The present invention refers to a plate heat exchanger.
JP-3527704 discloses such a plate heat exchanger comprising a plurality of heat exchanger plates which are provided beside each other. A first protective plate is provided beside a first outermost one of the heat exchanger plates and a first frame plate is provided outside the first protective plate. A second protective plate is provided beside the other second outermost heat exchanger plate and a second frame plate is provided outside the second protective plate. The plates are brazed to each other to form a plate package having first plate interspaces and second plate interspaces. Each heat exchanger plate has a heat exchanger area, a first porthole area, a second porthole area, a third porthole area and a fourth porthole area, each porthole area surrounding a respective porthole defined by a porthole edge. The plate heat exchanger comprises four connection pipes joined to a respective one of the porthole areas and each comprising an integral attachment flange. The attachment flanges are provided between the first frame plate and the first protective plate, between the first protective plate and the first outermost heat exchanger plate or between the frame plate and the first outermost heat exchanger plate.
In many heat exchanger applications, it is desirable to achieve a high, or a very high, design pressure, i.e. to be able to permit a high, or a very high, pressure of one or both of the media flowing through the plate interspaces. It is also desirable to be able to permit such high pressures in plate heat exchangers of the kind defined above having permanently joined heat exchanger plates, e.g. through brazing. Such high design pressures are difficult to achieve without the provision of external strengthening components.
A weak area in such plate heat exchangers is the porthole area, i.e. the area immediately around the portholes. These areas determine the design pressure in plate heat exchangers used today. However, although a certain design of the porthole area would improve the design pressure, this design would not improve the strength at another area of the plate heat exchanger, i.e. the problem would then merely be displaced.
One example of an application which requires very high design pressures is plate heat exchangers for evaporators and condensers in cooling circuits having carbon dioxide as a cooling agent. Carbon dioxide is in this context very advantageous from an environmental point of view in comparison with traditional cooling agents, such as freons.
The object of the present invention is to provide a plate heat exchanger having a high design pressure, and more precisely a plate heat exchanger permitting a very high pressure of at least one of the media flowing therethrough.
This object is achieved by the plate heat exchanger initially defined, which is characterised in that at least one of the flat elements comprises an annular protrusion extending from the bottom surface and tightly abutting one of the porthole areas of at least one of the outermost heat exchanger plates. Such a flat element will provide a strengthening of the porthole area. Thanks to the annular protrusion, the flat element will be tightly and securely attached to the heat exchanger plate in this area.
According to an embodiment of the invention, each heat exchanger plate extends along a main extension plane, wherein said areas extend between a primary level at a distance from the main extension plane and a secondary level at a distance from and on an opposite side of the main extension plane, wherein each of the porthole areas comprises an annular flat area located at one of the primary and secondary levels. Advantageously, the annular protrusion may then tightly abut the annular flat area at the secondary level.
According to a further embodiment of the invention, each of the porthole areas comprises a set of inner portions disposed on the annular flat area and distributed along the porthole edge, the inner portions being displaced from the annular flat area and extending to the other of the primary and secondary levels. Advantageously, the annular protrusion may then be located outside the inner portions seen from the respective porthole.
According to a further embodiment of the invention, each porthole area comprises a set of outer portions distributed along the annular flat area at a distance from the inner portions and being displaced from the annular flat area and extending to the other of the primary and secondary levels. Advantageously, the annular protrusion may then be located inside the outer portions seen from the respective porthole.
According to a further embodiment of the invention, the plate heat exchanger comprises a plurality of connection pipes joined to a respective porthole, wherein the flat element forms an annular attachment flange of a respective connection pipe. Such a flat element may be an integral part of the connection pipe. The flat element, as an annular attachment flange of the connection pipe, provides a tight and secure joining of the connection pipe to the respective porthole of the plate package.
According to a further embodiment of the invention, at least one of the flat elements is a separate part joined to the respective connection pipe. Such a solution is advantageous in case the connection pipe has any projecting parts, such as an external thread. The flat element may then be provided between the end plate and the outermost heat exchanger plate, whereafter the connection pipe is introduced into the porthole and joined to the flat element. Advantageously, the at least one of the flat elements may be joined to the respective connection pipe by means of brazing.
According to a further embodiment of the invention, the flat element covers a respective porthole. The flat element may then be joined to a porthole opposite to one of the connection pipes. In this case, the flat element functions as an element strengthening the porthole area when no connection pipe is joined there to. Further-more, the flat element will provide a secure sealing of the porthole area.
According to a further embodiment of the invention, the flat elements are brazed to at least one of the end plates and to at least one of the outermost heat exchanger plates.
According to a further embodiment of the invention, at least one of the end plates has a raised portion around each porthole to provide a space for the respective flat element.
According to a further embodiment of the invention, the porthole areas comprise a first porthole area, a second porthole area, a third porthole area and a forth porthole area.
The present invention will now be explained more closely by means of a description of various embodiments and with reference to the drawings attached hereto.
The heat exchanger plates 1 are produced through forming of a metal sheet and provided beside each other. The first end plate 2, the second end plate 3 and the heat exchanger plates 1 are permanently joined to each other through brazing by means of a braze material to form a plate package. The plate package define or have first plate interspaces 4 for a first medium and second plate interspaces 5 for a second medium, see
The plate heat exchanger of the embodiments disclosed has four portholes S1, S2, S3 and S4, wherein the porthole S1 is connected to a connection pipe 11 and communicates with the first plate interspaces 4, the porthole S2 is connected to a connection pipe 12 and communicates with the first plate interspaces 4, the porthole S3 is connected to a connection pipe 13 and communicates with the second plate interspaces 5 and the porthole S4 is connected to a connection pipe 14 and communicates with the second plate interspaces 5. It is to be noted that the plate heat exchanger may have another number of portholes than those disclosed, e.g. 2, 3, 5, 6, 7 or 8 portholes. Connection pipes may be provided extending from the first end plate 2, as disclosed, and/or from the second end plate 3.
Each heat exchanger plate 1 has, in the embodiments disclosed, a rectangular shape with two long side edges 15 and two short side edges 16, see
As can be seen from
All of the areas 20-24 extend, on one side of the heat exchanger plate 1, between a primary level p′ at a distance from the main extension plane p, and a secondary level p″ at a distance from and on an opposite side of the main extension plane p, see
Each heat exchanger plate 1 is made through forming of a metal sheet having a metal sheet thickness t. It is to be noted that the metal sheet thickness t may vary and be somewhat changed after the forming of the heat exchanger plate 1. The metal sheet thickness t, before the forming, may lie in the range 0.2≦t≦0.4 mm. Advantageously, the metal sheet thickness t, before the forming, may be 0.3 mm or approximately 0.3 mm.
Each heat exchanger plate 1 also has a depth d, see
As can be seen in
The ridges 27 and valleys 27′ extend along an extension line e forming an angle α of inclination with the centre line x, see
As mentioned above the plate heat exchanger is brazed by means of a braze material introduced between the heat exchanger plates 1 before the brazing operation. The braze material has a braze volume with respect to the heat transfer area 20 of the plate heat exchanger. The first interspaces 4 and the second interspaces 5 of the plate heat exchanger have an interspace volume with respect to the heat transfer area 20 of the plate heat exchanger. In order to obtain a high strength of the plate heat exchanger, it is advantageous to provide a sufficiently large quantity of braze material forming the above-mentioned joining areas 28, 29 between adjacent heat exchanger plates 1. Consequently, the proportion of the braze volume to the interspace volume may be at least 0.05, at least 0.06, at least 0.08 or at least 0.1.
Each porthole area 21-24 comprises an annular flat area 31, a set of inner portions 32 disposed on the annular flat area 31 and distributed along the porthole edge 25. The inner portions 32 are displaced from the annular flat area 31 in a normal direction with respect to the main extension plane p. Each porthole area 21-24 also comprises a set of outer portions 33 disposed on and distributed along the annular flat area 31 at a distance from the inner portions 32. The inner portions 32, which adjoin the porthole edge 25, extend to or are located at the same level as the outer portions 33, whereas the annular flat area 31 is located at another level than the inner portions 32 and the outer portions 33. More specifically, the inner portions 32 and the outer portions 33 of the first porthole area 21 and the second porthole area 22 extend to or are located at the secondary level p″, whereas the annular flat area 31 of the first porthole area 21 and the second porthole area 22 is located at the primary level p′. Furthermore, the inner portions 32 and the outer portions 33 of the third porthole area 23 and the fourth porthole area 24 extend to or are located at the primary level p′, whereas the annular flat area 31 of the third porthole area 23 and the fourth porthole area 24 is located at the secondary level p″. Each inner portion 32 have a flat extension at the respective level p′ and p″, and each outer portion 33 have a flat extension at the respective level p′ and p″. This means that the flat extension of the inner portions 32 and the outer portions 33 of the first and second porthole areas 21, 22 is located at the secondary level p″, whereas the flat extension of the inner portions 32 and the outer portions 33 of the third porthole area 23 and the fourth porthole area 24 is located at the primary level p′.
In the plate package, every second heat exchanger plate 1 is rotated 180° in the main extension plane p. This means that the inner portions 32 of one heat exchanger plate 1 will adjoin and be joined to a respective one of the inner portions 32 of an adjacent heat exchanger plate 1. In the same way, the outer portions 33 of one heat exchanger plate 1 will adjoin and be joined to a respective one of the outer portions 33 of an adjacent heat exchanger plate 1. More specifically, the inner portions 32 and the outer portions 33 of the first porthole area 21 of one heat exchanger plate 1 will be joined to a respective one of the inner portions 32 and the outer portions 33 of the third porthole area 23 of an adjacent heat exchanger plate in the plate package. In the same way, the inner portions 32 and the outer portions 33 of the second porthole area 22 of one heat exchanger plate 1 will be joined a respective one of the inner portions 32 and the outer portions 33 of the fourth porthole area 24 of an adjacent heat exchanger plate 1 in the plate package of the embodiment disclosed.
As can be seen in
Furthermore, each of the outer portions 33 may have an inner segment 45 adjoining the annular flat area 31 and having an angular extension of at least 90°, at least 120°, or at least 150°. The inner segment 45 preferably also has a continuous contour, and may have a radius R′, which is constant or substantially constant, and allowed to vary within a range 0.8 R′≦R′≦1.2 R′, more specifically within the range 0.9 R≦R≦1.1R, and most specifically within the range of 0.95 R≦R≦1.05 R.
As can be seen in
In the embodiment disclosed, each porthole area 21-24 comprises 9 inner portions 32 and 18 outer portions 33. This is a suitable number of inner portions 32 and outer portions 33. In the embodiments disclosed, the inner angular distance is about twice the outer angular distance. It is to be noted however, that the number of inner portions 32 and the number of outer portions 33 can vary and deviate from the numbers disclosed.
Each of the four connection pipes 11-14 is joined to a respective one of the porthole areas 21-24 and comprises a flat element 50. Each flat element 50 forms an attachment flange attached to or integral with a respective connection pipe 11-14 and joined to the plate package, see
With respect to the third and fourth portholes S3, S4, each flat element 50 comprises an annular protrusion 52 projecting from the flat bottom surface 51 and turned towards the plate package. The annular protrusion 52 tightly abuts the annular flat area 31 of the outermost heat exchanger plate 1 at the third porthole area 23 and the fourth porthole area 24, respectively. The annular flat area 31 is thus located at the secondary level p″, see
Between the second end plate 3 and the other outermost heat exchanger plate 1, there is provided a flat element 53 forming a strengthening washer 53. The flat elements 53 do not form a part of a connection pipe 11-14 and cover the respective porthole. The flat element 53 for the portholes S1 and S2 has a flat, or substantially flat, bottom surface 51 tightly abutting and joined to the annular flat area 31 of the other outermost heat exchanger plate 1 in the same way as the flat element 50. The flat element 53 for the portholes S3 and S4 has a flat bottom surface 51 with an annular protrusion 52 tightly abutting and joined to the annular flat area of the other outermost heat exchanger plate 1. Also the second end plate 3 has a raised portion 3a around each porthole.
It is to be noted that one or more of the flat elements 53 may be replaced by a respective connection pipe having a flat element 50 in case an inlet and/or an outlet is to be provided as an alternative or supplement through the second end plate 3.
The present invention is not limited to the embodiments disclosed but may be varied and modified within the scope of the following claims.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/SE2008/050396 | 4/4/2008 | WO | 00 | 10/21/2010 |
Publishing Document | Publishing Date | Country | Kind |
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WO2009/123516 | 10/8/2009 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
4987955 | Bergqvist et al. | Jan 1991 | A |
5435383 | Rajagopal | Jul 1995 | A |
6607026 | Naji et al. | Aug 2003 | B1 |
20040112579 | Strahle | Jun 2004 | A1 |
20070261833 | Yang et al. | Nov 2007 | A1 |
Number | Date | Country |
---|---|---|
1 850 082 | Oct 2007 | EP |
01-170881 | Dec 1989 | JP |
07-229687 | Aug 1995 | JP |
08-511863 | Dec 1996 | JP |
11-351765 | Dec 1999 | JP |
2001-280888 | Oct 2001 | JP |
2002195776 | Jul 2002 | JP |
03527704 | May 2004 | JP |
2006-517648 | Jul 2006 | JP |
WO 9500810 | Jan 1995 | WO |
WO 2004072570 | Aug 2004 | WO |
Entry |
---|
Form PCT/IB/326 Notification of Transmittal of Translation of the IPRP (Oct. 14, 2010). |
Form PCT/IB/373 International Preliminary Report on Patentability (IPRP) (Oct. 15, 2010). |
Form PCT/ISA/237 Written Opinion of the International Searching Authority (Jan. 23, 2009). |
European Search Report issued on Apr. 26, 2013 by European Patent Office in corresponding European Patent Application No. 08741886. |
Japanese Office Action issued on Aug. 2, 2012 by Japan Patent Office in corresponding Japanese Patent Application No. 2011-502890, and English translation thereof. |
Number | Date | Country | |
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20110036547 A1 | Feb 2011 | US |