TECHNICAL FIELD
[0001] The present disclosure relates to a stack-type plate fin heat exchanger.
BACKGROUND ART
[0002] PTL 1 discloses a conventional stack-type plate fin heat exchanger. As shown in Figs.
7 and 8, this stack-type plate fin heat exchanger includes plate fin stacked body
102 in which plate fins 101 having flow channels through which a first fluid such
as a refrigerant flows are stacked, end plates 103 stacked and disposed on both sides
of plate fin stacked body 102, and inlet and outlet pipes 104 and 105 into which the
first fluid flowing through the flow channels of plate fin stacked body 102 flows
or from which the first fluid flows out. A second fluid flows between layers of plate
fins 101 of plate fin stacked body 102 to allow heat to be exchanged between the first
fluid and the second fluid. Through-holes 107 are provided at appropriate positions
on a peripheral edge of header region 106 being an inlet and outlet portion of the
channel of the first fluid in plate fin stacked body 102. By passing bolts 109 through
through-holes 107 with reinforcing plate 108 interposed therebetween, portions of
the header regions of plate fins 101 are connected and fixed together.
Citation List
Patent Literature
SUMMARY OF THE INVENTION
[0004] The present disclosure provides a stack-type plate fin heat exchanger in which a
configuration of coupling and fixing portions of header regions of plate fins is simplified,
and deformation of the plate fins due to insufficient coupling and fixing strength
is suppressed.
[0005] The stack-type plate fin heat exchanger according to the present disclosure includes
tubular parts provided at appropriate positions on peripheral edges of the header
region of the plate fin. The tubular parts of the adjacent plate fins are fitted to
each other to cause the header regions of the plate fins to be coupled and fixed.
BRIEF DESCRIPTION OF THE DRAWINGS
[0006]
Fig. 1 is a perspective view showing an external appearance of a stack-type plate
fin heat exchanger according to a first exemplary embodiment.
Fig. 2 is an enlarged perspective view showing header regions of the heat exchanger.
Fig. 3 is an enlarged sectional view showing the header regions of the heat exchanger.
Fig. 4 is an enlarged sectional view showing a main part of the header regions of
the heat exchanger.
Fig. 5 is an enlarged sectional view of a portion indicated by A in Fig. 4.
Fig. 6 is an exploded perspective view of plate fins of the heat exchanger according
to the first exemplary embodiment.
Fig. 7 is a perspective view of a conventional stack-type plate fin heat exchanger.
Fig. 8 is a perspective view showing the conventional stack-type plate fin heat exchanger
in a state before the header regions are coupled and fixed together.
DESCRIPTION OF EMBODIMENT
(Knowledge and the like underlying the present disclosure)
[0007] The stack-type plate fin heat exchanger described in Patent Literature 1 is a heat
exchanger proposed by the inventors of the present invention. At the time when the
inventors arrived at the present disclosure, in the heat exchanger described in Patent
Literature 1, because header regions 106 where the first fluid such as the refrigerant
flowing through the flow channel gathers are easily deformed by the pressure of the
first fluid, reinforcing plate 108 is placed on the outer surface of header regions
106, and the portions of header regions 106 are coupled and fixed together by bolts
109. As a result of intensive studies by the inventors, it has been found that because
reinforcing plate 108, the bolts 109, and the like are required in the conventional
configuration, there is a problem that the configuration is complicated, the weight
of the entire heat exchanger increases, and assembling work for reinforcing plate
108 and bolts 109 is required, and productivity decreases.
[0008] In view of these problems, the inventors of the present disclosure have made the
subject matter of the present disclosure to solve the problems.
[0009] The present disclosure provides a heat exchanger in which a configuration of coupling
and fixing portions of header regions of plate fins is simplified and deformation
of the plate fins in the portions of the header regions is suppressed to improve reliability.
[0010] Hereinafter, an exemplary embodiment is described in detail with reference to the
accompanying drawings. It is noted that a more detailed description than needed may
be omitted. For example, detailed description of already well-known matters and repeated
description of substantially the same configuration are omitted in some cases. This
is to avoid an unnecessary redundancy in the following description and to facilitate
understanding by those skilled in the art.
[0011] Note that the heat exchanger according to the present disclosure is not limited to
configurations of a stack-type plate fin heat exchanger described in the following
exemplary embodiment, but includes configurations of heat exchangers equivalent to
a technical idea described in the following exemplary embodiment.
[0012] The exemplary embodiment described below shows an example of the present disclosure,
and configurations, functions, and operations described in the present exemplary embodiment
are mere examples and do not limit the present disclosure.
(First exemplary embodiment)
[0013] Hereinafter, the heat exchanger according to a first exemplary embodiment of the
present disclosure is described with reference to Figs. 1 to 6.
[1-1. Configuration]
[0014] Fig. 1 is a perspective view showing an appearance of stack-type plate fin heat exchanger
(hereinafter, simply referred to as heat exchanger) 1 according to the first exemplary
embodiment, Fig. 2 is an enlarged perspective view showing header regions of the stack-type
plate fin heat exchanger, Fig. 3 is an enlarged sectional view showing the header
regions of the stack-type plate fin heat exchanger, Fig. 4 is an enlarged sectional
view showing a main part of the header regions of the stack-type plate fin heat exchanger,
Fig. 5 is an enlarged sectional view of a portion indicated by A in Fig. 4, and Fig.
6 is an exploded perspective view of plate fins of the stack-type plate fin heat exchanger
according to the first exemplary embodiment.
[0015] As shown in Figs. 1 to 6, heat exchanger 1 according to the present exemplary embodiment
includes inlet pipe (inlet port header) 2, plate fin stacked body 4 including a plurality
of plate fins 3 that are stacked together, and outlet pipe (outlet port header) 5
allowing the refrigerant having flown through flow channels provided in plate fins
3 to be discharged. The refrigerant as the first fluid flows into the inlet pipe (inlet
port header) 2. In the example of the present exemplary embodiment, the plurality
of plate fins 3 each have a rectangular plate shape.
[0016] End plates 6a and 6b are respectively provided on both sides (upper side and lower
side in Fig. 1) in the stacking direction of plate fin stacked body 4. The shape of
end plates 6a and 6b and the shape of plate fins 3 are substantially the same in plan
view. End plates 6a and 6b are each made of a plate material having rigidity, and
are formed by, for example, grinding and machining metal material, such as aluminum,
an aluminum alloy, or stainless steel.
[0017] Note that end plates 6a and 6b and the plurality of plate fins 3 are stacked and
joined integrally by brazing. End plates 6a and 6b and the plurality of plate fins
3 may be joined by other heat-resistant fixing methods such as a method using a chemical
joining member.
[0018] Further, in the present exemplary embodiment, in plate fin stacked body 4 formed
by stacking plate fins 3, plate fins 3 are coupled and fixed at both ends in the longitudinal
direction of plate fin stacked body 4. A configuration of coupling and fixing plate
fin stacked body 4 is described later.
[0019] Note that, as shown in Fig. 6, plate fin 3 is formed by joining a pair of long plates
3a and 3b by brazing. The pair of plates 3a and 3b has a recessed groove serving as
flow channel 7. By joining the pair of plates 3a and 3b, inlet header flow channel
9 and outlet header flow channel 10 connected to flow channel 7 via communication
channel 8 are formed. Flow channel 7 provided in plates 3a and 3b are disposed along
the longitudinal direction of plates 3a and 3b. Flow channel 7 is configured to make
a U-turn at the ends of plates 3a and 3b. On one end side of plates 3a and 3b, inlet
header flow channel 9 connected to outgoing flow channel 7a and outlet header flow
channel 10 connected to return flow channel 7b are collectively disposed. Slit 11
that suppresses heat transfer between the first fluid flowing through outgoing flow
channel 7a and the first fluid flowing through return flow channel 7b is disposed
between outgoing flow channel 7a and return flow channel 7b. As described above, plate
fins 3 are stacked together with end plates 6a and 6b and brazed to form plate fin
stacked body 4. Each of inlet pipe 2 and outlet pipe 5 are connected to a corresponding
one of inlet header flow channel 9 and outlet header flow channel 10 of plate fin
stacked body 4.
[0020] Next, a configuration for coupling and fixing both ends of plate fin stacked body
4 is described. In plate fin 3 of the present exemplary embodiment, through-holes
12 are provided in a peripheral edge of header region X where inlet header flow channel
9 and outlet header flow channel 10 of plate fin 3 are located (see, for example,
Figs. 3 and 6). As shown in Fig. 6, tubular part 13 is disposed in an erected manner
in a portion of each of the pair of plates 3a and 3b provided with through-hole 12.
In other words, through-hole 12 is disposed inside the wall surface constituting tubular
part 13. Tubular parts 13 are disposed protruding outward from each of the pair of
plates 3a and 3b. As shown in Figs. 4 and 5, tubular part 13 is fitted to tubular
part 13 of another plate fin 3 adjacent in the stacking direction. By brazing tubular
parts 13 of adjacent plate fins 3 to each other, header regions X (see Fig. 1 and
others) of adjacent plate fins 3 are coupled and fixed to each other. Tubular part
13 is disposed protrudingly on the surface opposite to the brazed surface of the plates
3a and 3b to which brazing material is applied in advance. By fitting tubular parts
13 of adjacent plate fins 3 to each other and causing the brazing material to be melted
and solidified on the brazed surface on the inner peripheral surface of any one of
tubular parts 13 to integrate tubular parts 13 to each other, header regions X of
plate fin stacked body 4 formed by stacking the plurality of plate fins 3 are coupled
and fixed together.
[0021] Although not illustrated, similar through-holes 12 are also provided and tubular
parts 13 are disposed at the end of each plate fin 3 on the side opposite to header
region X. By fitting and brazing tubular parts 13 to each other, the ends of plate
fin stacked body 4 formed by stacking plate fins 3 are coupled and fixed together.
[0022] As shown in Fig. 6, tubular parts 13 each erected on through-hole 12 are disposed
surrounding inlet header flow channel 9 and outlet header flow channel 10. In the
example shown in Fig. 6, each of tubular parts 13 is provided on a line connecting
the approximate centers of inlet header flow channel 9 and outlet header flow channel
10. Specifically, tubular part 13 is provided to overlap, in at least a part of the
outer periphery of tubular part 13, on a line connecting the approximate centers of
outlet header flow channel 10 and outlet header flow channel 10. A fitting clearance
between tubular parts 13 of adjacent plate fins 3 is less than or equal to 0.2 mm,
preferably 0.2 mm to 0.1 mm.
[0023] Note that, in the example of the present exemplary embodiment, at least one tubular
part 13 among tubular parts 13 to be fitted to each other, that is, in the example
shown in Fig. 6, tubular part 13 of upper plate 3a among the pair of plates 3a and
3b has a tapered shape.
[1-2. Operation]
[0024] Functional effect of heat exchanger 1 configured as described above is described
below.
[0025] When heat exchanger 1 according to the present exemplary embodiment is, for example,
incorporated into a refrigeration system and used under evaporation conditions, the
refrigerant in a gas-liquid two-phase state that is the first fluid flows from inlet
pipe 2 into inlet header flow channel 9 of plate fin stacked body 4. The refrigerant
having flowed into inlet header flow channel 9 flows to a group of outgoing flow channels
7a through communication channels 8 of plate fins 3. The refrigerant having flowed
to the group of outgoing flow channels 7a of each plate fin 3 makes a U-turn and flows
from outlet pipe 5 in a gas state to the refrigerant circuit of the refrigeration
system through return flow channel 7b. While flowing through outgoing flow channel
7a, the refrigerant exchanges heat with the air (second fluid) passing between plate
fins 3 of plate fin stacked body 4.
[0026] At this time, because heat transfer between the refrigerant flowing through the group
of outgoing flow channels 7a and the refrigerant flowing through return flow channel
7b is suppressed by slit 11, high heat exchange efficiency is exhibited. In the case
where heat exchanger 1 is used as a condenser, the flow of the first fluid is opposite
to that when the heat exchanger 1 is used as an evaporator. That is, inlet pipe 2
and inlet header flow channel 9 respectively serve as an outlet pipe and an outlet
header flow channel, and outlet pipe 5 and outlet header flow channel 10 respectively
serve as an inlet pipe and an inlet header flow channel.
[0027] In heat exchanger 1, because the opening area of inlet header flow channel 9 is larger
than the opening areas of other flow channels, stress concentrates on the portion
of header regions X where inlet header flow channel 9 is disposed, and the portions
of the header regions X tend to be greatly deformed in the stacking direction. However,
in heat exchanger 1 according to the present exemplary embodiment, because the portions
of header regions X are firmly coupled and fixed together, deformation of the portions
of header regions X is suppressed, and thus heat exchanger 1 according to the present
exemplary embodiment can be a highly reliable heat exchanger.
[0028] More specifically, in heat exchanger 1 of the present exemplary embodiment, tubular
parts 13 are provided in header region X of each of plates 3a and 3b constituting
plate fin 3. Tubular parts 13 of adjacent plate fins 3 are fitted and brazed to each
other. The header regions X of adjacent plate fins 3 are thus coupled and fixed together
[0029] Therefore, tabular parts 13 of adjacent plate fins 3 are fitted to each other, and
tubular parts 13 are connected in a columnar shape in the stacking direction. Further,
because tubular parts 13 are joined to each other by brazing material, the joining
strength is further increased by the solidified brazing material, and a more robust
fixing structure is obtained. Therefore, the coupling strength of the portions of
the header regions is greatly improved, the rigidity of the plate fin stacked body
is improved, and a highly reliable heat exchanger can be obtained.
[0030] In addition, because a reinforcing plate, bolts, and the like for securing the coupling
strength at the portions of the header regions as in the conventional art are not
required, the configuration can be simplified as compared with the conventional heat
exchanger using the reinforcing plate, the bolts, and the like.
[0031] In addition, because workability at the time of manufacturing the heat exchanger
is improved, productivity can be improved. That is, according to the configuration
of the present exemplary embodiment, header regions X can be coupled and fixed together
by just inserting a guide-pin jig into through-hole 12, stacking and directly putting
plates 3a and 3b in a melting furnace, and brazing plates 3a and 3b. The number of
man-hours can be reduced, the man-hours being required in the conventional configuration
to assemble using the reinforcing plate and the bolts separately from the brazing
work, and as a result, the workability at the time of manufacturing is greatly improved.
Therefore, productivity of the heat exchanger is greatly improved.
[0032] In the heat exchanger of the present exemplary embodiment, tubular parts 13 are disposed
surrounding each of inlet header flow channel 9 and outlet header flow channel 10.
Therefore, even when a large amount of the first fluid flows in a concentrated manner
to cause a high pressure to be applied around inlet header flow channel 9 and outlet
header flow channel 10 of each of plates 3a and 3b, that is, at the portion of header
region X, the pressure resistance around inlet header flow channel 9 and the pressure
resistance around outlet header flow channel 10 can respectively be substantially
uniformly improved to enhance the pressure resistance of the entire portion of header
region X. In the example of the present exemplary embodiment, each tubular part 13
is provided such that at least a part of the outer periphery of tubular part 13 overlaps
on the line connecting the approximate centers of inlet header flow channel 9 and
outlet header flow channel 10. Therefore, the portions of header regions X are coupled
together by tubular parts 13 in the vicinity of the line connecting the substantial
centers of the inlet header flow channel 9 and outlet header flow channel 10, and
the pressure resistance of the portions of header regions X can be more uniformly
and reliably improved to prevent deformation of plate fin 3.
[0033] In the example of the present exemplary embodiment, at least one of tubular parts
13 provided in the pair of plates 3a and 3b is tapered. As a result, even if there
is a dimensional tolerance in tubular parts 13 fitted to each other, tubular parts
13 reliably come into contact with each other at least at a part thereof, and thus
tubular parts 13 can be reliably fixed to each other with the brazing material. Therefore,
the coupling strength of the portions of header regions X becomes strong, and the
pressure resistance can be more reliably improved.
[0034] In addition, the fitting clearance between tubular parts 13 to be fitted is set to
less than or equal to 0.2 mm, and in the example of the present exemplary embodiment,
is set to be in the range of 0.2 mm to 0.1 mm. As a result, in between tubular parts
13, the melted brazing material substantially uniformly goes around the entire circumference
of tubular parts 13 and is solidified. Therefore, the strength of a joint between
tubular parts 13 including the brazing material is reliably improved, and the pressure
resistance of the portions of header regions X can be further reliably improved.
[Other exemplary embodiments]
[0035] As described above, the first exemplary embodiment has been described as an example
of the techniques in the present disclosure. However, the technique in the present
disclosure is not limited thereto, and can also be applied to exemplary embodiments
subjected to alteration, substitution, addition, omission and the like. In addition,
new exemplary embodiments can be made by combining constituent elements described
in the first exemplary embodiment.
[0036] Accordingly, hereinafter, another exemplary embodiment is exemplified.
[0037] In the first exemplary embodiment, the heat exchanger is exemplified, in which flow
channel 7 through which the first fluid flows makes a U-turn and inlet header flow
channel 9 connected to outgoing flow channel 7a and outlet header flow channel 10
connected to return flow channel 7b are collectively provided on one end side of plate
fin 3. However, flow paths 7 may be linearly disposed and not make a U-turn, and inlet
header flow channel 9 may be provided on one end side of plate fin 3 and outlet header
flow channel 10 may be provided on the other end side of plate fin 3. Further, tubular
parts 13 may be provided surrounding each of inlet header flow channel 9 and outlet
header flow channel 10, and then plate fins 3 may be coupled and fixed to each other.
[0038] In the first exemplary embodiment, tubular parts 13 provided on the pair of plates
3a and 3b constituting plate fin 3 are described as tubular parts having a circular
section. However, the sectional shape of each of the tubular parts is not limited
to a circular shape, and may be any shape such as a polygonal shape including a hexagonal
shape or an elliptical shape. Note that the tubular parts may each be a tubular part
having a discontinuous wall surface with a cut, such as tubular part 13a provided
in the middle of slit 11 shown in Fig. 6.
[0039] In the first exemplary embodiment, it has been exemplified that at least one of tubular
parts 13 of adjacent plate fins 3 is tapered. However, neither of tubular parts 13
of adjacent plate fins 3 may be tapered. Alternatively, both of tubular parts 13 of
adjacent plate fins 3 may be tapered. In this case, taper angles of two tubular parts
13 to be fitted are preferably slightly different from each other. Alternatively,
although not illustrated, a distal end of one of tubular parts 13 of adjacent plate
fins 3 may be subjected to nesting processing.
[1-3. Effects and the like]
[0040] As described above, the heat exchanger according to the present disclosure includes
a plate fin stacked body in which the plate fins having the flow channels through
which the first fluid such as the refrigerant flows are stacked, the end plates respectively
stacked and disposed on both sides of the plate fin stacked body, and inlet header
flow channel and outlet header flow channel through which the first fluid flowing
through the flow channels of the plate fin stacked body passes. The second fluid flows
between layers of the plate fins of the plate fin stacked body to allow heat to be
exchanged between the first fluid and the second fluid. The plate fin includes the
pair of plates brazed to each other, and the pair of plates is provided with the flow
channel therebetween. The tubular part is provided at an appropriate position on the
periphery of the portion of the header region of the plate fin provided with the inlet
header flow channel and the outlet header flow channel connected to the flow channel.
The tubular parts of the adjacent plate fins are fitted to each other. In the present
exemplary embodiment, the tubular parts of the adjacent plate fins are fitted to each
other by brazing to couple and fix the header regions of the plate fins together.
[0041] As a result, the coupling strength of the portions of the header regions can be improved
with a simple configuration without using the reinforcing plate, bolts, and the like,
the rigidity of the plate fin stacked body can be improved, and a highly reliable
heat exchanger can be obtained.
[0042] The tubular parts are preferably provided surrounding the inlet header flow channel
and the outlet header flow channel. As a result, the pressure resistance of the portions
of the header regions can be more reliably improved.
[0043] In addition, at least one of the tubular parts provided on the pair of plates preferably
has a tapered shape or a shape obtained by being subjected to nesting processing.
Therefore, the bonding of the tubular parts becomes more reliable and the pressure
resistance in the portions of the header regions can be more reliably improved.
[0044] Note that the fitting clearance between the tubular parts disposed in the adjacent
plate fins and fitted to each other is preferably set to less than or equal to 0.2
mm. Therefore, the bonding of the tubular parts becomes more reliable and the pressure
resistance in the portions of the header regions can be still more reliably improved.
[0045] The stack-type plate fin heat exchanger according to the present disclosure has been
described above using the exemplary embodiments, but the present disclosure is not
limited thereto. That is, the exemplary embodiments disclosed herein is illustrative
in all points and not restrictive, the scope of the present disclosure is shown by
the claims, and all meanings equivalent to the claims and all modifications within
the claims are included.
INDUSTRIAL APPLICABILITY
[0046] The heat exchanger of the present disclosure can improve the coupling strength of
the portions of the header regions of the plate fins with a simple configuration,
improve the rigidity of the plate fin stacked body, and provide a highly reliable
heat exchanger. Accordingly, the present invention can be applied to a wide range
of applications including heat exchangers for domestic and industrial air conditioners
and various refrigerating devices, and thus shows great industrial value.
REFERENCE MARKS IN THE DRAWINGS
[0047]
- 1
- heat exchanger
- 2
- inlet pipe
- 3
- plate fin
- 3a, 3b
- plate
- 4
- plate fin stacked body
- 5
- outlet pipe
- 6a, 6b
- end plate
- 7
- flow channel
- 7a
- outgoing flow channel
- 7b
- return flow channel
- 8
- communication channel
- 9
- inlet header flow channel
- 10
- outlet header flow channel
- 11
- slit
- 12
- through-hole
- 13, 13a
- tubular part
1. A heat exchanger comprising:
a plate fin stacked body including a plurality of plate fins stacked, the plurality
of plate fins each having a flow channel through which a first fluid flows;
end plates respectively disposed on both sides of the plate fin stacked body in a
stacking direction of the plurality of plate fins;
an inlet header flow channel through which the first fluid flows into the flow channel;
and
an outlet header flow channel through which the first fluid flows out from the flow
channel,
wherein
the plurality of plate fins each include
a pair of plates brazed to each other to provide the flow channel between the pair
of plates, and
tubular parts each disposed in a portion of a header region of the heat exchanger
and protruding outward from a corresponding one of the pair of plates, the header
region being a region where the inlet header flow channel and the outlet header flow
channel are disposed, and
the plurality of plate fins include adjacent plate fins whose tubular parts are fitted
to each other.
2. The heat exchanger according to Claim 1, wherein the tubular parts of each of the
plurality of plate fins are disposed surrounding at least one of the inlet header
flow channel and the outlet header flow channel in plan view of each of the plurality
of plate fins.
3. The heat exchanger according to Claim 1 or 2, wherein at least one of the tubular
parts of each of the plurality of plate fins has a tapered shape or a shape obtained
by nesting processing.
4. The heat exchanger according to any one of Claims 1 to 3, wherein the adjacent plate
fins among the plurality of plate fins has a fitting clearance between the tubular
parts of less than or equal to 0.2 mm.
5. The heat exchanger according to any one of Claims 1 to 4, wherein the tubular parts
of the adjacent plate fins among the plurality of plate fins are brazed to each other
to connect portions of header regions of the adjacent plate fins.
6. The heat exchanger according to any one of Claims 1 to 5, wherein the tubular parts
protruding outward from the corresponding one of the pair of plates are disposed at
a same position in plan view of each of the plurality of plate fins.
7. The heat exchanger according to any one of Claims 1 to 6, wherein the plurality of
plate fins that are stacked together have a second fluid flowing between the plurality
of plate fins to allow heat to be exchanged between the first fluid and the second
fluid.