Heat exchanger with heat exchange chambers utilizing protrusion and medium directing members and medium directing channels

Abstract

A heat exchanger has a plurality of chamber units. The chamber units include an inlet orifice, an outlet orifice, and a plurality of walls defining a chamber interior. The inlet receives a heat exchange medium flowing in a first flow direction in an initial line of flow. Disposed within the chamber interior is a medium directing member, having an inclined surface, which diverts the heat exchange medium from the initial flow direction so that it disperses within the chamber interior in at least two distinct flow patterns. Directional flow of the medium may be facilitated by two medium directing channels disposed within one or more of the chamber walls. Protrusion members on one or more chamber walls enhance dispersion of the heat exchange medium, causing a turbulent flow pattern within the chamber interior. The heat exchange medium exits the chamber, via the outlet, in the initial line of flow. The chambers are interconnected to form assemblies. Plural assemblies are arranged between manifolds to complete the heat exchanger.

Description

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates generally to heat exchangers and, more specifically, to a tube and chamber apparatus for transporting heat exchange media.

2. Discussion of the Related Art

Heat exchangers are commonly utilized in systems where it is desired for heat to be removed. Typical basic heat exchangers are made of pipes, which channel heat exchanging media. Headers or manifolds are attached to each end of the pipes. These headers and manifolds act as receptacles for the heat exchanging media. The efficiency of the pipe heat exchangers is limited by the amount of surface area available for the transfer of heat.

To add more surface area, some heat exchangers, such as condensers, incorporate a “tube-and-fin” design. This type of heat exchanger typically includes flattened tubes having a fluid passing therethrough and a plurality of fins extending between the tubes. The fins are attached to the tubes to effectively increase the surface area of the tubes, thereby enhancing heat transfer capability of the tubes. A number of tubes and fins may be stacked on top of each other, which leaves a small opening to allow passage of air in between them. In another tube-and-fin design, the tube can be of a serpentine design, therefore eliminating the need for headers or manifolds, as the tube is bent back and forth in an “S” shape to create a similar effect. Typical applications of this type of heat exchanger, besides condensers, are evaporators, oil coolers, and heater cores. This tube-and-fin design is also utilized in radiators for automobiles. Outside of the automotive field, the tube and fin design is implemented by industrial oil coolers, compressor oil coolers, and in other similar applications requiring a higher efficiency heat exchanger.

In another effort to create a greater exchange of heat by increasing surface area, very thin flat tubes with intricate inner rib structures are utilized. This type of heat exchanger is similar to the tube-and-fin design, in that fins are combined with the flat tubes, but in this particular type of heat exchanger, the flat tubes contain intricate internal chambers formed by the inner rib structures. These inner rib structures help to increase the heat exchanging performance of the heat exchanger. To further improve heat transfer efficiency, the tube thickness is made thinner. As a result, the parts are lighter in weight, which in turn makes the overall heat exchanger lighter in weight. However, the pressure resistance is reduced, and the thinner tubes are more prone to damage. Also, the assembly process is complicated because of the fragile nature of the parts. In addition, the internal chambers are prone to plugging during the manufacturing process, particularly if a brazing process is utilized. The complexity of the extruding process potentially results in higher costs and higher defect rates. Also, by utilizing internal chambers within the flat tubes to help disperse heat, the overall cost for the heat exchanging system will be higher because a higher powered compressor may be necessary to move the heat exchanging medium through the smaller openings of the tubes. Conversely, if a higher powered compressor is not utilized, then additional tubes will be necessary to obtain the desired heat exchanging performance because the smaller tubes reduce the flow of the heat exchange media significantly. The additional tubes will increase the overall cost for the heat exchanging system. Currently, this type of heat exchanger is used in applications requiring high heat exchanging capabilities, such as automotive air conditioner condensers.

A variation on the tube-based heat exchanger involves stacking flat ribbed plates. When stacked upon each other, these ribbed plates create chambers for transferring heat exchanging media. In essence, this type of heat exchanger performs substantially the same function as tube-and-fin type heat exchangers, but is fabricated differently. This type of heat exchanger is commonly implemented by contemporary evaporators.

SUMMARY OF THE INVENTION

The present invention is an enhanced tube for heat exchanging applications including a flow tube and a chamber. The flow tube connects to the chamber. One end of the flow tube may connect to a header or a manifold. Heat exchange media flows from the header or the manifold into the flow tube. The heat exchange media then flows into the chamber. The heat exchange media then flows from the chamber into another flow tube, which is connected to another header or manifold.

In an embodiment of the present invention, the flow tube and the chamber for a heat exchanger are provided, for example, for a condenser, evaporator, radiator, etc. The heat exchanger may also be a heater core, intercooler, or an oil cooler for an automotive application (i.e., steering, transmission, engine, etc.) as well as for non-automotive applications. An advantage of the present invention is that the heat exchange media contact surface area for radiating heat is greater over a shorter distance than that of a conventional heat exchanger. Therefore, the efficiency of the heat exchanger is increased. Another advantage of the present invention is that the overall length and weight of the enhanced tube for heat exchanging applications may be less compared to a conventional heat exchanger, which in turn provides for a lower overall cost as less raw material and less packaging is necessary. Furthermore, the smaller footprint of the present invention lends itself to be used in applications where space is limited. Yet another advantage of the present invention over a conventional heat exchanger is that the manufacturing process may be simpler because the present invention requires less fragile components and less manufacturing steps. The entire unit may be brazed together, or any portion of the unit can be brazed first, and then additional components may be brazed or soldered together.

In another embodiment of the present invention, more than one chamber may be used, which will further increase the surface area of the enhanced tube for the heat exchanger. Also, a first chamber may be connected directly to another chamber.

In yet another embodiment of the present invention, the tube size may vary between the chambers, and if more than one chamber is used, the chamber size may vary from one chamber to the next.

In a further embodiment of the present invention, each chamber may disperse heat exchanging media throughout the chamber, which further enhances the heat exchanging capabilities of the present invention. Also, each chamber may also mix heat exchanging media.

In yet a further embodiment of the present invention, each chamber may include a medium directing member and medium redirection members that direct and redirect heat exchanging media in a particular directions through the chamber.

In another embodiment of the present invention, the inner surface of the tube may feature indentations to increase the surface area. Also, in yet another embodiment of the present invention, the inner surface of the chamber may also feature indentations to increase the surface area. In a further embodiment of the present invention, the redirection member may also feature indentations.

In other embodiments of the present invention, the tube and chamber combination may be repeated, and based on a particular application, there may be multiple tube and chamber assembly rows. Several of the tube and chamber units may be attached to a header or a manifold. There may be a plurality of tube and chamber units arranged in a row that are attached to a header or a manifold to enhance the overall performance of the heat exchanger.

In some embodiments, the chamber is of a greater diameter than the inlet and the outlet of the chamber. In other embodiments, the chamber is of a greater diameter than the inlet of the chamber, but may be the same diameter as the outlet. Alternatively, in yet other embodiments, the chamber may be of a greater diameter than the outlet of the chamber, but may be the same diameter as the inlet.

In yet some other embodiments, the chamber has at least one greater dimension than the tube. For instance, the chamber may have a greater fluid capacity, circumference, or surface area. The ratio of a particular dimension between the tube and the chamber may be 1:1.1; 1:1.5; or any other suitable ratio.

The tube and the chamber may be made of aluminum, either with cladding or without cladding. The tube and chamber may also be made of stainless steel, copper or other ferrous or non-ferrous materials. The tube and chamber may also be a plastic material or other composite materials.

The tube and chamber may be manufactured by stamping, cold forging, or machining The tube and chamber may be manufactured as one piece or may be manufactured as two separate pieces.

Other features and advantages of the present invention will be readily appreciated, as the same becomes better understood after reading the subsequent description taken in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a perspective view of a tube and a chamber illustrated in operational relationship with manifolds to provide heat exchanger according to embodiments of the present invention;

FIGS. 2A through 2B illustrate two embodiments of the present invention;

FIG. 2C is a perspective view of a tube and chamber with a medium-directing insert;

FIG. 3 is a view of a redirect chamber with redirection members;

FIGS. 4A through 4E illustrate various embodiments of the tube;

FIGS. 5A through 5D illustrate various embodiments of the redirect chamber;

FIGS. 6A and 6B are different views of the invention heat exchanger formed by stacked plates;

FIG. 7 is a cross-section of an embodiment of the invention surrounded by a compartment;

FIGS. 8A and 8B illustrate an embodiment of the invention illustrating a type of medium directing member;

FIGS. 9A and 9B illustrate another embodiment of the present invention;

FIGS. 10A and 10B illustrate yet another embodiment of the present invention;

FIGS. 11A and 11B illustrate a further embodiment of the present invention;

FIG. 12 illustrates another embodiment of the redirection chamber; and

FIGS. 13A and 13B illustrate an embodiment using unsecured redirection members in the redirection chamber;

FIG. 14A illustrates a perspective view of another embodiment of the present invention, showing an internal view of a disk member used to form the redirect chamber;

FIG. 14B illustrates another perspective view of the disk member, showing an external view of the disk member used to form the redirect chamber;

FIG. 14C illustrates an exploded view of the embodiment of the present invention, showing two disk members used to form the chamber, as well as a medium-directing insert positioned within the redirect chamber;

FIG. 14D illustrates a heat exchange medium flow pattern within the redirect chamber.

DETAILED DESCRIPTION

Referring to the drawings and in particular FIG. 1, an embodiment of a heat exchanger 100 is shown. The heat exchanger 100 includes a manifold 200 matingly engaged to free ends of tubes 10 that are brazed together to redirect chambers 20. As shown in FIG. 1, the redirect chambers 20 have a greater fluid capacity than the tubes 10. Heat exchange media 50 flows from the outlet 210 of the manifold 200 into the inlet 11 of the tube 10. The heat exchange medium 50 passes through the outlet 19 of the tube 10 into the inlet 21 of the redirect chamber 20. The heat exchange media 50 then flows out an outlet 29 of the redirect chamber 20. The process of going from a tube 10 to a redirect chamber 20 may repeat several times until the heat exchange media 50 is received by another manifold 202. There may also be several rows of the tube 10 and redirect chamber 20 combinations. Also, one embodiment may allow for just one tube 10 and one redirect chamber 20. Throughout the transport of the heat exchange media 50 through the heat exchanger 100, the heat from the heat exchange media 50 is transferred to the environment outside of the heat exchanger 100. Although not meant to be limiting, common heat exchange media known in the art includes various refrigerants (i.e., R-134A), carbon dioxide, butane, oils, gases (e.g., air), water, and mixtures of water and other coolants.

In another embodiment of the heat exchanger 100, the heat exchanger 100 may be used in a reversed method. Instead of the heat exchanger 100 being used in an environment where heat is transferred from the heat exchange media 50 to the surrounding environment of the heat exchanger 100, the heat exchanger 100 may be used to increase the temperature of the heat exchange media 50 flowing inside the present invention. For example, water of an ambient temperature may flow through the tube 10 and the chamber 20 of the heat exchanger 100, where the environment surrounding the heat exchanger 100 is of a higher temperature than that of the water. Continuing with this example, the heat from the environment surrounding the heat exchanger 100 is transferred to the water, thereby increasing the temperature of the water. An example of this embodiment, which is not intended to be limiting, would be a water heater.

Referring to FIG. 2A, the inside of tube 10 is hollow, which allows for the flowing of the heat exchange medium 50. The tube 10 is mated to the redirect chamber 20. The redirect chamber 20 houses a medium-directing insert 30. The medium-directing insert 30 is positioned within the intersecting space between the tube 10 and the redirect chamber 20. The heat exchanging medium 50 flows through the tube 10 until the heat exchanging medium 50 flows into contact with the medium-directing insert 30. The medium-directing insert 30 directs the heat exchanging medium 50 into the inside of the redirect chamber 20. According to the present embodiment, the heat exchange medium 50 disperses throughout the redirect chamber 20 and heat is transferred from the heat exchange medium 50 to the redirect chamber 20.

Referring to FIG. 3, an embodiment of the redirect chamber 20 is shown. Redirection members 28 are attached to the redirect chamber 20. In this embodiment, the redirection members 28 are attached to the inner wall of the redirect chamber 20. Although not meant to be limiting, in FIG. 3, the redirection members 28 are secured at an angle. In addition, other embodiments may secure the redirection members 28 perpendicularly to the inside of the redirect chamber 20, that is, the redirection members 28 are at 90 degree angles.

Referring to FIG. 2B, the inside of tube 10 is hollow, which allows for the flowing of a heat exchange medium 50. The tube 10 is mated to the redirect chamber 20. The redirect chamber 20 houses a medium-directing insert 30. The medium-directing insert 30 is fixed within the intersecting space between the tube 10 and the redirect chamber 20. The heat exchanging medium 50 flows through the tube 10 until the heat exchanging medium 50 flows into contact with the medium-directing insert 30. The medium-directing insert 30 directs the heat exchanging medium 50 into the inside of the redirect chamber 20. According to the embodiment in FIG. 2B, redirection members 28 direct the heat exchange medium 50 in a particular direction within the redirect chamber 20 and heat is transferred from the heat exchange medium 50 to the redirect chamber 20.

Referring to FIG. 2C, a perspective view of tube 10 and chamber 20 is shown. The inside of tube 10 is hollow, which allows for the flowing of the heat exchange medium 50, the flow direction is illustrated by the arrows. The tube 10 is mated to the redirect chamber 20. The redirect chamber 20 houses a medium-directing insert 30. The medium-directing insert 30 is fixed within the intersecting space between the tube 10 and the redirect chamber 20. The heat exchanging medium 50 flows through the tube 10 until the heat exchanging medium 50 flows into contact with the medium-directing insert 30. The medium-directing insert 30 directs the heat exchanging medium 50 into the inside of the redirect chamber 20. According to the present embodiment, the heat exchange medium 50 disperses throughout the redirect chamber 20 and heat is transferred from the heat exchange medium 50 to the redirect chamber 20.

Referring to FIG. 4A, the tube 10, in the illustrated embodiment, is hollow and circular. In another embodiment, as shown in FIG. 4B, the tube 10 is hollow and a non-circle shape. In yet another embodiment, as shown in FIG. 4C, ribs 18, which divide the area inside the tube 10 into smaller compartments for transferring the heat exchange media 50, are placed inside the tube 10 to increase heat exchange performance. FIG. 4D illustrates an embodiment of the tube 10 in which the tube wall 12 includes extensions 14. FIG. 4E illustrates a further embodiment of the tube 10 with tube fins 16 shrouding the outer surface of the tube 10.

Referring to FIG. 5A, redirect chamber 20, in the illustrated embodiment, is hollow and circular. In another embodiment, as shown in FIG. 5B, the redirect chamber 20 is hollow and a non-circular shape. FIG. 5C illustrates an embodiment of the redirect chamber 20 in which a chamber wall 22 includes extensions 24. FIG. 5D illustrates a further embodiment of the redirect chamber 20 with chamber fins 26 shrouding the outer surface of the redirect chamber 20. Although not meant to be limiting, the diameter of the inlet 21 of the redirect chamber 20 will be smaller than the overall diameter of the redirect chamber 20. Also, the diameter of the outlet 29 of the redirect chamber 20 will be smaller than the overall diameter of the redirect chamber 20.

The tube 10 embodiments shown in FIGS. 4A-4E may be mated in various combinations with the redirect chamber 20 embodiments shown in FIGS. 5A-5D. Additional tube fins 16 and chamber fins 26 or other materials can be attached to the outside surface of the tube 10 or the redirect chamber 20, and the additional material does not have to be attached for the full length of the tube 10. Tubes 10 and redirect chambers 20 near the inlet side of the invention may feature additional material. Other embodiments of the tubes and chambers not pictured may also be combined, and the invention is not limited to the embodiments described.

Referring to FIGS. 6A and 6B, another embodiment of a heat exchanger is shown. A plate 600 contains at least one hole 610 that goes through the thickness of the plate 600. On one side of the plate 600, and centered on the hole 610, a cavity 620, which is of a larger diameter than the diameter of the hole 610, is created in the plate 600 without going completely through the plate 600. One end of a medium-directing insert 30 is connected to an outer edge of the cavity 620, and the opposite end of the medium-directing insert 30 is connected to the inner edge of the cavity 620. When a plate 600a is stacked onto another plate 600b, and the respective holes 610 are aligned, the holes 610 create a tube-like segment and the cavities 620 create a chamber. Heat exchange media 50 may flow through the hole 610 into the cavity 620 where the heat exchange media 50 encounters the medium-directing insert 30 that redirects the heat exchange media 50 into the cavity 620, the flow direction is illustrated by the arrows.

Referring to FIG. 7, another embodiment of a heat exchanger is shown. A compartment 700 surrounds a tube and chamber combination 710. The compartment 700 has an inlet 701 and an outlet 702. The compartment 700 directs an air flow 750 around a tube and chamber combination 710 while a heat exchange medium 50 flows through the tube and chamber combination 710. According to this embodiment, the transfer of heat is further facilitated by the movement of the air flow 750 across the tube and chamber combination 710.

Referring to FIGS. 8A and 8B, one embodiment of the invention is shown. A chamber 20 is directly connected to another chamber 20, each of which house a medium directing member 30. In each chamber 20, the medium directing member 30 redirects heat exchange media 50 throughout the chamber 20. The arrows illustrate how the heat exchange media 50 may be redirected according to the embodiment as shown.

Referring to FIG. 9A, a cross-section of another embodiment of the invention is shown. A chamber 20 is connected to a tube 10 that is connected to another chamber 20. Each chamber 20 in the present embodiment houses a redirection member 28, which in this embodiment attaches to the inner surface of the chamber 20. The redirection member 28 allows passage of the heat exchange media through multiple holes 90 in the redirection member 28. The arrows illustrate how the heat exchange media 50 may be redirected according to the embodiment as shown. Referring to FIG. 9B, an embodiment of a redirection member 28 is shown. The redirection member 28 contains openings 90 that allow for the passage of heat exchange media 50.

Referring to FIG. 10A, a cross-section of yet another embodiment of the invention is shown. A chamber 20 is connected to a tube 10 that is connected to another chamber 20. Each chamber 20 in the present embodiment may house a medium directing member 30, which in this embodiment attaches at certain points to the inner surface of the chamber 20, which leaves openings 91 along the inner surface of the chamber 20. The medium directing member 30 allows passage of the heat exchange media 50 through these openings 91. The arrows illustrate how the heat exchange media 50 may be redirected according to the embodiment as shown. Referring to FIG. 1OB, an embodiment of a medium directing member 30 is shown. The openings 91 allow for the passage of heat exchange media 50.

Referring to FIG. 11A, a cross-section of yet another embodiment of the invention is shown. The tube 10 is mated to the redirect chamber 20. The redirect chamber 20 houses a medium-directing insert 30. The medium-directing insert 30 is fixed within the intersecting space between the tube 10 and the redirect chamber 20. A chamber 20 is connected to a tube 10 that is connected to another chamber 20. Each chamber 20 in the present embodiment have indentations 92 in the chamber walls. The arrows illustrate how the heat exchange media 50 may be directed according to the embodiment as shown. Referring to FIG. 11B, an embodiment of a wall of a chamber 20 is shown. The wall of the chamber 20 contains indentations 92 that redirect and mix the passage of heat exchange media 50 as it flows through the chamber 20.

Referring to FIG. 12, the redirect chamber 20, in combination with any of the above embodiments, does not have to be cylinder-shaped, other embodiments may be shaped like a cube (with various ratios of height, length, and width dimensions), or other geometric shapes.

FIGS. 13A and 13B illustrate an embodiment of the invention where the redirection members 28 are not secured to an inside surface of the chamber 20. The arrows illustrate how the heat exchange media 50 may be directed according to the embodiment as shown. By way of example, the redirection members 28 could be a ball bearing or combination of multiple ball bearings that participate in a mixing and churning process within the chamber 20, as shown by the arrows in FIG. 13, which aids in the heat exchange process. The, invention is not limited to using ball bearings in the chamber, as other unsecured redirection members may be used alone or in combination with one another for achieving greater heat exchange efficiency, such as a redirection member that is moved into a particular position by contact from heat exchange media.

In an embodiment of the present invention, the redirect chamber 20 may be formed by mating two disk members 400 and 410. Referring to FIG. 14C, an exploded view of the redirect chamber 20 is shown. The inside of an input tube 10 (not shown) is hollow, which allows for the flow of the heat exchange medium 50. The tube 10 is mated to the redirect chamber 20, connected over an orifice member 221 on a disk member 400, forming a fluid connection. The redirect chamber houses a medium-directing insert 30. The medium directing insert 30 is positioned within the redirect chamber 20, guiding the flow of heat exchange medium 50 from the tube, then into the interior of the redirect chamber 20, then out of the chamber. In an embodiment of the present invention, within the redirect chamber 20, the medium-directing insert 30 along with a first medium directing channel 415, guides the flow of heat exchange medium 50 from a first flow direction (defined by the tube 10) to a second flow direction within the redirect chamber, dispersing heat exchange medium 50 within the redirect chamber. Preferrably, within the chamber there are two distinct flow patterns, each of which traverses a generally semi-circular route. Within the redirect chamber 20, a plurality of protrusion members 405 on one or both of the lateral walls of the redirect chamber 20 causes the flow of heat exchange medium to become turbulent (see FIGS. 14A and 14B). The heat exchange medium 50 that has been introduced into the redirect chamber 20, then flows out an outlet orifice 229, led out to the outlet by the medium directing insert 30 along with a second medium directing channel 420. An output tube 10 (not shown) is connected over the outlet orifice 229 on the disk member 410, forming a fluid connection. FIG. 14D illustrates a general flow pattern of heat exchange medium 50 within the redirect chamber 20, the arrows illustrating a representative flow pattern of the heat exchange medium 50.

FIGS. 14A and 14 B illustrate respectively interior and exterior views of the disks member 400. The protrusion members 405 populate the lateral wall of the chamber. The plurality of protrusion members 405 may be formed by stamping the respective disk members, or they may be placed within the redirect chamber as separate components. Furthermore, the plurality of protrusion members may be a combination of stamped shapes on the respective disk members along with protrusion members placed within the redirect chamber.

The chamber generally has at least one greater dimension than the tube. For instance, the chamber may have a greater fluid capacity, circumference, or surface area. The ratio of a particular dimension between the tube and the chamber may be 1:1.1, 1:1.5, or any other ratio.

The tube and the chamber may be made of aluminum, either with cladding or without cladding. The tube and chamber may also be made of stainless steel, copper or other ferrous or non-ferrous material. The tube and chamber may also be a plastic material or other composite materials. Likewise, the redirect member may be made of aluminum, either with cladding or without cladding. The redirect member may also be made of stainless steel, copper or other ferrous or non-ferrous materials. The redirect member may also be a plastic material or other composite materials. Also, an embodiment of the present invention allows for the tube to be made of a different material than the material used for the chamber, and the redirect members may be made of a different material than the material used for the chamber and tube. If more than one redirect member is used in an embodiment of the invention, one redirect member may be made of a different material than another redirect member. The redirect members may also be of different shapes than one another. Also, in embodiments that use more than one redirect member, one or more of the redirect members may be secured to the inside wall of the chamber and the other redirect members may be free to move around inside the redirect chamber.

The tube and chamber may be manufactured by stamping, cold forging, or machining The tube and chamber may be manufactured as one piece or may be manufactured as two—separate pieces.

The present invention has been described in an illustrative manner. The term “redirect” means to change the direction or course of, or impede the progress of, the heat exchange media, even if by the smallest difference in angle or velocity. It is to be understood that the terminology which has been used is intended to be in the nature of words of description rather than of limitation.

Many modifications and variations of the present invention are possible in light of the above teachings. Therefore, within the scope of the appended claims, the present invention may be practiced other than as specifically described.

Claims

1. A heat exchanger having a plurality of chambers, at least one of the chambers comprising: an inlet for receiving a heat exchange medium flowing in a first flow direction in an initial line of flow;a plurality of walls defining a chamber interior which is in fluid communication with the inlet, at least one of the walls having a plurality of protrusion members extending toward at least another one of the walls, the protrusion members arranged around a center axis of the chamber;a medium directing member, having an inclined surface facing the inlet, the medium directing member diverting flow of the medium from the initial line of flow to a second flow direction which is generally perpendicular to the first flow direction; andan outlet in fluid communication with the chamber interior for outputting the medium, whereinthe chamber is configured to cause the medium to flow within the chamber interior in at least one generally semi-circular flow path which travels at least partially around a line segment extending from the inlet in the first flow direction and lies in the plane generally perpendicular to the first flow direction, andthe protrusion members lie within the at least one generally semi-circular flow path to facilitate a turbulent flow pattern for the heat exchange medium.

2. The heat exchanger according to claim 1, wherein the chamber is configured to cause the medium to flow within the chamber interior in opposing first and second generally semi-circular flow paths, each of which travels at least partially around the line segment and lies in the plane generally perpendicular to the first flow direction and wherein the protrusion members lie within each of the first and second generally semi-circular flow paths.

3. The heat exchanger according to claim 2, wherein the medium directing member has a declined surface facing the outlet and the chamber is configured to cause the medium, at the termination of each of the first and second semi-circular flow paths, into contact with the declined surface to divert the medium from the second flow direction through the outlet in the first flow direction.

4. The heat exchanger according to claim 1, wherein the at least one chamber is realized by a plate, the chamber interior being formed by a cavity within the plate and the inlet being formed by a hole in the plate, the cavity being centered on the hole and having a diameter larger than a diameter of the hole.

5. The heat exchanger according to claim 4, wherein a single plate is used to form a plurality of the chambers.

6. The heat exchanger according to claim 1, further including first and second manifolds between which the at least one chamber is disposed.

7. A heat exchange chamber having a plurality of chambers, at least one of the chambers comprising: an inlet for receiving a heat exchange medium flowing in a first flow direction in an initial line of flow;a plurality of walls defining a chamber interior which is in fluid communication with the inlet, at least one of the walls having first and second medium directing channels formed therein, the first and second medium directing channels being disposed on opposite sides of a line segment extending from the inlet in the first flow direction;an outlet in fluid communication with the chamber interior; anda medium directing member having an inclined surface facing the inlet and a declined surface facing the outlet, the medium directing member diverting flow of the medium from the initial line of flow to a second flow direction which is generally perpendicular to the first flow direction, whereinthe first and second medium directing channels and the medium directing member are arranged such that the heat exchange medium is directed to flow in two distinct flow paths, each of which is from the inlet, through the first medium directing channel, through a portion of the chamber interior, through the second medium directing channel and into the outlet.

8. The heat exchanger according to claim 7, wherein the two distinct flow paths are oppositing first and second generally semi-circular flow paths, each of which travels at least partially around the line segment extending from the inlet and lies in a plane generally perpendicular to the first flow direction.

9. The heat exchanger according to claim 7, wherein the at least one chamber is realized by a plate, the chamber interior being formed by a cavity within the plate and the inlet being formed by a hole in the plate, the cavity being centered on the hole and having a diameter larger than a diameter of the hole.

10. The heat exchanger according to claim 9, wherein a single plate is used to form a plurality of the chambers.

11. The heat exchanger according to claim 7, further including first and second manifolds between which the at least one chamber is disposed.

12. A heat exchanger having a plurality of chambers, at least one of the chambers comprising: an inlet for receiving a heat exchange medium flowing in a first flow direction in an initial line of flow;a plurality of walls defining a chamber interior which is in fluid communication with the inlet, at least one of the walls having a plurality of protrusion members extending toward at least another one of the walls, the protrusion members arranged around a line segment extending from the inlet in the first flow direction, at least one of the walls having first and second medium directing channels formed therein, the first and second medium directing channels being disposed on opposite sides of the line segment;an outlet in fluid communication with the chamber interior; anda medium directing member having an inclined surface facing the inlet and a declined surface facing the outlet, the medium directing member diverting flow of the medium from the initial line of flow to a second flow direction which is generally perpendicular to the first flow direction, whereinthe first and second medium directing channels and the medium directing member are arranged such that the heat exchange medium is directed to flow in opposing first and second generally semi-circular flow paths from the inlet, through the first medium directing channel, through a portion of the chamber interior, through the second medium directing channel and into the outlet, each of the first and second generally semi-circular flow paths traveling at least partially around the line segment and lying in a plane generally perpendicular to the first flow direction, andthe protrusion members lie within the generally semi-circular flow paths to facilitate a turbulent flow pattern for the heat exchange medium.

13. The heat exchanger according to claim 12, wherein the at least one wall having the protrusion members and the at least one wall having the first and second medium directing channels are the same wall.

14. The heat exchanger according to claim 12, wherein the at least one chamber is realized by a plate, the chamber interior being formed by a cavity within the plate and the inlet being formed by a hole in the plate, the cavity being centered on the hole and having a diameter larger than a diameter of the hole.

15. The heat exchanger according to claim 14, wherein a single plate is used to form a plurality of the chambers.

16. The heat exchanger according to claim 12, further including first and second manifolds between which the at least one chamber is disposed.