CN209763845U - collecting pipe and heat exchanger - Google Patents
collecting pipe and heat exchanger Download PDFInfo
- Publication number
- CN209763845U CN209763845U CN201822180893.9U CN201822180893U CN209763845U CN 209763845 U CN209763845 U CN 209763845U CN 201822180893 U CN201822180893 U CN 201822180893U CN 209763845 U CN209763845 U CN 209763845U
- Authority
- CN
- China
- Prior art keywords
- baffle
- manifold
- shunting
- collecting pipe
- flow dividing
- 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.)
- Active
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a pressure manifold and heat exchanger, wherein, the pressure manifold is including distributing at the inside reposition of redundant personnel baffle of pressure manifold, reposition of redundant personnel baffle includes: the connecting part is connected with the collecting pipe, and the shunting part is connected with the connecting part and used for shunting the fluid in the collecting pipe, and a fluid passage opening is formed by the periphery of the shunting part and the inner wall of the collecting pipe. The utility model discloses can effectively reduce the liquid phase refrigerant deposit volume of pressure manifold bottom, and increase the liquid phase refrigerant distribution volume of connecting in the flat pipe at pressure manifold middle part to make the whole homogeneity that divides liquid of heat exchanger improve by a wide margin.
Description
Technical Field
The utility model relates to a heat transfer technical field especially relates to a pressure manifold and heat exchanger.
background
The existing micro-channel heat exchanger is widely applied in the field of air-conditioning refrigeration, mainly comprises three parts, namely a collecting pipe, a flat pipe and a fin, wherein the collecting pipe is vertically arranged or horizontally arranged and is divided into a vertical micro-channel heat exchanger and a horizontal micro-channel heat exchanger. When the refrigerant flows in the horizontally arranged collecting pipes, pressure loss caused by gravity exists, the part of the loss can be avoided due to the fact that the collecting pipes are vertically arranged, and the heat exchange efficiency is higher.
After the refrigerant enters the collecting pipe, the main flow direction of the refrigerant is firstly decelerated and ascended along the direction of the collecting pipe until the end cover starts to accelerate and descend, the refrigerant is distributed to the flat pipes along the way during the descending, the refrigerant is deposited at the bottom of the collecting pipe, the liquid-phase refrigerant of the flat pipes at the bottom is excessive, the speed of the refrigerant in the middle of the collecting pipe is high, the liquid-phase refrigerant in the middle is little, the distribution conditions of the gas-liquid two-phase region and the overheating region of the refrigerant are shown in figure 1, wherein E represents the gas-liquid two-phase region, F represents the overheating region, a curve between E and F is a boundary line between the gas-liquid two-phase region and the overheating region of. Therefore, when the refrigerant in the vertically-arranged collecting pipe flows to the flat pipe, the flow of the refrigerant in the flat pipe is uneven under the influence of gravity, and when the refrigerant is in a gas-liquid two-phase state, the uneven degree of gas and liquid entering the flat pipe is intensified, so that the heat exchange performance is influenced.
SUMMERY OF THE UTILITY MODEL
Therefore, it is necessary to provide a collecting pipe and a heat exchanger for solving the problem of uneven heat exchange caused by the fact that a refrigerant enters a flat pipe through the collecting pipe.
in order to achieve the above purpose, the utility model adopts the following technical proposal: a manifold comprising a flow distribution baffle distributed within the manifold, the flow distribution baffle comprising:
A connecting part for connecting the collecting pipe,
And the flow dividing part is connected with the connecting part and used for dividing the fluid in the collecting pipe, and a fluid passage opening is formed by the periphery of the flow dividing part and the inner wall of the collecting pipe.
In one embodiment, the flow dividing baffle is sheet-shaped, and the plane of the flow dividing baffle is perpendicular to the axis of the collecting main.
In one embodiment, the side wall of the collecting pipe is provided with a positioning opening matched with the connecting part, and the connecting part is fixedly inserted into the positioning opening.
In one embodiment, the flow dividing portion is a strip shape having two opposite sides, one side is attached to the inner wall, the other side faces the inside of the flow collecting pipe, and the edge shape is a straight line or an arc.
In one embodiment, the flow dividing baffle further comprises a through hole which is formed in the flow dividing part and through which fluid in the collecting pipe passes.
In one embodiment, the part of the flow dividing part between the fluid passage opening and the through hole is strip-shaped and is located in the middle area of the cross section of the collecting main.
In one embodiment, the flow distribution baffle further comprises a mounting portion extending from the connecting portion toward the outside of the header.
In one embodiment, the connecting portion and the flow dividing portion are of an integral or separate structure.
The utility model also provides a heat exchanger, include the pressure manifold and with a plurality of flat pipes that the pressure manifold is connected.
In one embodiment, along the axial direction of the collecting pipe, the part of the collecting pipe between adjacent flat pipes is a shunting area, and the shunting baffle is arranged in each shunting area;
in the two adjacent flow dividing areas, a flow dividing baffle in one flow dividing area is positioned on one side opposite to the flat pipe port; and the shunting baffle in the other shunting area is in a position parallel to the side edge of the flat pipe.
In one embodiment, along the axial direction of the collecting pipe, the part of the collecting pipe between adjacent flat pipes is a shunting area, and the shunting baffle is arranged in each shunting area;
The shunting baffle of each shunting area is positioned at one side opposite to the flat pipe port; or
The shunting baffles in each shunting area are parallel to the side edges of the flat tubes.
The utility model provides a pressure manifold and the heat exchanger can effectively reduce the liquid phase refrigerant deposit volume of pressure manifold bottom, and has increased the liquid phase refrigerant distribution volume of connecting in the flat pipe at pressure manifold middle part to the homogeneity that makes the whole minute liquid of heat exchanger improves by a wide margin, has solved the refrigerant and has sedimentated in pressure manifold bottom, makes the flat pipe liquid phase refrigerant of bottom too much, and the refrigerant is very fast in pressure manifold middle part speed, leads to the liquid phase refrigerant at middle part technical problem less than a bit.
Drawings
FIG. 1 is a prior art distribution diagram of two gas and liquid phases and superheat zones of refrigerant in a header without a flow distribution baffle;
Fig. 2 is a schematic structural diagram of a heat exchanger according to an embodiment of the present invention;
FIG. 3 is a top view of FIG. 2;
3 FIG. 3 4 3 is 3 a 3 schematic 3 partial 3 cross 3- 3 sectional 3 view 3 taken 3 at 3 A 3- 3 A 3 of 3 FIG. 33 3; 3
FIG. 5 is a schematic cross-sectional view taken at B-B of FIG. 3;
Fig. 6 is a schematic structural view of a flow dividing baffle according to an embodiment of the present invention;
FIG. 7 is a front view of FIG. 6;
FIG. 8 is a schematic view of the distribution of the flow distribution baffles provided in FIG. 6 within a header;
FIG. 9 is a schematic cross-sectional view at C-C of FIG. 8;
FIG. 10 is a schematic cross-sectional view taken at D-D of FIG. 8;
Fig. 11 is a schematic view of a flow dividing baffle according to another embodiment of the present invention;
FIG. 12 is a front view of FIG. 11;
Fig. 13 is a schematic view of the distribution of the flow distribution baffles provided in fig. 11 within a header;
Fig. 14 is a schematic structural view of a flow dividing baffle according to another embodiment of the present invention;
FIG. 15 is a front view of FIG. 14;
fig. 16 is a schematic view of the distribution of the flow distribution baffles provided in fig. 14 within a header;
Fig. 17 is a schematic view of the flow direction of the flow dividing baffle of fig. 14 within a header.
Description of the main elements
The following detailed description of the invention will be further described with reference to the accompanying drawings.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
it will be understood that when an element is referred to as being "mounted on" another element, it can be directly on the other element or intervening elements may also be present. When a component is referred to as being "disposed on" another component, it can be directly on the other component or intervening components may also be present. When an element is referred to as being "secured to" another element, it can be directly secured to the other element or intervening elements may also be present.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "or/and" includes any and all combinations of one or more of the associated listed items.
it should be noted that the technical background is only described for the convenience of clear and complete description of the technical solutions of the present invention and for the understanding of the technical personnel in the field, and the technical solutions are not considered to be known to the technical personnel in the field only because the technical solutions are described in the background of the present invention.
Referring to fig. 2 to 17, the present invention further provides a heat exchanger, which includes a collecting pipe 100 and a plurality of flat tubes 200 connected to the collecting pipe 100.
It will be appreciated that the fluid flows into and collects in header 100 and redistributes into each of the flat tubes 200 connected to header 100, where the fluid exchanges heat within flat tubes 200. In the present embodiment, the fluid is a refrigerant, including a refrigerant having a gas-liquid two-phase, a gas-phase refrigerant, and a liquid-phase refrigerant, and the heat exchanger is a heat exchanger with flat tubes 200, that is, a microchannel heat exchanger. In other embodiments, a heat exchanger such as a round tube may be used, and will not be described in detail.
As shown in fig. 2-5, in the schematic structural diagrams of the heat exchanger, an inlet pipe 101 extending into the collecting main 100 is disposed on a side wall of the collecting main 100 opposite to a port of the flat pipe 200, and the inlet pipe 101 is used for conveying a fluid into the collecting main 100. The fluid flows into each flat pipe 200 behind pressure manifold 100, for improving heat exchange efficiency, is equipped with fin 300 between the flat pipe 200, and fin 300 is not the utility model discloses an invention main points, no longer gives details.
The inlet pipe 101 may be positioned at the bottom, middle, or top of the manifold 100 (as shown in the orientation of fig. 4), so as to deliver fluid into the manifold 100. In one embodiment, the inlet pipe 101 is located at the bottom of the flat pipe 200, and the inlet pipe 101 is opened with an opening 1011 on a side facing the top of the collecting main 100, so that the fluid can flow into the collecting main 100 from the inlet pipe 101 through the opening 1011.
specifically, when the heat exchanger is in an operating state, the collecting pipe 100 is vertically arranged, so that pressure loss caused by gravity of the horizontally arranged collecting pipe 100 can be avoided, the heat exchange efficiency is improved, and accordingly, the flat pipes 200 connected with the collecting pipe 100 are arranged in parallel. In other embodiments, the axis of the header 100 may be inclined at an angle to the horizontal plane, and the plane of the flat tube 200 may also be inclined from the horizontal plane. One end of flat tube 200 is connected to header 100 connected to inlet pipe 101, and the other end of flat tube 200 is connected to header 100 connected to outlet pipe 102.
The utility model provides a pressure manifold 100, including distributing at the inside reposition of redundant personnel baffle 10 of pressure manifold 100, reposition of redundant personnel baffle 10 includes: the fluid collecting device comprises a connecting part 11 connected with the collecting pipe 100, and a flow dividing part 12 connected with the connecting part 11 and used for dividing fluid in the collecting pipe 100, wherein a fluid passage opening 13 is formed between the periphery of the flow dividing part 12 and the inner wall of the collecting pipe 100. In the following description, the collecting main 100 is designated as collecting main 100 with the flow dividing baffle 10, i.e. collecting main 100 with the inlet pipe 101 in fig. 4.
The outer periphery of the flow dividing portion 12 is not sealed against the inner wall of the header 100 everywhere, and a fluid passage opening 13 allowing fluid to pass through is reserved, the position of the fluid passage opening 13 in the cross section of the header 100 can be in the middle area or close to the edge area or combined in various ways, and the fluid passage opening 13 in the cross section of the header 100 can be a whole area or a plurality of areas isolated from each other, which is related to the shape of the flow dividing portion 12 itself.
It can be understood that the flow dividing baffle 10 is distributed inside the header 100, connected to the header 100 through the connection portion 11, and provided with a flow dividing portion 12 for dividing the refrigerant inside the header 100, the refrigerant is divided by the flow dividing portion 12 into the fluid passage ports 13, and the liquid-phase refrigerant is deposited on the flow dividing portion 12 during descending, wherein the fluid passage ports 13 can be seen in fig. 8 and 17.
After flowing into the header 100 through the inlet pipe 101, the fluid flows in the axial direction of the header 100, flows in the main upward flow direction through the fluid passage port 13, reaches the end cap 400, and then flows downward. In the descending process, the part of the gas-liquid two-phase refrigerant enters the flat tube 200, and meanwhile, the liquid-phase refrigerant is separated due to the action of gravity and is gathered on the upper surface of the flow dividing baffle 10. As the amount of the liquid-phase refrigerant accumulated on the flow dividing baffle 10 increases, the liquid-phase refrigerant separates from the flow dividing baffle 10 and falls downward, the fallen liquid-phase refrigerant and the ascending gas-liquid two-phase refrigerant are mixed at the fluid passage port 13, and are distributed together with the gas-liquid two-phase refrigerant to enter the flat tube 200 positioned at the upper part of the flow dividing baffle 10 under the action of the ascending gas-liquid two-phase refrigerant, so that the distribution amount of the liquid-phase refrigerant at the flat tube 200 connected with the middle part of the collecting pipe 100 can be effectively increased.
therefore, the liquid-phase refrigerant separated and deposited at the bottom of the collecting pipe 100 is reduced to a great extent by arranging the collecting pipe 100 with the flow dividing baffle 10 in the heat exchanger, and meanwhile, the flow of the liquid-phase refrigerant is increased due to the fact that the distribution frequency of the flat pipe 200 connected with the middle of the collecting pipe 100 is increased, and the uniformity of the refrigerant in the flat pipe 200 of the heat exchanger is improved.
Specifically, taking the orientation in fig. 4 as an example, the dividing baffle 10 may be distributed in the central portion of the header 100, or may be distributed at the bottom, the central portion, and the top of the header 100 along the axial direction of the header 100. In this embodiment, the dividing baffle 10 is centrally distributed in the middle of the collecting main 100, and the structure is simple and convenient for processing. The number of the flow dividing baffles 10 can be set according to the requirement, such as 1, 2, 3 or more.
The dividing baffle 10 may be generally plate-like or other shapes, such as a hemispherical body with grooves, which may deposit liquid phase refrigerant. In one embodiment, the dividing baffle 10 is sheet-shaped, and the plane of the dividing baffle 10 is perpendicular to the axis of the collecting main 100, so that the liquid-phase refrigerant is deposited on the upper surface of the plane of the dividing baffle 10.
the dividing baffle 10 is fixed to the inner wall of the header 100 by a connecting portion 11, and may be fixedly connected by welding, for example. In order to facilitate the fixing, in one embodiment, the sidewall of the collecting main 100 is provided with a positioning opening 14 matching with the connecting portion 11, and the connecting portion 11 is fixedly inserted into the positioning opening 14.
The positioning hole 14 can be machined by cutting or the like, the shape, the width and the like of the positioning hole 14 correspond to the connecting portion 11 of the flow dividing baffle 10, so that the connecting portion 11 is in place and the positioning hole 14 is matched and sealed to the maximum extent, and in order to ensure the sealing effect, the inserting portion of the connecting portion 11 can be welded on the outer wall of the collecting main 100.
regardless of the width of the positioning port 14, the positioning port 14 may be a two-dimensional structure or a three-dimensional structure in itself, the two-dimensional structure extending, for example, along an arc in a plane perpendicular to the axis of the manifold 100 or at an angle to the axis of the manifold 100.
As shown in fig. 2 and 4, the positioning hole 14 can be used to weld the outer wall of the header 100 without welding the inner wall of the header 100, thereby reducing the difficulty in machining. The connecting portion 11 and the positioning opening 14 are correspondingly arranged, the connecting portion 11 extends along the circumferential direction of the collecting pipe 100, the end face of one side of the connecting portion 11 is flush with the inner wall of the collecting pipe 100, and the end face of the other side of the connecting portion 11 is flush with the outer wall of the collecting pipe 100.
To facilitate positioning and mounting of the flow dividing baffle 10, in one embodiment, the flow dividing baffle 10 further includes a mounting portion 16 extending from the connecting portion 11 toward the exterior of the manifold 100.
The mounting portion 16 may function as a handle during assembly, with the mounting portion 16 being grasped for insertion and welding operations. In addition, the mounting part 16 is positioned outside the collecting pipe 100, so that the edge of the positioning opening can be conveniently welded, and the damage to the connecting part 11 during welding is reduced.
in order to improve the sealing effect of the welding, the mounting parts 16 are distributed along the positioning opening 14; also, the mounting portion 16 is coplanar with the attachment portion 11 at a location adjacent the locating opening 14 to facilitate the welding operation.
The mounting portion 16 may be any shape, such as a protrusion. By acting on the mounting portion 16, the detachment and mounting of the diversion baffle 10 is achieved. In the present embodiment, as shown in fig. 6 and 7, the outer edge of the mounting portion 16 is located tangential to the outer wall of the header 100.
Specifically, the connecting portion 11 and the flow dividing portion 12 are integrated or separated. For convenience of processing, the connecting portion 11 and the flow dividing portion 12 may be integrally formed, and the mounting portion 16, the connecting portion 11 and the flow dividing portion 12 may also be integrally formed, and similarly, may be formed as separate structures.
The flow dividing portion 12 extends from the connecting portion 11 toward the inside of the header 100, and the extending distance thereof may be large or small, so that the flow dividing portion 12 covers a part of the cross-sectional area of the header 100 for the passage of fluid. In one embodiment, the flow dividing portion 12 is a strip having two opposite sides, one side is adjacent to the inner wall, the other side faces the inside of the collecting main 100, and the edge is linear or arc. The width of the strip-shaped shunt part is not limited.
In one embodiment, as shown in the flow dividing baffle 10 shown in fig. 6-7, the flow dividing portion 12 extends from the connecting portion 11 to the inside of the collecting main 100 for a relatively short distance, the flow dividing portion 12 is substantially in the shape of a closed figure formed by a circular arc and a straight line, and the edge of the other side of the flow dividing portion 12 is in the shape of a straight line. The distribution of the dividing baffle 10 in the collecting main 100 is: along the axial direction of the collecting pipe 100, the part of the collecting pipe 100 between the adjacent flat pipes 200 is a shunting area, and the shunting baffle 10 is arranged in each shunting area; in the two adjacent flow dividing areas, the flow dividing baffle 10 in one flow dividing area is positioned on one side opposite to the opening 200 of the flat pipe; the two shunt baffles 10 in the other shunt area are positioned at two opposite sides of the flat tube 200.
As shown in fig. 8-10, the first baffle 103 is located at the side opposite to the opening of the flat tube 200 and at the diversion area at the lower end. The second baffle 104 and the third baffle 105 are located in the upper end shunting area and are located in a position parallel to the side edge of the flat tube 200. Further, second baffle 104 and the third baffle are distributed on two opposite sides of flat tube 200.
In one embodiment, as shown in the flow dividing baffle 10 shown in fig. 11-12, the flow dividing portion 12 is in a fan-ring shape and is disposed coaxially with the collecting main 100, the edge of the other side of the flow dividing portion 12 is in an arc shape, and the circumferential angle corresponding to the flow dividing portion 12 ranges from 45 ° to 200 °. In other embodiments, the edge shape of the other side of the flow dividing part 12 may also be an irregular line. The distribution of the dividing baffle 10 in the collecting main 100 is: along the axial direction of the collecting pipe 100, the part of the collecting pipe 100 between the adjacent flat pipes 200 is a shunting area, and the shunting baffle 10 is arranged in each shunting area; the dividing baffles 10 in each dividing region are located at positions parallel to the side edges of the flat tubes 200, and further, two dividing baffles 10 in each dividing region are located at two opposite sides of the flat tubes 200, as shown in fig. 13. The difference in height between diverter baffle 10 and the adjacent flat tube 200 is not limited. Preferably, the dividing baffle 10 is distributed in the middle between the two flat tubes 200 in height.
In one embodiment, when the flow dividing portion 12 extends from the connecting portion 11 to the inside of the collecting main 100 for a relatively large distance, the flow dividing baffle 10 further includes a through hole 15 opened on the flow dividing portion 12 for allowing the fluid in the collecting main 100 to pass through. As shown in the flow dividing baffle 10 of fig. 14-15, the opening of the through holes 15 increases the flow dividing effect of the refrigerant in the collecting main 100. In particular, said through hole 15 is substantially semicircular. The area where the through hole 15 flows is used as a first diversion area, and the fluid passage opening 13 formed by the periphery of the diversion baffle 10 and the inner wall of the collecting main 100 is used as a second diversion area. When the gas-liquid two-phase refrigerant flows in the collecting pipe 100, the first shunting area serves as a main circulation area, most of the gas-liquid two-phase refrigerant flows in the first shunting area, and a small part of the gas-liquid two-phase refrigerant enters the second shunting area, so that the flow dead zone in the collecting pipe 100 provided with the shunting baffle 10 can be effectively prevented, the disturbance of the gas-liquid two-phase refrigerant is accelerated, and the distribution uniformity is improved.
Specifically, the part of the flow dividing part 12 located between the fluid passage opening 13 and the through hole 15 is strip-shaped and located in the middle area of the cross section of the collecting main 100. The flow dividing portion 12, which is located in the middle region of the cross-section of the header 100, facilitates the descending gas-liquid two-phase refrigerant to deposit a liquid-phase refrigerant. The distribution of the dividing baffle 10 in the collecting main 100 is: along the axial direction of the collecting pipe 100, the part of the collecting pipe 100 between the adjacent flat pipes 200 is a shunting area, and the shunting baffle 10 is arranged in each shunting area; the diversion baffle 10 of each diversion area is positioned on the side opposite to the opening of the flat tube 200, and specific reference can be made to fig. 16-17.
The utility model provides a heat exchanger with pressure manifold of reposition of redundant personnel baffle and use pressure manifold can effectively reduce the liquid phase refrigerant deposition volume of pressure manifold 100 bottom, and increased the liquid phase refrigerant distribution volume of connecting in the flat pipe 200 at pressure manifold 100 middle part, thereby make the whole homogeneity that divides liquid of heat exchanger improve by a wide margin, solved the refrigerant at the deposition of pressure manifold 100 bottom, the flat pipe 200 liquid phase refrigerant of the bottom that leads to is too much, and the refrigerant is very fast at pressure manifold 100 middle part speed, lead to the less technical problem of liquid phase refrigerant at middle part.
the technical features of the embodiments described above may be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the embodiments described above are not described, but should be considered as being within the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
the above-mentioned embodiments only represent some embodiments of the present invention, and the description thereof is specific and detailed, but not to be construed as limiting the scope of the present invention. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention. Therefore, the protection scope of the present invention should be subject to the appended claims.
Claims (10)
1. A manifold comprising a flow distribution baffle distributed within the manifold, the flow distribution baffle comprising:
a connecting part for connecting the collecting pipe,
And the flow dividing part is connected with the connecting part and used for dividing the fluid in the collecting pipe, and a fluid passage opening is formed by the periphery of the flow dividing part and the inner wall of the collecting pipe.
2. A manifold in accordance with claim 1, wherein said dividing baffle is sheet-like and is oriented in a plane perpendicular to the axis of said manifold.
3. The collecting main of claim 1, wherein the sidewall of the collecting main is provided with a positioning opening matching with the connecting portion, and the connecting portion is fixedly inserted into the positioning opening.
4. A manifold in accordance with claim 1, wherein said manifold portion is strip-shaped and has opposite sides, one side abutting the inner wall and the other side facing the interior of the manifold and having a straight or curved edge.
5. A manifold in accordance with claim 1, wherein said dividing baffle further comprises a through-hole in the flow dividing portion for passage of fluid in the manifold.
6. A manifold in accordance with claim 5, wherein the flow dividing portion is strip-shaped between the fluid passage opening and the through-hole and is located in a middle region of the cross-section of the manifold.
7. A manifold in accordance with claim 1, wherein said connecting portion is integral with or separate from the flow splitting portion, and said flow splitting baffle further comprises a mounting portion extending from the connecting portion toward the exterior of the manifold.
8. A heat exchanger comprising a header and a plurality of flat tubes connected to the header, wherein the header is a header according to any one of claims 1 to 7.
9. The heat exchanger according to claim 8, wherein along the axial direction of the collecting pipe, the part of the collecting pipe between the adjacent flat pipes is a shunting area, and the shunting baffle is arranged in each shunting area;
In the two adjacent flow dividing areas, a flow dividing baffle in one flow dividing area is positioned on one side opposite to the flat pipe port; and the shunting baffle in the other shunting area is in a position parallel to the side edge of the flat pipe.
10. The heat exchanger according to claim 8, wherein along the axial direction of the collecting pipe, the part of the collecting pipe between the adjacent flat pipes is a shunting area, and the shunting baffle is arranged in each shunting area;
the shunting baffle of each shunting area is positioned at one side opposite to the flat pipe port; or
the shunting baffles in each shunting area are parallel to the side edges of the flat tubes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822180893.9U CN209763845U (en) | 2018-12-25 | 2018-12-25 | collecting pipe and heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822180893.9U CN209763845U (en) | 2018-12-25 | 2018-12-25 | collecting pipe and heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209763845U true CN209763845U (en) | 2019-12-10 |
Family
ID=68747235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822180893.9U Active CN209763845U (en) | 2018-12-25 | 2018-12-25 | collecting pipe and heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209763845U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112944951A (en) * | 2021-04-01 | 2021-06-11 | 哈尔滨理工大学 | Microchannel heat exchanger and shunting structure |
| CN114812019A (en) * | 2021-01-28 | 2022-07-29 | 浙江盾安人工环境股份有限公司 | Micro-channel heat exchanger |
-
2018
- 2018-12-25 CN CN201822180893.9U patent/CN209763845U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114812019A (en) * | 2021-01-28 | 2022-07-29 | 浙江盾安人工环境股份有限公司 | Micro-channel heat exchanger |
| CN114812019B (en) * | 2021-01-28 | 2024-05-14 | 浙江盾安人工环境股份有限公司 | Microchannel heat exchanger |
| CN112944951A (en) * | 2021-04-01 | 2021-06-11 | 哈尔滨理工大学 | Microchannel heat exchanger and shunting structure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2660549B1 (en) | Heat exchanger | |
| CN209763845U (en) | collecting pipe and heat exchanger | |
| US11624565B2 (en) | Header box and heat exchanger | |
| US6920916B2 (en) | Layered heat exchangers | |
| JP2013537298A (en) | Refrigerant conduit and heat exchanger provided with the refrigerant conduit | |
| CN111780595B (en) | Heat exchange plate and micro-channel heat exchanger | |
| JP4256515B2 (en) | Multi-tube heat exchanger | |
| CN210051186U (en) | Three-medium heat exchanger | |
| CN208936591U (en) | Microchannel heat exchanger and air conditioner | |
| CN209857727U (en) | Collecting pipe, heat exchanger and air conditioner outdoor unit | |
| CN113959236A (en) | Annular steam condenser suitable for deep sea high pressure and working method thereof | |
| CN211084507U (en) | Parallel flow evaporator of automobile air conditioner | |
| CN106855369B (en) | Heat exchanger | |
| CN209745065U (en) | Plate heat exchanger with water collecting tank | |
| CN106895616A (en) | A kind of gas-liquid separator with surface tension formula cell body | |
| US10697717B2 (en) | Water head for an evaporator | |
| US20220026152A1 (en) | Heat Exchanger Flat Tube and Heat Exchanger with Heat Exchanger Flat Tube | |
| CN206959399U (en) | A kind of gas-liquid separator with surface tension formula cell body | |
| CN109084608B (en) | Heat exchange plate | |
| JPS6345606B2 (en) | ||
| CN111912283A (en) | Liquid separation structure and heat exchanger | |
| CN213841422U (en) | Oil separating assembly, oil separator and air conditioning system | |
| CN116154361B (en) | Cold plate and battery pack | |
| CN215177179U (en) | Heat exchanger flat tube and heat exchanger | |
| CN219064239U (en) | Plate heat exchanger and air conditioner |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |