EP2980521A1 - Plate-type heat exchanger - Google Patents
Plate-type heat exchanger Download PDFInfo
- Publication number
- EP2980521A1 EP2980521A1 EP13880645.0A EP13880645A EP2980521A1 EP 2980521 A1 EP2980521 A1 EP 2980521A1 EP 13880645 A EP13880645 A EP 13880645A EP 2980521 A1 EP2980521 A1 EP 2980521A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- flow channel
- flow channels
- heat transfer
- transfer plates
- fluid medium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000012530 fluid Substances 0.000 claims abstract description 133
- 238000007789 sealing Methods 0.000 description 9
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000005219 brazing Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 101100134058 Caenorhabditis elegans nth-1 gene Proteins 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- 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
-
- 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
- F28F2275/04—Fastening; Joining by brazing
Definitions
- the present invention relates to a plate heat exchanger that is used as an evaporator and a condenser.
- a plate heat exchanger is used as an evaporator that evaporates a first fluid medium along with heat exchange between the first fluid medium and a second fluid medium, and as a condenser that condenses a first fluid medium along with heat exchange between the first fluid medium and a second fluid medium (see Patent Literature 1, for example).
- a plate heat exchanger generally includes a body portion 3 that includes a plurality of heat transfer plates 2.
- the body portion 3 includes first flow channels 30, second flow channels 31, a pair of first communication flow channels 32 and 33, and a pair of second communication flow channels 34 and 35.
- the first flow channel 30 circulates a first fluid medium A.
- the second flow channel 31 circulates a second fluid medium B.
- the pair of first communication flow channels 32 and 33 communicate with the first flow channels 30 to allow the first fluid medium A to flow into and out of the first flow channels 30.
- a pair of second communication flow channels 34 and 35 communicate with the second flow channels 31 to allow the second fluid medium B to flow into and out of the second flow channels 31.
- the plurality of the heat transfer plates 2 each include at least four openings (no reference numeral is allocated).
- the plurality of the heat transfer plates 2 are stacked on each other in the body portion 3. With this configuration, the first flow channels 30 for circulation of the first fluid medium A and the second flow channels 31 for circulation of the second fluid medium B are alternately formed with the plurality of the heat transfer plates 2 respectively interposed therebetween. With the plurality of the heat transfer plates stacked on each other, each opening of each of the plurality of the heat transfer plates 2 forms a continuous opening extending in the stacked direction of the plurality of the heat transfer plates 2.
- the one first communication flow channel 32 for flowing the first fluid medium A into the first flow channels 30, the other first communication flow channel 33 for flowing the first fluid medium A out of the first flow channels 30, the one second communication flow channel 34 for flowing the second fluid medium B into the second flow channels 31, and the other second communication flow channel 35 for flowing the second fluid medium B out of the second flow channels 31 extend through the plurality of the heat transfer plates 2 in the stacked direction of the plurality of the heat transfer plates 2 (see Patent Literature 1, for example).
- a plate heat exchanger 1 of this type the first fluid medium A supplied into the one first communication flow channel 32 flows out to the other first communication flow channel 33 through the first flow channels 30.
- the second fluid medium B supplied into the one second communication flow channel 34 flows out to the other second communication flow channel 35 through the second flow channels 31.
- the plate heat exchanger 1 enables the heat exchange between the first fluid medium A and the second fluid medium B through a large heat transfer surface of each heat transfer plate 2 separating the first flow channel 30 and the second flow channel 31.
- the heat transfer surface area contributing to the heat exchange increases and thereby it is assumed that the heat exchange performance becomes high.
- the first communication flow channels 32 and 33 and the second communication flow channels 34 and 35 which extend in the stacked direction of the plurality of the heat transfer plates 2 increase in length according to the number of the stacked heat transfer plates 2.
- the pair of first communication flow channels 32 and 33 and the pair of second communication flow channels 34 and 35 each are formed by the alignment of the corresponding openings of the heat transfer plates 2, so that the flow channel length of each of the pair of first communication flow channels 32 and 33 and the pair of second communication flow channels 34 and 35 increases according to the number of the stacked heat transfer plates 2 when the number thereof increases.
- the resistance of the first fluid medium A in the first communication flow channel (the one first communication flow channel) 32 for flowing the first fluid medium A into the first flow channels 30 increases and thus the first fluid medium A is not easy to circulate. Therefore, in the plate heat exchanger 1 of this type, the inflow of the first fluid medium A into the first flow channels 30 at the inlet side of the one first communication flow channel 32 and the inflow of the first fluid medium A into the first flow channels 30 at the far side of the one first communication flow channel 32 become uneven. That is, in the plate heat exchanger 1 of this type, distribution unevenness of the first fluid medium A is caused in the plurality of the first flow channels 30 aligning in the stacked direction of the heat transfer plates 2. As a result, in the plate heat exchanger 1 of this type, even if the number of the heat transfer plates 2 is increased or the number of the first flow channels 30 is increased, there is a limit in improving the heat exchange performance (evaporation performance).
- an object of the present invention is to provide a plate heat exchanger that is capable of evenly supplying a first fluid medium into a plurality of first flow channels for circulation of the first fluid medium, while suppressing increase in pressure loss in the plurality of the first flow channels.
- a plate heat exchanger including a body portion that includes a plurality of heat transfer plates stacked on each other, the body portion further including a plurality of first flow channels that circulate a first fluid medium, a plurality of second flow channels that circulate a second fluid medium, a pair of first communication flow channels that communicate with the plurality of the first flow channels and allow the first fluid medium to flow into and out of the plurality of the first flow channels, a pair of second communication flow channels that communicate with the plurality of the second flow channels and allow the second fluid medium to flow into and out of the plurality of the second flow channels, the plurality of the first flow channels and the plurality of the second flow channels being alternately formed with the plurality of the heat transfer plates being respectively interposed therebetween, and the pair of first communication flow channels and the pair of second communication flow channels extending in the stacked direction of the plurality of the heat transfer plates through the plurality of the heat transfer plates.
- the plurality of the first flow channels communicate with each other to form a flow channel of the first fluid medium from one of the pair of first communication flow channels to the other of the pair of first communication flow channels.
- At least one of the plurality of the first flow channels located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a reference flow channel that serves as a branching position of the flow channel of the first fluid medium.
- the body portion includes at least one pair of primary branch flow channels that provide communication between the reference flow channel and at least one first flow channel located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the one of the pair of first communication flow channels communicates only with the reference flow channel.
- the other of the pair of first communication flow channels communicates only with the first flow channel that is located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium.
- the present invention may be configured such that three or more fist flow channels are provided on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is an intermediate reference flow channel that serves as a branching position of the flow channel of the first fluid medium.
- the body portion includes a pair of secondary branch flow channels that each provide communication between the corresponding intermediate reference flow channel and at least one first flow channel located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the pair of primary branch flow channels respectively communicate with the corresponding intermediate reference flow channels located respectively on the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the plate heat exchanger may be configured such that: two or more first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the body portion includes a connection flow channel that connects the two or more first flow channels with each other on the one side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, and a connection flow channel that connects the two or more first flow channels with each other on the other side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- At least one first flow channel that is located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates the other of the pair of first communication flow channels.
- a plurality of the first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of heat transfer plates.
- the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a branch reference flow channel that serves as a branching position of the flow channel of the first fluid medium.
- the body portion includes a pair of tertiary branch flow channels that provide communication between the branch reference flow channel and the first flow channel located on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the pair of secondary branch flow channels respectively communicate with the branch reference flow channels located respectively on the one side and the other side of the intermediate reference flow channel in the stacked direction of the heat transfer plates.
- the plate heat exchanger may be configured such that: one first flow channel is provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and communicates with the other of the pair of first communication flow channels.
- the plate heat exchanger may be configured such that: two or more first flow channels are provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- the body portion includes a connection flow channel that connects the two or more first flow channels located on the one side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and a connection flow channel that connects the two or more first flow channels located on the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- At least one first flow channel that is located on the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates with the other of the pair of first communication flow channels.
- the plate heat exchanger includes a body portion 3 that includes a plurality of heat transfer plates 2 stacked on each other.
- the body portion 3 includes first flow channels 30, second flow channels 31, a pair of first communication flow channels 32 and 33, and a pair of second communication flow channels 34 and 35.
- the first flow channels 30 circulate a first fluid medium A.
- the second flow channels 31 circulate a second fluid medium B.
- the pair of first communication flow channels 32 and 33 communicate with the first flow channels 30 to allow the first fluid medium A to flow into and out of the first flow channels 30.
- the pair of second communication flow channels 34 and 35 communicate with the second flow channels 31 to allow the second fluid medium B to flow into and out of the second flow channels 31.
- one passage 32 of the pair of first communication flow channels 32 and 33 is referred to as the "first inflow communication flow channel,” and the other passage 33 of the pair of first communication flow channels 32 and 33 is referred to as the “first outflow communication flow channel.”
- one passage 34 of the pair of second communication flow channels 34 and 35 is referred to as the “second inflow communication flow channel,” and the other passage 35 of the pair of second communication flow channels 34 and 35 is referred to as the "second outflow communication flow channel.”
- the first flow channels 30 and the second flow channels 31 are alternately formed with the heat transfer plates 2 respectively interposed therebetween.
- the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35 each extend through the heat transfer plates 2 in the stacked direction of the plurality of the heat transfer plates 2 (hereinafter referred to as the "first direction").
- a plate heat exchanger 1 includes the body portion 3 that includes the plurality of the heat transfer plates 2 stacked on each other, and a pair of end plates 4 and 5 that sandwich the body portion 3.
- the plurality of the heat transfer plates 2 each are provided by press forming a metal plate, as shown in Fig. 2 .
- the plurality of the heat transfer plates 2 each include a heat transfer portion 20 that defines the first flow channel 30 and the second flow channel 31, and an annular fitting portion 21 that extends from the outer circumference of the heat transfer portion 20 in a direction orthogonal to the plane of the heat transfer portion 20.
- Each of the heat transfer plates 2 includes a front side and a back side on which a plurality of ridges and valleys (not shown) are alternately formed.
- the heat transfer portion 20 of each heat transfer plate 2 includes openings (no reference number is allocated) for forming the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35. That is, openings are provided at at least four places of the heat transfer portion 20 of each heat transfer plate 2. These openings are to form flow channels extending in the first direction.
- the plate heat exchanger 1 according to the present embodiment is provided with different kinds of the heat transfer plates 2.
- the plate heat exchanger 1 according to the present embodiment includes the heat transfer plates 2 each having openings for forming primary branch flow channels 36a or secondary branch flow channels 36b, as well as the heat transfer plates 2 each having the openings for forming the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35.
- the flow channels such as the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, the second outflow communication flow channel 35, the primary branch flow channels 36a, and the secondary branch flow channels 36b, and the like.
- the number, arrangement, dimensions, and the like of the openings for forming them are appropriately determined according to, for example, the intended use of the plate heat exchanger 1, the kind and flow rate of each of the first fluid medium A and the second fluid medium B, in the same manner as a conventional plate heat exchanger.
- the pair of end plates 4 and 5 each are provided by press-forming a metal plate and has substantially the same shape as that of the heat transfer plates 2.
- the end plates 4 and 5 include sealing portions 40 and 50, and annular fitting portions 41 and 51.
- the sealing portions 40 and 50 have substantially the same shape as that of the heat transfer portion 20.
- the annular fitting portions 41 and 51 extend from the entire outer circumferences of the sealing portions 40 and 50 in a direction orthogonal to the plane of the sealing portions 40 and 50.
- One end plate (hereinafter referred to as the "first end plate") 4 includes openings (no reference numeral is allocated) that correspond to the openings formed in the adjacent heat transfer plates 2 and are configured to form the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35. That is, the openings are provided at four places of the sealing portion 40 of the first end plate 4.
- tubular nozzles (no reference numeral is allocated) for connection of conduits are connected to the outer surface of the sealing portion 40 of the first end plate 4 in an arrangement corresponding to the respective openings.
- the sealing portion 50 of the other end plate (hereinafter referred to as the "second end plate") 5 is not provided with openings. That is, the second end plate 5 is provided with the sealing portion 50 that can seal the flow channels formed by the openings of the stacked heat transfer plates 2.
- the plurality of the heat transfer plates 2 are stacked on each other. In this state, the ridges of each adjacent heat transfer plates 2 abut each other at their crossing points, and the annular fitting portions 21 of each adjacent heat transfer plates 2 fit each other. Accordingly, the tight contact portions of each adjacent heat transfer plates 2 are sealed by brazing to thereby form the body portion 3.
- the plurality of the heat transfer plates 2 are stacked on each other with the first end plate 4 and the second end plate 5 sandwiching the stacked heat transfer plates 2 (the body portion 3).
- the annular fitting portions 21 of the first end plate 4 and the second end plate 5 respectively fit the fitting portions 21 of the adjacent heat transfer plates 2. Accordingly, the tight contact portions of the adjacent heat transfer plates 2 (the body portion 3) with the first end plate 4 and the second end plate 5 are sealed by brazing.
- the first flow channels 30 and the second flow channels 31 are alternately formed with the heat transfer plates 2 respectively therebetween.
- the first flow channels 30 circulate the first fluid medium A such as chlorofluorocarbon or ammonia whose phase changes.
- the second flow channels 31 circulate the second fluid medium B in liquid form such as water or brine.
- the openings of the plurality of the heat transfer plates 2 are connected to each other, thereby forming the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35, which extend in the first direction.
- each heat transfer plate 2 has a rectangular shape in plan view (as viewed in the direction of the normal line of the heat transfer portion 20).
- the first inflow communication flow channel 32 and the second outflow communication flow channel 35 are provided on one side end of the heat transfer plates 2 in the longitudinal direction of the heat transfer portion 20 (hereinafter referred to as the "second direction").
- the first outflow communication flow channel 33 and the second inflow communication flow channel 34 are provided on the other side end of the heat transfer plates 2 in the second direction.
- Fig. 3 is a schematic view, and therefore the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34, and the second outflow communication flow channel 35 align in the second direction (arranged in parallel).
- the first inflow communication flow channel 32 and the second outflow communication flow channel 35 align in the short side direction of the heat transfer portion 20 (the direction orthogonal to the first direction and the second direction, hereinafter referred to as the "third direction").
- the second inflow communication flow channel 34 and the first outflow communication flow channel 33 also align in the short side direction of the heat transfer portion 20 (the third direction).
- the first fluid medium A is circulated within the first flow channels 30 in the second direction orthogonal to the first direction.
- the second fluid medium B is circulated within the second flow channels 31 in the second direction. That is, in the plate heat exchanger 1 of the present embodiment, the first fluid medium A is circulated within the first flow channels 30 in the longitudinal direction of the heat transfer portion 20, and the second fluid medium B is circulated within the second flow channels 31 in the longitudinal direction of the heat transfer portion 20.
- the first flow channels 30 are communicated with each other to form a flow channel for the first fluid medium A from the first communication flow channel 32 to the first outflow communication flow channel 33.
- at least one first flow channel 30 located at an intermediate position in the first direction is a reference flow channel Ra which serves as a branching position of the flow channel of the first fluid medium A.
- the intermediate position in the present embodiment is an arbitrary position excluding the first flow channels 30 on both ends in the first direction.
- the body portion 3 includes one pair of primary branch flow channels 36a.
- the pair of primary branch flow channels 36a provide communication between the reference flow channel Ra and at least one first flow channel 30 located on one side of the reference flow channel Ra in the first direction, and provide communication between the reference flow channel Ra and at least one first flow channel 30 located on the other side of the reference flow channel Ra in the first direction. That is, the body portion 3 includes the primary branch flow channel 36a that provides communication (connection) between the reference flow channel Ra and at least one first flow channel 30 located on the one side of the reference flow channel Ra in the first direction, and the primary branch flow channel 36a that provides communication (connection) between the reference flow channel Ra and at least one first flow channel 30 located on the other side of the reference flow channel Ra.
- the primary branch flow channels 36a of the present embodiment extend through a center portion in the second direction of the heat transfer portion 20.
- the body portion 3 includes a plurality of the first flow channels 30 located on each of the one side and the other side of the reference flow channel Ra in the first direction.
- the plurality of the first flow channels 30 of the body portion 3 are grouped into two or more blocks B1 and B2.
- the entire portion on the one side in the first direction with the reference flow channel Ra as a boundary is grouped as a single block (hereinafter referred to as the "first large block B1").
- the entire portion on the other side in the first direction with the reference flow channel Ra as a boundary is grouped as a single block (hereinafter referred to as the "second large block B2").
- the plurality of the first flow channels 30 located in each of the first large block B1 and the second large block B2 are further grouped into a set of blocks B1a, B2a, B1b and B2b.
- the blocks B1a, B2a, B1b and B2b each include three or more first flow channels 30.
- the first flow channel 30 located at an intermediate position in the first direction of each of the first large block B1 and the second large block B2 is an intermediate reference flow channel Rb at which the flow channel of the first fluid medium A is branched off. That is, the first large block B1 and the second large block B2 each are sectioned into a single block that includes all of the first flow channels 30 (the plurality of the first flow channels 30) located on the one side in the first direction with each corresponding intermediate reference flow channel Rb as a boundary (this block is hereinafter referred to as the "first small block") B1a or B2a, and a single block that includes all of the first flow channels 30 (the plurality of the first flow channels 30) located on the other side in the first direction with each corresponding intermediate reference flow channel Rb as a boundasry (this block is hereinafter referred to as the "second small block”) B1b or B2b.
- the pair of primary branch flow channels 36a respectively communicate with the intermediate reference flow channels Rb. Specifically, the one of the pair of primary branch flow channels 36a extends through the second small block B1b of the first large block B1 and communicates with the intermediate reference flow channel Rb of the first large block B1. The other of the pair of primary branch flow channels 36a extends through the first small block B2a of the second large block B2 and communicates with the intermediate reference flow channel Rb of the second large block B2.
- the first large block B1 and the second large block B2 of the body portion 3 of the present embodiment are each sectioned into the blocks with the corresponding intermediate reference flow channel Rb.
- the body portion 3 includes at least the pair of secondary branch flow channels 36b.
- This pair of secondary branch flow channels 36b each provide communication (connection) between the corresponding intermediate reference flow channel Rb and at least one first flow channel 30 located on the one side of the corresponding intermediate reference flow channel Rb, or between the corresponding intermediate reference flow channel Rb and at least one first flow channel 30 located on the other side of the corresponding intermediate reference flow channel Rb in the first direction.
- the body portion 3 of the present embodiment includes the secondary branch flow channel 36b that provides communication (connection) between the corresponding intermediate reference flow channel Rb and at least one first flow channel 30 of the first small blocks B1a and B2a, and between the corresponding intermediate reference flow channel Rb and at least one first flow channel 30 of the second small blocks B1b and B2b.
- the first small blocks B1a and B2a, and the second small blocks B1b and B2b each include the plurality of the first flow channels 30.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b each include three first flow channels 30.
- the body portion 3 includes connection flow channels 37a and 37b that provide communication between the adjacent first flow channels 30 in each of the first small blocks B1a and B2a, and the second small blocks B1b and B2b.
- first small blocks B1a and B2a and the second small blocks B1b and B2b each include three first flow channels 30, as described above.
- the three first flow channels 30 are aligned in the first direction.
- the first flow channel (hereinafter referred to as the "innermost first flow channel”) 30 adjacent to the intermediate reference flow channel Rb communicates with the intermediate reference flow channel Rb via the secondary branch flow channels 36b.
- the innermost first flow channel 30 communicates with the first flow channel (the intermediate one of the three first flow channels 30 aligned in the first direction) (hereinafter referred to as the "intermediate first flow channel") 30 adjacent to itself on the opposite side of the intermediate reference flow channel Rb via a connection flow channel (hereinafter referred to as the "first connection flow channel”) 37a.
- the intermediate first flow channel 30 communicates with the first flow channel
- connection flow channel 30 adjacent to itself on the opposite side of the innermost first flow channel 30
- second connection flow channel 37b a connection flow channel
- the secondary branch flow channels 36b and the first connection flow channel 37a are arranged with a distance from each other in the second direction so as to allow the first fluid medium A to circulate through the first flow channel 30 in the second direction.
- the first connection flow channel 37a and the second connection flow channel 37b are arranged with a distance from each other in the second direction.
- the first inflow communication flow channel 32 is formed to extend from the one end in the first direction to the reference flow channel Ra located at the intermediate position in the first direction, and communicate only with the reference flow channel Ra.
- the first outflow communication flow channel 33 extends from one end to the other end in the first direction and communicates only with each of the outermost first flow channels 30 of the first small blocks B1a and B2a and the second small blocks B1b and B2b. That is, in the present embodiment, the terminal ends of the flow channels of the first fluid medium A in the first large block B1 and the second large block B2 (the terminal ends of the flow channels of the first fluid medium A formed with the reference flow channel Ra as a starting point by the first flow channels 30 communicating with each other) are the outermost first flow channels 30 of the first small blocks B1a and B2a and the second small blocks B1b and B2b.
- the outermost first flow channels 30 of the first large block B1 and the second large block B2 communicate only with the first outflow communication flow channel 33.
- the second inflow communication flow channel 34 and the second outflow communication flow channel 35 each extend from one end to the other end in the first direction of the body portion 3.
- the plurality of the second flow channels 31 aligned in the first direction each communicate with the second inflow communication flow channel 34 and the second outflow communication flow channel 35.
- the flow channel of the first fluid medium A is arranged in serpentine manner between the first inflow communication flow channel 32 and the first outflow communication flow channel 33.
- the flow channel of the second fluid medium B is arranged to be straight between the second inflow communication flow channel 34 and the second outflow communication flow channel 35.
- the plate heat exchanger 1 of the present embodiment includes the body portion 3 that includes the plurality of the stacked heat transfer plates 2, as described above.
- the body portion 3 includes the first flow channels 30 for circulating the first fluid medium A, the second flow channels 31 for circulating the second fluid medium B, the first inflow communication flow channel 32 and the first outflow communication flow channel 33 that respectively communicate with the first flow channels 30 and allow the first fluid medium A to flow into and out of the first flow channels 30, and the second inflow communication flow channel 34 and the second outflow communication flow channel 35 that respectively communicate with the second flow channels 31 and allow the second fluid medium B to flow into and out of the second flow channels 31.
- the first flow channels 30 and the second flow channels 31 are alternately formed with the heat transfer plates 2 respectively therebetween.
- the first inflow communication flow channel 32, the first outflow communication flow channel 33, the second inflow communication flow channel 34 and the second outflow communication flow channel 35 respectively extend through the heat transfer plates 2 in the first direction.
- At least one first flow channel 30 located at an intermediate position in the first direction is the reference flow channel Ra serving as a branching position of the flow channel of the first fluid medium A.
- the body portion 3 includes one pair of primary branch flow channels 36a that provide communication between the reference flow channel Ra and the first flow channel 30 located in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction).
- the first inflow communication flow channel 32 communicates only with the reference flow channel Ra.
- the first outflow communication flow channel 33 communicates only with the first flow channel 30 that is located on each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction), that serves as a terminal end of the first fluid medium A and that is formed with the reference flow channel Ra as a starting point by the first flow channels 30 communicating with each other.
- the first inflow communication flow channel 32 communicates only with the reference flow channel Ra (first flow channel 30) located at an intermediate position in the first direction.
- the first inflow communication flow channel 32 is formed to extend up to only the intermediate position in the first direction. Whereby, it is possible to suppress increase in pressure loss of the first fluid medium A in the first inflow communication flow channel 32.
- the pair of primary branch flow channels 36a provide communication between the reference flow channel Ra and the first flow channel 30 located in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Consequently , two systems are formed as flow channels of the first fluid medium A within the body portion 3, one including the one primary branch flow channel 36a communicating with the reference flow channel Ra, and the other including the other primary branch flow channel 36a communicating with the reference flow channel Ra.
- the length of the flow channel (the length of the flow channel per one system) of the first fluid medium A from the first inflow communication flow channel 32 to the first outflow communication flow channel 33 is shortened.
- the plate heat exchanger 1 having the above configuration makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A, and hence achieve high heat exchange performance.
- three or more first flow channels 30 are provided in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction).
- the first flow channel 30 located at an intermediate position in the first direction among the three or more first flow channels 30 is the intermediate reference flow channel Rb, which serves as a branching position of the flow channel of the first fluid medium A.
- the body portion 3 includes one pair of secondary branch flow channels 36b that provide communication between the corresponding intermediate reference flow channel Rb and the first flow channel 30 located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction).
- the primary branch flow channels 36a communicate respectively with the intermediate reference flow channels Rb located in the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction).
- the primary branch flow channels 36a each communicate only with the intermediate reference flow channel Rb (first flow channel 30) located at an intermediate position in the first direction in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction).
- the primary branch flow channels 36a each are formed to extend up only to the intermediate position in the first direction in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Therefore, it is possible to suppress increase in pressure loss of the first fluid medium A in the primary branch flow channels 36a.
- each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of the body portion 3, two systems are formed as flow channels of the first fluid medium A, one including the one secondary branch flow channel 36b communicating with the intermediate reference flow channel Rb, and the other including the other secondary branch flow channel 36b communicating with the intermediate reference flow channel Rb. Accordingly, in each of the first large block B1 and the second large block B2 of the body portion 3, the length of the flow channel of the first fluid medium A from the primary branch flow channel 36a to the first outflow communication flow channel 33 (the flow channel length per one system) is shortened. Whereby, the plate heat exchanger 1 having the above configuration makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A, and hence achieve high heat exchange performance.
- first flow channels 30 are provided in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction) in the first large block B1 and the second large block B2.
- the body portion 3 includes the connection flow channels 37a and 37b that each provide connection between the two or more first flow channels 30 in each of the first small blocks B1a and B2a (blocks on the one side of the intermediate reference flow channel Rb in the first direction) and the connection flow channels 37a and 37b that each provide connection between the two or more first flow channels 30 in each of the second small blocks B1b and B2b (blocks on the other side of the intermediate reference flow channel Rb in the first direction), in the first large block B1 and the second large block B2.
- the first flow channel 30 that is located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction), and that is formed by the first flow channels 30 communicating with each other so as to serve as a terminal end of the flow channel of the first fluid medium A with the reference flow channel Ra serving as a starting point.
- the heat transmission area can be increased without increase in length of the flow channel of the first fluid medium A.
- the plate heat exchanger according to the present invention is not necessarily limited to the above embodiment, and can be appropriately modified without departing from the gist of the present invention.
- the flow channel of the first fluid medium A in the first large block B1 and the flow channel of the first fluid medium A in the second large block B2 are symmetrically formed with reference to the reference flow channel Ra, but the present invention is not necessarily limited to this arrangement.
- the flow channel of the first fluid medium A in the first large block B1 and the flow channel of the first fluid medium A in the second large block B2 may be formed unsymmetrically with reference to the reference flow channel Ra. That is, the number of the first flow channels 30, the arrangement of the intermediate reference flow channels Rb, the arrangement of the secondary branch flow channels 36b or the like may be different from each other between the first large block B1 and the second large block B2.
- the first large block B1 and the second large block B2 of the above embodiment each are sectioned into two small blocks (the first small block and the second small block) B1a, B2a, B1b and B2b with reference to the intermediate reference flow channel Rb, but there is no limitation thereto.
- all of the first flow channels 30 located in each of the first large block B1 and the second large block B2 may directly communicate with the first outflow communication flow channel 33.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass the three first flow channels 30.
- the present invention is not necessarily limited thereto.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b each may encompass at least one first flow channel 30, and allow itself (first flow channel 30) to communicate with the first outflow communication flow channel 33.
- the flow channel of one system may be formed by the first flow channels 30 encompassed in the first small blocks B1a and B2a and the second small blocks B1b and B2b, and the first flow channel 30 serving as its terminal end may communicate with the first outflow communication flow channel 33.
- the first large block B1 and the second large block B2 of the above embodiment are sectioned into the first small blocks B1a and B2a and the second small blocks B1b and B2b, only.
- the present invention is not necessarily limited thereto.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b may be further sectioned into smaller blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2.
- the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) each are sectioned into the first small blocks B1a and B2a and the second small blocks B1b and B2b.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b each include a plurality of the first flow channels 30.
- the first flow channel 30 located at an intermediate position in the first direction of the plurality of first flow channels 30 in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction) is a branch reference flow channel Rc that serves as a branching position of the flow channel of the first fluid medium A.
- the body portion 3 includes a pair of tertiary branch flow channels 36c that provide communication between the branch reference flow channel Rc and the first flow channel 30 located in each of the blocks on the one side and the other side of the branch reference flow channel Rc in the first direction (hereinafter referred to as the minimal blocks) B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2.
- the pair of secondary branch flow channels 36b each may communicate with the branch reference flow channel Rc located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction).
- At least one first flow channel 30 that is located in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and that serves as a terminal end of the flow channel of the first fluid medium A communicates with the first outflow communication flow channel 33.
- the secondary branch flow channels 36b communicate only with the branch reference flow channel Rc (first flow channel 30) located at an intermediate position in the first direction in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b in the first large block B1 and the second large block B2. Accordingly, the secondary branch flow channels 36b are formed to extend only up to the intermediate position in the first direction in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Thus, it is possible to suppress increase in pressure loss of the first fluid medium A in the secondary branch flow channels 36b.
- first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb) of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of the body portion 3
- two systems are provided as flow channels of the first fluid medium A, namely one system including the one of the pair of tertiary branch flow channels 36c communicating with the branch reference flow channel Rc, and the other system including the other of the pair of tertiary branch flow channels 36c communicating with the branch reference flow channel Rc.
- the length of the flow channel of the first fluid medium A from the secondary branch flow channel 36b to the first outflow communication flow channel 33 becomes shortened in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of the body portion 3.
- the plate heat exchanger 1 thus configured makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A and hence produce high heat exchange performance.
- two or more first flow channels 30 are provided in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction).
- the body portion 3 may include connection flow channels 37a, 37b and 37c for providing communication between the two or more first flow channels 30 in the minimum blocks B1a1, B1b1, B2a1 and B2b1 on the one side with reference to the branch reference flow channel Rc (blocks on the one side of the branch reference flow channel Rc in the first direction), and connection flow channels 37a, 37b and 37c for providing communication between the two or more first flow channels 30 in the minimum blocks B1a2, B1b2, B2a2 and B2b2 on the other side with reference to the branch reference flow channel Rc (blocks on the other side of the branch reference flow channel Rc in the first direction).
- the first flow channel 30 that is located in each of the blocks thus sectioned with reference to the branch reference flow channel Rc, namely the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and that serves as a terminal end of the flow channel of the first fluid medium A, communicates with the first outflow communication flow channel 33.
- this configuration it is possible to increase the heat transfer area without extending the length of the flow channel of the first fluid medium A.
- one first flow channel 30 may be provided in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and may communicate with the first outflow communication flow channel 33.
- this configuration it is possible to suppress pressure loss in the flow channel of the first fluid medium A.
- the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass three first flow channels 30, and these first flow channels 30 sequentially communicate with each other to allow the flow channel of the first fluid medium A to be formed in serpentine manner, but there is no limitation thereto.
- it may be configured such that the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass a plurality of first flow channels 30, and all of the plurality of the first flow channels 30 communicate with the secondary branch flow channels 36b and the first outflow communication flow channel 33.
- the first fluid medium A flows from the secondary branch flow channels 36b into the plurality of the first flow channels 30, then circulates in the plurality of the first flow channels 30, and then flows out of the first outflow communication flow channel 33.
- a large heat transfer area can be secured without extending the length of the flow channel of the first fluid medium A, and a high heat exchange can be achieved.
- the flow channel of the first fluid medium A in each of the first large block B1 and the second large block B2 is subsequently branched off at the intermediate reference flow channel Rb and the branch reference flow channel Rc as branching positions.
- the present invention is not necessarily limited thereto.
- it may be configured such that the primary branch flow channels 36a communicate with the plurality of the first flow channels 30 located in each of the first large block B1 and the second large block B2, and the plurality of the first flow channels 30 located in each of the first large block B1 and the second large block B2 directly communicate with the first outflow communication flow channel 33.
- the first communication flow channel 32 extends up to the intermediate position from the one end of the body portion 3, the length of the flow channel of the first communication flow channel 32 is not increased, and hence it is possible to suppress increase in pressure loss of the first fluid medium A.
- the body portion 3 of the above embodiment includes a pair of primary branch flow channels 36a, but there is no limitation thereto.
- the body portion 3 may include two or more pairs of primary branch flow channels 36a. That is, the body portion 3 may include at least a pair of primary branch flow channels 36a.
- the second pair of primary branch flow channels 36a each communicate only with the first flow channel 30 located in an area (second area) outside, with reference to the reference flow channel Ra, of the area (first area) in which the flow channel of the first fluid medium A with the first pair of primary branch flow channels 36a serving as a starting point is located.
- nth pair of primary branch flow channels 36a communicate only with the first flow channels 30 located in an area (the nth area) outside of the nth - 1 area of the body portion 3, and the flow channel of the first fluid medium A with the nth pair of primary branch flow channels 36a serving as a starting point is located in the nth area, in which n is natural number.
- the plurality of the second flow channels 31 each communicate with the second inflow communication flow channel 34 and the second outflow communication flow channel 35, and the flow channel of the second fluid medium B that connects the second inflow communication flow channel 34 and the second outflow communication flow channel 35 is formed to be straight, but there is no limitation thereto.
- the flow channel of the second fluid medium B that connects the second inflow communication flow channel 34 and the second outflow communication flow channel 35 may be formed in serpentine manner in the same manner as the flow channel of the first fluid medium A.
- the flow channel of the second fluid medium B may be branched off at least at one place on each of the one side and the other side of the body portion 3 in the first direction, in the same manner as the flow channel of the first fluid medium A, and the second outflow communication flow channel 35 may communicate only with the second flow channel 31 that is located on each of the one side and the other side in the first direction in the body portion 3, and that is a terminal end of the flow channel of the second fluid medium B.
- it may be configured such that a flow channel which serves as a branching position of the flow channel of the second fluid medium B is provided, and the body portion 3 is sectioned into small blocks with reference to this flow channel so that the circulation route of the second fluid medium B may be branched off at least at two places.
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Abstract
Description
- This application claims priority to Japanese Patent Application No.
2013-74896 - The present invention relates to a plate heat exchanger that is used as an evaporator and a condenser.
- There are hitherto many cases, in which a plate heat exchanger is used as an evaporator that evaporates a first fluid medium along with heat exchange between the first fluid medium and a second fluid medium, and as a condenser that condenses a first fluid medium along with heat exchange between the first fluid medium and a second fluid medium (see Patent Literature 1, for example).
- As shown in
Fig. 5 , a plate heat exchanger generally includes abody portion 3 that includes a plurality ofheat transfer plates 2. Thebody portion 3 includesfirst flow channels 30,second flow channels 31, a pair of firstcommunication flow channels communication flow channels first flow channel 30 circulates a first fluid medium A. Thesecond flow channel 31 circulates a second fluid medium B. The pair of firstcommunication flow channels first flow channels 30 to allow the first fluid medium A to flow into and out of thefirst flow channels 30. A pair of secondcommunication flow channels second flow channels 31 to allow the second fluid medium B to flow into and out of thesecond flow channels 31. - More specific description is given herein. The plurality of the
heat transfer plates 2 each include at least four openings (no reference numeral is allocated). The plurality of theheat transfer plates 2 are stacked on each other in thebody portion 3. With this configuration, thefirst flow channels 30 for circulation of the first fluid medium A and thesecond flow channels 31 for circulation of the second fluid medium B are alternately formed with the plurality of theheat transfer plates 2 respectively interposed therebetween. With the plurality of the heat transfer plates stacked on each other, each opening of each of the plurality of theheat transfer plates 2 forms a continuous opening extending in the stacked direction of the plurality of theheat transfer plates 2. Whereby, the one firstcommunication flow channel 32 for flowing the first fluid medium A into thefirst flow channels 30, the other firstcommunication flow channel 33 for flowing the first fluid medium A out of thefirst flow channels 30, the one secondcommunication flow channel 34 for flowing the second fluid medium B into thesecond flow channels 31, and the other secondcommunication flow channel 35 for flowing the second fluid medium B out of thesecond flow channels 31 extend through the plurality of theheat transfer plates 2 in the stacked direction of the plurality of the heat transfer plates 2 (see Patent Literature 1, for example). - In a plate heat exchanger 1 of this type, the first fluid medium A supplied into the one first
communication flow channel 32 flows out to the other firstcommunication flow channel 33 through thefirst flow channels 30. The second fluid medium B supplied into the one secondcommunication flow channel 34 flows out to the other secondcommunication flow channel 35 through thesecond flow channels 31. As described above, in the plate heat exchanger 1, the first fluid medium A circulates in thefirst flow channels 30, and the second fluid medium B circulates in thesecond flow channels 31. Whereby, the plate heat exchanger 1 enables the heat exchange between the first fluid medium A and the second fluid medium B through a large heat transfer surface of eachheat transfer plate 2 separating thefirst flow channel 30 and thesecond flow channel 31. - Meanwhile, in the plate heat exchanger 1 of this type, as the number of the
heat transfer plates 2 increases, the heat transfer surface area contributing to the heat exchange increases and thereby it is assumed that the heat exchange performance becomes high. - However, as the number of the
heat transfer plates 2 increases, the firstcommunication flow channels communication flow channels heat transfer plates 2 increase in length according to the number of the stackedheat transfer plates 2. - That is, the pair of first
communication flow channels communication flow channels heat transfer plates 2, so that the flow channel length of each of the pair of firstcommunication flow channels communication flow channels heat transfer plates 2 when the number thereof increases. - As a result, the resistance of the first fluid medium A in the first communication flow channel (the one first communication flow channel) 32 for flowing the first fluid medium A into the
first flow channels 30 increases and thus the first fluid medium A is not easy to circulate. Therefore, in the plate heat exchanger 1 of this type, the inflow of the first fluid medium A into thefirst flow channels 30 at the inlet side of the one firstcommunication flow channel 32 and the inflow of the first fluid medium A into thefirst flow channels 30 at the far side of the one firstcommunication flow channel 32 become uneven. That is, in the plate heat exchanger 1 of this type, distribution unevenness of the first fluid medium A is caused in the plurality of thefirst flow channels 30 aligning in the stacked direction of theheat transfer plates 2. As a result, in the plate heat exchanger 1 of this type, even if the number of theheat transfer plates 2 is increased or the number of thefirst flow channels 30 is increased, there is a limit in improving the heat exchange performance (evaporation performance). - PATENT LITERATURE 1
JP-1999-287572 A - In view of the above, an object of the present invention is to provide a plate heat exchanger that is capable of evenly supplying a first fluid medium into a plurality of first flow channels for circulation of the first fluid medium, while suppressing increase in pressure loss in the plurality of the first flow channels.
- According to the present invention, there is provided a plate heat exchanger including a body portion that includes a plurality of heat transfer plates stacked on each other, the body portion further including a plurality of first flow channels that circulate a first fluid medium, a plurality of second flow channels that circulate a second fluid medium, a pair of first communication flow channels that communicate with the plurality of the first flow channels and allow the first fluid medium to flow into and out of the plurality of the first flow channels, a pair of second communication flow channels that communicate with the plurality of the second flow channels and allow the second fluid medium to flow into and out of the plurality of the second flow channels, the plurality of the first flow channels and the plurality of the second flow channels being alternately formed with the plurality of the heat transfer plates being respectively interposed therebetween, and the pair of first communication flow channels and the pair of second communication flow channels extending in the stacked direction of the plurality of the heat transfer plates through the plurality of the heat transfer plates. The plurality of the first flow channels communicate with each other to form a flow channel of the first fluid medium from one of the pair of first communication flow channels to the other of the pair of first communication flow channels. At least one of the plurality of the first flow channels located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a reference flow channel that serves as a branching position of the flow channel of the first fluid medium. The body portion includes at least one pair of primary branch flow channels that provide communication between the reference flow channel and at least one first flow channel located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates. The one of the pair of first communication flow channels communicates only with the reference flow channel. The other of the pair of first communication flow channels communicates only with the first flow channel that is located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium.
- According to one aspect of the present invention, it may be configured such that three or more fist flow channels are provided on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates. In this configuration, of the three or more first flow channels provided on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is an intermediate reference flow channel that serves as a branching position of the flow channel of the first fluid medium. The body portion includes a pair of secondary branch flow channels that each provide communication between the corresponding intermediate reference flow channel and at least one first flow channel located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates. The pair of primary branch flow channels respectively communicate with the corresponding intermediate reference flow channels located respectively on the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates.
- In this case, the plate heat exchanger may be configured such that: two or more first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates. In this configuration, the body portion includes a connection flow channel that connects the two or more first flow channels with each other on the one side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, and a connection flow channel that connects the two or more first flow channels with each other on the other side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates. At least one first flow channel that is located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates the other of the pair of first communication flow channels.
- In this case, according to another aspect of the present invention, it may be configured such that: a plurality of the first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of heat transfer plates. In this configuration, of the plurality of the first flow channels provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a branch reference flow channel that serves as a branching position of the flow channel of the first fluid medium. The body portion includes a pair of tertiary branch flow channels that provide communication between the branch reference flow channel and the first flow channel located on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates. The pair of secondary branch flow channels respectively communicate with the branch reference flow channels located respectively on the one side and the other side of the intermediate reference flow channel in the stacked direction of the heat transfer plates. At least one first flow channel that is located on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates with the other of the pair of first communication flow channels.
- In this case, the plate heat exchanger may be configured such that: one first flow channel is provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and communicates with the other of the pair of first communication flow channels.
- Also, the plate heat exchanger may be configured such that: two or more first flow channels are provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates. In this configuration, the body portion includes a connection flow channel that connects the two or more first flow channels located on the one side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and a connection flow channel that connects the two or more first flow channels located on the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates. At least one first flow channel that is located on the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates with the other of the pair of first communication flow channels.
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Fig. 1 is a schematic overall perspective view of a plate heat exchanger according to one embodiment of the present invention. -
Fig. 2 is a schematic exploded perspective view of the plate heat exchanger according to the embodiment of the present invention. -
Fig. 3 is a schematic view for explaining a flow channel of a first fluid medium and a flow channel of a second fluid medium in the plate heat exchanger according to the embodiment of the present invention. -
Fig. 4 is a schematic view for explaining a flow channel of a first fluid medium and a flow channel of a second fluid medium in a plate heat exchanger according to another embodiment of the present invention. -
Fig. 5 is a schematic view for explaining a flow channel of a first fluid medium and a flow channel of a second fluid medium in a conventional plate heat exchanger. - A description is given for a plate heat exchanger according to one embodiment of the present invention with reference to the attached drawings.
- As shown in
Fig. 1 , the plate heat exchanger includes abody portion 3 that includes a plurality ofheat transfer plates 2 stacked on each other. - As shown in
Fig. 2 andFig. 3 , thebody portion 3 includesfirst flow channels 30,second flow channels 31, a pair of firstcommunication flow channels communication flow channels first flow channels 30 circulate a first fluid medium A. Thesecond flow channels 31 circulate a second fluid medium B. The pair of firstcommunication flow channels first flow channels 30 to allow the first fluid medium A to flow into and out of thefirst flow channels 30. The pair of secondcommunication flow channels second flow channels 31 to allow the second fluid medium B to flow into and out of thesecond flow channels 31. In the following description, onepassage 32 of the pair of firstcommunication flow channels other passage 33 of the pair of firstcommunication flow channels passage 34 of the pair of secondcommunication flow channels other passage 35 of the pair of secondcommunication flow channels - The
first flow channels 30 and thesecond flow channels 31 are alternately formed with theheat transfer plates 2 respectively interposed therebetween. On the other hand, the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35 each extend through theheat transfer plates 2 in the stacked direction of the plurality of the heat transfer plates 2 (hereinafter referred to as the "first direction"). - A more specific description is given herein. A plate heat exchanger 1 according to this embodiment includes the
body portion 3 that includes the plurality of theheat transfer plates 2 stacked on each other, and a pair ofend plates 4 and 5 that sandwich thebody portion 3. - The plurality of the
heat transfer plates 2 each are provided by press forming a metal plate, as shown inFig. 2 . The plurality of theheat transfer plates 2 each include aheat transfer portion 20 that defines thefirst flow channel 30 and thesecond flow channel 31, and an annularfitting portion 21 that extends from the outer circumference of theheat transfer portion 20 in a direction orthogonal to the plane of theheat transfer portion 20. - Each of the
heat transfer plates 2 includes a front side and a back side on which a plurality of ridges and valleys (not shown) are alternately formed. Theheat transfer portion 20 of eachheat transfer plate 2 includes openings (no reference number is allocated) for forming the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35. That is, openings are provided at at least four places of theheat transfer portion 20 of eachheat transfer plate 2. These openings are to form flow channels extending in the first direction. - The plate heat exchanger 1 according to the present embodiment is provided with different kinds of the
heat transfer plates 2. The plate heat exchanger 1 according to the present embodiment includes theheat transfer plates 2 each having openings for forming primarybranch flow channels 36a or secondarybranch flow channels 36b, as well as theheat transfer plates 2 each having the openings for forming the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35. In the present embodiment, detailed description is given for the flow channels such as the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, the second outflowcommunication flow channel 35, the primarybranch flow channels 36a, and the secondarybranch flow channels 36b, and the like. The number, arrangement, dimensions, and the like of the openings for forming them are appropriately determined according to, for example, the intended use of the plate heat exchanger 1, the kind and flow rate of each of the first fluid medium A and the second fluid medium B, in the same manner as a conventional plate heat exchanger. - The pair of
end plates 4 and 5 each are provided by press-forming a metal plate and has substantially the same shape as that of theheat transfer plates 2. Specifically, theend plates 4 and 5 include sealingportions fitting portions portions heat transfer portion 20. The annularfitting portions portions portions - One end plate (hereinafter referred to as the "first end plate") 4 includes openings (no reference numeral is allocated) that correspond to the openings formed in the adjacent
heat transfer plates 2 and are configured to form the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35. That is, the openings are provided at four places of the sealingportion 40 of the first end plate 4. Along with this configuration, tubular nozzles (no reference numeral is allocated) for connection of conduits are connected to the outer surface of the sealingportion 40 of the first end plate 4 in an arrangement corresponding to the respective openings. - On the other hand, the sealing
portion 50 of the other end plate (hereinafter referred to as the "second end plate") 5 is not provided with openings. That is, thesecond end plate 5 is provided with the sealingportion 50 that can seal the flow channels formed by the openings of the stackedheat transfer plates 2. - The plurality of the
heat transfer plates 2 are stacked on each other. In this state, the ridges of each adjacentheat transfer plates 2 abut each other at their crossing points, and the annularfitting portions 21 of each adjacentheat transfer plates 2 fit each other. Accordingly, the tight contact portions of each adjacentheat transfer plates 2 are sealed by brazing to thereby form thebody portion 3. - The plurality of the
heat transfer plates 2 are stacked on each other with the first end plate 4 and thesecond end plate 5 sandwiching the stacked heat transfer plates 2 (the body portion 3). In this state, the annularfitting portions 21 of the first end plate 4 and thesecond end plate 5 respectively fit thefitting portions 21 of the adjacentheat transfer plates 2. Accordingly, the tight contact portions of the adjacent heat transfer plates 2 (the body portion 3) with the first end plate 4 and thesecond end plate 5 are sealed by brazing. - With the above configuration, as shown in
Fig. 2 andFig. 3 , thefirst flow channels 30 and thesecond flow channels 31 are alternately formed with theheat transfer plates 2 respectively therebetween. In the present embodiment, thefirst flow channels 30 circulate the first fluid medium A such as chlorofluorocarbon or ammonia whose phase changes. Thesecond flow channels 31 circulate the second fluid medium B in liquid form such as water or brine. - The openings of the plurality of the
heat transfer plates 2 are connected to each other, thereby forming the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35, which extend in the first direction. - A more specific description is given herein. In the present embodiment, the
heat transfer portion 20 of eachheat transfer plate 2 has a rectangular shape in plan view (as viewed in the direction of the normal line of the heat transfer portion 20). - The first inflow
communication flow channel 32 and the second outflowcommunication flow channel 35 are provided on one side end of theheat transfer plates 2 in the longitudinal direction of the heat transfer portion 20 (hereinafter referred to as the "second direction"). The first outflowcommunication flow channel 33 and the second inflowcommunication flow channel 34 are provided on the other side end of theheat transfer plates 2 in the second direction. -
Fig. 3 is a schematic view, and therefore the first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34, and the second outflowcommunication flow channel 35 align in the second direction (arranged in parallel). However, according to the actual arrangement, the first inflowcommunication flow channel 32 and the second outflowcommunication flow channel 35 align in the short side direction of the heat transfer portion 20 (the direction orthogonal to the first direction and the second direction, hereinafter referred to as the "third direction"). The second inflowcommunication flow channel 34 and the first outflowcommunication flow channel 33 also align in the short side direction of the heat transfer portion 20 (the third direction). - With the above configuration, in the plate heat exchanger 1, the first fluid medium A is circulated within the
first flow channels 30 in the second direction orthogonal to the first direction. The second fluid medium B is circulated within thesecond flow channels 31 in the second direction. That is, in the plate heat exchanger 1 of the present embodiment, the first fluid medium A is circulated within thefirst flow channels 30 in the longitudinal direction of theheat transfer portion 20, and the second fluid medium B is circulated within thesecond flow channels 31 in the longitudinal direction of theheat transfer portion 20. - In the plate heat exchanger 1 of the present embodiment, the
first flow channels 30 are communicated with each other to form a flow channel for the first fluid medium A from the firstcommunication flow channel 32 to the first outflowcommunication flow channel 33. In the plate heat exchanger 1 of the present embodiment, at least one first flow channel 30 (one first flow channel in an example of the present embodiment) located at an intermediate position in the first direction is a reference flow channel Ra which serves as a branching position of the flow channel of the first fluid medium A. The intermediate position in the present embodiment is an arbitrary position excluding thefirst flow channels 30 on both ends in the first direction. - The
body portion 3 includes one pair of primarybranch flow channels 36a. The pair of primarybranch flow channels 36a provide communication between the reference flow channel Ra and at least onefirst flow channel 30 located on one side of the reference flow channel Ra in the first direction, and provide communication between the reference flow channel Ra and at least onefirst flow channel 30 located on the other side of the reference flow channel Ra in the first direction. That is, thebody portion 3 includes the primarybranch flow channel 36a that provides communication (connection) between the reference flow channel Ra and at least onefirst flow channel 30 located on the one side of the reference flow channel Ra in the first direction, and the primarybranch flow channel 36a that provides communication (connection) between the reference flow channel Ra and at least onefirst flow channel 30 located on the other side of the reference flow channel Ra. The primarybranch flow channels 36a of the present embodiment extend through a center portion in the second direction of theheat transfer portion 20. - In the present embodiment, the
body portion 3 includes a plurality of thefirst flow channels 30 located on each of the one side and the other side of the reference flow channel Ra in the first direction. - The plurality of the
first flow channels 30 of thebody portion 3 are grouped into two or more blocks B1 and B2. In thebody portion 3 of the present embodiment, the entire portion on the one side in the first direction with the reference flow channel Ra as a boundary is grouped as a single block (hereinafter referred to as the "first large block B1"). In thebody portion 3, the entire portion on the other side in the first direction with the reference flow channel Ra as a boundary is grouped as a single block (hereinafter referred to as the "second large block B2"). - The plurality of the
first flow channels 30 located in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) are further grouped into a set of blocks B1a, B2a, B1b and B2b. The blocks B1a, B2a, B1b and B2b each include three or morefirst flow channels 30. - In the present embodiment, the
first flow channel 30 located at an intermediate position in the first direction of each of the first large block B1 and the second large block B2 is an intermediate reference flow channel Rb at which the flow channel of the first fluid medium A is branched off. That is, the first large block B1 and the second large block B2 each are sectioned into a single block that includes all of the first flow channels 30 (the plurality of the first flow channels 30) located on the one side in the first direction with each corresponding intermediate reference flow channel Rb as a boundary (this block is hereinafter referred to as the "first small block") B1a or B2a, and a single block that includes all of the first flow channels 30 (the plurality of the first flow channels 30) located on the other side in the first direction with each corresponding intermediate reference flow channel Rb as a boundasry (this block is hereinafter referred to as the "second small block") B1b or B2b. - The pair of primary
branch flow channels 36a respectively communicate with the intermediate reference flow channels Rb. Specifically, the one of the pair of primarybranch flow channels 36a extends through the second small block B1b of the first large block B1 and communicates with the intermediate reference flow channel Rb of the first large block B1. The other of the pair of primarybranch flow channels 36a extends through the first small block B2a of the second large block B2 and communicates with the intermediate reference flow channel Rb of the second large block B2. - As described above, the first large block B1 and the second large block B2 of the
body portion 3 of the present embodiment are each sectioned into the blocks with the corresponding intermediate reference flow channel Rb. With this configuration, thebody portion 3 includes at least the pair of secondarybranch flow channels 36b. This pair of secondarybranch flow channels 36b each provide communication (connection) between the corresponding intermediate reference flow channel Rb and at least onefirst flow channel 30 located on the one side of the corresponding intermediate reference flow channel Rb, or between the corresponding intermediate reference flow channel Rb and at least onefirst flow channel 30 located on the other side of the corresponding intermediate reference flow channel Rb in the first direction. That is, thebody portion 3 of the present embodiment includes the secondarybranch flow channel 36b that provides communication (connection) between the corresponding intermediate reference flow channel Rb and at least onefirst flow channel 30 of the first small blocks B1a and B2a, and between the corresponding intermediate reference flow channel Rb and at least onefirst flow channel 30 of the second small blocks B1b and B2b. - In the present embodiment, the first small blocks B1a and B2a, and the second small blocks B1b and B2b each include the plurality of the
first flow channels 30. Specifically, the first small blocks B1a and B2a and the second small blocks B1b and B2b each include threefirst flow channels 30. - In association with the above configuration, the
body portion 3 includesconnection flow channels first flow channels 30 in each of the first small blocks B1a and B2a, and the second small blocks B1b and B2b. - More specifically, the first small blocks B1a and B2a and the second small blocks B1b and B2b each include three
first flow channels 30, as described above. The threefirst flow channels 30 are aligned in the first direction. The first flow channel (hereinafter referred to as the "innermost first flow channel") 30 adjacent to the intermediate reference flow channel Rb communicates with the intermediate reference flow channel Rb via the secondarybranch flow channels 36b. The innermostfirst flow channel 30 communicates with the first flow channel (the intermediate one of the threefirst flow channels 30 aligned in the first direction) (hereinafter referred to as the "intermediate first flow channel") 30 adjacent to itself on the opposite side of the intermediate reference flow channel Rb via a connection flow channel (hereinafter referred to as the "first connection flow channel") 37a. The intermediatefirst flow channel 30 communicates with the first flow channel - (hereinafter referred to as the "outermost first flow channel") 30 adjacent to itself on the opposite side of the innermost first flow channel 30) via a connection flow channel (hereinafter referred to as the "second connection flow channel") 37b.
- As described above, the secondary
branch flow channels 36b and the firstconnection flow channel 37a are arranged with a distance from each other in the second direction so as to allow the first fluid medium A to circulate through thefirst flow channel 30 in the second direction. Also, the firstconnection flow channel 37a and the secondconnection flow channel 37b are arranged with a distance from each other in the second direction. With this configuration, in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b, the flow channel of the first fluid medium A is arranged in serpentine manner through the innermostfirst flow channel 30, the firstconnection flow channel 37a, the intermediatefirst flow channel 30, the secondconnection flow channel 37b, and the outermostfirst flow channel 30. - In the present embodiment, the first inflow
communication flow channel 32 is formed to extend from the one end in the first direction to the reference flow channel Ra located at the intermediate position in the first direction, and communicate only with the reference flow channel Ra. - Contrary to the above, the first outflow
communication flow channel 33 extends from one end to the other end in the first direction and communicates only with each of the outermostfirst flow channels 30 of the first small blocks B1a and B2a and the second small blocks B1b and B2b. That is, in the present embodiment, the terminal ends of the flow channels of the first fluid medium A in the first large block B1 and the second large block B2 (the terminal ends of the flow channels of the first fluid medium A formed with the reference flow channel Ra as a starting point by thefirst flow channels 30 communicating with each other) are the outermostfirst flow channels 30 of the first small blocks B1a and B2a and the second small blocks B1b and B2b. - Along with this, the outermost
first flow channels 30 of the first large block B1 and the second large block B2 communicate only with the first outflowcommunication flow channel 33. - Contrary to the above, the second inflow
communication flow channel 34 and the second outflowcommunication flow channel 35 each extend from one end to the other end in the first direction of thebody portion 3. The plurality of thesecond flow channels 31 aligned in the first direction each communicate with the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35. - Accordingly, in the plate heat exchanger 1 of the present embodiment, the flow channel of the first fluid medium A is arranged in serpentine manner between the first inflow
communication flow channel 32 and the first outflowcommunication flow channel 33. On the other hand, the flow channel of the second fluid medium B is arranged to be straight between the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35. - The plate heat exchanger 1 of the present embodiment includes the
body portion 3 that includes the plurality of the stackedheat transfer plates 2, as described above. Thebody portion 3 includes thefirst flow channels 30 for circulating the first fluid medium A, thesecond flow channels 31 for circulating the second fluid medium B, the first inflowcommunication flow channel 32 and the first outflowcommunication flow channel 33 that respectively communicate with thefirst flow channels 30 and allow the first fluid medium A to flow into and out of thefirst flow channels 30, and the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35 that respectively communicate with thesecond flow channels 31 and allow the second fluid medium B to flow into and out of thesecond flow channels 31. Thefirst flow channels 30 and thesecond flow channels 31 are alternately formed with theheat transfer plates 2 respectively therebetween. The first inflowcommunication flow channel 32, the first outflowcommunication flow channel 33, the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35 respectively extend through theheat transfer plates 2 in the first direction. - In the plate heat exchanger 1 of the present embodiment, at least one
first flow channel 30 located at an intermediate position in the first direction is the reference flow channel Ra serving as a branching position of the flow channel of the first fluid medium A. Thebody portion 3 includes one pair of primarybranch flow channels 36a that provide communication between the reference flow channel Ra and thefirst flow channel 30 located in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). The first inflowcommunication flow channel 32 communicates only with the reference flow channel Ra. The first outflowcommunication flow channel 33 communicates only with thefirst flow channel 30 that is located on each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction), that serves as a terminal end of the first fluid medium A and that is formed with the reference flow channel Ra as a starting point by thefirst flow channels 30 communicating with each other. - Thus, according to the plate heat exchanger 1 of the present embodiment, the first inflow
communication flow channel 32 communicates only with the reference flow channel Ra (first flow channel 30) located at an intermediate position in the first direction. Thus, the first inflowcommunication flow channel 32 is formed to extend up to only the intermediate position in the first direction. Whereby, it is possible to suppress increase in pressure loss of the first fluid medium A in the first inflowcommunication flow channel 32. - The pair of primary
branch flow channels 36a provide communication between the reference flow channel Ra and thefirst flow channel 30 located in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Consequently , two systems are formed as flow channels of the first fluid medium A within thebody portion 3, one including the one primarybranch flow channel 36a communicating with the reference flow channel Ra, and the other including the other primarybranch flow channel 36a communicating with the reference flow channel Ra. - Accordingly, the length of the flow channel (the length of the flow channel per one system) of the first fluid medium A from the first inflow
communication flow channel 32 to the first outflowcommunication flow channel 33 is shortened. Whereby, the plate heat exchanger 1 having the above configuration makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A, and hence achieve high heat exchange performance. - In the present embodiment, three or more
first flow channels 30 are provided in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). In each of the first large block B1 and the second large block B2, thefirst flow channel 30 located at an intermediate position in the first direction among the three or morefirst flow channels 30 is the intermediate reference flow channel Rb, which serves as a branching position of the flow channel of the first fluid medium A. Thebody portion 3 includes one pair of secondarybranch flow channels 36b that provide communication between the corresponding intermediate reference flow channel Rb and thefirst flow channel 30 located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction). The primarybranch flow channels 36a communicate respectively with the intermediate reference flow channels Rb located in the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). - Accordingly, the primary
branch flow channels 36a each communicate only with the intermediate reference flow channel Rb (first flow channel 30) located at an intermediate position in the first direction in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Thus, the primarybranch flow channels 36a each are formed to extend up only to the intermediate position in the first direction in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Therefore, it is possible to suppress increase in pressure loss of the first fluid medium A in the primarybranch flow channels 36a. In each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of thebody portion 3, two systems are formed as flow channels of the first fluid medium A, one including the one secondarybranch flow channel 36b communicating with the intermediate reference flow channel Rb, and the other including the other secondarybranch flow channel 36b communicating with the intermediate reference flow channel Rb. Accordingly, in each of the first large block B1 and the second large block B2 of thebody portion 3, the length of the flow channel of the first fluid medium A from the primarybranch flow channel 36a to the first outflow communication flow channel 33 (the flow channel length per one system) is shortened. Whereby, the plate heat exchanger 1 having the above configuration makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A, and hence achieve high heat exchange performance. - In particular, two or more
first flow channels 30 are provided in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction) in the first large block B1 and the second large block B2. Thebody portion 3 includes theconnection flow channels first flow channels 30 in each of the first small blocks B1a and B2a (blocks on the one side of the intermediate reference flow channel Rb in the first direction) and theconnection flow channels first flow channels 30 in each of the second small blocks B1b and B2b (blocks on the other side of the intermediate reference flow channel Rb in the first direction), in the first large block B1 and the second large block B2. Thefirst flow channel 30 that is located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction), and that is formed by thefirst flow channels 30 communicating with each other so as to serve as a terminal end of the flow channel of the first fluid medium A with the reference flow channel Ra serving as a starting point. Whereby, the heat transmission area can be increased without increase in length of the flow channel of the first fluid medium A. - It is a matter of course that the plate heat exchanger according to the present invention is not necessarily limited to the above embodiment, and can be appropriately modified without departing from the gist of the present invention.
- In the above embodiment, the flow channel of the first fluid medium A in the first large block B1 and the flow channel of the first fluid medium A in the second large block B2 are symmetrically formed with reference to the reference flow channel Ra, but the present invention is not necessarily limited to this arrangement. The flow channel of the first fluid medium A in the first large block B1 and the flow channel of the first fluid medium A in the second large block B2 may be formed unsymmetrically with reference to the reference flow channel Ra. That is, the number of the
first flow channels 30, the arrangement of the intermediate reference flow channels Rb, the arrangement of the secondarybranch flow channels 36b or the like may be different from each other between the first large block B1 and the second large block B2. - The first large block B1 and the second large block B2 of the above embodiment each are sectioned into two small blocks (the first small block and the second small block) B1a, B2a, B1b and B2b with reference to the intermediate reference flow channel Rb, but there is no limitation thereto. For example, all of the
first flow channels 30 located in each of the first large block B1 and the second large block B2 may directly communicate with the first outflowcommunication flow channel 33. - In the above embodiment, the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass the three
first flow channels 30. However, the present invention is not necessarily limited thereto. For example, the first small blocks B1a and B2a and the second small blocks B1b and B2b each may encompass at least onefirst flow channel 30, and allow itself (first flow channel 30) to communicate with the first outflowcommunication flow channel 33. Alternatively, the flow channel of one system may be formed by thefirst flow channels 30 encompassed in the first small blocks B1a and B2a and the second small blocks B1b and B2b, and thefirst flow channel 30 serving as its terminal end may communicate with the first outflowcommunication flow channel 33. - The first large block B1 and the second large block B2 of the above embodiment are sectioned into the first small blocks B1a and B2a and the second small blocks B1b and B2b, only. However, the present invention is not necessarily limited thereto. For example, as shown in
Fig. 4 , the first small blocks B1a and B2a and the second small blocks B1b and B2b may be further sectioned into smaller blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2. - A more specific description is given. The first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) each are sectioned into the first small blocks B1a and B2a and the second small blocks B1b and B2b. The first small blocks B1a and B2a and the second small blocks B1b and B2b each include a plurality of the
first flow channels 30. Thefirst flow channel 30 located at an intermediate position in the first direction of the plurality offirst flow channels 30 in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction) is a branch reference flow channel Rc that serves as a branching position of the flow channel of the first fluid medium A. In association with this configuration, thebody portion 3 includes a pair of tertiarybranch flow channels 36c that provide communication between the branch reference flow channel Rc and thefirst flow channel 30 located in each of the blocks on the one side and the other side of the branch reference flow channel Rc in the first direction (hereinafter referred to as the minimal blocks) B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2. The pair of secondarybranch flow channels 36b each may communicate with the branch reference flow channel Rc located in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb in the first direction). In this case, at least onefirst flow channel 30 that is located in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and that serves as a terminal end of the flow channel of the first fluid medium A communicates with the first outflowcommunication flow channel 33. - With the above configuration, the secondary
branch flow channels 36b communicate only with the branch reference flow channel Rc (first flow channel 30) located at an intermediate position in the first direction in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b in the first large block B1 and the second large block B2. Accordingly, the secondarybranch flow channels 36b are formed to extend only up to the intermediate position in the first direction in each of the first small blocks B1a and B2a and the second small blocks B1b and B2b of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction). Thus, it is possible to suppress increase in pressure loss of the first fluid medium A in the secondarybranch flow channels 36b. - In each of the first small blocks B1a and B2a and the second small blocks B1b and B2b (blocks on the one side and the other side of the intermediate reference flow channel Rb) of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of the
body portion 3, two systems are provided as flow channels of the first fluid medium A, namely one system including the one of the pair of tertiarybranch flow channels 36c communicating with the branch reference flow channel Rc, and the other system including the other of the pair of tertiarybranch flow channels 36c communicating with the branch reference flow channel Rc. Accordingly, the length of the flow channel of the first fluid medium A from the secondarybranch flow channel 36b to the first outflow communication flow channel 33 (flow channel length per one system) becomes shortened in each of the first large block B1 and the second large block B2 (blocks on the one side and the other side of the reference flow channel Ra in the first direction) of thebody portion 3. Thus, the plate heat exchanger 1 thus configured makes it possible to suppress increase in pressure loss in the entire flow channel of the first fluid medium A and hence produce high heat exchange performance. - In this case, as shown in
Fig. 4 , two or morefirst flow channels 30 are provided in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction). Thebody portion 3 may includeconnection flow channels first flow channels 30 in the minimum blocks B1a1, B1b1, B2a1 and B2b1 on the one side with reference to the branch reference flow channel Rc (blocks on the one side of the branch reference flow channel Rc in the first direction), andconnection flow channels first flow channels 30 in the minimum blocks B1a2, B1b2, B2a2 and B2b2 on the other side with reference to the branch reference flow channel Rc (blocks on the other side of the branch reference flow channel Rc in the first direction). In association with this configuration, thefirst flow channel 30 that is located in each of the blocks thus sectioned with reference to the branch reference flow channel Rc, namely the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and that serves as a terminal end of the flow channel of the first fluid medium A, communicates with the first outflowcommunication flow channel 33. With this configuration, it is possible to increase the heat transfer area without extending the length of the flow channel of the first fluid medium A. - Separately from the above, one
first flow channel 30 may be provided in each of the minimum blocks B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, and B2b2 (blocks on the one side and the other side of the branch reference flow channel Rc in the first direction), and may communicate with the first outflowcommunication flow channel 33. With this configuration, it is possible to suppress pressure loss in the flow channel of the first fluid medium A. - In the above embodiment, the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass three
first flow channels 30, and thesefirst flow channels 30 sequentially communicate with each other to allow the flow channel of the first fluid medium A to be formed in serpentine manner, but there is no limitation thereto. For example, it may be configured such that the first small blocks B1a and B2a and the second small blocks B1b and B2b each encompass a plurality offirst flow channels 30, and all of the plurality of thefirst flow channels 30 communicate with the secondarybranch flow channels 36b and the first outflowcommunication flow channel 33. In this way, the first fluid medium A flows from the secondarybranch flow channels 36b into the plurality of thefirst flow channels 30, then circulates in the plurality of thefirst flow channels 30, and then flows out of the first outflowcommunication flow channel 33. In such a way in which the first fluid medium A is circulated in the plurality of thefirst flow channels 30, a large heat transfer area can be secured without extending the length of the flow channel of the first fluid medium A, and a high heat exchange can be achieved. - In the above embodiment, the flow channel of the first fluid medium A in each of the first large block B1 and the second large block B2 is subsequently branched off at the intermediate reference flow channel Rb and the branch reference flow channel Rc as branching positions. However, the present invention is not necessarily limited thereto. For example, it may be configured such that the primary
branch flow channels 36a communicate with the plurality of thefirst flow channels 30 located in each of the first large block B1 and the second large block B2, and the plurality of thefirst flow channels 30 located in each of the first large block B1 and the second large block B2 directly communicate with the first outflowcommunication flow channel 33. Even in such a way, since the firstcommunication flow channel 32 extends up to the intermediate position from the one end of thebody portion 3, the length of the flow channel of the firstcommunication flow channel 32 is not increased, and hence it is possible to suppress increase in pressure loss of the first fluid medium A. - The
body portion 3 of the above embodiment includes a pair of primarybranch flow channels 36a, but there is no limitation thereto. Thebody portion 3 may include two or more pairs of primarybranch flow channels 36a. That is, thebody portion 3 may include at least a pair of primarybranch flow channels 36a. - In this case, the second pair of primary
branch flow channels 36a each communicate only with thefirst flow channel 30 located in an area (second area) outside, with reference to the reference flow channel Ra, of the area (first area) in which the flow channel of the first fluid medium A with the first pair of primarybranch flow channels 36a serving as a starting point is located. A plurality of thefirst flow channels 30, which serve as a terminal end of the flow channel of the first fluid medium A with the primarybranch flow channel 36a (one of the second pair of the primarybranch flow channels 36a) serving as a starting point on the one side of the reference flow channel Ra in the first direction, and a plurality of thefirst flow channels 30, which serve as a terminal end of the flow channel of the first fluid medium A with the primarybranch flow channel 36a (the other of the second pair of the primarybranch flow channels 36a) serving as a starting point on the other side of the reference flow channel Ra in the first direction communicate with the first outflowcommunication flow channel 33. - That is, it may be configured such that the nth pair of primary
branch flow channels 36a communicate only with thefirst flow channels 30 located in an area (the nth area) outside of the nth - 1 area of thebody portion 3, and the flow channel of the first fluid medium A with the nth pair of primarybranch flow channels 36a serving as a starting point is located in the nth area, in which n is natural number. - In the above embodiment, the plurality of the
second flow channels 31 each communicate with the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35, and the flow channel of the second fluid medium B that connects the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35 is formed to be straight, but there is no limitation thereto. For example, the flow channel of the second fluid medium B that connects the second inflowcommunication flow channel 34 and the second outflowcommunication flow channel 35 may be formed in serpentine manner in the same manner as the flow channel of the first fluid medium A. That is, the flow channel of the second fluid medium B may be branched off at least at one place on each of the one side and the other side of thebody portion 3 in the first direction, in the same manner as the flow channel of the first fluid medium A, and the second outflowcommunication flow channel 35 may communicate only with thesecond flow channel 31 that is located on each of the one side and the other side in the first direction in thebody portion 3, and that is a terminal end of the flow channel of the second fluid medium B. Also, in this case, it may be configured such that a flow channel which serves as a branching position of the flow channel of the second fluid medium B is provided, and thebody portion 3 is sectioned into small blocks with reference to this flow channel so that the circulation route of the second fluid medium B may be branched off at least at two places. -
- 1
- Plate Heat Exchanger
- 2
- Heat Transfer Plate
- 3
- Body Portion
- 4
- First End Plate (End Plate)
- 5
- Second End Plate (End Plate)
- 20
- Heat Transfer Portion
- 21
- Fitting Portion
- 30
- First Flow channel
- 31
- Second Flow channel
- 32
- First Inflow Communication flow channel (One First Communication flow channel)
- 33
- First Outflow Communication flow channel (Another First Communication flow channel)
- 34
- Second Inflow Communication flow channel (One Second Communication flow channel)
- 35
- Second Outflow Communication flow channel (Another Second Communication flow channel)
- 36a
- Primary Branch Flow channel
- 36b
- Secondary Branch Flow channel
- 36c
- Tertiary Branch Flow channel
- 37a
- First Connection Flow channel (Connection Flow channel)
- 37b
- Second Connection Flow channel (Connection Flow channel)
- 37c
- Connection Flow channel
- 40, 50
- Sealing Portion
- 41, 51
- Fitting Portion
- A
- First Fluid medium
- B
- Second Fluid medium
- B1
- First Large Block (Block)
- B2
- Second Large Block (Block)
- B1a, B2a
- First Small Block (Block)
- B1b, B2b
- Second Small Block (Block)
- B1a, B2a
- First Small Block (Block)
- B1a1, B1a2, B1b1, B1b2, B2a1, B2a2, B2b1, B2b2
- Minimum Block (Block)
- Ra
- Reference Flow channel
- Rb
- Intermediate Reference Flow channel
- Rc
- Branch Reference Flow channel
Claims (6)
- A plate heat exchanger comprising a body portion that includes a plurality of heat transfer plates stacked on each other, the body portion further including a plurality of first flow channels that circulate a first fluid medium, a plurality of second flow channels that circulate a second fluid medium, a pair of first communication flow channels that communicate with the plurality of the first flow channels and allow the first fluid medium to flow into and out of the plurality of the first flow channels, a pair of second communication flow channels that communicate with the plurality of the second flow channels and allow the second fluid medium to flow into and out of the plurality of the second flow channels, the plurality of the first flow channels and the plurality of the second flow channels being alternately formed with the plurality of the heat transfer plates being respectively interposed therebetween, and the pair of first communication flow channels and the pair of second communication flow channels extending in the stacked direction of the plurality of the heat transfer plates through the plurality of the heat transfer plates,
wherein the plurality of the first flow channels communicate with each other to form a flow channel of the first fluid medium from one of the pair of first communication flow channels to the other of the pair of first communication flow channels,
wherein at least one of the plurality of the first flow channels located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a reference flow channel that serves as a branching position of the flow channel of the first fluid medium,
wherein the body portion includes at least one pair of primary branch flow channels that provide communication between the reference flow channel and at least one first flow channel located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates,
wherein the one of the pair of first communication flow channels communicates only with the reference flow channel, and
wherein the other of the pair of first communication flow channels communicates only with the first flow channel that is located on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium. - The plate heat exchanger according to claim 1, wherein three or more fist flow channels are provided on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates,
wherein, of the three or more first flow channels provided on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is an intermediate reference flow channel that serves as a branching position of the flow channel of the first fluid medium,
wherein the body portion includes a pair of secondary branch flow channels that each provide communication between the corresponding intermediate reference flow channel and at least one first flow channel located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, and
wherein the pair of primary branch flow channels respectively communicate with the corresponding intermediate reference flow channels located respectively on the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates. - The plate heat exchanger according to claim 2, wherein two or more first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates,
wherein the body portion includes a connection flow channel that connects the two or more first flow channels with each other on the one side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, and a connection flow channel that connects the two or more first flow channels with each other on the other side of the intermediate reference flow channel in the stacked direction of the plurality of heat transfer plates, on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of the heat transfer plates, and
wherein at least one first flow channel that is located on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves a terminal end of the flow channel of the first fluid medium, communicates the other of the pair of first communication flow channels. - The plate heat exchanger according to claim 2, wherein a plurality of the first flow channels are provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates on each of the one side and the other side of the reference flow channel in the stacked direction of the plurality of heat transfer plates,
wherein, of the plurality of the first flow channels provided on each of the one side and the other side of the intermediate reference flow channel in the stacked direction of the plurality of the heat transfer plates, the first flow channel located at an intermediate position in the stacked direction of the plurality of the heat transfer plates is a branch reference flow channel that serves as a branching position of the flow channel of the first fluid medium,
wherein the body portion includes a pair of tertiary branch flow channels that provide communication between the branch reference flow channel and the first flow channel located on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates,
wherein the pair of secondary branch flow channels respectively communicate with the branch reference flow channels located respectively on the one side and the other side of the intermediate reference flow channel in the stacked direction of the heat transfer plates, and
wherein at least one first flow channel that is located on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates with the other of the pair of first communication flow channels. - The plate heat exchanger according to claim 4, wherein one first flow channel is provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and communicates with the other of the pair of first communication flow channels.
- The plate heat exchanger according to claim 4, wherein two or more first flow channels are provided on each of the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates,
wherein the body portion includes a connection flow channel that connects the two or more first flow channels located on the one side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and a connection flow channel that connects the two or more first flow channels located on the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and
wherein at least one first flow channel that is located on the one side and the other side of the branch reference flow channel in the stacked direction of the plurality of the heat transfer plates, and that serves as a terminal end of the flow channel of the first fluid medium, communicates with the other of the pair of first communication flow channels.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2013074896 | 2013-03-29 | ||
PCT/JP2013/082583 WO2014155839A1 (en) | 2013-03-29 | 2013-12-04 | Plate-type heat exchanger |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2980521A1 true EP2980521A1 (en) | 2016-02-03 |
EP2980521A4 EP2980521A4 (en) | 2016-11-23 |
EP2980521B1 EP2980521B1 (en) | 2019-03-13 |
Family
ID=51622874
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP13880645.0A Active EP2980521B1 (en) | 2013-03-29 | 2013-12-04 | Plate-type heat exchanger |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2980521B1 (en) |
JP (1) | JP5818397B2 (en) |
CN (1) | CN105008843B (en) |
WO (1) | WO2014155839A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014155838A1 (en) * | 2013-03-29 | 2014-10-02 | 株式会社日阪製作所 | Plate-type heat exchanger |
US20190011193A1 (en) * | 2016-01-13 | 2019-01-10 | Hisaka Works, Ltd. | Plate heat exchanger |
JP7300500B2 (en) * | 2019-04-23 | 2023-06-29 | 株式会社日阪製作所 | plate heat exchanger |
JP2020186834A (en) * | 2019-05-13 | 2020-11-19 | パナソニックIpマネジメント株式会社 | Heat exchanger, and air conditioner using the same |
EP4199325A1 (en) * | 2021-12-15 | 2023-06-21 | Siemens Aktiengesellschaft | Attachment radiator of a dynamoelectric machine with plate coolers |
CN217387293U (en) * | 2022-04-29 | 2022-09-06 | 比亚迪股份有限公司 | Radiator assembly, battery package and vehicle |
KR102689592B1 (en) * | 2022-05-03 | 2024-07-31 | 한국가스공사 | Gas heater for plate type high frequency induction heating |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3106243A (en) * | 1957-11-29 | 1963-10-08 | Danske Mejeriers Maskinfabrik | Plate for holding section in a plate heat exchanger |
JP2992606B2 (en) * | 1991-12-24 | 1999-12-20 | 株式会社日阪製作所 | Plate heat exchanger |
DK9300044U4 (en) * | 1993-01-21 | 1994-05-27 | Tarm H S As | Plate heat exchanger and heat exchanger system with plate heat exchanger |
JPH10288480A (en) * | 1997-04-15 | 1998-10-27 | Daikin Ind Ltd | Plate type heat-exchanger |
JPH11287572A (en) | 1998-03-31 | 1999-10-19 | Hisaka Works Ltd | Brazing plate type heat exchanger |
US7241423B2 (en) * | 2000-02-03 | 2007-07-10 | Cellular Process Chemistry, Inc. | Enhancing fluid flow in a stacked plate microreactor |
JP2002267289A (en) * | 2001-03-09 | 2002-09-18 | Sanyo Electric Co Ltd | Plate heat exchanger |
US6717175B2 (en) * | 2001-09-27 | 2004-04-06 | The Furukawa Electric Co., Ltd. | Semiconductor laser device and method for manufacturing the same |
DE102005031026B3 (en) * | 2005-07-02 | 2007-04-12 | Danfoss A/S | heat exchangers |
JP5100860B2 (en) * | 2011-04-27 | 2012-12-19 | 株式会社日阪製作所 | Plate heat exchanger |
-
2013
- 2013-12-04 WO PCT/JP2013/082583 patent/WO2014155839A1/en active Application Filing
- 2013-12-04 JP JP2015507956A patent/JP5818397B2/en not_active Expired - Fee Related
- 2013-12-04 EP EP13880645.0A patent/EP2980521B1/en active Active
- 2013-12-04 CN CN201380073887.0A patent/CN105008843B/en active Active
Also Published As
Publication number | Publication date |
---|---|
EP2980521A4 (en) | 2016-11-23 |
CN105008843B (en) | 2017-05-17 |
CN105008843A (en) | 2015-10-28 |
EP2980521B1 (en) | 2019-03-13 |
WO2014155839A1 (en) | 2014-10-02 |
JPWO2014155839A1 (en) | 2017-02-16 |
JP5818397B2 (en) | 2015-11-18 |
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