US20190086155A1 - Diffusion-Bonded Heat Exchanger - Google Patents
Diffusion-Bonded Heat Exchanger Download PDFInfo
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- US20190086155A1 US20190086155A1 US16/081,312 US201716081312A US2019086155A1 US 20190086155 A1 US20190086155 A1 US 20190086155A1 US 201716081312 A US201716081312 A US 201716081312A US 2019086155 A1 US2019086155 A1 US 2019086155A1
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- Prior art keywords
- heat transfer
- fluid
- fluid passages
- passages
- transfer plate
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K20/00—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating
- B23K20/002—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating specially adapted for particular articles or work
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K20/00—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating
- B23K20/02—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating by means of a press ; Diffusion bonding
- B23K20/023—Thermo-compression bonding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K20/00—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating
- B23K20/22—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating taking account of the properties of the materials to be welded
- B23K20/227—Non-electric welding by applying impact or other pressure, with or without the application of heat, e.g. cladding or plating taking account of the properties of the materials to be welded with ferrous layer
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0093—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/02—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the heat-exchange media travelling at an angle to one another
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/048—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K2101/00—Articles made by soldering, welding or cutting
- B23K2101/04—Tubular or hollow articles
- B23K2101/14—Heat exchangers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K2103/00—Materials to be soldered, welded or cut
- B23K2103/02—Iron or ferrous alloys
- B23K2103/04—Steel or steel alloys
- B23K2103/05—Stainless steel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/02—Heat exchange conduits with particular branching, e.g. fractal conduit arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2275/00—Fastening; Joining
- F28F2275/06—Fastening; Joining by welding
- F28F2275/061—Fastening; Joining by welding by diffusion bonding
Definitions
- the present invention relates to a diffusion-bonded heat exchanger, and more particularly, it relates to a diffusion-bonded heat exchanger in which a plurality of heat transfer plates including groove-like fluid passages are stacked and diffusion-bonded to each other.
- a diffusion-bonded heat exchanger in which a plurality of heat transfer plates including groove-like fluid passages are stacked and diffusion-bonded to each other is known.
- Such a diffusion-bonded heat exchanger is disclosed in Japanese Patent Laid-Open No. 2013-155971, for example.
- Japanese Patent Laid-Open No. 2013-155971 discloses a heat exchanger including a core in which first heat transfer plates and second heat transfer plates are alternately stacked and are diffusion-bonded to each other.
- first heat transfer plates A, B, C, and D There are four types of first heat transfer plates A, B, C, and D, and each type includes a plurality of first heat transfer plates.
- second heat transfer plates E There is one type of second heat transfer plates E, and this type includes a plurality of second heat transfer plates.
- the respective heat transfer plates are stacked in the order of EAE . . . , EBE . . . , ECE . . . , and EDE . . . .
- the outer shapes of the four types of first heat transfer plates and one type of second heat transfer plates are common.
- the heat exchanger disclosed in Japanese Patent Laid-Open No. 2013-155971 is configured as an intercooler of a multistage compression system using four compressors.
- a fluid (hydrogen) that has passed through the first to fourth stage compressors flows through each of the four types of first heat transfer plates A, B, C, and D, and a refrigerant (cooling water) flows through the second heat transfer plate E.
- the core is provided with a plurality of ports connected to connection passages that pass through the heat transfer plates in a thickness direction and corresponding to the heat transfer plates A to E, respectively. Fluid distribution to each of the heat transfer plates A to E is performed through the corresponding port.
- Patent Document 1 Japanese Patent Laid-Open No. 2013-155971
- each of the four types of first heat transfer plates A to D and one type of second heat transfer plates E that sandwich each first heat transfer plate therebetween in an upward-downward direction need to include a plurality of heat transfer plates. Therefore, in Japanese Patent Laid-Open No. 2013-155971, when a common diffusion-bonded heat exchanger handles a plurality of types of fluids, the number of types of components (the number of types of heat transfer plates) and the number of components (the total number of heat transfer plates) disadvantageously increase.
- the present invention has been proposed in order to solve the aforementioned problems, and one object of the present invention is to provide a diffusion-bonded heat exchanger capable of reducing the number of types of components and the number of components even when a plurality of types of fluids are handled by a common diffusion-bonded heat exchanger, and capable of sufficiently ensuring the degree of freedom of the configuration of fluid passages.
- a diffusion-bonded heat exchanger includes a core in which a first heat transfer plate and a second heat transfer plate each including a groove-like fluid passage are stacked and diffusion-bonded to each other, a plurality of pairs of first ports through which fluids are introduced into and discharged from the first heat transfer plate, and at least a pair of second ports through which a fluid is introduced into and discharged from the second heat transfer plate, and the first heat transfer plate includes a plurality of first fluid passages connected to different pairs of the first ports and isolated from each other.
- the diffusion-bonded heat exchanger includes the first heat transfer plate including the plurality of first fluid passages connected to the different pairs of first ports and isolated from each other.
- the first heat transfer plate including a plurality of types of first fluid passages can be provided instead of providing a heat transfer plate for each type of fluid. That is, instead of providing a heat transfer plate for each type of fluid, the first heat transfer plate common to a plurality of types of fluids can be provided. Consequently, even when the plurality of types of fluids are handled by the common diffusion-bonded heat exchanger, the number of types of components and the number of components can be reduced.
- the plurality of types of first fluid passages can be formed in the same first heat transfer plate, and thus for example, one first fluid passage is reduced in size according to a load (the amount of heat exchange) on each fluid etc. such that another first fluid passage can be formed in an empty space, or the planar size of a product can be reduced. That is, the degree of freedom in the configuration of the fluid passages can be sufficiently ensured.
- the second ports preferably include a plurality of pairs of second ports
- the second heat transfer plate preferably includes a plurality of second fluid passages formed so as to correspond to the first fluid passages of the first heat transfer plate and isolated from each other
- the plurality of second fluid passages are preferably respectively connected to different pairs of the second ports.
- the term “corresponding” indicates the relationship in which heat exchange is mostly performed between the fluid that flows through one first fluid passage and the fluid that flows through the second fluid passage(s).
- One first fluid passage may correspond to one second fluid passage, or one second fluid passage may correspond to a plurality of first fluid passages.
- the plurality of second fluid passages are formed so as to correspond to the plurality of first fluid passages such that heat exchange between the fluids can be efficiently performed. Furthermore, the plurality of second fluid passages are connected to the different pairs of second ports such that the type, the flow rate, etc. of the fluid that flows through each of the second fluid passages can be individually set for each of the second fluid passages according to the amount of heat exchange between the fluids that flow through the first fluid passages and the second fluid passages corresponding to each other.
- the second fluid passages are preferably equal in number to the first fluid passages, and the second fluid passages are preferably respectively disposed at locations that overlap the plurality of first fluid passages of the first heat transfer plate in a planar view.
- the plurality of second fluid passages can be provided in a one-to-one correspondence with the plurality of first fluid passages.
- one wide second fluid passage one second fluid passage corresponding to the plurality of first fluid passages
- the first fluid passages are provided in a one-to-one correspondence with the second fluid passages such that heat exchange can be efficiently performed between the fluids that flow through pairs of the first fluid passages 11 a , 11 b , and 11 c and the second fluid passages 21 a , 21 b , and 21 c corresponding to each other. Furthermore, the flow rate of the fluid that flows through the second fluid passages, for example, can be easily optimized.
- the plurality of first fluid passages are each preferably formed into an elongated shape that extends in a first direction from one end connected to the first port on an entrance side toward another end connected to the first port on an exit side corresponding thereto in a plane of the first heat transfer plate, and are preferably disposed side by side along a second direction orthogonal to the first direction.
- the term “elongated shape” indicates a shape in which in the plane of the first heat transfer plate, one (first direction) of two directions orthogonal to each other is a longitudinal direction, and the other one (second direction) is a short-side direction.
- the plurality of first fluid passages are each formed into an elongated shape from one end toward another end such that the flow rate can be easily increased to improve the heat transfer coefficient even with a simple flow passage shape as compared with the case where the plurality of first fluid passages are each formed into a wide shape.
- the outer shape of the entire first heat transfer plate is more elongated, a load applied to a stacked body of the first heat transfer plate and the second heat transfer plate when diffusion bonding is performed is more likely to vary, and the ease of manufacturing the core is reduced.
- the first fluid passages each having an elongated shape that extends in the first direction are disposed side by side along the second direction such that the vertical and horizontal dimensions of the outer shape of the entire first heat transfer plate can be brought closer to each other (the aspect ratio can be brought closer to 1). Consequently, variations in the load at the time of performing diffusion bonding can be suppressed, and the ease of manufacturing the core can be improved.
- the plurality of first fluid passages are preferably spaced apart from each other in the second direction on a same surface of the first heat transfer plate, and the first heat transfer plate preferably includes a diffusion bonding surface with the second heat transfer plate between the first fluid passages adjacent to each other in the second direction. According to this configuration, each of the plurality of first fluid passages disposed on the same surface of the first heat transfer plate can be easily isolated as an independent fluid passage.
- the diffusion bonding surface that extends in the first direction can be formed between the plurality of first fluid passages aligned in the second direction, and thus the diffusion bonding strength between the first heat transfer plate and the second heat transfer plate can be easily ensured as compared with the case where the first heat transfer plate and the second heat transfer plate are bonded to each other only with the outer peripheral portion of the heat transfer plate surface or a gap (partition wall) between the flow passages constituting the first fluid passages, for example.
- each of the plurality of first fluid passages preferably includes a flow passage that connects one end connected to the first port on an entrance side to another end connected to the first port on an exit side corresponding thereto, and at least one of the plurality of first fluid passages is preferably different from another one of the plurality of first fluid passages in at least one of a flow passage width of the flow passage, a flow passage length of the flow passage, a flow passage depth of the flow passage, and a number of the flow passages.
- the plurality of types of first fluid passages are different in configuration (the flow passage width of the flow passage, the flow passage length of the flow passage, the flow passage depth of the flow passage, or the number of flow passages) such that a surplus amount of heat exchange that cannot be adjusted by the number of heat transfer plates can be easily and finely adjusted for each of the first fluid passages. Consequently, the amount of heat exchange can be easily and accurately optimized according to the load (the amount of heat exchange) on each type of first fluid passage.
- the diffusion-bonded heat exchanger capable of reducing the number of types of components and the number of components even when the plurality of types of fluids are handled by the common diffusion-bonded heat exchanger, and capable of sufficiently ensuring the degree of freedom of the configuration of the fluid passages can be provided.
- FIG. 1 A schematic view of a heat exchanger according to a first embodiment of the present invention as viewed from the upper surface side thereof.
- FIG. 2 A schematic view of the heat exchanger according to the first embodiment of the present invention as viewed from the side surface side thereof.
- FIG. 3 A schematic perspective view showing a first heat transfer plate and a second heat transfer plate.
- FIG. 4 A schematic view illustrating a stacked structure of first heat transfer plates and second heat transfer plates.
- FIG. 5 A plan view showing a configuration example of first fluid passages of the first heat transfer plate.
- FIG. 6 A plan view showing a configuration example of second fluid passages of the second heat transfer plate.
- FIG. 7 A sectional view of a core showing a cross section orthogonal to the first fluid passages and the second fluid passages.
- FIG. 8 A schematic view showing a first heat transfer plate of a heat exchanger according to a second embodiment.
- FIG. 9 A sectional view of the first heat transfer plate showing a cross section orthogonal to first fluid passages in FIG. 8 .
- FIG. 10 A schematic view showing a first heat transfer plate (A) and a second heat transfer plate (B) according to a first modified example of the first embodiment.
- FIG. 11 A schematic view showing a first heat transfer plate (A) and a second heat transfer plate (B) according to a second modified example of the first embodiment.
- the configuration of a heat exchanger 100 according to a first embodiment is now described with reference to FIGS. 1 to 7 .
- the heat exchanger 100 according to the first embodiment is a diffusion-bonded plate heat exchanger in which first heat transfer plates 10 and second heat transfer plates 20 , each of which includes groove-like fluid passages, are stacked and diffusion-bonded to each other to be integral and unitary with each other.
- the heat exchanger 100 is an example of a “diffusion-bonded heat exchanger” in the claims.
- the heat exchanger 100 includes a core 1 , a plurality of pairs (three pairs) of first ports 2 , and a plurality of pairs (three pairs) of second ports 3 .
- the core 1 includes a plurality of first heat transfer plates 10 including groove-like first fluid passages 11 (see FIG. 3 ) and a plurality of second heat transfer plates 20 including groove-like second fluid passages (see FIG. 3 ).
- the core 1 is a heat exchanging portion that performs heat exchange between fluids flowing through the first heat transfer plates 10 and a fluid flowing through the second heat transfer plates 20 .
- the first ports 2 are entrances and exits through which the fluids are introduced into and discharged from the first heat transfer plates 10 (first fluid passages 11 ), and are provided as pairs of the entrance side and the exit side.
- the second ports 3 are entrances and exits through which the fluid is introduced into and discharged from the second heat transfer plates 20 (second fluid passages 21 ), and are provided as pairs of the entrance side and the exit side.
- side plates 4 are provided at both ends of the core 1 in the stacking direction (direction Z) of the first heat transfer plates 10 and the second heat transfer plates 20 , respectively.
- the core 1 is formed by alternately stacking and diffusion-bonding the first heat transfer plates 10 and the second heat transfer plates 20 , each of which includes the groove-like fluid passages. That is, the core 1 is formed into a rectangular box shape (rectangular parallelepiped shape) as a whole by sandwiching a stacked body of the first heat transfer plates 10 and the second heat transfer plates 20 alternately stacked between a pair of side plates 4 and mutually joining the first heat transfer plates 10 and the second heat transfer plates 20 by diffusion bonding.
- the stacking direction of the first heat transfer plates 10 and the second heat transfer plates 20 shown in FIG. 2 is defined as a direction Z.
- the longitudinal direction of the core 1 as viewed in the direction Z is defined as a direction X
- the short-side direction of the core 1 is defined as a direction Y.
- the first heat transfer plates 10 and the second heat transfer plates 20 each have a flat plate shape and are formed into a rectangular shape in a planar view.
- the first heat transfer plates 10 and the second heat transfer plates 20 have substantially the same planar shape, and both of them have a length L 0 in the direction X (longitudinal direction) and a width W 0 in the direction Y (short-side direction).
- the first heat transfer plates 10 and the second heat transfer plates 20 each have substantially the same thickness t, but the thicknesses t of the first heat transfer plates 10 and the second heat transfer plates 20 may be different from each other.
- the first heat transfer plates 10 and the second heat transfer plates 20 are made of a stainless steel material.
- the first heat transfer plates 10 and the second heat transfer plates 20 may be made of a high thermal conductive metal material other than the stainless steel material.
- the first fluid passages 11 and the second fluid passages 21 are respectively formed on one surface 10 a (the upper surface) of each of the first heat transfer plates 10 and one surface 20 a (the upper surface) of each of the second heat transfer plates 20 .
- Another surface 10 b (the lower surface) of each of the first heat transfer plates 10 and another surface 20 b (the lower surface) of each of the second heat transfer plates 20 are both flat surfaces.
- the first heat transfer plates 10 each include a plurality of first fluid passages 11 connected to different pairs of first ports 2 (pairs of first ports 2 on the entrance side and the exit side) and isolated from each other. That is, in each of the first heat transfer plates 10 , the plurality of first fluid passages 11 through which fluids can flow independently of each other are disposed side by side.
- each of the first heat transfer plates 10 includes three first fluid passages 11 a , 11 b , and 11 c .
- the first fluid passage 11 a is connected to a pair of first ports 2 a and 2 b .
- the first fluid passage 11 b is connected to a pair of first ports 2 c and 2 d .
- the first fluid passage 11 c is connected to a pair of first ports 2 e and 2 f .
- the first ports 2 a , 2 c , and 2 e on the X 2 side are ports on the entrance side
- the first ports 2 b , 2 d , and 2 f on the X 1 side are ports on the exit side.
- Each of the first ports 2 ( 2 a to 2 f ) is a cylindrical pipe member.
- Each of the first ports 2 may be a member other than the cylindrical pipe member.
- the first ports 2 a , 2 c , and 2 e ( 2 b , 2 d , and 2 f ) may be collectively formed by forming as many through-holes as the number of ports in a block member that extends in the direction Y.
- each of the three first fluid passages 11 a , 11 b , and 11 c includes an inlet port 12 and an outlet port 13 .
- the inlet port 12 and the outlet port 13 are examples of “one end” and “another end” in the claims, respectively. Both the inlet port 12 and the outlet port 13 are circular through-holes that pass through the first heat transfer plate 10 in a thickness direction.
- (six) through-holes 5 c similar to the inlet port 12 and the outlet port 13 are formed at the corresponding locations (locations that overlap each other in the direction Z) of each of the second heat transfer plates 20 and the upper side plate 4 .
- the inlet ports 12 and the through-holes 5 c of the stacked first heat transfer plates 10 and second heat transfer plates 20 are connected in the thickness direction (direction Z) to form, as a whole, three inlet passages 5 a that extend in the direction Z in the core 1 .
- the inlet passages 5 a are connected to the first ports 2 a , 2 c , and 2 e on the entrance side, respectively.
- the outlet ports 13 and the through-holes 5 c are connected to each other to form, as a whole, three outlet passages 5 b that extend in the direction Z in the core 1 .
- the outlet passages 5 b are connected to the first ports 2 b , 2 d , and 2 f on the exit side, respectively. As described later, the second fluid passages 21 of the second heat transfer plates 20 do not communicate with the through-holes 5 c and are isolated from each other.
- Different fluids can be supplied to the first fluid passages 11 a , 11 b , and 11 c via the first ports 2 a , 2 c , and 2 e , respectively.
- the same fluid may be supplied to the first fluid passages 11 a , 11 b , and 11 c .
- the heat exchanger 100 is used as an intercooler of a multistage compression system including a plurality of compressors is shown. In this case, as shown in FIG.
- the fluid (fluid A) that has passed through a first stage compressor is supplied to the first fluid passage 11 a
- the fluid (fluid B) that has passed through a second stage compressor is supplied to the first fluid passage 11 b
- the fluid (fluid C) that has passed through a third stage compressor is supplied to the first fluid passage 11 c .
- the fluids A, B, and C are common, but the pressures thereof are different.
- the fluids may be gas or liquid.
- each of the plurality of first fluid passages 11 is formed into an elongated shape that extends in a first direction from the inlet port 12 connected to the first port 2 on the entrance side toward the corresponding outlet port 13 connected to the first port 2 on the exit side in the plane (in one surface 10 a ) of the first heat transfer plate 10 .
- the plurality of first fluid passages 11 are disposed side by side along a second direction orthogonal to the first direction.
- the first direction coincides with the direction X
- the second direction coincides with the direction Y. That is, each of the three first fluid passages 11 extends along the longitudinal direction (the long side of the first heat transfer plate 10 ) of the core 1 .
- the three first fluid passages 11 are disposed side by side along the short-side direction (the short side of the first heat transfer plate 10 ) of the core 1 .
- the plurality of first fluid passages 11 are spaced apart from each other in the second direction on the same surface (one surface 10 a ) of the first heat transfer plate 10 .
- the first heat transfer plate 10 includes a diffusion bonding surface 14 with the second heat transfer plate 20 between the first fluid passages 11 adjacent to each other in the second direction.
- the first fluid passage 11 a and the first fluid passage 11 b are disposed at an interval CL 1 in the direction Y.
- the first fluid passage 11 b and the first fluid passage 11 c are disposed at an interval CL 2 in the direction Y.
- the intervals CL 1 and CL 2 may be equal to or different from each other.
- the diffusion bonding surface 14 is a region of the interval CL 1 and a region of the interval CL 2 between the first fluid passages 11 .
- the diffusion bonding surface 14 extends in the direction X so as to partition the three first fluid passages 11 .
- An outer peripheral portion of one surface 10 a of the first heat transfer plate 10 that surrounds the three first fluid passages 11 is also a bonding surface.
- the diffusion bonding surface 14 extends from the outer peripheral portion on one end side to the outer peripheral portion on the other end side in the direction X.
- the second heat transfer plates 20 each include a plurality of second fluid passages 21 formed so as to correspond to the first fluid passages 11 of the first heat transfer plate 10 and isolated from each other. That is, in each of the second heat transfer plates 20 , the plurality of second fluid passages 21 through which fluids can flow independently of each other are disposed side by side. The plurality of second fluid passages 21 are respectively connected to different pairs of second ports 3 (pairs of second ports 3 on the entrance side and the exit side) (see FIG. 1 ).
- each of the second heat transfer plates 20 includes three second fluid passages 21 a , 21 b , and 21 c corresponding to the three first fluid passages 11 a , 11 b , and 11 c . That is, a pair of first and second fluid passages 11 a and 21 a , a pair of first and second fluid passages 11 b and 21 b , and a pair of first and second fluid passages 11 c and 21 c are formed, and heat exchange is mostly performed between each pair of fluid passages.
- the second fluid passages 21 are respectively disposed at locations that overlap the plurality of first fluid passages 11 of the first heat transfer plate 10 in a planar view. That is, each pair of first and second fluid passages 11 and 21 overlap in the stacking direction (direction Z). Therefore, heat exchange can be efficiently performed as compared with the case where each pair are disposed at locations shifted in the direction Y in a planar view and do not overlap in the direction Z, for example.
- each of the second fluid passages 21 a , 21 b , and 21 c shown in FIG. 3 is continuous from one end to another end of the second heat transfer plate 20 .
- the second fluid passages 21 a , 21 b , and 21 c each include an inlet opening 22 that opens into the interior of the header 6 a (see FIG. 2 ) from the side end face of the second heat transfer plate 20 on the X 1 side, and respectively communicate with second ports 3 a , 3 c , and 3 e (see FIG. 1 ).
- the second fluid passages 21 a , 21 b , and 21 c each include an outlet opening 23 that opens into the interior of the header 6 b (see FIG. 2 ) from the side end face of the second heat transfer plate 20 on the X 2 side, and respectively communicate with second ports 3 b , 3 d , and 3 f (see FIG. 1 ).
- the second ports 3 a , 3 c , and 3 e are ports on the entrance side
- the second ports 3 b , 3 d , and 3 f are ports on the exit side.
- each of the headers 6 a and 6 b has a semicylindrical shape (see FIG. 2 ) that extends in the direction Y, and both ends thereof in the direction Y are closed.
- the header 6 a covers the side end face of the core 1 on the X 1 side, and is provided to internally store fluids.
- the header 6 b covers the side end face of the core 1 on the X 2 side, and is provided to internally store fluids.
- Partition plates 6 c are provided inside each of the headers 6 a and 6 b .
- the interior of the header 6 a is partitioned by the partition plates 6 c into a space that connects the second fluid passage 21 a and the second port 3 a , a space that connects the second fluid passage 21 b and the second port 3 c , and a space that connects the second fluid passage 21 c and the second port 3 e .
- the interior of the header 6 b is partitioned by the partition plates 6 c into a space that connects the second fluid passage 21 a and the second port 3 b , a space that connects the second fluid passage 21 b and the second port 3 d , and a space that connects the second fluid passage 21 c and the second port 3 f .
- the second fluid passages 21 a , 21 b , and 21 c are respectively connected to the different pairs of second ports 3 (a pair of second ports 3 a and 3 b , a pair of second ports 3 c and 3 d , and a pair of second ports 3 e and 3 f ).
- Different fluids can be supplied to the second fluid passages 21 a , 21 b , and 21 c via the second ports 3 a , 3 c , and 3 e , respectively.
- the fluids to be supplied to the second fluid passages 21 may be gas or liquid.
- the same fluid may be supplied to the second fluid passages 21 a , 21 b , and 21 c .
- a fluid (fluid D) which serves as a refrigerant for cooling the compressed fluids (fluid A, fluid B, and fluid C) on the first fluid passage 11 side, is supplied to each of the second fluid passages 21 a , 21 b , and 21 c .
- the fluid D is a coolant, for example.
- the second fluid passages 21 a , 21 b , and 21 c are independent fluid passages individually connected to the second ports 3 a , 3 c , and 3 e , respectively. Therefore, even when the common fluid D is allowed to flow through each of the second fluid passages 21 a , 21 b , and 21 c , fluid characteristics such as a supply pressure and a flow rate from each port can be made different.
- each of the plurality of second fluid passages 21 is formed into an elongated shape that extends in the first direction (direction X) from the inlet opening 22 connected to the second port 3 on the entrance side toward the corresponding outlet opening 23 connected to the second port 3 on the exit side in the plane of the second heat transfer plate 20 .
- the plurality of second fluid passages 21 are disposed side by side along the second direction (direction Y) orthogonal to the first direction. That is, each of the three second fluid passages 21 extends along the longitudinal direction (the long side of the second heat transfer plate 20 ) of the core 1 .
- the three second fluid passages 21 are disposed side by side along the short-side direction (the short side of the second heat transfer plate 20 ) of the core 1 . Therefore, the plurality of first fluid passages 11 and the plurality of second fluid passages 21 overlap each other in an upward-downward direction (direction Z), and extend substantially in parallel to each other.
- the plurality of second fluid passages 21 are spaced apart from each other in the direction Y on the same surface (one surface 20 a ) of the second heat transfer plate 20 .
- the second fluid passage 21 a and the second fluid passage 21 b are disposed at an interval CL 3 in the direction Y.
- the second fluid passage 21 b and the second fluid passage 21 c are disposed at an interval CL 4 in the direction Y.
- the intervals CL 3 and CL 4 may be equal to or different from each other.
- the second heat transfer plate 20 includes a diffusion bonding surface 24 with the first heat transfer plate 10 between the second fluid passages 21 adjacent to each other in the direction Y.
- the diffusion bonding surface 24 is a region of the interval CL 3 and a region of the interval CL 4 .
- the arrangement and shape of the first fluid passages 11 of the first heat transfer plate 10 and the arrangement and shape of the second fluid passages 21 of the second heat transfer plate 20 may be substantially common.
- the intervals CL 1 , CL 2 , CL 3 , and CL 4 may be equal to each other.
- the fluids respectively flow through the first fluid passages 11 from the X 2 side to the X 1 side in the first heat transfer plate 10 , as shown in FIG. 2 .
- the fluid (fluid D) flows through the second fluid passages 21 from the X 1 side to the X 2 side.
- the heat exchanger 100 is a counter-flow heat exchanger in which the fluids that pass through the first heat transfer plate 10 and the fluid that passes through the second heat transfer plate 20 flow in opposite directions.
- the layer structure of the core 1 is schematically shown in FIG. 4 .
- the first heat transfer plates 10 through which the fluid A, the fluid B, and the fluid C to be cooled flow are stacked so as to be sandwiched by the second heat transfer plates 20 through which the fluid D serving as a refrigerant flows.
- the first fluid passages 11 each have a flow passage shape, as shown in FIG. 5 .
- FIG. 5 an example in which the three first fluid passages ( 11 a , 11 b , and 11 c ) have a common configuration is shown. That is, in the example shown in FIG. 5 , the three first fluid passages 11 ( 11 a to 11 c ) are formed into substantially the same shape.
- the three first fluid passages 11 ( 11 a to 11 c ) each have an outer shape having a length L 1 in the direction X (longitudinal direction) and a width W 1 in the direction Y (short-side direction).
- Each of the plurality of first fluid passages 11 includes a flow passage 15 that connects the inlet port 12 connected to the first port 2 on the entrance side to the outlet port 13 connected to the corresponding first port 2 on the exit side.
- the first fluid passages 11 each include the inlet port 12 , the outlet port 13 , a plurality of heat exchange passages 16 , and connection passages 17 .
- the flow passage 15 includes the heat exchange passages 16 and the connection passages 17 .
- the heat exchange passages 16 are linear flow passages provided to perform heat exchange between the fluids, extend in the direction X, and are aligned in parallel to each other in the direction Y.
- the first fluid passages 11 each include eight heat exchange passages 16 .
- the number of heat exchange passages 16 may be other than eight.
- connection passages 17 are provided between the inlet port 12 and the plurality of heat exchange passages 16 and between the outlet port 13 and the plurality of heat exchange passages 16 , respectively.
- the structures of the connection passages 17 are common on the inlet port 12 side and the outlet port 13 side, and thus only the connection passage 17 of the inlet port 12 is described.
- connection passage 17 One end side of the connection passage 17 is connected to the inlet port 12 , and another end side of the connection passage 17 is connected to each of the plurality of (eight) heat exchange passages 16 . Accordingly, the connection passage 17 has a function of distributing the fluid from the inlet port 12 to each of the heat exchange passages 16 .
- the connection passage 17 is divided from one inlet port 12 into eight branches, and is connected to each of the eight heat exchange passages 16 .
- the flow passage 15 (the heat exchange passages 16 and the connection passages 17 ) is formed as a concave groove on one surface 10 a of the first heat transfer plate 10 .
- the cross-sectional shape orthogonal to a direction in which the flow passage 15 extends is substantially semicircularly recessed.
- the flow passage 15 is formed by etching or machining, for example.
- the flow passage 15 has a flow passage width W 11 and a flow passage depth H 11 .
- the flow passage width and the flow passage depth are common in the heat exchange passages 16 and the connection passages 17 .
- the heat exchange passages 16 each have a flow passage length L 11 (see FIG.
- a partition wall 18 between the heat exchange passages 16 has a width W 12 .
- the flow passage width W 11 of the flow passage 15 is larger than the width W 12 of the partition wall 18 .
- the width (interval CL 1 or CL 2 ) of the diffusion bonding surface 14 is larger than the width W 12 of the partition wall 18 between the heat exchange passages 16 .
- the second fluid passages 21 each have a flow passage shape, as shown in FIG. 6 .
- the three second fluid passages 21 21 a , 21 b , and 21 c ) have a common configuration is shown.
- the three second fluid passages ( 21 a to 21 c ) are formed into substantially the same shape.
- the three second fluid passages 21 ( 21 a to 21 c ) each have an outer shape having a length L 2 in the direction X (longitudinal direction) and a width W 2 in the direction Y (short-side direction).
- the width W 2 is substantially equal to the width W 1 of each of the first fluid passages 11 .
- the second fluid passages 21 open to the end face of the second heat transfer plate 20 (core 1 ) in the X direction, and thus the length L 2 is larger than the length L 1 of each of the first fluid passages 11 .
- Each of the plurality of second fluid passages 21 includes a flow passage 25 that connects the inlet opening 22 connected to the second port 3 on the entrance side to the outlet opening 23 connected to the corresponding second port 3 on the exit side.
- the second fluid passages 21 each include the inlet opening 22 , the outlet opening 23 , a plurality of heat exchange passages 26 , and connection passages 27 .
- the flow passage 25 includes the heat exchange passages 26 and the connection passages 27 .
- the configurations of the heat exchange passages 26 are the same as those of the heat exchange passages 16 of the first fluid passages 11 in FIG. 5 , and the same number of (eight) heat exchange passages 26 with the same shape are provided.
- the connection passage 27 on the inlet opening 22 side includes a flow passage portion 27 a connected to the inlet opening 22 formed in the end face of the second heat transfer plate 20 .
- the flow passage portion 27 a is linearly formed, and a pair of flow passage portions 27 a are provided on both outer sides of the through-hole 5 c in the direction Y.
- the connection passage 27 is divided from each of the pair of flow passage portions 27 a into four branches so as to be divided into eight flow passages in total.
- connection passage 27 of each of the second fluid passages 21 is divided into one side and the other side in the direction Y across the through-hole 5 c , and is divided into four branch passages on each side.
- a flow passage portion 27 a is also provided in the connection passage 27 on the outlet opening 23 side, and has the same configuration.
- the flow passage 25 (the heat exchange passages 26 and the connection passages 27 ) is formed as a concave groove on one surface 20 a of the second heat transfer plate 20 .
- the cross-sectional shape orthogonal to a direction in which the flow passage 25 extends is a substantially semicircularly recessed.
- the flow passage 25 has a flow passage width W 21 and a flow passage depth H 21 .
- the flow passage width W 21 and the flow passage depth H 21 are substantially equal to the flow passage width W 11 and the flow passage depth H 11 of the flow passage 15 .
- the flow passage width W 21 of the flow passage 25 and the flow passage width W 11 of the flow passage 15 may be different from each other.
- the heat exchange passages 26 each have a flow passage length L 21 (see FIG. 6 ).
- the flow passage length L 21 is substantially equal to the flow passage length L 11 of each of the heat exchange passages 16 .
- the width (interval CL 3 or CL 4 ) of the diffusion bonding surface 24 between the adjacent second fluid passages 21 is larger than the width W 22 of a partition wall 28 between the heat exchange passages 26 .
- FIG. 7 shows an example in which the position of the flow passage 15 and the position of the flow passage 25 in the direction Y (the center positions of the flow passages) coincide with each other, but the position of the flow passage 15 in the direction Y and the position of the flow passage 25 in the direction Y may be shifted from each other.
- the high-temperature and high-pressure fluid A, fluid B, and fluid C that have passed through different compressors are supplied to the first fluid passages 11 a , 11 b , and 11 c of the first heat transfer plate 10 , respectively.
- the fluid A, the fluid B, and the fluid C flow in through the first ports 2 a , 2 c , and 2 e (see FIG. 1 ) on the entrance side connected to the respective exit sides of the compressors, and are distributed to the respective inlet ports 12 of the first fluid passages 11 a , 11 b , and 11 c .
- the respective fluids are cooled while passing through the respective flow passages 15 (the heat exchange passages 16 and the connection passages 17 ) of the first fluid passages 11 a , 11 b , and 11 c , and flow out through the corresponding first ports 2 b , 2 d , and 2 f (see FIG. 1 ) on the exit side, respectively.
- the fluid (fluid D) serving as a refrigerant is supplied to each of the second fluid passages 21 a , 21 b , and 21 c of the second heat transfer plate 20 .
- the fluid D flows in through each of the second ports 3 a , 3 c , and 3 e (see FIG. 1 ) on the entrance side, passes through an internal space of the header 6 a partitioned by the partition plates 6 c , and flows into each of the second fluid passages 21 a , 21 b , and 21 c .
- the supply pressures to the second ports 3 a , 3 c , and 3 e are individually adjusted according to variations in the amount of heat exchange with the first fluid passages 11 a , 11 b , and 11 c .
- the fluid D is heated (draws heat) while passing through the respective flow passages 25 (the heat exchange passages 26 and the connection passages 27 ) of the second fluid passages 21 a , 21 b , and 21 c , and flows out through each of the second ports 3 b , 3 d , and 3 f (see FIG. 1 ) on the exit side.
- the first heat transfer plate 10 including the plurality of first fluid passages 11 connected to the different pairs of first ports 2 (the pair of 2 a and 2 b , the pair of 2 c and 2 d , and the pair of 2 e and 2 f ) and isolated from each other is provided.
- the first heat transfer plate 10 including a plurality of types of first fluid passages 11 can be provided. That is, instead of providing a heat transfer plate for each type of fluid, the first heat transfer plate 10 common to a plurality of types of fluids can be provided.
- the number of types of components (the number of types of first heat transfer plates 10 ) and the number of components (the total number of first and second heat transfer plates 10 and 20 ) can be reduced.
- the same configuration as in the first embodiment is realized by individual heat transfer plates, for example, three types of three heat transfer plates corresponding to the first fluid passages 11 a , 11 b , and 11 c (three types and nine plates in total) and ten heat transfer plates corresponding to the second fluid passages 21 (one type and ten plates) are required. That is, four types of nineteen heat transfer plates in total are required.
- the first embodiment only needs two types of seven first and second heat transfer plates 10 and 20 in total.
- the plurality of types of first fluid passages 11 can be formed in the same first heat transfer plate 10 , and thus for example, one first fluid passage 11 is reduced in size according to a load (the amount of heat exchange) on each fluid etc. such that another first fluid passage 11 can be formed in an empty space, or the planar size of a product can be reduced. That is, the degree of freedom in the configuration of the fluid passages can be sufficiently ensured.
- a load the amount of heat exchange
- the second heat transfer plate 20 including the plurality of second fluid passages 21 formed so as to correspond to the first fluid passages 11 of the first heat transfer plate 10 and isolated from each other is provided.
- the plurality of second fluid passages 21 are formed so as to correspond to the plurality of first fluid passages 11 such that heat exchange between the fluids can be efficiently performed.
- the plurality of second fluid passages 21 are respectively connected to the different pairs of second ports 3 (the pair of 3 a and 3 b , the pair of 3 c and 3 d , and the pair of 3 e and 3 f ).
- the type, the flow rate, etc. of the fluid that flows through each of the second fluid passages 21 can be individually set for each of the second fluid passages 21 according to the amount of heat exchange between the fluids that flow through the first fluid passages 11 and the second fluid passages 21 corresponding to each other.
- the second fluid passages 21 are equal in number to the first fluid passages 11 . Furthermore, the second fluid passages 21 are respectively disposed at the locations that overlap the plurality of first fluid passages 11 of the first heat transfer plate 10 in the planar view. Thus, the plurality of second fluid passages 21 can be provided in a one-to-one correspondence with the plurality of first fluid passages 11 .
- one wide second fluid passage (one second fluid passage corresponding to the three first fluid passages 11 ) is provided at a location that overlaps the first fluid passages 11 a to 11 c , for example, it becomes difficult to independently adjust the amount of heat exchange between one first fluid passage 11 a and the second fluid passage and the amount of heat exchange between another first fluid passage 11 b and the second fluid passage.
- the first fluid passages 11 a , 11 b , and 11 c are provided in a one-to-one correspondence with the second fluid passages 21 a , 21 b , and 21 c such that heat exchange can be efficiently performed between the fluids that flow through pairs of the first fluid passages 11 a , 11 b , and 11 c and the second fluid passages 21 a , 21 b , and 21 c corresponding to each other.
- the flow rate of the fluid that flows through the second fluid passages 21 for example, can be easily optimized.
- the plurality of first fluid passages 11 are each formed into an elongated shape that extends in the direction X from the inlet port 12 toward the corresponding outlet port 13 in one surface 10 a of the first heat transfer plate 10 , and are disposed side by side along the direction Y orthogonal to the direction X.
- the flow rate can be easily increased to improve the heat transfer coefficient even with a simple flow passage shape.
- first fluid passages 11 each having an elongated shape that extends in the direction X are disposed side by side along the direction Y such that the vertical and horizontal dimensions of the outer shape of the entire first heat transfer plate 10 can be brought closer to each other (the aspect ratio can be brought closer to 1). Consequently, variations in the load at the time of performing diffusion bonding can be suppressed, and the ease of manufacturing the core 1 can be improved.
- the plurality of first fluid passages 11 are spaced apart from each other in the direction Y on one surface 10 a of the first heat transfer plate 10 . Furthermore, the diffusion bonding surface 14 with the second heat transfer plate 20 is provided in the first heat transfer plate 10 between the first fluid passages 11 adjacent to each other in the direction Y. Thus, each of the plurality of first fluid passages 11 disposed on one surface 10 a of the first heat transfer plate 10 can be easily isolated as an independent fluid passage. Furthermore, the diffusion bonding surface 14 that extends in the direction X can be formed between the plurality of first fluid passages 11 aligned in the direction Y.
- the width (CL 1 or CL 2 ) of the diffusion bonding surface 14 is larger than the width W 12 of the partition wall 18 such that the diffusion bonding strength between the first heat transfer plate 10 and the second heat transfer plate 20 can be easily ensured as compared with the case where the first heat transfer plate 10 and the second heat transfer plate 20 are bonded to each other only with the outer peripheral portion of the heat transfer plate surface or a gap (partition wall 18 ) between the flow passages constituting the first fluid passages 11 , for example.
- the plurality of second fluid passages 21 of the second heat transfer plate 20 are spaced apart from each other in the direction Y, and the diffusion bonding surface 24 with the first heat transfer plate 10 is provided between the second fluid passages 21 adjacent to each other in the direction Y such that each of the plurality of second fluid passages 21 can be easily isolated as an independent fluid passage.
- the width (CL 3 or CL 4 ) of the diffusion bonding surface 24 is larger than the width W 22 of the partition wall 28 such that the diffusion bonding strength between the first heat transfer plate 10 and the second heat transfer plate 20 can be easily ensured.
- a second embodiment is now described with reference to FIGS. 8 and 9 .
- this second embodiment an example in which the shapes of three first fluid passages 111 a to 111 c are different is described unlike the aforementioned first embodiment in which the three first fluid passages 11 a to 11 c are formed into a common shape.
- a first heat transfer plate 110 includes three first fluid passages 111 ( 111 a , 111 b , and 111 c ) connected to different pairs of first ports 2 (a pair of first ports 2 a and 2 b , a pair of first ports 2 c and 2 d , and a pair of first ports 2 e and 2 f ) (see FIG. 1 ) and isolated from each other.
- the heat exchanger 200 is an example of a “diffusion-bonded heat exchanger” in the claims.
- At least one of a plurality of (three) first fluid passages 111 is different from another one of the plurality of first fluid passages 111 in at least one of the flow passage width of a flow passage 15 , the flow passage length of the flow passage 15 , the flow passage depth of the flow passage 15 , and the number of flow passages 15 .
- the first fluid passage 111 b at the center in a direction Y of the three first fluid passages 111 a , 111 b , and 111 c is larger in size than the first fluid passages 111 a and 111 c on both sides in the direction Y.
- the first fluid passages 111 a and 111 c have a common configuration.
- the first fluid passage 111 b as a whole has a length L 3 b in a direction X and a width W 3 b in the direction Y.
- the first fluid passages 111 a and 111 c as a whole each have a length L 3 a in the direction X and a width W 3 a in the direction Y.
- the length L 3 a of each of the first fluid passages 111 a and 111 c and the length L 3 b of the first fluid passage 111 b are equal to each other.
- the length L 3 a and the length L 3 b may be different from each other.
- the width W 3 a of each of the first fluid passages 111 a and 111 c is smaller than the width W 3 b of the first fluid passage 111 b .
- the width W 3 a may be larger than the width W 3 b .
- the length L 3 a is equal to the length L 1 of the first fluid passage 11 in FIG.
- the width W 3 a is smaller than the width W 1 of the first fluid passage 11 in FIG. 5 .
- the length L 3 b is equal to the length L 1 of the first fluid passage 11 in FIG. 5 .
- the width W 3 b is larger than the width W 1 of the first fluid passage 11 in FIG. 5 . Therefore, according to the second embodiment, in the first heat transfer plate 110 , the first fluid passages 111 a and 111 c are reduced in size, and thus a larger space is allocated to the first fluid passage 111 b.
- a flow passage 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ) includes four heat exchange passages 116 a ( 116 c ). Unlike the aforementioned first embodiment, connection passages 117 a ( 117 c ) are divided into four branches and are connected in parallel to each of the heat exchange passages 116 a ( 116 c ). The heat exchange passages 116 a ( 116 c ) each have a flow passage length L 31 . As shown in FIG. 9 , the flow passage 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ) has a flow passage width W 31 and a flow passage depth H 31 .
- a flow passage 115 b of the first fluid passage 111 b includes nine heat exchange passages 116 b , which are more than the four first fluid passages 111 a ( 111 c ).
- Connection passages 117 b are divided into nine branches and are connected in parallel to each of the heat exchange passages 116 b .
- the heat exchange passages 116 b each have a flow passage length L 32 .
- the flow passage 115 b of the first fluid passage 111 b has a flow passage width W 32 and a flow passage depth H 32 .
- the flow passage width W 32 of the flow passage 115 b of the first fluid passage 111 b is larger than the flow passage width W 31 of the flow passage 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ).
- the flow passage depth H 32 of the flow passage 115 b of the first fluid passage 111 b is equal to the flow passage depth H 31 of the flow passage 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ).
- the flow passage length L 32 of each of the heat exchange passages 116 b of the first fluid passage 111 b is equal to the flow passage length L 31 of the flow passage 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ).
- the flow passage width W 32 of the first fluid passage 111 b is larger than the flow passage width W 31 of each of the first fluid passages 111 a and 111 c
- the number of (nine) flow passages 115 b of the first fluid passage 111 b is larger than the number of (four) flow passages 115 a ( 115 c ) of the first fluid passage 111 a ( 111 c ).
- These flow passage widths and the number of flow passages 115 are set according to the types of fluids that respectively flow through the first fluid passages 111 a to 111 c or the magnitudes of the loads (amount of heat exchange) on the fluids. Therefore, in the first fluid passage 111 b , the amount of heat exchange is larger than in the first fluid passages 111 a and 111 c.
- the first fluid passage 111 b is different from the remaining first fluid passages 111 a and 111 c in the flow passage width and the number of flow passages.
- the example in which the flow passage width and the number of flow passages are different is shown, but only one of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages may alternatively be different. All of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages may alternatively be different.
- first fluid passages 111 a , 111 b , and 111 c may have configurations different from each other (configurations in which any of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages is different).
- second fluid passages 21 of the second heat transfer plate 20 also have the same shapes corresponding to the aforementioned first fluid passages 111 a to 111 c , respectively.
- the first heat transfer plate 110 including the plurality of first fluid passages 111 connected to the different pairs of first ports 2 (the pair of 2 a and 2 b , the pair of 2 c and 2 d , and the pair of 2 e and 2 f ) and isolated from each other is provided such that even when a plurality of types of fluids are handled by the common diffusion-bonded heat exchanger 200 , the number of types of components and the number of components can be reduced.
- first fluid passages 111 a to 111 c can be formed in the same first heat transfer plate 110 , and thus the degree of freedom of the configuration of the fluid passage for each type according to the load (amount of heat exchange) on each fluid can be sufficiently ensured. That is, the shapes and layouts of the first fluid passages 111 a , 111 b , and 111 c can be freely set in the first heat transfer plate 110 .
- the first fluid passage 111 b of the plurality of first fluid passages 111 a to 111 c is different from another first fluid passages 111 a ( 111 c ) in at least one of the flow passage width W 32 of the flow passage 115 b , the flow passage length L 32 of the flow passage 115 b , the flow passage depth H 32 of the flow passage 115 b , and the number of flow passages 115 b .
- the configurations (the flow passage width of the flow passage, the flow passage length of the flow passage, the flow passage depth of the flow passage, and the number of flow passages) of the plurality of types of first fluid passages 111 a to 111 c are different in this manner such that a surplus amount of heat exchange that cannot be adjusted with a change in the number of stacked heat transfer plates can be easily and finely adjusted for each of the first fluid passages 111 a to 111 c . Consequently, the amount of heat exchange can be easily and accurately optimized according to the load (amount of heat exchange) on each type of first fluid passage 111 .
- the heat exchanger may be a parallel-flow heat exchanger in which the fluids that pass through the first heat transfer plate 10 and the fluid that passes through the second heat transfer plate 20 flow in the same direction, or a cross-flow heat exchanger in which the flows of the fluids cross (see FIG. 10 ), for example.
- the present invention is not restricted to this.
- the first heat transfer plates and the second heat transfer plates may not necessarily be alternately stacked.
- two (a plurality of) second heat transfer plates may be stacked on one first heat transfer plate such that a second heat transfer plate, a first heat transfer plate, a second heat transfer plate, a second heat transfer plate, a first heat transfer plate, . . . are stacked along a direction Z.
- one second heat transfer plate may be stacked on two (a plurality of) first heat transfer plates.
- first fluid passages 11 are provided in the first heat transfer plate 10 ( 110 )
- the present invention is not restricted to this. According to the present invention, two or four or more first fluid passages 11 may be provided in the first heat transfer plate 10 .
- the present invention is not restricted to this. According to the present invention, only one second fluid passage may be provided, for example.
- one common second fluid passage 221 may be provided in a second heat transfer plate 220 for three first fluid passages 11 of a first heat transfer plate 10 .
- the second fluid passage 221 extends in a direction Y orthogonal to the first fluid passages 11 , and a cross-flow heat exchanger is formed.
- the width W 5 of the second fluid passage 221 in a direction X is substantially equal to the length L 1 of each of the first fluid passages 11 , and the second fluid passage 221 extends from one end to the other end of the second heat transfer plate 220 in the direction Y.
- heat exchange is performed between a fluid D that flows through one (common) second fluid passage 221 and fluids, A, B, and C that respectively flow through the three first fluid passages 11 .
- the number of second fluid passages may be any number.
- the second fluid passages may be equal in number to the first fluid passages, or a plurality of second fluid passages other than one may be provided.
- a plurality of (two, for example) second fluid passages may be provided so as to correspond to one first fluid passage.
- the present invention is not restricted to this.
- the three second fluid passages 21 a to 21 c may be connected to common second ports.
- the partition plates 6 c provided in each of the headers 6 a and 6 b may be removed.
- the internal spaces of the headers 6 a and 6 b are connected, and the three second fluid passages 21 a to 21 c are connected to the common second ports 3 .
- three pairs of second ports 3 may be provided, but it is only required to provide at least a pair of second ports 3 on the entrance side ( 3 c , for example) and on the exit side ( 3 d , for example).
- FIG. 11 a fluid A, a fluid B, and a fluid C are respectively supplied to three first fluid passages 11 of a first heat transfer plate 10 ( FIG. 11(A) ), and a fluid D, a fluid E, and a fluid F are respectively supplied to three second fluid passages 21 of a second heat transfer plate ( FIG. 11(B) ).
- heat exchange is performed between the fluid A in a first fluid passage 11 a and the fluid D in a second fluid passage 21 a , between the fluid B in a first fluid passage 11 b and the fluid E in a second fluid passage 21 b , and between the fluid C in a first fluid passage 11 c and the fluid F in a second fluid passage 21 c .
- the fluids A to F may be different types of fluids, or some of the fluids A to F may be the same type of fluids.
- first and second heat transfer plates 10 and 20 are provided has been shown in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, three or more types of heat transfer plates including a third heat transfer plate, for example, may be provided. However, rather than providing the third heat transfer plate, fluid passages provided in the third heat transfer plate are preferably provided in the first heat transfer plate 10 and the second heat transfer plate 20 since the number of types of components (the number of types of heat transfer plates) and the number of components can be reduced.
- each of the first fluid passages 11 are each formed into an elongated shape that extends in the direction X from the inlet port 12 on the entrance side toward the corresponding outlet port 13 on the exit side, and are disposed side by side along the direction Y orthogonal to the direction X
- each of the first fluid passages may not be formed into an elongated shape.
- each of the first fluid passages may be formed into a square shape or a shape other than a rectangular shape.
- first fluid passages may not be disposed side by side in the short-side direction (direction Y) orthogonal to the longitudinal direction (direction X).
- first fluid passages may be respectively disposed in regions obtained by dividing the first heat transfer plate into four vertically and horizontally (in a matrix).
- the configuration of the flow passage constituting each of the first fluid passages and the second fluid passages is not particularly limited.
- the shape of the flow passage and the number of flow passages may be arbitrarily set.
- bent or curved heat exchange passages may be provided.
- the number of branches of the connection passages may be other than the aforementioned four branches, eight branches, and nine branches, and may be the number of branches corresponding to the number of heat exchange passages to be connected.
- the flow passage 15 constituting each of the first fluid passages 11 a to 11 c may have shapes different from each other.
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Abstract
Description
- The present invention relates to a diffusion-bonded heat exchanger, and more particularly, it relates to a diffusion-bonded heat exchanger in which a plurality of heat transfer plates including groove-like fluid passages are stacked and diffusion-bonded to each other.
- Conventionally, a diffusion-bonded heat exchanger in which a plurality of heat transfer plates including groove-like fluid passages are stacked and diffusion-bonded to each other is known. Such a diffusion-bonded heat exchanger is disclosed in Japanese Patent Laid-Open No. 2013-155971, for example.
- Japanese Patent Laid-Open No. 2013-155971 discloses a heat exchanger including a core in which first heat transfer plates and second heat transfer plates are alternately stacked and are diffusion-bonded to each other. There are four types of first heat transfer plates A, B, C, and D, and each type includes a plurality of first heat transfer plates. There is one type of second heat transfer plates E, and this type includes a plurality of second heat transfer plates. In the core, the respective heat transfer plates are stacked in the order of EAE . . . , EBE . . . , ECE . . . , and EDE . . . . The outer shapes of the four types of first heat transfer plates and one type of second heat transfer plates are common. The heat exchanger disclosed in Japanese Patent Laid-Open No. 2013-155971 is configured as an intercooler of a multistage compression system using four compressors. A fluid (hydrogen) that has passed through the first to fourth stage compressors flows through each of the four types of first heat transfer plates A, B, C, and D, and a refrigerant (cooling water) flows through the second heat transfer plate E. The core is provided with a plurality of ports connected to connection passages that pass through the heat transfer plates in a thickness direction and corresponding to the heat transfer plates A to E, respectively. Fluid distribution to each of the heat transfer plates A to E is performed through the corresponding port.
- However, in Japanese Patent Laid-Open No. 2013-155971, each of the four types of first heat transfer plates A to D and one type of second heat transfer plates E that sandwich each first heat transfer plate therebetween in an upward-downward direction need to include a plurality of heat transfer plates. Therefore, in Japanese Patent Laid-Open No. 2013-155971, when a common diffusion-bonded heat exchanger handles a plurality of types of fluids, the number of types of components (the number of types of heat transfer plates) and the number of components (the total number of heat transfer plates) disadvantageously increase.
- Furthermore, in Japanese Patent Laid-Open No. 2013-155971, in order to stack and diffusion-bond the four types of first heat transfer plates and one type of second heat transfer plates, it is necessary to commonize the outer shapes of the respective heat transfer plates, and when loads on the first heat transfer plates are greatly different from each other, the degree of freedom disadvantageously decreases, and the optimization disadvantageously becomes difficult.
- The present invention has been proposed in order to solve the aforementioned problems, and one object of the present invention is to provide a diffusion-bonded heat exchanger capable of reducing the number of types of components and the number of components even when a plurality of types of fluids are handled by a common diffusion-bonded heat exchanger, and capable of sufficiently ensuring the degree of freedom of the configuration of fluid passages.
- In order to attain the aforementioned object, a diffusion-bonded heat exchanger according to the present invention includes a core in which a first heat transfer plate and a second heat transfer plate each including a groove-like fluid passage are stacked and diffusion-bonded to each other, a plurality of pairs of first ports through which fluids are introduced into and discharged from the first heat transfer plate, and at least a pair of second ports through which a fluid is introduced into and discharged from the second heat transfer plate, and the first heat transfer plate includes a plurality of first fluid passages connected to different pairs of the first ports and isolated from each other.
- As described above, the diffusion-bonded heat exchanger according to the present invention includes the first heat transfer plate including the plurality of first fluid passages connected to the different pairs of first ports and isolated from each other. Thus, instead of providing a plurality of types of first heat transfer plates, the first heat transfer plate including a plurality of types of first fluid passages can be provided. That is, instead of providing a heat transfer plate for each type of fluid, the first heat transfer plate common to a plurality of types of fluids can be provided. Consequently, even when the plurality of types of fluids are handled by the common diffusion-bonded heat exchanger, the number of types of components and the number of components can be reduced. Furthermore, the plurality of types of first fluid passages can be formed in the same first heat transfer plate, and thus for example, one first fluid passage is reduced in size according to a load (the amount of heat exchange) on each fluid etc. such that another first fluid passage can be formed in an empty space, or the planar size of a product can be reduced. That is, the degree of freedom in the configuration of the fluid passages can be sufficiently ensured.
- In the aforementioned diffusion-bonded heat exchanger according to the present invention, the second ports preferably include a plurality of pairs of second ports, the second heat transfer plate preferably includes a plurality of second fluid passages formed so as to correspond to the first fluid passages of the first heat transfer plate and isolated from each other, and the plurality of second fluid passages are preferably respectively connected to different pairs of the second ports. Here, the term “corresponding” indicates the relationship in which heat exchange is mostly performed between the fluid that flows through one first fluid passage and the fluid that flows through the second fluid passage(s). One first fluid passage may correspond to one second fluid passage, or one second fluid passage may correspond to a plurality of first fluid passages. According to this configuration, the plurality of second fluid passages are formed so as to correspond to the plurality of first fluid passages such that heat exchange between the fluids can be efficiently performed. Furthermore, the plurality of second fluid passages are connected to the different pairs of second ports such that the type, the flow rate, etc. of the fluid that flows through each of the second fluid passages can be individually set for each of the second fluid passages according to the amount of heat exchange between the fluids that flow through the first fluid passages and the second fluid passages corresponding to each other.
- In this case, the second fluid passages are preferably equal in number to the first fluid passages, and the second fluid passages are preferably respectively disposed at locations that overlap the plurality of first fluid passages of the first heat transfer plate in a planar view. According to this configuration, the plurality of second fluid passages can be provided in a one-to-one correspondence with the plurality of first fluid passages. Here, when one wide second fluid passage (one second fluid passage corresponding to the plurality of first fluid passages) is provided at a location that overlaps the plurality of first fluid passages, for example, it becomes difficult to independently adjust the amount of heat exchange between one first fluid passage and the second fluid passage and the amount of heat exchange between another first fluid passage and the second fluid passage. On the other hand, the first fluid passages are provided in a one-to-one correspondence with the second fluid passages such that heat exchange can be efficiently performed between the fluids that flow through pairs of the
first fluid passages second fluid passages - In the aforementioned diffusion-bonded heat exchanger according to the present invention, the plurality of first fluid passages are each preferably formed into an elongated shape that extends in a first direction from one end connected to the first port on an entrance side toward another end connected to the first port on an exit side corresponding thereto in a plane of the first heat transfer plate, and are preferably disposed side by side along a second direction orthogonal to the first direction. Here, the term “elongated shape” indicates a shape in which in the plane of the first heat transfer plate, one (first direction) of two directions orthogonal to each other is a longitudinal direction, and the other one (second direction) is a short-side direction. According to this configuration, the plurality of first fluid passages are each formed into an elongated shape from one end toward another end such that the flow rate can be easily increased to improve the heat transfer coefficient even with a simple flow passage shape as compared with the case where the plurality of first fluid passages are each formed into a wide shape. On the other hand, as the outer shape of the entire first heat transfer plate is more elongated, a load applied to a stacked body of the first heat transfer plate and the second heat transfer plate when diffusion bonding is performed is more likely to vary, and the ease of manufacturing the core is reduced. Therefore, the first fluid passages each having an elongated shape that extends in the first direction are disposed side by side along the second direction such that the vertical and horizontal dimensions of the outer shape of the entire first heat transfer plate can be brought closer to each other (the aspect ratio can be brought closer to 1). Consequently, variations in the load at the time of performing diffusion bonding can be suppressed, and the ease of manufacturing the core can be improved.
- In this case, the plurality of first fluid passages are preferably spaced apart from each other in the second direction on a same surface of the first heat transfer plate, and the first heat transfer plate preferably includes a diffusion bonding surface with the second heat transfer plate between the first fluid passages adjacent to each other in the second direction. According to this configuration, each of the plurality of first fluid passages disposed on the same surface of the first heat transfer plate can be easily isolated as an independent fluid passage. Furthermore, on the surface of the first heat transfer plate, the diffusion bonding surface that extends in the first direction can be formed between the plurality of first fluid passages aligned in the second direction, and thus the diffusion bonding strength between the first heat transfer plate and the second heat transfer plate can be easily ensured as compared with the case where the first heat transfer plate and the second heat transfer plate are bonded to each other only with the outer peripheral portion of the heat transfer plate surface or a gap (partition wall) between the flow passages constituting the first fluid passages, for example.
- In the aforementioned diffusion-bonded heat exchanger according to the present invention, each of the plurality of first fluid passages preferably includes a flow passage that connects one end connected to the first port on an entrance side to another end connected to the first port on an exit side corresponding thereto, and at least one of the plurality of first fluid passages is preferably different from another one of the plurality of first fluid passages in at least one of a flow passage width of the flow passage, a flow passage length of the flow passage, a flow passage depth of the flow passage, and a number of the flow passages. Here, when a plurality of types of fluid passages are individually provided on separate heat transfer plates (a plurality of types of heat transfer plates are provided), there is almost no degree of freedom in the configuration of the fluid passages in each of the heat transfer plates, and thus it is necessary to adjust the load using the number of stacked heat transfer plates as a unit. Therefore, even when a change in the number of stacked heat transfer plates, i.e. any number of stacked heat transfer plates such as two or three stacked heat transfer plates, does not result in a balance of the amount of heat exchange, according to the present invention, the plurality of types of first fluid passages are different in configuration (the flow passage width of the flow passage, the flow passage length of the flow passage, the flow passage depth of the flow passage, or the number of flow passages) such that a surplus amount of heat exchange that cannot be adjusted by the number of heat transfer plates can be easily and finely adjusted for each of the first fluid passages. Consequently, the amount of heat exchange can be easily and accurately optimized according to the load (the amount of heat exchange) on each type of first fluid passage.
- According to the present invention, as described above, the diffusion-bonded heat exchanger capable of reducing the number of types of components and the number of components even when the plurality of types of fluids are handled by the common diffusion-bonded heat exchanger, and capable of sufficiently ensuring the degree of freedom of the configuration of the fluid passages can be provided.
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FIG. 1 A schematic view of a heat exchanger according to a first embodiment of the present invention as viewed from the upper surface side thereof. -
FIG. 2 A schematic view of the heat exchanger according to the first embodiment of the present invention as viewed from the side surface side thereof. -
FIG. 3 A schematic perspective view showing a first heat transfer plate and a second heat transfer plate. -
FIG. 4 A schematic view illustrating a stacked structure of first heat transfer plates and second heat transfer plates. -
FIG. 5 A plan view showing a configuration example of first fluid passages of the first heat transfer plate. -
FIG. 6 A plan view showing a configuration example of second fluid passages of the second heat transfer plate. -
FIG. 7 A sectional view of a core showing a cross section orthogonal to the first fluid passages and the second fluid passages. -
FIG. 8 A schematic view showing a first heat transfer plate of a heat exchanger according to a second embodiment. -
FIG. 9 A sectional view of the first heat transfer plate showing a cross section orthogonal to first fluid passages inFIG. 8 . -
FIG. 10 A schematic view showing a first heat transfer plate (A) and a second heat transfer plate (B) according to a first modified example of the first embodiment. -
FIG. 11 A schematic view showing a first heat transfer plate (A) and a second heat transfer plate (B) according to a second modified example of the first embodiment. - Embodiments of the present invention are hereinafter described on the basis of the drawings.
- The configuration of a
heat exchanger 100 according to a first embodiment is now described with reference toFIGS. 1 to 7 . Theheat exchanger 100 according to the first embodiment is a diffusion-bonded plate heat exchanger in which firstheat transfer plates 10 and secondheat transfer plates 20, each of which includes groove-like fluid passages, are stacked and diffusion-bonded to each other to be integral and unitary with each other. Theheat exchanger 100 is an example of a “diffusion-bonded heat exchanger” in the claims. - As shown in
FIGS. 1 and 2 , theheat exchanger 100 includes acore 1, a plurality of pairs (three pairs) offirst ports 2, and a plurality of pairs (three pairs) ofsecond ports 3. As shown inFIG. 2 , thecore 1 includes a plurality of firstheat transfer plates 10 including groove-like first fluid passages 11 (seeFIG. 3 ) and a plurality of secondheat transfer plates 20 including groove-like second fluid passages (seeFIG. 3 ). Thecore 1 is a heat exchanging portion that performs heat exchange between fluids flowing through the firstheat transfer plates 10 and a fluid flowing through the secondheat transfer plates 20. Thefirst ports 2 are entrances and exits through which the fluids are introduced into and discharged from the first heat transfer plates 10 (first fluid passages 11), and are provided as pairs of the entrance side and the exit side. Thesecond ports 3 are entrances and exits through which the fluid is introduced into and discharged from the second heat transfer plates 20 (second fluid passages 21), and are provided as pairs of the entrance side and the exit side. - As shown in
FIG. 2 , side plates 4 are provided at both ends of thecore 1 in the stacking direction (direction Z) of the firstheat transfer plates 10 and the secondheat transfer plates 20, respectively. Thecore 1 is formed by alternately stacking and diffusion-bonding the firstheat transfer plates 10 and the secondheat transfer plates 20, each of which includes the groove-like fluid passages. That is, thecore 1 is formed into a rectangular box shape (rectangular parallelepiped shape) as a whole by sandwiching a stacked body of the firstheat transfer plates 10 and the secondheat transfer plates 20 alternately stacked between a pair of side plates 4 and mutually joining the firstheat transfer plates 10 and the secondheat transfer plates 20 by diffusion bonding. For the sake of simplicity,FIG. 2 shows an example in which three layers of (three) firstheat transfer plates 10 and four layers of (four) secondheat transfer plates 20 are alternately stacked, but the number of stacked plates is not restricted to this, and any number of plates may be stacked. In the following description, the stacking direction of the firstheat transfer plates 10 and the secondheat transfer plates 20 shown inFIG. 2 is defined as a direction Z. As shown inFIG. 1 , the longitudinal direction of thecore 1 as viewed in the direction Z is defined as a direction X, and the short-side direction of thecore 1 is defined as a direction Y. - As shown in
FIG. 3 , the firstheat transfer plates 10 and the secondheat transfer plates 20 each have a flat plate shape and are formed into a rectangular shape in a planar view. The firstheat transfer plates 10 and the secondheat transfer plates 20 have substantially the same planar shape, and both of them have a length L0 in the direction X (longitudinal direction) and a width W0 in the direction Y (short-side direction). The firstheat transfer plates 10 and the secondheat transfer plates 20 each have substantially the same thickness t, but the thicknesses t of the firstheat transfer plates 10 and the secondheat transfer plates 20 may be different from each other. The firstheat transfer plates 10 and the secondheat transfer plates 20 are made of a stainless steel material. The firstheat transfer plates 10 and the secondheat transfer plates 20 may be made of a high thermal conductive metal material other than the stainless steel material. The firstfluid passages 11 and the secondfluid passages 21 are respectively formed on onesurface 10 a (the upper surface) of each of the firstheat transfer plates 10 and onesurface 20 a (the upper surface) of each of the secondheat transfer plates 20. Another surface 10 b (the lower surface) of each of the firstheat transfer plates 10 and anothersurface 20 b (the lower surface) of each of the secondheat transfer plates 20 are both flat surfaces. - According to the first embodiment, the first
heat transfer plates 10 each include a plurality of firstfluid passages 11 connected to different pairs of first ports 2 (pairs offirst ports 2 on the entrance side and the exit side) and isolated from each other. That is, in each of the firstheat transfer plates 10, the plurality of firstfluid passages 11 through which fluids can flow independently of each other are disposed side by side. - In an example shown in
FIG. 3 , each of the firstheat transfer plates 10 includes three firstfluid passages FIG. 1 , thefirst fluid passage 11 a is connected to a pair offirst ports 2 a and 2 b. The first fluid passage 11 b is connected to a pair offirst ports 2 c and 2 d. Thefirst fluid passage 11 c is connected to a pair of first ports 2 e and 2 f. According to the first embodiment, thefirst ports first ports 2 may be a member other than the cylindrical pipe member. For example, thefirst ports - As shown in
FIG. 3 , each of the three firstfluid passages inlet port 12 and anoutlet port 13. Theinlet port 12 and theoutlet port 13 are examples of “one end” and “another end” in the claims, respectively. Both theinlet port 12 and theoutlet port 13 are circular through-holes that pass through the firstheat transfer plate 10 in a thickness direction. As shown inFIG. 2 , (six) through-holes 5 c similar to theinlet port 12 and theoutlet port 13 are formed at the corresponding locations (locations that overlap each other in the direction Z) of each of the secondheat transfer plates 20 and the upper side plate 4. Therefore, theinlet ports 12 and the through-holes 5 c of the stacked firstheat transfer plates 10 and second heat transfer plates 20 (side plate 4) are connected in the thickness direction (direction Z) to form, as a whole, three inlet passages 5 a that extend in the direction Z in thecore 1. The inlet passages 5 a are connected to thefirst ports outlet ports 13 and the through-holes 5 c are connected to each other to form, as a whole, three outlet passages 5 b that extend in the direction Z in thecore 1. The outlet passages 5 b are connected to the first ports 2 b, 2 d, and 2 f on the exit side, respectively. As described later, the secondfluid passages 21 of the secondheat transfer plates 20 do not communicate with the through-holes 5 c and are isolated from each other. - Different fluids can be supplied to the first
fluid passages first ports fluid passages heat exchanger 100 is used as an intercooler of a multistage compression system including a plurality of compressors is shown. In this case, as shown inFIG. 3 , the fluid (fluid A) that has passed through a first stage compressor is supplied to thefirst fluid passage 11 a, the fluid (fluid B) that has passed through a second stage compressor is supplied to the first fluid passage 11 b, and the fluid (fluid C) that has passed through a third stage compressor is supplied to thefirst fluid passage 11 c. In this case, the fluids A, B, and C are common, but the pressures thereof are different. The fluids may be gas or liquid. - According to the first embodiment, each of the plurality of first
fluid passages 11 is formed into an elongated shape that extends in a first direction from theinlet port 12 connected to thefirst port 2 on the entrance side toward thecorresponding outlet port 13 connected to thefirst port 2 on the exit side in the plane (in onesurface 10 a) of the firstheat transfer plate 10. The plurality of firstfluid passages 11 are disposed side by side along a second direction orthogonal to the first direction. - According to the first embodiment, the first direction coincides with the direction X, and the second direction coincides with the direction Y. That is, each of the three first
fluid passages 11 extends along the longitudinal direction (the long side of the first heat transfer plate 10) of thecore 1. The three firstfluid passages 11 are disposed side by side along the short-side direction (the short side of the first heat transfer plate 10) of thecore 1. - According to the first embodiment, the plurality of first
fluid passages 11 are spaced apart from each other in the second direction on the same surface (onesurface 10 a) of the firstheat transfer plate 10. The firstheat transfer plate 10 includes adiffusion bonding surface 14 with the secondheat transfer plate 20 between the firstfluid passages 11 adjacent to each other in the second direction. In the example shown inFIG. 3 , thefirst fluid passage 11 a and the first fluid passage 11 b are disposed at an interval CL1 in the direction Y. The first fluid passage 11 b and thefirst fluid passage 11 c are disposed at an interval CL2 in the direction Y. The intervals CL1 and CL2 may be equal to or different from each other. Thediffusion bonding surface 14 is a region of the interval CL1 and a region of the interval CL2 between the firstfluid passages 11. Thediffusion bonding surface 14 extends in the direction X so as to partition the three firstfluid passages 11. An outer peripheral portion of onesurface 10 a of the firstheat transfer plate 10 that surrounds the three firstfluid passages 11 is also a bonding surface. Thediffusion bonding surface 14 extends from the outer peripheral portion on one end side to the outer peripheral portion on the other end side in the direction X. - According to the first embodiment, the second
heat transfer plates 20 each include a plurality of secondfluid passages 21 formed so as to correspond to the firstfluid passages 11 of the firstheat transfer plate 10 and isolated from each other. That is, in each of the secondheat transfer plates 20, the plurality of secondfluid passages 21 through which fluids can flow independently of each other are disposed side by side. The plurality of secondfluid passages 21 are respectively connected to different pairs of second ports 3 (pairs ofsecond ports 3 on the entrance side and the exit side) (seeFIG. 1 ). - According to the first embodiment, the second
fluid passages 21 are equal in number to the firstfluid passages 11. Therefore, in the example shown inFIG. 3 , each of the secondheat transfer plates 20 includes three secondfluid passages fluid passages fluid passages fluid passages fluid passages 21 are respectively disposed at locations that overlap the plurality of firstfluid passages 11 of the firstheat transfer plate 10 in a planar view. That is, each pair of first and secondfluid passages - Fluids are supplied to the second
fluid passages 21 a to 21 c viaheaders FIG. 2 ) that cover both side end faces of thecore 1 in the direction X. Therefore, each of the secondfluid passages FIG. 3 is continuous from one end to another end of the secondheat transfer plate 20. Specifically, the secondfluid passages inlet opening 22 that opens into the interior of theheader 6 a (seeFIG. 2 ) from the side end face of the secondheat transfer plate 20 on the X1 side, and respectively communicate withsecond ports FIG. 1 ). Furthermore, the secondfluid passages outlet opening 23 that opens into the interior of theheader 6 b (seeFIG. 2 ) from the side end face of the secondheat transfer plate 20 on the X2 side, and respectively communicate withsecond ports FIG. 1 ). According to the first embodiment, thesecond ports second ports - As shown in
FIG. 1 , each of theheaders FIG. 2 ) that extends in the direction Y, and both ends thereof in the direction Y are closed. Theheader 6 a covers the side end face of thecore 1 on the X1 side, and is provided to internally store fluids. Theheader 6 b covers the side end face of thecore 1 on the X2 side, and is provided to internally store fluids.Partition plates 6 c are provided inside each of theheaders header 6 a is partitioned by thepartition plates 6 c into a space that connects thesecond fluid passage 21 a and thesecond port 3 a, a space that connects the second fluid passage 21 b and thesecond port 3 c, and a space that connects thesecond fluid passage 21 c and the second port 3 e. Similarly, the interior of theheader 6 b is partitioned by thepartition plates 6 c into a space that connects thesecond fluid passage 21 a and the second port 3 b, a space that connects the second fluid passage 21 b and thesecond port 3 d, and a space that connects thesecond fluid passage 21 c and thesecond port 3 f. Consequently, the secondfluid passages second ports 3 a and 3 b, a pair ofsecond ports second ports 3 e and 3 f). - Different fluids can be supplied to the second
fluid passages second ports fluid passages 21 may be gas or liquid. The same fluid may be supplied to the secondfluid passages first fluid passage 11 side, is supplied to each of the secondfluid passages - The second
fluid passages second ports fluid passages - As shown in
FIG. 3 , according to the first embodiment, each of the plurality of secondfluid passages 21 is formed into an elongated shape that extends in the first direction (direction X) from the inlet opening 22 connected to thesecond port 3 on the entrance side toward the corresponding outlet opening 23 connected to thesecond port 3 on the exit side in the plane of the secondheat transfer plate 20. The plurality of secondfluid passages 21 are disposed side by side along the second direction (direction Y) orthogonal to the first direction. That is, each of the three secondfluid passages 21 extends along the longitudinal direction (the long side of the second heat transfer plate 20) of thecore 1. Furthermore, the three secondfluid passages 21 are disposed side by side along the short-side direction (the short side of the second heat transfer plate 20) of thecore 1. Therefore, the plurality of firstfluid passages 11 and the plurality of secondfluid passages 21 overlap each other in an upward-downward direction (direction Z), and extend substantially in parallel to each other. - According to the first embodiment, the plurality of second
fluid passages 21 are spaced apart from each other in the direction Y on the same surface (onesurface 20 a) of the secondheat transfer plate 20. In the example shown inFIG. 3 , thesecond fluid passage 21 a and the second fluid passage 21 b are disposed at an interval CL3 in the direction Y. The second fluid passage 21 b and thesecond fluid passage 21 c are disposed at an interval CL4 in the direction Y. The intervals CL3 and CL4 may be equal to or different from each other. The secondheat transfer plate 20 includes adiffusion bonding surface 24 with the firstheat transfer plate 10 between the secondfluid passages 21 adjacent to each other in the direction Y. Thediffusion bonding surface 24 is a region of the interval CL3 and a region of the interval CL4. According to the first embodiment, the arrangement and shape of the firstfluid passages 11 of the firstheat transfer plate 10 and the arrangement and shape of the secondfluid passages 21 of the secondheat transfer plate 20 may be substantially common. For example, the intervals CL1, CL2, CL3, and CL4 may be equal to each other. - With the above configuration, the fluids (fluid A, fluid B, and fluid C) respectively flow through the first
fluid passages 11 from the X2 side to the X1 side in the firstheat transfer plate 10, as shown inFIG. 2 . In the secondheat transfer plate 20, the fluid (fluid D) flows through the secondfluid passages 21 from the X1 side to the X2 side. That is, theheat exchanger 100 is a counter-flow heat exchanger in which the fluids that pass through the firstheat transfer plate 10 and the fluid that passes through the secondheat transfer plate 20 flow in opposite directions. - The layer structure of the
core 1 is schematically shown inFIG. 4 . In thecore 1, the firstheat transfer plates 10 through which the fluid A, the fluid B, and the fluid C to be cooled flow are stacked so as to be sandwiched by the secondheat transfer plates 20 through which the fluid D serving as a refrigerant flows. - As an example, the first
fluid passages 11 each have a flow passage shape, as shown inFIG. 5 . In the first embodiment, an example in which the three first fluid passages (11 a, 11 b, and 11 c) have a common configuration is shown. That is, in the example shown inFIG. 5 , the three first fluid passages 11 (11 a to 11 c) are formed into substantially the same shape. The three first fluid passages 11 (11 a to 11 c) each have an outer shape having a length L1 in the direction X (longitudinal direction) and a width W1 in the direction Y (short-side direction). - Each of the plurality of first
fluid passages 11 includes aflow passage 15 that connects theinlet port 12 connected to thefirst port 2 on the entrance side to theoutlet port 13 connected to the correspondingfirst port 2 on the exit side. In the configuration example ofFIG. 5 , the firstfluid passages 11 each include theinlet port 12, theoutlet port 13, a plurality ofheat exchange passages 16, and connection passages 17. Theflow passage 15 includes theheat exchange passages 16 and the connection passages 17. - The
heat exchange passages 16 are linear flow passages provided to perform heat exchange between the fluids, extend in the direction X, and are aligned in parallel to each other in the direction Y. In the configuration example ofFIG. 5 , the firstfluid passages 11 each include eightheat exchange passages 16. The number ofheat exchange passages 16 may be other than eight. - The connection passages 17 are provided between the
inlet port 12 and the plurality ofheat exchange passages 16 and between theoutlet port 13 and the plurality ofheat exchange passages 16, respectively. The structures of the connection passages 17 are common on theinlet port 12 side and theoutlet port 13 side, and thus only the connection passage 17 of theinlet port 12 is described. - One end side of the connection passage 17 is connected to the
inlet port 12, and another end side of the connection passage 17 is connected to each of the plurality of (eight)heat exchange passages 16. Accordingly, the connection passage 17 has a function of distributing the fluid from theinlet port 12 to each of theheat exchange passages 16. The connection passage 17 is divided from oneinlet port 12 into eight branches, and is connected to each of the eightheat exchange passages 16. - As shown in
FIG. 7 , the flow passage 15 (theheat exchange passages 16 and the connection passages 17) is formed as a concave groove on onesurface 10 a of the firstheat transfer plate 10. In an example ofFIG. 7 , the cross-sectional shape orthogonal to a direction in which theflow passage 15 extends is substantially semicircularly recessed. Theflow passage 15 is formed by etching or machining, for example. Theflow passage 15 has a flow passage width W11 and a flow passage depth H11. The flow passage width and the flow passage depth are common in theheat exchange passages 16 and the connection passages 17. Theheat exchange passages 16 each have a flow passage length L11 (seeFIG. 5 ), and apartition wall 18 between theheat exchange passages 16 has a width W12. The flow passage width W11 of theflow passage 15 is larger than the width W12 of thepartition wall 18. The width (interval CL1 or CL2) of thediffusion bonding surface 14 is larger than the width W12 of thepartition wall 18 between theheat exchange passages 16. - As an example, the second
fluid passages 21 each have a flow passage shape, as shown inFIG. 6 . In the first embodiment, an example in which the three second fluid passages 21 (21 a, 21 b, and 21 c) have a common configuration is shown. - In the example of
FIG. 6 , the three second fluid passages (21 a to 21 c) are formed into substantially the same shape. The three second fluid passages 21 (21 a to 21 c) each have an outer shape having a length L2 in the direction X (longitudinal direction) and a width W2 in the direction Y (short-side direction). The width W2 is substantially equal to the width W1 of each of the firstfluid passages 11. The secondfluid passages 21 open to the end face of the second heat transfer plate 20 (core 1) in the X direction, and thus the length L2 is larger than the length L1 of each of the firstfluid passages 11. - Each of the plurality of second
fluid passages 21 includes aflow passage 25 that connects the inlet opening 22 connected to thesecond port 3 on the entrance side to the outlet opening 23 connected to the correspondingsecond port 3 on the exit side. In the configuration example ofFIG. 6 , the secondfluid passages 21 each include theinlet opening 22, theoutlet opening 23, a plurality ofheat exchange passages 26, andconnection passages 27. Theflow passage 25 includes theheat exchange passages 26 and theconnection passages 27. - The configurations of the
heat exchange passages 26 are the same as those of theheat exchange passages 16 of the firstfluid passages 11 inFIG. 5 , and the same number of (eight)heat exchange passages 26 with the same shape are provided. Theconnection passage 27 on the inlet opening 22 side includes aflow passage portion 27 a connected to the inlet opening 22 formed in the end face of the secondheat transfer plate 20. Theflow passage portion 27 a is linearly formed, and a pair offlow passage portions 27 a are provided on both outer sides of the through-hole 5 c in the direction Y. Theconnection passage 27 is divided from each of the pair offlow passage portions 27 a into four branches so as to be divided into eight flow passages in total. Ends (other ends) of the eight branches of the dividedconnection passage 27 are connected to the corresponding eightheat exchange passages 26, respectively. In this manner, theconnection passage 27 of each of the secondfluid passages 21 is divided into one side and the other side in the direction Y across the through-hole 5 c, and is divided into four branch passages on each side. Similarly, aflow passage portion 27 a is also provided in theconnection passage 27 on the outlet opening 23 side, and has the same configuration. - As shown in
FIG. 7 , the flow passage 25 (theheat exchange passages 26 and the connection passages 27) is formed as a concave groove on onesurface 20 a of the secondheat transfer plate 20. In the example ofFIG. 7 , the cross-sectional shape orthogonal to a direction in which theflow passage 25 extends is a substantially semicircularly recessed. Theflow passage 25 has a flow passage width W21 and a flow passage depth H21. The flow passage width W21 and the flow passage depth H21 are substantially equal to the flow passage width W11 and the flow passage depth H11 of theflow passage 15. The flow passage width W21 of theflow passage 25 and the flow passage width W11 of theflow passage 15 may be different from each other. Similarly, the flow passage depth H21 of theflow passage 25 and the flow passage depth H11 of theflow passage 15 may be different from each other. Theheat exchange passages 26 each have a flow passage length L21 (seeFIG. 6 ). The flow passage length L21 is substantially equal to the flow passage length L11 of each of theheat exchange passages 16. The width (interval CL3 or CL4) of thediffusion bonding surface 24 between the adjacent secondfluid passages 21 is larger than the width W22 of apartition wall 28 between theheat exchange passages 26.FIG. 7 shows an example in which the position of theflow passage 15 and the position of theflow passage 25 in the direction Y (the center positions of the flow passages) coincide with each other, but the position of theflow passage 15 in the direction Y and the position of theflow passage 25 in the direction Y may be shifted from each other. - With the above configuration, according to the first embodiment, the high-temperature and high-pressure fluid A, fluid B, and fluid C that have passed through different compressors are supplied to the first
fluid passages heat transfer plate 10, respectively. The fluid A, the fluid B, and the fluid C flow in through thefirst ports FIG. 1 ) on the entrance side connected to the respective exit sides of the compressors, and are distributed to therespective inlet ports 12 of the firstfluid passages heat exchange passages 16 and the connection passages 17) of the firstfluid passages FIG. 1 ) on the exit side, respectively. - The fluid (fluid D) serving as a refrigerant is supplied to each of the second
fluid passages heat transfer plate 20. The fluid D flows in through each of thesecond ports FIG. 1 ) on the entrance side, passes through an internal space of theheader 6 a partitioned by thepartition plates 6 c, and flows into each of the secondfluid passages second ports fluid passages heat exchange passages 26 and the connection passages 27) of the secondfluid passages second ports FIG. 1 ) on the exit side. - According to the first embodiment, the following effects can be obtained.
- According to the first embodiment, as described above, the first
heat transfer plate 10 including the plurality of firstfluid passages 11 connected to the different pairs of first ports 2 (the pair of 2 a and 2 b, the pair of 2 c and 2 d, and the pair of 2 e and 2 f) and isolated from each other is provided. Thus, instead of providing a plurality of types of firstheat transfer plates 10, the firstheat transfer plate 10 including a plurality of types of firstfluid passages 11 can be provided. That is, instead of providing a heat transfer plate for each type of fluid, the firstheat transfer plate 10 common to a plurality of types of fluids can be provided. Consequently, even when the plurality of types of fluids are handled by the common diffusion-bondedheat exchanger 100, the number of types of components (the number of types of first heat transfer plates 10) and the number of components (the total number of first and secondheat transfer plates 10 and 20) can be reduced. When the same configuration as in the first embodiment is realized by individual heat transfer plates, for example, three types of three heat transfer plates corresponding to the firstfluid passages heat transfer plates - With the above configuration, the plurality of types of first
fluid passages 11 can be formed in the same firstheat transfer plate 10, and thus for example, onefirst fluid passage 11 is reduced in size according to a load (the amount of heat exchange) on each fluid etc. such that anotherfirst fluid passage 11 can be formed in an empty space, or the planar size of a product can be reduced. That is, the degree of freedom in the configuration of the fluid passages can be sufficiently ensured. A specific example in which the configuration of the fluid passages is changed is described later. - According to the first embodiment, as described above, the second
heat transfer plate 20 including the plurality of secondfluid passages 21 formed so as to correspond to the firstfluid passages 11 of the firstheat transfer plate 10 and isolated from each other is provided. Thus, the plurality of secondfluid passages 21 are formed so as to correspond to the plurality of firstfluid passages 11 such that heat exchange between the fluids can be efficiently performed. Furthermore, the plurality of secondfluid passages 21 are respectively connected to the different pairs of second ports 3 (the pair of 3 a and 3 b, the pair of 3 c and 3 d, and the pair of 3 e and 3 f). Thus, the type, the flow rate, etc. of the fluid that flows through each of the secondfluid passages 21 can be individually set for each of the secondfluid passages 21 according to the amount of heat exchange between the fluids that flow through the firstfluid passages 11 and the secondfluid passages 21 corresponding to each other. - According to the first embodiment, as described above, the second
fluid passages 21 are equal in number to the firstfluid passages 11. Furthermore, the secondfluid passages 21 are respectively disposed at the locations that overlap the plurality of firstfluid passages 11 of the firstheat transfer plate 10 in the planar view. Thus, the plurality of secondfluid passages 21 can be provided in a one-to-one correspondence with the plurality of firstfluid passages 11. Here, when one wide second fluid passage (one second fluid passage corresponding to the three first fluid passages 11) is provided at a location that overlaps the firstfluid passages 11 a to 11 c, for example, it becomes difficult to independently adjust the amount of heat exchange between onefirst fluid passage 11 a and the second fluid passage and the amount of heat exchange between another first fluid passage 11 b and the second fluid passage. On the other hand, the firstfluid passages fluid passages fluid passages fluid passages fluid passages 21, for example, can be easily optimized. - According to the first embodiment, as described above, the plurality of first
fluid passages 11 are each formed into an elongated shape that extends in the direction X from theinlet port 12 toward thecorresponding outlet port 13 in onesurface 10 a of the firstheat transfer plate 10, and are disposed side by side along the direction Y orthogonal to the direction X. Thus, as compared with the case where the plurality of firstfluid passages 11 are each formed into a wide shape, the flow rate can be easily increased to improve the heat transfer coefficient even with a simple flow passage shape. Furthermore, the firstfluid passages 11 each having an elongated shape that extends in the direction X are disposed side by side along the direction Y such that the vertical and horizontal dimensions of the outer shape of the entire firstheat transfer plate 10 can be brought closer to each other (the aspect ratio can be brought closer to 1). Consequently, variations in the load at the time of performing diffusion bonding can be suppressed, and the ease of manufacturing thecore 1 can be improved. - According to the first embodiment, as described above, the plurality of first
fluid passages 11 are spaced apart from each other in the direction Y on onesurface 10 a of the firstheat transfer plate 10. Furthermore, thediffusion bonding surface 14 with the secondheat transfer plate 20 is provided in the firstheat transfer plate 10 between the firstfluid passages 11 adjacent to each other in the direction Y. Thus, each of the plurality of firstfluid passages 11 disposed on onesurface 10 a of the firstheat transfer plate 10 can be easily isolated as an independent fluid passage. Furthermore, thediffusion bonding surface 14 that extends in the direction X can be formed between the plurality of firstfluid passages 11 aligned in the direction Y. The width (CL1 or CL2) of thediffusion bonding surface 14 is larger than the width W12 of thepartition wall 18 such that the diffusion bonding strength between the firstheat transfer plate 10 and the secondheat transfer plate 20 can be easily ensured as compared with the case where the firstheat transfer plate 10 and the secondheat transfer plate 20 are bonded to each other only with the outer peripheral portion of the heat transfer plate surface or a gap (partition wall 18) between the flow passages constituting the firstfluid passages 11, for example. Similarly, the plurality of secondfluid passages 21 of the secondheat transfer plate 20 are spaced apart from each other in the direction Y, and thediffusion bonding surface 24 with the firstheat transfer plate 10 is provided between the secondfluid passages 21 adjacent to each other in the direction Y such that each of the plurality of secondfluid passages 21 can be easily isolated as an independent fluid passage. Furthermore, the width (CL3 or CL4) of thediffusion bonding surface 24 is larger than the width W22 of thepartition wall 28 such that the diffusion bonding strength between the firstheat transfer plate 10 and the secondheat transfer plate 20 can be easily ensured. - A second embodiment is now described with reference to
FIGS. 8 and 9 . In this second embodiment, an example in which the shapes of three first fluid passages 111 a to 111 c are different is described unlike the aforementioned first embodiment in which the three firstfluid passages 11 a to 11 c are formed into a common shape. - As shown in
FIG. 8 , in aheat exchanger 200 according to the second embodiment, a firstheat transfer plate 110 includes three first fluid passages 111 (111 a, 111 b, and 111 c) connected to different pairs of first ports 2 (a pair offirst ports 2 a and 2 b, a pair offirst ports 2 c and 2 d, and a pair of first ports 2 e and 2 f) (seeFIG. 1 ) and isolated from each other. Theheat exchanger 200 is an example of a “diffusion-bonded heat exchanger” in the claims. - According to the second embodiment, at least one of a plurality of (three) first
fluid passages 111 is different from another one of the plurality of firstfluid passages 111 in at least one of the flow passage width of aflow passage 15, the flow passage length of theflow passage 15, the flow passage depth of theflow passage 15, and the number offlow passages 15. - In
FIG. 8 , thefirst fluid passage 111 b at the center in a direction Y of the three firstfluid passages 111 a, 111 b, and 111 c is larger in size than the first fluid passages 111 a and 111 c on both sides in the direction Y. In an example ofFIG. 8 , the first fluid passages 111 a and 111 c have a common configuration. Thefirst fluid passage 111 b as a whole has a length L3 b in a direction X and a width W3 b in the direction Y. The first fluid passages 111 a and 111 c as a whole each have a length L3 a in the direction X and a width W3 a in the direction Y. In the example ofFIG. 8 , the length L3 a of each of the first fluid passages 111 a and 111 c and the length L3 b of thefirst fluid passage 111 b are equal to each other. The length L3 a and the length L3 b may be different from each other. The width W3 a of each of the first fluid passages 111 a and 111 c is smaller than the width W3 b of thefirst fluid passage 111 b. The width W3 a may be larger than the width W3 b. As compared with the configuration according to the first embodiment shown inFIG. 5 , the length L3 a is equal to the length L1 of thefirst fluid passage 11 inFIG. 5 , but the width W3 a is smaller than the width W1 of thefirst fluid passage 11 inFIG. 5 . The length L3 b is equal to the length L1 of thefirst fluid passage 11 inFIG. 5 . The width W3 b is larger than the width W1 of thefirst fluid passage 11 inFIG. 5 . Therefore, according to the second embodiment, in the firstheat transfer plate 110, the first fluid passages 111 a and 111 c are reduced in size, and thus a larger space is allocated to thefirst fluid passage 111 b. - A
flow passage 115 a (115 c) of the first fluid passage 111 a (111 c) includes fourheat exchange passages 116 a (116 c). Unlike the aforementioned first embodiment,connection passages 117 a (117 c) are divided into four branches and are connected in parallel to each of theheat exchange passages 116 a (116 c). Theheat exchange passages 116 a (116 c) each have a flow passage length L31. As shown inFIG. 9 , theflow passage 115 a (115 c) of the first fluid passage 111 a (111 c) has a flow passage width W31 and a flow passage depth H31. - A
flow passage 115 b of thefirst fluid passage 111 b includes nineheat exchange passages 116 b, which are more than the four first fluid passages 111 a (111 c). Connection passages 117 b are divided into nine branches and are connected in parallel to each of theheat exchange passages 116 b. Theheat exchange passages 116 b each have a flow passage length L32. As shown inFIG. 9 , theflow passage 115 b of thefirst fluid passage 111 b has a flow passage width W32 and a flow passage depth H32. - The flow passage width W32 of the
flow passage 115 b of thefirst fluid passage 111 b is larger than the flow passage width W31 of theflow passage 115 a (115 c) of the first fluid passage 111 a (111 c). The flow passage depth H32 of theflow passage 115 b of thefirst fluid passage 111 b is equal to the flow passage depth H31 of theflow passage 115 a (115 c) of the first fluid passage 111 a (111 c). The flow passage length L32 of each of theheat exchange passages 116 b of thefirst fluid passage 111 b is equal to the flow passage length L31 of theflow passage 115 a (115 c) of the first fluid passage 111 a (111 c). - As described above, in
FIGS. 8 and 9 , the flow passage width W32 of thefirst fluid passage 111 b is larger than the flow passage width W31 of each of the first fluid passages 111 a and 111 c, and the number of (nine)flow passages 115 b of thefirst fluid passage 111 b is larger than the number of (four)flow passages 115 a (115 c) of the first fluid passage 111 a (111 c). These flow passage widths and the number of flow passages 115 are set according to the types of fluids that respectively flow through the first fluid passages 111 a to 111 c or the magnitudes of the loads (amount of heat exchange) on the fluids. Therefore, in thefirst fluid passage 111 b, the amount of heat exchange is larger than in the first fluid passages 111 a and 111 c. - As described above, according to the second embodiment, the
first fluid passage 111 b is different from the remaining first fluid passages 111 a and 111 c in the flow passage width and the number of flow passages. In the second embodiment, the example in which the flow passage width and the number of flow passages are different is shown, but only one of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages may alternatively be different. All of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages may alternatively be different. In addition, the firstfluid passages 111 a, 111 b, and 111 c may have configurations different from each other (configurations in which any of the flow passage width, the flow passage length, the flow passage depth, and the number of flow passages is different). - Although the description of a second
heat transfer plate 20 is omitted, secondfluid passages 21 of the secondheat transfer plate 20 also have the same shapes corresponding to the aforementioned first fluid passages 111 a to 111 c, respectively. - The remaining configurations of the second embodiment are similar to those of the aforementioned first embodiment.
- According to the second embodiment, similarly to the aforementioned first embodiment, the first
heat transfer plate 110 including the plurality of firstfluid passages 111 connected to the different pairs of first ports 2 (the pair of 2 a and 2 b, the pair of 2 c and 2 d, and the pair of 2 e and 2 f) and isolated from each other is provided such that even when a plurality of types of fluids are handled by the common diffusion-bondedheat exchanger 200, the number of types of components and the number of components can be reduced. - With the above configuration, a plurality of types of first fluid passages 111 a to 111 c can be formed in the same first
heat transfer plate 110, and thus the degree of freedom of the configuration of the fluid passage for each type according to the load (amount of heat exchange) on each fluid can be sufficiently ensured. That is, the shapes and layouts of the firstfluid passages 111 a, 111 b, and 111 c can be freely set in the firstheat transfer plate 110. - According to the second embodiment, as described above, the
first fluid passage 111 b of the plurality of first fluid passages 111 a to 111 c is different from another first fluid passages 111 a (111 c) in at least one of the flow passage width W32 of theflow passage 115 b, the flow passage length L32 of theflow passage 115 b, the flow passage depth H32 of theflow passage 115 b, and the number offlow passages 115 b. The configurations (the flow passage width of the flow passage, the flow passage length of the flow passage, the flow passage depth of the flow passage, and the number of flow passages) of the plurality of types of first fluid passages 111 a to 111 c are different in this manner such that a surplus amount of heat exchange that cannot be adjusted with a change in the number of stacked heat transfer plates can be easily and finely adjusted for each of the first fluid passages 111 a to 111 c. Consequently, the amount of heat exchange can be easily and accurately optimized according to the load (amount of heat exchange) on each type offirst fluid passage 111. - The remaining effects of the second embodiment are similar to those of the aforementioned first embodiment.
- The embodiments disclosed this time must be considered as illustrative in all points and not restrictive. The range of the present invention is not shown by the above description of the embodiments but by the scope of claims for patent, and all modifications (modified examples) within the meaning and range equivalent to the scope of claims for patent are further included.
- For example, while the
counter-flow heat exchanger 100 in which the fluids that pass through the firstheat transfer plate 10 and the fluid that passes through the secondheat transfer plate 20 flow in opposite directions has been shown as an example in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, the heat exchanger may be a parallel-flow heat exchanger in which the fluids that pass through the firstheat transfer plate 10 and the fluid that passes through the secondheat transfer plate 20 flow in the same direction, or a cross-flow heat exchanger in which the flows of the fluids cross (seeFIG. 10 ), for example. - While the example in which the
core 1 is formed by alternately stacking the plurality of firstheat transfer plates 10 and the plurality of secondheat transfer plates 20 has been shown in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, the first heat transfer plates and the second heat transfer plates may not necessarily be alternately stacked. For example, two (a plurality of) second heat transfer plates may be stacked on one first heat transfer plate such that a second heat transfer plate, a first heat transfer plate, a second heat transfer plate, a second heat transfer plate, a first heat transfer plate, . . . are stacked along a direction Z. Conversely, one second heat transfer plate may be stacked on two (a plurality of) first heat transfer plates. - While the example in which the three first
fluid passages 11 are provided in the first heat transfer plate 10 (110) has been shown in each of the aforementioned first and second embodiments, the present invention is not restricted to this. According to the present invention, two or four or more firstfluid passages 11 may be provided in the firstheat transfer plate 10. - While the example in which the plurality of second
fluid passages 21 are provided in the secondheat transfer plate 20 so as to correspond to the firstfluid passages 11 of the firstheat transfer plate 10 has been shown in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, only one second fluid passage may be provided, for example. Specifically, as in a first modified example shown inFIG. 10 , one common secondfluid passage 221 may be provided in a secondheat transfer plate 220 for three firstfluid passages 11 of a firstheat transfer plate 10. In this first modified example, thesecond fluid passage 221 extends in a direction Y orthogonal to the firstfluid passages 11, and a cross-flow heat exchanger is formed. The width W5 of thesecond fluid passage 221 in a direction X is substantially equal to the length L1 of each of the firstfluid passages 11, and thesecond fluid passage 221 extends from one end to the other end of the secondheat transfer plate 220 in the direction Y. Thus, heat exchange is performed between a fluid D that flows through one (common)second fluid passage 221 and fluids, A, B, and C that respectively flow through the three firstfluid passages 11. - The number of second fluid passages may be any number. In other words, the second fluid passages may be equal in number to the first fluid passages, or a plurality of second fluid passages other than one may be provided. For example, a plurality of (two, for example) second fluid passages may be provided so as to correspond to one first fluid passage.
- While the example in which the three second
fluid passages 21 a to 21 c are respectively connected to the different pairs of second ports 3 (the pair of 3 a and 3 b, the pair of 3 c and 3 d, and the pair of 3 e and 3 f) has been shown in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, the three secondfluid passages 21 a to 21 c may be connected to common second ports. In this case, inFIG. 6 , for example, thepartition plates 6 c provided in each of theheaders headers fluid passages 21 a to 21 c are connected to the commonsecond ports 3. In this case, three pairs ofsecond ports 3 may be provided, but it is only required to provide at least a pair ofsecond ports 3 on the entrance side (3 c, for example) and on the exit side (3 d, for example). - While the example in which the same type of fluid (fluid D) is supplied to the three second
fluid passages 21 of the secondheat transfer plate 20 has been shown in the aforementioned first embodiment, the present invention is not restricted to this. According to the present invention, as in a second modified example shown inFIG. 11 , different types of fluids may be supplied to the three secondfluid passages 21. InFIG. 11 , a fluid A, a fluid B, and a fluid C are respectively supplied to three firstfluid passages 11 of a first heat transfer plate 10 (FIG. 11(A) ), and a fluid D, a fluid E, and a fluid F are respectively supplied to three secondfluid passages 21 of a second heat transfer plate (FIG. 11(B) ). In the second modified example, heat exchange is performed between the fluid A in afirst fluid passage 11 a and the fluid D in asecond fluid passage 21 a, between the fluid B in a first fluid passage 11 b and the fluid E in a second fluid passage 21 b, and between the fluid C in afirst fluid passage 11 c and the fluid F in asecond fluid passage 21 c. The fluids A to F may be different types of fluids, or some of the fluids A to F may be the same type of fluids. - While the example in which two types of first and second
heat transfer plates heat transfer plate 10 and the secondheat transfer plate 20 since the number of types of components (the number of types of heat transfer plates) and the number of components can be reduced. - While the example in which the plurality of first
fluid passages 11 are each formed into an elongated shape that extends in the direction X from theinlet port 12 on the entrance side toward thecorresponding outlet port 13 on the exit side, and are disposed side by side along the direction Y orthogonal to the direction X has been shown in each of the aforementioned first and second embodiments, the present invention is not restricted to this. According to the present invention, each of the first fluid passages may not be formed into an elongated shape. For example, in the first heat transfer plate, each of the first fluid passages may be formed into a square shape or a shape other than a rectangular shape. Furthermore, the first fluid passages may not be disposed side by side in the short-side direction (direction Y) orthogonal to the longitudinal direction (direction X). For example, the first fluid passages may be respectively disposed in regions obtained by dividing the first heat transfer plate into four vertically and horizontally (in a matrix). - While the example in which the flow passage 15 (25) including the heat exchange passages 16 (26) and the connection passages 17 (27) is provided in each of the first
fluid passages 11 and the secondfluid passages 21 has been shown in the aforementioned first embodiment, the present invention is not restricted to this. The configuration of the flow passage constituting each of the first fluid passages and the second fluid passages is not particularly limited. The shape of the flow passage and the number of flow passages may be arbitrarily set. For example, instead of the linear heat exchange passages, bent or curved heat exchange passages may be provided. The number of branches of the connection passages may be other than the aforementioned four branches, eight branches, and nine branches, and may be the number of branches corresponding to the number of heat exchange passages to be connected. Theflow passage 15 constituting each of the firstfluid passages 11 a to 11 c may have shapes different from each other. -
- 1: core
- 2 (2 a to 2 f): first port
- 3 (3 a to 3 f): second port
- 10, 110: first heat transfer plate
- 11 (11 a to 11 c), 111 (111 a to 111 c): first fluid passage
- 12: inlet port (one end)
- 13: outlet port (another end)
- 14: diffusion bonding surface
- 15: flow passage
- 20, 220: second heat transfer plate
- 21 (21 a to 21 c), 221: second fluid passage
- 100, 200: heat exchanger (diffusion-bonded heat exchanger)
- X: direction (first direction)
- Y: direction (second direction)
Claims (6)
Applications Claiming Priority (3)
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JP2016-070834 | 2016-03-31 | ||
JP2016070834A JP6321067B2 (en) | 2016-03-31 | 2016-03-31 | Diffusion bonding type heat exchanger |
PCT/JP2017/011612 WO2017170091A1 (en) | 2016-03-31 | 2017-03-23 | Diffusion bonding-type heat exchanger |
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US20190086155A1 true US20190086155A1 (en) | 2019-03-21 |
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US16/081,312 Abandoned US20190086155A1 (en) | 2016-03-31 | 2017-03-23 | Diffusion-Bonded Heat Exchanger |
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US (1) | US20190086155A1 (en) |
EP (1) | EP3438591A4 (en) |
JP (1) | JP6321067B2 (en) |
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US20160375740A1 (en) * | 2014-03-17 | 2016-12-29 | Mahle International Gmbh | Heating and cooling module |
IT201900020376A1 (en) * | 2019-11-05 | 2021-05-05 | Microchannel Devices S R L | METHOD FOR MANUFACTURING MONOLITHIC MULTI-PIPE HYDRAULIC DEVICES, IN PARTICULAR HEAT EXCHANGERS |
US20220009022A1 (en) * | 2018-12-21 | 2022-01-13 | Nhk Spring Co., Ltd. | Joining method and joined body |
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EP4400796A1 (en) * | 2023-01-12 | 2024-07-17 | Kabushiki Kaisha Kobe Seiko Sho (Kobe Steel, Ltd.) | Microchannel heat exchanger |
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JP7206609B2 (en) * | 2018-03-26 | 2023-01-18 | 株式会社富士通ゼネラル | Metal laminate and method for manufacturing metal laminate |
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Also Published As
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JP2017180984A (en) | 2017-10-05 |
WO2017170091A1 (en) | 2017-10-05 |
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