To improve the overall efficiency of a gas turbine engine, a heat exchanger or recuperator can be used to provide heated air for the turbine intake. The heat exchanger operates to transfer heat from the hot exhaust of the turbine engine to the compressed air being drawn into the turbine. As such, the turbine saves fuel it would otherwise expend raising the temperature of the intake air to the combustion temperature.
The heat of the exhaust is transferred by ducting the hot exhaust gases past the cooler intake air. Typically, the exhaust gas and the intake air ducting share multiple common walls, or other structures, which allow the heat to transfer between the two gases (or fluids depending on the specific application). That is, as the exhaust gases pass through the ducts, they heat the common walls, which in turn heat the intake air passing on the other side of the walls. Generally, the greater the surface areas of the common walls, the more heat which will transfer between the exhaust and the intake air. Also, the more heat which is transferred between the exhaust and the air, the greater the efficiency of the heat exchanger.
As shown in the cross-sectional view of
Typically, during construction of such a heat exchanger 5, the plates 22 are positioned on top of one another and then compressed to form the stack 26. Since the plates 22 can separate if not held together, the compression of the plates 22 ensures that there are always positive compressive forces on the core 20 to hold the plates 22 in place.
Applying a high pre-load to the stack 26 reduces the potential for separation of the plates 22. However, to be able to apply pre-loads to the stack 26, a pre-load assembly or support structure 50 positioned about the stack 26, is needed. In addition to applying the pre-load to the stack 26, the support structure 50 carries any additional loading exerted by the stack 26. Such additional loads can come from a variety of sources, including thermal expansion of the stack 26 and the pressurization of air (or other medium) in the stack 26.
The support structure 50 collectively includes strongbacks 40, tie rods 30, and the shell 10. The tie rods 30 are held to the strongbacks 40 by fasteners 36 positioned at the ends 32 of the tie rods 30. Because the support structure 50 supports the core 20 (namely the stack 26) and is not a heat transfer medium, the components of the support structure 50 are made of much thicker materials than those of the core 20. Unfortunately, these thicker materials cause the support structure 50 to thermally expand at a much slower rate than the quick responding core 20, with its thin plates 22. The thickness (and thus the thermal response) of the support structure 50 will also be affected by the amount of the pre-load applied to the core 20.
Differential expansion or contraction between the core 20 and the support structure 50 can result from a variety of sources, including differential thermal expansion rates and air (or fluid) pressure variations. Differential expansion or contraction between elements of the heat exchanger 5 can occur in any dimension, and typically in all dimensions at the same time. That is, not only will the core 20 expand or contract along its length, LA1, quicker than the support structure 50 will, but it also deforms faster along its width, WA1, and depth (not show).
As can be seen in
Approaches to preventing damage from lateral expansion of the core 20 have included attempts to restrain the expansion and/or contraction of the core by application of additional compressive forces. However, such expansion/contraction restraining has resulted in the core and the support structure being put under excessive loading. This loading can result in high stresses and thermal damage or failure to both the core and the support structure. Such thermal damage includes creep and/or buckling of the associated structures.
While the structures of the heat exchanger can be enlarged to carry greater loads, doing so results in certain disadvantages. These disadvantages include: a lowering of the heat transfer characteristics of the core, an increase in the differential expansion/contraction between the core and the support structure, and an increase in the cost and weight of the heat exchanger.
One approach to accommodate the width-wise differential thermal expansion and contraction has been to use an inlet bellows 60 and an outlet bellows 70, as shown in
This prevents stresses from being placed on the tubes 23 and 29, as well as on the core 20.
One problem with the use of the bellows is that the outlet bellows 70 is very expensive and difficult to manufacture. This is because the outlet bellows 70 must be able function under the extreme temperatures associated with the outlet side of the core 20. Typically, these temperatures are very close to, or the same as, the temperature of exhaust gases, which enter the core 20 just after exiting from the attached turbine engine (not shown). Materials which can withstand these temperatures and continue to be sufficiently flexible over time are very expensive and difficult to use in fabricating the outlet bellows 70.
An additional problem with using a bellows system such as that shown in
Therefore, a need exists for a heat exchanger which accommodates differential expansion or contraction between the core and the supporting structure, such that the airflow through the core is not significantly disrupted. The heat exchanger must be configured to prevent failures or damage caused by buckling, creep or any other similar source. Further, the heat exchanger should be relatively simple in construction and operation to minimize its cost, weight and complexity.
The present invention provides a heat exchanger which in at least some embodiments includes a core, a support structure and a mount. The core is variable in its size and has a first port and a second port. The mount is positioned between the core and the support structure, adjacent to the second port of the core. The mount restrains the core relative to the support structure, such that when the core varies in size it does so either away from or towards the mount.
The heat exchanger can also include a deformable or flexible connector (e.g. bellows). This connector is attached to the core in a manner which allows it and the first port of the core to remain in fluid communication as the core varies in size. In this manner, the heat exchanger can remain attached to a substantially fixed structure (e.g. external ducting), while the core expands and contracts. The connector can be a bellows, a flexible high temperature hose or the like.
The mount includes a pin and a receiver. The receiver receives the pin so as to restrain the movement of the core. The arrangement of the mount varies by embodiments of the invention. For example, the pin can be attached to the support structure and the receiver is defined in the core. Another embodiment has the pin attached to the core and receiver is defined in the support structure. In yet another embodiment, the mount has a core receiver, a support structure receiver and a pin. In turn, the pin has a first end and an opposing second end, with the core receiver receiving the first end and the support structure receiver receiving the second end. The core receiver is defined in the core and the support structure receiver is defined in the support structure.
In some embodiments of the present invention, a lower temperature fluid (e.g. air) passes through the first port of the core and a higher-temperature fluid (e.g. air) passes through the second port of the core. In this manner, the connector carries a lower temperature fluid and the mount is positioned adjacent the second port, which channels a high temperature fluid. As such, the connector needs only to be fabricated to carry lower temperature fluids and a minimum amount of core expansion will occur at the second port. The connector can be flexible to accommodate the expansion and contraction of the core and remain in fluid communication with the first port and any attached external fluid transport means (e.g. ducting).
In other embodiments, the heat exchanger includes a laterally expandable core, a support structure, a mount and a bellows. Being expandable, the core is variable in its size. The core has a lower temperature fluid port and a higher temperature fluid port. The mount is positioned between the core and the support structure, adjacent the higher temperature fluid port. The mount functions to restrain the core, such that the core varies in size laterally away from and towards the mount. The bellows is attached at the lower temperature fluid port. This is done so that the bellows, the lower temperature fluid port and any external ducting (e.g. tube), are in constant fluid communication as the core varies in size.
a and b are perspective views of cross-sections of a heat exchanger and a portion of a heat exchanger.
a and b are isometric views of a turbine/heat exchanger system in accordance with the present invention.
a and b are perspective views of cross-sections of a portion of a heat exchanger in accordance with the present invention.
The present invention is embodied in an apparatus which provides several advantages over prior devices. One such advantage is that the invention allows differential expansion or contraction between the core and the support structure without structural damage. Another advantage is that the airflow to, or from, the core is kept substantially unrestricted during the expansion and contraction of the core.
In at least some embodiments of the invention, the core is secured to the support structure at a single location and is allowed to expand out from the location and contract in towards it. It is preferred that the securing location is set near (e.g. adjacent) the core's higher temperature fluid port. The core can be secured to the support structure by a pin and receiver apparatus. A flexible connector is used to maintain fluid flow through the core during the core's expansion and contraction. It is preferred that this connector (e.g. bellows, flexible hose, etc.) is positioned at the core's lower temperature fluid port. This allows the connector to be designed and fabricated to transport only lower temperature fluids, reducing cost and complexity of the connector.
With the core held in place near the higher temperature fluid port, the rest of the core is free to expand and contract. As such, the lower temperature fluid port and the flexible connector move with the expansion and contraction of the core. While the flexible connector moves, it functions to maintains a substantially unrestricted fluid passage way between the core and any external structure (e.g. ducting) attached thereto.
Another advantage of the present invention is that, by allowing relatively free differential expansion and contraction of the core, it prevents damage which would otherwise occur by restricting the movement of the structures. This damage potentially would occur from a variety of sources including buckling, fatigue, creep or the like. Preventing such damage results in an increased life span of the heat exchanger and reduces the amount of supporting structure needed.
Still another advantage of the present invention is that the overall cost and complexity of the heat exchanger is reduced. This reduction is due to, among other things, the simplicity of construction, reduction in the structural elements and reduced material costs. For example, with the core secured at or near the core's higher temperature fluid port, a direct connection can be made from this port to any external structure (e.g. ducting), eliminating the need for a flexible connector at this location. Since a flexible connector at the higher temperature port must be able to withstand the extreme heat, while remaining sufficiently flexible, it must be made of relatively expensive materials. As such, the overall cost of the heat exchanger can be reduced. Further, eliminating this high temperature flexible output connector reduces the complexity of the heat exchanger, which in turn eases the assembly.
Heat exchanger apparatuses which provide for differential thermal expansion are set forth in U.S. patent application (Number to be assigned) filed on Feb. 5, 2002, entitled HEAT EXCHANGER HAVING VARIABLE THICKNESS TIE RODS AND METHODS OF FABRICATION THEREOF, by David Beddome, Steve Ayres and Yuhung Edward Yeh, which is hereby incorporated by reference in its entirety, U.S. patent application (Number to be assigned), filed Dec. 21, 2001, entitled HEAT EXCHANGER WITH BIASED AND EXPANDABLE CORE SUPPORT STRUCTURE, by David Beddome, Steve Ayres and Yuhung Edward Yeh, which is hereby incorporated by reference in its entirety, U.S. patent application Ser. No. 09/652,949, filed on Aug. 31, 2000, entitled HEAT EXCHANGER WITH BYPASS SEAL ALLOWING DIFFERENTIAL THERMAL EXPANSION, by Yuhung Edward Yeh, Steve Ayres and David Beddome, which is hereby incorporated by reference in its entirety, and U.S. patent application Ser. No. 09/864,581, filed on May 24, 2001, entitled HEAT EXCHANGER WITH MANIFOLD TUBES FOR STIFFENING AND LOAD BEARING, by David W. Beddome, Steve Ayres, Yuhung Edward Yeh, Ahmed Hammoud, David Bridgnell and Brian Comiskey, which is hereby incorporated by reference in its entirety.
As shown in
While
b (
For some embodiments of the present invention, as shown in the cut-away views of
The core 110a is positioned within the shell 160a. The core 110a functions to duct the inlet air pass the exhaust gas, so that the heat of the exhaust gas can be transferred to the cooler inlet air. The core 110a performs this function while keeping the inlet air separated from the exhaust gas, such that there is no mixing of the air and the gas. By moving air near the gas without mixing the two, the heat exchanger 100 transfers heat at a high level of efficiency. Further, the heat exchanger 100 also maximizes engine performance by not allowing the exhaust gases to be introduced into the intake air of the turbine (or other engine).
As shown in
While the heat exchanger 100 is operating, the core 110a has a variable size (e.g. length and width) caused by thermal expansion or contraction. That is, as the core 110a is heated up by the exhaust gases passing through the shell, the core 110a will expand and as the heat exchanger 100 stops operating the core 110a will contract as it cools.
The heat exchange region 122 can be any of a variety of configurations that allow heat to transfer from the exhaust gas to the inlet air, while keeping the gases separate. However, it is preferred that the heat exchange region 122 is a prime surface heat exchanger having a series of layered plates 128, which form a stack 130. The plates 128 are arranged to define heat exchange members or layers 132 and 136 which alternate from ducting air, in the air layers 132, to ducting exhaust gases, in the exhaust layers 136. These layers typically alternate in the core 110a (e.g. air layer 132, gas layer 136, air layer 132, gas layer 136, etc.). Separating each layer 132 and 136 is a plate 128.
On either end of the stack 130 are a first end plate 142a and a second end plate 144. The first end plate 142a is positioned against the upper portion of the shell assembly 160a and the second end plate 144 is positioned against the lower portion of the shell assembly 160a.
Also shown in
On the outside of the shell 160a and above and below the core 110a, are the upper strongback 143a and the lower strongback 145. The tie rods 150 and the strongbacks 143a and 145 (as well as the shell 160) carry compressive loads applied to the stack 130. These compressive loads can be from a variety of sources including pre-loading, differential thermal expansion, air pressure, and the like.
The upper strongback 143a, the lower strongback 145, the tie rods 150, and the shell 160a, together form the support structure 170a. The support structure 170a functions to apply the compressive force to the stack 130 of the core 110a. In contrast to the tie rods 150, the upper strongback 143a and the lower strongback 145 are generally not deformable.
As can be seen, the plates 128 are generally aligned with the flow of the exhaust gas through the shell assembly 160a. The plates 128 can be made of any well known suitable material, such as steel, stainless steel or aluminum, with the specific material dependent on the operating temperatures and conditions of the particular use. The plates 128 are stacked and connected (e.g. welded or brazed) together in an arrangement such that the air layers 132 are closed at their ends 134. With the air layers 132 closed at ends 134, the core 110a retains the air as it passes through the core 110a. The air layers 132 are, however, open at air layer intakes 124 and air layer outputs 126. As shown in
In contrast to the air layers 132, the gas layers 136 of the stack 130 are open on each end 138 to allow exhaust gases to flow through the core 110a. Further, the gas layers 136 have closed or sealed regions 140 located where the layers 136 meet both the inlet manifold 116 and the outlet manifold 120. These closed regions 140 prevent air, from either the inlet manifold 116 or the outlet manifold 120, from leaking out of the core 110a into the gas layers 136. Also, the closed regions keep the exhaust gases from mixing with the air.
Therefore, as shown in
With the stack 130 arranged as shown in
As the plates 128 and the connected structure of the core 110a heat up, they expand. This results in an expansion of the entire stack 130 and thus of the core 110a. As noted in detail below, the inlet bellows 180a and the mount or restraining apparatus 200a are configured to allow the core 110a to thermally expand separately from the support structure 170a. In this manner, the core 110a can expand and contract laterally without the build-up of excessive forces between the core 110a and the support structure 170a and without the use of a bellows at the air outlet port 118 of the core 110a. This saves the core 110a from being damaged by forces which would otherwise be created by affixing the core 110a in place. Also, it reduces the cost of the heat exchanger 100 by eliminating the need for an expensive outlet bellows.
Although the core 110a can be arranged to allow the air to flow through it in any of a variety of ways, it is preferred that the air is channeled so that it generally flows in a direction opposite, or counter, to that of the flow of the exhaust gas in the gas layers 136 (as shown in the cross-section of FIG. 4). With the air flowing in an opposite direction to the direction of the flow of the exhaust gas, it has been found by the Applicants that the efficiency of the heat exchanger is significantly increased as compared to other flow configurations. As noted in detail below, some embodiments of the present invention have the core functioning to cool hot fluid entering the core inlet with a cooler fluid being direct through the shell.
The arrangement of the core 110a can be any of a variety of alternate configurations. For example, the air layers 132 and gas layers 136 do not have to be in alternating layers, instead they can be in any arrangement which allows for the exchange of heat between the two layers. For example, the air layers 132 can be defined by a series of tubes or ducts running between the inlet manifold 116 and the outlet manifold 120. While the gas layers 136 are defined by the space outside of, or about, these tubes or ducts.
To facilitate heat transfer, the core 110a can also include secondary surfaces such as fins or thin plates connected to the inlet air side of the plates 128 and/or to the exhaust gas side of the plates 128.
The core 110a and shell 160a can carry various gases, other than, or in addition to, those mentioned above. Also, the core 100a and shell 160a can carry any of a variety of fluids.
As shown in
The openings 164 of shell 160a are positioned through the upper panel 166a. The shell assembly 160a can be made of any suitable well known material including, but not limited to, steel and aluminum. Preferably, the shell 160a is a stainless steel.
The construction of the shell assembly 160a can vary depending on the particular embodiment of the present invention. In some embodiments the shell 160a is constructed to carry some of the compressive load generated by the support structure 170a and applied to the core 110a. The shell 160a can also be configured to carry other internally created loads (e.g. air pressure loads) and externally exerted loads (e.g. inertia loads or vibration loads). Because in some embodiments of the present invention, the walls 162, upper panel 166a and lower panel 168 of the shell 160a are thick relative to the thin core plates 128, the shell 160a will thermally expand at a slower rate than the core 110a. This can result in differential thermal expansion or contraction between the shell 160a and the core 110a, as the two are either heated or cooled, as the case may be. To avoid, or to minimize, gaps or spaces forming between the core 110a and the shell 160a during differential expansion, the shell 160a is flexible enough to be deformed by the forces applied by the strongbacks 143a and 145 and the tie rods 150.
In other embodiments, the structure of the shell 160a is relatively thin. In such embodiments, the compressive loads created by the support structure 170a are primarily carried by the strongbacks 143a and 145 and the tie rods 150. In such embodiments, because the shell 160a is thinner, the shell 160a, thermally expands and contracts much quicker. This allows any differential thermal expansion between the shell 160a and the core 110a to be minimized. Which, in turn, aids in preventing gaps from forming between the core 110a and the shell 160a. This thinner structure also increases the shell's flexibility and allows the shell 160a to be more easily deformed by the strongbacks 143a and 145 and the tie rods 150. As such, in these embodiments, the potential for exhaust gases being able to pass around the core 110a, through gaps between the core 110a and the shell 160a, is further reduced.
The present invention, however, provides for differential thermal expansion between the structures of the heat exchanger 100 by employing the inlet bellows 180a and the mount 200a to allow the core 110a to thermally expand separately from the support structure 170a, while maintaining a substantially unrestricted airflow through the core 110a. As shown herein, a variety of embodiments of the support structure and tie rods exist.
As shown in
This embodiment is achieved by using the deformable connector, flexible bellows or hose 180a positioned between the air inlet port 114 and any external air ducting (e.g. the air inlet). A direct, substantially rigid or fixed outlet connector 190a is set between the air outlet port 118 and any external ducting (e.g. the air outlet).
With the core 110a fixed in place by the mount 200a near air outlet port 118 and the outlet connector 190a, the core 110a will have little or no movement at the outlet connector 190a during the differential thermal expansion or contraction of the core 110a. All the lateral expansion and contraction of the core 110a occurs out away from the mount 200a, and thus, out from the connector 190a (being positioned in close proximity to the mount 200a).
As such, the outlet connector 190a can be fixed and does not have to deform (at least not in any significant manner) to accommodate the differential expansion or contraction of the core 110a. That is, as shown in
It should be noted that since the mount 200a is slightly offset from the connector 190a that in some embodiments of the present invention the connector 190a may be subject to some relatively minor lateral deformation. It is preferred that the connector 190a be sufficiently laterally deformable to accept any such differential expansion. As such, a bellows is not needed between the air outlet port 118 the air outlet duct.
By not needing to use an outlet bellows, the present invention reduces the cost and complexity of the heat exchanger 100. A bellows set between the manifold 120 and the outlet 118 would have to remain sufficiently flexible at the higher temperatures found at the core's outlet. Such bellows are significantly more expensive and complex than a straight connector, such as the outlet connector 190a.
Of course, because the air inlet port 114 is positioned much further away from the mount 200a than the air outlet port 118, the lateral movement of the core 110a is much greater at the air inlet port 114 than at the air outlet port 118. To maintain a sealed and generally clear path for the inlet air, the inlet bellows 180a is positioned between the air inlet port 114 and the air inlet duct, as shown in
As shown in
The inlet bellows 180a can be any of a variety of materials including steel and aluminum, however it is preferred that stainless steel is used. In place of a bellows a flexible high temperature hose or a braided (e.g. woven) metal hose can be used.
The bellows 180a can be any of a variety of shapes and dimensions, however, it is preferred that the bellows 180a have a round shape to match that of the preferred tube shapes of the air inlet port 114 and air inlet tube. The length of the bellows 180a can vary, but is preferably dependent on the maximum differential expansion and/or contraction of the core 110a. The greater the overall difference between the lateral dimensions of the core 110a and the support structure 170a, the greater length of the bellows 180a will be.
As the core 110a expands or contracts, the inlet manifold 116 moves laterally to one side or the other, relative to the support structure 170a, as shown in
In contrast,
In either the case of the differential expansion or contraction of core 110a, the inlet bellows 180a maintains a seal with the inlet manifold tube 115 and with air inlet duct. As can be seen, with either the core's expansion or contraction, the bellows 180a maintains a clear pathway for the passage of air into the core 110a.
As can be seen in
Of course, the mount 200a can be positioned at any of a variety of locations about the connector 190a other than that shown in
As shown in
a and b and 7 show that the pin 202a is positioned in the receiver 206a, such that the pin 202a restrains movement of the core 110a relative to the support structure 170a at the mount 200a. As the core 110a begins to displace laterally, the sides 204a of the pin 202a contact the sides 208a of the receiver 206a to prevent the core 110a from moving. However, since the remainder of the core 110a can move laterally substantially freely (with the first end plate 142a moving adjacent to the upper panel 166a of the shell 160), the core 110a will expand out from the mount 200a and contract towards it. As such, the expansion and/or contraction at the connector 190a will be much less than that at the bellows 180a.
The pin 202a can be any of a variety of materials including steel and aluminum but it is preferred that stainless steel is used. The pin 202a preferably has a cylindrical shape, of course other shapes are possible as well.
The pin 202a is secured to the upper strongback 143a and for additional strength can also be secured to the shell 160a. In some embodiments, the pin 202a is attached to the shell 160a and/or the upper strongback 143a by welding, brazing, adhesives or any similar method. In other embodiments, the pin 202a can be a formed part of either the strongback 143a (as shown in
The dimensions of the pin 202a are variable, depending on the specific use in which it is employed and material used. The dimensions of the pin can be determined by one skilled in the art using well known analytical and/or empirical methods.
The receiver 206a can be created by forming, drilling and/or any other similar well known method. The receiver 206a is sized to closely receive the pin 202a. This prevents lateral movement of the core 110a at the mount 200a.
The mount 200a, including the pin 202a and the receiver 206a must be strong enough to carry the loads generated by the differential thermal expansion and/or contraction of the core 110a, without any significant damage to the mount 200a. The mount 200a needs to be able to carry such loads over repeated cycles of differential expansion and contraction of the core 110a.
Certain embodiments of the present invention use more than one mount 200a to secure the core 110a. It is preferred that such embodiments have the mounts 200a positioned close enough to each other to prevent damage from differential expansion and/or contraction of the core 110a. In certain embodiments the multiple mounts 200a are positioned about the outlet manifold 120 so as to minimize or prevent lateral movement of the core 110a at the connector 190a.
In some embodiments of the present invention, the mount has a reverse arrangement.
As shown, in
In other embodiments, a mount 200c includes a pin 202c, a core receiver 206c and a support structure receiver 207c, as shown in
As shown in
In still other embodiments of the present invention, the core 110e and the support structure 170e are attached in a fixed manner to one another. As shown in
In some embodiments of the present invention a bellows 180f is positioned between the core 110f and the support structure 170f, as shown in
In other embodiments of the present invention a higher temperature fluid enters the core at the inlet, is cooled in the core and exits at the outlet at a lower temperature. Also, a separate lower temperature fluid enters the inlet of the shell, is heated as it passes through the core and exits the shell at the outlet at a higher temperature. In such embodiments the core functions to reduce the temperature of the fluid passing through it. In these embodiments the mount (e.g. mounts 200a-f) is positioned adjacent the input to the core and the flexible connector (e.g. bellows 180a-f) is positioned at the output of the core. In this manner, the core has a minimum amount (if any) of differential expansion or contraction near the higher temperature fluid port of the core. This eliminates the need for an expensive and complex flexible connector to be employed at the higher temperature fluid port to carry the high temperature fluid. Also, with the flexible connector positioned at the lower temperature fluid port of the core, the flexible connector can be constructed to carry lower temperature fluid. This reduces the cost and complexity of the heat exchanger.
While the preferred embodiments of the present invention have been described in detail above, many changes to these embodiments may be made without departing from the true scope and teachings of the present invention. The present invention, therefore, is limited only as claimed below and the equivalents thereof.
Number | Name | Date | Kind |
---|---|---|---|
3968834 | Mangus et al. | Jul 1976 | A |
3996997 | Regan et al. | Dec 1976 | A |
4134449 | La Haye et al. | Jan 1979 | A |
4328860 | Hoffmuller | May 1982 | A |
4511106 | Graves | Apr 1985 | A |
5114588 | Greene | May 1992 | A |
6119766 | Blomgren | Sep 2000 | A |
6283199 | Nakamura et al. | Sep 2001 | B1 |
6703154 | Gorbell et al. | Mar 2004 | B1 |
Number | Date | Country | |
---|---|---|---|
20030159807 A1 | Aug 2003 | US |