HEAT EXCHANGER

Abstract

A high pressure heat exchanger having a first manifold and a second manifold connected fluidly by a plurality of tube sets arranged in a spaced manner along the manifolds. At least one of the manifold includes a rear cover, a header with slots receiving tube end sections of the tube sets and several internal plates interposed between the header and the rear cover and configured to create a flow path within the manifold, this flow path being in fluid connection with the tubes to allow a circulation of a refrigerant in the tubes and the manifold. The header has preferably at least a first area adjacent to at least one of the slots and having a first thickness and at least a second area surrounding at least partially the first area and having a second thickness, the first thickness being smaller than the second thickness.

Claims

1. A high pressure heat exchanger comprising a first manifold and a second manifold connected fluidly by a plurality of tube sets having tube end sections and arranged in a spaced manner along the first manifold and the second manifold, wherein at least the first manifold includes a rear cover, a header with slots receiving the tube end sections, and at least one internal plate interposed between the header and the rear cover and configured to create a flow path within the first manifold, the flow path being in fluid connection with the tube sets to allow circulation of a refrigerant in the tube sets and the first manifold and the second manifold, and wherein the header has at least a first area adjacent to at least one of the slots and having a first thickness measured along the insertion direction of the respective tube end section, and at least a second area surrounding at least partially the first area and having a second thickness measured along the insertion direction of the respective tube end section, the first thickness being smaller than the second thickness.

2. The high pressure heat exchanger according to claim 1, wherein the first areas are located adjacent to each slot of the header so that that the thickness of the header is locally smaller, around the slots, than throughout the rest of the header.

3. The high pressure heat exchanger according to claim 1, wherein the header thickness changes from the first thickness having a minimum value at the contact with the tube end section in the slot up to the second thickness.

4. The high pressure heat exchanger according to claim 1, wherein 3<h/w1<h/c where h is the height of a distribution channel of the manifold formed between the rear cover and the header and measured along the insertion direction of the respective tube end section, w1 is the first thickness of the header, and c is a smallest wall thickness of the tube end section.

5. The high pressure heat exchanger according to claim 1, wherein the first manifold includes a plurality of internal pates stacked together.

6. The high pressure heat exchanger according to claim 1, wherein the at least one internal plate has internal slots extending so as to create U form flow paths within the first manifold.

7. The high pressure heat exchanger according to claim 1, wherein the header includes two lateral folded walls, to encompass and stack the at least one internal plate and the rear cover all together.

8. The high pressure heat exchanger according to claim 1, wherein each slot of the header has a tapered shape to guide the tube end sections during their insertion.

9. The high pressure heat exchanger according to claim 1, wherein the at least one internal plate is brazed with the header.

10. A high pressure heat exchanger according to claim 1, wherein the at least one internal plate has slots to form flow paths within the first manifold, these slots communicating each with another to form the flow paths.

11. The high pressure heat exchanger according to claim 1, wherein the refrigerant flow path is deviated at least once in the shape of a U.

12. The high pressure heat exchanger according to claim 1, wherein the tubes have refrigerant channels with a ratio of at least 0.3 between their wall thickness and the diameter.

13. The high pressure heat exchanger according to claim 1, wherein at least one tube has at least two refrigerant channels with a web placed therebetween and having a width equal to at least 40% of the diameter of the refrigerant channels.

14. The high pressure heat exchanger according to claim 1, wherein the high pressure heat exchanger is a chiller.

15. The high pressure heat exchanger according to claim 1, wherein a connecting block is attached to the first manifold or the second manifold.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0057] Examples of the invention will be apparent from and described in detail with reference to the accompanying drawings, in which:

[0058] FIG. 1 shows a known heat exchanger with flat tubes in partial cross-section;

[0059] FIG. 2 shows the heat exchanger of FIG. 1 in greater detail;

[0060] FIG. 3 shows a heat exchanger according to the invention in a first embodiment;

[0061] FIG. 4 shows a heat exchanger according to the invention in a second embodiment;

[0062] FIG. 5 shows a heat exchanger according to the invention in a third embodiment;

[0063] FIG. 6 shows a heat exchanger according to the invention in another embodiment;

[0064] FIG. 7 shows a heat exchanger according to the invention in another embodiment;

[0065] FIG. 8 shows a heat exchanger according to the invention in another embodiment; and

[0066] FIG. 9 shows a heat exchanger according to the invention in another embodiment.

DETAILED DESCRIPTION OF THE INVENTION

[0067] FIG. 1 shows a known heat exchanger 1 with flat tubes 11 in partial cross-section. The heat exchanger 1 comprises a plurality of flat tubes 11 for guiding the first fluid, in particular a fluid operating at high pressure, for example R744. These tubes 11 are connected at their end portions with manifolds 10a, 10b. The flat tubes 11 are arranged in horizontally parallel rows so that the first fluid can enter through the block 30 into the first manifold 10a, travel through the first column of tubes 11, reach the second manifold 10b and make a U-turn, returning to the first manifold 10a via second column of tubes 11, and then exit through outlet channel in the manifold 10a and the connecting block 30.

[0068] FIG. 2 shows the heat exchanger of FIG. 1 in greater detail. The flat tubes 11 are placed in slots 13 of the manifold 10b (in a consecutive manner along the vertical direction). The other ends of the tubes 11 are situated in manifold 10a in an analogous manner. The heat exchanger 1 further comprises flow disruptors 15, which disrupt the flow of the second fluid, in order to improve the heat exchange with the first fluid. The tube height h1 is slightly smaller than manifold material height h3 between consecutive slots 13. The flow disruptor 15 has a height h2. As the height of the disruptor 15 approaches the h1 value, h3 also decreases, which is detrimental to the manifolds strength. The following embodiments propose avoiding this negative dependency.

[0069] FIG. 3 shows a heat exchanger according to the invention in a first embodiment. The example is explained relative to manifold 10b, but this description applies to manifold 10a in an analogous manner. A plurality of tube sets 20, each comprising a first tube 11 and a second tube 12, is arranged along the manifold 10b in a spaced manner. Each of the first and the second tubes 11, 12 comprises an intermediate tube section 11a between two opposing tube end sections 11b. The manifolds 10a, 10b comprise slots 13, in which the tube end sections 11b of tubes 11, 12 are mounted in a fluid-tight manner. Within the tube set 20, at least the first tube 11 comprises a bent tube section 11c between the tube end section 11b and the intermediate tube section 11 a. The intermediate tube sections 11a of the first and second tubes 11, 12 then run substantially in a parallel and spaced manner to each other, while the tube end sections 11b are stacked on each other within a single slot 13. Because at least one of the tubes 11, 12 is bent in this manner, the distance between the consecutive slots 13 is enlarged. It is therefore clear that by the term ‘bent’ it is understood any shape which allows providing two sections of the tube 11, preceding the bend and following the bend, which would run in parallel but in shifted relation, as shown in the drawings. For example, the first tube 11 is bent so that it has two opposing bends (i.e. forms a chicane). Preferably, the tube bent section 11c is located close to the tube end section 11b. Consequently, the disruptors 15 can occupy most of the space between the tubes 11, 12 and prevent excessive by-passing of the second fluid. In the example of FIG. 3, the second tube 12 is a straight (i.e. non bent) flat tube, which nevertheless comprises an intermediate portion 11a and a tube end section 11b, the tube end section 10b being placed in the slot 13.

[0070] The arrangement according to the invention improves mechanical resistance of the header 103, and at the same time allows application of known, standard flow disrupters 15. The number of tubes 11, 12 applied along the manifold consequently can also be greater.

[0071] FIG. 4 shows a heat exchanger according to the invention in a second embodiment. This embodiment differs from the first embodiment in that a third tube 16 is present in the tube set 20. It has the same shape as the first tube 11, but is arranged inversely and stacked below the second tube 12.

[0072] For embodiment with three tubes 11, 12, 13 in one header slot 13, the overall tube height h1 is preferably between 3 mm and 4.5 mm, the flow disruptor height h2 is between 1.7 mm and 2.5 mm, and the material height h3 between the consecutive tube slots 13 is (3*h2)−a, a being between 0.4 and 0.8 mm.

[0073] For the above examples, the boundary values of the ranges are understood to be not

[0074] excluded.

[0075] FIG. 5 shows a heat exchanger according to the invention in a third embodiment. It differs from the previous embodiments in that both the first tube 11 and the second tube 12 comprise tube bent sections 11c, and there is no flat tube between them. The disruptors 15 can be located between the tubes 11, 12 and/or between the consecutive tube sets 20.

[0076] For embodiments with two tubes 11, 12 in one header slot 13, the overall tube height h1 is preferably between 2 mm and 3 mm, the flow disruptor height h2 is between 1.7 mm and 2.5 mm, and the material height h3 between the consecutive tube slots 13 is (2*h2)−a, a being between 0.4 and 0.8 mm.

[0077] For the above examples, the boundary values of the ranges are understood to be not excluded.

[0078] The spaces between the tubes 11, 12, 13 in a tube set 20 can have equal height to the spaces between the tube sets 20. This can enable applying identical flow distributors 15.

[0079] Other variations to the disclosed embodiments can be understood and effected by those skilled in the art in practicing the claimed invention, from a study of drawings, the disclosure, and the appended claims. The mere fact that certain measures are recited in mutually different dependent claims does not indicate that a combination of these measures cannot be used to the advantage.

[0080] FIGS. 6 to 8 discloses another embodiment of the invention.

[0081] A high pressure heat exchanger 100 is shown on FIGS. 6 to 8. The high pressure heat exchanger 100 comprises a first manifold 101 and a second manifold (not shown) connected fluidly by a plurality of tube sets 20 arranged in a spaced manner along the the first manifold 101 and the second manifold, wherein the first manifold 101 comprises a rear cover 102, a header 103 with slots 104 receiving tube end sections 11b of the tube sets 20 and internal plates 105 interposed between the header 103 and the rear cover 102 and configured to create a flow path 106 within the first manifold 101, this flow path being in fluid connection with the tubes 11 to allow a circulation of a refrigerant in the tubes and the manifold 101.

[0082] The header 103 has preferably a first area 110 adjacent to each slot 104 and having a first thickness w1 and a second area 111 surrounding the first area 110 and having a second thickness w2, the first thickness w1 being smaller than the second thickness w2.

[0083] Each slot 104 of the header 103 is adjacent to the first areas 110 with the first thickness so that that the thickness of the header 103 is locally smaller, around the slots 104, than in the rest of the header 103.

[0084] In the first area 110, the thickness has a minimum value w1min on the side adjacent with the slot 104.

[0085] First thickness w1 may be variable from a minimum value w1min at the contact with the tube 11 in the slot 104 up to the second thickness w2. This may be advantageous to form a tapered guiding shape 125.

[0086] The heat exchanger has the following ratios: 3<h/w1<h/(c*60%), in particular 3<h/w1<h/c where h is the height of the distribution channel of the manifold and w1 is the wall thickness of the header 103 in the first zone, where thickness w1 is minimum in the first area, and c is smallest wall thickness in tubes 11.

[0087] When w1 is variable in the first area 110, w1 is taken as its smallest value w1min in the first area 110.

[0088] Dimensions h, w1 and w2 are measured relatively to the same axis perpendicular to the plane of the internal plates 105.

[0089] The first manifold 101 comprises a plurality of internal pates 105 stacked together, which may be in number of 3.

[0090] The internal plates 105 have internal slots 115 extending in different directions, in particular perpendicular directions so as to create U form flow paths.

[0091] Some internal plates 105 can have parallel longitudinal internal slots 115, in particular forming group of two slots, these two slots 115 being aligned.

[0092] Two of the internal plates 105 have parallel internal slots 115 and one of the internal plate 105 has internal slots 115 perpendicular to the internal slots 115 of the two other internal plates 105.

[0093] The internal plates 105 are flat stamped plates.

[0094] The internal pates 105 create internal channels for distribution of refrigerant.

[0095] The rear cover 102 works as a closing plate, preventing from leak of refrigerant outside the first manifold 101 region.

[0096] The rear cover 102 is configured to close the internal slots 115 of the adjacent internal

[0097] plate 105.

[0098] The header 103 is configured to stick together all internal plates 105 in position before and during brazing process.

[0099] The header 103 comprises two folded lateral walls 117, to encompass and stack the internal plates 105 and the rear cover 102 all together. The slots 104 are formed on a flat main wall 118 of the header 103. The lateral walls 117 are connected to this main wall 118.

[0100] The header 103 forms a part with an accurate shape of slots 104 in order to create a brazing connection with the tubes 11.

[0101] The header 103 is configured with a shape ensuring proper guiding of tubes 11 into the slots 104 during assembly of heat exchanger core.

[0102] Each slot 104 has a tapered shape 125 to guide the tubes 11 during their insertion.

[0103] The guiding shape may be of a rectilinear shape 126 on the bottom of FIG. 9, or of a rounded shape 125 on the top of FIG. 9.

[0104] The header 103 can have globally small thickness in order to easier bend it around other plates and have as small radiuses in the corners as possible.

[0105] In parallel the invention makes it possible not to increase the thickness of the first manifold 101 too much in order to cut the slots 104 precisely without creating major deformations.

[0106] The header 103 can be made in stamping process.

[0107] The distance between slots 104 on the header 103 is sufficient, for instance above 7 mm, and the size of the slots 104 is relatively small, so that it is possible to punch the slots 104 in a way to create drafted angles for guiding the tubes 11 during assembly.

[0108] The internal plates 105 are configured to support the structure between the slots 104.

[0109] The internal plate 105 is brazed with the header 103.

[0110] The internal plates 105 enable to withstand high pressure despite limited thickness of header 103 in order to create the guiding surfaces in the first area 110 of small thickness.

[0111] The internal plates 105 have internal slots 115 to form flow paths within the first manifold 101, these internal slots 115 communicating each with another in a certain manner to form the flow paths.

[0112] The invention, in particular thanks to internal plates 105, enables to create a robust structure of the first manifold 101, for instance which is able to withstand pressure up to 26 MPa or even bigger for other applications. The invention also enables to use an assembly of parts made using reasonably cheap serial processes such as stamped components instead of machining components.

[0113] The heat exchanger 100 comprises rows of tubes 11 connecting the first manifold 101 and the second manifold and forming an inlet row and an outlet row for refrigerant.

[0114] The refrigerant is flowing from an inlet through the second manifold to first row of the tubes 11. Then the refrigerant is flowing through the tubes 11 to opposite first manifold 101 where the refrigerant is transferred from first row of the tubes 11 to the second row of the tubes 11. Then the refrigerant is flowing through the second row to the second manifold having IN/OUT connections and to the connecting block ensuring tight hydraulic connection with the rest of the system.

[0115] The heat exchanger 100 for cooling a heat source of a motor vehicle has coolant channels forming a coolant flow path and refrigerant channels 120 forming a refrigerant flow path.

[0116] The refrigerant flow path is deviated at least once in the shape of a U.

[0117] The refrigerant channels 120 in the tubes 11 have a ratio of at least 0.3 between their wall thickness and their diameter.

[0118] A web 121 is placed between two refrigerant channels 120 in the tubes 11 and has a width b equal to at least 40% of the diameter of the refrigerant channel 120.

[0119] Internal plates 105, header 103 and rear cover 102 can be made of metal.

[0120] The heat exchanger 100 is a chiller.

[0121] According to one aspect of the invention, the refrigerant is CO2. However, the invention is not limited to such a refrigerant.

[0122] According to one aspect of the invention, the connecting block is attached to the first manifold 101 or the second manifold.