The present disclosure relates to a cooling device.
Priority is claimed on Japanese Patent Application No. 2020-028002, filed on Feb. 21, 2020, the content of which is incorporated herein by reference.
When a fluid is compressed by a compressor, the temperature of the compressed fluid increases. In a multi-stage compressor, when the compressed fluid is fed to another compressor in a rear stage, a cooling device for cooling the fluid may be used to improve the compression efficiency of the fluid in the compressor in the rear stage in some cases.
For example, Japanese Unexamined Patent Application, First Publication No. 2014-137219 discloses a cooling device having a configuration including a housing formed in a cylindrical shape and a heat exchanger disposed inside the housing as a cooler. In this configuration, the fluid flows into the housing through an inlet port formed in the housing. Inside the housing, the fluid flows into the heat exchanger from an inlet side portion of the heat exchanger, and flows out from an outlet side portion. In the heat exchanger, the fluid flows around a plurality of tubes extending in an axial direction of the housing. A cooling medium (coolant) flows inside the tube. The fluid is cooled by exchanging heat with the cooling medium via the tube.
In this cooling device, it is desirable to improve the heat exchange efficiency of the fluid in the heat exchanger. Therefore, in Japanese Unexamined Patent Application, First Publication No. 2014-137219, a flow homogenizing element having a perforated plate shape is provided in an inlet side portion of the heat exchanger. The flow homogenizing element homogenizes a flow of the fluid flowing into the heat exchanger from the inlet side portion, thereby improving the heat exchange efficiency of the fluid in the heat exchanger as a whole.
Incidentally, the cooling device disclosed in Japanese Unexamined Patent Application, First Publication No. 2014-137219 includes a separation plate that internally partitions a housing between an inlet port and an outlet port. The separation plate prevents a possibility that the fluid flowing into the housing from the inlet port may flow in an axial direction and may be discharged outward of the housing as it is from the outlet port without passing through the heat exchanger serving as a cooler.
However, since the separation plate is provided, the fluid flowing into the housing from the inlet port is less likely to reach a region on the outlet port side of the separation plate in the axial direction, which is the inlet side portion of the cooler. Therefore, the fluid is likely to concentrate on the region on the inlet side of the separation plate in the axial direction, which is the inlet side portion of the cooling device. Accordingly, there is room for improvement in the heat exchange efficiency in the cooler.
The present disclosure provides a cooling device which can further improve the heat exchange efficiency in the cooler.
According to an aspect of the present disclosure, there is provided a cooling device including a shell having a shell main body formed in a cylindrical shape extending around an axis, an inlet nozzle configured to feed a fluid into the shell main body, and an outlet nozzle disposed away from the inlet nozzle in an axial direction in which the axis extends and configured to feed the fluid inside the shell main body to an outside of the shell main body, a cooler disposed inside the shell main body, configured to cool the fluid flowing from the inlet nozzle toward the outlet nozzle by internally circulating the fluid, and having a first surface extending in the axial direction to face the inlet nozzle and the outlet nozzle, and a partition member fixed to the first surface, and partitioning a space portion between the cooler and an inner peripheral surface of the shell main body into a first space communicating with the inlet nozzle and a second space communicating with the outlet nozzle. The partition member includes a main partition plate disposed between the inlet nozzle and the outlet nozzle in the axial direction, and extending from the first surface to the inner peripheral surface of the shell main body to spread in a direction intersecting with the axis, a first guide portion extending from an end portion on a first side of the main partition plate in the direction intersecting with the axis toward a first end surface of the shell main body close to the inlet nozzle in the axial direction, and a second guide portion extending from an end portion on a second side of the main partition plate in the direction intersecting with the axis toward a second end surface of the shell main body close to the outlet nozzle in the axial direction.
According to the aspect of the cooling device of the present disclosure, the heat exchange efficiency in the cooler can be further improved.
Hereinafter, an embodiment for implementing a cooling device according to the present disclosure will be described with reference to the accompanying drawings. However, the present disclosure is not limited only to the embodiment.
(Configuration of Compressor System)
As illustrated in
A fluid G serving as a compression target in the compressor system 8 is compressed by a compressor 9A in a front stage, and thereafter, is fed into a compressor 9B in a rear stage. The fluid G compressed by the compressor 9A in the front stage is further compressed by the compressor 9B in the rear stage. The cooling device 1 is disposed between the compressor 9A in the front stage and the compressor 9B in the rear stage. The cooling device 1 is connected to an outlet side of the compressor 9A in the front stage via the front stage connection pipe 10A. The cooling device 1 is connected to the inlet side of the compressor 9B in the rear stage via a rear stage connection pipe 10B.
(Configuration of Cooling Device)
As illustrated in
(Configuration of Shell)
As illustrated in
The inlet nozzle 24 and the outlet nozzle 25 are integrally connected to the shell main body 21. The inlet nozzle 24 and the outlet nozzle 25 are disposed at a distance in an axial direction Da in which the axis O extends. The inlet nozzle 24 is disposed on a first side Da1 in the axial direction Da with respect to a center 21c of the shell main body 21 in the axial direction Da. The outlet nozzle 25 is disposed on a second side Da2 in the axial direction Da with respect to the center 21c of the shell main body 21. As illustrated in
(Configuration of Cooler)
As illustrated in
The tube bank 31 includes a plurality of cooling tubes 35 and fin plates 37. Each of the cooling tubes 35 extends in the axial direction Da inside the shell main body 21. As illustrated in
As illustrated in
The tube insertion hole 371 is fixed in a state where the cooling tube 35 is inserted in the axial direction Da. Each of the tube insertion holes 371 penetrates the fin plate main body 370 in the axial direction Da (plate thickness direction). Each of the cooling tube is expanded and joined to or inserted into each of the tube insertion holes 371 so that each of the cooling tubes 35 is in sliding contact therewith. Therefore, the plurality of tube insertion holes 371 are disposed in a staggered array in accordance with a layout of the plurality of cooling tubes 35. That is, the plurality of tube insertion holes 371 are disposed so that center lines La, Lb, and Lc of three tube insertion holes 371 closest to one another form a triangle (equilateral triangle or isosceles triangle) when viewed in the axial direction Da. Each of the tube insertion holes 371 is formed by performing a punching process on the fin plate 37. Each of the tube insertion holes 371 has an edge portion 372 formed through a diameter expansion step or an insertion step during the punching process. The edge portion 372 is formed to protrude in a cylindrical shape in the axial direction Da from a peripheral edge portion of the tube insertion hole 371.
The protrusion portion 38 is formed between the plurality of tube insertion holes 371 when viewed in the axial direction Da. The protrusion portion 38 is a turbulent flow portion that disturbs a flow of the fluid G flowing between the plurality of tube insertion holes 371 in a gap between the pair of fin plate main bodies 370. As illustrated in
As illustrated in
That is, when the fin plates 37 are aligned in the axial direction Da, the protrusion portion 38 protrudes to be in contact with the other fin plate 37 adjacent in the axial direction Da. In addition, in the present embodiment, the protrusion dimension of the protrusion portion 38 is equal to the protrusion dimension from the fin plate main body 370 in the axial direction Da in the edge portion 372.
As illustrated in
As illustrated in
In the cooler 3, the fluid G comes into contact with the cooling tube 35 of the tube bank 31 by passing between the first plate portion 32 and the second plate portion 33 which are vertically disposed in the vertical direction Dv. Here, the fluid G flows along the width direction Dw orthogonal to the axial direction Da between the first plate portion 32 and the second plate portion 33. That is, the width direction Dw orthogonal to the axial direction Da coincides with a flow direction Df of the fluid G in the cooler 3. In the following description, in the width direction Dw, a side where the fluid G flows into the cooler 3 will be referred to as a first side Dw1, and a side where the fluid G flows out from the cooler 3 will be referred to as a second side Dw2. Therefore, the flow direction Df is a direction from the first side Dw1 toward the second side Dw2 in the width direction Dw.
An end portion 32a of the first side Dw1 of the first plate portion 32 in the width direction Dw is disposed at a distance from the shell main body 21. An end portion 32b of the second side Dw2 of the first plate portion 32 in the width direction Dw is disposed at a distance from the shell main body 21.
Similarly, an end portion 33a of the first side Dw1 of the second plate portion 33 in the width direction Dw is disposed at a distance from the shell main body 21. An end portion 33b of the second side Dw2 of the second plate portion 33 in the width direction Dw is disposed at a distance from the shell main body 21.
In addition, it is preferable that the first plate portion 32 and the second plate portion 33 have a distance as small as possible from the tube bank 31 in the vertical direction Dv. In the present embodiment, for example, an upper plate material 39A parallel to the first plate portion 32 is inserted between a lower surface of the first plate portion 32 and an upper end of the fin plate 37. In this manner, the tube bank 31 and the first plate portion 32 are disposed without any gap via the upper plate material 39A. In addition, in the present embodiment, for example, a lower plate material 39B parallel to the second plate portion 33 is inserted between an upper surface of the second plate portion 33 and a lower end of the fin plate 37. In this manner, the tube bank 31 and the second plate portion 33 are disposed without any gap via the lower plate material 39B. In addition, a short pass prevention jig of a structure (rib) having a hydraulic diameter the same as that of the cooling tube 35 may be installed in the upper plate material 39A or the lower plate material 39B. The first plate portion 32 or the second plate portion 33 may be simply disposed to be vertically in close contact with the tube bank 31.
(Configuration of Extension Portion)
In addition, the cooler 3 further includes an extension portion 34. The extension portion 34 extends from the end portion (plate end portion) 33a on the first side Dw1 in the width direction Dw in the second plate portion 33 toward the inner peripheral surface 21f of the shell main body 21. The extension portion 34 has a flat plate shape. The extension portion 34 extends from the end portion 33a of the second plate portion 33 to be inclined toward the first side Dw1 in the width direction Dw, as the extension portion 34 faces downward in the vertical direction Dv. A tip portion of a second guide portion 53 is in contact with the inner peripheral surface 21f on a lower side of the shell main body 21.
(Configuration of Partition Member)
As illustrated in
Da from the first end surface 22A which is the end surface close to the inlet nozzle 24 in the axial direction Da. The partition member 5 partitions a space portion 2S between the cooler 3 and the inner peripheral surface 21f of the shell main body 21. Specifically, the partition member 5 partitions the space portion 2S into a first space 21S communicating with the inlet nozzle 24 and a second space 22S communicating with the outlet nozzle 25. The partition member 5 integrally includes a main partition plate 51, a first guide portion 52, and a second guide portion 53.
(Configuration of Main Partition Plate)
As illustrated in
The main partition plate 51 is disposed between the inlet nozzle 24 and the outlet nozzle 25 in the axial direction Da. The main partition plate 51 is disposed at a position close to the second end surface 22B of the shell main body 21 with respect to a central portion 32m of the first plate portion 32 (first surface 320) in the axial direction Da. It is preferable that the main partition plate 51 is disposed at a position offset to the second side Da2 in the axial direction Da by approximately ⅛ to 2/8 of a total length V in the axial direction Da of the first plate portion 32 with respect to the central portion 32m of the first plate portion 32 in the axial direction Da. A first end portion 51a which is an end portion on the first side Dw1 of the main partition plate 51 in the width direction Dw is disposed at a position away from an end (end portion 32a of the first plate portion 32 when viewed in the vertical direction Dv) on the first side Dw1 of the first surface 320 in the width direction Dw. In addition, a second end portion 51b which is an end portion on the second side Dw2 of the main partition plate 51 in the width direction Dw is disposed at a position away from an end portion (end portion 32b of the first plate portion 32 when viewed in the vertical direction Dv) on the second side Dw2 of the first surface 320 in the width direction Dw.
The main partition plate 51 spreads to be inclined with respect to a plane orthogonal to the axial direction Da. When viewed in the vertical direction Dv, the main partition plate 51 is inclined to face the second side Da2 from the first side Da1 in the axial direction Da, as the main partition plate 51 faces the second end portion 51b from the first end portion 51a. The tip portion of the main partition plate 51 is in contact with the inner peripheral surface 21f on an upper side of the shell main body 21.
(Configuration of First Guide Portion)
The first guide portion 52 extends upward from the first surface 320 in the vertical direction Dv. The first guide portion 52 is formed in a flat plate shape having a plate thickness which is approximately the same as that of the main partition plate 51. The first guide portion 52 is disposed on the first side Da1 in the axial direction Da with respect to the main partition plate 51. The first guide portion 52 extends from the second end portion 51b of the main partition plate 51 to the first side Da1 in the axial direction Da. The first guide portion 52 extends to be parallel to the end portion 32b of the first plate portion 32 from the second end portion 51b toward the first end surface 22A. As illustrated in
(Configuration of Second Guide Portion)
As illustrated in
As illustrated in
(Configuration of Perforated Plate)
As illustrated in
(Description of Flow of Fluid inside Shell)
As illustrated in
In addition, the fluid G3 flowing to the second side Da2 in the axial direction Da on the first surface 320 is guided from the second end portion 51b toward the first end portion 51a along the main partition plate 51, and is guided to the first side Dw1 in the width direction Dw with respect to the second guide portion 53. In addition, the fluid G4 flowing to the first side Da1 in the axial direction Da on the first surface 320 hits the first end surface 22A of the shell main body 21 located on the first side Da1 in the axial direction Da. In this manner, a flow direction thereof is reversed to the second side Da2 in the axial direction Da. In this manner, the fluid G of the space portion 2S is pushed to the second side Da2 in the axial direction Da, and a portion of the fluid G of the space portion 2S is pushed into the first side Dw1 in the width direction Dw with respect to the second guide portion 53.
As illustrated in
Here, a flow path cross-sectional area of a region surrounded by the second guide portion 53, a virtual extending surface of the first surface 320, and the inner peripheral surface 21f of the shell main body 21 in a cross section orthogonal to the axial direction Da is extremely smaller than a flow path cross-sectional area of a region surrounded by the first guide portion 52, the first surface 320, and the inner peripheral surface 21f of the shell main body 21. Therefore, a flow velocity of the fluid G flowing from the first side Da1 in the axial direction Da to the second side Da2 in the axial direction Da along the second guide portion 53 with respect to the main partition plate 51 increases. In this manner, the fluid G is more likely to spread to the second side Da2 in the axial direction Da. The fluid G oriented to the second side Da2 in the axial direction Da flows to the first side Dw1 in the width direction Dw with respect to the tube bank 31 to turn around the end portion 32a of the first plate portion 32.
(Operational Effect)
In the cooling device 1 having the above-described configuration, the space portion 2S between the first plate portion 32 and the inner peripheral surface 21f of the shell main body 21 facing the first plate portion 32 is partitioned by the partition member 5 between the inlet nozzle 24 and the outlet nozzle 25. The fluid G flows from the inlet nozzle 24 into the first space 21S which is the first side Da1 in the axial direction Da with respect to the main partition plate 51. The first guide portion 52 extending to the first side Da1 in the axial direction Da and the second guide portion 53 extending to the second side Da2 with respect to the main partition plate 51 causes the fluid G flowing into the first space 21S to flow to spread to the first side Da1 and the second side Da2 in the axial direction Da inside the first space 21S. In this manner, in the shell main body 21, the fluid G flows from a deep portion on the first side Da1 close to the inlet nozzle 24 in the axial direction Da to a deep portion on the second side Da2 away from the inlet nozzle 24 in the axial direction Da. In this manner, a flow rate distribution of the fluid G flowing into the cooler 3 can be homogenized. As a result, the heat exchange efficiency in the cooler 3 can be further improved.
In addition, the main partition plate 51 is disposed on the second side Da2 in the axial direction Da to be close to the second end surface 22B of the shell main body 21 with respect to the central portion 32m of the first plate portion 32 in the axial direction Da. In this manner, the fluid G flowing from the inlet nozzle 24 into the first space 21S flows to spread to the second side Da2 from the center in the axial direction Da until the fluid G reaches the main partition plate 51. As a result, the fluid G can efficiently spread to a wide region on the second side Da2 in the axial direction Da.
In addition, the second guide surface 530 is inclined to face the outlet nozzle 25. In this manner, the fluid G flowing out of the cooler 3 and flowing on the first surface 320 in the second space 22S can be efficiently guided to the outlet nozzle 25.
In addition, the first guide surface 520 is inclined to face the inlet nozzle 24. In this manner, the first guide surface 520 causes the fluid G flowing from the inlet nozzle 24 into the first space 21S to flow along the first surface 320 in the first space 21S. As a result, the fluid G flowing into the shell main body 21 can be efficiently guided to the main partition plate 51, the first guide portion 52, and the second guide portion 53 which are connected to the first surface 320.
In addition, the first end portion 51a of the main partition plate 51 is away from the end portion 32a of the first plate portion 32. That is, the main partition plate 51 is formed away from the end portion of the first surface 320 in the width direction Dw when viewed in the vertical direction Dv. In this manner, the second guide portion 53 extends at a position away from the end portion 32a of the first plate portion 32. Therefore, when viewed in the vertical direction Dv, a portion of the first surface 320 is in a spreading state between the second guide portion 53 and the end portion of the first surface 320. Furthermore, the main partition plate 51 is inclined to face the second side Da2 from the first side Da1 in the axial direction Da, as the main partition plate 51 faces the second end portion 51b from the first end portion 51a when viewed in the vertical direction Dv. Therefore, the fluid G flowing into the first space 21S is guided by the main partition plate 51 toward the second guide portion 53 located on the second side Da2 in the axial direction Da with respect to the main partition plate 51. The fluid G guided toward the second guide portion 53 further flows toward the second side Da2 in the axial direction Da on the first surface 320 between the second guide portion 53 and the end portion 32a of the first plate portion 32. As a result, the fluid G can efficiently spread to a deep portion of the second side Da2 in the axial direction Da.
In addition, the extension portion 34 extending toward the inner peripheral surface 21f of the shell main body 21 is formed in the end portion 33a on the first side Dw1 in the width direction Dw in the second plate portion 33. The extension portion 34 closes a portion between the second plate portion 33 and the shell main body 21. In this manner, it is possible to prevent a possibility that the fluid G flowing into the lower portion of the second plate portion 33 may flow toward the outlet nozzle 25 to turn around the cooler 3 without passing through the tube bank 31. Therefore, the fluid G inside the shell main body 21 can be efficiently guided to the tube bank 31.
In addition, the first plate portion 32 or the second plate portion 33 is in close contact with the tube bank 31 in the vertical direction Dv. In this way, there is no gap between the first plate portion 32 or the second plate portion 33 and the tube bank 31. Accordingly, it is possible to suppress a possibility that the fluid G may pass upward and downward of the tube bank 31 without passing through the tube bank 31. As a result, the fluid G inside the shell main body 21 can be efficiently guided to the tube bank 31. In this manner, it is possible to suppress a possibility that heat transfer performance of the cooler 3 may be degraded.
In addition, the perforated plate 4 is disposed on the first side Dw1 in the width direction Dw with respect to the tube bank 31. Therefore, the fluid G flowing into the shell main body 21 from the inlet nozzle 24 is fed to the tube bank 31 in a homogenized state by the perforated plate 4. As a result, the heat exchange efficiency in the cooler 3 can be further improved.
In addition, the cooler 3 includes a protrusion portion 38 that protrudes from the fin plate main body 370 in the axial direction Da between the plurality of cooling tubes 35. The fluid G passing through the inside of the tube bank 31 comes into contact with the plurality of cooling tubes 35 when passing through a gap between the fin plate main bodies 370 adjacent to each other in the axial direction Da. In this case, as illustrated in
In particular, the protrusion portion 38 is formed at a center position D of a triangle (equilateral triangle or isosceles triangle) drawn by center lines La, Lb, and Lc of three tube insertion holes 371 closest to one another in the plurality of tube insertion holes 371 disposed in a staggered array. That is, the protrusion portion 38 is formed at a position where the heat is particularly likely to concentrate in the fin plate main body 370. Therefore, since the protrusion portion 38 is disposed in the portion where the heat is particularly likely to concentrate, the deformability of the fin plate 37 is improved. As a result, it is possible to effectively suppress the thermal deformation of the fin plate 37.
Furthermore, the protrusion portion 38 improves the heat exchange efficiency of the fluid G in the tube bank 31. In this manner, even when the fin plate 37 is formed of a two-phase stainless steel material having lower thermal conductivity than an aluminum alloy or copper, cooling performance can be ensured as the cooler 3. As a result, not only the cooling performance but also other performance such as corrosion resistance can be improved.
In addition, the protrusion portion 38 has a cylindrical shape that protrudes from the fin plate main body 370 in the axial direction Da. In this manner, a punching process is performed on the through-hole 375 in the fin plate 37. Accordingly, it is possible to easily form the protrusion portion 38 having the cylindrical shape which protrudes from a peripheral edge portion of the through-hole 375 in the axial direction Da. Therefore, in order to form the protrusion portion 38, it is not necessary to prepare a separate component, and the protrusion portion 38 can be formed at low cost.
Furthermore, the protrusion portion 38 having the cylindrical shape is in contact with the other fin plate main body 370 adjacent in a protrusion direction of the protrusion portion 38 in the axial direction Da. In this manner, the protrusion portion 38 having the cylindrical shape is provided without any gap between the fin plate main bodies 370 adjacent to each other in the axial direction Da. Therefore, the fluid G flowing between the fin plate main bodies 370 can be more efficiently brought into contact with the protrusion portion 38. The fluid G whose flow is disturbed by the protrusion portion 38 flows along the cooling tube 35 between the fin plate main bodies 370. In this manner, the heat exchange efficiency of the fluid G in the tube bank 31 is improved.
Hitherto, the embodiment of the present disclosure has been described in detail with reference to the drawings. However, a specific configuration is not limited to the embodiment, and includes a design change within the scope not departing from the concept of the present disclosure.
The turbulent flow portion is not limited to the protrusion portion 38. The turbulent flow portion may have any configuration as long as the flow of the fluid G can be disturbed. Therefore, the turbulent flow portion may be a through-hole penetrating the fin plate main body 370.
In addition, in the above-described embodiment, the protrusion portion 38 has the cylindrical shape. However, a shape of the protrusion portion 38 is not limited to the cylindrical shape. For example, as illustrated in
In addition, instead of the protrusion portion 38, a slit may be formed around the edge portion 372 of the tube insertion hole 371. In this manner, the rigidity of the fin plate 37 may be lowered to suppress thermal deformation of the fin plate 37.
In addition, as the protrusion portion 38, in addition to the protrusion portion 38 having the cylindrical shape which rises from the peripheral edge portion of the through-hole 375 formed in the fin plate 37, a projection formed to rise from the fin plate 37, a member having a cylindrical shape provided to penetrate the fin plate 37, or a member having a shaft shape may be adopted.
For example, the cooling device 1 described in the embodiment is understood as follows.
(1) According to a first aspect, the cooling device 1 includes the shell 2 having the shell main body 21 formed in the cylindrical shape extending around the axis O, the inlet nozzle 24 configured to feed the fluid G into the shell main body 21, and the outlet nozzle 25 disposed away from the inlet nozzle 24 in the axial direction Da in which the axis O extends and configured to feed the fluid G inside the shell main body 21 to the outside of the shell main body 21, the cooler 3 disposed inside the shell main body 21, configured to cool the fluid G flowing from the inlet nozzle 24 toward the outlet nozzle 25 by internally circulating the fluid G, and having the first surface 320 extending in the axial direction Da to face the inlet nozzle 24 and the outlet nozzle 25, and the partition member 5 fixed to the first surface 320, and partitioning the space portion 2S between the cooler 3 and the inner peripheral surface 21f of the shell main body 21 into the first space 21S communicating with the inlet nozzle 24 and the second space 22S communicating with the outlet nozzle 25. The partition member 5 includes the main partition plate 51 disposed between the inlet nozzle 24 and the outlet nozzle 25 in the axial direction Da, and extending from the first surface 320 to the inner peripheral surface 21f of the shell main body 21 to spread in the direction intersecting with the axis O, the first guide portion 52 extending from the end portion on the first side Dw1 of the main partition plate 51 in the direction intersecting with the axis O toward the first end surface 22A of the shell main body 21 close to the inlet nozzle 24 in the axial direction Da, and the second guide portion 53 extending from the end portion on the second side Dw2 of the main partition plate 51 in the direction intersecting with the axis O toward the second end surface 22B of the shell main body 21 close to the outlet nozzle 25 in the axial direction Da.
In the cooling device 1, the fluid G flows from the inlet nozzle 24 into the first space 21S which is the first side Da1 in the axial direction Da with respect to the main partition plate 51. The first guide portion 52 extending to the first side Da1 in the axial direction Da and the second guide portion 53 extending to the second side Da2 with respect to the main partition plate 51 causes the fluid G flowing into the first space 21S to flow to spread to the first side Da1 and the second side Da2 in the axial direction Da inside the first space 21S. In this manner, in the shell main body 21, the fluid G flows from the deep portion on the first side Da1 close to the inlet nozzle 24 in the axial direction Da to the deep portion on the second side Da2 away from the inlet nozzle 24 in the axial direction Da. In this manner, a flow rate distribution of the fluid G flowing into the cooler 3 can be homogenized. As a result, the heat exchange efficiency in the cooler 3 can be further improved.
(2) According to a second aspect of the cooling device 1, in the cooling device 1 of the aspect (1), the main partition plate 51 is disposed at a position close to the second end surface 22B of the shell main body 21 with respect to the central portion 32m of the first surface 320 in the axial direction Da.
In this manner, the fluid G flowing from the inlet nozzle 24 into the first space 21S reaches the main partition plate 51, and thereafter, flows to spread to the second side Da2 from the center in the axial direction Da. As a result, the fluid G can efficiently spread to a wide region on the second side Da2 in the axial direction Da.
(3) According to a third aspect of the cooling device 1, in the cooling device 1 of the aspect (1) or (2), the second guide portion 53 has the second guide surface 530 extending from the first surface 320 to the inner peripheral surface 21f of the shell main body 21 and inclined to face the outlet nozzle 25.
In this manner, the fluid G flowing out of the cooler 3 and flowing on the first surface 320 in the second space 22S can be efficiently guided to the outlet nozzle 25.
(4) According to a fourth aspect of the cooling device 1, in the cooling device 1 of any one of the aspects (1) to (3), the first guide portion 52 has the first guide surface 520 extending from the first surface 320 to the inner peripheral surface 21f of the shell main body 21 and inclined to face the inlet nozzle 24.
In this manner, the first guide surface 520 causes the fluid G flowing from the inlet nozzle 24 into the first space 21S to flow along the first surface 320 in the first space 21S. As a result, the fluid G flowing into the shell main body 21 can be efficiently guided to the main partition plate 51, the first guide portion 52, and the second guide portion 53 which are connected to the first surface 320.
(5) According to a fifth aspect of the cooling device 1, in the cooling device 1 of any one of the aspects (1) to (4), the main partition plate 51 is disposed at a position away from the end portion of the first surface 320 in the width direction Dw orthogonal to the axis O, and the second guide portion 53 extends in the axial direction Da at the position away from the end portion of the first surface 320 in the width direction Dw.
In this manner, the second guide portion 53 extends at a position away from the end portion of the first surface 320. Therefore, when viewed in the vertical direction Dv, a portion of the first surface 320 is in a spreading state between the second guide portion 53 and the end portion of the first surface 320. Therefore, the fluid G guided toward the second guide portion 53 further flows toward the second side Da2 in the axial direction Da on the first surface 320 between the second guide portion 53 and the end portion of the first surface 320. As a result, the fluid G can efficiently spread to a deep portion of the second side Da2 in the axial direction Da.
(6) According to a sixth aspect of the cooling device 1, the cooling device 1 of any one of the aspects (1) to (5) further includes the perforated plate 4 disposed to cover the side surface into which the fluid flows in the cooler 3, and having a plurality of holes.
In this manner, the fluid G flowing into the shell main body 21 from the inlet nozzle 24 is fed to the cooler 3 in a homogenized state by the perforated plate 4. As a result, the heat exchange efficiency in the cooler 3 can be further improved.
(7) According to a seventh aspect of the cooling device 1, in the cooling device 1 of any one of the aspects (1) to (6), the cooler 3 includes the plurality of cooling tubes 35 extending in the axial direction Da, and which the cooling medium configured to flow therein, and the plurality of fin plates 37 having the plate shape orthogonal to the axial direction Da, disposed at a distance in the axial direction Da, and having the plurality of tube insertion holes 371 for fixing the plurality of cooling tubes 35 in a state where the plurality of cooling tubes 35 are inserted in the axial direction Da. Each of the plurality of fin plates 37 has the turbulent flow portion configured to disturb the flow of the fluid G between the plurality of tube insertion holes 371.
In this manner, the fluid G comes into contact with the plurality of cooling tubes 35 when passing through the gap between the fin plates 37 adjacent to each other in the axial direction Da. In this case, the flow of the fluid G is disturbed by the turbulent flow portion disposed between the plurality of cooling tubes 35. Accordingly, the direction of the flow of the fluid G is dispersed, and the fluid G is likely to hit the plurality of cooling tubes 35 around the turbulent flow portion. In this manner, the heat exchange efficiency of the fluid G in the cooling tube 35 is improved.
(8) According to an eighth aspect of the cooling device 1, in the cooling device 1 of the aspect (7), the turbulent flow portion has the protrusion portion 38 having the cylindrical shape to have the through-hole 375 penetrating in the axial direction Da, and protruding in the axial direction Da.
In this manner, the fluid G comes into contact with the plurality of cooling tubes 35 when passing through the gap between the fin plates 37 adjacent to each other in the axial direction Da. In this case, the fluid G collides with the protrusion portion 38 disposed between the plurality of cooling tubes 35. Accordingly, the flow of the fluid G is easily disturbed. In addition, in the fin plate 37, a cooling effect between the plurality of cooling tubes 35 is lowered since a distance from the cooling tubes 35 is far. As a result, the heat is likely to concentrate, and thermal deformation of the fin plate 37 is likely to occur in the portion. The turbulent flow portion is disposed in the portion where the heat is likely to concentrate in this way. Accordingly, the deformability of the fin plate 37 is improved. As a result, it is possible to suppress the thermal deformation of the fin plate 37. In this manner, it is possible to suppress a decrease in contact resistance of a joint portion between the fin plate 37 and the cooling tube 35. In addition, a punching process is performed on the through-hole 375 in the fin plate 37. Accordingly, it is possible to easily form the protrusion portion 38 having the cylindrical shape which protrudes from the peripheral edge portion of the through-hole 375 in the axial direction Da. Therefore, in order to form the protrusion portion 38, it is not necessary to prepare a separate component, and the protrusion portion 38 can be formed at low cost.
(9) According to a ninth aspect of the cooling device 1, in the cooling device 1 of the aspect (8), the protrusion portion 38 protrudes to be in contact with another fin plate 37 adjacent in the axial direction Da among the plurality of fin plates 37.
In this manner, the protrusion portion 38 is provided without any gap between the fin plates 37 adjacent to each other in the axial direction Da. Therefore, the fluid G flowing between the fin plates 37 can be more efficiently brought into contact with the protrusion portion 38. The fluid G whose flow is disturbed by the protrusion portion 38 flows along the cooling tube 35 between the fin plates 37. In this manner, the heat exchange efficiency of the fluid G in the cooler 3 is improved.
(10) According to a tenth aspect of the cooling device 1, in the cooling device 1 of any one of the aspects (7) to (9), the plurality of the tube insertion holes 371 are disposed so that the center lines of three tube insertion holes 371 closest to one another form the triangle when viewed in the axial direction Da. The turbulent flow portion is disposed to be located at the center of the triangle.
In this manner, the turbulent flow portion is formed at a position where the heat is particularly likely to concentrate in the fin plate 37. Therefore, since the turbulent flow portion such as the protrusion portion 38 is disposed in the portion where the heat is particularly likely to concentrate, the deformability of the fin plate 37 is greatly improved. As a result, it is possible to effectively suppress the thermal deformation of the fin plate 37.
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