This application is the National stage of International Patent Application No. PCT/EP2013/056322, filed on Mar. 25, 2013. which claims priority to and all advantages of French Patent Application No. 12/52934, filed on Mar. 30, 2012, the content of which is incorporated herein by reference.
The invention concerns a heat exchanger, in particular for vehicles, especially electric and/or hybrid vehicles.
In vehicles with a thermal engine, using the heat given off by the engine to heat the vehicle passenger compartment is known. In vehicles with an electric motor, the heat given off by the electric machine used to drive the vehicle is too small to fulfill such a function. An identical problem is posed, even if this is to a lesser degree, in hybrid vehicles, that is to say with a both thermal and electric drive.
To solve this problem, it has already been proposed to operate air-conditioning loops reversibly. They are thus configured so as to introduce alternately cold air or hot air into the passenger compartment, according to the request from the user.
They use a heat exchanger, situated at the front face of the vehicle, so as to be swept by an airflow at ambient temperature passing through the radiator grille. Said exchanger serves to condense the refrigerant fluid circulating in the air-conditioning loop when said air-conditioning loop is used to cool the passenger compartment and to evaporate said fluid in the opposite case, that is to say when the air-conditioning loop is functioning as a heat pump to heat the passenger compartment.
The thermal performance of such heat exchangers is difficult to optimise since the solutions for improving the functioning thereof as a condenser are generally opposed to those for improving the functioning thereof as an evaporator.
More precisely, in condensers or evaporators of the interlayered tube type, it has been known for a long time that it is advantageous to circulate the refrigerant fluid serially in passes containing a given number of tubes. In condensers, it has also been known for a long time that decreasing the number of tubes from one pass to another optimises the heat exchange while limiting losses of pressure. Persons skilled in the art also know that such a distribution of tubes is on the other hand unfavourable to the functioning of evaporators.
A first solution for avoiding this situation is to reverse the direction of circulation of the fluid in the heat exchanger, but such a solution increases the complexity of the air-conditioning loop.
For heat exchangers that are to serve alternately as condenser and evaporator, without reversal of the direction of circulation of the refrigerant fluid in the heat exchanger, a person skilled in the art is then naturally led to propose heat exchangers having a configuration that is as symmetrical as possible in order to avoid being detrimental to one operating mode with respect to the other. In the case of heat exchangers of the interlayered tube type with a plurality of passes, this results in the use of two passes, having an identical number of tubes per pass or at the least that remains similar from one pass to another.
This being the case, a particularly critical problem is the risk of icing of the heat exchanger in heat pump mode. The appearance of such a phenomenon tends to stop all or some of the heat exchange because of the increase in the loss of air pressure. The degradation of the heat exchange due to the icing tends to reduce the evaporation temperature and the pressure of the refrigerant fluid inside the heat exchanger, which increases the risk of icing of the exchanger accordingly.
Another particularly critical problem relates to the loss of pressure internal to the heat exchanger. In evaporator mode, it is known that the density of the refrigerant fluid is lower than in condenser mode, which has the effect of increasing the loss of pressure. It thus appears essential to seek to reduce the loss of pressure in evaporator functioning in order to improve the thermal performance.
To avoid such a risk, the use of a smaller number of tubes in the first pass has already been considered, while placing this first pass in the bottom portion of the exchanger, the exchanger being positioned in a substantially vertical plane and the tubes being oriented substantially horizontally.
Tests carried out by the applicant have however shown that some of the tubes of such an exchanger participate little or not at all in the exchange. These are in particular tubes in the second pass situated close to the first pass. It appears moreover that this problem is more general and is encountered also in heat exchangers having a larger number of passes, a different distribution of the tubes per pass and/or a different, in particular vertical, orientation of the tubes.
The present invention aims to improve the situation and for this purpose proposes a heat exchanger, said heat exchanger comprising a bundle of tubes, providing an exchange of heat between a refrigerant fluid circulating in said tubes and an external airflow, and a first header, said heat exchanger being configured so as to establish a serial circulation for the refrigerant fluid between a first portion of said tubes, emerging in a first portion of said first header, said first header and a second portion of said tubes, emerging in a second portion of said first header.
According to the invention, said first header comprises a partition configured so as to disturb the circulation of fluid between the first and second portions of said tubes.
The applicant has found that the use of such a partition improves the distribution of the refrigerant fluid inside the tubes of the bundle, which has the effect of increasing the heat exchange whilst controlling losses of pressure, in particular in evaporator operating mode. Although it seems that this type of partition must accelerate the refrigerant fluid by reducing its cross section of flow and therefore being unfavourable to the supply to the tubes situated downstream, on the contrary an improved supply to said tubes is observed. Without claiming to constitute an explanation, such a phenomenon could originate in the two-phase state of the refrigerant fluid when it goes from one pass to another.
According to various embodiments, which can be used separately or in combination:
The invention will be better understood, and other aims, details, features and advantages thereof will emerge more clearly during the following detailed explanatory description of a plurality of embodiments of the invention given by way of purely illustrative and non-limitative examples, with reference to the accompanying drawings.
In these drawings:
As illustrated in
Said heat exchanger comprises a bundle of tubes 2, affording an exchange of heat between a refrigerant fluid circulating in said tubes and an external airflow. It can for this purpose be provided with inserts 3, in particular corrugated inserts, situated between the tubes 2 in order to increase the exchange surface area between the tubes and the external airflow.
Said heat exchanger in this case comprises first and second headers 4, 5 in which the tubes emerge through the opposite ends 2A of said tubes 2. Said tubes 2 are, for example, parallel to one another. They may have substantially the same length. Said headers 4, 5 are in this case parallel and oriented substantially perpendicular to the tubes 2.
Preferably, the tubes lie substantially parallel to the transverse axis of the vehicle, the headers therefore lying at right angles to the tubes.
The refrigerant fluid circulates in the heat exchanger in at least two passes. The exchanger is thus configured so as to establish a serial circulation for the refrigerant fluid passing first of all, in the direction of an arrow marked 6, in a first portion 4 of said tubes 2, emerging in a first portion 4a of the first header 4, next passing, in the direction of an arrow marked 7, in said first header 4 and finally passing, in the direction of an arrow marked 8, in a second portion of said tubes 2, emerging in a second portion 4b of said first header 4. The refrigerant fluid circulates in the heat exchanger from bottom to top, that is to say from the first pass arranged beneath the second pass along a vertical axis of the point of reference associated with the vehicle.
In order to provide circulation in various passes, the first header 4 and/or the second header 5 are provided with partitions 9, referred to as separation partitions, dividing said headers into various chambers 5a, 5b and forcing the refrigerant fluid to pass through the tubes 2 connected to the upstream chamber, situated on one side of one of said separation partitions, and then through the opposite header and through the tubes connected to the downstream chamber, situated on the other side of said separation partition. Said separation partitions are preferably sealed.
The tubes 2 of the bundle are here distributed in a first pass and a second pass, corresponding respectively to the first portion and second portion of said tubes 2. In
Said heat exchanger may also comprise, for example, an inlet 10 and/or an outlet 11 for the refrigerant fluid, here situated on the same header, in this case the second header 5.
According to the invention, said first header 4 comprises a partition 12 configured so as to disturb the circulation of fluid between the first portion and the second portion of said tubes 2, namely, in this case, the first pass and the second pass.
It has been found that said partition 12 for disturbing the circulation of fluid between the two passes promotes better distribution of the flow of refrigerant fluid in all the tubes in a bundle, more precisely when this flow takes place from bottom to top. The heat exchange is thus improved while controlling losses of pressure.
It should be noted that the partition or partitions disturbing the circulation of refrigerant fluid are functions different from those of the separation partitions. The separation partitions serve to define a circulation in a plurality of passes in the bundle while the partitions disturbing the circulation of refrigerant fluid serve, said circulation in passes being established, to make the flow of fluid turbulent when it goes from one pass to another. The partition or partitions disturbing the circulation of refrigerant fluid are also situated inside the header or headers; the one illustrated in
The refrigerant fluid in the first pass represents, for example, 50% to 70% of the cross section of flow for the refrigerant fluid in the bundle. According to a first variant, the cross section of flow for the refrigerant fluid is identical in each pass. In other words, if the tubes 2 in the bundle are all identical, each pass has the same number of tubes 2.
This being the case, according to another variant, it was found that superior results were obtained by using a cross section of flow for the refrigerant fluid in the first pass strictly greater than 50%, and in particular approximately 60%. By virtue of said partition disturbing the flow of fluid, although then favouring operation in the form of a condenser operation in the form of an evaporator remains satisfactory. In other words, according to this other variant, if the tubes 2 in the bundle are all identical, the first pass comprises 50% to 70% of the tubes, in particular 60% of the tubes 2.
Said disturbance partition 12 is situated here at a passage zone 13 between the first 4a and second portion 4b of the first header 4. This being the case, in a variant, it may be slightly at a distance. More precisely, it may be situated at a distance d from said passage zone 3 while being positioned either in said first portion 4a, the distance d then being less than half an axial length of said first portion 4a of the first header 4, or in said second portion 4b, the distance d then being less than half the axial length of said second portion 4b of the first header 4.
The partition 12 disturbing the circulation of the refrigerant fluid can be configured so as to orient the refrigerant fluid preferentially towards the tubes 2 of the second tube portion situated close to the separation partition 9 situated in the second header 5. It can be seen that the tubes 2 in question are here opposite the outlet 11 for the refrigerant fluid, and arranged above the disturbance partition 12.
According to a first embodiment, the partition 12 disturbing the circulation of refrigerant fluid is arranged, for example, transversely, in particular perpendicular, to a longitudinal axis of the first header and has one or more passage orifices for the refrigerant fluid. What is meant by this is that said partition 12 disturbing the circulation of refrigerant fluid has a periphery coming into contact with the first header 4 while following the internal contour thereof. Said passage orifices have in particular a round or rectangular cross section. They are through-orifices and allow said refrigerant fluid to pass from said first 4a to said second 4b portion of the first header 4. The partitions illustrated in
According to the variants in
According to the variant in
According to the variants in
According to the variant in
According to the variant in
According to the variant in
According to the variant in
In an additional variant, not illustrated, the partition 12 disturbing the circulation of refrigerant fluid may consist of an element of the filter type arranged transversely in the first header 4.
According to the embodiment in
Said exchanger is, for example, made of aluminium or aluminium alloy. It is produced for example by brazing. The tubes 2 may be of the flat type and/or have a plurality of circulation channels for the refrigerant fluid. They are, for example, extruded tubes or tubes provided with an internal disturbance member defining said channels. The headers 4, 5 have, in particular, a substantially rectangular cross section. They may be formed by a header plate, in which said tubes 2 are inserted through corresponding orifices, and a cover closing said headers in combination with two end partitions.
Said heat exchanger is in particular configured so as to be positioned on the front face of a motor vehicle, in a substantially vertical orientation, the circulation of the refrigerant fluid taking place from bottom to top. In other words, the first pass is, for example, the bottom pass.
Number | Date | Country | Kind |
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12 52934 | Mar 2012 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2013/056322 | 3/25/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2013/149879 | 10/10/2013 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
5341872 | Mercurio | Aug 1994 | A |
6062303 | Ahn | May 2000 | A |
6250103 | Watanabe | Jun 2001 | B1 |
6684662 | Manaka | Feb 2004 | B2 |
7096930 | Nobuta | Aug 2006 | B2 |
7757753 | Yanik | Jul 2010 | B2 |
9115934 | Kopchick | Aug 2015 | B2 |
20080023185 | Beamer | Jan 2008 | A1 |
20150053383 | Citti | Feb 2015 | A1 |
Number | Date | Country |
---|---|---|
0 887 611 | Dec 1998 | EP |
03140764 | Jun 1991 | JP |
H 03-140764 | Jun 1991 | JP |
H 11-337293 | Dec 1999 | JP |
2001-235255 | Aug 2001 | JP |
2005-140374 | Jun 2005 | JP |
WO 2007083680 | Jul 2007 | WO |
Entry |
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International Search Report for Application No. PCT/EP2013/056322 dated Apr. 24, 2013, 7 pages. |
English language abstract for JPH 03-140764 extracted from PAJ database on Oct. 9, 2014, 1 page. |
English language abstract and machine-assisted English translation for JPH 11-337293 extracted from PAJ database on Oct. 9, 2014, 18 pages. |
English language abstract and machine-assisted English translation for JP 2001-235255 extracted from the PAJ database on Oct. 9, 2014, 19 pages. |
English language abstract and machine-assisted English translation for JP 2005-140374 extracted from PAJ database on Oct. 9, 2014, 26 pages. |
English language abstract for WO 2007/083680 extracted from espacenet.com database on Oct. 9, 2014, 1 page. |
Number | Date | Country | |
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20150053383 A1 | Feb 2015 | US |