EP2980521A1 - Plattenwärmetauscher - Google Patents

Plattenwärmetauscher Download PDF

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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
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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
Application number
EP13880645.0A
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English (en)
French (fr)
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EP2980521A4 (de
EP2980521B1 (de
Inventor
Nobuo Tanaka
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Hisaka Works Ltd
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Hisaka Works Ltd
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Publication of EP2980521A1 publication Critical patent/EP2980521A1/de
Publication of EP2980521A4 publication Critical patent/EP2980521A4/de
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Publication of EP2980521B1 publication Critical patent/EP2980521B1/de
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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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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
EP13880645.0A 2013-03-29 2013-12-04 Plattenwärmetauscher Active EP2980521B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2013074896 2013-03-29
PCT/JP2013/082583 WO2014155839A1 (ja) 2013-03-29 2013-12-04 プレート式熱交換器

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EP2980521A1 true EP2980521A1 (de) 2016-02-03
EP2980521A4 EP2980521A4 (de) 2016-11-23
EP2980521B1 EP2980521B1 (de) 2019-03-13

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JP5918904B2 (ja) * 2013-03-29 2016-05-18 株式会社日阪製作所 プレート式熱交換器
US20190011193A1 (en) * 2016-01-13 2019-01-10 Hisaka Works, Ltd. Plate heat exchanger
CN113424010B (zh) * 2019-04-23 2023-07-18 株式会社日阪制作所 板式热交换器
EP4199325A1 (de) * 2021-12-15 2023-06-21 Siemens Aktiengesellschaft Aufsatzkühler einer dynamoelektrischen maschine mit plattenkühlern
CN217387293U (zh) * 2022-04-29 2022-09-06 比亚迪股份有限公司 散热器总成、电池包和车辆

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US3106243A (en) * 1957-11-29 1963-10-08 Danske Mejeriers Maskinfabrik Plate for holding section in a plate heat exchanger
JP2992606B2 (ja) * 1991-12-24 1999-12-20 株式会社日阪製作所 プレート式熱交換器
DK9300044U4 (da) * 1993-01-21 1994-05-27 Tarm H S As Pladevarmeveksler og varmevekslersystem med pladevarmeveksler
JPH10288480A (ja) * 1997-04-15 1998-10-27 Daikin Ind Ltd プレート式熱交換器
JPH11287572A (ja) 1998-03-31 1999-10-19 Hisaka Works Ltd ブレージングプレート式熱交換器
US7241423B2 (en) * 2000-02-03 2007-07-10 Cellular Process Chemistry, Inc. Enhancing fluid flow in a stacked plate microreactor
JP2002267289A (ja) * 2001-03-09 2002-09-18 Sanyo Electric Co Ltd プレート熱交換器
US6717175B2 (en) * 2001-09-27 2004-04-06 The Furukawa Electric Co., Ltd. Semiconductor laser device and method for manufacturing the same
DE102005031026B3 (de) * 2005-07-02 2007-04-12 Danfoss A/S Wärmetauscher
JP5100860B2 (ja) * 2011-04-27 2012-12-19 株式会社日阪製作所 プレート式熱交換器

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EP2980521A4 (de) 2016-11-23
JPWO2014155839A1 (ja) 2017-02-16
CN105008843A (zh) 2015-10-28
WO2014155839A1 (ja) 2014-10-02
CN105008843B (zh) 2017-05-17
JP5818397B2 (ja) 2015-11-18
EP2980521B1 (de) 2019-03-13

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