This invention relates to heat exchangers, and more particularly to heat exchangers that utilize a header plate to receive the ends of flattened heat exchanger tubes for use in distributing the working fluid to and from the interior of the heat exchanger tubes.
In heat exchangers that utilize flattened tubes, it is known to provide header plates that have pierced tube receiving openings with flanges or collars surrounding the openings and conforming to the tube ends received in the openings so as to reduce the stress risers at the interfaces between the tubes and the header plate. It is also known for the flanges or collars to either extend into the fluid tank or manifold associated with the header plate or to extend away from (i.e., towards the core of the heat exchanger) the fluid tank or manifold associated with the header plate is attached. While the known designs may have proven adequate for their current applications, there is a continuous push to increase the design limits of heat exchanges in an effort to improve performance, compactness, life, etc., and because of this, there is a continuing need to improve the design of header plates and the associated heat exchangers.
In accordance with one feature of the invention, a header plate is provided for receiving the flattened tubes of a heat exchanger core, each of the flattened tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. A blend radius R1 is provided at the interface between a central portion of each of the long side walls and the base wall. A blend radius R2 is also provided at the interface between each of the short side walls and the base wall. R2 is in the range of 1.25×R1 to 5×R1.
In one feature of the invention, a header plate is provided for receiving the flattened tubes of a heat exchanger core, each of the flattened tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. A blend radius is provided at the interface between the flange and the base wall, the blend radius having a size that increases from a radius R1 central to the length of the long side walls to a radius R2 central to he length of the short side walls, with R2 being in the range of 1.25×R1 to 5×R1.
In accordance with one feature of the invention, a heat exchanger includes a header plate, and a plurality of spaced, parallel, flattened tubes, each of the tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. A blend radius R1 is provided at the interface between a central portion of each of the long side walls and the base wall. A blend radius R2 is also provided at the interface between each of the short side walls and the base wall. R2 is in the range of 1.25×R1 to 5×R1.
According to one feature of the invention, a heat exchanger includes a header plate, and a plurality of spaced, parallel, flattened tubes, each of the tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. A blend radius is provided at the interface between the flange and the base wall, the blend radius having a size that increases from a radius R1 central to the length of the long side walls to a radius R2 central to the length of the short side walls, with R2 being in the range of 1.25×R1 to 5×R1.
As one feature of the invention, a header plate is provided for receiving the flattened tubes of a heat exchanger core, each of the flattened tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. The broad side walls are flared away from each other as they extend away from the base wall and a blend radius R1 is provided at the interface between a central portion of each of the long side walls and the base wall. A blend radius R2 is also provided at the interface between each of the short side walls and the base wall. R2 is in the range of 1.25×R1 to 5×R1.
In one feature of the invention, a header plate is provided for receiving the flattened tubes of a heat exchanger core, each of the flattened tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. The broad side walls are flared away from each other as they extend away from the base wall and a blend radius is provided at the interface between the flange and the base wall, the blend radius having a size that increases from a radius R1 central to the length of the long side walls to a radius R2 central to he length of the short side walls, with R2 being in the range of 1.25×R1 to 5×R1.
In accordance with one feature of the invention, a heat exchanger includes a header plate, and a plurality of spaced, parallel, flattened tubes, each of the tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. The broad side walls are flared away from each other as they extend away from the base wall and a blend radius R1 is provided at the interface between a central portion of each of the long side walls and the base wall. A blend radius R2 is also provided at the interface between each of the short side walls and the base wall. R2 is in the range of 1.25×R1 to 5×R1.
According to one feature of the invention, a heat exchanger includes a header plate, and a plurality of spaced, parallel, flattened tubes, each of the tubes having an exterior cross section defined by a pair of broad side walls joined by a pair of shorter nose walls. The header plate includes a planar base wall, and a plurality of tube receiving openings in the base wall, each of the openings surrounded by a flange (collar) extending from the base wall towards the core to surround the exterior cross section of a flattened tube received in the opening. The flange is shaped to conform to the exterior cross section and has a pair of long side walls that conform to the broad side walls of the flattened tube and a pair of short side walls that conform to the nose walls of the flattened tube. The broad side walls are flared away from each other as they extend away from the base wall and a blend radius is provided at the interface between the flange and the base wall, the blend radius having a size that increases from a radius R1 central to the length of the long side walls to a radius R2 central to the length of the short side walls, with R2 being in the range of 1.25×R1 to 5×R1.
In one feature, R2 is at least equal to or greater than 2×R1.
As one feature, R2 is at least 3.0 mm.
According to one feature, the base wall has a thickness of about 2.5 mm, the walls of the flange have a thickness of about 0.71 mm, R1 is about 1.5 mm, R2 is about 3 mm, and the flange has a height above the base wall in the range of about 7.0 mm to about 6.2 mm.
In accordance with one feature, a blend radius RT is provided at the interface between the base wall and portions of each of the long side walls adjacent the short side walls, the blend radius RT decreasing from R2 to R1 as the interface extends from corresponding short side wall toward the central portion of the corresponding long side wall.
Other objects, features, and advantages of the invention will become apparent from a review of the entire specification, including the appended claims and drawings.
With reference to
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Preferably, R2 is in the range of 1.25×R1 to 5×R1 and, in one highly preferred embodiment, analysis has shown that R2 should be equal to about 2×R1. In one very specific embodiment, the base wall 24 has a thickness TB of about 2.5 mm (0.098 inch), the walls 30 and 32 of the flange 28 have a thickness TF of about 0.71 mm (0.028 inch), R1 is about 1.5 mm (0.059 inch), R2 is about 3 mm (0.12 inch), and the flange 28 has a height HF above the base wall 24 in the range of about 7 mm (0.28 inch) to about 6.2 mm (0.24 inch). As used herein, the terms “about” or “nominally” are intended to indicate a range around the stated number that is generated by the conventional tolerances associated with the manufacturing technique used to make the header plate 20.
Preferably, the header plate 20 is formed using known pierce/flange stamp tooling methods wherein the opening 26 is pierced and then the flange 28 is formed using suitable stamp tooling. It is also preferred that the header plate be made of a suitable aluminum material. However, in some applications it may be desirable to utilize other manufacturing methods and other materials for the header plate 20.
With reference to
It has been determined through analysis that by varying the blend radius R at the interface between the flange 28 and the base wall 24, an improved distribution of thermal and pressure loads can be achieved at the tube to header joint, and can also result in improved thermal and pressure life cycles for the header plate 20 and the associated heat exchanger 10. Furthermore, when the header plate 20 is formed by piercing the openings 26 and using stamp tooling methods to form the flange 28, the variations in the blend radius R as described above tends to limit or prevent cracking or tearing of the material of the header plate 20 during formation of the flanges 28.