CROSS REFERENCE TO RELATED APPLICATIONS

The present application claims priority to U.S. Provisional application No.

61/410,053 filed November 4, 2010, which is herein incorporated by reference in its entirety.

FIELD OF THE INVENTION

This invention relates generally to the field of geothermal heating and cooling, and more particularly to an improved heat transfer geothermal system that includes at least one geothermal column positioned within an earth mass for transfer of heat to and from the earth mass.

BACKGROUND OF THE INVENTION

Any publications or references discussed herein are presented to describe the background of the invention and to provide additional detail regarding its practice.

Nothing herein is to be construed as an admission that the inventors are not entitled to antedate such disclosure by virtue of prior invention.

Geothermal energy is becoming more and more important in the global environment as the supply of fossil fuels diminish, the demand for energy increases, control and demands from oil producing companies are at issue and the costs of energy continues to rise. Although large geothermal energy production facilities are being used throughout the world to produce more and more electricity especially in areas like California where there is tremendous inner earth activity, more focus needs to be placed on individual systems which are based on the earth's constant temperature at shallow depths to enable efficient heating and cooling for buildings and which can be installed at the site of use. In order for individual systems to gain broader market acceptance, there is a need for better control of the earth-refrigerant interface, easier installation methods, and greater efficiencies.

SUMMARY OF THE INVENTION

These features, together with other objects and advantages which will become subsequently apparent in light of the present description, reside in the details of construction and operation as more fully hereinafter described and claimed, reference being had to the accompanying drawings forming a part hereof, whereinlike numerals refer to like parts throughout.

An object of the present invention is to provide an improved geothermal system that can include at least one geothermal column that is configured so that it is easy to install, has enhanced heat transfer qualities that uses an antifreeze free liquid disposed therewithin to transfer heat to or from the surrounding earth mass in substantially vertical orientation. This orientation and approach requires far less digging, drilling and landmass than conventional horizontal and deep vertical well systems and provides low impact to the environment (i.e. is "green").

One embodiment of the improved geothermal system includes at least one geothermal column including at least one spirally wound refrigeration coil configured to communicate with a heat pump compressor; a hollow tube having an outer wall of diameter substantially greater than that of the at least one spirally wound refrigeration coil and positioned so as to surround said at least one spirally wound refrigeration coil, said outer wall having.a substantially rigid configuration so that said hollow tube maintains its shape under ordinary conditions of deployment; and a support member configured to retain a shape of said at least one spirally wound refrigeration coil and maintain a centrally located position of said at least one spirally wound refrigeration coil within said hollow tube. The system further includes an expansion device such as a thermostatic expansion valve (TXV) configured to communicate with the at least one spirally wound refrigeration coil. The system further includes a compressor section configured to communicate with the at least one spirally wound refrigeration coil, the expansion device, and at least one of a building heating system and cooling system.

Another embodiment of the improved geothermal system includes at least one geothermal column, comprising at least one spirally wound refrigeration coil configured to communicate with a heat pump compressor; a hollow tube having an outer wall of diameter substantially greater than that of said at least one spirally wound refrigeration coil and positioned so as to surround said at least one spirally wound refrigeration coil, said outer wall having a substantially rigid configuration such that said hollow tube maintains its shape under ordinary conditions of deployment; and a support member configured to retain a shape of said at least one spirally wound refrigeration coil and maintain a centrally located position of said at least one spirally wound refrigeration coil within said hollow tube; and a compressor section in communication with the at least one geothermal column and at least one of a climate system such as a heating system and/or a cooling system. Moreover, the geothermal system can be integrated such that the geothermal column, compressor section and climate system are incorporated into a single packaged system which is deployable as a single unit.

In addition to the above aspects, the substantially rigid hollow tube configuration of the present invention allows for the production of a pre-fabricated unit that can be installed quickly and easily in the field without the need of skilled laborers. The outer wall can be constructed from flexible, rigid, or semi-rigid corrugated material designed to more efficiently transfer heat energy to the environment such that an antifreeze-free liquid vehicle in the hollow tube can be used, which is better for the environment. That is, the improved wall construction and heat circulation within the hollow tube of the present invention is such that antifreeze is not necessary reducing the chance of contaminating the surrounding soil should an accidental leak/spill occur.

The new factory assembled unit of the improved geothermal column of the present invention are positioned within an earth mass whereby during operation, the refrigerant coils transfer heat to and from the antifreeze-free liquid vehicle disposed within the hollow tube to cause a convection cycle within the antifreeze-free liquid to bring the antifreeze-free liquid to a more uniform temperature throughout so as to prevent freezing in one part and overheating in others. This configuration and structure results in is a superior degree of heat transfer with a reduction of hot or cold spots as would be experienced in traditional direct exchange geothermal technologies. BRIEF DESCRIPTION OF THE DRAWING(S)

In the drawings, to which reference will be made in the specification, similar reference characters have been employed to designate corresponding parts throughout the several views.

Figs. 1 A to 1C are perspective views of various stages of cutaways of a geothermal column according to an embodiment of the present invention.

Fig. 2 is a cross sectional view of a geothermal column according to an embodiment of the present invention.

Fig. 3 is a top view of a geothermal column according to an embodiment of the present invention.

Fig. 4 is a perspective view of a geothermal system according to an embodiment of the present invention.

Fig. 5 is a diagrammatic view of the distribution and compressor sections of the present invention.

Figs. 6-8 are various views according to an embodiment of the present invention.

DETAILED DESCRIPTION OF THE DISCLOSED EMBODIMENT

The present invention may be understood more readily by reference to the following detailed description of the invention taken in connection with the

accompanying figures, which form a part of this disclosure. It is to be understood that this invention is not limited to the specific devices, methods, conditions or parameters described and/or shown herein, and that the terminology used herein is for the purpose of describing particular embodiments by way of example only and is not intended to be limiting of the claimed invention.

As used in the specification and including the appended claims, the singular forms "a," "an," and "the" include the plural, and reference to a particular numerical value includes at least that particular value, unless the context clearly dictates otherwise.

Ranges may be expressed herein as from "about" or "approximately" one particular value and/or to "about" or "approximately" another particular value. When such a range is expressed, another embodiment includes from the one particular value and/or to the other particular value. Similarly, when values are expressed as

approximations, by use of the antecedent "about," it will be understood that the particular value forms another embodiment.

It is also understood that all spatial references, such as, for example, horizontal, vertical, top, upper, lower, bottom, left and right, are for illustrative purposes only and can be varied within the scope of the disclosure. For example, the references "upper" and "lower" are relative and used only in the context to the other, and are not necessarily "superior" and "inferior".

All methods described herein may be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., "such as") provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.

As used herein, "comprising," "including," "containing," "characterized by," and grammatical equivalents thereof are inclusive or open-ended terms that do not exclude additional, unrecited elements or method steps, but will also be understood to include the more restrictive terms "consisting of and "consisting essentially of."

The following discussion includes a description of a new and improved geothermal system of the present invention, related components and exemplary methods of employing the device in accordance with the principles of the present disclosure. Alternate embodiments are also disclosed. The geothermal system of the present invention provides a geothermal system that utilizes one or more vertical geothermal heat exchange column to exchange heat with the surrounding soil environment in an efficient and environmentally safe way. The system is designed to reduce the use of fossil fuels and therefore reduce the carbon footprint associated with conventional heating and cooling systems presently available on the market today.

Reference will now be made in detail to the exemplary embodiments of the present disclosure, which are illustrated in the accompanying figures. Turning now to the drawings, there are illustrated components of the geothermal column in accordance with the principles of the present disclosure.

In accordance with the invention, the geothermal system 100 comprises at least one geothermal column, generally indicated by reference character 10, which includes at least one spirally wound refrigeration coil 11. The spirally wound refrigeration coil 11 can be configured to communicate with a compressor section 30. These connections can be facilitated through ports 20 and 21 located on top cap 19.

Also included in the geothermal column 10 is a hollow tube 12. The hollow tube 12 includes an outer wall 13 of a diameter substantially greater than that of the spirally wound refrigeration coil 11. The outer wall 13 can be positioned so as to surround the spirally wound refrigeration coil 11. The outer wall 13 can be of a substantially rigid configuration so that the hollow tube 12 maintains its shape. The geothermal column 10 also can include a support member 14, shown in this embodiment as being comprised of a column 17 and a plurality of combs 18. Annular supports 23 are situated in a manner so as to retain their position within the hollow tube 12. The inner radius of the annular supports 23 is greater than the distance from the center of the column and an extended end 18a of each comb 18 if combs are employed in the embodiment. The combs 18 used in conjunction with the annular supports 23 restrict lateral movement of the support member 14 and allow vertical movement of the support member 14.

A bottom cap 22 Is securely attachable to the bottom of the hollow tube 12 in a manner to provide a watertight seal between bottom cap 22 and the hollow tube 12. The top cap may be fastened to the hollow tube 12 in such a way as to allow removal for service but secure attachment for transport and installation. This removable method of securement may allow for venting of any internal pressures built up within the column 10. The support member 14 is attached to the top cap 19. The support member 14 is configured to retain the shape of the spirally wound refrigeration coil 11. The support member 14 can also function to maintain a centrally located position of the spirally wound refrigeration coil 11 within said hollow tube 12. The geothermal column 10 is designed to be positioned within a void in a surrounding earth mass (not shown). A non-antifreeze fluid 16 fills the space within the hollow tube 12 and surrounds substantially all of the surface area of the spirally wound refrigeration coil 11 ; water is a preferred non-anti-freeze fluid 16.

The spirally wound refrigeration coil 11 is sized to optimum performance levels based on system requirements. System requirements can include size of an area to be heated/cooled, geological conditions in and around the geothermal column installation area, etc. The geothermal heat exchange column components are sized independently and as a system to match heat exchange from the copper coil to water to the heat exchange from the water to the earth, while optimizing the trade off between pressure drop and component cost. At the same time, critical oil entrainment velocities are ensured, and coil diameter to column diameter ratios are maintained to facilitate convective mixing in the described annulus. Further, overall dimensions are selected from a limited array of values that are constrained by commonly available materials (e.g. standard copper tube diameters, standard corrugated column diameters and lengths, common augur bit diameters, etc.) and practically maneuvered and transported sizes. Additionally, practicality is exercised in sizing geothermal columns to factors of or fractions of heating and cooling tons (one ton = 12,000 btuh and is the commonly used measurement of HVAC system size). The required refrigerant velocity for oil

entrainment is given roughly by the equation:

MinimumVelocity = A ^* SquareRoot(lnnerDiameter) where A is a constant that varies depending upon refrigerant phase and orientation (horizontal or vertical) of flow. Mass flow through each circuit (coil) within the heat exchanger is based on the rated mass flow of the selected compressor and its rated tonnage:

MassFlowCircuit = MassFlowSystem / ColumnsPerSystem / CircuitsPerColumn. Minimum required mass flow through each circuit is determined by calculating the mass flow through a tube of given diameter in the liquid phase vertical orientation with certain density characteristics:

MinimumMassFlow = MinimumVelocity * CrossSectionalArea * Density(p,t).

Equating MassFlowCircuit to MinimumMassFlow allows a direct relationship between pipe diameter (via CrossSectionalArea) and the required number of circuits per column. Discretion here must be used to select applicable results based on practical applications such as even numbers of circuits or reasonable numbers of circuits relative to creating a practically sized manifold. Given the number of circuits required per column at a given pipe diameter as well as a mass flow at that diameter, and assuming certain operating conditions near the extremes (for example water temperatures near 32 or 90 degrees F) one skilled in the art can determine the required length of tubing for effecting phase change from liquid to vapor or vice versa. Further, based upon this required circuit length and associated velocity and density at certain conditions including vapor quality, one can determine the pressure drop along the length of the circuit. Finally given the length of circuit, number of circuits, cost of raw materials, and pressure drop along the length, one can evaluate the tradeoff of pressure drop against added cost - both of which impact the success of the invention negatively. The column containment vessel is sized based upon both the volume of the fluid contained, which is a function of the physical dimensions of the containment, and the amount of energy which can be transferred to or from the column which is based upon the temperature differential between the fluid and the earth, the surface area of the transfer medium, and the thermal conductivities of the water, the containment, and the soil. The transfer rate of energy between the heat exchanger coil and the water given adequate minima of design is a function of the number of columns per the rated capacity of the compressor (e.g. two columns per ton), and as such the minimum design of the geothermal column is to sufficiently match that heat exchange into the earth. As the energy is absorbed or rejected by the earth, the earth will subsequently change temperature. As the temperature is measured in all directions away from the heat exchange column, the temperature change asymptotically approaches zero. Based upon a proposed work load of the system and an allowable earth temperature change rate, the minimum required geothermal column spacing can be determined for a geothermal column of particular size and energy transfer rate.

In a preferred embodiment at least one of upper oil trap 24, upper oil trap 25, and lower oil traps 26 provide oil entrainment and return. Oil entrainment and return is a critical design issue in nearly all HVAC products, as standard compressors are sealed and do not contain independent oil reservoirs. As such, the compressor relies on the refrigerant to carry oil away from and returning to the compressor in order to maintain lubrication. While the oil is designed to be miscible in the refrigerant, there is a certain velocity that is required in order to keep the oil from falling out of suspension. Oil separation resulting from poor design or improper operation can result in insufficient return and ultimately compressor failure. Additionally, in long piping runs or in unusually high vertical drops, oil which has naturally fallen out of suspension upon shut down of a system has a tendency to migrate to a natural low point. Often when the system is restarted, that oil only very slowly or never returns to the compressor. Vertical drops and rises and long piping runs are unavoidable aspects of the present invention.

Embodiments of the present invention include optimized piping sizing to ensure sufficient oil entrainment, but also include newly designed oil traps into the piping configuration. Oil traps 24, 25 and/or 26 are incorporated at the top entrance and exit points of the spirally wound refrigeration coil 1. Upper oil traps 24 and/or 25 include a loop design having loops approximately 8" in diameter oriented in a vertical plane.

Lower oil traps 26 include a U-bend design.

Spirally wound refrigeration coil 11 includes one or more individual sections. In the drawings two sections 11a and 11b are shown. While individual sections are coiled and stacked vertically along the column 17, the lower exit of each coil extends to the lowest point in the column to equalize pressure head among all sections and to equalize the oil "plug" induced pressures among all circuits, aiding in oil return from the lowest points in the systems. That is, each section 11 a and 11 b are equal in length. By varying the number of sections, the heating/cooling capacity of the geothermal column 10 can be varied. For example, each section can represent ¼ of a ton of conditioning capacity - i.e. two sections can be incorporated into a ½-ton geothermal column 10, and four sections can be incorporated into a 1-ton geothermal column 10. As stated above, each section should preferably be of substantially equal length in order to ensure equal refrigerant distribution to each column as a result of pressure differentials.

Sections 1 a and 11 b of the spirally wound refrigeration coil 1 lean be so arranged such that the refrigerant enters at a plurality of positions in the coil and exits from the upper region. This arrangement assures that there is an equal distribution of refrigerant in the spirally wound refrigeration coil 11 so that the heat transfer can be uniform throughout the device, which, in turn, can prevent sections of the tubing from overheating or freezing.

Sections 11 a and 11 b of the spirally wound refrigeration coil 11 are preferably constructed from copper tubing. The tubing, which is preferably between one-eighth of an inch to 1 inch in diameter, are in substantially full contact with the non-antifreeze liquid 16 in the hollow tube 12. The diameter of the tubing is determined by the number of columns and the cooling/heating capacity that the system is designed to cool/heat. By design, the non-antifreeze liquid 16 contained within the hollow tube 12 at the lower region is heated to a greater temperature than at the upper region, which causes the water within the tube to move upward to create a cyclic motion.

Depending upon operational mode (that is, heating or cooling mode), continuing compressor operation may cause an increase in the temperature of the lower region thereby increasing the rate of flow of the tube and, as a result, the mixing rate of the liquid mass is also increased. Since heat transfer is a function of temperature

difference, the greater the difference between the refrigerant temperature and the water, the greater the heat transfer there between. Similarly, as heat is transferred from the refrigerant to the water, the difference between the water and the earth mass increases as does the heat transfer.

In a preferred embodiment the hollow tube 12 has a diameter between 12 and 40 inches and a length between 12 and 30 feet. Also in a preferred embodiment the spirally wound refrigeration coil 11 has a spiral diameter of between 4 and 16 inches and a spiral length of between 10 and 100 feet, and an overall length between 30 and 50 feet.

Although the support member 14 is depicted in Figs. 1A to 1C as a column 17 and a plurality of combs 18, the support member 14 can be configured in other forms. As stated above, one use of the support member 14 is to maintain the form of the spirally wound refrigeration coil 1 , while another use of the support member 14 is to maintain the lateral position of the spirally wound refrigeration coil 11 within the hollow tube 2. Yet another use of support member 14 is to provide vertical lifting support to the spirally wound refrigeration coil 11 during repair and/or replacement, to be described in more detail below.

In light of these uses, column 17 can be for example tubular in nature, i.e. a pipe, a thin rod, etc. Another embodiment envisions the use of spacing clips or attachment devices that can be secured to the tubing of the spirally wound refrigeration coil 11 to maintain an evenly spaced coil.

Lift support 27 is provided on the top cap 19 of the geothermal column 10 to provide an attachment location for lifting means to lift the geothermal column 10. Lifting is required during installation and repair. During the installation process the top cap 19 can be secured to the hollow tube 12 and the entire geothermal column 10 can be lifted to be inserted into a pre-bored hole in the earth. During repair, the top cap 19 is unsecured from the hollow tube 12 and the top cap 19 the support member 14 and the spirally wound refrigeration coil 11 can be removed for inspection and access. This repairable design is unique to the present invention and prevents the need to excavate the entire geothermal column 10 for repair. Even in the event that the hollow tube 2 develops a leak, the top cap 19 the support member 14 and the spirally wound refrigeration coil 11 can be removed to effect a repair on the hollow tube 12. one embodiment of the repair envisions the use of a flexible non-porous insert that can be inserted into the hollow tube 12, and into which the top cap 19 the support member 14 and the spirally wound refrigeration coil 11 can be reinserted.

Also shown on top cap 19 are ports 28 and 29, Ports 28 and 29 can be used for access to the interior of hollow tube 2. Access can be used to fill the hollow tube 12 with the non-antifreeze fluid 16 after the geothermal column 10 is installed. In addition, a temp sensor and fluid level switch (not shown) can be installed and accessed through ports 28 and/or 29.

The geothermal column 0 is not a sealed unit, and as such, changes in temperature can result in expansion and contraction of the geothermal column 10 and subsequently the earth surrounding it. As such, there is moderate opportunity for water to escape as a result of evaporation during operation of a system incorporating a geothermal column 10. Loss of the non-anti-freeze fluid 16 can be detrimental to the efficient operation of the system incorporating a geothermal column 10. In order to mitigate this possibility, a float switch at the top of each geothermal column 10 wired to a single or multiple water solenoid valve(s) (not shown) and a power supply can be included. The solenoid valve(s) is/are plumbed into a water supply and, upon the triggering of the circuit by the float switch indicating an insufficient water level, water can be added to the geothermal column 10. Low water level alarms and/or indicators can also be incorporated into the system. Referring to Fig. 4, in a preferred embodiment, a plurality of geothermal columns 10 are provided in the geothermal system 100. A preferred embodiment can also include a compressor section 30 and a distribution section 50. The geothermal system 100 is configured to be in communication with a climate system 99. The climate system can be at least one of a heating system and a cooling system.

The geothermal system 100 is a closed refrigerant system. HCFC refrigerants are contemplated, and can include the industry standard R-22. Other refrigerants can include HFC refrigerants, for example, R-407C and R-410A. Both of these HFC refrigerants are zeotropic blends of other HFC refrigerants that provide both usability and high efficiency potential. R-407C shares similar psychometric properties as HCFC R-22, while R-41 OA operates at pressure and temperature ranges in the range of 75% higher than R-22. R-41 OA is marginally more efficient than R-407C and has emerged as the new standard in Heating-Ventilation-Air Conditioning (HVAC) equipment. While equipment design characteristics for R-407C are essentially identical to the former R-22 equipment with the exception of the use of polyolester oil rather than mineral oils as lubricants, R-41 OA requires different tubing lengths and diameters, pressure vessels and ports, and some critical components (compressors, TXVs, etc.)

Referring to Fig. 5, the distribution section 50 can include an expansion device 51 such as a Thermostatic Expansion Valve (TXV), a check valve 52, a distribution manifold 53 and a collector manifold 54. Each of the geothermal columns 10 can be connected to an output of the distribution manifold 53 and an input of the collector manifold 54. In this manner, the geothermal columns 10 are connected in a parallel fashion with each other. This provides for even distribution of heating and cooling among the geothermal columns 10. This also provides to equally distribute the refrigerant into each of the geothermal column 10 spirally wound refrigeration coil 11 sections 1 a and 11 b. Parallel distribution also provides multiple points of entry into the heat exchange process resulting in heat exchange driven by greater temperature differences at each of the multiple points as opposed to a single point of maximum temperature differential followed by a subsequent extended length of heat exchange device interacting at reduced and less effective temperature differential. Additionally these multiple shorter lengths allow for smaller diameter tubing resulting in more surface area per volume than a necessarily larger diameter tube. The expansion device 51 can be connected to the input of the distribution manifold 53. A check valve 52 can be included in parallel but opposite functional direction with the expansion device 51.

The expansion device 51 can be included to provide adiabatic expansion

(pressure drop and temperature drop but no energy loss) of the refrigerant. A TXV expansion device is a sophisticated method of providing for the adiabatic expansion in that the orifice opening through which the high pressure refrigerant flows has a variable size, and this size is controlled by the downstream temperature and pressure of the refrigerant. An embodiment of the present invention utilizes a single TXV expansion device 51 , sized for the corresponding system size {e.g. tonnage) which is close- coupled to the distribution manifold 53.

In an alternate embodiment, a single smaller TXV can be placed within each geothermal column 10 (e.g. a Ya-ton TXV within a ½-ton geothermal column and/or a 1- ton TXV within a 1-ton geothermal column), along with the removal of the centrally located expansion device 51. In this alternate embodiment, the refrigerant tubing arrangement is simplified from a radial array with multiple circuits running to each geothermal column 10 to a common supply and return pipe running from one

geothermal column 10 to the next. This is made possible due to the fact the each geothermal column 10 can be regulated by its own expansion device, and as such the system can perform in a more naturally balanced manner. System efficiencies should likewise increase due to the reduced length of restrictive copper tubing. From a cost perspective, the amount of copper is substantially reduced, as is the amount of trenching required. This also in turn results in an increased ease of installation by reducing trenching and connection complexity. The alternate embodiment also represents an improvement over the current technology in that geothermal column(s) placed in areas of differing subsurface conditions (e.g. one column in a high-water table area with another in dry sand) would traditionally result in a misbalanced system where refrigerant follows a path preferring one column over the other as a result of

temperature and/or pressure conditions and in turn underutilizes the remaining geothermal column(s). However in the alternate embodiment, each geothermal column 10 functions at optimum efficiency as a result of localized controls. Another

improvement effected by the alternate embodiment is the ability to further componentize the system with regards to sales and installation by removing an entire system component, and second by defining each geothermal column 10 as a standalone unit rather than a heat exchanger which is reliant upon additional components. In this embodiment, the columns still interact in a parallel manner (refrigerant does not travel from one column to any subsequent column) although the supply and return piping is contained within a single trench which connects each of the columns in a single loop. Compressor section 30 can include a first isolation valve 31 , a reversing valve 32, a compressor 33, a desuperheater 34, an accumulator 35, a second isolation valve 36, a first sight glass 37, a filter/dryer 38, a receiver 39, a solenoid valve 40 and a second sight glass 41. The first and second isolation valves 31 and 40 are typically pall or gate type valves which serve the purpose of allowing the isolation of various sections of the system as a whole so that the various isolated sections can be serviced by removing the refrigerant and or pulling the section into a vacuum state. These also allow the compressor section as an independent unit to be transported and stored in a pressurized or vacuum state. The reversing valve 32, also known as a four-way valve, provides the ability to redirect the flow of refrigerant gases so that the system can function in either a heating (heat pump) or cooling (air conditioner) mode by electrical control mechanisms. The compressor 33 is a device, preferably a hermetically sealed scroll type compressor but possibly of multiple other refrigerant compressor designs, which compresses refrigerant typically from a lower pressure gas phase to a higher pressure liquid phase. The desuperheater 34 is a water-to-refrigerant heat exchanger which is designed to provide heated water to the user at a relatively low cost. The accumulator 35 is a hollow canister with two ports which is used primarily to flash liquid refrigerant to a gaseous state or store it prior to entering the suction side of the compressor, where liquid refrigerant could cause damage. The first and second sight glasses 37 and 41 consist of components with transparent windows within the piping arrangement that allow for visual observation and confirmation of liquid levels and quality entering and leaving the receiver 39. The filter/dryer 38 is a component containing an absorbent material and filter medium used for preventing such contaminants as water, acids, and/or particulates from moving throughout the system. The filter/dryer 38 is necessarily a bi-directional flow component, as the refrigerant flow through the filter/drier changes direction from one mode to the other (heating to cooling). The receiver 39 is a hollow canister type component designed to hold excess levels of liquid refrigerant as is required when switching between the two operational modes. This is necessitated by the typical difference in the internal volume of the heat exchange coils within the air handler unit and the geothermal heat exchange columns. This device must also be designed to operate bi-directionally as mode change will reverse refrigerant flow. The solenoid valve 40 is an electrically operated refrigerant shut-off valve which is interlocked with the operation of the compressor 33 to prevent liquid refrigerant from flowing from the receiver 39 to the geothermal heat exchange columns and/or into the accumulator 35, which would cause significant amounts of liquid refrigerant to enter the suction port of the compressor upon startup. Various other designs of a compressor section are contemplated wherein not all of the above components are included or additional components are included.

The first isolation valve 31 is configured to be in communication with the collector manifold 54. The second sight glass 41 is configured to be in communication with the distributor manifold 53. The second isolation valve 36 and the first sight glass 37 are configured to be in communication with the climate system 99. In a preferred

embodiment climate system 99 is an air handler system. As stated above climate system 99 can be a heating system, a cooling system, or a combination heating/cooling system associated with a structure such as building B (Fig. 4). Also, although an air handler system is described herein, other heating and/or cooling systems are contemplated, for example, a hydronic heating system can be utilized.

It may thus be seen that the present invention can eliminate direct heat transfer from the refrigerant to the ground to obtain a number of substantial advantages. Rather than dispose the transfer tubing in horizontal orientation in the earth mass, the present invention provides for vertical positioning of refrigeration lines within a volume of water, such that the water circulates by convection to transfer heat to the landmass over a large vertically extending area. Depending upon requirements, several geothermal columns may be provided, each functioning in a similar manner. Land utilization is increased, and installation and servicing is less disruptive.

It will be understood that various modifications may be made to the embodiments disclosed herein. Therefore, the above description should not be construed as limiting, but merely as exemplification of the various embodiments. Those skilled in the art will envision other modifications within the scope and spirit of the claims appended hereto.