CN220541435U - Shunt and air conditioner with same - Google Patents

Shunt and air conditioner with same Download PDF

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Publication number
CN220541435U
CN220541435U CN202322265829.1U CN202322265829U CN220541435U CN 220541435 U CN220541435 U CN 220541435U CN 202322265829 U CN202322265829 U CN 202322265829U CN 220541435 U CN220541435 U CN 220541435U
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China
Prior art keywords
section
transition section
flow
shunt
length
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CN202322265829.1U
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Chinese (zh)
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郑丹平
林裕亮
黄城
赵智翀
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Gree Green Refrigeration Technology Center Co Ltd of Zhuhai
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Gree Green Refrigeration Technology Center Co Ltd of Zhuhai
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Abstract

The utility model provides a shunt and an air conditioner with the shunt, comprising: the split flow structure is provided with a first transition section, a second transition section and a split flow section which are sequentially connected, one end of the first transition section, which is far away from the second transition section, is communicated with an inlet of the split flow structure, and one end of the split flow section, which is far away from the second transition section, forms a split flow outlet of the split flow structure; the flow cross-sectional area of the first transition section gradually increases and the flow cross-sectional area of the second transition section gradually decreases along the extending direction from the first transition section to the second transition section. The technical problem that the flushing sound of the current divider in the prior art is large can be solved through the technical problem provided by the utility model.

Description

Shunt and air conditioner with same
Technical Field
The utility model relates to the technical field of current splitters, in particular to a current splitter and an air conditioner with the same.
Background
Currently, with the development of air conditioning technology, users have increasingly high demands on air conditioning systems. The existing air conditioner has the disadvantages that refrigerant scouring sound occurs about 20s during the refrigeration starting operation, the low-frequency sound penetrability is strong, and the noise radiation area is wider when the refrigerant flows into the evaporator of the inner machine from the outer machine due to the larger area of the evaporator, so that the comfort of users is influenced. In the prior art, in order to reduce noise generated by flushing of the refrigerant, the opening degree of the electronic expansion valve is generally adjusted.
However, the electronic expansion valve opening is adjusted adaptively according to the refrigerant quantity, so that the electronic expansion valve opening is complicated in adjusting mode and cannot effectively reduce the refrigerant flushing sound.
Disclosure of Invention
The utility model mainly aims to provide a current divider and an air conditioner with the same, so as to solve the technical problem of large flushing sound of the current divider in the prior art.
In order to achieve the above object, according to one aspect of the present utility model, there is provided a shunt including:
the split flow structure is provided with a first transition section, a second transition section and a split flow section which are sequentially connected, one end of the first transition section, which is far away from the second transition section, is communicated with an inlet of the split flow structure, and one end of the split flow section, which is far away from the second transition section, forms a split flow outlet of the split flow structure;
the flow cross-sectional area of the first transition section gradually increases and the flow cross-sectional area of the second transition section gradually decreases along the extending direction from the first transition section to the second transition section.
Further, the length of the second transition section is less than the length of the first transition section.
Further, the second transition section is a first conical section, and the cone angle of the first conical section is alpha, and alpha is more than or equal to 40 degrees and less than or equal to 50 degrees; and/or the number of the groups of groups,
the length of the first transition section is L 2 The length of the second transition section is L 4 ,11≤L 2 /L 4 Less than or equal to 15; and/or the number of the groups of groups,
the flow cross-sectional area of the first transition section is S 2 The flow cross-sectional area of the second transition section is S 4 ,2≤S 2 /S 4 ≤6。
Further, the diverting structure also has a throat section disposed between the second transition section and the diverting section.
Further, the first transition section has a length L 2 The length of the shunt section is L 5 The length of the throat section is L 1 The total length of the shunt is L; wherein 0.01XL 2 2 +0.003×L 5 +0.001×L 1 2 +72=L。
Further, the flow cross-sectional area of the throat section is S 1 The flow cross-sectional area of the first transition section is S 2 ,2≤S 2 /S 1 Less than or equal to 6; and/or the number of the groups of groups,
the length of the throat section is L 1 The length of the first transition section is L 2 ,9≤L 2 /L 1 ≤11。
Further, the flow dividing structure is also provided with an inlet section, the inlet section is connected with one end of the first transition section far away from the second transition section, and an inlet is formed at one end of the inlet section far away from the first transition section;
the flow cross-sectional area of the inlet section is S 3 The flow cross-sectional area of the first transition section is S 2 ,1.04≤S 2 /S 3 Less than or equal to 1.24; and/or the number of the groups of groups,
the length of the inlet section is L 3 The length of the first transition section is L 2 ,4.5≤L 3 /L 2 ≤6.5。
Further, the first transition section is a tapered section.
Further, the shunt structure includes:
the first split-flow shell is provided with a first transition section;
the second shunt shell is arranged on the first shunt shell, and a second transition section and a shunt section are arranged on the first shunt shell.
Further, the second split-flow shell is sleeved on the first split-flow shell.
Further, the second split-flow shell is provided with a mounting channel, the mounting channel is arranged at one end of the second transition section, which is far away from the split-flow section, one end of the mounting channel, which is close to the second transition section, is provided with a positioning step, and the end part of the first split-flow shell is abutted to the positioning step.
According to another aspect of the present utility model, there is provided an air conditioner including the above-provided flow divider.
By applying the technical scheme of the utility model, the fluid at the inlet of the flow dividing structure is firstly slowed down through the first transition section and then is rapidly accelerated in the second transition section, so that the fluid forms vortex in high-speed movement, thereby fully mixing the gas phase and the liquid phase of the refrigerant, and enters the flow dividing section after mixing, and the speed is reduced as the loss of the refrigerant flowing Cheng Zuli in the flow dividing section increases until the refrigerant flows to the outlet. Because the flow cross-sectional area of the first transition section is gradually increased, vortex is not generated; the vortex is generated in the second transition section, the flow cross-sectional area of the second transition section is gradually reduced, so that the vortex corresponding to the vortex is smaller in size, the generation of large-size vortex is avoided, noise generated by the large-size vortex can be avoided, a noise source is weakened, the scouring sound of the refrigerant is lower, and the scouring sound can be effectively reduced.
Drawings
The accompanying drawings, which are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate embodiments of the utility model and together with the description serve to explain the utility model. In the drawings:
FIG. 1 illustrates a cross-sectional view of a shunt provided in accordance with an embodiment of the present utility model;
FIG. 2 shows a schematic structural view of a shunt provided in accordance with an embodiment of the present utility model;
FIG. 3 illustrates a flow splitter velocity profile cloud provided in accordance with an embodiment of the utility model;
FIG. 4 illustrates a splitter outlet velocity cloud provided in accordance with an embodiment of the utility model;
FIG. 5 illustrates an internal swirl schematic of a flow splitter provided in accordance with an embodiment of the utility model;
FIG. 6 shows a schematic view of the internal swirl of other diverters.
Wherein the above figures include the following reference numerals:
10. a shunt structure; 11. a first transition section; 12. a second transition section; 13. a shunt section; 14. a laryngeal section; 15. an inlet section; 16. a first split housing; 17. a second split housing.
Detailed Description
It should be noted that, in the case of no conflict, the embodiments and features in the embodiments may be combined with each other. The utility model will be described in detail below with reference to the drawings in connection with embodiments.
As shown in fig. 1 to 2, a first embodiment of the present utility model provides a diverter including a diverter structure 10, the diverter structure 10 having a first transition section 11, a second transition section 12 and a diverter section 13 connected in sequence, an end of the first transition section 11 remote from the second transition section 12 being in communication with an inlet of the diverter structure 10, and an end of the diverter section 13 remote from the second transition section 12 forming a diverter outlet of the diverter structure 10. Wherein, along the extending direction of the first transition section 11 to the second transition section 12, the flow cross-sectional area of the first transition section 11 gradually increases, and the flow cross-sectional area of the second transition section 12 gradually decreases.
Specifically, the inlet of the flow divider in this embodiment is introduced with refrigerant. By adopting the structure, the fluid at the inlet of the flow dividing structure 10 is firstly slowed down through the first transition section 11 and then is rapidly accelerated in the second transition section 12, so that the fluid forms vortex in high-speed movement, the gas phase and the liquid phase of the refrigerant are fully mixed, the mixed gas phase and the mixed liquid phase enter the flow dividing section 13, the speed is reduced along with the increase of the loss of the refrigerant flowing in the flow dividing section 13 Cheng Zuli, and the mixed gas phase and the mixed liquid phase flow enter the outlet of the evaporator, and then flow into coils of each path of the evaporator for heat exchange. Since the flow cross-sectional area of the first transition section 11 is gradually increased, no vortex is generated; the vortex is generated in the second transition section 12, and the flow cross-sectional area of the second transition section 12 is gradually reduced, so that the vortex corresponding to the vortex is smaller in size, the generation of large-size vortex is avoided, the noise generated by the large-size vortex can be avoided, the noise source is weakened, the scouring sound of the refrigerant is lower, and the scouring sound can be effectively reduced.
The flow cross-sectional area of the first transition section 11 may be understood as a cross-sectional area perpendicular to the extending direction of the first transition section 11, and the flow cross-sectional nep of the second transition section 12 may be immediately a cross-sectional area perpendicular to the extending direction of the second transition section 12. The flow cross-sectional area in this application is understood to be the cross-sectional area perpendicular to the extension direction of the corresponding structure.
Preferably, the first transition section 11 has a length of 46mm and the second transition section 12 has a length of 3.5mm.
Specifically, the number of the flow dividing sections 13 in the present embodiment is plural, and each flow dividing section 13 has a flow dividing outlet. The plurality of diversion sections 13 are arranged around the second transition section 12, the plurality of diversion sections 13 are connected with the second transition section 12, and the refrigerant enters the plurality of diversion sections 13 after being accelerated by the second transition section 12 and finally flows out through diversion outlets of the diversion sections 13.
In the present embodiment, the length of the second transition section 12 is smaller than the length of the first transition section 11. By adopting the structure, the refrigerant can be conveniently and rapidly accelerated in the second transition section 12, so that the refrigerant can conveniently flow at a high speed, and a vortex can be conveniently and well formed, so that the gas phase and the liquid phase of the refrigerant can be conveniently and fully mixed.
Specifically, the second transition section 12 in the present embodiment is a first tapered section having a taper angle α, which is 40 ° or more and α or less than 50 °. With such a structural arrangement, it is possible to facilitate rapid acceleration of the refrigerant in the second transition section 12, and to facilitate flow of the refrigerant at a higher speed.
Specifically, the first transition section 11 has a length L2, and the second transition section 12 has a length L 4 ,11≤L 2 /L 4 And is less than or equal to 15. With this arrangement, it is possible to facilitate ensuring that the refrigerant passes through the first transition section 11 of a sufficient length and undergoes a certain deceleration in the first transition section 11 and swiftly advances in the second transition section 12The speed is increased to facilitate a smaller size vortex being created in the second transition section 12 to better reduce the flushing sound of the refrigerant.
In the present embodiment, the first transition section 11 has a flow cross-sectional area S 2 The second transition section 12 has a flow cross-sectional area S 4 ,2≤S 2 /S 4 And is less than or equal to 6. With such an arrangement, it is possible to facilitate a reduction in the flow velocity at which the refrigerant can sufficiently flow in the first transition section 11 of a larger flow cross section, and to better avoid the possibility of generating a vortex in the first transition section 11, thereby facilitating a better reduction in the flushing sound.
In this embodiment, the flow dividing structure 10 further has a throat section 14, and the throat section 14 is disposed between the second transition section 12 and the flow dividing section 13, so that the refrigerant enters the throat section 14 through the second transition section 12, the liquid film of the refrigerant in the throat section 14 becomes thinner, and the flow pattern in the corresponding gas phase is closer to the mist flow shape, thereby improving the flow dividing performance. And the experiment proves that the refrigerant flushing sound can be effectively weakened and the duration is very short by arranging the throat section 14, so that the use comfort of a user is greatly improved.
Specifically, the first transition section 11 has a length L 2 The length of the shunt section 13 is L 5 The throat section 14 has a length L 1 The total length of the shunt is L; wherein 0.01XL 2 2 +0.003×L 5 +0.001×L 1 2 +72=l. By adopting the arrangement, the dimensional relationship among the total lengths of the first transition section 11, the diversion section 13, the throat section 14 and the diverter can be further optimized, so that vortex generation can be reduced better under the comprehensive action of the first transition section 11, the diversion section 13 and the throat section 14, and scouring sound generated in the flowing process of the refrigerant can be reduced better.
Specifically, the throat section 14 in this embodiment has a flow cross-sectional area S 1 The first transition section 11 has a flow cross-sectional area S 2 ,2≤S 2 /S 1 And is less than or equal to 4. With the structure, the flow cross-section area of the throat section 14 is smaller than that of the first transition section 11, so that the refrigerant in the throat section 14 maintains high flow velocity, thereby facilitating formationThe vortex is convenient for fully mixing the gas phase and the liquid phase of the refrigerant, improves the mixing uniformity, enters the diversion section 13 after mixing, and can reduce the vortex size of the vortex. Therefore, by adopting the arrangement, the flushing sound of the refrigerant can be reduced on the basis of improving the flow distribution uniformity.
Specifically, the length of the throat section 14 in this embodiment is L 1 The first transition section 11 has a length L 2 ,9≤L 2 /L 1 And is less than or equal to 11. By adopting the structure, under the condition that the flow speed of the refrigerant in the throat section 14 is kept high, the vortex of oversized along the longitudinal direction is avoided, the gas-liquid two phases of the refrigerant are convenient to fully mix, the mixing uniformity is improved, the refrigerant enters the flow dividing section 13 after being mixed, and the vortex size of the vortex can be reduced. Therefore, by adopting the arrangement, the flushing sound of the refrigerant can be further reduced on the basis of improving the flow distribution uniformity.
In particular, the throat section 14 may be a constant cross-section flow passage.
In this embodiment, the flow dividing structure 10 further has an inlet section 15, the inlet section 15 being connected to an end of the first transition section 11 remote from the second transition section 12, the end of the inlet section 15 remote from the first transition section 11 forming an inlet.
Specifically, the flow cross-sectional area of the inlet section 15 in the present embodiment is S 3 The first transition section 11 has a flow cross-sectional area S 2 ,1.04≤S 2 /S 3 And is less than or equal to 1.24. By adopting the structure, the flow velocity of the refrigerant at the inlet section 15 can be conveniently and effectively reduced through the first transition section 11, the condition that the refrigerant generates vortex with larger size at the first transition section 11 due to overhigh flow velocity is avoided, and the condition that the flushing sound of the refrigerant is overhigh is further avoided.
Specifically, the inlet section 15 in this embodiment has a length L 3 The first transition section 11 has a length L 2 ,4.5≤L 3 /L 2 And is less than or equal to 6.5. By adopting the structural arrangement, the refrigerant can be fully decelerated through the first transition section 11, the condition that the speed of the refrigerant is too high in the first transition section 11 is avoided, and the refrigerant is better prevented from being in the first transitionThe higher flow velocity at segment 11 creates a larger sized vortex and thus more effective reduction of the scouring sound.
In the present embodiment, the first transition section 11 is a conical section.
Specifically, the flow splitting structure 10 includes a first flow splitting housing 16 and a second flow splitting housing 17, with the first flow splitting housing 16 having the first transition section 11 disposed thereon. The second splitter housing 17 is mounted on the first splitter housing 16, and the first splitter housing 16 is provided with the second transition section 12 and the splitter section 13. By adopting such split structure arrangement, the first split shell 16 and the second split shell 17 are arranged separately, so that the production and the manufacture of the first transition channel and the second transition channel can be facilitated, and the production and the manufacture difficulty can be reduced conveniently.
In this embodiment, the second split casing 17 is sleeved on the first split casing 16. By adopting the structure, the installation can be conveniently carried out, the production and manufacturing difficulty is reduced, and the installation efficiency is improved.
Specifically, the second split casing 17 in this embodiment is provided with a mounting channel, the mounting channel is disposed at one end of the second transition section 12 away from the split section 13, one end of the mounting channel, which is close to the second transition section 12, has a positioning step, and the end of the first split casing 16 abuts against the positioning step. With such a structural arrangement, the first split casing 16 can be easily installed and positioned, so that the first split casing 16 and the second split casing 17 can be easily installed, positioned, and connected.
Preferably, the flow cross-sectional area of the first transition section 11 is 14% larger than the flow cross-sectional area of the inlet section 15 in this embodiment, the first transition section 11 is in a gradually expanding shape, the length of the length arm inlet section 15 of the first transition section 11 is 4.5 times, the refrigerant forms a gradually expanding taper shape through the second transition section 12 before entering the throat section 14, the corresponding taper angle is 45 °, the refrigerant enters the throat section, the throat section design size is 3 times smaller than the transition section cross-sectional area, and the throat section length size is 9 times smaller than the transition section length size. By adopting the arrangement, the refrigerant can be efficiently split, and the flushing sound of the refrigerant of the air conditioner can be effectively solved.
As shown in fig. 3 and 4, specifically, the internal structure of the flow divider in the present embodiment is Y-shaped, and the refrigerant enters from the inlet section 15 during cooling. Assuming that the refrigerant enters the first transition section 11 after entering the flow divider at a speed of 5m/s, the first transition section 11 should be designed to be 14% larger than the sectional area of the inlet section 15, the first transition section 11 is in a gradually expanding shape, and the length dimension of the first transition section 11 should be designed to be 4.5 times larger than the length dimension of the inlet section 15, at this time, the kinetic energy of the refrigerant in the flow channel is reduced, and the speed is reduced to 4.7m/s. Then, the refrigerant enters the second transition section 12, the refrigerant forms a tapered taper shape before entering the throat section 14, the corresponding taper angle is 45 degrees, the speed gradient in the flow channel is enhanced, the high-speed area and the low-speed area start to differentiate, and the speed is increased to 8.8m/s. Then, the refrigerant enters the throat section 14, the speed is increased from 8.8m/s to 16m/s, the design size of the throat section 14 is 3 times smaller than the sectional area of the transition section, the length size of the throat section 14 is 9 times smaller than the length size of the transition section, vortex is formed in high-speed movement, the gas phase and the liquid phase of the refrigerant are fully mixed, the refrigerant enters each shunt section 13, the speed is reduced along with the increase of the resistance loss, and the refrigerant flows into each shunt outlet of each shunt and then flows into each coil pipe of the evaporator for heat exchange. The flow divider in this embodiment not only can make the liquid film of the refrigerant in the throat section 14 thin, and the corresponding gas phase flow pattern is closer to the fog flow shape, thereby improving the flow dividing performance, and in experimental verification, the refrigerant scouring sound is obviously weakened and the duration is very short, thereby greatly improving the user experience comfort.
As shown in the following table and fig. 5 and 6, the splitter of the present application performs internal speed comparison with splitters of other sizes, the throat speed of the splitter is obviously reduced by 36%, and the internal speed gradient is obviously reduced, so that the flow field at the outlet of the splitter is more uniform, and the performance of the splitter is effectively improved. The large part of airflow noise is generated by large-scale vortexes, the size of the large-scale vortexes is effectively reduced in the diverging section, a noise source is weakened, and the reason that the refrigerant scouring sound is lower is also explained.
An embodiment II of the present utility model provides an air conditioner, which includes the diverter provided in the above embodiment I.
From the above description, it can be seen that the above embodiments of the present utility model achieve the following technical effects: the refrigerant can be efficiently split, and the flushing sound of the refrigerant of the air conditioner can be effectively reduced.
It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments in accordance with the present application. As used herein, the singular is also intended to include the plural unless the context clearly indicates otherwise, and furthermore, it is to be understood that the terms "comprises" and/or "comprising" when used in this specification are taken to specify the presence of stated features, steps, operations, devices, components, and/or combinations thereof.
The relative arrangement of the components and steps, numerical expressions and numerical values set forth in these embodiments do not limit the scope of the present application unless it is specifically stated otherwise. Meanwhile, it should be understood that the sizes of the respective parts shown in the drawings are not drawn in actual scale for convenience of description. Techniques, methods, and apparatus known to one of ordinary skill in the relevant art may not be discussed in detail, but should be considered part of the specification where appropriate. In all examples shown and discussed herein, any specific values should be construed as merely illustrative, and not a limitation. Thus, other examples of the exemplary embodiments may have different values. It should be noted that: like reference numerals and letters denote like items in the following figures, and thus once an item is defined in one figure, no further discussion thereof is necessary in subsequent figures.
In the description of the present application, it should be understood that, where azimuth terms such as "front, rear, upper, lower, left, right", "transverse, vertical, horizontal", and "top, bottom", etc., indicate azimuth or positional relationships generally based on those shown in the drawings, only for convenience of description and simplification of the description, these azimuth terms do not indicate and imply that the apparatus or elements referred to must have a specific azimuth or be constructed and operated in a specific azimuth, and thus should not be construed as limiting the scope of protection of the present application; the orientation word "inner and outer" refers to inner and outer relative to the contour of the respective component itself.
Spatially relative terms, such as "above … …," "above … …," "upper surface at … …," "above," and the like, may be used herein for ease of description to describe one device or feature's spatial location relative to another device or feature as illustrated in the figures. It will be understood that the spatially relative terms are intended to encompass different orientations in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as "above" or "over" other devices or structures would then be oriented "below" or "beneath" the other devices or structures. Thus, the exemplary term "above … …" may include both orientations of "above … …" and "below … …". The device may also be positioned in other different ways (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
In addition, the terms "first", "second", etc. are used to define the components, and are merely for convenience of distinguishing the corresponding components, and unless otherwise stated, the terms have no special meaning, and thus should not be construed as limiting the scope of the present application.
The above description is only of the preferred embodiments of the present utility model and is not intended to limit the present utility model, but various modifications and variations can be made to the present utility model by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.

Claims (12)

1. A shunt, comprising:
the split-flow structure (10) is provided with a first transition section (11), a second transition section (12) and a split-flow section (13) which are sequentially connected, wherein one end of the first transition section (11) away from the second transition section (12) is communicated with an inlet of the split-flow structure (10), and one end of the split-flow section (13) away from the second transition section (12) forms a split-flow outlet of the split-flow structure (10);
wherein, along the extending direction from the first transition section (11) to the second transition section (12), the flow cross-sectional area of the first transition section (11) is gradually increased, and the flow cross-sectional area of the second transition section (12) is gradually decreased.
2. The flow divider according to claim 1, characterized in that the length of the second transition section (12) is smaller than the length of the first transition section (11).
3. The flow divider according to claim 1, characterized in that the second transition section (12) is a first conical section with a cone angle α,40 ° - α -50 °; and/or the number of the groups of groups,
the length of the first transition section (11) is L 2 The second transition section (12) has a length L 4 ,11≤L 2 /L 4 Less than or equal to 15; and/or the number of the groups of groups,
the first transition section (11) has a flow cross-sectional area S 2 The second transition section (12) has a flow cross-sectional area S 4 ,2≤S 2 /S 4 ≤6。
4. The shunt of claim 1 wherein said shunt structure (10) further has a throat section (14), said throat section (14) being disposed between said second transition section (12) and said shunt section (13).
5. The flow divider according to claim 4, characterized in that the first transition section (11) has a length L 2 The length of the shunt section (13) is L 5 The length of the throat section (14) is L 1 The total length of the shunt is L;
wherein 0.01XL 2 2 +0.003×L 5 +0.001×L 1 2 +72=L。
6. The shunt according to claim 4, wherein said shunt is configured to provide a flow path for said fluid,
the flow cross-sectional area of the throat section (14) is S1, and the flow cross-sectional area of the first transition section (11) is S 2 ,2≤S 2 /S 1 Less than or equal to 6; and/or the number of the groups of groups,
the length of the throat section (14) is L 1 The length of the first transition section (11) is L 2 ,9≤L 2 /L 1 ≤11。
7. The flow divider according to claim 1, characterized in that the flow dividing structure (10) further has an inlet section (15), which inlet section (15) is connected to an end of the first transition section (11) remote from the second transition section (12), which inlet section (15) forms the inlet at an end remote from the first transition section (11);
the flow cross-sectional area of the inlet section (15) is S3, and the flow cross-sectional area of the first transition section (11) is
S 2 ,1.04≤S 2 /S 3 Less than or equal to 1.24; and/or the number of the groups of groups,
the length of the inlet section (15) is L 3 The length of the first transition section (11) is L 2 ,4.5≤L 3 /L 2 ≤6.5。
8. The flow divider according to claim 1, characterized in that the first transition section (11) is a conical section.
9. The shunt according to claim 1, wherein said shunt structure (10) comprises:
a first flow splitting housing (16), the first flow splitting housing (16) being provided with the first transition section (11);
and the second split shell (17) is installed on the first split shell (16), and the second transition section (12) and the split section (13) are arranged on the first split shell (16).
10. The shunt according to claim 9, characterized in that the second shunt housing (17) is sleeved over the first shunt housing (16).
11. The flow divider according to claim 10, characterized in that the second flow dividing housing (17) is provided with a mounting channel arranged at the end of the second transition section (12) remote from the flow dividing section (13), the end of the mounting channel close to the second transition section (12) being provided with a positioning step, the end of the first flow dividing housing (16) being abutted at the positioning step.
12. An air conditioner comprising the flow divider according to any one of claims 1 to 11.
CN202322265829.1U 2023-08-22 2023-08-22 Shunt and air conditioner with same Active CN220541435U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202322265829.1U CN220541435U (en) 2023-08-22 2023-08-22 Shunt and air conditioner with same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202322265829.1U CN220541435U (en) 2023-08-22 2023-08-22 Shunt and air conditioner with same

Publications (1)

Publication Number Publication Date
CN220541435U true CN220541435U (en) 2024-02-27

Family

ID=89976097

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202322265829.1U Active CN220541435U (en) 2023-08-22 2023-08-22 Shunt and air conditioner with same

Country Status (1)

Country Link
CN (1) CN220541435U (en)

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