A HEAT EXCHANGER PLATE, AND A PLATE HEAT EXCHANGER
20230061944 · 2023-03-02
Assignee
Inventors
Cpc classification
F28F2225/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F3/042
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D9/005
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F3/10
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F3/046
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D2021/0071
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F28F3/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A plate heat exchanger comprises heat exchanger plates each comprising a heat exchanger area extending in parallel with an extension plane and comprising a corrugation extending from a primary level on one side of the extension plane to a secondary level on an opposite side of the extension plane. Four porthole areas enclose a respective porthole and comprise two first porthole areas comprising a respective annular base area around the porthole at the secondary level. Each first porthole area comprises a first annular ridge around the porthole and projecting from the annular base area to the primary level, and a second annular ridge around and at a distance from the first annular ridge and projecting from the annular base area to the primary level. The first and second annular ridges are through-broken by a number of depressions.
Claims
1. A heat exchanger plate to be comprised by a plate heat exchanger configured for heat exchange between a first fluid and a second fluid, the heat exchanger plate comprising a heat exchanger area extending in parallel with an extension plane of the heat exchanger plate and comprising a corrugation of ridges and valleys, wherein the corrugation extends from a primary level on one side of the extension plane to a secondary level on an opposite side of the extension plane, an edge area extending around the heat exchanger area, and a number of porthole areas located inside the edge area and each enclosing a respective porthole defined by a porthole edge and extending through the heat exchanger plate, that porthole areas comprise two first porthole areas comprising a respective annular base area extending around the porthole and being located at the secondary level, that each of the first porthole areas comprises a first annular ridge provided around the porthole and projecting from the annular base area at the secondary level to the primary level, and a second annular ridge provided around and at a distance from the first annular ridge and projecting from the annular base area at the secondary level to the primary level, and that each of the first and second annular ridges is through-broken by a number of depressions.
2. A heat exchanger plate according to claim 1, wherein the depressions of the first annular ridge and the second annular ridge form a fluid communication path through the first and second annular ridges.
3. A heat exchanger plate according to claim 1, wherein the first annular ridge of each of the first porthole areas is located at a distance from the porthole edge of the respective porthole.
4. A heat exchanger plate according to claim 1, wherein any one of said number of depressions extending through the first annular ridge is displaced from any radial line of the porthole that extends through the any one of said number of depressions extending through the second annular ridge so that any one of said number of depressions extending through the first annular ridge is located opposite to a portion of the second annular ridge that has no depression.
5. A heat exchanger plate according to claim 1, wherein each of the first porthole areas comprises a third annular ridge provided around and at a distance from the second annular ridge and projecting from annular base area at the secondary level to the primary level.
6. A heat exchanger plate according to claim 5, wherein the third annular ridges is through-broken by a number of depressions.
7. A heat exchanger plate according to claim 6, wherein the depressions of the third annular ridge form a fluid communication path through the third annular ridge.
8. A heat exchanger plate according to claim 6, wherein any radial line of the porthole of the first porthole areas extends through at most two depressions.
9. A heat exchanger plate according to claim 1, wherein the depressions extend to the secondary level.
10. A heat exchanger plate according to claim 1, wherein the number of depressions is at least one and at most ten, at most nine, at most eight, at most seven or at most six.
11. A heat exchanger plate according to claim 1, wherein each depression has a width in parallel with a peripheral direction of the porthole edges and a length perpendicular to the width, and wherein the width is in the order of the length.
12. A plate heat exchanger for evaporation, comprising a plurality of heat exchanger plates according to claim 1, wherein the heat exchanger plates form first plate interspaces for the first fluid and second plate interspaces for the second fluid.
13. A plate heat exchanger according to claim 12, wherein the heat exchanger plates are permanently joined to each other through brazing.
14. A plate heat exchanger according to claim 12, wherein at least one of the first and second fluid is carbon dioxide.
15. A plate heat exchanger according to claim 12, wherein every second heat exchanger plate of the plate heat exchanger is arranged so that an upper surface the first annular ridge of one heat exchanger plate adjoins an upper surface of the first annular ridge of an adjacent heat exchanger plate.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0030] The present invention is now to be explained more closely through a description of various embodiments and with reference to the drawings attached hereto.
[0031]
[0032]
[0033]
[0034]
[0035]
[0036]
[0037]
[0038]
DETAILED DESCRIPTION OF VARIOUS EMBODIMENTS
[0039]
[0040] Each of the heat exchanger plates 2, the first end plate 3 and the second end plate 4 extends along a longitudinal central axis x, indicated in
[0041] Each of the heat exchanger plates 2, the first end plate 3, and the second end plate 4 extends in parallel with a respective extension plane p, indicated in
[0042] The heat exchanger plates 2 of the plate package 5 may be permanently joined to each other, and to the first and second end plates 3 and 4, for instance by means of a brazing material and through a brazing process.
[0043] Each of the heat exchanger plates 2, see
[0044] The heat exchanger plates 2 are stacked onto each other in the plate package 5 to form first plate interspaces 8 for a first fluid and second plate interspaces 9 for a second fluid. The first and second plate interspaces 8 and 9 are arranged in an alternating order in the plate package 5, as illustrated in
[0045] Each of the heat exchanger plates 2 also comprises an edge area 10 extending around and enclosing the heat exchanger area 6. The edge area 10 may adjoin the central area 6. The edge area 10 may consist of or may comprise a flange forming an angle of inclination to the extension plane p, see
[0046] In the embodiments disclosed, each of the heat exchanger plates 2 and the first end plate 3, comprises four porthole areas 11′, 11″ located inside the edge area 10 and each enclosing a respective porthole 12 defined by a porthole edge 13 and extending through the heat exchanger plate 2. The porthole areas 11′, 11″ comprise two first porthole areas 11′ and two second porthole areas 11″, see
[0047] In the embodiments disclosed, the portholes 12 of the first porthole areas 11′ are comprised by or form an inlet and an outlet, respectively, for the first fluid to and from the first plate interspaces 8. The portholes 12 of the second porthole areas 11″ are comprised by or form an inlet and an outlet, respectively, for the second fluid to and from the second plate interspaces 9. As illustrated in
[0048] Alternatively, the first porthole areas 11′ may be located diagonally opposite to each other. It follows that the second porthole areas 11″ then will be located diagonally opposite to each other.
[0049] In the embodiments disclosed, each of the porthole areas 11′, 11″ comprises an annular base area 14 extending around the porthole 12 to the porthole edge 13. The annular base area 14 may thus extend from the heat exchanger area 6 and/or the edge area 10 to the porthole edge 13. The annular base area 14 of the first porthole areas 11′ is located at or on the secondary level p″, see
[0050] In the first embodiment, each of the first porthole areas 11′ comprises a first annular ridge 21, a second annular ridge 22 and a third annular ridge 23, see
[0051] The first annular ridge 21 is provided around the porthole 12 and projects from the annular base area 14 at the secondary level p″ to the primary level p′.
[0052] The first annular ridge 21 may be located at a distance from the porthole edge 13 of the respective porthole 12. An inner annular portion of the annular base area 14 may thus be provided between the porthole edge 13 and the first annular ridge 21.
[0053] The second annular ridge 22 is provided around and at a distance from the first annular ridge 21 and projects from the annular base area 14 at the secondary level p″ up to the primary level p′. A first intermediate annular portion of the annular base area 14 may thus be provided between the first annular ridge 21 and the second annular ridge 22.
[0054] The third annular ridge 23 provided around and at a distance from the second annular ridge 22 and projects from annular base area 14 at the secondary level p″ up to the primary level p′. A second intermediate annular portion of the annular base area 14 may thus be provided between the second annular ridge 22 and the third annular ridge 23.
[0055] Each of the first, second and third annular ridges 21, 22, 23 has an upper surface located at the primary level p′. The upper surface may be flat, as schematically illustrated in
[0056] Each of the first, second and third annular ridges 21, 22, 23 is through-broken by a number of depressions 25, as can be seen in
[0057] The depressions 25 of the first, second and third annular ridges 21, 22, 23 extend from the upper surface at the primary level p′ to the secondary level p″, i.e. to the same level as the annular base area 14.
[0058] It should be noted that all or some of the depressions 25 of some or all of the first, second and third annular ridges 21, 22, 23 may extend from the upper surface at the primary level p′ to an intermediate level above, or at a distance from, the secondary level p″.
[0059] Each of the depressions 25 of the first, second and third annular ridges 21, 22, 23 has a width in parallel with a peripheral direction of the porthole edges 13 and a length in a radial direction perpendicular to the width. The width of the depressions 25 may be equal to, or in the order of, the length of the depressions 25.
[0060] Each of the first, second and third annular ridges 21, 22, 23 comprises at least one depression 25 in order to permit fluid flow from the porthole 12 to the plate interspace 8, 9 adjacent to the heat exchanger area 6. In the first embodiment, each of the first, second and third annular ridges 21, 22, 23 comprises only one depression 25.
[0061] Each of the first, second and third annular ridges 21, 22, 23 may comprise at most ten, at most nine, at most eight, at most seven, at most six, at most five, at most four, at most three or at most two depressions 25. The number of depressions 25 may be equal for each of the first, second or third annular ridge 21, 22, 23. Alternatively, the first, second and third annular ridges 21, 22, 23 may have different numbers of depressions 25. The number of depressions 25 may be selected for each individual heat exchanger plate 2 or plate heat exchanger 1, and may be determined by the requirements of strength and the need for a large flow area for the first or second fluid.
[0062] In the first embodiment, any radial line of the porthole 12 of the first porthole areas 11′ extends through at most two depressions 25 from the center of the porthole 12. In particular, there is a radial line extending from the center of the porthole 12 through the depressions 25 of the second and third annular ridges 22, 23, and through a portion of the first annular ridge 21 that has no depression 25, as can be seen in
[0063] The two second portholes areas 11″ may have the same configuration as the two first porthole areas 11′, but the first, second and third annular ridges 21, 22, 23 may instead extend from annular base area 14 at or on the primary level p′ to the secondary level p″. The depressions 25 of the first, second and third ridges 21, 22, 33 may thus extend form the secondary level p″, and all the way to the primary level p′, or to an intermediate level.
[0064] In the plate heat exchanger 1, every second heat exchanger plate 2 may be arranged so that an upper surface the first, second and third annular ridges 21, 22, 23 of one heat exchanger plate 1 adjoins, and may be joined to, an upper surface of the respective on of the first, second and third annular ridges 21, 22, 23 of an adjacent heat exchanger plate 1. Furthermore, the annular base area 14 of the porthole areas 11′, 11″ of one heat exchanger plate 2 may adjoin and be joined to an opposite annular base area 14 of an adjacent heat exchanger plate 2. This arrangement of the heat exchanger plats may be achieved by pressing two different kinds of heat exchanger plates, by rotating every second heat exchanger plate 180 degrees in the extension plane p. In the latter case, all of the porthole areas 11′, 11″ need to have the same configuration, or diagonally positioned porthole areas 11′, 11″ need to have the same configuration.
[0065] As illustrated in
[0066] Alternatively, the depressions 25 of one or more of the first, second and third annular ridges 21-23 may be displaced in a peripheral direction from the depression of the respective annular ridge 21-23 of the adjacent heat exchanger plates 2. This configuration means that the depressions 25 may create a fluid communication path having a height corresponding to half the distance between adjacent heat exchanger plates 2, or in other words half the press depth.
[0067]
[0068]
[0069]
[0070] It should be noted that there are many various possibilities to arrange the depressions 25 through the different annular ridges 21, 22, 23, both with regard the number of depressions 25 and the positions of the different depressions 25.
[0071] The invention is not limited to the embodiments disclosed, but may be varied and modified within the scope of the following claims.