Stacked plate heat exchanger

Abstract

A stacked plate heat exchanger for a motor vehicle may include a plurality of elongated plates stacked on one another between which a plurality of cavities are disposed alternately for two media. The plurality of cavities may be respectively delimited by a respective plate of the plurality of plates zonally by a plate surface and a surrounding wall. The respective plate may include two flow openings, two passage openings, and two domes respectively arranged around one of the two passage openings. At least of one of the plurality of plates may further include an elongated separation shaping arranged on the plate surface, projecting into the respective cavity, and extending from the first short side between the two flow openings in a direction of the second short side. The separation shaping may adjoin the first short side at an angle α of 45° to 90°.

Claims

1. A stacked plate heat exchanger for a motor vehicle, comprising: a plurality of elongated plates stacked on one another, between which a plurality of cavities are disposed alternately for two media; the plurality of cavities respectively delimited by a respective plate of the plurality of plates zonally by a plate surface of the respective plate and a surrounding wall projecting from and surrounding the plate surface; the respective plate including two flow openings adjacently disposed at a first short side and two passage openings adjacently disposed at a second short side opposite the first short side; the respective plate further including two domes respectively arranged around one of the two passage openings, the two domes projecting from the plate surface into a respective cavity of the plurality of cavities; wherein at least of one of the plurality of plates further includes an elongated separation shaping arranged on the plate surface and projecting into the respective cavity, the separation shaping extending from the first short side between the two flow openings in a direction of the second short side; wherein the separation shaping has at least two sections that extend transversely relative to one another and define an angle β therebetween; and wherein the separation shaping adjoins the first short side at an angle α of 45° to 90°.

2. The stacked plate heat exchanger according to claim 1, wherein the separation shaping is one of rectilinear and curved towards a long side of the respective plate connecting the first short side and the second short side.

3. The stacked plate heat exchanger according to claim 1, wherein: the separation shaping has at least two rectilinear separation regions which adjoin one another and extend at the bend angle β relative to one another; and a ratio of a length of one of the two separation regions to a total length of the separation shaping is 0 to 1.

4. The stacked plate heat exchanger according to claim 1, wherein the separation shaping divides the first short side into two regions such that a ratio of a length of one of the two regions to a total length of the first short side is 0.3 to 0.5.

5. The stacked plate heat exchanger according to claim 1, wherein the separation shaping extends, from the first short side in the direction of the second short side, a length of 0.2 times to 0.8 times a length of a long side of the respective plate connecting the first short side and the second short side.

6. The stacked plate heat exchanger according to claim 1, further comprising at least one flow guide structure arranged in the respective cavity of at least one of the plurality of plates.

7. The stacked plate heat exchanger according to claim 6, wherein at least one of: the at least one flow guide structure is a turbulence insert; and the at least one flow guide structure projects from the plate surface of the at least one of the plurality of plates into the respective cavity and includes at least one of a plurality of nub-like shapings, a plurality of elongated shapings, and a plurality of undulating shapings.

8. The stacked plate heat exchanger according to claim 6, wherein: the at least one flow guide structure includes at least two flow guide structures; at least one of the plurality of plates includes both the at least two flow guide structures and the separation shaping, the at least two flow guide structures arranged on opposite sides of the separation shaping; and the at least two flow guide structures are configured one of identically and differently.

9. The stacked plate heat exchanger according to claim 6, wherein the at least one flow guide structure projects from the plate surface of the at least one of the plurality of plates into the respective cavity and includes a plurality of undulating shapings that define a chevron-like pattern.

10. The stacked plate heat exchanger according to claim 1, wherein at least one of the two flow openings and the two passage openings of at least one of the plurality of plates have a respective flow cross-sectional area differing from one another.

11. The stacked plate heat exchanger according to claim 1, wherein: the two flow openings and the two passage openings of each of the plurality of plates, which are stacked on one another, correspond with one another fluidically; and a respective flow cross-sectional area of the two flow openings and of the two passage openings of each of the plurality of plates, which are stacked on one another, one of increase and decrease continuously from plate to plate such that a flow cross-sectional area of a flow channel defined by the two flow openings of each of the plurality of plates and a flow cross-sectional area of a passage channel defined by the two passage openings of each of the plurality of plates one of increases and decreases continuously.

12. The stacked plate heat exchanger according to claim 1, wherein at least a portion of the separation shaping is rectilinear.

13. The stacked plate heat exchanger according to claim 1, wherein the separation shaping is curved towards a long side of the respective plate connecting the first short side and the second short side.

14. The stacked plate heat exchanger according to claim 1, wherein: the surrounding wall extends along an outer perimeter of the respective plate; the separation shaping projects from the surrounding wall at the first short side and extends between the two flow openings; and the two flow openings are disposed spaced apart from the surrounding wall at the first short side and a portion of the plate surface extends between the two flow openings and the surrounding wall at the first short side.

15. A stacked plate heat exchanger for a motor vehicle, comprising: a plurality of elongated plates stacked on one another, between which a plurality of cavities are disposed alternately for two media; each of the plurality of plates including: a first short side and a second short side disposed opposite the first short side; a plate surface; a surrounding wall projecting from and surrounding the plate surface, the plate surface and the surrounding wall delimiting a respective cavity of the plurality of cavities; two flow openings disposed in the plate surface adjacent to one another in a region of the first short side; two passage openings disposed in the plate surface adjacent to one another in a region of the second short side; and two domes respectively arranged around one of the two passage openings and projecting from the plate surface into the respective cavity; wherein at least one plate of the plurality of plates further includes an elongated separation shaping arranged on the plate surface and projecting into the respective cavity, the separation shaping extending from the first short side in a direction of the second short side between the two flow openings; wherein the separation shaping adjoins the first short side at an angle α of 45° to 90°; and wherein the separation shaping includes at least two rectilinear separation portions extending transversely to one another at a bend angle β.

16. The stacked plate heat exchanger according to claim 15, wherein: at least one of the plurality of plates includes at least one flow guide structure projecting from the plate surface into the respective cavity; and the at least one flow guide includes at least one of a plurality of nub-like shapings, a plurality of elongated shapings, and a plurality of undulating shapings.

17. The stacked plate heat exchanger according to claim 15, wherein: the two flow openings and the two passage openings of each of the plurality of plates correspond with one another fluidically; and a respective flow cross-sectional area of the two flow openings and of the two passage openings one of increase and decrease continuously from plate to plate of the plurality of plates such that a flow cross-sectional area of a flow channel defined by the two flow openings of each of the plurality of plates and a flow cross-sectional area of a passage channel defined by the two passage openings of each of the plurality of plates one of increases and decreases continuously.

18. A stacked plate heat exchanger for a motor vehicle, comprising: a plurality of elongated plates stacked on one another, between which a plurality of cavities are disposed alternately for two media; the plurality of cavities respectively delimited by a respective plate of the plurality of plates zonally by a plate surface of the respective plate and a surrounding wall projecting from and surrounding an outer perimeter of the respective plate; the respective plate including two flow openings adjacently disposed at a first short side and two passage openings adjacently disposed at a second short side opposite the first short side; the respective plate further including two domes respectively arranged around one of the two passage openings, the two domes projecting from the plate surface into a respective cavity of the plurality of cavities; wherein at least of one of the plurality of plates further includes an elongated separation shaping arranged on the plate surface and projecting into the respective cavity, the separation shaping projecting from the surrounding wall at the first short side and extending between the two flow openings in a direction of the second short side; and wherein the separation shaping has at least two sections that extend transversely relative to one another and define an angle β therebetween.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) There are shown, respectively diagrammatically

(2) FIG. 1 shows a view of a plate in a stacked plate heat exchanger according to the invention, which has a rectilinear separation shaping;

(3) FIG. 2 shows a view of a plate in a stacked plate heat exchanger according to the invention, which has a separation shaping with two separation regions;

(4) FIG. 3 shows a view of a plate in a stacked plate heat exchanger according to the invention, in which a separation shaping adjoins a short side centrally;

(5) FIG. 4 shows a view of a plate in a stacked plate heat exchanger according to the invention, which has a turbulence insert;

(6) FIG. 5 shows a view of a plate in a stacked plate heat exchanger according to the invention, which has an identical flow guide structure on both sides on a separation shaping.

(7) FIGS. 6A and 6B show a simplified illustration of a cross-section of a stacked plate heat exchanger in a region of the flow openings and a region of the passage openings, respectively;

(8) FIGS. 7A and 7B show a simplified illustration of a cross-section of a stacked plate heat exchanger in a region of the flow openings and a region of the passage openings, respectively.

DETAILED DESCRIPTION

(9) FIG. 1 shows a view of a plate 1 in a stacked plate heat exchanger 2 according to the invention. On the respective plate 1, a cavity 3 is delimited zonally by a plate surface 4 and a surrounding wall 5, which projects from the plate surface 4 and runs around the latter. The stacked plate heat exchanger 2 has several such plates 1 stacked on one another, between which the cavities 3 are formed. In particular, the stacked plate heat exchanger 2 can be an oil cooler, a chiller or a condenser for a motor vehicle.

(10) The respective plate 1 is shaped so as to be elongate and has a first short side 6a and a second short side 6b lying opposite the first short side 6a. The two short sides 6a and 6b are connected with one another by two opposite long sides 7a and 7b. The short sides 6a and 6b and the long sides 7a and 7b delimit the plate surface 4. On the first short side 6a, two flow openings 8a and 8b are formed. A first medium M.sub.1 can flow through the flow openings 8a and 8b into the cavity 3 and can flow out from the cavity 3. On the second short side 6b, two passage openings 9a and 9b are arranged, around which respectively a dome 10a and 10b is formed, projecting from the plate surface 4 into the cavity 3. The domes 10a and 10b prevent an inflow of a second medium M.sub.2 into the cavity 3 and an outflow of the first medium M.sub.1 out from the cavity 3. The flow openings 8a and 8b and the passage openings 9a and 9b alternate in the plates 1 of the stacked plate heat exchanger 2 which lie on one another, so that in the stacked cavities 3 respectively the first medium M.sub.1 or the second medium M.sub.2 flows. As generally shown in FIGS. 6A, 6B, 7A, and 7B, provision can be made that the flow openings 8a, 8b and/or the passage openings 9a, 9b at least of one of the plates 1 have a flow cross-section differing from one another. In addition, the flow openings 8a, 8b and the passage openings 9a, 9b of the plates 1 which are stacked on one another can correspond with one another fluidically, and flow cross-sections of the flow- and passage openings 8a, 8b, 9a, 9b of the plates 1 which are stacked on one another in the stacked plate heat exchanger 2 can continuously increase or decrease from plate 1 to plate 1. In this advantageous manner, a flow cross-section of a channel 12a, 12b, 15a, 15b formed by the flow- and passage openings 8a, 8b, 9a, 9b can continuously increase or decrease. The ratio of the minimum flow cross-section to the maximum flow cross-section of the respective channel 12a, 12b, 15a, 15b can lie here between 0.25 and 1. In this advantageous manner, the flow cross-section of the respective channel 12a, 12b, 15a, 15b can also be adapted to the aggregate state of the through-flowing medium.

(11) On the plate surface 4, an elongate separation shaping 11—a so-called bead—is formed projecting into the cavity 3, which bead extends from the first short side 6a between the two flow openings 8a and 8b in the direction of the second short side 6b. Here, the separation shaping 11 adjoins the first short side 6a at an angle α, which lies preferably between 45° and 90°. In this example embodiment, the separation shaping 11 is rectilinear and adjoins the first short side 6a at an angle α equal to 60°. The separation shaping 11 divides the first short side 6a in a ratio of 0.3 to the total length of the first short side 6a and extends from the first short side 6a in the direction of the second short side 6b up 0.8 times the length of the long sides 7a and 7b.

(12) The separation shaping 11 divides the plate surface 4 into two flow regions 4a and 4b, which have an unequal flow cross-section. From a feed channel 12a, the first medium M.sub.1 flows through the first flow opening 8a into the first flow region 4a and further in the direction of the second short side 6b. At the second short side 6b, the first medium M.sub.1 is diverted and flows in the second flow region 4b to the flow opening 8b and into the discharge channel 12b. The first medium M.sub.1 flows in the plate 1 in a u-shaped manner, as indicated here and further by arrows, and the flow cross-section decreases in the flow direction from the flow opening 8a to the flow opening 8b. The flow cross-section is thereby adapted to the aggregate state of the first medium M.sub.1, which changes here from gaseous to liquid, as in a condenser. In particular, the output- and pressure ratio can thereby be optimized in the stacked plate heat exchanger 2, and the volume of the first medium M.sub.1 available for the heat exchange can be utilized optimally. In addition, the flow openings 8a and 8b also have flow cross-sections differing from one another and adapted to the aggregate state of the first medium M.sub.1. It shall be understood that the flow cross-section in the plate 1 and the flow cross-sections of the flow openings 8a and 8b can also be adapted to a first medium M.sub.1, which changes the aggregate state from liquid to gaseous—such as for example in a chiller or an evaporator.

(13) In addition, in the flow region 4a a first flow guide structure 13a is arranged, and in the flow region 4b a second flow guide structure 13b is arranged. In this example embodiment, the first flow guide structure 13a comprises several nubs 14, which are formed integrally—stamped, for example—in the plate surface 4 in the flow region 4a, and project into the cavity 3. In this example embodiment, the second flow guide structure 13b is formed in an undulating manner and integrally—stamped, for example—on the plate surface 4, and expediently projects into the cavity 3. The flow guide structures 13a and 13b guide and mix the first medium M.sub.1 at the plate 1, and the heat exchange can thereby be intensified. In addition, the separation shaping 11 is formed zonally on the second flow structure 13b, so that an unimpeded throughflow of the first medium M.sub.1 is prevented at the separation shaping 11.

(14) It shall be understood that plates for the second medium M.sub.2 can be configured in an identical manner. At the plate 1 shown here, however, the second medium M.sub.2 does not flow, and is delivered through a feed channel 15a of the first throughflow opening 9a and a discharge channel 15b of the second throughflow opening 9b into a cavity of a next plate, as is indicated here and further by arrows.

(15) FIG. 2 shows a view of the alternatively configured plate 1 in the stacked plate heat exchanger 2 according to the invention. In this example embodiment, the separation shaping 11 has two rectilinear separation regions 11a and 11b, which adjoin one another at a bend angle β. The bend angle β here is approximately 160°, and a ratio of the length of the shorter separation region 11a to the total length of the separation shaping 11 lies at approximately 0.3. Accordingly, a ratio of the length of the longer separation region 11b to the total length of the separation shaping 11 is approximately 0.7. In the flow regions 4a and 4b respectively a flow guide structure 13a and 13b are arranged. The first flow guide structure 13a comprises several nubs 14, and the second flow guide structure 13b is shaped in an undulating manner. In this example embodiment, the flow cross-sections of the flow openings 8a and 8b are identical.

(16) FIG. 3 shows a view of the alternatively configured plate 1 in the stacked plate heat exchanger 2 according to the invention. In this example embodiment, the separation shaping 11 adjoins the first short side 6a with the angle α close to 90°. In the flow region 4a, the flow guide structure 13a is formed with several nubs 14, and in the flow region 4b the second undulating flow guide structure 13b is formed.

(17) FIG. 4 shows a view of the alternatively configured plate 1 in the stacked plate heat exchanger 2 according to the invention. In the flow region 4a, the flow guide structure 13a is arranged in the form of a turbulence insert 16, and in the flow region 4b the second undulating flow guide structure 13b is formed. In this example embodiment, the separation shaping 11 adjoins the first short side 6a with the angle α close to 90°.

(18) FIG. 5 shows a view of the plate 1 in the stacked plate heat exchanger 2 according to the invention. Here, the two undulating flow guide structures 13a and 13b are configured in an identical manner and are formed mirror-symmetrically at the separation shaping 11. The separation shaping 11 adjoins the first short side with the angle α close to 90°.

(19) In summary, in the stacked plate heat exchanger 2 according to the invention, the flow cross-section in the respective plate 1 can be adapted to the aggregate state of the respective through-flowing medium M.sub.1 and M.sub.2. Thereby, the output- and pressure ratio in the stacked plate heat exchanger 2 can be optimized, and the volume of the respective medium M.sub.1 and M.sub.2 available for the heat exchange can be utilized optimally.