CN109751752A - A kind of heat exchanger and air conditioner - Google Patents
A kind of heat exchanger and air conditioner Download PDFInfo
- Publication number
- CN109751752A CN109751752A CN201910023148.XA CN201910023148A CN109751752A CN 109751752 A CN109751752 A CN 109751752A CN 201910023148 A CN201910023148 A CN 201910023148A CN 109751752 A CN109751752 A CN 109751752A
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- CN
- China
- Prior art keywords
- supercooling
- heat exchanger
- bypass pipe
- pipeline section
- heat exchange
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000004781 supercooling Methods 0.000 claims abstract description 222
- 239000003507 refrigerant Substances 0.000 claims description 135
- 238000010438 heat treatment Methods 0.000 abstract description 56
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 27
- 238000004378 air conditioning Methods 0.000 description 13
- 238000000034 method Methods 0.000 description 11
- 230000008569 process Effects 0.000 description 10
- 238000005057 refrigeration Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 5
- 238000009833 condensation Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 230000003631 expected effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
-
- 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
-
- 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
- F25B41/00—Fluid-circulation arrangements
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention belongs to technical field of heat exchangers, disclose a kind of heat exchanger and air conditioner, heat exchanger includes set of heat exchange tubes, supercooling tube group, supercooling bypass pipe, shunts bypass pipe, supercooling check valve and shunt check valve, supercooling tube group and the set of heat exchange tubes are connected in series, supercooling tube group and set of heat exchange tubes constitute the flow path of single-row arrangement, supercooling bypass pipe is arranged in parallel with supercooling tube group, and supercooling check valve is set on supercooling bypass pipe, is shunted check valve and is set on shunting bypass pipe.The beneficial effects of the invention are as follows heat exchanger is realized in heating operation, realizes that heat exchanging device is shunted by check valve, system complexity can be reduced, mitigate the voltage loss generated in heating by supercooling tube group, to improve system heat exchange efficiency.
Description
Technical field
The present invention relates to technical field of heat exchangers, in particular to a kind of heat exchanger and air conditioner.
Background technique
Existing heat exchanger is shunted if necessary, generallys use isocon or current divider carries out diversion design, still
Conventional shunting mode is distinguished without direction, and same pipeline is passed through when carrying out refrigerating operaton and carrying out heating operation, is being changed
When hot device carries out refrigerating operaton, by super-cooling pipeline, meet refrigerating operaton demand, and when carrying out heating operation, it still passes through
Super-cooling pipeline can be passed through, will lead to increase voltage loss, and then reduce system heat exchange efficiency.
Summary of the invention
The embodiment of the invention provides a kind of heat exchanger and air conditioners, to solve heat exchanger heat exchange efficiency when heating operation
The problem of reduction.In order to which some aspects of the embodiment to disclosure have a basic understanding, simple summary is shown below.
The summarized section is not extensive overview, nor to determine key/critical component or describe the protection model of these embodiments
It encloses.Its sole purpose is that some concepts are presented with simple form, in this, as the preamble of following detailed description.
According to a first aspect of the embodiments of the present invention, a kind of heat exchanger is provided.
In some optional embodiments, above-mentioned heat exchanger, including set of heat exchange tubes;
Supercooling tube group is connected in series with set of heat exchange tubes;And supercooling tube group and set of heat exchange tubes constitute the stream of single-row arrangement
Road;
Bypass pipe is subcooled, bypass pipe is subcooled and the first pipeline section of supercooling tube group and set of heat exchange tubes is connected in parallel;
Bypass pipe is shunted, it is in parallel at least partly pipeline section of the second pipeline section of the first pipeline section and set of heat exchange tubes to shunt bypass pipe
Connection;
Check valve is subcooled, is set on supercooling bypass pipe, the conducting direction that check valve is subcooled is limited to by supercooling bypass pipe
The sys node with the sys node of supercooling tube group flow direction and the first pipeline section;
Check valve is shunted, is set to and shunts on bypass pipe, the conducting direction for shunting check valve is limited to by set of heat exchange tubes
With the sys node of the sys node flow direction and at least partly pipeline section of the second pipeline section of the first pipeline section.
Optionally, the quantity of the heat exchanger tube of the first pipeline section of supercooling bypass pipe set of heat exchange tubes in parallel, is less than or equal to
The quantity of the heat exchanger tube of its supercooling tube group in parallel.
Optionally, the quantity of the heat exchanger tube of the first pipeline section of supercooling bypass pipe set of heat exchange tubes in parallel, is less than or equal to
Shunt the quantity of the heat exchanger tube of at least partly pipeline section of bypass pipe the second pipeline section in parallel.
Optionally, the quantity of the heat exchanger tube of supercooling bypass pipe supercooling tube group in parallel, is greater than or equal to and shunts bypass pipe
The heat exchanger tube of at least partly pipeline section of the second pipeline section in parallel quantity.
Optionally, be subcooled bypass pipe quantity be it is multiple, multiple supercooling bypass pipes are connected in parallel.
Optionally, the quantity of the heat exchanger tube of the first pipeline sections of multiple supercooling bypass pipes set of heat exchange tubes in parallel it is identical or
It is not identical.
Optionally, shunt bypass pipe quantity be it is multiple, multiple supercooling bypass pipes are connected in parallel.
Optionally, the quantity of the heat exchanger tube of multiple the second pipeline sections for shunting bypass pipes set of heat exchange tubes in parallel it is identical or
It is not identical.
According to a second aspect of the embodiments of the present invention, a kind of air conditioner is provided.
In some optional embodiments, above-mentioned air conditioner includes indoor heat exchanger, outdoor heat exchanger, compressor and four-way valve
The refrigerant circulation flow path connected and composed;Wherein, outdoor heat exchanger is the heat exchanger as described in above-mentioned any alternative embodiment, heat exchange
The set of heat exchange tubes of device is connected with compressor, and supercooling tube group is connected with indoor heat exchanger.
According to a third aspect of the embodiments of the present invention, it is further provided another air conditioner.
In some optional embodiments, above-mentioned air conditioner includes indoor heat exchanger, outdoor heat exchanger, compressor and four-way valve
The refrigerant circulation flow path connected and composed;Wherein, indoor heat exchanger is the heat exchanger as described in above-mentioned any alternative embodiment, heat exchange
The set of heat exchange tubes of device is connected with compressor, and supercooling tube group is connected with indoor heat exchanger.
Technical solution provided in an embodiment of the present invention can include the following benefits: realize heat exchanger in heating operation
When, it realizes that heat exchanging device is shunted by check valve, system complexity can be reduced, mitigate and pass through supercooling tube in heating
Group and the voltage loss generated, to improve system heat exchange efficiency.
It should be understood that above general description and following detailed description be only it is exemplary and explanatory, not
It can the limitation present invention.
Detailed description of the invention
The drawings herein are incorporated into the specification and forms part of this specification, and shows and meets implementation of the invention
Example, and be used to explain the principle of the present invention together with specification.
Fig. 1 is a kind of structural schematic diagram of heat exchanger shown according to an exemplary embodiment.
Specific embodiment
The following description and drawings fully show the specific embodiment of this paper, to enable those skilled in the art to reality
Trample them.The part of some embodiments and feature can be included in or replace part and the feature of other embodiments.This
The range of the embodiment of text includes equivalent obtained by the entire scope of claims and all of claims
Object.Herein, term " first ", " second " etc. are used only for distinguishing an element and another element, without requiring
Either imply that there are any actual relationship or sequences between these elements.Actually the first element can also be referred to as second
Element, vice versa.Moreover, the terms "include", "comprise" or any other variant thereof is intended to cover non-exclusive inclusion,
So that the structure, device or the equipment that include a series of elements not only include those elements, but also including not clear
The other element listed, or further include for this structure, device or the intrinsic element of equipment.Do not limiting more
In the case where, the element that is limited by sentence "including a ...", it is not excluded that include the structure of the element, device or
There is also other identical elements in equipment.Each embodiment herein is described in a progressive manner, each embodiment emphasis
What is illustrated is the difference from other embodiments, and the same or similar parts in each embodiment may refer to each other.
Term " longitudinal direction " herein, " transverse direction ", "upper", "lower", "front", "rear", "left", "right", "vertical", " water
It is flat ", "top", "bottom" "inner", the instructions such as "outside" orientation or positional relationship be to be based on the orientation or positional relationship shown in the drawings, only
It is to be described herein with simplified for ease of description, rather than the device or element of indication or suggestion meaning must have specific side
Position is constructed and operated in a specific orientation, therefore is not considered as limiting the invention.In description herein, unless separately
There are regulation and restriction, term " installation ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being mechanically connected or being electrically connected
Connect, the connection being also possible to inside two elements can be directly connected, can also indirectly connected through an intermediary, for
For those skilled in the art, the concrete meaning of above-mentioned term can be understood as the case may be.
Herein, unless otherwise indicated, term " multiple " indicates two or more.
Herein, character "/" indicates that front and back object is a kind of relationship of "or".For example, A/B is indicated: A or B.
Herein, term "and/or" is a kind of incidence relation of description object, indicates may exist three kinds of relationships.For example,
A and/or B is indicated: A or B, or, these three relationships of A and B.
In some optional embodiments, providing a kind of heat exchanger includes set of heat exchange tubes 1, supercooling tube group 2, supercooling bypass pipe
3, it shunts bypass pipe 5, supercooling check valve 4, shunt check valve 6, wherein supercooling tube group 2 and set of heat exchange tubes 1 are series connections, and
Supercooling tube group 2 and set of heat exchange tubes 1 constitute the flow path of single-row arrangement;Bypass pipe 3 and supercooling tube group 2 and the first pipeline section is subcooled simultaneously
Connection connection;It shunts bypass pipe 5 and at least partly pipeline section of the first pipeline section and the second pipeline section is connected in parallel;Check valve 4 is subcooled to be arranged
In on supercooling bypass pipe 3;Check valve 6 is shunted, is set to and shunts on bypass pipe 5;Set of heat exchange tubes 1 includes the first pipeline section and the second pipe
Section.
Optionally, the conducting direction that check valve 4 is subcooled is limited to, by supercooling bypass pipe 3 and supercooling tube group 2 and interlink
Point, the sys node of flow direction supercooling bypass pipe 3 and the first pipeline section;
Optionally, the conducting direction for shunting check valve 6 is limited to, by the sys node of set of heat exchange tubes 1 and the first pipeline section, stream
To the sys node of set of heat exchange tubes 1 and at least partly pipeline section of the second pipeline section.
Herein, set of heat exchange tubes 1 includes the first pipeline section and the second pipeline section being connected in series, and the first pipeline section can be heat exchanger tube
Group 1 is connected with supercooling tube group 2, and is subcooled one section of the set of heat exchange tubes 1 that bypass pipe 3 is in parallel, and the second pipeline section can be to change
Part of the heat pipe heat 1 in addition to the first pipeline section, wherein the second pipeline section part in parallel with bypass pipe 5 is shunted is the second pipeline section
At least partly pipeline section, the part in addition at least partly pipeline section of the second pipeline section of the second pipeline section are other pipeline sections of the second pipeline section.
Herein, the sys node of supercooling tube group 2 and supercooling bypass pipe 3 can be first node, the first pipeline section and shunting
The sys node of bypass pipe 5 can be second node, and the first pipeline section and the sys node that bypass pipe 3 is subcooled can be third section
Point, the sys node for shunting at least partly pipeline section of bypass pipe 5 and the second pipeline section can be fourth node.
Optionally, in refrigerating operaton, refrigerant circulates heat exchanger in the second pipeline section, the first pipeline section, supercooling tube group 2,
The circulation path of refrigerant is at least partly pipeline section for entering the second pipeline section from fourth node, flows through third node, to the first pipe
Section, flows through second node, arrives supercooling tube group 2, since supercooling check valve 4 and shunting check valve 6 are check valve, is freezing
When operation, the process of circulation of the refrigerant from fourth node to first node is not passed through supercooling check valve 4 and shunts check valve 6,
That is, the process of circulation of the refrigerant from fourth node to first node, is not passed through supercooling bypass pipe 3 and shunts bypass pipe 5, refrigerant
By the second pipeline section of set of heat exchange tubes 1 to the first pipeline section, then pass through supercooling tube group 2, makes refrigerant by supercooling tube group 2
When cooled down again, enable the refrigerant to be fully cooled, so that it will not excessive evaporations, to improve changing for refrigerating operaton process
The thermal efficiency.
Optionally, refrigerant provided by the invention is not construed as limiting, and can be refrigerant, heat exchanger is in refrigerating operaton, refrigerant
Flow path be a paths, when refrigerant enters at least partly pipeline section of the second pipeline section, refrigerant is gaseous state, is successively passed through with refrigerant
The first pipeline section and supercooling tube group 2 are crossed, the state of refrigerant gradually passes through gas-liquid mixed, by supercooling tube group 2, finally in first node
The refrigerant guarantee of outflow is sufficiently condensed into liquid, must by 20 points of longer supercooling tube group to carry out condensation process sufficiently
It wants, ensure that cooling effect, the heat exchanger of supercooling tube group 2 is added compared with the heat exchanger only Jing Guo set of heat exchange tubes 1, cooling effect
More preferably, refrigeration effect is more preferable, and heat exchange efficiency is guaranteed.
Optionally, for heat exchanger in heating operation, refrigerant is in supercooling bypass pipe 3, the first pipeline section, shunting bypass pipe 5
Circulation, the circulation path of refrigerant are to enter supercooling bypass pipe 3 from first node, and shunt two-way in first node, are flowed all the way
To supercooling tube group 2, another way flow direction supercooling bypass pipe 3, the refrigerant of flow direction supercooling bypass pipe 3 flows to third node, in point three
Node shunts two-way again, flows to the first pipeline section all the way, in second node, flows through the refrigerant all the way of supercooling tube group 2 and flows through
The refrigerant all the way of first pipeline section converges, and flow direction shunts bypass pipe 5, flows to the second pipeline section at least in the another way of third node
Portions flow through the refrigerant all the way for shunting bypass pipe 5 and at least partly pipeline section for flowing through the second pipeline section in fourth node
Refrigerant converges all the way, flows to other pipeline sections of the second pipeline section, forms three roads and shunts, when the refrigerant of gas-liquid mixture phase is from the
When one node enters, if not being equipped with the supercooling bypass pipe 3 of supercooling check valve 4 and equipped with the shunting bypass pipe for shunting check valve 6
5, refrigerant resistance is larger, can reduce heat exchange efficiency, influence heating effect.
Herein, the circulation path from first node by supercooling tube group 2 to second node can be first flow path, from the
One node can be second flow path by the circulation path of supercooling bypass pipe 3 to third node, other by shunting from second node
The circulation path of siphunculus 5 to fourth node can be third flow path, from third node by the first pipeline section to the road of second node
Path can be the 4th flow path, pass through at least partly pipeline section of the second pipeline section to the circulation path of fourth node from third node
It can be the 5th flow path.
Optionally, refrigerant provided by the invention is not construed as limiting, and can be refrigerant, heat exchanger is in heating operation, refrigerant
Flow path be three paths, a paths are by supercooling tube group 2 from first node to second node, by shunting bypass pipe 5
To fourth node;One paths are first node by supercooling bypass pipe 3 to third node, by the first pipeline section to the second section
Point arrives fourth node by shunting bypass pipe 5;Another path is first node by supercooling bypass pipe 3 to third node, is passed through
At least partly pipeline section of second pipeline section is to fourth node.That is, first path is first flow path to third flow path;Second path is the
Two flow paths to the 4th flow path are to third flow path;Third path is second flow path to the 5th flow path.Heat exchanger leads in heating operation
Multipath shunting is crossed, larger resistance when refrigerant enters first node is alleviated, flow path resistance loss is reduced, improves system
The thermal efficiency.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of the heat exchanger tube of the first pipeline section of supercooling bypass pipe 3 set of heat exchange tubes 1 in parallel, is less than or waits
In the quantity of the heat exchanger tube of its supercooling tube group 2 in parallel.
Optionally, for heat exchanger in heating operation, the flow path of refrigerant is three paths, and a paths are from first node
Second node is arrived by supercooling tube group 2, arrives fourth node by shunting bypass pipe 5;One paths are first node by supercooling
Bypass pipe 3 arrives third node, by the first pipeline section to second node, arrives fourth node by shunting bypass pipe 5;Another path is
First node arrives third node by supercooling bypass pipe 3, by at least partly pipeline section of the second pipeline section to fourth node.That is, the
One path is first flow path to third flow path;Second path is second flow path to the 4th flow path to third flow path;Third path is
Second flow path is to the 5th flow path.If the number of heat exchange tubes of the first pipeline section is greater than the quantity of the heat exchanger tube of supercooling tube group 2, the first pipeline section
Both ends flow pressure difference can be greater than 2 both ends flow pressure difference of supercooling tube group, then refrigerant circulates in first node to first path
Refrigerant flow can be greater than the refrigerant flow that circulate to the second path, at this point, the effect of bypass pipe 3, which is subcooled, to be cut significantly
Weak, the setting of supercooling bypass pipe 3 does not just have predictive role, and refrigerant circulation can not be allowed to realize that multipath shunts, cannot be fine
Alleviate flow path resistance loss in ground.So when the quantity of the heat exchanger tube of the first pipeline section of set of heat exchange tubes 1 is less than or equal to supercooling tube group
When the quantity of 2 heat exchanger tube, heat exchanger in heating operation, just can more preferably realize multipath shunt, alleviate refrigerant into
Enter larger resistance when first node, reduces flow path resistance loss, improve heating efficiency.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of the heat exchanger tube of the first pipeline section of supercooling bypass pipe 3 set of heat exchange tubes 1 in parallel, is less than or waits
In the quantity of the heat exchanger tube for at least partly pipeline section for shunting second pipeline section in parallel of bypass pipe 5.
Optionally, for heat exchanger in heating operation, the flow path of refrigerant is three paths, and a paths are from first node
Second node is arrived by supercooling tube group 2, arrives fourth node by shunting bypass pipe 5;One paths are first node by supercooling
Bypass pipe 3 arrives third node, by the first pipeline section to second node, arrives fourth node by shunting bypass pipe 5;Another path is
First node arrives third node by supercooling bypass pipe 3, by at least partly pipeline section of the second pipeline section to fourth node.That is, the
One path is first flow path to third flow path;Second path is second flow path to the 4th flow path to third flow path;Third path is
Second flow path is to the 5th flow path.If the number of heat exchange tubes of the first pipeline section is greater than the heat exchanger tube of at least partly pipeline section of the second pipeline section
Quantity, the first pipeline section both ends flow pressure difference can be greater than at least partly pipeline section both ends flow pressure difference of the second pipeline section, then freeze
In third node, the refrigerant flow to circulate to the 5th path can be greater than the refrigerant flow to circulate to the 4th path for agent, at this point,
The effect for shunting bypass pipe 5 can be weakened severely, and the setting for shunting bypass pipe 5 does not just have predictive role, can not allow refrigerant
Circulation realize multipath shunt, cannot alleviate well flow path resistance loss.So when first pipeline section of set of heat exchange tubes 1
When the quantity of heat exchanger tube is less than or equal to the quantity of the heat exchanger tube of at least partly pipeline section of the second pipeline section, heat exchanger is in heating operation
When, it just can more preferably realize that multipath shunts, alleviate larger resistance when refrigerant enters first node, reduce flow path resistance
Power loss, improves heating efficiency.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of the heat exchanger tube of supercooling bypass pipe 3 supercooling tube group 2 in parallel, is greater than or equal to and shunts bypass
The quantity of the heat exchanger tube of at least partly pipeline section of second pipeline section in parallel of pipe 5.
Optionally, for heat exchanger in heating operation, the flow path of refrigerant is three paths, and a paths are from first node
Second node is arrived by supercooling tube group 2, arrives fourth node by shunting bypass pipe 5;One paths are first node by supercooling
Bypass pipe 3 arrives third node, by the first pipeline section to second node, arrives fourth node by shunting bypass pipe 5;Another path is
First node arrives third node by supercooling bypass pipe 3, by at least partly pipeline section of the second pipeline section to fourth node.That is, the
One path is first flow path to third flow path;Second path is second flow path to the 4th flow path to third flow path;Third path is
Second flow path is to the 5th flow path.If the number of heat exchange tubes of at least partly pipeline section of the second pipeline section is greater than the heat exchanger tube of supercooling tube group 2
Quantity, at least partly pipeline section both ends flow pressure difference of the second pipeline section can be greater than 2 both ends flow pressure difference of supercooling tube group, then make
For cryogen in first node, the refrigerant flow to circulate to first path can be greater than the refrigerant flow to circulate to third path, this
When, the effect of supercooling bypass pipe 3 can be weakened severely, and the setting of supercooling bypass pipe 3 does not just have predictive role, can not allow refrigeration
Agent circulation realizes that multipath shunts, and cannot alleviate flow path resistance loss well.So the number of the heat exchanger tube when supercooling tube group 2
When amount is greater than or equal to the quantity of the heat exchanger tube of at least partly pipeline section of the second pipeline section, heat exchanger, just can be in heating operation
It is more preferable to realize that multipath shunts, larger resistance when refrigerant enters first node is alleviated, flow path resistance loss is reduced, mentions
High heating efficiency.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of supercooling bypass pipe 3 is multiple, and multiple supercooling bypass pipes 3 are connected in parallel.
Optionally, the quantity of bypass pipe 3 is subcooled, is not construed as limiting, may include that the first supercooling bypass pipe 3 and the second supercooling are other
Siphunculus 3, the first supercooling bypass pipe 3 and the second supercooling bypass pipe 3 can be parallel, flow at supercooling 3 both ends of bypass pipe
In the case that amount pressure difference is constant, better shunting function can be played to the refrigerant for entering first node.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of the heat exchanger tube of the first pipeline sections of multiple supercooling bypass pipes 3 set of heat exchange tubes 1 in parallel it is identical or
Person is not identical.
Optionally, the connection type of multiple supercooling bypass pipes 3 is to be connected in parallel, in supercooling 3 both ends flow pressure of bypass pipe
In the case that difference is constant, shunting function can be played to the refrigerant for entering first node, and each heat exchanger tube in set of heat exchange tubes 1
It can be series connection mode, concatenated number of heat exchange tubes is more, and refrigerant circulation path is longer, and the pressure drag of set of heat exchange tubes 1 is got over
Greatly, power loss is also bigger, and the first pipeline section of set of heat exchange tubes 1 belongs to set of heat exchange tubes 1, similarly, so, the first of set of heat exchange tubes 1
The quantity of the quantity of the heat exchanger tube of the pipeline section set of heat exchange tubes 1 in parallel with supercooling bypass pipe 3 can be identical.
Optionally, the connection type of multiple supercooling bypass pipes 3 is to be connected in parallel, in supercooling 3 both ends flow pressure of bypass pipe
In the case that difference is constant, shunting function can be played to the refrigerant for entering first node, and each heat exchanger tube in set of heat exchange tubes 1
It can be series connection mode, concatenated number of heat exchange tubes is more, and refrigerant circulation path is longer, and the pressure drag of set of heat exchange tubes 1 is got over
Greatly, power loss is also bigger, and the first pipeline section of set of heat exchange tubes 1 belongs to set of heat exchange tubes 1, similarly, so, the first of set of heat exchange tubes 1
The quantity of the quantity of the heat exchanger tube of the pipeline section set of heat exchange tubes 1 in parallel with supercooling bypass pipe 3 can not be identical.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of shunting bypass pipe 5 is multiple, and multiple supercooling bypass pipes 3 are connected in parallel.
Optionally, the quantity for shunting bypass pipe 5, is not construed as limiting, and may include that the first shunting bypass pipe and second shunt side
Siphunculus, the first shunting bypass pipe and the second shunting bypass pipe can be parallel, shunt 5 both ends flow pressure of bypass pipe
It is strong it is poor it is constant in the case where, better shunting function can be played to the refrigerant for entering third node.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
Optionally, the quantity of the heat exchanger tube of multiple the second pipeline sections for shunting the set of heat exchange tubes 1 in parallel of bypass pipes 5 it is identical or
Person is not identical.
Optionally, multiple connection types for shunting bypass pipe 5 are to be connected in parallel, and are shunting 5 both ends flow pressure of bypass pipe
In the case that difference is constant, shunting function can be played to the refrigerant for entering third node, and each heat exchanger tube in set of heat exchange tubes 1
It can be series connection mode, concatenated number of heat exchange tubes is more, and refrigerant circulation path is longer, and the pressure drag of set of heat exchange tubes 1 is got over
Greatly, power loss is also bigger, and the second pipeline section of set of heat exchange tubes 1 belongs to set of heat exchange tubes 1, similarly, so, the second of set of heat exchange tubes 1
The quantity of the quantity of the heat exchanger tube of the pipeline section set of heat exchange tubes 1 in parallel with bypass pipe 5 is shunted can be identical.
Optionally, multiple connection types for shunting bypass pipe 5 are to be connected in parallel, and are shunting 5 both ends flow pressure of bypass pipe
In the case that difference is constant, shunting function can be played to the refrigerant for entering third node, and each heat exchanger tube in set of heat exchange tubes 1
It can be series connection mode, concatenated number of heat exchange tubes is more, and refrigerant circulation path is longer, and the pressure drag of set of heat exchange tubes 1 is got over
Greatly, power loss is also bigger, and the second pipeline section of set of heat exchange tubes 1 belongs to set of heat exchange tubes 1, similarly, so, the second of set of heat exchange tubes 1
The quantity of the quantity of the heat exchanger tube of the pipeline section set of heat exchange tubes 1 in parallel with bypass pipe 5 is shunted can not be identical.
In this way, being achieved that heat exchanger in heating operation, realizes that heat exchanging device is shunted by check valve, can subtract
Mini system complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange effect
Rate.
The embodiment of the present invention further provides a kind of air conditioner, including indoor heat exchanger, outdoor heat exchanger, compressor and
The refrigerant circulation flow path that four-way valve connects and composes;Wherein, outdoor heat exchanger is the heat exchange as described in above-mentioned any alternative embodiment
The set of heat exchange tubes 1 of device, heat exchanger is connected with compressor, and supercooling tube group 2 is connected with indoor heat exchanger.
Optionally, the outdoor heat exchanger of air-conditioning is mounted in air-conditioner outdoor unit, and the outdoor unit volume of air-conditioning is more unrestricted
System, outdoor heat exchanger be as above outdoor heat exchanger described in any alternative embodiment when, it is in parallel multiple in 3 groups of bypass pipe of supercooling
Bypass pipe 3 is subcooled, and, multiple shunting bypass pipes 5, taking up space can be bigger, and air-conditioning heat exchange efficiency is also higher.
Optionally, for air conditioner when carrying out refrigerating operaton, outdoor heat exchanger includes set of heat exchange tubes 1, supercooling tube group 2, supercooling
Bypass pipe 3 shunts bypass pipe 5, supercooling check valve 4, shunts check valve 6, and wherein supercooling tube group 2 is the company of series connection with set of heat exchange tubes 1
It connects, and supercooling tube group 2 and set of heat exchange tubes 1 constitute the flow path of single-row arrangement;Bypass pipe 3 and supercooling tube group 2 and the is subcooled
One pipeline section is connected in parallel;It shunts bypass pipe 5 and at least partly pipeline section of the first pipeline section and the second pipeline section is connected in parallel;Supercooling is unidirectional
Valve 4 is set on supercooling bypass pipe 3;Check valve 6 is shunted, is set to and shunts on bypass pipe 5.Refrigerant is in the second pipeline section, the first pipe
It circulates in section, supercooling tube group 2, the circulation path of refrigerant is at least partly pipeline section for entering the second pipeline section from fourth node, is flowed through
Third node flows through second node to the first pipeline section, arrives supercooling tube group 2, since supercooling check valve 4 and shunting check valve 6 are
Check valve, therefore in refrigerating operaton, the process of circulation of the refrigerant from fourth node to first node is not passed through supercooling check valve 4
With shunting check valve 6, that is, the process of circulation of the refrigerant from fourth node to first node is not passed through supercooling bypass pipe 3 and shunts other
Siphunculus 5, refrigerant, to the first pipeline section, are then passed through supercooling tube group 2, were passing through refrigerant by the second pipeline section of set of heat exchange tubes 1
It is cooled down again when cold pipe group 2, refrigerant is enable to be fully cooled, so that it will not excessive evaporations, so that it is whole to improve air conditioner
The refrigeration effect of machine system.
Optionally, for air conditioner when carrying out refrigerating operaton, the flow path of refrigerant is a paths in outdoor heat exchanger, in refrigerant
Into the second pipeline section at least partly pipeline section when, refrigerant is gaseous state, successively pass through the first pipeline section and supercooling tube group 2 with refrigerant,
The state of refrigerant gradually passes through gas-liquid mixed, by supercooling tube group 2, finally guarantees sufficiently condensation in the refrigerant of first node outflow
It is very necessary by longer supercooling tube group 2 to carry out condensation process sufficiently for liquid, it ensure that cooling effect, be added
For the outdoor heat exchanger of cold pipe group 2 compared with the outdoor heat exchanger only Jing Guo set of heat exchange tubes 1, cooling effect is more preferable, and refrigeration effect is more
Good, heat exchange efficiency is guaranteed, the refrigeration work efficiency of air conditioner machine system is also improved.
Optionally, air conditioner is when carrying out heating operation, in outdoor heat exchanger refrigerant supercooling bypass pipe 3, the first pipeline section,
It shunts and circulates in bypass pipe 5, the circulation path of refrigerant is to enter supercooling bypass pipe 3 from first node, and shunt in first node
Two-way, flows to supercooling tube group 2, another way flow direction supercooling bypass pipe 3 all the way, and the refrigerant of flow direction supercooling bypass pipe 3 flows to third section
Point shunts two-way putting three nodes again, flows to the first pipeline section all the way, in second node, flow through the refrigerant all the way of supercooling tube group 2
Converge with the refrigerant all the way for flowing through the first pipeline section, flow direction shunts bypass pipe 5, flows to the second pipeline section in the another way of third node
At least partly pipeline section flows through the refrigerant all the way for shunting bypass pipe 5 and at least partly pipeline section for flowing through the second pipeline section in fourth node
Refrigerant all the way converge, flow to other pipeline sections of the second pipeline section, form three roads and shunt, when the refrigerant of gas-liquid mixture phase is from first
When node enters, if being equipped with the supercooling bypass pipe 3 of supercooling check valve 4 and the shunting bypass pipe 5 equipped with shunting check valve 6,
Refrigerant resistance is larger, can reduce heat exchange efficiency, influences the heating effect of air-conditioning.
Optionally, for air conditioner when carrying out heating operation, the flow path of refrigerant is three paths, Yi Tiaolu in outdoor heat exchanger
Diameter is from first node by supercooling tube group 2 to second node, arrives fourth node by shunting bypass pipe 5;One paths are the
One node arrives third node by supercooling bypass pipe 3, by the first pipeline section to second node, by shunting bypass pipe 5 to the 4th
Node;Another path is first node by supercooling bypass pipe 3 to third node, is arrived by at least partly pipeline section of the second pipeline section
Fourth node.That is, first path is first flow path to third flow path;Second path is second flow path to the 4th flow path to third stream
Road;Third path is second flow path to the 5th flow path.Outdoor heat exchanger is shunted in heating operation by multipath, is alleviated
Refrigerant enters larger resistance when first node, reduces flow path resistance loss, improves the heating efficiency of air-conditioning.
Optionally, the quantity of the heat exchanger tube of the first pipeline section is less than or equal to the quantity of the heat exchanger tube of supercooling tube group 2, the first pipe
Section both ends flow pressure difference can be less than 2 both ends flow pressure difference of supercooling tube group, then refrigerant is in first node, to first via runoff
Logical refrigerant flow can be less than the refrigerant flow to circulate to the second path, at this point, the setting of supercooling bypass pipe 3 reaches expected
Effect, makes refrigerant circulation realize that multipath shunts, and alleviates flow path resistance loss well, improves heating efficiency.
Optionally, the quantity of the heat exchanger tube of the first pipeline section is less than or equal to the heat exchanger tube of at least partly pipeline section of the second pipeline section
Quantity, the first pipeline section both ends flow pressure difference can then make less than at least partly pipeline section both ends flow pressure difference of the second pipeline section
For cryogen in third node, the refrigerant flow to circulate to the 5th path can be less than the refrigerant flow to circulate to the 4th path, this
When, the effect for shunting bypass pipe 5 can be weakened severely, and the setting for shunting bypass pipe 5 does not just have predictive role, can not allow refrigeration
The setting of agent achieves the desired results, and refrigerant circulation is made to realize that multipath shunts, and alleviates flow path resistance loss well, improves
Heating efficiency.
Optionally, the quantity of the heat exchanger tube of supercooling tube group 2 is greater than or equal to the heat exchange of at least partly pipeline section of the second pipeline section
At least partly pipeline section both ends flow pressure difference of the quantity of pipe, the second pipeline section can be less than 2 both ends flow pressure difference of supercooling tube group, then
For refrigerant in first node, the refrigerant flow to circulate to first path can be less than the refrigerant flow to circulate to third path,
At this point, the setting of supercooling bypass pipe 3 achieves the desired results, so that refrigerant circulation is realized that multipath shunts, alleviate flow path well
Drag losses improve heating efficiency.
Optionally, supercooling bypass pipe 3 can pass through the first supercooling bypass pipe 3 of parallel way connection and the second mistake for two
Cold bypass pipe 3, the first supercooling bypass pipe 3 and the second supercooling bypass pipe 3 can be parallel, in 3 liang of bypass pipe of supercooling
In the case where holding flow pressure difference constant, better shunting function can be played to the refrigerant for entering first node.
Optionally, bypass pipe and second point can be shunted by the first of parallel way connection for two by shunting bypass pipe 5
Bypass pipe is flowed, it can be parallel that the first shunting bypass pipe and second, which shunt bypass pipe, flow shunting 5 both ends of bypass pipe
In the case that amount pressure difference is constant, better shunting function can be played to the refrigerant for entering third node.
In this way, air-conditioning in heating operation, shunts outdoor heat exchanger by check valve realization, can reduce system
Complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange efficiency.
The embodiment of the present invention further provides another air conditioner, including indoor heat exchanger, outdoor heat exchanger, compressor
The refrigerant circulation flow path connected and composed with four-way valve;Wherein, indoor heat exchanger is changing as described in above-mentioned any alternative embodiment
The set of heat exchange tubes 1 of hot device, heat exchanger is connected with compressor, and supercooling tube group 2 is connected with indoor heat exchanger.
Optionally, air-conditioning can also include throttling set, be not construed as limiting, and throttling set can be capillary, the pressure of air-conditioning
Contracting machine can be invariable frequency compressor, and capillary can connect the separate heat exchange in supercooling tube group 2 and supercooling 3 sys node of bypass pipe
One end of pipe group 1.
Optionally, air-conditioning can also include throttling set, be not construed as limiting, and throttling set can be electric expansion valve, air-conditioning
Compressor can be frequency-changeable compressor, electric expansion valve can connect in supercooling tube group 2 and supercooling bypass pipe 3 sys node
One end far from set of heat exchange tubes 1.
Optionally, for air conditioner when carrying out refrigerating operaton, indoor heat exchanger includes set of heat exchange tubes 1, supercooling tube group 2, supercooling
Bypass pipe 3 shunts bypass pipe 5, supercooling check valve 4, shunts check valve 6, and wherein supercooling tube group 2 is the company of series connection with set of heat exchange tubes 1
It connects, and supercooling tube group 2 and set of heat exchange tubes 1 constitute the flow path of single-row arrangement;Bypass pipe 3 and supercooling tube group 2 and the is subcooled
One pipeline section is connected in parallel;It shunts bypass pipe 5 and at least partly pipeline section of the first pipeline section and the second pipeline section is connected in parallel;Supercooling is unidirectional
Valve 4 is set on supercooling bypass pipe 3;Check valve 6 is shunted, is set to and shunts on bypass pipe 5.Refrigerant is in the second pipeline section, the first pipe
It circulates in section, supercooling tube group 2, the circulation path of refrigerant is at least partly pipeline section for entering the second pipeline section from fourth node, is flowed through
Third node flows through second node to the first pipeline section, arrives supercooling tube group 2, since supercooling check valve 4 and shunting check valve 6 are
Check valve, therefore in refrigerating operaton, the process of circulation of the refrigerant from fourth node to first node is not passed through supercooling check valve 4
With shunting check valve 6, that is, the process of circulation of the refrigerant from fourth node to first node is not passed through supercooling bypass pipe 3 and shunts other
Siphunculus 5, refrigerant, to the first pipeline section, are then passed through supercooling tube group 2, were passing through refrigerant by the second pipeline section of set of heat exchange tubes 1
It is cooled down again when cold pipe group 2, refrigerant is enable to be fully cooled, so that it will not excessive evaporations, so that it is whole to improve air conditioner
The refrigeration effect of machine system.
Optionally, for air conditioner when carrying out refrigerating operaton, the flow path of refrigerant is a paths in indoor heat exchanger, in refrigerant
Into the second pipeline section at least partly pipeline section when, refrigerant is gaseous state, successively pass through the first pipeline section and supercooling tube group 2 with refrigerant,
The state of refrigerant gradually passes through gas-liquid mixed, by supercooling tube group 2, finally guarantees sufficiently condensation in the refrigerant of first node outflow
It is very necessary by longer supercooling tube group 2 to carry out condensation process sufficiently for liquid, it ensure that cooling effect, be added
For the indoor heat exchanger of cold pipe group 2 compared with the indoor heat exchanger only Jing Guo set of heat exchange tubes 1, cooling effect is more preferable, and refrigeration effect is more
Good, heat exchange efficiency is guaranteed, the refrigeration work efficiency of air conditioner machine system is also improved.
Optionally, the separate set of heat exchange tubes in supercooling tube group 2 and supercooling 3 sys node of bypass pipe can be set in throttling set
1 one end is connected with supercooling tube group 2, and supercooling tube group 2 cools down refrigerant again, has enough degree of supercoolings that can control refrigerant and is saving
Excessive evaporation is not generated before stream unit, to improve the refrigerating efficiency of air conditioner.
Optionally, air conditioner is when carrying out heating operation, in indoor heat exchanger refrigerant supercooling bypass pipe 3, the first pipeline section,
It shunts and circulates in bypass pipe 5, the circulation path of refrigerant is to enter supercooling bypass pipe 3 from first node, and shunt in first node
Two-way, flows to supercooling tube group 2, another way flow direction supercooling bypass pipe 3 all the way, and the refrigerant of flow direction supercooling bypass pipe 3 flows to third section
Point shunts two-way putting three nodes again, flows to the first pipeline section all the way, in second node, flow through the refrigerant all the way of supercooling tube group 2
Converge with the refrigerant all the way for flowing through the first pipeline section, flow direction shunts bypass pipe 5, flows to the second pipeline section in the another way of third node
At least partly pipeline section flows through the refrigerant all the way for shunting bypass pipe 5 and at least partly pipeline section for flowing through the second pipeline section in fourth node
Refrigerant all the way converge, flow to other pipeline sections of the second pipeline section, form three roads and shunt, when the refrigerant of gas-liquid mixture phase is from first
When node enters, if being equipped with the supercooling bypass pipe 3 of supercooling check valve 4 and the shunting bypass pipe 5 equipped with shunting check valve 6,
Refrigerant resistance is larger, can reduce heat exchange efficiency, influences the heating effect of air-conditioning.
Optionally, for air conditioner when carrying out heating operation, the flow path of refrigerant is three paths, Yi Tiaolu in indoor heat exchanger
Diameter is from first node by supercooling tube group 2 to second node, arrives fourth node by shunting bypass pipe 5;One paths are the
One node arrives third node by supercooling bypass pipe 3, by the first pipeline section to second node, by shunting bypass pipe 5 to the 4th
Node;Another path is first node by supercooling bypass pipe 3 to third node, is arrived by at least partly pipeline section of the second pipeline section
Fourth node.That is, first path is first flow path to third flow path;Second path is second flow path to the 4th flow path to third stream
Road;Third path is second flow path to the 5th flow path.Indoor heat exchanger is shunted in heating operation by multipath, is alleviated
Refrigerant enters larger resistance when first node, reduces flow path resistance loss, improves the heating efficiency of air-conditioning.
Optionally, the quantity of the heat exchanger tube of the first pipeline section is less than or equal to the quantity of the heat exchanger tube of supercooling tube group 2, the first pipe
Section both ends flow pressure difference can be less than 2 both ends flow pressure difference of supercooling tube group, then refrigerant is in first node, to first via runoff
Logical refrigerant flow can be less than the refrigerant flow to circulate to the second path, at this point, the setting of supercooling bypass pipe 3 reaches expected
Effect, makes refrigerant circulation realize that multipath shunts, and alleviates flow path resistance loss well, improves heating efficiency.
Optionally, the quantity of the heat exchanger tube of the first pipeline section is less than or equal to the heat exchanger tube of at least partly pipeline section of the second pipeline section
Quantity, the first pipeline section both ends flow pressure difference can then make less than at least partly pipeline section both ends flow pressure difference of the second pipeline section
For cryogen in third node, the refrigerant flow to circulate to the 5th path can be less than the refrigerant flow to circulate to the 4th path, this
When, the effect for shunting bypass pipe 5 can be weakened severely, and the setting for shunting bypass pipe 5 does not just have predictive role, can not allow refrigeration
The setting of agent achieves the desired results, and refrigerant circulation is made to realize that multipath shunts, and alleviates flow path resistance loss well, improves
Heating efficiency.
Optionally, the quantity of the heat exchanger tube of supercooling tube group 2 is greater than or equal to the heat exchange of at least partly pipeline section of the second pipeline section
At least partly pipeline section both ends flow pressure difference of the quantity of pipe, the second pipeline section can be less than 2 both ends flow pressure difference of supercooling tube group, then
For refrigerant in first node, the refrigerant flow to circulate to first path can be less than the refrigerant flow to circulate to third path,
At this point, the setting of supercooling bypass pipe 3 achieves the desired results, so that refrigerant circulation is realized that multipath shunts, alleviate flow path well
Drag losses improve heating efficiency.
Optionally, supercooling bypass pipe 3 can pass through the first supercooling bypass pipe 3 of parallel way connection and the second mistake for two
Cold bypass pipe 3, the first supercooling bypass pipe 3 and the second supercooling bypass pipe 3 can be parallel, in 3 liang of bypass pipe of supercooling
In the case where holding flow pressure difference constant, better shunting function can be played to the refrigerant for entering first node.
Optionally, bypass pipe and second point can be shunted by the first of parallel way connection for two by shunting bypass pipe 5
Bypass pipe is flowed, it can be parallel that the first shunting bypass pipe and second, which shunt bypass pipe, flow shunting bypass pipe both ends
In the case that amount pressure difference is constant, better shunting function can be played to the refrigerant for entering third node.
In this way, air-conditioning in heating operation, shunts indoor heat exchanger by check valve realization, can reduce system
Complexity reduces the voltage loss generated in heating by supercooling tube group 2, to improve system heat exchange efficiency.
The invention is not limited to the structures for being described above and being shown in the accompanying drawings, and can not depart from its model
It encloses and carry out various modifications and change.The scope of the present invention is limited only by the attached claims.
Claims (10)
1. a kind of heat exchanger, which is characterized in that the heat exchanger includes:
Set of heat exchange tubes;
Supercooling tube group is connected in series with the set of heat exchange tubes;And the supercooling tube group and the set of heat exchange tubes constitute single-row arrangement
The flow path of structure;
Bypass pipe is subcooled, the supercooling bypass pipe and the first pipeline section of the supercooling tube group and the set of heat exchange tubes are connected in parallel;
Shunt bypass pipe, the shunting bypass pipe and first pipeline section and the second pipeline section of the set of heat exchange tubes at least partly
Pipeline section is connected in parallel;
Check valve is subcooled, is set on the supercooling bypass pipe, the conducting direction of the supercooling check valve is limited to by the mistake
The sys node with the sys node flow direction and first pipeline section of the supercooling tube group of cold bypass pipe;
Check valve is shunted, is set on the shunting bypass pipe, the conducting direction for shunting check valve is limited to be changed by described
Heat pipe heat with the sys node of first pipeline section flow direction with described in second pipeline section at least partly pipeline section and interlink
Point.
2. heat exchanger according to claim 1, which is characterized in that the supercooling bypass pipe set of heat exchange tubes in parallel
First pipeline section heat exchanger tube quantity, less than or equal to the quantity of the heat exchanger tube of its supercooling tube group in parallel.
3. heat exchanger according to claim 1, which is characterized in that the supercooling bypass pipe set of heat exchange tubes in parallel
First pipeline section heat exchanger tube quantity, less than or equal to the institute of the shunting bypass pipe second pipeline section in parallel
State the quantity of at least partly heat exchanger tube of pipeline section.
4. heat exchanger according to claim 1, which is characterized in that the supercooling bypass pipe supercooling tube group in parallel
Heat exchanger tube quantity, more than or equal at least partly pipeline section described in the shunting bypass pipe second pipeline section in parallel
Heat exchanger tube quantity.
5. heat exchanger according to claim 1, which is characterized in that the quantity of the supercooling bypass pipe is multiple, Duo Gesuo
Supercooling bypass pipe is stated to be connected in parallel.
6. heat exchanger according to claim 5, which is characterized in that the heat exchange in parallel of multiple supercooling bypass pipes
The quantity of the heat exchanger tube of first pipeline section of pipe group is identical or not identical.
7. heat exchanger according to claim 1, which is characterized in that the quantity for shunting bypass pipe is multiple, Duo Gesuo
Supercooling bypass pipe is stated to be connected in parallel.
8. heat exchanger according to claim 7, which is characterized in that the heat exchange in parallel of multiple shunting bypass pipes
The quantity of the heat exchanger tube of second pipeline section of pipe group is identical or not identical.
9. a kind of air conditioner, which is characterized in that the air conditioner includes indoor heat exchanger, outdoor heat exchanger, compressor and four-way
The refrigerant circulation flow path that valve connects and composes;Wherein, the outdoor heat exchanger is described in any item heat exchange such as claim 1-8
The set of heat exchange tubes of device, the heat exchanger is connected with the compressor, the supercooling tube group and the indoor heat exchanger phase
Connection.
10. a kind of air conditioner, which is characterized in that the air conditioner includes indoor heat exchanger, outdoor heat exchanger, compressor and four-way
The refrigerant circulation flow path that valve connects and composes;Wherein, the indoor heat exchanger is described in any item heat exchange such as claim 1-8
The set of heat exchange tubes of device, the heat exchanger is connected with the compressor, the supercooling tube group and the indoor heat exchanger phase
Connection.
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CN201910023148.XA CN109751752B (en) | 2019-01-10 | 2019-01-10 | Heat exchanger and air conditioner |
PCT/CN2020/070180 WO2020143538A1 (en) | 2019-01-10 | 2020-01-03 | Heat exchanger and air conditioner |
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WO2020143539A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
WO2020143537A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
WO2020143538A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
CN113719901A (en) * | 2021-08-26 | 2021-11-30 | Tcl空调器(中山)有限公司 | Air conditioner heat exchange assembly and air conditioner |
CN114543402A (en) * | 2022-03-23 | 2022-05-27 | 广东美的制冷设备有限公司 | Heat exchanger, heat exchanger flow path control method, readable storage medium and air conditioner |
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CN109751752B (en) * | 2019-01-10 | 2023-04-07 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
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CN206919454U (en) * | 2017-04-28 | 2018-01-23 | 青岛海尔空调器有限总公司 | Heat exchanger and air-conditioning device for air-conditioning device |
CN107631514A (en) * | 2017-09-22 | 2018-01-26 | 珠海格力电器股份有限公司 | Air-conditioning system |
CN209744696U (en) * | 2019-01-10 | 2019-12-06 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
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WO2020143539A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
WO2020143537A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
WO2020143538A1 (en) * | 2019-01-10 | 2020-07-16 | 青岛海尔空调器有限总公司 | Heat exchanger and air conditioner |
CN113719901A (en) * | 2021-08-26 | 2021-11-30 | Tcl空调器(中山)有限公司 | Air conditioner heat exchange assembly and air conditioner |
CN113719901B (en) * | 2021-08-26 | 2023-09-19 | Tcl空调器(中山)有限公司 | Air conditioner heat exchange assembly and air conditioner |
CN114543402A (en) * | 2022-03-23 | 2022-05-27 | 广东美的制冷设备有限公司 | Heat exchanger, heat exchanger flow path control method, readable storage medium and air conditioner |
CN114543402B (en) * | 2022-03-23 | 2024-05-28 | 广东美的制冷设备有限公司 | Heat exchanger, heat exchanger flow path control method, readable storage medium and air conditioner |
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CN109751752B (en) | 2023-04-07 |
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Address after: 266101 Haier Industrial Park, Haier Road, Laoshan District, Shandong, Qingdao, China Applicant after: QINGDAO HAIER AIR CONDITIONER GENERAL Corp.,Ltd. Applicant after: Haier Smart Home Co., Ltd. Address before: 266101 Haier Industrial Park, Haier Road, Laoshan District, Shandong, Qingdao, China Applicant before: QINGDAO HAIER AIR CONDITIONER GENERAL Corp.,Ltd. Applicant before: QINGDAO HAIER JOINT STOCK Co.,Ltd. |
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GR01 | Patent grant | ||
GR01 | Patent grant |