This application is a 35 U. S. C. § 371 National Phase conversion of International (PCT) Patent Application No. PCT/CN2019/087390, entitled “Heat Exchanger”, filed on May 17, 2019, which requires priorities of a Chinese Patent Application filed on May 17, 2018 with Application No. 201820733443.5 and a Chinese Patent Application filed on Jul. 27, 2018 with Application No. 201821207479.6, the entire contents of which are incorporated into this application herein by reference. The PCT International Patent Application was filed and published in Chinese.
The present disclosure relates to a field of heat exchange technology, for example, a heat exchanger.
Taking CO2 as a refrigerant fluid for example, working pressure of a double-row heat exchanger is high, thus the strength requirement of the heat exchanger collecting pipe is relatively high. Commonly used D-tubes cannot meet the bursting pressure requirements, so in order to meet their design requirements, the collecting pipe mostly adopts a method of increasing the wall thickness of the D-tubes. However, this will cause a size of the collecting pipe to be too large which renders the weight of the heat exchanger to be too heavy, and reduce the windward area under the same external dimensions.
The present disclosure provides a heat exchanger to solve the problems that when the heat exchanger uses a refrigerant fluid with high working pressure in the related art, the size of the collecting pipe is too large and the windward area is reduced under the same external dimensions.
In one embodiment, the present disclosure provides a heat exchanger including a first collecting pipe which includes a first upper main board and a first lower main board. A first channel and a second channel are formed between the first upper main board and the first lower main board. Flat tubes extend into the first channel and the second channel.
In the drawings:
This embodiment provides a heat exchanger. As shown in
As shown in
In this embodiment, a vertical height between the highest point and the lowest point of the first channel 14 and the second channel 15 is L1, and a maximum value of the width of the first channel 14 and the second channel 15 is L2. The ratio of L1 to L2 is not greater than 1:4. Through the setting of the above ratio and the structure of the first upper main board 11 with a flat top surface, the size of the first collecting pipe 1 can be made more compact, and thus the heat exchanger has a larger windward area and higher heat exchange performance. Moreover, the heat exchanger has a higher structural strength and can meet high strength requirements when using a refrigerant fluid with high working pressure.
In this embodiment, a plurality of first flat tube slots 123 are provided on the first lower main board 12, and the wall of the first flat tube slots 123 protrudes toward the second collecting pipe 2. The two rows of flat tubes 3 are inserted into the first flat tube slots 123 so as to be placed in the first channel 14 and the second channel 15. The above-mentioned first flat tube slots 123 adopt a structure of outward burring (specifically burring away from the first upper main board 11), which can increase the contact area with the flat tubes 3, thereby increasing the connection strength of the first flat tube slots 123 and the flat tubes 3. In this embodiment, the first flat tube slots 123 and the flat tubes 3 are connected by brazing. In this embodiment, the length of the first flat tube slot 123 is greater than of the shrinkage width of the flat tubes 3 by 0.05 mm to 0.1 mm. The width of the first flat tube slot 123 is greater than the thickness of the flat tubes 3 by 0.05 mm to 0.12 mm. The height of the burring of the first flat tube slot 123 is 0.7-1.3 times of the thickness of the flat tubes 3.
Referring to
In each channel of the second lower main board 21, a group of partition slots 114 are formed along a width direction. Each partition slot 114 is inserted by the corresponding one of the fourth partitions 26. By the arrangement of the fourth partitions 26, the third channel 24 and the fourth channel 25 can be divided into two parts, which can realize the multi-process operation of the refrigerant.
As shown in
The second collecting pipe 2 of this embodiment is composed of three main boards, which can further meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure.
The operating principle of the above heat exchanger in this embodiment is as follows:
Firstly, the refrigerant fluid flows through the inlet 4 into a partial channel of the third channel 24 which is located on the first side of the fourth partitions 26 of the second collecting pipe 2. At this time, the refrigerant fluid enters a first process. In the first process, the refrigerant fluid enters the rear flat tubes 3 and flows downwardly along the rear flat tubes 3. During this time, the air and the refrigerant fluid exchange heat, the refrigerant fluid evaporates and absorbs heat, and part of the liquid evaporates into steam, and the dryness increases. Then, the refrigerant fluid enters the first channel 14 of the first collecting pipe 1 along the rear flat tubes 3 and thus enters a second process. In the second process, the refrigerant fluid enters part of the third channel 24 located on the second side of the fourth partitions 26 through the rear flat tubes 3, and further evaporates and absorbs heat during this process. Subsequently, the refrigerant fluid enters part of the channel on the second side of the fourth partitions 26 of the fourth channel 25 of the second collecting pipe 2 and thus enters a third process. In the third process, the refrigerant fluid enters the front flat tubes 3, further evaporates and absorbs heat, and then enters the second channel 15 of the first collecting pipe 1 and thus enters a fourth process. In the fourth process, the refrigerant fluid flows through the front row of flat tubes 3 to part of the fourth channel 25 on the first side of the fourth partitions 26, and further exchanges heat with the air during the flow process, evaporates into steam, and then the steam flows out through the outlet 5 to complete a heat exchange process.
This embodiment provides a heat exchanger. The difference between the heat exchanger and the heat exchanger described in the first embodiment is that the structure of the first collecting pipe 1 in this embodiment is different. The rest of the structure is the same as the first embodiment which will not be repeated here. Only the structure of the first collecting pipe 1 of this embodiment will be described in detail below.
Referring to
Two grooves 111 are defined in the first upper main board 11. A second middle rib 112 is provided between the two grooves 111. A first channel 14 and a second channel 15 are formed by the two grooves 111, the second middle rib 112 and the first lower main board 12. One ends of a first row of flat tubes 3 are placed in the first channel 14, and the same ends of a second row of flat tubes 3 are placed in the second channel 15.
In one embodiment, a vertical height respectively between the highest point of the first channel 14 and the second channel 15 and the lowest point of the first channel 14 and the second channel 15 is L1, and a maximum value of the width of the first channel 14 and the second channel 15 is L2. The ratio of L1 to L2 is not greater than 1:4. Through the setting of the above ratio and the structure of the first upper main board 11 with a flat top surface, while working with a refrigerant fluid of high working pressure, the size of the first collecting pipe 1 can be made more compact, and thus the heat exchanger has a larger windward area and higher heat exchange performance. Moreover, the heat exchanger has a higher structural strength and can meet high strength requirements when using a refrigerant fluid with high working pressure.
In this embodiment, a plurality of first flat tube slots 123 are provided on the first lower main board 12, and the wall of the first flat tube slots 123 protrudes toward the second collecting pipe 2. The two rows of flat tubes 3 are inserted into the first flat tube slots 123 so as to be placed in the first channel 14 and the second channel 15. The above-mentioned first flat tube slots 123 adopt a structure of outward burring (specifically burring away from the first upper main board 11), which can increase the contact area with the flat tubes 3, thereby increasing the connection strength of the first flat tube slots 123 and the flat tubes 3. In this embodiment, the first flat tube slots 123 and the flat tubes 3 are connected by brazing. In this embodiment, the length of the first flat tube slots 123 is greater than of the shrinkage width of the flat tubes 3 by 0.05 mm to 0.1 mm. The width of the first flat tube slots 123 is greater than the thickness of the flat tubes 3 by 0.05 mm to 0.12 mm. The height of the burring of the tube slots 123 is 0.7-1.3 times of the thickness of the flat tubes 3.
The working principle of the heat exchanger of this embodiment is the same as that of the first embodiment, which will not be repeated here.
This embodiment provides a heat exchanger. The difference between the heat exchanger and the heat exchanger described in the second embodiment is that the structure of the first collecting pipe 1 in this embodiment is different. The rest of the structure is the same as the second embodiment which will not be repeated here. Only the structure of the first collecting pipe 1 of this embodiment will be described in detail below.
As shown in
This embodiment provides a heat exchanger. The difference between the heat exchanger and the heat exchanger described in the third embodiment is that the structure of the first collecting pipe 1 in this embodiment is different. The rest of the structure is the same as the first embodiment which will not be repeated here. Only the structure of the first collecting pipe 1 of this embodiment will be described in detail below.
As shown in
The structure of the above-mentioned first upper main board 11 is the same as the structure of the first upper main board 11 in the second embodiment, which will not be repeated here.
In this embodiment, two rows of first slots 131 are formed on the first intermediate main board 13. A first channel 14 and a second channel 15 are formed by the grooves 111 of the first upper main board 11, the first slots 131 and the first lower main board 12. With the above structure, not only the strength of the overall structure of the first collecting pipe 1 is increased, but also the structure of the first collecting pipe 1 is made more compact. Each of the first flat tube slots 123 of the first lower main board 12 corresponds to one of the first slots 131. One ends of the flat tubes 3 are sealed through the first flat tube slots 123 and placed in the first slots 131.
This embodiment provides a heat exchanger, which differs from the fourth embodiment in that the structure of the first collecting pipe 1 in this embodiment is different, and mounting positions of an end cap 8 and the inlet 4 and the outlet 5 thereon are different in this embodiment.
In one embodiment, referring to
In this embodiment, along a horizontal direction, the above-mentioned first partitions 16 are disposed adjacent to the inlet 4. The fourth partitions 26 are located on a side of the first partitions 16 away from the inlet 4, that is, the first partitions 16 are closer to the inlet 4 than the fourth partitions 26. In this way, the channel length of the second collecting pipe 2 on a first side of the fourth partitions 26 (a right side shown in
The rest of the structure of this embodiment is the same as that of the fourth embodiment, so it will not be repeated here.
The operation principle of the six-process heat exchange structure of the heat exchanger in this embodiment is described below:
Firstly, the refrigerant fluid enters a part of the first channel 14 located on the first side (the right side shown in
This embodiment provides a heat exchanger. As shown in
Referring to
As shown in
In this embodiment, the first collecting pipe 1 further includes a first reinforcing rib 113 which can be supported at the ends of the flat tubes 3. As shown in
In this embodiment, a plurality of sets of partition slots can be formed in each through slot of the first upper main board 11 along the width direction. The second partitions 116 can be inserted into each partition slot. Through the arrangement of multiple sets of second partitions 116, the above-mentioned through slots can be divided into multiple parts. The multiple parts of the through slots are capable of forming at least two chambers together with the first lower main board 12, so that the multi-process operation of the refrigerant can be realized.
In this embodiment, referring to
Moreover, since each through slot is provided with a first reinforcing rib 113 which separates each through slot into two sub-slots. Therefore, in this embodiment, by forming a through hole in the first reinforcing rib 113, or forming a slot at a lower end of the first reinforcing rib 113, or cutting off a part of the lower end of the first reinforcing rib 113, the two sub-slots can be achieved to communicate with each other (as shown in
As shown in
In this embodiment, an end of the first collecting pipe 1 that is not connected to the end cap 7 is provided with a blocking cap 8 to close the end of the first collecting pipe 1.
In this embodiment, as shown in
Referring to
In one embodiment, the above-mentioned second lower main board 21 has a structure of half Arabic number eight. The second lower main board 21 includes a fourth middle rib 211, a plurality of flow equalizing plates 212 and a second reinforcing rib 213. The fourth middle rib 211 is provided along the length direction of the second lower main board 21, and the fourth middle rib 211 separates the second lower main board 21 into two through slots. The two through slots encloses with the second upper main board 23 to form the third channel 24 and the fourth channel 25 described above. In the two rows of flat tubes 3, the lower ends of one row of flat tubes 3 extend into the third channel 24, and the lower ends of the other row of flat tubes 3 extend into the fourth channel 25. In this embodiment, the above-mentioned third channel 24 is provided corresponding to the first channel 14 of the first collecting pipe 1. The fourth channel 25 is provided corresponding to the second channel 15 of the first collecting pipe 1.
There are two second reinforcing ribs 213 supported on the ends of the flat tubes 3. The two second reinforcing ribs 213 are both arranged along the length direction of the second lower main board 21 and are parallel to the fourth middle rib 211. The two second reinforcing ribs 213 can increase the strength of the above-mentioned second lower main board 21, and thus also increase the overall strength of the second collecting pipe 2 in order to withstand the high pressure of the refrigerant fluid of high working pressure. In this embodiment, the above two second reinforcing ribs 213 are respectively placed in two through slots of the second lower main board 21, and the second reinforcing rib 213 divides each through slot into two mutually connected sub-slots. In one embodiment, the two sub-slots can be communicated by opening a through hole in the second reinforcing rib 213 or grooving the lower end of the second reinforcing rib 213 or cutting off a part of the second reinforcing rib 213.
Referring to
In this embodiment, the structure of the second upper main board 23 is exactly the same as the structure of the first lower main board 12, so the structure will not be repeated here. The second upper main board 23 can fix the second lower main board 21 to form the second collecting pipe 2. The second upper main board 23 can fix the second lower main board 21 to form the second collecting pipe 2.
In this embodiment, both ends of the second collecting pipe 2 are provided with blocking caps 8 to close the ends of the second collecting pipe 2.
The operating principle of the above heat exchanger in this embodiment is as follows:
First, the refrigerant fluid enters the first chamber 91 of the first collecting pipe 1 through the inlet 4. At this time, the refrigerant fluid enters a first process. The refrigerant fluid enters the rear flat tubes 3 and flows downwardly along the rear flat tubes 3. At this time, the air and the refrigerant fluid exchange heat, the refrigerant fluid evaporates and absorbs heat, part of the liquid evaporates into steam, and the dryness increases. The refrigerant fluid enters the third channel 24 of the second collecting pipe 2 along the rear flat tubes 3. Areas of the equalizing holes of the flow equalizing plates 212 in the third channel 24 sequentially decrease along the flow direction so as to partly throttle the refrigerant fluid, adjust the distribution, and the refrigerant fluid enters a second process. In the second process, the refrigerant fluid enters the second chamber 92 of the first collecting pipe 1 through the rear flat tubes 3, and further evaporates and absorbs heat during this process. Subsequently, the refrigerant fluid enters the third chamber 101 of the first collecting pipe 1 communicating with the second chamber 92, and enters a third process. In the third process, the refrigerant fluid enters the front flat tubes 3, and further evaporates and absorbs heat, and enters the fourth channel 25 of the second collecting pipe 2. Areas of the equalizing holes of the flow equalizing plates 212 in the fourth channel 25 sequentially decrease along the flow direction so as to partly throttle the refrigerant fluid, adjust the distribution, and the refrigerant fluid enters a fourth process. In the fourth process, the refrigerant fluid flows into the fourth chamber 102 of the first collecting pipe 1 through the front flat tubes 3. The refrigerant fluid further exchanges heat with the air during the flow process and evaporates into steam. Subsequently, the steam flows out through the outlet 5 to complete a heat exchange process.
The structure of the first collecting pipe 1 and the second collecting pipe 2 of this embodiment can meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure. Moreover, with the above-mentioned first collecting pipe 1 and second collecting pipe 2 having a more compact size, the heat exchanger of this embodiment has a larger windward area under the same external dimensions.
This embodiment also provides an air conditioner that uses the heat exchanger described in this embodiment as an evaporator, which can realize efficient heat exchange in a compact space of the air conditioner.
This embodiment provides a heat exchanger, which differs from the sixth embodiment in that the structure of the first collecting pipe 1 of this embodiment is different. Therefore, in this embodiment only the structure of the first collecting pipe 1 is described. Since the remaining structure is the same as that of the sixth embodiment, it will not be described in detail.
Referring to
As shown in
The above-mentioned third slots 172 are correspondingly disposed at the second chamber 92 and the third chamber 101. The second chamber 92 and the third chamber 101 are communicated with each other through the third slots 172. The upper ends of the other part of the flat tubes 3 in the two rows of flat tubes 3 are placed in the third slots 172. Referring to
The first collecting pipe 1 of this embodiment is composed of three main boards, which can further meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure.
This embodiment also provides an air conditioner that uses the heat exchanger described in this embodiment as an evaporator, which can realize efficient heat exchange in a compact space of the air conditioner.
This embodiment provides a heat exchanger, which differs from the sixth embodiment in that the structure of the second collecting pipe 2 of this embodiment is different. Therefore, in this embodiment, only the structure of the first collecting pipe 2 will be described. Since the remaining structures are the same as those in the sixth embodiment, it will not be repeated here.
In one embodiment, as shown in
As shown in
The lower ends of the flat tubes 3 are placed in the fourth slots 221. The distance between the ends of the flat tubes 3 placed in the fourth slots 221 and the second reinforcing rib 213 of the second lower main board 21 is half the thickness of the third intermediate main board 22. With the above structure, the refrigerant fluid in the through slot of the second lower main board 21 can enter the flat tubes 3 through the fourth slots 221, and the refrigerant fluid in the flat tubes 3 can enter the through slot of the second lower main board 21 through the fourth slots 221.
The second collecting pipe 2 of this embodiment is composed of three main boards, which can further meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure.
This embodiment also provides an air conditioner that uses the heat exchanger described in this embodiment as an evaporator, which can realize efficient heat exchange in a compact space of the air conditioner.
This embodiment provides a heat exchanger, which differs from the sixth embodiment in that the structures of the first collecting pipe 1 and the second collecting pipe 2 of this embodiment are different. The structure of the first collecting pipe 1 of this embodiment is the same as the structure of the first collecting pipe 1 described in the seventh embodiment, and the structure of the second collecting pipe 2 is the same as the structure of the second collecting pipe 2 described in the eighth embodiment. The rest of the structures of this embodiment is the same as those of the sixth embodiment, which will not be repeated here. A schematic view of the heat exchanger of this embodiment can be referred to
The first collecting pipe 1 and the second collecting pipe 2 of this embodiment are both composed of three main boards, which can further meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure.
This embodiment also provides an air conditioner that uses the heat exchanger described in this embodiment as an evaporator, which can realize efficient heat exchange in a compact space of the air conditioner.
This embodiment provides a heat exchanger, which differs from the ninth embodiment in that the structure of the second collecting pipe 2 in this embodiment is different, and the mounting positions of the end cap 7 and the inlet 4 and outlet 5 thereon are different in this embodiment.
In one embodiment, referring to
In this embodiment, the third partitions 214 are located adjacent to the inlet 4. The second partitions 116 are located on the side of the third partitions 214 away from the inlet 4. That is, the third partitions 214 are closer to the inlet 4 than the second partitions 116. This makes the length of the chamber of the first collecting pipe 1 be greater than the length of the chamber of the second collecting pipe 2, in the chambers of the first collecting pipe 1 and the second collecting pipe 2 on the same side. With the above structure, a six-process heat exchange structure of the heat exchanger can be realized.
The rest of the structure of this embodiment is the same as that of the ninth embodiment, so it will not be repeated here.
The operation principle of the six-process heat exchange structure of the heat exchanger in this embodiment is as follows:
Firstly, the refrigerant fluid enters a chamber of the third channel 24 through the inlet 4. At this time, the refrigerant fluid enters the first process. The refrigerant fluid enters the rear flat tubes 3 and flows upwardly along the rear flat tubes 3. At this time, the air and the refrigerant fluid exchange heat, the refrigerant fluid evaporates and absorbs heat, part of the liquid evaporates into steam, and the dryness increases. The refrigerant fluid enters the first chamber 91 of the first collecting pipe 1 along the rear flat tubes 3 and thus the refrigerant fluid enters the second process. Because of the second partitions 116, the refrigerant fluid in the second process enters the other chamber of the second collecting pipe 2 through a part of the flat tubes 3 communicating with the other chamber of the third channel 24 in the rear row, and the refrigerant fluid further evaporates and absorbs heat during this process. Subsequently, the refrigerant fluid in the other chamber of the second collecting pipe 2 flows from a side close to the third partitions 214 to a side far away from the third partitions 214. The refrigerant fluid enters the rear flat tubes 3 which are on the side away from the third partitions 214 and have not entered the refrigerant fluid, and refrigerant fluid flows upwardly along the rear flat tubes 3 to enter a third process. In the third process, the refrigerant fluid enters the second chamber 92 of the first collecting pipe 1 along the rear flat tubes 3. The refrigerant fluid evaporates and absorbs heat, part of the liquid evaporates into steam, and the dryness increases. After that, the refrigerant enters the third chamber 101 communicating with the second chamber 92 through the third slots 172 from the second chamber 92, and enters a fourth process. In the fourth process, the refrigerant flows downwardly through the front flat tubes 3, evaporates and absorbs heat, and flows into a chamber of the fourth channel 25. After that, the refrigerant flows into a part of the front flat tubes 3 on a side of the third partitions 214 near the inlet 4 through the chamber. The refrigerant flows upwardly along the part of the front flat tubes 3 to enter a fifth process. The refrigerant further evaporates and absorbs heat when flowing upwardly. When the refrigerant in the fifth process flows into the fourth chamber 102, the refrigerant will flow to a side away from the second partitions 116 in the fourth chamber 102, and the refrigerant will flow downwardly into the front flat tubes 3 corresponding to the other chamber of the fourth channel 25, and then enter the other chamber of the fourth channel 25. That is, the refrigerant enters a sixth process. In the sixth process, the refrigerant further evaporates and absorbs heat and eventually forms steam. Then the steam flows out through the outlet 5 to complete a heat exchange process.
In the heat exchanger of this embodiment, through the first collecting pipe 1 and the second collecting pipe 2 described above, a six-process heat exchange is realized. Moreover, the first collecting pipe 1 and the second collecting pipe 2 are composed of three main boards, which can further meet the high strength requirements of the heat exchanger when using a refrigerant fluid with high working pressure.
This embodiment also provides an air conditioner that uses the above-mentioned heat exchanger as an evaporator, which can realize efficient heat exchange in a compact space of the air conditioner.
This embodiment provides a thermal management system including a compressor, a throttling device and the heat exchanger described in any one of the first to tenth embodiments. The heat exchanger is arranged between the compressor and the throttling device, and the heat exchanger can be used as an evaporator or a condenser. Through the above heat exchanger, while working with a refrigerant fluid of high working pressure, the size of the heat exchanger is made more compact, the windward area of the heat exchanger is larger, and the heat exchange performance is higher.
Number | Date | Country | Kind |
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201820733443.5 | May 2018 | CN | national |
201821207479.6 | Jul 2018 | CN | national |
Filing Document | Filing Date | Country | Kind |
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PCT/CN2019/087390 | 5/17/2019 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2019/219076 | 11/21/2019 | WO | A |
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Number | Date | Country | |
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20210033343 A1 | Feb 2021 | US |