TECHNICAL FIELD
[0001] The present invention relates to a heat exchanger used for a heat-exchange cycle
which is mounted on vehicles and the like.
BACKGROUND ART
[0002] It is generally known that a heat exchanger configuring a heat-exchange cycle mounted
on vehicles or the like is, for example, a radiator, a condenser, an evaporator or
the like.
[0003] For example, the condenser has a plurality of flat tubes and a plurality of fins
alternately stacked, the ends of the tubes inserted in the tube insertion holes of
tanks, and integrally bonded by a brazing material which is clad to the tanks and
tubes in a heating furnace. The condenser performs heat exchange of the medium flowing
through the tanks and tubes with the open air. Partition plates are disposed within
the tanks to change a flowing direction of the medium. The tanks may be provided with
a brazing material on the outer surfaces of the tanks to connect accessories such
as a connector or the like.
[0004] The heat exchanger used for the heat-exchange cycle for vehicles is desired to be
light-weighted. Therefore, respective members configuring the heat exchanger are considered
to be made of a material having a thickness as thin as possible with safety taken
into consideration. Generally, the brazing material contains silicon (Si) and, when
the brazing material melts in a heating furnace, it forms an Al-Si eutectic liquid
phase with aluminum (Al) or an aluminum alloy, which is a material forming the tubes
and the tanks, to braze the respective members.
[0005] The Al-Si eutectic liquid phase has a liquidus temperature lower than that of the
aluminum or aluminum alloy configuring the tubes and the like. Therefore, when an
excessive amount of brazing material flows to the tubes having a thickness thinner
than that of the tanks in the heating furnace, the A1 of the tube surface reacts with
the excessive amount of brazing material to form a large amount of Al-Si eutectic
liquid phase. This may result in a disadvantage in that a hole is formed in the tubes,
erosion is caused or the like. The erosion is a phenomenon in which the melted brazing
material erodes a base metal.
[0006] Accordingly, the present invention provides a heat exchanger with high safety which
prevents an excessive amount of brazing material from flowing to the tubes and has
an appropriate amount of brazing material used to braze the respective members.
[0007] The heat exchanger used for a condenser or the like of a car air conditioner has
its core configured by alternately stacking a plurality of tubes and fins and a pair
of tanks connected for communication with both ends of the stacked tubes. A block
member is attached to the top and bottom ends of both tanks, an inlet joint for introduction
of a medium is attached to an appropriate portion of one of the tanks, and an outlet
joint for discharging the medium is attached to an appropriate portion of the other
tank.
[0008] Partition plates for dividing the tank interiors are disposed at required positions
in the tanks so that the medium flows to meander between the inlet joint and the outlet
joint.
[0009] The above-described tanks each generally has a substantially cylindrical shape and
is formed to have a single body or a two-split type body which is formed by assembling
members having a substantially semicircular cross section. Between the members forming
the two-split type tank, one having holes for connection of the ends of the tubes
is called the end plate and the other is called the tank plate. This two-split type
tank has advantages in that the holes for connection of the ends of the tubes are
readily formed and the partition plates are easily attached.
[0010] It was necessary to accurately fit the dimensions of the partition plates to the
inside surface of the tank so not to have any gap between the inside wall of the tank
and the partition plates because such a gap allows the medium partly bypass through
the gap and degrades the performance.
[0011] But, the two-split type tank often has a complex sectional shape at the junction
of the end plate and the tank plate, and it was hard to match the dimensions of the
partition plates.
[0012] Under the circumstances described above, an object of the present invention is to
provide a heat exchanger having two-split type tanks and high airtightness which is
free from leakage of a medium between the inside surface of the tank and the partition
plates without strictly controlling the dimensions of the partition plates.
[0013] As described above, the heat exchanger such as a radiator or an evaporator of the
refrigeration cycle is configured by alternately stacking a plurality of tubes and
a plurality of fins to form a core and connecting the ends of the tubes to the tanks.
[0014] The medium is taken into the inside through the inlet joint formed on the tank, passed
through the tubes while conducting heat exchange by the heat conducted to the core
and discharged to the outside through the outlet joint formed on the tank. A fan may
be disposed on the outside of the heat exchanger to send air to the core.
[0015] Besides, this type of heat exchanger is produced by assembling respective aluminum
or aluminum alloy members and heating the assembly in a furnace to be brazed into
one body.
[0016] In view of the heat-exchanging performance of such a heat exchanger, a gap between
the fins and the tank is desired to be as small as possible. Because, if the gap between
the fins and the tank is large, air leaks through the gap, and the heat-exchanging
performance drops.
[0017] But, there is a problem that, when the fins and the end plates are approached to
one another, the brazing material melted from the tank at the time of brazing reaches
the ends of the fins, and the ends of the fins are melted by erosion.
[0018] In other words, the fins are thin and their ends have a disadvantage of easily causing
unnecessary erosion because of an effect of the brazing material.
[0019] The present invention was achieved under the circumstances as described above, and
it is to provide a heat exchanger which effectively avoids the ends of fins from being
eroded by a brazing material.
DISCLOSURE OF THE INVENTION
[0020] The invention described in Claim 1 is a heat exchanger which has tubes for flowing
a medium and a tank comprising an end plate having tube insertion holes for connecting
the tubes and a tank plate connected to the end plate and formed by assembling the
respective members and brazing the members for connection in a heating furnace; wherein
the tank plate is formed of a plate provided with a brazing material, and at least
one of the tank plate and the end plate is provided with a separator portions not
having a brazing material for prevention of a brazing material from outflowing.
[0021] Thus, the heat exchanger is formed of two members of the tank plate and the end plate,
and at least one of the end plate and the tank plate is provided with the separator
portion for prevention of the brazing material from outflowing, so that the molten
brazing material is prevented from moving by the separator portion within the heating
furnace.
[0022] Generally, the molten brazing material flows along the brazing material disposed
on the members in the heating furnace and guided into the gaps formed when the members
are assembled. An excessive amount of molten brazing material is especially accumulated
in the gaps between the tubes and the tube insertion holes to form a large amount
of Al-Si eutectic liquid phase, and erosion tends to occur on the tubes in contact
with the tube insertion holes.
[0023] According to the invention, the separator portion which is not provided with the
brazing material and prevents the brazing material from outflowing is disposed on
at least one of the tank plate and the end plate, so that the separator portion prevents
the brazing material from flowing, and an excessive amount of brazing material is
prevented from flowing to the tubes. Therefore, erosion of the tubes configuring the
heat exchanger can be prevented, and a highly safe heat exchanger can be provided.
[0024] For example, even if the molten brazing material flows over the separator portion
in the heating furnace, a flowing amount of the molten material to the tubes can be
reduced by the separator portion, and the flow of the excessive amount of brazing
material to the tubes can be prevented.
[0025] The invention described in Claim 2 relates to the invention according to Claim 1,
wherein the separator portion is disposed on a surface of the end plate which is in
contact with the tank plate.
[0026] For example, when the tank plate is formed to have a substantially U-shaped cross
section and the outer surface of the end plate is contacted with the inside of the
U-shaped opening to configure the tubular tank, the edges of the end plate is contacted
with the tank plate. The separator portion not having the brazing material is disposed
on one surface of the edges of the end plate contacted with the tank plate. In the
heating furnace, the separator portion prevents the brazing material disposed on the
tank plate from flowing. Therefore, an excessive amount of brazing material does not
flow to the tubes, and the tubes can be brazed for connection into the tube insertion
holes of the end plate with an appropriate amount of brazing material.
[0027] The invention described in Claim 3 relates to the invention according to Claim 2,
wherein the tank plate has the brazing material disposed on its surface which becomes
at least the inner surface of the tank, and the end plate has the brazing material
disposed on its surface which becomes the inner surface of the tank.
[0028] Thus, even when the brazing material is disposed on the surface of the tank plate
which becomes the inside of the tank and the surface of the end plate which becomes
the inside of the tank, the separator portion prevents the brazing material disposed
on the tank plate from flowing and prevents an excessive amount of brazing material
from flowing to the tubes in the heating furnace.
[0029] The invention described in Claim 4 relates to the invention according to any one
of Claims 1 to 3, wherein the tank plate is provided with the separator portion on
its surface which is in contact with the end plate.
[0030] For example, even when the brazing material is disposed on the surface of the tank
plate which becomes the outside of the tank, the separator portion prevents the brazing
material disposed on the tank plate from flowing and prevents an excessive amount
of brazing material from flowing to the tubes.
[0031] The invention described in Claim 5 relates to the invention according to any one
of Claims 1 to 4, wherein the tank is provided with a partition plate within it, and
the tank is formed by assembling the tank plate and the end plate while positioning
by the partition plate.
[0032] Thus, the tank formed of two members, the tank plate and the end plate, has the tank
plate and the end plate positioned by the partition plate disposed within the tank,
so that the tank plate and the end plate can be prevented from displacing.
[0033] The invention described in Claim 6 relates to the invention according to any one
of Claims 1 to 5, wherein the heat exchanger uses tubes which are formed of a plate.
[0034] When the tubes are formed of a plate, the tubes which can secure the required pressure
resistance can be formed even if the plate is thin. Thus, when the tubes formed of
a thin plate is used, the heat exchanger can be light-weighted.
[0035] And, even when the thin tubes are used, the separator portion prevents the brazing
material from flowing, so that an excessive amount of brazing material does not outflow
to the tubes. Therefore, erosion resulting from the outflowing of an excessive amount
of brazing material to the tubes can be prevented from occurring, and a highly safe
heat exchanger can be provided.
[0036] The invention described in Claim 7 relates to the invention according to any one
of Claims 1 to 6, wherein the tubes have slits on the outer surfaces of the tubes
which are in contact with tube insertion holes of the end plate.
[0037] As described above, when the tubes have the slits, the molten brazing material in
the heating furnace is introduced into the slits. In other words, the brazing material
flows through the gaps between the tube insertion holes and the tubes and is drawn
into the slits. Therefore, the tubes and the end plate are joined with an appropriate
amount of brazing material, and defective brazing can be avoided.
[0038] The invention described in Claim 8 relates to a heat exchanger having tubes for flowing
a medium and tanks to which ends of the tubes are connected, wherein the tanks are
formed by brazing an end plate which is formed with holes for connection of the ends
of the tubes, a tank plate connected to the end plate, and a partition plate for dividing
the interior, and a brazing material is clad to the inner surface of at least one
of the tank plate and the end plate, and the partition plate is formed of a bare material
which is not clad with a brazing material.
[0039] Conventionally, when the partition plate clad with the brazing material was used,
the molten brazing material on the inner surface of the tank became integral with
the molten brazing material of the partition plate at the time of brazing, attracted
by gravitation or capillary phenomenon and outflown to another portion along the partition
plate. Therefore, the brazing material for brazing the partition plate became short
in amount, and the partition plat was apt to be brazed defectively.
[0040] According to the present invention, since the partition plate is a bare material
which is not clad with the brazing material, the molten brazing material on the inner
surface of the tank when brazing hardly outflows along the unwet partition plate.
As a result, the brazing material for brazing the partition plate does not become
short, and the partition plates can be brazed adequately even if there are some gaps
between the inner surface of the tank and the partition plate.
[0041] Therefore, the medium does not leak between the inner surface of the tank and the
partition plate even if the dimensions of the partition plate are not controlled strictly
as before, and a highly airtight heat exchanger can be provided.
[0042] The invention described in Claim 9 relates to the invention according to Claim 8,
wherein the tubes have slits formed on the surfaces.
[0043] The present invention is particularly effective for a heat exchanger having tubes
which have slits in the surface.
[0044] When the tubes have the slits in the surface, the brazing material melted on the
inner surface of the tank at the time of brazing is drawn into the slits by capillarity
phenomenon and outflown to the tubes. Therefore, the brazing material for brazing
the partition plate became short, and the partition plate was apt to be brazed defectively.
[0045] According to the invention, even if the brazing material on the inner surface of
the tank outflows to the tubes, the brazing material does not outflow along the partition
plates as before, so that an outflow amount is substantially reduced, the brazing
material for brazing the partition plate does not become short, and the partition
plate can be brazed adequately.
[0046] The invention described in Claim 10 relates to the invention according to Claim 9,
wherein the tubes are formed of a plate material.
[0047] The present invention is particularly effective for a heat exchanger having the tubes
which are formed of a plate material.
[0048] So-called roll forming tubes which are formed of a plate material have partitions
in their interiors formed by bending a plate material to have a corrugated shape,
and slits are formed in the surface. Therefore, the brazing material melted on the
inner surface of the tank at the time of brazing is drawn into the slits by capillary
phenomenon and outflows to the tubes. Therefore, the brazing material for brazing
the partition plate became short, and the partition plate was brazed defectively.
[0049] According to the present invention, even when the brazing material on the inner surface
of the tank outflows to the tubes, the brazing material does not flow along the partition
plate as before, so that an outflowing amount is substantially reduced. Thus, the
brazing material for brazing the partition plates does not become short, and the partition
plate can be brazed adequately.
[0050] The invention described in Claim 11 is a heat exchanger having a core which is formed
by stacking tubes and fins and tanks to which the ends of the tubes are connected,
and performing heat exchange by a medium flowing through the tubes by heat conducted
to the core, wherein the tanks have an end plate which is formed with holes for connection
of the tubes and a tank plate to which the end plate is attached, the heat exchanger
is formed by assembling and brazing the tubes, the fins, the end plate and the tank
plate in a furnace, the end plate has a brazing material clad on its one surface only,
and the ends of the fins are opposed to a surface of the end plate not clad with the
brazing material at the time of brazing.
[0051] By configuring as described above, erosion of the ends of the fins by the brazing
material can be avoided efficiently.
[0052] In other words, the ends of the fins have a disadvantage that unnecessary erosion
is apt to be caused by an influence of the brazing material. But, according to the
present invention, the brazing material melted from the tank can be prevented from
being brought to the ends of the fins, and such a disadvantage can be avoided.
[0053] Besides, it is desirable that the fins and the tanks are mutually approached as close
as possible in view of the heat-exchange performance of the core. Especially, when
air is sent to the core, air leaks through the gap between the fins and the tanks
if it is large. In this connection, the present invention has no possibility of causing
erosion at the ends of the fins even if the fins and the tanks are close to each other.
And, the heat exchanger is configured quite rationally.
[0054] The invention described in Claim 12 relates to the invention according to Claim 11,
wherein the ends of the fins have a minimum distance of 2.0 mm or less from the surface
of the end plate which is not clad with the brazing material.
[0055] By configuring as described above, the heat-exchange performance of the core can
be secured adequately.
[0056] In other words, if the gap between the fins and the tanks is large, it causes lowering
of the heat-exchange performance, but the present invention sets the upper limit of
the gap to 2.0 mm in order to prevent the heat-exchange performance from lowering.
[0057] The invention described in Claim 13 relates to the invention according to Claim 11,
wherein the ends of the fins are in contact with the surface of the end plate which
is not clad with the brazing material.
[0058] By configuring as described above, the heat-exchange performance of the core can
be secured adequately.
[0059] In other words, if the gap between the fins and the tanks is large, the heat-exchange
performance is lowered, but the present invention has them mutually contacted to prevent
the heat-exchange performance from lowering.
BRIEF DESCRIPTION OF THE DRAWINGS
[0060]
Fig. 1 is a top view showing a general structure of a heat exchanger according to
an embodiment of the present invention.
Fig. 2 is an exploded perspective view showing a structure of a tank according to
an embodiment of the invention.
Fig. 3 is a sectional view of a tank to which a tube is attached according to an embodiment
of the invention.
Fig. 4 is an end face view of a tube according to an embodiment of the invention.
Fig. 5 is a partially enlarged view of the end face of the tube shown in Fig. 4.
Fig. 6 is a sectional view showing a tank to which a tube is attached according to
an embodiment of the invention.
Fig. 7 is a sectional view showing a tank to which a tube is attached according to
an embodiment of the invention.
Fig. 8 is a front view showing a general structure of a heat exchanger according to
an embodiment of the invention.
Fig. 9 is an exploded perspective view showing a structure of a tank according to
an embodiment of the invention.
Fig. 10 is a transverse sectional view showing a tank according to an embodiment of
the invention.
Fig. 11 is a vertical sectional view showing a tank according to an embodiment of
the invention.
Fig. 12 is a cross sectional view showing a tank according to an embodiment of the
invention.
Fig. 13 is a perspective view showing a tube according to an embodiment of the invention.
Fig. 14 is a front view showing a heat exchanger according to an embodiment of the
invention.
Fig. 15 is an exploded perspective view showing the main portion of a heat exchanger
according to an embodiment of the invention.
Fig. 16 is an explanatory view showing a tank and a fin according to an embodiment
of the invention.
BEST MODE FOR CARRYING OUT THE INVENTION
[0061] Embodiments of the invention will be described in detail with reference to the accompanying
drawings.
[0062] Fig. 1 is a top view showing a general structure of a heat exchanger 1.
[0063] The heat exchanger 1 shown in Fig. 1 shows an example of a condenser. The heat exchanger
1 has tubes 21 and fins 4 alternately stacked and both ends of the tubes 21 inserted
and connected to tube insertion holes 5 of a pair of tanks 3. Partition plates 7 for
dividing a medium passage which is formed of the tanks 3 and the tubes 21 are disposed
within the tanks 3. The openings of the tanks 3 are sealed with the partition plates
7. The tanks 3 are provided with an outflow/inflow ports 31b for feeding or discharge
of the medium to/from the heat exchanger 1. A side plate 8 is disposed on either side
of the stacked tubes 21 and fins 4. The side plate 8 on the bottom end of the heat
exchanger 1 is provided with mounting members 10 for mounting the heat exchanger 1
on a vehicle body.
[0064] The heat exchanger 1 has the above-described members assembled and integrally brazed
by a brazing material disposed on the respective members in a heating furnace.
[0065] Fig. 2 is a perspective view showing the tank 3. Fig. 2 is an exploded perspective
view of the tank 3 which is comprised of a tank plate 31, an end plate 32 and the
partition plate 7.
[0066] The tank 3 is formed to have a tubular shape by attaching the outside face of the
end plate 32 to a U-shape open inside face of the tank plate 31 which is formed to
have a U-shaped cross section. The end plate 32 is formed with the tube insertion
holes 5 into which the tubes 21 are inserted.
[0067] The tank plate 31 and the end plate 32 are positioned by the partition plate 7 which
is disposed within the tank 3 to configure the tubular tank 3. The tank plate 31 of
this embodiment is provided with an attachment hole 31a for attachment of the partition
plate 7 and the outflow/inflow port 31b for the medium. The partition plate 7 has
a projection 7a for insertion into the attachment hole 31a and notches 7b for engagement
of the end plate 32. Specifically, the projection 7a of the partition plate 7 is inserted
into the attachment hole 31a of the tank plate 31 to attach the partition plate 7
to the tank plate 31. Then, the end plate 32 is attached to fit the inside surface
of the U-shaped opening of the tank plate 31. Then, the edges of the end plate 32
are connected to the notches 7b of the partition plate 7, and the tank plate 31 and
the end plate 32 are positioned to enable to assemble the tank 3.
[0068] Fig. 3 is a sectional view of the tank 3 having the tube 21 assembled.
[0069] As shown in Fig. 3, the tank plate 31 is formed with a brazing material R1 on its
surface which becomes the outer surface of the tank 3 and a brazing material R2 on
its surface which becomes the inner surface of the tank 3. The brazing material R1
disposed on the outer surface of the tank plate 31 is a brazing material for attaching
an accessory such as the connector 4 to the tank 3, and the brazing material R1 is
a brazing material for attaching the partition plate 7 to be disposed within the tank
3.
[0070] The end plate 32 is formed with a brazing material R3 on its surface which becomes
the inner surface of the tank 3. The brazing material R3 is a brazing material for
attaching the tube 21 and also the partition plate 7.
[0071] The end plate 32 has its surfaces which are in contact with the tank plate 31 determined
as separator portions 321 which are not provided with a brazing material and prevents
the brazing material from outflowing. The separator portions 321 prevent flowing of
the brazing material R2 which is disposed on the inside of tank plates 31 within the
heating furnace.
[0072] Generally, the molten brazing material in the heating furnace flows along the brazing
material which is clad to the plate. The end plate 32 of this embodiment is provided
with the separator portions 321 which are not provided with a brazing material and
prevent the brazing material from outflowing, so that the flow of the brazing material
R2 disposed on the inner surface of the tank plate 31 in the heating furnace is prevented
by the separator portions 321 and it does not flow to the end plate 32. Even if the
molten brazing material R2 flows over the separator portions 321, its flowing amount
becomes smaller than when the separator portions 321 are not disposed.
[0073] The tank plate 31 has its surfaces which are in contact with the end plate 32 determined
as separator portions 311 which are not provided with a brazing material. The brazing
material R1 disposed on the outer surface of the tank plate 31 is prevented its flow
by the separator portions 311 in the heating furnace and does not flow to reach the
end plate 32.
[0074] Therefore, the tube 21 is brazed for connection to the tube insertion hole 5 of the
end plate 32 with an appropriate amount of brazing material, and the occurrence of
erosion which may result from an excessive amount of brazing material flowing to the
tube 21 can be prevented.
[0075] Fig. 4 is a diagram showing an end face of the tube 21. As shown in Fig. 4, the tube
21 used for the heat exchanger 1 of this embodiment is formed of a plate by roll forming
for forming the tube 21 by sequentially bending the plate. In the drawing, 21a indicates
medium passages, 21b beads, and 21c a junction.
[0076] When the tube is formed by the roll forming, the tube 21 can be formed of a thin
plate. In the heat exchanger 1 of this embodiment, an excessive amount of brazing
material does not flow toward the tube in the heating furnace even though the tube
21 is thin, and the tube 21 can be prevented from having a hole, and the occurrence
of erosion can be prevented. Therefore, the heat exchanger 1 can be made light in
weight, and the safety of the heat exchanger 1 can be improved.
[0077] Fig. 5 is a partially enlarged view of the end face of the tube 21. As shown in Fig.
5, the tube 21 is provided with the beads 21b which divides the interior of the tube
21 to provide the medium passages 21a by bending a plate. When the beads 21b are formed
by bending the plate, slits 21d are formed on the outer surfaces of the tube 21. In
the heating furnace, the brazing material R3 disposed on the end plate 32 melts and
drawn into the slits 21d. Therefore, the molten brazing material flowing through the
tube 21 and the tube insertion hole 5 of the end plate 32 does not remain in the gap
between the tube 21 and the tube insertion hole 5 but flows to the slits 21d, and
the tube 21 and the end plate 32 are connected by an appropriate amount of brazing
material.
[0078] Fig. 6 is a sectional view of the tank 3 to show another embodiment.
[0079] In this embodiment, the tank plate 31 has the brazing material R1 formed on its surface
which forms the outside of the tank 3 as shown in Fig. 6. The end plate 32 is provided
with a brazing material R4 on its surface which forms the outside of the tank 3 and
the brazing material R3 on its surface which forms the inside.
[0080] In this embodiment, the tank plate 31 is provided with the separator portions 311
for prevention of leakage of the brazing material from outflowing on its surfaces
which are in contact with the end plate 32 and not provided with a brazing material.
The separator portions 311 prevent the flow of the brazing material R1 disposed on
the outer surface of the tank plate 31. Therefore, an excessive amount of brazing
material does not flow to reach the tube insertion hole 7 of the end plate 31.
[0081] It is not limited to this embodiment, but it is possible to configure the tank by
disposing the brazing material on the partition plate itself and not disposing the
brazing material on the inside surface of the end plate or the tank plate.
[0082] Fig. 7 is a sectional diagram of a tank 30 to show another embodiment.
[0083] In this embodiment, an end plate 33 is attached from the outside of a U-shaped opening
of the tank plate 31 having a U-shaped cross section as shown in Fig. 7. The tank
plate 31 has the brazing material R1 disposed on its surface which becomes the outer
surface of the tank 30 and the brazing material R2 disposed on its surface which becomes
the inner surface of the tank 30. And, the end plate 33 has a brazing material R5
disposed on its surface which becomes the outer surface of the tank 30.
[0084] The tank plate 31 is provided with the separator portions 311 on its surfaces which
are in contact with the end plate 33 and not provided with the brazing material. The
end plate 33 has its two surfaces which are contacted with the tank plate 31, namely
the surface which becomes the inner surface of the tank 30 and the edges of the end
plate 33, which are designated as separator portions 331, 332.
[0085] Therefore, the separator portions 311, 331, 332 prevent flow of the brazing materials
R1 and R2 disposed on the tank plate 31. Therefore, outflow of an excessive amount
of brazing material is prevented by the separator portions 311, 331, 332, and the
tube 21 and the end plate 31 are brazed for connection with an appropriate amount
of brazing material.
[0086] Next, another embodiment of the invention will be described.
[0087] Fig. 8 is a front view showing a general structure of the heat exchanger 1. This
heat exchanger 1 is a condenser for a car air conditioner. The heat exchanger 1 is
configured of a core 2, which is configured by alternately stacking a plurality of
tubes 21, 21 and fins 4, 4, and a pair of tanks 3, 3 into which both ends of the plurality
of tubes 21, 21 are inserted. Within the tanks 3, 3, partition plates 7, 7 are disposed
to divide the insides of the tanks 3, 3. Upper and lower openings of the tanks 3,
3 are sealed by block members 6, 6, and a pair of side plates 8, 8 are disposed on
top and bottom of the core 2 for reinforcement. Besides, the tank 3, 3 are provided
with an inlet joint 41 and an outlet joint 42 for introduction and discharge of the
medium.
[0088] The upper and lower openings of the tanks 3, 3 may be sealed by partition plates
7, 7 without using the block members 6, 6.
[0089] Those component members of the heat exchanger 1 are made of an aluminum alloy and
assembled, then connected into one body by brazing in a furnace.
[0090] Fig. 9 is an exploded perspective view showing the tank 3. The tank 3 is a two-split
type tank which is comprised of a tank plate 31 and an end plate 32.
[0091] The tank 3 has the outer periphery of the end plate 32 contacted with the inner surface
of a U-shaped opening of the tank plate 31 which has a U-shaped cross section to form
the tubular tank 3. The end plate 32 is formed with tube insertion holes 5, 5 into
which tubes are inserted.
[0092] The tank plate 31 and the end plate 32 are positioned by the partition plate 7 disposed
within the tank 3, so that the tank plate 31 and the end plate 32 are attached in
position.
[0093] The tank plate 31 of this embodiment is provided with an attachment hole 31a into
which the partition plate 7 is attached and an outflow/inflow port 31b for connection
of an inlet joint 41 or an outlet joint 42. And, the partition plate 7 is provided
with a projection 7a which is inserted into the attachment hole 31a and notches 7b,
7b for engagement with the end plate 32.
[0094] To assemble the tank 3, the projection 7a of the partition plate 7 is first inserted
into the attachment hole 31a of the tank plate 31 to attach the partition plate 7
to the tank plate 31. Then, the end plate 32 is assembled to be attached to the inner
surface of a U-shaped opening of the tank plate 31 so the edges of the end plate 32
are engaged with the notch 7b of the partition plate 7, and the tank plate 31 and
the end plate 32 can be positioned to assemble the tank 3.
[0095] Fig. 10 is a cross sectional view of the tank 3 having the tube 21 assembled.
[0096] As shown in Fig. 10, the tank plate 31 is provided with the brazing material R1 on
its surface which becomes the outer surface of the tank 3 and the brazing material
R2 on its surface which becomes the inner surface of the tank 3. The brazing material
R1 disposed on the surface of the tank plate 31 which becomes the outer surface is
a brazing material for bonding accessories such as the inlet joint 41 and the outlet
joint 42 to the tank 3, and the brazing material R2 is a brazing material for bonding
the partition plate 7 within the tank 3 and for bonding the tank plate 31 and the
end plate 32.
[0097] And, the end plate 32 is provided with the brazing material R3 on its surface which
becomes the inner surface of the tank 3. The brazing material R3 is a brazing material
for connecting the tube 21 to the tube insertion hole 5 and for connecting the partition
plate 7.
[0098] Fig. 11 is a partially vertical sectional view showing the tank.
[0099] As shown in Fig. 11, the outer and inner surfaces of the tank plate 31 are clad with
the brazing materials R1, R2, and the partition plate 7 is formed of a bare material
not clad with the brazing material.
[0100] According to this embodiment, the partition plate 7 is not clad with the brazing
material, so that the brazing materials R2, R3 melted during the brazing hardly outflow
along the partition plate 7 which is not wet. As a result, the brazing material for
brazing the partition plate does not become short, and the partition plate 7 can be
brazed adequately even if there is a gap between the inner surfaces of the tank plate
31 and the end plate 32 and the partition plate 7.
[0101] Therefore, a highly airtight heat exchanger which is free from a leakage of the medium
between the inner surface of the tank and the partition plate 7 without strictly controlling
the dimensions of the partition plate 7 as before.
[0102] Fig. 12 is a cross sectional view of the tank 3 to show another embodiment.
[0103] In this embodiment, the tank plate 31 is provided with the brazing material R1 on
its surface which becomes the outer surface of the tank 3 as shown in Fig. 12. The
brazing material R1 is a brazing material for connecting accessories such as the inlet
joint 41 and the outlet joint 42 to the tank 3.
[0104] The end plate 32 has the brazing material R3 disposed on its surface which becomes
the inner surface of the tank 3 and the brazing material R4 disposed on its surface
which becomes the outer surface. The brazing material R3 disposed on the surface which
becomes the inner surface of the end plate 32 is a brazing material for attaching
the tube 21 to the tube insertion hole 5 and for attaching the partition plate 7 disposed
within the tank 3, and the brazing material R4 is a brazing material for connecting
the tube 21 to the tube insertion hole 5 and for connecting the tank plate 31 and
the end plate 32.
[0105] Thus, even when the brazing material R3 is clad to the end plate 32 and not clad
to the tank plate 31 on the inner surface of the tank 3, the partition plate 7 can
be brazed without forming a gap because the molten brazing material R3 enters the
gap between the inner surface of the tank plate 31 and the side surface of the partition
plate 7 by capillary phenomenon.
[0106] Fig. 13 is a perspective view of the tube 21 to show another embodiment.
[0107] The tube 21 of this embodiment is a so-called roll forming tube which is formed by
roll forming a plate material, and a plurality of passages 21a, 21a for flowing a
medium are formed within it.
[0108] The tube 21 is formed with partitions by bending a plate material into a corrugated
shape to form a plurality of beads 21b, 21b, folding in two and bonding to have the
beads 21b, 21b inside, and mutually contacting the beads 21b, 21b. Slits 21d are formed
in the surface of the tube 21 by the beads 21b, 21b and the junction 21c.
[0109] Therefore, the heat exchanger 1 using the tubes 21 tends to suffer from a shortage
of the brazing material for brazing the partition plate 7 and defective brazing of
the partition plate 7 because the molten brazing material on the inner surface of
the tank 3 at the time of brazing is taken into the slits 21d, 21d by capillary phenomenon
and outflows to the tubes 21.
[0110] But, when the partition plate 7 is determined to be a bare material, the brazing
material does not outflow along the partition plate 7 as before even if the brazing
material on the inner surface of the tank 3 flows to the tube 21, so that an outflow
amount is considerably reduced, the brazing material for brazing the partition plate
7 does not become short, and the partition plate 7 can be brazed adequately.
[0111] In the above embodiment, the condenser has been described as an example, but the
invention is not limited to it, and the object of the invention can be achieved for
an evaporator or a heater core.
[0112] Then, another embodiment of the invention will be described.
[0113] The heat exchanger 1 of this embodiment is a radiator of a refrigeration cycle for
a car air conditioner mounted on an automobile and provided with the core 2 which
is formed by alternately stacking a plurality of tubes 21 for flowing a medium (namely,
refrigerant) and a plurality of fins 4 and a pair of tanks 3 to which both ends of
the tubes 21 are connected as shown in Fig. 14 and Fig. 15 and is configured to perform
heat exchange between the medium and air flowing to the core 2 by heat conducted to
the core 2.
[0114] A side plate 8 as a reinforcing member is disposed on the upper and lower sides of
the core 2. Ends of each side plate 8 are supported by the tanks 3.
[0115] Besides, the tank 3 is provided with the inlet joint 41 for introducing the medium
and the outlet joint 42 for discharging the medium, and the medium flows into the
tank 3 through the inlet joint 41, flows through the tubes 21 while performing heat
exchange and is discharged to the outside of the tank 3 through the outlet joint 42.
[0116] Each tank 3 is substantially cylindrical with its both ends blocked by the block
member 6 and the interior divided by the partition plates 7 at prescribed intervals,
and the medium is reciprocated for a plurality of times between the tanks 3.
[0117] The tube 21 is formed flat by extrusion forming or roll forming of a plate. Its interior
is divided into a plurality of sections in order to provide a prescribed pressure
resistant performance. Fins 4 of this embodiment are formed of a clad material which
has its front and rear sides clad with an appropriate amount of brazing material required
for brazing with the tubes and is roll-formed into a corrugated shape. Its wave pitch
is approximately 1.6 mm to 3.0 mm. And, many louvers which are not shown are disposed
at necessary portions of the fins 4.
[0118] Besides, each tank 3 of this embodiment is configured by attaching the end plate
32 to the tank plate 31. The tank plate 31 and the end plate 32 are formed by cutting
and press-forming a plate having a required thickness.
[0119] The tank plate 31 is a semicircular cylindrical member, and the end plate 32 is a
member having a plurality of tube insertion holes 5 into which the ends of the tubes
21 are inserted for attachment. The tube insertion holes 5 are formed in series at
prescribed intervals in the longitudinal direction of the tank 3.
[0120] The end plate 32 is inserted between both ends of the tank plate 31 for attachment
to the tank plate 31. An inserted amount of the end plate 32 is restricted by the
partition plates 7.
[0121] Bent pieces 31c for holding the end plate 32 and wall sections 31d which are protruded
toward the core 2 are disposed in parallel at both ends of the tank plate 31. The
bent pieces 31c and the wall sections 31d are alternately disposed at prescribed intervals
along the longitudinal direction of the tank 3.
[0122] The end plate 32 is fixed by positioning on the tank plate 31 and bending the bent
pieces 31c. The bent pieces 31c are bent by a caulking jig or the like.
[0123] And, the tubes 21, fins 4, tank plate 31, end plate 32, inlet joint 41, outlet joint
42, side plate 8, block member 6 and partition plate 7 which configure the heat exchanger
1 are members formed of aluminum or aluminum alloy, assembled by a jig, and brazed
into one body by heating the assembly in a furnace. The brazing material and flux
required for brazing are disposed on required portions of the respective members before
the heating process.
[0124] As shown in Fig. 16, the tank plate 31 has a brazing material F clad on both surfaces
in this embodiment. The end plate 32 has the brazing material F clad on its one surface
only, and the end of the fin 4 and the surface of the end plate 32 not clad with the
brazing material are opposed to each other when brazing.
[0125] The brazing material F which is clad to the tank plate 31 and the end plate 32 brazes
the tank plate 31 and the end plate 32 and also brazes the tube 21, the inlet joint
41, outlet joint 42, the block member 6 and the partition plate 7.
[0126] And, when the end of the fin 4 and the surface of the end plate 32 not clad with
the brazing material are opposed, even if the brazing material F clad to the tank
plate 31 and the end plate 32 melts, the brazing material F does not reach the end
of the fin 4, and unnecessary erosion at the end of the fin 4 can be avoided.
[0127] Therefore, the above configuration can make the gap between the fin 4 and the tank
3 as small as possible, and the heat exchange performance of the core 2 can be improved.
[0128] Especially, it is determined in this embodiment that the fin 4 has a length which
is slightly smaller than the gap between the tanks 3, a minimum distance G between
the end of the fin 4 and the surface of the end plate 32 not clad with the brazing
material is 2.0 mm or less at the ends of all the fins 4 of the heat exchanger 1.
[0129] But, some of the ends of the fins 4 may come into contact with the surface of the
end plate 32 not clad with the brazing material. And, some of the ends of the fins
4 may have a minimum distance G of 2.0 mm or more depending on some dimensional error.
[0130] The minimum distance G is a distance of the minimum one of the gaps. Specifically,
the end plate 32 of this embodiment has a sectional shape which swells toward the
core 2, and the minimum distance G is a distance between the center of the end of
the fin 4 and the swelled top of the tank plate 32.
[0131] By configuring as described above, leakage of air from the gap between the fin 4
and the tank 3 can be remedied, and the heat exchange performance of the core can
be secured satisfactorily.
[0132] The minimum distance G between the end of the fin 4 and the surface of the end plate
32 not clad with the brazing material is determined to be 2.0 mm or less in this embodiment,
but it is desirably 1.0 mm or less in order to remedy the air leak.
[0133] It may also be configured that the fin 4 has a length slightly larger than the gap
of the tanks 3, and the fin 4 is compressed slightly to assemble, so to contact the
ends of all fins 4 of the heat exchanger 1 to the surface of the end plate 32 not
clad with the brazing material.
[0134] By configuring as described above, the air leak from the gap between the fin 4 and
the tank 3 can be remedied more securely.
[0135] As described above, the heat exchanger of this embodiment efficiently avoids the
ends of the fins from being eroded by the brazing material and is preferably used
as a radiator of the refrigeration cycle. And, the configuration of this embodiment
can also be applied to another heat exchanger such as an evaporator, a car radiator
or the like.
INDUSTRIAL APPLICABILITY
[0136] The present invention is a heat exchanger generally used for a refrigeration cycle
of car and home air conditioner and the like, and particularly suitable for a radiator,
a condenser, an evaporator and the like.