This invention relates to heat exchangers, and more particularly to improved turbulators for heat exchangers.
For many years, various types of turbulators have been employed in the flow channels for one or more heat exchange fluids in a heat exchanger. The turbulators induce turbulence in the flow of the heat exchange fluid through the channel and as is well known, the resulting increased turbulence increases the heat exchange coefficient, which, in turn, increases the rate of heat transfer.
Turbulators come in many shapes and forms. In some cases, the turbulators are manufactured as elements separate from other constituents of the heat exchanger and are placed in a fluid flow channel at the time of assembly of the heat exchanger with which they are to be used. In other cases, turbulators are formed in the walls that define a flow channel. This type of turbulator is frequently found in so-called plate heat exchangers, drawn cup heat exchangers, and in heat exchangers utilizing so-called flattened tubes. In each of these types of heat exchangers, two or more generally parallel walls of high thermal conductivity, along with other constituents, define one or more channels. Dimple-like turbulator structures are formed in one or both of the walls. In some cases, where the dimples are formed in only one wall, they will extend entirely across the channel to contact and typically be bonded to the opposite wall to improve the strength of the heat exchanger.
In some cases, dimples will be formed in both walls and extend across the flow channel to be bonded to the opposite wall, again to provide strength. In still other cases, the dimples will be aligned with each other and formed in both walls in which case the dimples extend only half-way across the flow channel and then are bonded to one another, again to provide strength to the heat exchanger.
A typical plate heat exchanger having dimples which serve as turbulators formed in only one wall of the flow channel is illustrated in European patent Publication EP 0 263 798 B1. An example of dimples formed on both walls and extending partway across the flow channel to be bonded t one another is illustrated, for example, in European patent Publication EP 0 418 227 B1.
As mentioned in the '798 European patent publication, and as mentioned above, it is common to provide turbulator plates in various flow channels. The plates can be formed with a significant variety of structure that can be adapted to the particular heat exchange requirements. However, from a manufacturing standpoint, the provision of separate turbulators is not the preferred choice because separate parts are involved that must be produced and inserted into the flow channels, thus complicating production and assembly.
Another restriction that hampers the use of separate turbulators is that in many applications, a great degree of cleanliness of the flow channels is required and residues used to bond the separate turbulators in place can have deleterious effects on the entire system.
Thus, there is a real need for improved turbulator configurations where the turbulators are integrally formed with a wall or walls of a heat exchanger flow channel to avoid the problems associated with the use of separate turbulators and yet provide enhanced performance and adaptability to different heat exchange requirements that is more readily achievable with separate turbulators.
The principal object of the invention is to provide a new and improved turbulator structure for use in the flow channels of heat exchangers. More particularly, it is an object of the invention to provide a new and improved turbulator that is integrally formed with the walls defining a flow channel in a heat exchanger.
An exemplary embodiment of the invention achieves the foregoing objects in a heat exchanger having at least one flow channel for a heat exchange fluid defined by spaced, generally parallel walls between which the heat exchange fluid flows. A plurality of dimples are formed in at least one of the walls to extend therefrom toward the other wall to be secured thereto or to another dimple extending from the other wall toward the one wall. The dimples, as is conventional, act as turbulators to induce turbulence in the heat exchange fluid as it flows between the generally parallel walls. The invention specifically contemplates the provision of protrusions on the sides of the dimples that extend into the flow channel or channels to increase the inducement of turbulence in the heat exchange fluid as it flows between the parallel walls and around the dimples.
In one embodiment, the walls are aluminum sheets and the dimples and the protrusions are formed by a metal-forming die.
The invention contemplates that the dimples have bases integral with at least one of the walls and opposite flat tops bonded to the other of the walls or to the flat top of another of the dimples.
In one embodiment of the invention, the protrusions on the dimples are located between the base and flat top of the corresponding dimple.
In a preferred embodiment, the protrusions are ribs that extend from the base to the flat top of the dimples.
In one embodiment, each dimple has a plurality of the ribs spaced from one another about the periphery of the dimple.
A preferred embodiment contemplates that the ribs on each dimple are generally radially oriented. In a highly preferred embodiment, as mentioned previously, the dimples are die-formed in at least one of the walls and the protrusions are integral with the sheet of which the wall is formed and die-formed in the dimples.
Other objects and advantages will become apparent from the following specification taken in connection with the accompanying drawings.
In considering the invention, it must be kept in mind that same is not limited to any one specific type of heat exchanger. While it will most often be used in plate heat exchangers, drawn cup heat exchangers, or heat exchangers employing flattened tubes, those skilled in the art will readily appreciate that the same is susceptible to use in any sort of heat exchanger wherein flow channels are defined by two, generally parallel walls in which turbulating dimples can be formed. Hence, no restriction to any particular type of heat exchanger is intended except insofar as expressly stated in the appended claims.
With the foregoing in mind, reference is made to
Projecting upwardly from the wall 10 is a pattern of a plurality of dimple-like turbulators 18 to be described in greater detail hereinafter. The pattern can take on any of a plurality of different forms depending upon the heat exchange requirements of the heat exchanger, the type of flow, i.e., cross current, counter current, or concurrent, etc., the overall resistance of the flow path within the heat exchanger, etc.
As is well known, the plates shown in
Referring to
As can be seen in both
a, 1b, and
a and 1b show that the rib-like protuberances 30 may have relatively sharp apexes as desired. It will also be appreciated that with the dimples 18 being die-formed from the plates 10, 22, that the protuberances 30 can be simultaneously formed using a concave die of the desired configuration operating against radially outer surface 40 of each dimple 18 as shown in
It should be noted that the protuberances 30 need not be in the form of ribs as shown in
It is also observed that with two heat exchange fluids flowing in opposite sides of a plate, as, for example, the plate 10 as shown in
The presence of the protrusions greatly enhances the turbulating effect provided the dimples like those shown at 18 or 20 but without the protrusions 30 to achieve efficiencies more comparable to those achieved with the use of separate turbulators without the attendant disadvantage of the use of separate parts requiring additional assembly and/or contamination problems as a result of extensive bonding operations.
Typically, the protuberances 30 can be in the millimeter range, and with such a height, will enhance the bonding of the flat tops 26 to the plates 20, 22.
Number | Date | Country | Kind |
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DE 103 33 177.8 | Jul 2003 | DE | national |