line second portion


54




b


is adequate to return the liquid refrigerant to the heat source and to the inlet of the float evaporator


60


.




The apparatus (


10


,


50


) for heating and cooling according to the present invention includes the heat source (


12


,


52


) for transferring incident heat energy to a liquid refrigerant material thereby changing the refrigerant material from the liquid state to a gaseous state, the heat source having an inlet for receiving the refrigerant material in the liquid state and an outlet for discharging the refrigerant material in the gaseous state; the venturi (


30


,


68


) for reducing a pressure of the refrigerant material, the venturi having an inlet connected to the heat source outlet for receiving the gaseous refrigerant material and having an outlet for discharging the reduced pressure gaseous refrigerant material; the condenser means (


34


,


70


) for removing heat energy from the refrigerant material thereby changing the refrigerant material from the gaseous state to the liquid state, the condenser means having an inlet connected to the venturi outlet for receiving the reduced pressure gaseous refrigerant material and an outlet for discharging the refrigerant material in the liquid state, the condenser means outlet being connected to the heat source inlet for returning the liquid refrigerant material to the heat source; the heat exchange means (


36


,


70




a


) associated with the condenser means for receiving the heat energy removed from the refrigerant material by the condenser means; the cold chamber (


24


,


62


) containing an atmosphere; the evaporator means (


22


,


60


) mounted in the cold chamber for transferring heat energy from the cold chamber atmosphere to the liquid refrigerant material thereby changing the refrigerant material from the liquid state to the gaseous state and cooling the cold chamber atmosphere, the evaporator means having an inlet connected to the condenser means outlet for receiving the liquid refrigerant material and having an outlet connected to another inlet of the expansion means for discharging the gaseous refrigerant material to the expansion means; and the valve (


22




a


,


60




a


) connected to the evaporator means inlet and being responsive to a level of the liquid refrigerant material in the evaporator means for regulating a flow of the liquid refrigerant material into the evaporator means whereby the heat energy incident upon the heat source produces heat energy in the heat exchange means and cools the cold chamber atmosphere.




The method according to the present invention for simultaneously heating and cooling from a source of heat energy comprises the steps of: a. providing a source of liquid refrigerant material and transferring incident heat energy from a source of the heat energy to the liquid refrigerant material thereby changing a first portion of the refrigerant material from the liquid state to a gaseous state; b. reducing a pressure of the gaseous refrigerant material; c. removing the heat energy from the refrigerant material thereby condensing the reduced pressure gaseous refrigerant material to change the refrigerant material from the gaseous state to the liquid state; d. providing a heat exchange means for receiving the heat energy removed from the reduced pressure gaseous refrigerant material; e. evaporating a second portion of the liquid refrigerant material condensed from the reduced pressure gaseous refrigerant material by transferring heat energy from an atmosphere to the second portion of the liquid refrigerant material thereby changing the refrigerant material from the liquid state to the gaseous state and cooling the atmosphere; and f. returning the first portion of the liquid refrigerant material to the source of the liquid refrigerant material whereby the incident heat energy simultaneously produces heat energy in the heat exchange means and cools the atmosphere. The method also includes adding the gaseous first portion of the refrigerant material to the gaseous second portion of the refrigerant material prior to performing the step c.




In accordance with the provisions of the patent statutes, the present invention has been described in what is considered to represent its preferred embodiment. However, it should be noted that the invention can be practiced otherwise than as specifically illustrated and described without departing from its spirit or scope.



Claims
  • 1. An apparatus using incident heat energy and a refrigerant material for heating a transfer medium and cooling an atmosphere comprising:a heat source for transferring incident heat energy to a liquid refrigerant material thereby changing the refrigerant material from the liquid state to a gaseous state, said heat source having an inlet for receiving the refrigerant material in the liquid state and an outlet for discharging the refrigerant material in the gaseous state; a venturi for reducing a pressure of the refrigerant material, said venturi having a first inlet connected to said heat source outlet for receiving the gaseous refrigerant material, an outlet for discharging the reduced pressure gaseous refrigerant material and a second inlet; a condenser means for removing heat energy from the refrigerant material thereby changing the refrigerant material from the gaseous state to the liquid state, said condenser means having an inlet connected to said venturi outlet for receiving the reduced pressure gaseous refrigerant material and an outlet for discharging the refrigerant material in the liquid state, said condenser means outlet being connected to said heat source inlet for returning the liquid refrigerant material to said heat source; a heat exchange means associated with said condenser means for receiving the heat energy removed from the refrigerant material by said condenser means, said heat exchange means having an inlet line and an outlet line for circulating a transfer medium to absorb the heat energy removed from the refrigerant material for heating purposes; a cold chamber containing an atmosphere; and an evaporator means mounted in said cold chamber for transferring heat energy from the cold chamber atmosphere to the liquid refrigerant material thereby changing the refrigerant material from the liquid state to the gaseous state and cooling the cold chamber atmosphere for cooling purposes, said evaporator means having an inlet connected to said condenser means outlet for receiving the liquid refrigerant material and having an outlet connected to said second inlet of said venturi for discharging the gaseous refrigerant material to said venturi whereby a first portion of the refrigerant material circulates through said heat source for heating said transfer medium from the incident heat energy and simultaneously a second portion of the refrigerant material circulates through said evaporator means for heating said transfer medium and cooling the atmosphere in said cold chamber.
  • 2. The apparatus according to claim 1 wherein said evaporator means is one of a low side float and an expansion valve.
  • 3. The apparatus according to claim 1 including a sight glass connected between said heat source and said venturi.
  • 4. The apparatus according to claim 1 including a valve connected to said evaporator means inlet and being responsive to a level of the liquid refrigerant material in said evaporator means for regulating a flow of the liquid refrigerant material into said evaporator means whereby the heat energy incident upon said heat source produces heat energy in said heat exchange means and cools the cold chamber atmosphere.
US Referenced Citations (11)
Number Name Date Kind
2199779 Buchet May 1940
2475897 Iwanski Jul 1949
3146603 Porter, Jr. Sep 1964
4120289 Bottum Oct 1978
4142678 Bottum Mar 1979
4301662 Whitnah Nov 1981
4321801 Collard, Jr. Mar 1982
4345440 Allen et al. Aug 1982
4383419 Bottum May 1983
4765148 Ohashi Aug 1988
5419155 Boehde et al. May 1995