STACKED PLATE HEAT EXCHANGER

Abstract

The invention relates to a stacked plate heat exchanger, comprising a plurality of elongate plates which are stacked on one another and connected to one another and which have a corrugated profile, which plates have a cavity for leading through a medium to be cooled in the longitudinal direction of the plates and define a further cavity for leading through a coolant, wherein leadthrough openings for supplying or discharging the medium to be cooled or the coolant are formed approximately in the end regions of each elongate plate and each elongate plate is surrounded by a bent-off edge, wherein an nth corrugation of the corrugated profile of each plate is drawn close to the edge, preferably into the edge, whereas the other corrugations of the corrugated profile of the plate terminate before the edge, where n=2, 3, 4 etc.

Description

TECHNICAL FIELD

The invention relates to a stacked plate heat exchanger in accordance with the preamble of claim 1.

PRIOR ART

In cooler manufacture, stacked plate heat exchangers are sufficiently well known which cool air which is supplied to a combustion engine by means of an oil coolant or air cooling. DE 43 14 808 A1 discloses a plate heat exchanger, in particular an oil/coolant cooler, which has elongate plates which are stacked on one another and whose peripheral edges lie against one another. The plates of the heat exchanger all have the same shape. The plates have locally turbulence generating elevations in the form of knobs or sealing embossments. However, internal fittings in the form of turbulence inserts or sealing washers are also known.

DE 10 2004 036 951 A1 shows a heat exchanger which is constructed from identical plates which are stacked above one another, wherein each plate has a bent edge. In each case two plates lying above one another here form a cavity for leading through a medium to be cooled in the longitudinal direction of the plates or a further cavity for leading through a coolant. Through-openings for supplying or discharging the medium to be cooled or the coolant are formed in the end regions of each elongate plate. Here, each plate has a corrugated profile in order to ensure that the medium to be cooled or the coolant does not flow rectilinearly from the supply side to the discharge side. In the case of the stacked plate heat exchangers described, the same thermodynamic conditions are present on both fluid sides.

In order to create different thermodynamic conditions on the two fluid sides, it is necessary to use additional plates, this requiring increased outlay in terms of construction and at the same time increasing the costs of the heat exchanger.

SUMMARY OF THE INVENTION, OBJECT, ACHIEVEMENT, ADVANTAGES

It is the object of the invention to provide a stacked plate heat exchanger by means of which differentiated thermodynamic conditions are set on the two fluid sides of the stacked plate heat exchanger without further increasing the manufacturing costs.

This is achieved by the features of claim 1. One exemplary embodiment relates to a stacked plate heat exchanger in which an nth corrugation of the corrugated profile of each plate is drawn close to the edge, preferably into the edge, whereas the other corrugations of the corrugated profile of the plate terminate before the edge, where n=2, 3, 4 etc. This has the advantage that a pressure drop can be set inside the fluid duct.

Furthermore, it is advantageous if each nth corrugation of the corrugated profile of each plate is drawn close to the edge, preferably into the edge, where n=2, 3, 4 etc.

Advantageously, the plates are arranged in a block, wherein each xth plate of which the corrugated profile has at least one corrugation drawn into the edge is bounded on both sides by two plates of which the corrugations of the corrugated profile terminate before the edge. Such a stacked plate heat exchanger offers the possibility of setting two different thermodynamic conditions on the two fluid sides of the stacked plate heat exchanger without thereby requiring turbulence inserts or the installation of an external bypass. Merely as a result of the design of the different corrugations, either an internal bypass is formed on one fluid side in the vicinity of the edge of the plates or the thermodynamic conditions, such as power and pressure loss, are designed to be different as a result of the changed geometry on the two fluid sides.

In one refinement, every second plate has corrugations of the corrugated profile which are drawn into the edge. Hence, highly turbulent flows can be generated and thus variable thermodynamic conditions are produced on one fluid side of the heat exchanger. By combining two different stacked plate designs in a heat exchanger block, it is possible to form an internal bypass which is formed in particular between the corrugation and the edge of the plate, where the corrugations terminate before the edge. The second plate, which delimits this bypass and in which the corrugations are drawn into the edge, thus forms the closure of the bypass.

In one variant, the plates have a recurring corrugated profile which extends substantially transversely with respect to the main throughflow direction of the coolant or the medium to be cooled. The corrugated profile ensures that the flow profile of the coolant or the medium to be cooled does not extend rectilinearly over the longitudinal extent of the plates. As a result, the flow is multiply deflected in a cavity between two plates, which results in the coolant or the medium to be cooled being better distributed over the plate width.

In one development, the corrugated profile is corrugated in a zig-zag shape about the longitudinal extent of the plates. Here, the corrugated profile extending in a zig-zag shape is characterized by the leg length, the leg angle between adjacent legs and the profile depth.

In a further embodiment, the corrugated profile is formed as a stamping in the plates which consist of a heat-conducting material. Since this material is preferably aluminum, the stampings can be produced simply and cost-effectively in a stamping process.

Advantageously, the bent-off edges, which lie on top of one another, of the plates are brazed to one another. This ensures that no coolant and also no medium to be cooled can exit from the stacked plate heat exchanger.

In a further embodiment, the through-openings for supplying and for discharging the medium to be cooled or the coolant of each plate are situated diagonally opposite one another. This ensures that the medium to be cooled or the coolant flows through the plates over a large area, resulting in good heat exchange between the medium to be cooled and the coolant.

Further advantageous refinements are described by the following description of the figures and by the dependent claims.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention is explained in more detail below on the basis of at least one exemplary embodiment with reference to the drawings, in which:

FIG. 1 shows a first exemplary embodiment of the stacked plate heat exchanger according to the invention having a first plate design,

FIG. 2 shows the first exemplary embodiment of the stacked plate heat exchanger according to the invention having a second plate design,

FIG. 3 shows a further exemplary embodiment of a stacked plate heat exchanger according to the invention,

FIG. 4 shows a further exemplary embodiment of a heat exchanger according to the invention, and

FIG. 5 shows a detail of the exemplary embodiment shown in FIG. 4.

PREFERRED EMBODIMENT OF THE INVENTION

FIG. 1 shows a first exemplary embodiment of the heat exchanger 1 according to the invention in which a plan view of a first plate 2 having a first plate design is depicted. Here, each of the plates 2 has a corrugated profile 4 of which the corrugations 42 terminate before the edge and which is stamped into a base plate 5. Leadthrough openings 6, 7, 8, 9 are in each case arranged in the vicinity of the edge of the base plates 5. The leadthrough openings 6, 7 and 8, 9 situated diagonally opposite one another form a pair, wherein the leadthrough opening 6 forms the supply for the coolant, whereas the leadthrough opening 7 forms the outflow for the coolant. Correspondingly, the leadthrough opening 9 forms the supply for the medium to be cooled, whereas the leadthrough opening 8 situated diagonally opposite forms the discharge for the medium to be cooled. Here, the leadthrough openings 7, 8 forming the outflow for the media are in each case bordered by a dome. The base plate 5 is surrounded by a peripheral bent edge 10.

The second plate 3, the plan view of which is shown in FIG. 2, differs from the first plate 2 shown in FIG. 1 in that it has, at least at certain points, a corrugated profile 4 in which the corrugation 41 is drawn into the edge 10. In the case of the first plate 2, the corrugations 42 of the corrugated profile 4 terminate in principle before the edge 10.

FIG. 3 depicts a cross section through the second plate 3 in which the corrugation 41 is drawn partially through the edge 10 and is connected thereto. Here, the corrugation 41 has a zig-zag-shaped design in the longitudinal direction of the second plate 3 and merges into the edge 10 (region A).

FIG. 4 shows a cross section through the stacked plate heat exchanger 1 according to the invention in which, for example, a first plate 2 is surrounded by two second plates 3. These three plates 2, 3 lie on top of one another, wherein the edges 10 are brazed to one another. In the central, first plate 2 in which the corrugation 42 terminates before the edge 10, an interspace 11 which is used as an internal bypass 12 is formed between the last corrugation 42 and the edge 10. By virtue of the fact that the corrugations 41 of the second plates 3 situated above and below the first plate go directly into the edge 10, they thus form the closure of the bypass 12. Here, this bypass 12 can be formed on both sides of the plate 2.

FIG. 5 shows once again an enlargement of the combination of the plates 2 and 3 in which the bypass 12 is formed by the corrugation 42, which does not extend as far as the edge, of the plate 2. The bypass 12 is closed by the corrugation 41 of the plates 3 which engage directly in the edge 10.

In such a stacked plate heat exchanger 1, the pressure drop inside a fluid duct can be set. Here, two different thermodynamic fluid sides can be produced. In one fluid side, power and pressure loss are reduced, with the result that relatively high volume flows are allowed, and, on the second fluid side, the bypass serves as a power amplifier with a relatively high pressure loss, which entails relatively low volume flows.

Claims

1. Stacked plate heat exchanger, comprising a plurality of elongate plates which are stacked on one another and connected to one another and which have a corrugated profile which plates have a cavity for leading through a medium to be cooled in the longitudinal direction of the plates and define a further cavity for leading through a coolant, wherein leadthrough openings for supplying or discharging the medium to be cooled or the coolant are formed approximately in the end regions of each elongate plate and each elongate plate is surrounded by a bent-off edge, wherein an nth corrugation of the corrugated profile of each plate is drawn close to the edge, preferably into the edge, whereas the other corrugations of the corrugated profile of the plate terminate before the edge, where n=2, 3, 4 etc.

2. Stacked plate heat exchanger according to claim 1, wherein each nth corrugation of the corrugated profile of each plate is drawn close to the edge, preferably into the edge, where n=2, 3, 4 etc.

3. Stacked plate heat exchanger according to claim 1, wherein the plates are arranged in a block, wherein each xth plate of which the corrugated profile has at least one corrugation drawn into the edge is bounded on both sides by two plates of which the corrugations of the corrugated profile terminate before the edge.

4. Stacked plate heat exchanger according to claim 1, wherein every second plate has corrugations of the corrugated profile which are drawn into the edge.

5. Stacked plate heat exchanger according to claim 1, wherein the plates have a recurring corrugated profile which extends substantially transversely with respect to the main throughflow direction of the coolant or the medium to be cooled.

6. Stacked plate heat exchanger according to claim 5, wherein the corrugated profile is corrugated in a zig-zag shape about the direction of longitudinal extent of the plates.

7. Stacked plate heat exchanger according to claim 1, wherein the corrugated profile is formed as a stamping in the plates which consist of a heat-conducting material.

8. Stacked plate heat exchanger according to claim 1, wherein the bent-off edges, which lie on top of one another, of the plates are brazed to one another.

9. Stacked plate heat exchanger according to claim 1, wherein the leadthrough openings for supplying and for discharging the medium to be cooled or the coolant of each plate are situated diagonally opposite one another.