CROSS-REFERENCE TO RELATED APPLICATION
[0001] This application claims priority to Japanese Patent Application No.
2013-74896, the disclosure of which is incorporated herein by reference in its entirety.
FIELD OF THE INVENTION
[0002] The present invention relates to a plate heat exchanger that is used as an evaporator
and a condenser.
BACKGROUND ART
[0003] 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).
[0004] As shown in Fig. 5, 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.
[0005] 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 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. Whereby, 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).
[0006] 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 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. As described above, in the plate
heat exchanger 1, the first fluid medium A circulates in the first flow channels 30,
and the second fluid medium B circulates in the second 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 each heat
transfer plate 2 separating the first flow channel 30 and the second flow channel
31.
[0007] 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.
[0008] However, as the number of the heat transfer plates 2 increases, 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.
[0009] That is, 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.
[0010] 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 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).
CITATION LIST
Patent Literature
SUMMARY OF THE INVENTION
PROBLEMS TO BE SOLVED BY THE INVENTION
[0012] 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.
[0013] 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.
[0014] 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.
[0015] 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.
[0016] 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.
[0017] 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.
[0018] 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.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019]
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.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0020] A description is given for a plate heat exchanger according to one embodiment of
the present invention with reference to the attached drawings.
[0021] As shown in Fig. 1, the plate heat exchanger includes a body portion 3 that includes
a plurality of heat transfer plates 2 stacked on each other.
[0022] As shown in Fig. 2 and Fig. 3, 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. In the following description,
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." Also, 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."
[0023] The first flow channels 30 and the second flow channels 31 are alternately formed
with the heat transfer plates 2 respectively interposed therebetween. On the other
hand, 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").
[0024] 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 the heat
transfer plates 2 stacked on each other, and a pair of end plates 4 and 5 that sandwich
the body portion 3.
[0025] 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.
[0026] 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.
[0027] 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.
In the present embodiment, detailed description is given for 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.
[0028] 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. Specifically,
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.
[0029] 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. Along with this configuration, 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.
[0030] 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, 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.
[0031] 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.
[0032] 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). In this state, 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.
[0033] With the above configuration, as shown in Fig. 2 and Fig. 3, the first flow channels
30 and the second flow channels 31 are alternately formed with the heat transfer plates
2 respectively therebetween. In the present embodiment, 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.
[0034] 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.
[0035] A more specific description is given herein. In the present embodiment, the heat
transfer portion 20 of 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).
[0036] 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.
[0037] 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). However, according to the actual arrangement,
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).
[0038] 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 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.
[0039] 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 first communication flow channel 32 to the first outflow communication
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
the first flow channels 30 on both ends in the first direction.
[0040] 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.
[0041] In the present embodiment, 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.
[0042] The plurality of the first flow channels 30 of the body portion 3 are grouped into
two or more blocks B1 and B2. In the body 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 the body 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").
[0043] 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 more first flow channels 30.
[0044] 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.
[0045] 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.
[0046] 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, 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. That is, 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.
[0047] 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
three first flow channels 30.
[0048] In association with the above configuration, 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.
[0049] 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 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
[0050] (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.
[0051] As described above, 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. Also, 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. 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 innermost first flow channel 30, the
first connection flow channel 37a, the intermediate first flow channel 30, the second
connection flow channel 37b, and the outermost first flow channel 30.
[0052] 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.
[0053] 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 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.
[0054] 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 outflow communication
flow channel 33.
[0055] Contrary to the above, 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.
[0056] 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 outflow communication flow channel 33.
On the other hand, 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.
[0057] 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.
[0058] 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. 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.
[0059] 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 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.
[0060] 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.
[0061] 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 outflow communication 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.
[0062] 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, 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).
[0063] 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 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. 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, 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.
[0064] 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. 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. Whereby, the heat transmission area can
be increased without increase in length of the flow channel of the first fluid medium
A.
[0065] 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.
[0066] 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 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.
[0067] 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 outflow communication flow channel 33.
[0068] 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 one
first flow channel 30, and allow itself (first flow channel 30) to communicate with
the first outflow communication flow channel 33. Alternatively, 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.
[0069] 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.
[0070] 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. 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. In association with this configuration, 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). In this case, 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.
[0071] 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 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.
[0072] 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 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. Accordingly, 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 (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 the body 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.
[0073] In this case, as shown in Fig. 4, 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). In association with this configuration, 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. 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.
[0074] 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 outflow communication flow channel 33. With this
configuration, it is possible to suppress pressure loss in the flow channel of the
first fluid medium A.
[0075] 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 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. 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 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. In this way, 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. In such a way in which the first fluid medium A is circulated in
the plurality of the first 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.
[0076] 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 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.
Even in such a way, since 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.
[0077] 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.
[0078] In this case, 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. A plurality of the first flow
channels 30, which serve as a terminal end of the flow channel of the first fluid
medium A with the primary branch flow channel 36a (one of the second pair of the primary
branch 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 the first flow channels
30, which serve as a terminal end of the flow channel of the first fluid medium A
with the primary branch flow channel 36a (the other of the second pair of the primary
branch 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 outflow communication
flow channel 33.
[0079] That is, it may be configured such that the 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.
[0080] In the above embodiment, 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. For example,
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. 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 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. 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 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.
REFERENCE SIGNS LIST
[0081]
- 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