TECHNICAL FIELD
[0001] The present invention relates to a heat exchanger in which a medium exchanges heat
by conducting heat to a heat-exchange tube.
BACKGROUND ART
[0002] A conventionally known heat exchanger is comprised of a heat-exchange tube for performing
a heat exchange of a medium and a pair of headers for receiving and supplying the
medium, which are connected to be communicative.
[0003] Specifically, the medium taken in from one of the headers is flown through the medium
passages in the heat-exchange tube and discharged from the other header, and the heat
exchange of the medium is performed by heat conducted to the heat-exchange tube.
[0004] The heat-exchange tube used for such a heat exchanger of the type as described above
is produced by extruding or the like of an aluminum alloy. It is formed to have a
flat appearance and provided with a plurality of small medium passages so to improve
the efficiency of heat exchange.
[0005] For example, one disclosed in Japanese Patent Application Laid-Open Publication No.
5-215482 has a plurality of medium passages with a circular cross section in order
to reduce a pressure loss. Thus, when the medium passages have a circular cross section,
a pressure resistance to the medium can be improved as compared with those having
a triangle or square cross section.
[0006] As described above, the heat-exchange tube having the plurality of medium passages
with the circular cross section has the pressure resistance of the medium passages
improved as compared with those having the triangle or square-shaped medium passages,
but has a drawback that the passages has a small inner surface area to a flow rate
of the medium.
[0007] In other words, a contact area between the medium and the heat-exchange tube becomes
relatively small, so that there is a disadvantage that a heat-exchange rate is lowered.
[0008] Particularly, when the heat-exchange tube made of an aluminum alloy is used for a
gas cooler or the like in which the medium is not condensed and which therefore needs
a remarkable pressure resistance, there are drawbacks that the heat-exchange tube
has a thick wall and results in a considerably lowered heat-exchange rate as compared
with those made of titanium or copper.
[0009] Therefore, in view of the drawbacks described above, the present invention provides
a heat exchanger which can improve the pressure resistance and heat-exchange rate
of the heat-exchange tube.
DISCLOSURE OF THE INVENTION
[0010] The invention described in claim 1 is a heat exchanger comprising a heat-exchange
tube having medium passages and a pair of headers disposed at ends of the heat-exchange
tube to receive and supply a medium, and having the medium to perform heat exchange
by heat which is conducted to the heat-exchange tube, wherein the medium passages
in the heat-exchange tube have a substantially circular cross section and an uneven
inner surface.
[0011] Thus, according to the heat exchanger of the present invention, the medium passages
in the heat-exchange tube have a substantially circular cross section and an uneven
inner surface, so that the heat-exchange tube is improved its performance as its pressure
resistance and heat-exchange rate are improved.
[0012] More specifically, when the heat-exchange tube having the medium passages in the
circular shape, their pressure resistance is improved as compared with those having
a triangle or square shape, but a contact area between the medium and the heat-exchange
tube becomes relatively small, resulting in a degradation of the heat-exchange rate.
But, the present invention solves such a drawback by having the uneven inner surface
in the passages so to secure a large contact area between the medium and the heat-exchange
tube.
[0013] The invention described in claim 2 is the heat exchanger according to the invention
of claim 1, wherein the medium is a non-condensation medium, and the heat-exchange
tube is made of an aluminum alloy.
[0014] Thus, according to the heat exchanger of the present invention, the medium is a non-condensation
medium, and the heat-exchange tube is made of an aluminum alloy, so that the heat-exchange
tube is produced lightweight at a low cost.
[0015] Specifically, when the heat-exchange tube of an aluminum alloy is used for a gas
cooler or the like for which the medium is not condensed, an excellent pressure resistance
is required, and there are drawbacks that the heat-exchange tube has a thick wall
and a considerably lowered heat-exchange rate as compared with those made of titanium
or copper. But, the present invention forms the medium passages with an uneven-shaped
inner surface, so that the heat-exchange tube made of a relatively lightweight and
inexpensive aluminum alloy can secure sufficient performance.
[0016] The invention described in claim 3 is the heat exchanger according to the invention
of claim 1 or 2, wherein the heat-exchange tube is formed by bending an extruded member.
[0017] Thus, according to the heat exchanger of the present invention, the heat-exchange
tube is formed by bending the extruded member, so that the uneven shape is formed
readily on the inner surface of the passages.
[0018] Especially, when the extruded member is bent, the medium passages can be prevented
from becoming narrow, and the bent portions of the tube can be prevented from having
a high passage resistance. This is because the uneven inner surface of the passages
reinforces a resistance against an extra thickness or a crease involved in such bending.
[0019] The invention described in claim 4 is the heat exchanger according to the invention
of claim 3, wherein the medium passages in the heat-exchange tube are formed to protrude
on a center line which divides a cross section of the tube into two in a direction
of width thereof.
[0020] Thus, according to the heat exchanger of the present invention, the medium passages
in the heat-exchange tube are protruded on the center line which divides the cross
section of the tube into two in the direction of width thereof, so that the inner
surfaces of the passages are efficiently prevented from contacting mutually when the
extruded member is bent.
BRIEF DESCRIPTION OF THE DRAWINGS
[0021]
Fig. 1 is an external diagram showing a heat exchanger according to an embodiment
of the present invention;
Fig. 2 is an external diagram showing a heat-exchange tube according to the embodiment
of the present invention;
Fig. 3 is a cross sectional diagram showing the heat-exchange tube according to the
embodiment of the present invention; and
Fig. 4 is a cross sectional diagram showing a heat exchange tube according to an embodiment
of the present invention.
BEST MODE FOR CARRYING OUT THE INVENTION
[0022] An embodiment of the present invention will be described in detail with reference
to the accompanying drawings.
[0023] Fig. 1 is an external diagram showing a heat exchanger 1 of this embodiment. This
heat exchanger 1 is a gas cooler comprising a heat-exchange tube 2 which is provided
with fins 3, 3 and formed into a meandered shape and a pair of headers 4, 5 which
are disposed at ends of the heat-exchange tube 2, wherein carbon dioxide (CO
2), which is a non-condensation medium, is used as the medium.
[0024] The respective headers 4, 5 are provided with an inlet joint 41 for connecting a
pipe for supplying the medium or an outlet joint 51 for connecting a pipe for discharging
the medium, so that the medium supplied through the header 4 flows through the heat-exchange
tube 2 and discharged from the header 5.
[0025] In the aforesaid structure, the heat exchange of the medium is performed by heat
conducted to the heat exchange tube. And, the heat exchange is promoted by the fins
3, 3 fitted to the heat-exchange tube 2.
[0026] Respective points of the tube 2, the fins 3, 3 and the pair of headers 4, 5 are connected
by brazing.
[0027] The heat-exchange tube 2 of this embodiment is formed to have a flat shape and provided
with a plurality of medium passages 21, 21 therein as shown in Fig. 2 and Fig. 3.
[0028] The plurality of passages 21, 21 are arranged in parallel along a center line A which
divides the tube into two in a direction of width.
[0029] The medium passages 21, 21 are substantially circular in cross section and have an
uneven inner surface. The heat-exchange tube 2 is improved its pressure resistance
and heat-exchange rate by virtue of the structure of the medium passages 21, 21.
[0030] Specifically, the shape of the respective medium passages 21, 21 based on a circular
shape in order to improve the pressure resistance is gathered or corrugated in its
cross section to secure a wide contact area between the medium and the heat-exchange
tube 2.
[0031] And, the heat-exchange tube 2 is produced by bending the extruded member of an aluminum
alloy into a predetermined shape.
[0032] Here, the plurality of medium passages 21, 21 of this embodiment are formed to protrude
on the center line A, so that the inner surfaces of the respective medium passages
21, 21 are efficiently prevented from contacting each other when the extruded member
is bent.
[0033] Thus, to prevent the mutual contact of the inner surfaces of the respective medium
passages 21, 21, the gathering or corrugating intervals on the center line A may be
increased as shown in Fig. 4.
[0034] As described above, according to the heat exchanger of this embodiment, the heat-exchange
tube has a flat shape and the plurality of medium passages have a substantially circular
shape in cross section and an uneven inner surface, so that the heat-exchange tube
can be improved its pressure resistance and heat-exchange rate, and its performance
can be improved.
[0035] More specifically, in the heat-exchange tube having the plurality of medium passages,
when the medium passages are circular, the heat-exchange tube has an improved pressure
resistance as compared with one having the medium passages in a triangle or square
shape but has a drawback that its heat-exchange rate is lowered because a contact
area between the medium and the heat-exchange tube is relatively small. But, because
the inner surface of each passage is formed to have an uneven shape in this embodiment,
a large contact area between the medium and the heat-exchange tube can be secured,
so that such a drawback can be solved.
[0036] According to the heat exchanger of this embodiment, the medium is a non-condensation
medium, and the heat-exchange tube is made of an aluminum alloy, so that the heat-exchange
tube can be produced lightweight at a low cost.
[0037] More specifically, when the heat-exchange tube of an aluminum alloy is used for a
gas cooler or the like for which the medium is not condensed and requires an excellent
pressure resistance, there are drawbacks that the heat-exchange tube has a thick wall
and a considerably lowered heat-exchange rate as compared with those made of titanium
or copper. But, the present embodiment forms the plurality of medium passages with
an uneven-shaped inner surface, so that the heat-exchange tube made of a relatively
lightweight and inexpensive aluminum alloy can secure sufficient performance.
[0038] According to the heat exchanger of this embodiment, the heat-exchange tube is formed
by bending the extruded member, so that the uneven-shaped inner surface of the passage
can be formed readily.
[0039] Especially, when the extruded member is bent, the medium passages can be prevented
from becoming narrow, and the bent portions of the tube can be prevented from having
a high passage resistance. It is because the uneven-shaped inner surface of the passage
reinforces a resistance against an excess thickness or a crease involved in such bending.
[0040] According to the heat exchanger of this embodiment, the plurality of medium passages
of the heat-exchange tube are protruded on the center line which divides the cross
section of the tube into two in a direction of width, so that the inner surfaces of
the passages can be efficiently prevented from contacting mutually when the extruded
member is bent.
INDUSTRIAL APPLICABILITY
[0041] The heat exchanger according to the present invention is a heat exchanger having
a heat-exchange tube with an improved pressure resistance and heat-exchange rate and
also a next-generation heat exchanger suitable for a high-pressure medium such as
carbon dioxide which will take the place of a conventional heat-exchange medium, and
is particularly suitable for a refrigerating cycle for automobiles and consumer products.