AU2017226110B2 - Heat exchanger and air conditioner - Google Patents
Heat exchanger and air conditioner Download PDFInfo
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- AU2017226110B2 AU2017226110B2 AU2017226110A AU2017226110A AU2017226110B2 AU 2017226110 B2 AU2017226110 B2 AU 2017226110B2 AU 2017226110 A AU2017226110 A AU 2017226110A AU 2017226110 A AU2017226110 A AU 2017226110A AU 2017226110 B2 AU2017226110 B2 AU 2017226110B2
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- header part
- header
- heat exchanger
- refrigerant
- transfer tubes
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0202—Header boxes having their inner space divided by partitions
- F28F9/0204—Header boxes having their inner space divided by partitions for elongated header box, e.g. with transversal and longitudinal partitions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
- F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/06—Derivation channels, e.g. bypass
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Provided is a heat exchanger which is equipped with first heat transfer tubes (21), a first header (52), second heat transfer tubes (23), a second header (53), and a plurality of communication paths (61, 71) that each have one end connected to the first header (52) and the other end connected to the second header (53) so as to allow communication between the first header (52) and the second header (53). The height positions where said ends of the communication paths (61, 71) are connected to the first header (52) are the same as each other. The height positions where the other ends of the communication paths (61, 71) are connected to the second header (53) are different from each other.
Description
Title of Invention
Technical Field
[0001]
The present invention relates to a heat exchanger
and an air conditioner.
This application claims priority from Japanese
Patent Application No. 2016-038328 filed on February 29,
2016; the contents of which are incorporated herein by
reference.
Background Art
[0002]
A reference herein to a patent document or any
other matter identified as prior art, is not to be taken
as an admission that the document or other matter was
known or that the information it contains was part of the
common general knowledge as at the priority date of any
of the claims.
[0002a]
Where any or all of the terms "comprise",
"comprises", "comprised" or "comprising" are used in this
specification (including the claims) they are to be interpreted as specifying the presence of the stated features, integers, steps or components, but not precluding the presence of one or more other features, integers, steps or components.
[0002b]
A heat exchanger, in which a plurality of heat
transfer tubes extending in a horizontal direction are
disposed at intervals in a vertical direction and a fin is
provided on an outer surface of each heat transfer tube,
is known as a heat exchanger of an air conditioner. Both
ends of the plurality of heat transfer tubes are connected
to a pair of headers extending in the vertical direction,
respectively. Such a heat exchanger is configured such
that a refrigerant, which is introduced into one header
and is circulated in the other header via the heat
transfer tubes, turns back at the other header to return
to one header again via the heat transfer tubes, in order
to secure a flow passage length for the refrigerant.
[00031
The inside of the header at a turnback side is
partitioned into a plurality of regions with a partition
plate partitioning the inside of the header in the
vertical direction. Accordingly, a refrigerant introduced
in one region of the header via the heat transfer tubes
returns to one header on an entrance side via the plurality of heat transfer tubes connected to the other region after being introduced into the other region of the header via a connection pipe.
For example, a heat exchanger having the connection
pipe connected to a lower portion of each region of a
header, into which a refrigerant that has turned back is
introduced, is disclosed in PTL 1.
Citation List
Patent Literature
[00041
[PTL 1] Japanese Patent No. 5071597
Summary of Invention
[0005]
However, in a case where the heat exchanger is used
as an evaporator, not the entire refrigerant, which is
introduced into one region of the header via heat transfer
tubes, evaporates, and the refrigerant is in a state of a
gas-liquid two phase refrigerant, in which a liquid phase
refrigerant and a gas phase refrigerant are mixed. In a
case where such a gas-liquid two phase refrigerant is
introduced in a lower portion of the other region of the
header via the connection pipe, a liquid phase refrigerant
with a high density is unlikely to reach upper heat
transfer tubes. For this reason, a refrigerant flowing in
the upper heat transfer tubes is a liquid phase refrigerant having a lower flow rate. As a consequence, there is a problem that the heat exchanger does not show a desired performance.
[00061
It is desirable to provide a heat exchanger which
can suppress a performance decrease and an air conditioner
in which the heat exchanger is used.
[00071
In order to solve the problems, the invention adopts
the following means.
According to a first aspect of the invention, there
is provided a heat exchanger comprising a plurality of
first heat transfer tubes that extend in a horizontal
- 3a - direction to allow a refrigerant to circulate therein, and are arranged at intervals in a vertical direction, a first header part that has a cylindrical shape extending in the vertical direction and is connected to one end of each of the first heat transfer tubes in a communicating state, a plurality of second heat transfer tubes that extend in the horizontal direction to allow the refrigerant to circulate therein, and are arranged at intervals in the vertical direction, a second header part that has a cylindrical shape extending in the vertical direction and is connected to one end of each of the second heat transfer tubes in a communicating state, and a plurality of communication paths each of which has one end connected to the first header part and the other end connected to the second header part so as to allow the first header part to communicate with the second header part. A connection point of one end of each of one end of the communication paths to the first header part is at a height position which is the same for each of the communication paths, and a connection point of the other end of each of the communication paths to the second header part is at a height position different for each of the communication paths.
[0008]
In such a heat exchanger, the refrigerant introduced in the first header part via the first heat transfer tubes is introduced into the communication paths connected to the same vertical position of the first header part.
Herein, a liquid phase is likely to stay in a lower
portion of the first header part and a gas phase is likely
to stay in an upper portion of the first header part due
to a density difference between a gas and a liquid in the
refrigerant. For this reason, a difference in the gas
liquid ratios of refrigerants occurs in the vertical
direction in the first header part.
In the heat exchanger of the invention, the
plurality of communication paths connected to the second
header part are connected to the same vertical position in
the first header part. Therefore, refrigerants with
almost the same gas-liquid ratio are introduced into each
communication path. For this reason, the uniformization
of flow rates of refrigerants for the plurality of
respective communication paths can be achieved. Since the
connection points of the plurality of communication paths
to the second header part are at vertical positions
different from each other, refrigerants with almost the
same gas-liquid ratio are introduced from the plurality of
height positions in the second header part into the second
header part. Accordingly, since the refrigerants are
mixed in the second header part in the vertical direction, a gas-liquid ratio of the refrigerant over the entire area in the second header part in the vertical direction can be homogenized. Accordingly, the uniformization of mass flow rates of refrigerants introduced into the respective second heat transfer tubes can be achieved.
[0009]
The heat exchanger may further include a
partitioning plate that partitions a space in the second
header part into upper and lower regions vertically
separated from each other between connection points of the
communication paths to the second header part, which are
vertically adjacent to each other, and has a
communication-hole formed vertically therethrough.
[0010]
In a case where there is no partitioning plate, a
liquid phase with a high density is likely to go downwards
and a gas phase with a low density is likely to go upwards
in the second header part. Therefore, a difference in the
mass flow rate in the vertical direction occurs in the
second header part as a whole in some cases. On the
contrary, a refrigerant is allowed to circulate through
the respective regions and a refrigerant is likely to stay
in each region at the same time by dividing the inside of
the second header part into small regions with the
partitioning plate having the communication-hole.
Therefore, a density difference of a refrigerant in the
second header part as a whole in the vertical direction
can be reduced.
[0011]
In the heat exchanger, the connection points having
the height positions different from each other of the
plurality of communication paths may be present in the
respective regions partitioned with the partitioning plate.
[00121
Accordingly, a density difference of a refrigerant
in each region can be further reduced since the
refrigerant in each region is caused to be mixed.
[0013]
The heat exchanger may further include a connection
pipe that has a main pipe portion, of which one end is
connected to the first header part and in which a
plurality of split flow passages arranged in the
horizontal direction are formed, and branch pipe portions,
which branch off into a plurality of portions from the
other end side of the main pipe portion, in which branch
flow passages are formed so as to communicate with the
split flow passages, and each of which is connected to the
second header part. Each of the communication paths may
be a flow passage formed by each of the split flow
passages and each of the branch flow passages.
[00141
Consequently, construction is easy compared to a
case where each communication path is configured of a
separate individual connection pipe since there is one
construction point to the first header part in the case of
the branch connection pipe.
[0015]
The heat exchanger may further include a header that
has a header body which has a cylindrical shape extending
in the vertical direction and a main partition plate which
partitions an inside of the header body into upper and
lower parts. The first header part may be a portion below
the main partition plate in the header, and the second
header part may be a portion above the main partition
plate in the header.
[0016]
The heat exchanger having the first header part and
the second header part can be easily configured by forming
the first header part and the second header part with the
main partition plate in one header part.
[0017]
According to a second aspect of the invention, there
is provided an air conditioner including any one of the
heat exchangers described above.
[0018]
Accordingly, a decrease in a heat exchange
performance caused by inhomogeneous distribution of the
refrigerant is suppressed, and thus the air conditioner
with a high efficiency can be provided.
Advantageous Effects of Invention
[0019]
The heat exchanger and the air conditioner of the
invention can achieve the suppression of an efficiency
decrease.
Brief Description of Drawings
[0020]
Fig. 1 is an overall configuration view of an air
conditioner according to a first embodiment of the
invention.
Fig. 2 is a longitudinal sectional view of a heat
exchanger according to the first embodiment of the
invention.
Fig. 3 is a perspective view of the heat exchanger
according to the first embodiment of the invention.
Fig. 4 is a side view of a turnback side header and
a branch connection pipe of a heat exchanger according to
a second embodiment of the invention.
Fig. 5A is a view illustrating a sectional shape of
a flow passage of a main pipe portion in the branch
connection pipe of the heat exchanger according to the second embodiment of the invention.
Fig. 5B is a view illustrating the sectional shape
of the flow passage of the main pipe portion in the branch
connection pipe of the heat exchanger according to the
second embodiment of the invention.
Fig. 6 is a side view of a turnback side header and
a connection pipe of a heat exchanger according to a third
embodiment of the invention.
Fig. 7 is a side view of a turnback side header and
a connection pipe of a heat exchanger according to a
fourth embodiment of the invention.
Fig. 8 is a side view of a turnback side header and
a connection pipe of a heat exchanger according to a fifth
embodiment of the invention.
Description of Embodiments
[0021]
Hereinafter, an air conditioner including a heat
exchanger according to a first embodiment of the invention
will be described with reference to Figs. 1 to 3.
As illustrated in Fig. 1, an air conditioner 1
includes a compressor 2, an indoor heat exchanger 3 (heat
exchanger 10), an expansion valve 4, an outdoor heat
exchanger 5 (heat exchanger 10), a four-way valve 6, and a
pipe 7 that connects the configuration elements together,
and a refrigerant circuit formed of the configuration elements is configured.
[00221
The compressor 2 compresses a refrigerant and
supplies the compressed refrigerant to the refrigerant
circuit.
The indoor heat exchanger 3 performs heat exchange
between the refrigerant and indoor air. The indoor heat
exchanger 3 is used as an evaporator to absorb heat from
the inside during cooling operation, and is used as a
condenser to radiate heat to the inside during heating
operation.
The expansion valve 4 reduces a pressure by
expanding the high-pressure refrigerant liquefied by the
condenser exchanging heat.
The outdoor heat exchanger 5 performs heat exchange
between the refrigerant and outdoor air. The outdoor heat
exchanger is used as a condenser to radiate heat to the
outside during cooling operation and is used as an
evaporator to absorb heat from the outside during heating
operation.
The four-way valve 6 switches between directions
where a refrigerant circulates during heating operation
and during cooling operation. Consequently, a refrigerant
circulates in the compressor 2, the outdoor heat exchanger
5, the expansion valve 4, and the indoor heat exchanger 3 in this order during cooling operation. On the other hand, a refrigerant circulates in the compressor 2, the indoor heat exchanger 3, the expansion valve 4, and the outdoor heat exchanger 5 in this order during heating operation.
[0023]
Next, the heat exchangers 10 which are used as the
indoor heat exchanger 3 and the outdoor heat exchanger 5
will be described with reference to Figs. 2 and 3.
The heat exchangers 10 each include a plurality of
heat transfer tubes 20, a plurality of fins 28, a pair of
headers 30, a first connection pipe 60, and a second
connection pipe 70.
[0024]
The heat transfer tubes 20 are tubular members
linearly extending in a horizontal direction, and flow
passages through which a refrigerant circulates are formed
therein. The plurality of heat transfer tubes 20 are
arranged at intervals in a vertical direction, and are
disposed so as to be parallel to each other.
In the embodiment, the heat transfer tubes 20 each
have a flat tubular shape, and the plurality of flow
passages arranged in the horizontal direction orthogonal
to an extending direction of the heat transfer tubes 20
are formed inside the heat transfer tubes 20. The
plurality of flow passages are arranged so as to be parallel to each other. Consequently, a sectional shape orthogonal to the extending direction of the heat transfer tubes 20 is a flat shape of which a longitudinal direction is the horizontal direction orthogonal to the extending direction of the heat transfer tubes 20.
[0025]
The fins 28 each are disposed between the heat
transfer tubes 20 arranged as described above, and extend
in a so-called corrugated shape so as to be alternately in
contact with the vertically nearby heat transfer tubes 20
as facing the extending direction of each of the heat
transfer tubes 20 in the embodiment. Without being
limited thereto, the shapes of the fins 28 may be any
shape insofar as the fins are provided so as to protrude
from outer peripheral surfaces of the heat transfer tubes
20.
[0026]
At both ends of the plurality of heat transfer tubes
20, the pair of headers 30 is provided such that the heat
transfer tubes 20 are sandwiched therebetween. One of the
pair of headers 30 is set as an entrance side header 40,
which is an entrance of a refrigerant from the outside
into the heat exchanger 10, and the other one is set as a
turnback side header 50 for a refrigerant to turn back in
the heat exchanger 10.
[00271
The entrance side header 40 is a cylindrical member
extending in the vertical direction. An upper end and a
lower end of the entrance side header are closed and the
inside of the entrance side header is partitioned into two
upper and lower regions with a partition plate 41. The
lower region partitioned with the partition plate 41 is
set as a lower entry region 42 and the upper region is set
as an upper entry region 43. The lower entry region 42
and the upper entry region 43 are in a state of not
communicating with each other in the entrance side header
40. The lower entry region 42 and the upper entry region
43 each are connected to the pipe 7 configuring the
refrigerant circuit.
Herein, out of the plurality of heat transfer tubes
20, the heat transfer tubes 20 connected to the lower
entry region 42 in a communicating state are set as first
heat transfer tubes 21, and the heat transfer tubes 20
connected to the upper entry region 43 in a communicating
state are set as second heat transfer tubes 23.
[0028]
The turnback side header 50 includes a header body
51 and a main partition plate 58.
The header body 51 is a cylindrical member extending
in the vertical direction, and an upper end and a lower end of the header body are closed. The main partition plate 58 is provided in the header body 51, and partitions a space in the header body 51 into two upper and lower regions. A portion below the main partition plate 58 of the header body 51 is set as a first header part 52, and a portion above the main partition plate 58 of the header body 51 is set as a second header part 53. That is, in the embodiment, the first header part 52 and the second header part 53 each of which has a space therein are formed in the turnback side header 50 by the inside of the header body 51 being partitioned with the main partition plate 58. In other words, the turnback side header 50 is configured with the first header part 52 and the second header part 53.
[0029]
The plurality of first heat transfer tubes 21 each
are connected to the first header part 52 so as to be in a
communicating state with the inside of the first header
part 52. That is, the heat transfer tubes 20 connected to
the first header part 52 are set as the first heat
transfer tubes 21.
The plurality of second heat transfer tubes 23 each
are connected to the second header part 53 so as to be in
a communicating state with the inside of the second header
part 53. That is, the heat transfer tubes 20 connected to the second header part 53 are set as the second heat transfer tubes 23.
[0030]
The first connection pipe 60 is a tubular member in
which a flow passage is formed. One end of the first
connection pipe is connected to the first header part 52
in a communicating state with the inside of the first
header part 52, and the other end is connected to the
second header part 53 in a communicating state with the
inside of the second header part 53. More specifically,
one end of the first connection pipe 60 is connected to an
upper portion of the first header part 52. In addition,
the other end of the first connection pipe 60 is connected
to a lower portion of the second header part 53. In the
embodiment, the flow passage in the first connection pipe
is set as a first communication path 61 (communication
path) that connects the first header part 52 and the
second header part 53 together.
[0031]
The second connection pipe 70 is a tubular member in
which a flow passage is formed. One end of the second
connection pipe is connected to the first header part 52
in a communicating state with the inside of the first
header part 52 as in the first connection pipe 60. On the
other hand, the other end of the second connection pipe 70 is connected to the second header part in a communicating state with the inside of the second header part 53. More specifically, one end of the second connection pipe 70 is connected to the upper portion of the first header part 52.
In addition, the other end of the second connection pipe
is connected to an upper portion of the second header
part 53. In the embodiment, the flow passage in the
second connection pipe 70 is set as a second communication
path 71 (communication path) that connects the first
header part 52 and the second header part 53 together.
[00321
Herein, a connection point of the first connection
pipe 60 to the first header part 52 and a connection point
of the second connection pipe 70 to the first header part
52 are at the same vertical position, in the embodiment.
That is, the connection point of the first connection pipe
to the first header part 52 is disposed so as to be
adjacent to or to be spaced apart from the connection
point of the second connection pipe 70 to the first header
part 52 in the horizontal direction, and has the same
vertical position as the connection point of the second
connection pipe to the first header part.
"The same vertical position" is not limited to a
case where the vertical position of a center of the
connection point of the first connection pipe 60 to the first header part 52 and the vertical position of a center of the connection point of the second connection pipe 70 to the first header part 52 are the same, and it is sufficient that at least a part of the connection point of the first connection pipe 60 to the first header part 52 and a part of the connection point of the second connection pipe 70 to the first header part 52 overlap each other in the vertical direction.
[0033]
In the embodiment, the connection point of the
second connection pipe 70 to the second header part 53 is
provided above the connection point of the first
connection pipe 60 to the second header part 53, that is,
the connection point of the first connection pipe 60 to
the second header part 53 and the connection point of the
second connection pipe 70 to the second header part 53 are
at vertical positions different from each other.
[0034]
Next, operation and effects in a case where the heat
exchanger 10 is used as an evaporator will be described.
In a case where the heat exchanger 10 is the indoor heat
exchanger 3, the heat exchanger is used as an evaporator
during cooling operation of the air conditioner 1, and in
a case where the heat exchanger is the outdoor heat
exchanger 5, the heat exchanger is used as an evaporator during heating operation of the air conditioner 1.
[0035]
When the heat exchanger 10 is used as an evaporator,
a gas-liquid two phase refrigerant having a high liquid
phase content is supplied from the pipe 7 to the lower
entry region 42 of the entrance side header 40 illustrated
in Fig. 2. The refrigerant is divided and supplied to the
plurality of first heat transfer tubes 21 in the lower
entry region 42, and exchanges heat with the external
atmosphere of the first heat transfer tubes 21 in the
process of circulating in the first heat transfer tubes 21,
thereby causing evaporation. Consequently, the
refrigerant supplied from the first heat transfer tubes 21
into the first header part 52 of the turnback side header
becomes a gas-liquid two phase refrigerant, in which
the proportion of a liquid phase has dropped, by some of
the refrigerant changing from the liquid phase to a gas
phase.
[0036]
Out of gas-liquid two phase refrigerants supplied
into the first header part 52, a refrigerant with a high
liquid phase content and a high density gathers at the
lower portion of the first header part 52 due to gravity,
and a refrigerant with a high gas phase content and a low
density gathers at the upper portion of the first header part 52. That is, in the first header part 52, the gas liquid ratio (density) of a refrigerant differs according to a vertical position. Herein, if the connection point of the first connection pipe 60 to the first header part
52 and the connection point of the second connection pipe
to the first header part 52 are different from each
other in the vertical direction, the gas-liquid ratios of
refrigerants introduced into the first connection pipe 60
and the second connection pipe 70 are different from each
other. As a consequence, as a result of a refrigerant
with a high density being introduced into one of the first
connection pipe 60 and the second connection pipe 70,
which is connected to a lower part of the first header
part 52, the mass flow rate of the refrigerant becomes
higher. In addition, as a result of a refrigerant with a
low density being introduced into one of the first
connection pipe 60 and the second connection pipe 70,
which is connected to an upper part of the first header
part 52, the mass flow rate of the refrigerant becomes
lower.
[00371
On the contrary, in the embodiment, the connection
point of the first connection pipe 60 to the first header
part 52 and the connection point of the second connection
pipe 70 to the first header part 52 are at the same vertical position. For this reason, refrigerants having almost the same gas-liquid ratio are introduced into the first connection pipe 60 and the second connection pipe 70 respectively. As a consequence, the gas-liquid ratios of the refrigerants introduced into the vertical positions of the second header part 53 different from each other via the first connection pipe 60 and the second connection pipe 70 respectively are almost the same. That is, the uniformization of the mass flow rates of refrigerants circulating in the first connection pipe 60 and the second connection pipe 70 is achieved.
[0038]
In the embodiment, refrigerants having almost the
same gas-liquid ratio are introduced into the second
header part 53 from a plurality of height positions of the
second header part 53. Accordingly, since the
refrigerants are mixed in the second header part 53 in the
vertical direction, a gas-liquid ratio of the refrigerant
over the entire area in the second header part 53 in the
vertical direction can be homogenized. Accordingly, the
uniformization of mass flow rates of refrigerants
introduced into the respective second heat transfer tubes
23 can be achieved.
[0039]
After then, a refrigerant introduced in the second header part 53 via the first connection pipe 60 or the second connection pipe 70 is diverted to the plurality of second heat transfer tubes 23 connected thereto and circulates in the second heat transfer tubes 23. Then, the refrigerant again causes evaporation by exchanging heat with the external atmosphere of the second heat transfer tubes 23 in the process of circulating in the second heat transfer tubes 23. Consequently, in the second heat transfer tubes 23, the remaining liquid phase in the refrigerant changes to the gas phase and the refrigerant in a gas phase state is supplied to the upper entry region 43 of the entrance side header 40. Then, the refrigerant is introduced from the upper entry region 43 to the pipe 7, thereby circulating in the refrigerant circuit.
[0040]
As described above, in the heat exchanger 10 of the
invention, the first communication path 61 of the first
connection pipe 60 and the second communication path 71 of
the second connection pipe 70, each of which is connected
to one of the second header part 53, are connected to the
first header part 52 at the same vertical position.
Therefore, refrigerants with almost the same gas phase
liquid phase ratio are introduced into respective
communication paths 102. For this reason, the uniformization of flow rates of refrigerants for the plurality of respective communication paths 102 can be achieved. Refrigerants introduced in the second header part 53 via the first connection pipe 60 and the second connection pipe 70 are caused to be mixed in the second header part 53 in the vertical direction. Accordingly, the homogenization of a gas-liquid ratio in the second header part 53 can be further achieved. As a consequence, for example, in a case where the heat exchanger 10 is used as an air conditioner, a cooling performance and a heating performance are not impaired.
[0041]
Next, a heat exchanger 80 according to a second
embodiment of the invention will be described with
reference to Fig. 4, Fig. 5A, and Fig. 5B. In the second
embodiment, the same configuration elements as the first
embodiment will be assigned with the same reference signs
as the first embodiment, and the detailed description
thereof will be omitted.
As illustrated in Fig. 4, the heat exchanger 80 of
the second embodiment is different from the heat exchanger
of the first embodiment in that one branch connection pipe
81 is included instead of the first connection pipe 60 and
the second connection pipe 70 of the first embodiment.
[00421
The branch connection pipe 81 has a main pipe
portion 82 and a plurality of (two, in the embodiment)
branch pipe portions 85.
One end of the main pipe portion 82 is connected to
the first header part 52. In the first header part 52,
two split flow passages 83, which are formed by splitting
the inside of the first header part 52 in the horizontal
direction into two regions, are formed as illustrated in
Fig. 5A and Fig. 5B. The split flow passages 83 are
arranged in the horizontal direction so as to extend from
one end to the other end of the main pipe portion 82. As
illustrated in Fig. 5A, the main pipe portion 82 may have
a structure in which the two split flow passages 83 are
formed by providing a split wall portion 84 in the middle
of a circular section of the flow passage in the
horizontal direction. In addition, as illustrated in Fig.
5B, the main pipe portion may have a structure in which
the split flow passages 83 obtained by linearly cutting
out a part of the circular section of the flow passage are
provided so as to be arranged side by side via the split
wall portion 84 configuring the linear portion.
[0043]
The two branch pipe portions 85 are provided so as
to branch off into a plurality of portions from the other
end side of the main pipe portion 82. One branch pipe portion of the two branch pipe portions 85 is connected to the lower portion of the second header part 53. The other branch pipe portion of the two branch pipe portions 85 is connected to the upper portion of the second header part
53. In addition, branch flow passages 86, which are flow
passages inside the respective branch pipe portions 85,
communicate with the split flow passages 83 in the main
pipe portion 82 in a one-to-one relationship. Accordingly,
out of the two split flow passages 83 of the main pipe
portion 82, one split flow passage 83 is in a
communicating state with the lower portion of the second
header part 53 via one branch flow passage 86, that is,
the first communication path 61 that allows the first
header part 52 to communicate with the lower portion of
the second header part 53 by means of one split flow
passage 83 and one branch flow passage 86 is formed. In
addition, the other split flow passage 83 is in a
communicating state with the inside of the upper portion
of the second header part 53 via the other branch flow
passage 86, that is, the second communication path 71 that
allows the first header part 52 to communicate with the
upper portion of the second header part 53 by means of the
other split flow passage 83 and the other branch flow
passage 86 is formed.
[00441
In such a heat exchanger 80 of the second embodiment,
the two split flow passages 83 in the main pipe portion 82
of the branch connection pipe 81 are arranged in the
horizontal direction side by side. Therefore,
refrigerants with almost the same density are introduced
into the two split flow passages 83. Then, the
refrigerants are introduced into the lower portion and the
upper portion of the second header part 53 via the
respective branch flow passages 86. Thus, the
homogenization of mass flow rates of refrigerants
introduced into the second header part 53 can be achieved
as in the first embodiment.
[0045]
In addition, since there is only one connection
point to the first header part 52, construction can be
performed more easily compared to a case where the first
connection pipe 60 and the second connection pipe 70 are
separately provided as in the first embodiment.
Although one of the two branch pipe portions 85 is
connected to the lower portion of the second header part
53 and the other one is connected to the upper portion of
the second header part 53 in the embodiment, it is
sufficient that the connection points of the two branch
pipe portions 85 to the second header part 53 are
different from each other in the vertical direction.
[0046]
Next, a heat exchanger 90 according to a third
embodiment of the invention will be described with
reference to Fig. 6. In the third embodiment, the same
configuration elements as the first embodiment will be
assigned with the same reference signs as the first
embodiment, and the detailed description thereof will be
omitted.
As illustrated in Fig. 6, the heat exchanger 90 of
the third embodiment is different from the first
embodiment in that a partitioning plate 91 is further
included in the second header part 53.
[0047]
The partitioning plate 91 is provided at a vertical
position between the first connection pipe 60 and the
second connection pipe 70 in the second header part 53,
and partitions the inside of the second header part 53
into two upper and lower regions. A lower region, out of
the two regions, is set as a second header lower region 93.
The other end of the first connection pipe 60 is connected
to the second header lower region 93 in a communicating
state. In addition, an upper region, out of the two
regions, is set as a second header upper region 94. The
other end of the second connection pipe 70 is connected to
the second header upper region 94 in a communicating state.
[0048]
The partitioning plate 91 has a communication-hole
92 formed in the vertical direction. The communication
hole 92 allows the second header lower region 93 and the
second header upper region 94, which are partitioned with
the partitioning plate 91, to be in a communicating state.
A position at which the communication-hole 92 is formed
may be the middle of the partitioning plate 91 in the
horizontal direction, or may be a position off the middle.
[0049]
In a case where there is no partitioning plate 91, a
liquid phase with a high density is likely to go downwards
and a gas phase with a low density is likely to go upwards
in the second header part 53. Therefore, a difference in
the mass flow rate in the vertical direction occurs in the
second header part 53 as a whole. On the contrary, in the
embodiment, refrigerants are allowed to circulate through
the respective regions and a refrigerant of each region is
likely to stay in each region at the same time by dividing
the inside of the second header part 53 into small regions
with the partitioning plate 91 having the communication
hole 92. That is, the movement of the gas phase content
of a refrigerant from the second header lower region 93 to
the second header upper region 94 is inhibited by the
partitioning plate 91. On the other hand, the movement of the liquid phase content of a refrigerant from the second header upper region 94 to the second header lower region
93 is inhibited by the partitioning plate 91. As a
consequence, a tendency in which the liquid phase is
likely to stay in the lower portion and the gas phase is
likely to stay in the upper portion in the second header
part 53 as a whole can be suppressed. Accordingly, a
density difference of a refrigerant in the second header
part 53 as a whole in the vertical direction can be
reduced.
[0050]
Next, a heat exchanger 100 according to a fourth
embodiment of the invention will be described with
reference to Fig. 7. In the fourth embodiment, the same
configuration elements as the first and third embodiments
will be assigned with the same reference signs as the
embodiments, and the detailed description thereof will be
omitted.
As illustrated in Fig. 7, the heat exchanger 100 of
the embodiment has two partitioning plates 91 provided in
the second header part 53. That is, the partitioning
plates 91 are provided at intervals in the vertical
direction, and accordingly a region in the second header
part 53 is partitioned into three regions in the vertical
direction. The same communication-holes 92 as in the third embodiment are formed in the partitioning plates 91.
[0051]
Three connection pipes 101 that connect the first
header part 52 and the three regions in the second header
part 53 together respectively are provided in the
embodiment. A flow passage in each of the connection
pipes 101 is set as each of the communication paths 102
allowing the first header part 52 to communicate with the
second header part 53.
The connection points of the three connection pipes
101 to the first header part 52 are at the same vertical
position, as in the first embodiment. The other end of
the first connection pipe 101, out of the three connection
pipes 101, is connected to the lowermost region, out of
the three regions in the second header part 53. The other
end of the second connection pipe 101, out of the three
connection pipes 101, is connected to the middle region,
out of the three regions in the second header part 53.
The other end of the third connection pipe 101, out of the
three connection pipes 101, is connected to the uppermost
region, out of the three regions in the second header part
53.
[00521
In the embodiment, since the inside of the second
header part 53 is divided into the three regions by the partitioning plate 91, a deviation in the density of a refrigerant in the second header part 53 can be suppressed more than the third embodiment.
The inside of the second header part 53 may be
partitioned into four or more regions and four or more
connection pipes 101 may be provided according to the
number of the partitioned regions. A density difference
of a refrigerant in the second header part 53 as a whole
can be further reduced by subdividing the inside of the
second header part 53.
[0053]
Next, a heat exchanger 110 according to a fifth
embodiment of the invention will be described with
reference to Fig. 8. In the fifth embodiment, the same
configuration elements as the first and third embodiments
will be assigned with the same reference signs as the
first embodiment, and the detailed description thereof
will be omitted.
[0054]
As illustrated in Fig. 8, the heat exchanger 110 of
the embodiment has one partitioning plate 91 provided in
the second header part 53, as in the third embodiment.
Accordingly, the inside of second header part 53 is
partitioned into two regions in the vertical direction.
The same communication-hole 92 as in the third embodiment is formed in the partitioning plate 91.
[0055]
Six connection pipes 101 that connect the first
header part 52 and the second header part 53 together are
provided in the embodiment. The communication paths 102
are formed in the connection pipes 101, and the connection
points of all the communication paths to the first header
part 52 are at the same vertical position.
In addition, the other end of each of three
connection pipes 101, out of the six connection pipes 101,
is connected to the second header lower region 93. The
connection points of the three connection pipes 101 to the
second header lower region 93 are at vertical positions
different from each other.
The other end of each of remaining three connection
pipes 101, out of the six connection pipes 101, is
connected to the second header upper region 94. The
connection points of the three connection pipes 101 to the
second header upper region 94 are at vertical positions
different from each other.
[0056]
In the heat exchanger 110 of the embodiment having
the configuration described above, a refrigerant is
introduced into the second header lower region 93 and the
second header upper region 94 in the second header part 53 from the vertical positions different from each other.
Accordingly, the mixing of a refrigerant in the second
header lower region 93 and the second header upper region
94 can be further caused.
Although an example in which one partitioning plate
91 is provided is described in the embodiment, the inside
of the second header part 53 may be partitioned into three
or more regions with two or more partitioning plates 91.
In addition, the other end of each of four or more
connection pipes 101, without being limited to only three,
may be connected to each region in the second header part
53.
[0057]
Although the embodiments of the invention are
described, the invention is not limited thereto, and can
be modified as appropriate without departing from the
technical scope of the invention.
Reference Signs List
[0058]
1 air conditioner
2 compressor
3 indoor heat exchanger
4 expansion valve
5 outdoor heat exchanger
6 four-way valve
7 pipe
heat exchanger
heat transfer tube
21 first heat transfer tube
23 second heat transfer tube
28 fin
header
entrance side header
41 partition plate
42 lower entry region
43 upper entry region
turnback side header
51 header body
52 first header part
53 second header part
58 main partition plate
first connection pipe
61 first communication path
second connection pipe
71 second communication path
heat exchanger
81 branch connection pipe
82 main pipe portion
83 split flow passage
84 split wall portion heat exchanger
91 partitioning plate
92 communication-hole
93 second header lower region
94 second header upper region
100 heat exchanger
101 connection pipe
102 communication path
110 heat exchanger
Claims (6)
- Claims[Claim 1]A heat exchanger comprising:a plurality of first heat transfer tubes that extendin a horizontal direction to allow a refrigerant tocirculate therein, and are arranged at intervals in avertical direction;a first header part that has a cylindrical shapeextending in the vertical direction and is connected toone end of each of the first heat transfer tubes in acommunicating state;a plurality of second heat transfer tubes thatextend in the horizontal direction to allow therefrigerant to circulate therein, and are arranged atintervals in the vertical direction;a second header part that has a cylindrical shapeextending in the vertical direction and is connected toone end of each of the second heat transfer tubes in acommunicating state; anda plurality of communication paths each of which hasone end connected to the first header part and the otherend connected to the second header part so as to allow thefirst header part to communicate with the second headerpart, wherein a connection point of one end of each of the communication paths to the first header part is at a height position which is the same for each of the communication paths, and a connection point of the other end of each of the communication paths to the second header part is at a height position different for each of the communication paths.
- [Claim 2]The heat exchanger according to Claim 1, furthercomprising:a partitioning plate that partitions a space in thesecond header part into upper and lower regions verticallyseparated from each other between connection points of thecommunication paths to the second header part, which arevertically adjacent to each other, and has acommunication-hole formed vertically therethrough.
- [Claim 3]The heat exchanger according to Claim 2,wherein the connection points having the heightpositions different from each other of the plurality ofcommunication paths are present in the respective regionspartitioned with the partitioning plate.
- [Claim 4]The heat exchanger according to any one of Claims 1 to 3, further comprising: a connection pipe that has a main pipe portion, of which one end is connected to the first header part and in which a plurality of split flow passages arranged in the horizontal direction are formed, and branch pipe portions, which branch off into a plurality of portions from the other end side of the main pipe portion, in which branch flow passages are formed so as to communicate with the split flow passages, and each of which is connected to the second header part, wherein each of the communication paths is a flow passage formed by each of the split flow passages and each of the branch flow passages.
- [Claim 5]The heat exchanger according to any one of Claims 1to 4, further comprising:a header that has a header body which has acylindrical shape extending in the vertical direction anda main partition plate which partitions an inside of theheader body into upper and lower parts,wherein the first header part is a portion below themain partition plate in the header, andthe second header part is a portion above the mainpartition plate in the header.
- [Claim 6]An air conditioner comprising the heat exchangeraccording to any one of Claims 1 to 5.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2016038328A JP6611335B2 (en) | 2016-02-29 | 2016-02-29 | Heat exchanger and air conditioner |
| JP2016-038328 | 2016-02-29 | ||
| PCT/JP2017/005921 WO2017150219A1 (en) | 2016-02-29 | 2017-02-17 | Heat exchanger and air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU2017226110A1 AU2017226110A1 (en) | 2018-07-12 |
| AU2017226110B2 true AU2017226110B2 (en) | 2020-04-16 |
Family
ID=59744175
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2017226110A Active AU2017226110B2 (en) | 2016-02-29 | 2017-02-17 | Heat exchanger and air conditioner |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP3382316B1 (en) |
| JP (1) | JP6611335B2 (en) |
| CN (1) | CN108474633A (en) |
| AU (1) | AU2017226110B2 (en) |
| WO (1) | WO2017150219A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6521116B1 (en) | 2018-01-31 | 2019-05-29 | ダイキン工業株式会社 | Refrigeration apparatus having a heat exchanger or heat exchanger |
| JP6466047B1 (en) * | 2018-08-22 | 2019-02-06 | 三菱電機株式会社 | Heat exchanger and air conditioner |
| JP7048905B2 (en) * | 2020-03-06 | 2022-04-06 | ダイキン工業株式会社 | Transport refrigeration equipment and transport containers |
| JP6880277B1 (en) * | 2020-04-08 | 2021-06-02 | 三菱重工サーマルシステムズ株式会社 | Evaporator |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015111220A1 (en) * | 2014-01-27 | 2015-07-30 | 三菱電機株式会社 | Heat exchanger and air conditioning device |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004177041A (en) * | 2002-11-28 | 2004-06-24 | Matsushita Electric Ind Co Ltd | Heat exchanger |
| DK2212639T3 (en) * | 2007-10-12 | 2016-09-19 | Carrier Corp | Heat exchange with baffelforgreninger |
| JP5693346B2 (en) * | 2010-07-30 | 2015-04-01 | 株式会社ケーヒン・サーマル・テクノロジー | Evaporator |
| AU2012208123B2 (en) * | 2011-01-21 | 2015-05-07 | Daikin Industries, Ltd. | Heat exchanger and air conditioner |
| JP5376010B2 (en) * | 2011-11-22 | 2013-12-25 | ダイキン工業株式会社 | Heat exchanger |
| CN103267390B (en) * | 2013-05-06 | 2016-03-02 | 广东美的制冷设备有限公司 | Parallel-flow heat exchanger and air-conditioner |
| JP2015052444A (en) * | 2013-09-09 | 2015-03-19 | ダイキン工業株式会社 | Heat exchanger |
| JP5741657B2 (en) * | 2013-09-11 | 2015-07-01 | ダイキン工業株式会社 | Heat exchanger and air conditioner |
| JP5754490B2 (en) * | 2013-09-30 | 2015-07-29 | ダイキン工業株式会社 | Heat exchanger and air conditioner |
| JP6259703B2 (en) * | 2014-04-10 | 2018-01-10 | 株式会社ケーヒン・サーマル・テクノロジー | Capacitor |
-
2016
- 2016-02-29 JP JP2016038328A patent/JP6611335B2/en active Active
-
2017
- 2017-02-17 CN CN201780005081.6A patent/CN108474633A/en active Pending
- 2017-02-17 EP EP17759688.9A patent/EP3382316B1/en active Active
- 2017-02-17 WO PCT/JP2017/005921 patent/WO2017150219A1/en not_active Ceased
- 2017-02-17 AU AU2017226110A patent/AU2017226110B2/en active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015111220A1 (en) * | 2014-01-27 | 2015-07-30 | 三菱電機株式会社 | Heat exchanger and air conditioning device |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2017226110A1 (en) | 2018-07-12 |
| WO2017150219A1 (en) | 2017-09-08 |
| EP3382316A1 (en) | 2018-10-03 |
| EP3382316A4 (en) | 2018-12-05 |
| EP3382316B1 (en) | 2019-08-28 |
| JP6611335B2 (en) | 2019-11-27 |
| JP2017155990A (en) | 2017-09-07 |
| CN108474633A (en) | 2018-08-31 |
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