1. Field of the Invention
The invention relates to heat exchangers and more particularly to counter-flow heat exchangers of the type comprising two sets of medium through-flow channels which are placed mutually interlaced and through which two media can flow physically separated from each other but in heat-exchanging contact.
2. Description of the Related Art
Such heat exchangers are known in many embodiments and comprise walls separating said channels with heat-conducting fins arranged on both sides of each wall. The fins extend with their main planes in the respective flow directions of said media, wherein a fin on the one side of a wall is in thermal contact with a fin on the other side of this wall. A housing may accommodate the walls with the fins and may be provided with inlets and outlets for the channels either individually per channel or commonly for the sets of channels via respective manifolds.
In known heat exchangers of this type, the walls and heat-conducting fins are manufactured of metal and joined together by welding, brazing or the like. Heat transfer may take place both through the wall and also along the wall by conduction. Such conduction in the plane of the wall can be detrimental to the efficiency of the heat exchanger.
The present invention addresses certain problems of the prior art by providing a heat exchanger, comprising a plurality of walls of plastic material, the walls being held in spaced, generally parallel relation to form through-flow channels, heat-conducting metal fins arranged between adjacent walls, which fins have a width extending between the walls and a length defining a flow direction, the heat-conducting metal fins being generally parallel to one another and structurally connected to the respective adjacent walls to maintain said spaced parallel relation and wherein the fins on a first side of a wall are each aligned with and in direct thermal contact with a corresponding fin on a second side of that wall, whereby heat conduction can take place from fin to fin through the wall, wherein the fins are arranged in a plurality of strips, spaced from one another in said flow direction and thermally separated by the plastic material of the wall, the fins in each strip being spaced from each other by a pitch distance and the fins in a first strip being offset from the fins in an adjacent strip by a fraction of the pitch distance. As a result of this configuration, the leading edge of each fin is always situated in a practically undisturbed flow, which enhances the heat transfer. Furthermore, the resulting heat exchanger may be very light and can be manufactured inexpensively, while nevertheless still having excellent efficiency.
According to another aspect of the invention, the walls may be embodied as membranes and the fins may be embodied as heat-transferring, for instance metal strips with a general wave shape, which fins are provided with contact surfaces connected to the walls and main planes extending between two walls, this such that, in addition to a thermal function, the fins also have a structural function. The coefficient of heat transfer of the whole separating wall preferably amounts to a minimum of 1 W/m2K. The heat exchanger according to the invention thus derives its mechanical strength and rigidity substantially from the fins. According to the prior art the mechanical strength and rigidity of heat exchangers are not generally determined by fins but by the heat-exchanging walls. This requires the use of mechanically strong and therefore thick walls, which thereby have the inherent drawback of a greater thermal resistance, to the extent the same materials are used. The heat exchanger according to the present invention can combine high efficiency with a very compact construction.
In this context it should also be understood that in theoretical sense a membrane is an “infinitely thin” skin-like element, which has a negligible bending stiffness and can therefore only derive its stiffness from the fact that it is clamped on its ends, optionally in combination with a certain tensile stress in the form of a bias. When a pressure difference occurs between the primary circuit and the secondary circuit, a certain bending of a practical membrane cannot be wholly prevented. In practice, the pressure resistance of a heat exchanger according to the invention is limited to a value determined by the mechanical properties, such as the thickness of the material used, the tensile strength, the ability to stretch, the limit of stretch, the bias, the mutual distance between the walls and the like. When a bias is used, this forms an extra load on the wall material. The maximum tensile stress in the wall is therefore equal to the total maximal tensile stress minus the bias.
In order to make the heat transfer between the layers of fins as great as possible, an embodiment is recommended in which corresponding contact surfaces are in thermal contact via the wall.
In a practical embodiment the heat exchanger has the feature that the contact surfaces are adhered to the wall by means of an adhesive layer applied to at least one contact surface.
An alternative has the feature that corresponding contact surfaces are directly connected to each other via a perforation in the wall by means of an adhesive layer applied to at least one contact surface.
It will be apparent that it is essential that the thermal resistance formed by the wall and the glue layer must be as small as possible. In this respect these layers should preferably be thin.
In respect of the thermal contact between adjacent layers of fins, an embodiment is recommended in which the walls consist of PVC and the fins are connected to the walls by an ultrasonic treatment or a thermal treatment, in combination with pressure. The connection can for instance take place by welding, soldering or the like, in any case such that the thermal resistance formed by the adhesive is absent.
A preferred embodiment has the special feature that the housing is form-retaining and the walls are connected to the housing in manner resistant to tensile stress, such that the tensile stresses occurring in the walls as a result of a pressure difference between the two sets of channels can be absorbed by the housing.
Another embodiment has the feature that the walls are biased such that, at a preselected maximum permissible pressure difference between the two sets of medium through-flow channels, the bending of the wall between the free space defined by the contact surfaces of the fins i.e. the bending of the membrane occurring at the relevant pressure divided by the relevant mutual distance between the contact surfaces in question, amounts to a maximum of 2.5%.
In the embodiment in which corresponding contact surfaces are in thermal contact via the wall, the heat exchanger preferably has the feature that the thermal resistance of the wall transversely of its main plane amounts to a maximum of 0.1 of the thermal resistance in the case of direct contact between contact surfaces directed toward each other, and is therefore negligible.
The heat exchanger preferably has the feature that the thermal resistance of the wall in its main plane over the mutual distance between two fins adjoining in flow direction is at least 10 times greater than in the case of fins directly coupled to each other thermally.
A practical embodiment has the special feature that the walls consist of PET, for instance reinforced PET, are treated with a corona discharge, are then provided with a primer, followed by a glue layer for connection to the contact surfaces of the fins.
An alternative embodiment has the feature that the walls consist of PVC and that the fins are connected to the walls by an ultrasonic treatment or a thermal treatment, in combination with pressure.
A substantial improvement in the tensile strength relative to the usual wall materials is obtained with a heat exchanger which has the feature that the wall consists of a fiber-reinforced material, which fibers consist for instance of glass, boron, carbon. The fibers can for instance be embodied as fabric or as non-woven.
A great improvement of the thermal conductivity of the wall is realized with a heat exchanger which has the feature that the walls consist of a plastic in which aluminum powder is embedded.
In order to enable the heat exchanger to be maintenance-free and make it suitable for the most diverse applications, the heat exchanger can have the feature that the walls consist of PET, for instance reinforced PET, are treated with a corona discharge, are then provided with a primer, followed by a glue layer for connection to the contact surfaces of the fins.
A very practical embodiment has the special feature that the walls protrude outside the fins such that they can be connected to a frame, for instance in order to place them under bias, or such that the protruding wall parts can be thermally formed into interlacing units and manifolds for respectively joining together and separating again the sets of channels. This embodiment alleviates the problem of embodying an interlacing unit and manifold on both sides of the heat exchanger.
A determined embodiment has the feature that the heat exchanger is given a modular structure with blocks which can be releasably coupled to each other. Thus is achieved that the heat exchanger can be manufactured in different dimensions by making use of blocks, without substantial change-over of a production line being necessary for this purpose.
A particular embodiment has the feature that the layers are ordered in the sequence P, S, P, S, P, S and so on. Another embodiment has the feature that the layers are ordered in the sequence P, P, S, S, P, P and so on.
In order to limit the mechanical load on the walls as much as possible during production of the heat exchanger, a preferred embodiment has the special feature that the contact surfaces of the fins have rounded peripheral edges.
In an embodiment in which the wall consists of a fiber-reinforced material, the heat exchanger can have the special feature that the fibers have an anisotropic heat conduction, such as carbon fibers, wherein the heat conduction is smaller in the main plane of the wall than in transverse direction thereof. The tensile strength of the wall and thereby the pressure resistance of the heat exchanger is hereby substantially improved, and a very good heat contact between adjacent fins is also achieved.
A suitable choice of the wall material can be made with an eye to operating conditions and applications. Thermoplastic plastics as well as thermosets such as polyether imide are suitable. The wall materials can also be provided with a coating, for instance of another plastic, a silicon material or the like. In the case of fiber reinforcement the fibers can have diameters of a few microns.
Another choice of material for the wall is metal, in particular a plastic foil with a metal coating on at least one of the two sides.
A very simple solution to a possibly occurring corrosion problem consists of an anticorrosive coating applied to at least one of the two contact surfaces and for instance comprising a primer layer and/or an adhesive layer extending over the whole surface of the fins and optionally the wall.
A specific embodiment has the special feature that the adhesive layer is of the type which can be thermally activated and that the fins are adhered to the relevant wall and/or to an adjacent set of fins at the position of the contact surfaces by heating and pressure by means of a heated pressing punch.
In yet another variant the heat exchanger has the feature that the fins are provided on the side remote from said coating with a second coating which can withstand said heating and pressure.
The features and advantages of the invention will be appreciated upon reference to the following drawings, in which:
a shows a schematic perspective view on small scale of a heat exchanger according to the invention with a housing and interlacing units and manifolds;
b shows the detail II of
a and 7b show respective phases of adhesion of the contact surfaces of fins to a membrane;
a shows a cross-section corresponding with
b is a perspective view of the preliminary stage of the structure according to
a and 10b show views corresponding with
c is a perspective view of the phase shown in
a shows a highly schematic view of a device for manufacturing a heat exchanger according to the invention in industrial manner;
b shows detail XIII of
c shows a perspective view in slightly further developed and detailed form of the device of
The following is a description of certain embodiments of the invention, given by way of example only and with reference to the drawings. Referring to
By means of means to be described below the fins are adhered with their mutually facing contact surfaces to walls 2 on either side of these walls 2. In this embodiment the successive walls alternately bound a primary and a secondary circuit, designated in the figure with arrows P and S respectively. These medium circuits relate to the flow of media for placing in heat-exchanging contact with each other, for instance gaseous media, liquid media or respectively gas and liquid or two-phase media.
The drawing further shows that strips 3, 4, 5 have a limited length in the medium flow direction and that the subsequent fin strips 6,7, 8 are placed at a distance. This enhances the effective heat transfer. The intermediate space 9, which is not provided with fins, acts effectively as thermal separation in the transport direction. A prerequisite is that the wall material has limited heat conductivity and is for instance not manufactured from a good heat-conducting material such as copper. Plastic is for instance a very suitable choice. Because the walls are embodied as membranes and are therefore very thin, they present only a negligible thermal resistance at the position of the heat-transferring contact surfaces of the fins directed toward each other.
b shows the interior of heat exchanger 10.
This is essentially the same unit as in
a shows a membrane 28 with glue layers 29 at the position of contact surfaces 30 of fins 31. The structure drawn in
The membrane material is hereby made thinner in the intermediate zone 33 and the material is pressed slightly outward at the side in zones 34. This embodiment is favorable in the sense that a good seal is always ensured, while the already thin membrane material is made extra-thin.
a shows a variant in which fins 35, 36 are provided with complementary corrugations 37, 38 respectively. A good positioning of the contact surfaces is hereby always ensured. The corrugations 37, 38 also extend in transverse direction. This aspect is clearly shown in
In
As
b, which corresponds with
Finally,
Thus, the invention has been described by reference to certain embodiments discussed above. It will be recognized that these embodiments are susceptible to various modifications and alternative forms well known to those of skill in the art. Further modifications in addition to those described above may be made to the structures and techniques described herein without departing from the spirit and scope of the invention as defined by the claims.
Number | Date | Country | Kind |
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1020483 | Apr 2002 | NL | national |
This application claims priority from Dutch application number 1020483 filed on 26 Apr. 2002, and is a continuation of U.S. application Ser. No. 10/512,482 which was filed on 8 Jul. 2005 based on international application no. PCT/NL03/00151, the contents of which are hereby incorporated by reference in their entirety.
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Entry |
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Summary of Manufacturing and Application of Composite Material Carbon Fiber. |
Study & Development of the surface coating on Aluminium Foil Heat Exchanger Fin Materials for Air Conditioner. |
Number | Date | Country | |
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20100243222 A1 | Sep 2010 | US |
Number | Date | Country | |
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Parent | 10512482 | US | |
Child | 12795890 | US |