WO2023045073A1 - Heat dissipation assembly and fiber laser - Google Patents

Heat dissipation assembly and fiber laser Download PDF

Info

Publication number
WO2023045073A1
WO2023045073A1 PCT/CN2021/134479 CN2021134479W WO2023045073A1 WO 2023045073 A1 WO2023045073 A1 WO 2023045073A1 CN 2021134479 W CN2021134479 W CN 2021134479W WO 2023045073 A1 WO2023045073 A1 WO 2023045073A1
Authority
WO
WIPO (PCT)
Prior art keywords
flow channel
channel
commutation
heat dissipation
inner layer
Prior art date
Application number
PCT/CN2021/134479
Other languages
French (fr)
Chinese (zh)
Inventor
徐海军
李瑞清
朱亚辉
杨伟
刘江
Original Assignee
北京热刺激光技术有限责任公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 北京热刺激光技术有限责任公司 filed Critical 北京热刺激光技术有限责任公司
Publication of WO2023045073A1 publication Critical patent/WO2023045073A1/en

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01SDEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
    • H01S3/00Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
    • H01S3/02Constructional details
    • H01S3/04Arrangements for thermal management
    • H01S3/0404Air- or gas cooling, e.g. by dry nitrogen
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01SDEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
    • H01S3/00Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
    • H01S3/02Constructional details
    • H01S3/04Arrangements for thermal management
    • H01S3/0405Conductive cooling, e.g. by heat sinks or thermo-electric elements
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01SDEVICES USING THE PROCESS OF LIGHT AMPLIFICATION BY STIMULATED EMISSION OF RADIATION [LASER] TO AMPLIFY OR GENERATE LIGHT; DEVICES USING STIMULATED EMISSION OF ELECTROMAGNETIC RADIATION IN WAVE RANGES OTHER THAN OPTICAL
    • H01S3/00Lasers, i.e. devices using stimulated emission of electromagnetic radiation in the infrared, visible or ultraviolet wave range
    • H01S3/02Constructional details
    • H01S3/04Arrangements for thermal management
    • H01S3/042Arrangements for thermal management for solid state lasers

Definitions

  • the present application relates to the technical field of heat dissipation, in particular to heat dissipation components and fiber lasers.
  • Fiber laser refers to a laser that uses rare earth-doped glass fiber as a gain medium. Fiber laser has a wide range of applications, such as: laser fiber communication, laser space long-distance communication, industrial shipbuilding, automobile manufacturing, laser engraving, laser marking, laser cutting And metal or non-metal drilling, cutting or welding, etc.
  • a heat dissipation assembly includes a heat dissipation air duct and heat dissipation teeth arranged in the heat dissipation air duct, and a fan is arranged at one end of the heat dissipation air duct, so that the gas flows from the air inlet end of the heat dissipation air duct to the air outlet end of the heat dissipation air duct, and the gas is flowing During the process, heat is exchanged with the optical fiber disk to dissipate heat from the optical fiber disk.
  • the problem is that after the gas enters the air inlet end, it starts to exchange heat with the fiber optic disk. With the movement of the gas, the temperature of the gas also increases, and the temperature difference between the gas and the fiber optic disk decreases. The heat is reduced; therefore, the part of the optical fiber disk close to the air outlet has a small heat transfer, less heat dissipation, and a higher temperature.
  • the present application provides a heat dissipation assembly and a fiber laser to solve the technical problems of low heat transfer, less heat dissipation and high temperature existing in the prior art at the part of the fiber optic disc near the air outlet.
  • the present application provides a heat dissipation assembly, which may include: a flow channel, the flow channel may include an inner layer flow channel and an outer layer flow channel arranged side by side; in the length direction of the flow channel, the inner layer flow channel
  • the layer flow channel may include at least two inner layer sub-channels arranged at intervals
  • the outer layer flow channel may include at least two outer layer sub-channels arranged at intervals; in the length direction of the flow channel, adjacently arranged
  • the inner layer sub-channels and the outer layer sub-channels may communicate with each other, and the interconnected inner layer sub-channels and the outer layer sub-channels may be located at different positions.
  • the inner flow channel can be attached to the plate surface of the heat sink, and the outer flow channel can be set far away from the inner flow channel.
  • One side of the part to be radiated; at least one end of the flow channel can be provided with a fluid power source, and the fluid power source makes the cooling medium enter the inner layer flow channel and the outer layer flow channel respectively from the medium inlet end of the flow channel.
  • the medium In the medium conveying direction, the medium can first enter the first inner layer sub-channel and the first outer layer sub-channel, and then the medium can flow from the first inner layer sub-channel into the downstream second outer layer sub-channel, similarly , the medium can enter the downstream second inner layer outer channel from the first outer layer sub-channel, and so on until the medium flows out from the medium outflow end, during this process, the medium in the inner layer channel can be connected with the outer layer channel
  • the medium in the inner flow channel close to the radiated part has a large heat transfer rate, and the temperature difference with the radiated part is small, and the medium in the outer flow channel far away from the radiated part is compared with the medium in the inner flow channel The amount of heat exchange is small, and the temperature difference with the heat-dissipated parts is large.
  • the medium in the inner flow channel can exchange with the medium in the outer flow channel. After the medium in the outer flow channel enters the inner flow channel, it can communicate with the downstream flow channel.
  • the radiated part realizes a large amount of heat exchange, so that the heat dissipation of the radiated part is large and the cooling is large, so that the part of the radiated part close to the medium outflow end can have a large heat transfer, a large heat dissipation, a large cooling, and a low temperature.
  • the temperature difference between the two ends of the radiated part can be reduced, which is beneficial to improving the heat dissipation uniformity and temperature uniformity of the radiated part.
  • the heat-dissipated part is an optical fiber disc
  • it can naturally make the part of the optical fiber disc close to the medium outflow end have a large heat transfer, large heat dissipation, more cooling, and low temperature, which can be reduced, and then the temperature difference between the two ends of the optical fiber disc can be reduced. , which is conducive to improving the heat dissipation uniformity and temperature uniformity of the optical fiber disk.
  • a baffle may be provided in the flow channel, and the baffle may separate the flow channel to form the inner flow channel and the outer flow channel; the two sides of the baffle may be respectively connected
  • the baffle in the inner layer flow channel can divide the inner layer flow channel into At least two inner layer sub-channels
  • the baffle in the outer layer channel can divide the outer layer channel into at least two outer layer sub-channels
  • the number of sub-channels in the inner layer is the same as the number of sub-channels in the outer layer.
  • the baffle may include an upper baffle, a lower baffle, and a middle baffle connected between the upper baffle and the lower baffle; in the width direction of the partition, adjacent Among the two diversion ports, the upper baffle may be provided upstream of one of the diverter ports, the lower baffle may be provided downstream of the other diverter port, and the two adjacent diverter ports A middle baffle may be provided between them, and for the same diversion port, in the length direction of the flow channel, an upper baffle may be provided on one side of the diversion port, and a lower baffle may be provided on the other side of the diversion port. plate.
  • the heat dissipating assembly may further include a plurality of basic tooth pieces arranged in the inner layer sub-channel, the length direction of the basic tooth pieces may be the same as the length direction of the flow channel, and the plurality of The basic tooth pieces can be arranged at intervals along the width direction of the flow channel; the end of the basic tooth piece close to the commutation port can be arranged on a slope, and in the thickness direction of the flow channel, the basic tooth piece The side close to the separator can be set away from the commutation port.
  • one side of the basic tooth piece may be connected to one inner wall of the inner layer sub-channel, and the other side of the basic tooth piece may be connected to the The other inner wall of the inner sub-channel is connected, and a medium flow channel is formed between two adjacent basic tooth pieces
  • a plurality of commutation teeth can be provided at the position of the inner layer sub-channel facing the commutation port, and the length direction of the commutation teeth can be aligned with the length direction of the flow channel.
  • a plurality of the commutation teeth can be arranged at intervals; the sides of the commutation teeth close to the partition plate can be arranged on an inclined plane, and on the side of the flow channel In the thickness direction, the side of the commutation tooth piece away from the partition plate may be disposed away from the baffle plate.
  • the number of the flow change ports may be one, and in the width direction of the flow channel, the number of the flow change ports may be multiple; Both sides of the plate can be respectively provided with a said baffle plate, said inner layer sub flow channel can be two, one can be inner layer upstream flow channel, the other can be inner layer downstream flow channel, said outer layer sub flow channel The number of flow channels may be two, one may be an outer layer upstream flow channel, and the other may be an outer layer downstream flow channel.
  • the number of commutation ports can be three, one of which can be an inner and outer commutation port, and the other two can be outer and inner commutation ports, and the inner and outer commutation ports can be located between the two outer and inner commutation ports.
  • the inner layer upstream flow channel can communicate with the outer layer upstream flow channel through the inner and outer flow ports
  • the outer layer upstream flow channel can communicate with the inner layer through the outer and inner flow ports Downstream channel communication.
  • the slope of the commutation gear at the inner and outer commutation ports can be arranged face to face with the slope of the basic tooth in the inner upstream flow channel, and the slopes of the internal and external commutation ports A V-shaped channel facing the inner and outer commutation ports may be formed between the slope of the commutation gear and the slope of the basic gear in the inner upstream channel.
  • the slope of the commutation tooth at the outer and inner commutation port can be arranged face to face with the slope of the basic tooth in the inner layer downstream channel, and the slope of the outer and internal commutation port A V-shaped channel facing the outer and inner commutation ports may be formed between the slope of the commutation gear and the slope of the basic gear in the inner downstream channel.
  • the center of the flow change port may be located at one-half to two-thirds of the partition.
  • the present application provides a fiber laser.
  • the fiber laser may include a heat dissipation component and the above heat dissipation assembly.
  • the flow channel may be connected to the heat dissipation component, and the outer flow channel may be located at the inner layer of the flow channel The side away from the part to be dissipated.
  • the heat-dissipated part may form a side wall of the flow channel.
  • the flow channel may include a plurality of folded-line pipes sequentially arranged along the width direction of the heat-dissipated part, a part of the same folded-line pipe may be arranged close to the heat-dissipated part, and another part of the folded-line pipe may be disposed close to the heat-dissipated part. A part may be disposed away from the heat-dissipated member.
  • FIG. 1 is a schematic structural diagram of a heat dissipation assembly according to an embodiment of the present application
  • FIG. 2 is an exploded view of the heat dissipation assembly shown in FIG. 1;
  • Fig. 3 is a structural schematic diagram of a partition in the heat dissipation assembly shown in Fig. 1;
  • Fig. 4 is a structural schematic diagram of the basic tooth piece and the commutation tooth piece in the heat dissipation assembly shown in Fig. 1;
  • FIG. 5 is a schematic diagram of the flow path of the fluid in the inner layer flow channel in the heat dissipation assembly shown in 1;
  • FIG. 6 is a schematic diagram of the flow path of the fluid in the outer channel in the heat dissipation assembly shown in FIG. 1 .
  • Icon 10-baffle; 20-inner flow channel; 30-outer flow channel; 40-inner baffle; 50-outer baffle; 80-basic tooth piece; 90-converter tooth piece; 100-radiated parts; 21-upstream flow channel of inner layer; 22-downstream flow channel of inner layer; 31-upstream flow channel of outer layer; 32-downstream flow channel of outer layer 41-inner upper baffle; 42-inner lower baffle; 43-inner middle baffle;
  • connection should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it may be mechanically connected or electrically connected; it may be directly connected or indirectly connected through an intermediary, and it may be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in this application in specific situations.
  • the heat sink provided in the embodiment of the present application can be used, but not limited, to dissipate heat from fiber optic disks, and can also be used to dissipate heat from power supplies and other components that require heat dissipation; it can be used, but not limited to, fiber lasers, and can also Used for other equipment.
  • the length direction of the flow channel is also the conveying direction of the medium, that is, in the length direction of the flow channel, one end of the flow channel is the medium inlet end, and the other end of the flow channel is the medium outflow end. That is, from the medium inlet end to the medium outflow end.
  • the present application provides a heat dissipation assembly, which may include a flow channel, and the flow channel may include an inner layer flow channel 20 and an outer layer flow channel 30 arranged side by side; in the length direction of the flow channel
  • the inner layer channel 20 may include at least two inner layer sub-channels arranged at intervals (at least two inner layer sub-channels are independent of each other and cannot be directly communicated with each other)
  • the outer layer channel 30 may include at least two Outer layer sub-channels arranged at intervals (at least two outer layer sub-channels are independent of each other and cannot be directly connected to each other); in the length direction of the flow channel, the adjacently arranged inner layer sub-channels and the outer layer
  • the sub-channels can be connected to each other, and the interconnected inner layer sub-channels and outer layer sub-channels can be located in different positions, specifically, one end of the flow channel can be the medium inlet end, and the other end of the flow channel can be the medium outflow end , along the medium convey
  • an inner layer sub-channel located at the most upstream that is, at the medium inlet end
  • other inner layer sub-channels are sorted in sequence, and can be defined as being located at the most upstream
  • one outer layer sub-channel located at the medium inlet end is the first outer layer sub-channel
  • the other outer layer sub-channels are arranged sequentially; in the medium conveying direction, the first outer layer sub-channel and the second inner layer sub-channel
  • the channels can be adjacent and communicated, and the second inner layer sub-channel can be located downstream of the first outer layer sub-channel, the first inner layer sub-channel can be adjacent to and communicate with the second outer layer sub-channel, and the second The second outer sub-channel may be located downstream of the first inner sub-channel, and so on.
  • the heat dissipation assembly provided in this embodiment can be connected to the heat sink 100, the inner flow channel 20 can be attached to the plate surface of the heat sink 100, and the outer flow channel 30 can be set The side of the inner layer flow channel 20 away from the heat sink 100; at least one end of the flow channel can be provided with a fluid power source, and the fluid power source makes the cooling medium enter the inner layer flow channel 20 and the outer layer respectively from the medium inlet end of the flow channel. In the laminar flow channel 30.
  • the medium can first enter the first inner layer sub-channel and the first outer layer sub-channel, and then the medium can flow from the first inner layer sub-channel into the downstream second outer layer sub-channel, similarly , the medium can enter the downstream second inner outer flow channel from the first outer layer sub-channel, and so on until the medium flows out from the medium outflow end, during this process, the medium in the inner layer flow channel 20 can be connected with the outer layer
  • the medium in the flow channel 30 is exchanged; the medium in the inner flow channel 20 close to the heat sink 100 has a large heat transfer amount, and the temperature difference with the heat sink 100 is small, and the medium in the outer flow channel 30 far away from the heat sink 100 Compared with the medium in the inner layer flow channel 20, the heat exchange rate of the medium is smaller, and the temperature difference with the heat sink 100 is larger.
  • the medium in the inner layer flow channel 20 can exchange with the medium in the outer layer flow channel 30, and the outer layer flow After the medium in the channel 30 enters the inner layer channel 20, it can realize a large amount of heat exchange with the downstream heat sink 100, so that the heat dissipation of the heat sink 100 is large, and the temperature drop is large, so that the heat sink 100 can be close to the medium.
  • the portion at the outflow end has large heat transfer, large heat dissipation, large cooling, and low temperature, thereby reducing the temperature difference between the two ends of the heat sink 100, which is beneficial to improving the heat dissipation uniformity and temperature uniformity of the heat sink 100.
  • the heat-dissipated part is an optical fiber disc
  • it can naturally make the part of the optical fiber disc close to the medium outflow end have a large heat transfer, large heat dissipation, more cooling, and low temperature, which can be reduced, and then the temperature difference between the two ends of the optical fiber disc can be reduced. , which is conducive to improving the heat dissipation uniformity and temperature uniformity of the optical fiber disk.
  • the fluid power source can be selected according to the properties of the fluid, for example: when the fluid is gas, the fluid power source can be a fan, a blower can be set at the medium inlet end, or an exhaust fan can be set at the medium outflow end, or both can be installed in the medium A blower is set at the inlet end and an exhaust fan is set at the medium outflow end; when the fluid is liquid, a pump and other power parts can be set.
  • the number of sub-channels in the inner layer can be set to be the same as the number of sub-channels in the outer layer, which facilitates processing, facilitates the replacement of channels for the medium, and is more conducive to the uniformity of heat dissipation of the heat sink 100 .
  • the number of sub-channels in the inner layer can be three, four or five, etc., and correspondingly, the number of sub-channels in the outer layer can be three, four, or five, etc. .
  • the first outer layer sub-channel may be adjacent to and communicated with the second inner layer sub-channel, and the second inner layer sub-channel may be located downstream of the first outer layer sub-channel;
  • the layer sub-channel can be adjacent to and communicated with the second outer layer sub-channel, and the second outer layer sub-channel can be located downstream of the first inner layer sub-channel;
  • the second outer layer sub-channel can be connected to the third inner layer sub-channel.
  • the layer sub-channels are adjacent and connected, and the third inner layer sub-channel may be located downstream of the second outer layer sub-channel; the second inner layer sub-channel and the third outer layer sub-channel may be adjacent and communicated, And the third outer layer sub-channel can be located downstream of the second inner layer sub-channel, and so on, at this time, the two flow paths of the medium can both be wave-shaped.
  • the number of sub-channels in the inner layer can be two, and the number of sub-channels in the outer layer can be two.
  • the first outer layer sub-channel can be connected to the second inner layer sub-channel. Adjacent and communicated, and the second inner layer sub-channel can be located downstream of the first outer layer sub-channel; the first inner layer sub-channel can be adjacent to and communicated with the second outer layer sub-channel, and the second outer layer sub-channel can The layer sub-channel may be located downstream of the first inner layer sub-channel.
  • the upstream part of the heat sink 100 (the part near the medium inlet end) may correspond to the first inner layer sub-channel, and the heat sink 100
  • the downstream part (the part close to the medium outflow end) can correspond to the second inner layer sub-channel; the medium in the first inner layer sub-channel can be transferred to the second outer layer sub-channel and then directly flow to the medium outflow end, the first The medium in the outer layer sub-channel can be transferred to the second inner layer sub-channel and then directly flow to the medium outflow end.
  • This structure makes the structure of the channel simple, and on the other hand, the medium in the first outer layer sub-channel
  • the amount of heat exchange is small, and there is still a large temperature difference with the downstream part of the radiated part 100, which can exchange heat with the downstream part of the radiated part 100 to a large extent, and can further make the downstream part of the radiated part 100 dissipate more heat. , the temperature is lowered more, and the heat dissipation uniformity and temperature uniformity of the heat sink 100 are further improved.
  • the structural forms of the inner layer flow channel 20 and the outer layer flow channel 30 can be various, for example: the flow channel can include a plurality of zigzag pipes arranged in sequence along the width direction of the heat sink 100, a part of the same zigzag pipe It can be arranged close to the heat dissipation part 100, and this part forms the inner layer flow channel 20.
  • the other part of the folded line pipe can be arranged away from the heat dissipation part 100, and this part forms the outer layer flow channel 30.
  • the specific number of the outer flow channels 30 is used to set the number of corners of the zigzag pipeline.
  • a partition 10 can be provided in the flow channel, and the partition 10 can separate the flow channel to form an inner layer flow channel 20 and an outer layer flow channel 30;
  • the two sides can be respectively connected with baffles, and the side of the baffle away from the partition 10 can all abut against the inner wall of the flow channel, and the baffle in the inner layer flow channel 20 can divide the inner layer flow channel 20 into at least two The inner layer sub-channel, the baffle plate in the outer layer channel 30 can divide the outer layer channel 30 into at least two outer layer sub-channels;
  • the flow channel and the sub-channel of the outer layer can be communicated through the commutation port.
  • baffles can be set on both sides of the partition 10, that is, an inner baffle 40 can be set in the inner flow channel 20, and an outer baffle 50 can be set in the outer flow channel 30; In the thickness direction of the inner layer baffle 40, one side of the inner layer baffle 40 can be connected with the partition 10, and the other side of the inner layer baffle 40 can be in contact with the inner wall of the inner layer flow channel 20.
  • the inner Both sides of the layer baffle plate 40 can abut against the corresponding inner wall of the inner layer flow channel 20 respectively; similarly, in the thickness direction of the flow channel, one side of the outer layer baffle plate 50 can be connected with the partition plate 10, and the outer layer The other side of the baffle 50 may be in contact with the inner wall of the outer channel 30 , and in the width direction of the channel, both sides of the outer baffle 50 may be in contact with corresponding outer walls of the outer channel 30 .
  • the inner layer baffle plate 40 can divide the inner layer flow channel 20 into at least two inner layer sub-channels (for example: when two inner layer baffle plates 40 can be arranged at intervals along the length direction of the flow channel, There can be three inner layer sub-flow channels, correspondingly, two outer layer baffles 50 can be arranged at intervals on the dividing plate 10, and there can be three outer layer sub-flow channels; in the same way, the inner layer baffles 40 and the outer layer When there can be three baffle plates 50, there can be four sub-channels in the inner layer and four sub-channels in the outer layer).
  • the flow channel structure of this structure is further simple; on the other hand, in the width direction of the flow channel, the inner sub-flow channel on one side of the partition 10 can be continuous, and the outer layer sub-flow on the other side of the partition 10
  • the channel can also be continuous, then in the width direction of the radiated part 100, the inner layer sub-channel and the radiated part 100 can be continuously abutted, so that the heat exchange between the inner layer sub-channel and the radiated part 100 can be improved.
  • Uniform similarly, the heat exchange between the outer layer flow channel 30 and the inner layer flow channel 20 is uniform.
  • the width of the inner layer sub-channel is not smaller than the width of the heat sink 100
  • the width of the outer layer sub-channel is the same as that of the inner layer sub-channel.
  • the baffle may include an upper baffle, a lower baffle, and a middle baffle connected between the upper baffle and the lower baffle;
  • An upper baffle can be provided upstream of the flow opening, a lower baffle can be provided downstream of the other flow opening, and a middle baffle can be provided between two adjacent flow openings, and for the same flow opening, the In the length direction of the flow channel, an upper baffle may be provided on one side of the flow change port, and a lower baffle may be provided on the other side of the flow change port.
  • the baffle can be arranged at the edge of the commutation port.
  • the inner baffle 40 can include an upper inner baffle 41 , an inner lower baffle 42 and an inner middle baffle 43 , and one end of the inner middle baffle 43 can be connected to the inner upper baffle 41 , the other end of the baffle plate 43 in the inner layer can be connected with the lower baffle plate 42 of the inner layer;
  • One end of the middle baffle 53 can be connected with the upper baffle 51 of the outer layer, and the other end of the middle baffle 53 of the outer layer can be connected with the lower baffle 52 of the outer layer;
  • an upper inner layer baffle 41 can be provided on the upper edge of the first flow change port (along the medium conveying direction, the upstream direction is upward), and the lower edge of the second flow change port can be
  • the inner lower baffle 42 is set, and the inner middle baffle 43 can be arranged between the two commutation ports.
  • the lower edge of the first commutation port can be provided with an outer lower baffle Plate 52
  • the upper edge of the second commutation port can be provided with an outer upper baffle 51
  • an outer middle baffle 53 can be arranged between the two commutation ports
  • the middle baffles of the baffles can be placed between two adjacent
  • the diverter ports are isolated in the width direction of the flow channel, that is, the inner baffle 40 may include at least one Z-shaped plate segment, and the outer baffle 50 may include at least one Z-shaped plate segment.
  • the upper baffle located on the upper edge of the commutation port can prevent the medium from passing through the corresponding commutation port, and the lower baffle located on the lower edge of the commutation port can promote the medium to pass through the corresponding commutation port; thus, the medium in the inner sub-channel can Change the way to flow into the corresponding outer sub-channel through the second commutation port; the medium in the outer sub-channel can flow into the corresponding inner sub-channel through the first commutation port; that is, two adjacent commutation channels
  • One of the mouths can be the internal and external commutation port 60 for the medium used in the inner layer sub-channel to transfer to the outer layer sub-channel, and the other can be the outer port 60 for the medium used in the outer layer sub-channel to transfer to the inner layer sub-channel.
  • the inner commutation port 70 realizes the mutual exchange of the medium of the inner layer flow channel 20 and the medium of the outer layer flow channel 30 .
  • the flange of the diverter port can be used as the upper baffle or the lower baffle on one side of the partition 10, and the baffle on the other side of the partition 10 can be fixed on the partition by welding, threaded connection or adhesive bonding. Plate 10 or the inner wall of the flow channel.
  • the number of baffles on one side of the separator 10 can be equal to the number of flow change ports in the length direction of the flow channel, for example: in the length direction of the flow channel, when the number of flow change ports can be two, the inner layer block
  • the number of plates 40 can be two, then the number of inner layer sub-runners can be three, the number of outer layer baffles 50 can be two, the number of outer layer sub-runners can be three, etc., and so on .
  • the number of sub-channels in the inner layer can be two, and the number of sub-channels in the outer layer can be two, that is, the number of inner baffles 40 and the number of outer baffles 50 can be both
  • the number of commutation ports can be one (at the same position in the width direction of the flow channel, that is, in the length direction of the flow channel, one commutation port has no positive
  • a baffle plate can be provided on both sides of the partition plate 10
  • there can be two inner layer sub-flow channels one can be the inner layer upstream flow channel 21, and the other can be the inner layer
  • the number of the outer layer sub-channels may be two, one may be the outer layer upstream flow channel 31 , and the other may be the outer layer downstream flow channel 32 .
  • the quantity of the flow change port can be two, that is, one inner and outer flow change port 60 and one outer and inner flow change port 70 are set; or the number of flow change ports can be four, one
  • the inner and outer commutation ports 60 and one outer and inner commutation port 70 may be arranged alternately with each other.
  • the number of commutation ports can be three, one of which can be the inner and outer commutation ports 60, and the other two can be the outer and inner commutation ports 70, and the inner and outer commutation ports 60 can be located in the two outer and inner commutation ports.
  • the inner upstream channel 21 can communicate with the outer upstream channel 31 through the inner and outer commutation ports 60
  • the outer upstream channel 31 can communicate with the inner downstream channel 22 through the outer and inner commutation ports 70 connected.
  • the medium in the upstream channel 21 of the inner layer can gather toward the internal and external commutation ports 60 located in the middle, and enter the downstream channel 32 of the outer layer through the internal and external commutation ports 60, and the medium enters the downstream channel 32 of the outer layer and then Diffuse in all directions of the downstream flow channel 32 of the outer layer, and the medium is transported to the medium outflow end as a whole;
  • the medium of the upstream flow channel 31 of the outer layer can be divided into two paths at the inner-to-outer flow port, and the medium of one line can pass through an outer-inner flow port 70 intervenes in the downstream channel 22 of the inner layer, and the other channel of medium can enter the downstream channel 22 of the inner layer through another outer-inner commutation port 70, and the two channels of media can merge into the downstream channel 22 of the inner layer, and together with the heat sink 100 Heat exchange in the downstream part, this structure can make the lower temperature medium in the outer layer upstream flow channel 31 quickly enter the inner layer downstream flow channel 22, speed up the heat
  • the position of the diversion port on the partition plate 10 can be set as required, for example: the center of the diversion port can be located at one-half to two-thirds of the partition plate 10 (for example: one-half, twelve Seven-thirds or two-thirds, etc.), after the assembly is completed, the distance between the commutation port and the medium inlet end of the partition plate 10 can be one-half to two-thirds of the length of the partition plate 10.
  • the medium in the upstream channel 31 of the outer layer will also exchange heat during transportation, and the temperature will increase. The above structure can ensure the heat dissipation effect of the heat sink 100 .
  • the heat dissipation assembly may also include a plurality of basic tooth pieces 80 arranged in the inner sub-flow channel, and the length direction of the basic tooth pieces 80 may be consistent with the The length direction of the flow channel is the same, and a plurality of basic tooth pieces 80 can be arranged at intervals along the width direction of the flow channel; the end of the basic tooth piece 80 close to the commutation port can be arranged on a slope, and in the thickness direction of the flow channel, the basic tooth A side of the sheet 80 close to the separator 10 may be disposed away from the commutation port.
  • a basic tooth piece 80 can be provided in the inner layer flow channel 20, and in the thickness direction of the flow channel, one side of the basic tooth piece 80 can be connected with the inner wall of one side of the inner layer sub-flow channel, and the basic tooth piece The other side of 80 can be connected with the inner wall of the other side of the inner layer sub-channel, and a medium flow channel can be formed between two adjacent basic tooth pieces 80; multiple basic tooth pieces 80 can improve the strength of the inner layer sub-channel , It can also increase the heat exchange area of the medium, thereby improving the heat exchange efficiency, and can also disturb the flow direction of the medium, making the medium turbulent, improving the heat exchange effect, thereby improving the heat dissipation effect of the heat sink.
  • a slope can be set at the end of the basic tooth piece 80 near the commutation port, so that a plurality of basic tooth plates 80 can form gaps at the commutation port, so that multiple medium circulation channels can communicate with each other, so that the medium can be collected or flowed around. diffusion.
  • a plurality of commutation teeth 90 may be provided at the position of the inner layer sub-channel facing the commutation port, and the commutation teeth
  • the length direction of 90 can be the same as the length direction of the flow channel, along the width direction of the flow channel, a plurality of commutation teeth 90 can be arranged at intervals; the side of the commutation teeth 90 close to the separator 10 can be arranged on a slope, and In the thickness direction of the flow channel, the side of the commutation tooth piece 90 away from the partition plate 10 can be set away from the baffle plate (specifically, along the medium conveying direction: in the inner layer flow channel, the lower edges of the inner and outer commutation ports can be set Inner layer lower baffle plate, inner layer upper baffle plate can be set on the upper edge of outer and inner commutation port; The outer lower baffle can be set).
  • the commutation gear 90 can improve the strength of the inner channel 20 at the commutation port and improve the heat exchange effect at the commutation port.
  • the notch on one side of the commutation tooth 90 can realize the collection or diffusion of the medium.
  • the slope of the commutation gear 90 at the inner and outer commutation ports 60 can be arranged face to face with the slope of the basic gear 80 in the inner upstream channel 21 , forming a V-shaped channel between the two.
  • the opening of the V-shaped channel can face the inner and outer commutation ports 60; as shown in FIG.
  • the inclined surfaces are arranged facing each other, and a V-shaped channel can be formed between them, and the opening of the V-shaped channel can face the outer-inner commutation port 70 .
  • the embodiment of the present application also provides a fiber laser.
  • the fiber laser can include a heat sink 100 and a heat dissipation assembly of any of the above-mentioned technical solutions.
  • the flow channel can be connected to the heat sink 100, and the outer flow channel 30 can be located at The side of the inner flow channel 20 away from the heat sink 100 .
  • the fiber laser in this embodiment may include the heat dissipation component of any of the above technical solutions, and thus has all the beneficial technical effects of the heat dissipation component, which will not be repeated here.
  • the flow channel may independently include a plurality of side plates connected end to end in sequence, and the flow channel may be installed on the heat sink 100 as an independent component.
  • the heat-dissipated part 100 can form a side wall of the flow channel, that is, one side plate of the flow channel can be the heat-dissipated part 100, and the medium in the inner layer flow channel 20 can directly contact the heat-dissipated part The 100 contact can improve the heat exchange efficiency and heat exchange effect, thereby improving the heat dissipation efficiency and heat dissipation effect of the radiated part 100 .
  • the heat-dissipated part 100 may be a fiber optic disk, the flow channel may be connected to the fiber optic disk, and the fiber optic disk may directly serve as a side wall of the flow channel.
  • the present application relates to the technical field of fiber laser heat dissipation, in particular to a heat dissipation component and a fiber laser.
  • the heat dissipation assembly includes: a flow channel, the flow channel includes an inner layer flow channel and an outer layer flow channel arranged side by side; in the length direction of the flow channel, the inner layer flow channel includes at least two inner layer sub-channels arranged at intervals , the outer layer flow channel includes at least two outer layer sub-channels arranged at intervals; in the length direction of the flow channel, the adjacent inner layer sub-channels and outer layer sub-channels communicate with each other, and the interconnected inner layer Sub-runners and outer sub-runners are in different positions.
  • the heat dissipation assembly provided by the present invention can make the part of the heat-dissipated part close to the medium outflow end have a large heat transfer amount, a large heat dissipation, a large temperature drop, and a low temperature, thereby reducing the temperature difference between the two ends of the heat-dissipated part, which is conducive to improving Heat dissipation uniformity and temperature uniformity of the heat sink.
  • the heat dissipation assembly and fiber laser of the present application are reproducible and can be applied in various industrial applications.
  • the heat dissipation assembly and the fiber laser of the present application can be used in any field requiring heat dissipation.

Landscapes

  • Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Engineering & Computer Science (AREA)
  • Plasma & Fusion (AREA)
  • Optics & Photonics (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)

Abstract

The present application relates to the technical field of heat dissipation of fiber lasers, in particular to a heat dissipation assembly and a fiber laser. The heat dissipation assembly comprises: a flow channel, wherein the flow channel comprises an inner flow channel and an outer flow channel, which are arranged in parallel; in the lengthwise direction of the flow channel, the inner flow channel comprises at least two inner sub-flow channels, which are arranged at an interval, and the outer flow channel comprises at least two outer sub-flow channels, which are arranged at an interval; and in the lengthwise direction of the flow channel, the inner sub-flow channel and the outer sub-flow channel, which are adjacently arranged, communicate with each other, and the inner sub-flow channel and the outer sub-flow channel, which communicate with each other, are located at different positions. By means of the heat dissipation assembly provided by the present application, the part of a component subjected to heat dissipation that is close to a medium outflow end has a large heat exchange amount and a large heat dissipation amount, and the temperature of the part is greatly reduced so that same has a low temperature; therefore, the temperature difference between two ends of the component subjected to heat dissipation can be reduced, which is beneficial to improving the heat dissipation uniformity and the temperature uniformity of the component subjected to heat dissipation.

Description

散热组件及光纤激光器Cooling components and fiber lasers
相关申请的交叉引用Cross References to Related Applications
本申请要求于2021年09月27日提交中国专利局的申请号为2021111387427、名称为“散热组件及光纤激光器”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims the priority of the Chinese patent application with application number 2021111387427 and titled "Heat Dissipation Component and Fiber Laser" filed with the China Patent Office on September 27, 2021, the entire contents of which are incorporated herein by reference.
技术领域technical field
本申请涉及散热技术领域,尤其是涉及散热组件及光纤激光器。The present application relates to the technical field of heat dissipation, in particular to heat dissipation components and fiber lasers.
背景技术Background technique
光纤激光器是指用掺稀土元素玻璃光纤作为增益介质的激光器,光纤激光器应用范围非常广泛,例如:激光光纤通讯、激光空间远距通讯、工业造船、汽车制造、激光雕刻、激光打标、激光切割以及金属或非金属钻孔、切割或者焊接等等。Fiber laser refers to a laser that uses rare earth-doped glass fiber as a gain medium. Fiber laser has a wide range of applications, such as: laser fiber communication, laser space long-distance communication, industrial shipbuilding, automobile manufacturing, laser engraving, laser marking, laser cutting And metal or non-metal drilling, cutting or welding, etc.
一种散热组件包括散热风道和设置在散热风道内的散热齿,在散热风道的一端设置风机,使气体由散热风道的进风端流至散热风道的出风端,气体在流动过程中与光纤盘进行换热,从而对光纤盘散热。存在的问题是,气体进入进风端后开始与光纤盘进行换热,随着气体的运动,气体的温度也随之升高,则气体与光纤盘之间的温差减小,两者的换热量减小;因此,光纤盘的靠近出风端的部分的换热量小,散热少,温度较高。A heat dissipation assembly includes a heat dissipation air duct and heat dissipation teeth arranged in the heat dissipation air duct, and a fan is arranged at one end of the heat dissipation air duct, so that the gas flows from the air inlet end of the heat dissipation air duct to the air outlet end of the heat dissipation air duct, and the gas is flowing During the process, heat is exchanged with the optical fiber disk to dissipate heat from the optical fiber disk. The problem is that after the gas enters the air inlet end, it starts to exchange heat with the fiber optic disk. With the movement of the gas, the temperature of the gas also increases, and the temperature difference between the gas and the fiber optic disk decreases. The heat is reduced; therefore, the part of the optical fiber disk close to the air outlet has a small heat transfer, less heat dissipation, and a higher temperature.
发明内容Contents of the invention
本申请提供了散热组件及光纤激光器,以在一定程度上解决现有技术中存在的光纤盘部的靠近出风端的部分的换热量小,散热少,温度较高的技术问题。The present application provides a heat dissipation assembly and a fiber laser to solve the technical problems of low heat transfer, less heat dissipation and high temperature existing in the prior art at the part of the fiber optic disc near the air outlet.
本申请提供了一种散热组件,该散热组件可以包括:流道,所述流道可以包括并列设置的内层流道和外层流道;在所述流道的长度方向上,所述内层流道可以包括至少两个间隔设置的内层子流道,所述外层流道可以包括至少两个间隔设置的外层子流道;在所述流道的长度方向上,相邻设置的所述内层子流道和所述外层子流道可以相互连通,且相互连通的所述内层子流道和所述外层子流道可以位于不同位置。The present application provides a heat dissipation assembly, which may include: a flow channel, the flow channel may include an inner layer flow channel and an outer layer flow channel arranged side by side; in the length direction of the flow channel, the inner layer flow channel The layer flow channel may include at least two inner layer sub-channels arranged at intervals, and the outer layer flow channel may include at least two outer layer sub-channels arranged at intervals; in the length direction of the flow channel, adjacently arranged The inner layer sub-channels and the outer layer sub-channels may communicate with each other, and the interconnected inner layer sub-channels and the outer layer sub-channels may be located at different positions.
在使用本申请提供的散热组件时,将本申请提供的散热组件与被散热件连接,内层流道可以贴在被散热件的板面,外层流道可以设置在内层流道的远离被散热件的一侧;在流道的至少一端可以设置流体动力源,流体动力源使得冷却介质由流道的介质进入端分别进入内层流道和外层流道内。在介质输送方向上,介质首先可以进入第一内层子流道和第一外层子流道,然后介质可以由第一内层子流道流入下游的第二外层子流道,同理,介质可以由第一外层子流道进入下游的第二内层外流道,以此类推,直至介质由介质流出端流出,在此过程中,内层流道内的介质可以与外层流道的介质进行交换;靠近被散热件的内层流 道内的介质换热量大,与被散热件的温差较小,远离被散热件的外层流道内的介质相较于内层流道内的介质换热量小,与被散热件的温差较大,内层流道的介质可以与外层流道的介质进行交换,则外层流道的介质进入内层流道后,又可以与下游的被散热件实现大换热量,使得被散热件的散热量大、降温大,从而可以使被散热件的靠近介质流出端的部分的换热量大,散热量大,降温多,温度低,进而可以减小被散热件两端的温差,有利于改善被散热件的散热均匀性和温度均匀性。当被散热件为光纤盘时,自然可以使光纤盘的靠近介质流出端的部分的换热量大,散热量大,降温多,温度低,进而可以减小,进而可以减小光纤盘两端的温差,有利于改善光纤盘的散热均匀性和温度均匀性。When using the heat dissipation assembly provided by this application, connect the heat dissipation assembly provided by this application to the heat sink, the inner flow channel can be attached to the plate surface of the heat sink, and the outer flow channel can be set far away from the inner flow channel. One side of the part to be radiated; at least one end of the flow channel can be provided with a fluid power source, and the fluid power source makes the cooling medium enter the inner layer flow channel and the outer layer flow channel respectively from the medium inlet end of the flow channel. In the medium conveying direction, the medium can first enter the first inner layer sub-channel and the first outer layer sub-channel, and then the medium can flow from the first inner layer sub-channel into the downstream second outer layer sub-channel, similarly , the medium can enter the downstream second inner layer outer channel from the first outer layer sub-channel, and so on until the medium flows out from the medium outflow end, during this process, the medium in the inner layer channel can be connected with the outer layer channel The medium in the inner flow channel close to the radiated part has a large heat transfer rate, and the temperature difference with the radiated part is small, and the medium in the outer flow channel far away from the radiated part is compared with the medium in the inner flow channel The amount of heat exchange is small, and the temperature difference with the heat-dissipated parts is large. The medium in the inner flow channel can exchange with the medium in the outer flow channel. After the medium in the outer flow channel enters the inner flow channel, it can communicate with the downstream flow channel. The radiated part realizes a large amount of heat exchange, so that the heat dissipation of the radiated part is large and the cooling is large, so that the part of the radiated part close to the medium outflow end can have a large heat transfer, a large heat dissipation, a large cooling, and a low temperature. The temperature difference between the two ends of the radiated part can be reduced, which is beneficial to improving the heat dissipation uniformity and temperature uniformity of the radiated part. When the heat-dissipated part is an optical fiber disc, it can naturally make the part of the optical fiber disc close to the medium outflow end have a large heat transfer, large heat dissipation, more cooling, and low temperature, which can be reduced, and then the temperature difference between the two ends of the optical fiber disc can be reduced. , which is conducive to improving the heat dissipation uniformity and temperature uniformity of the optical fiber disk.
可选地,所述流道内可以设有隔板,所述隔板可以将所述流道分隔形成所述内层流道和所述外层流道;所述隔板的两侧可以分别连接有挡板,所述挡板的远离所述隔板的侧部可以均与所述流道的内壁抵接,所述内层流道内的所述挡板可以将所述内层流道分隔成至少两个所述内层子流道,所述外层流道内的所述挡板可以将所述外层流道分隔成至少两个所述外层子流道;所述隔板上可以设有至少两个换流口,所述内层子流道和所述外层子流道可以通过所述换流口连通。Optionally, a baffle may be provided in the flow channel, and the baffle may separate the flow channel to form the inner flow channel and the outer flow channel; the two sides of the baffle may be respectively connected There is a baffle, and the side parts of the baffle away from the partition can all abut against the inner wall of the flow channel, and the baffle in the inner layer flow channel can divide the inner layer flow channel into At least two inner layer sub-channels, the baffle in the outer layer channel can divide the outer layer channel into at least two outer layer sub-channels; There are at least two commutation ports, and the inner layer sub-channel and the outer layer sub-channel can be communicated through the commutation port.
可选地,内层子流道的数量与外层子流道的数量是相同的。Optionally, the number of sub-channels in the inner layer is the same as the number of sub-channels in the outer layer.
可选地,所述挡板可以包括上挡板、下挡板以及连接在所述上挡板和所述下挡板之间的中挡板;在所述隔板的宽度方向上,相邻两个所述换流口中,一个所述换流口的上游可以设有所述上挡板,另一个所述换流口的下游可以设有下挡板,相邻两个所述换流口之间可以设有中挡板,且对于同一个所述换流口,在流道的长度方向上,换流口的一侧可以设置上挡板,换流口的另一侧可以设置下挡板。Optionally, the baffle may include an upper baffle, a lower baffle, and a middle baffle connected between the upper baffle and the lower baffle; in the width direction of the partition, adjacent Among the two diversion ports, the upper baffle may be provided upstream of one of the diverter ports, the lower baffle may be provided downstream of the other diverter port, and the two adjacent diverter ports A middle baffle may be provided between them, and for the same diversion port, in the length direction of the flow channel, an upper baffle may be provided on one side of the diversion port, and a lower baffle may be provided on the other side of the diversion port. plate.
可选地,所述散热组件还可以包括设置在所述内层子流道内的多个基础齿片,所述基础齿片的长度方向可以与所述流道的长度方向相同,多个所述基础齿片可以沿所述流道的宽度方向间隔设置;所述基础齿片的靠近所述换流口的一端可以呈斜面设置,且在所述流道的厚度方向上,所述基础齿片的靠近所述隔板的一侧可以远离所述换流口设置。Optionally, the heat dissipating assembly may further include a plurality of basic tooth pieces arranged in the inner layer sub-channel, the length direction of the basic tooth pieces may be the same as the length direction of the flow channel, and the plurality of The basic tooth pieces can be arranged at intervals along the width direction of the flow channel; the end of the basic tooth piece close to the commutation port can be arranged on a slope, and in the thickness direction of the flow channel, the basic tooth piece The side close to the separator can be set away from the commutation port.
可选地,在所述流道的厚度方向上,所述基础齿片的一侧可以与所述内层子流道的一侧内壁连接,所述基础齿片的另一侧可以与所述内层子流道的另一侧内壁连接,相邻两个基础齿片之间形成介质流通通道Optionally, in the thickness direction of the flow channel, one side of the basic tooth piece may be connected to one inner wall of the inner layer sub-channel, and the other side of the basic tooth piece may be connected to the The other inner wall of the inner sub-channel is connected, and a medium flow channel is formed between two adjacent basic tooth pieces
可选地,所述内层子流道的与所述换流口正对的位置可以设有多个换流齿片,所述换流齿片的长度方向可以与所述流道的长度方向相同,沿所述流道的宽度方向,多个所述换流齿片可以间隔设置;所述换流齿片的靠近所述隔板的侧部可以呈斜面设置,且在所述流道的厚度方向上,所述换流齿片的远离所述隔板的一侧可以远离所述挡板设置。Optionally, a plurality of commutation teeth can be provided at the position of the inner layer sub-channel facing the commutation port, and the length direction of the commutation teeth can be aligned with the length direction of the flow channel. Similarly, along the width direction of the flow channel, a plurality of the commutation teeth can be arranged at intervals; the sides of the commutation teeth close to the partition plate can be arranged on an inclined plane, and on the side of the flow channel In the thickness direction, the side of the commutation tooth piece away from the partition plate may be disposed away from the baffle plate.
可选地,在所述流道的长度方向上,所述换流口的数量可以为一个,在所述流道的宽 度方向上,所述换流口的数量可以为多个;所述隔板的两侧可以各设有一个所述挡板,所述内层子流道可以为两个,一个可以为内层上游流道,另一个可以为内层下游流道,所述外层子流道的数量可以为两个,一个可以为外层上游流道,另一个可以为外层下游流道。Optionally, in the length direction of the flow channel, the number of the flow change ports may be one, and in the width direction of the flow channel, the number of the flow change ports may be multiple; Both sides of the plate can be respectively provided with a said baffle plate, said inner layer sub flow channel can be two, one can be inner layer upstream flow channel, the other can be inner layer downstream flow channel, said outer layer sub flow channel The number of flow channels may be two, one may be an outer layer upstream flow channel, and the other may be an outer layer downstream flow channel.
可选地,换流口的数量可以为三个,其中一个可以为内外换流口,另外两个可以为外内换流口,所述内外换流口可以位于两个所述外内换流口之间;所述内层上游流道可以通过所述内外换流口与所述外层上游流道连通,所述外层上游流道可以通过所述外内换流口与所述内层下游流道连通。Optionally, the number of commutation ports can be three, one of which can be an inner and outer commutation port, and the other two can be outer and inner commutation ports, and the inner and outer commutation ports can be located between the two outer and inner commutation ports. Between the ports; the inner layer upstream flow channel can communicate with the outer layer upstream flow channel through the inner and outer flow ports, and the outer layer upstream flow channel can communicate with the inner layer through the outer and inner flow ports Downstream channel communication.
可选地,所述内外换流口处的所述换流齿片的斜面可以与所述内层上游流道内的所述基础齿片的斜面面对面设置,所述内外换流口处的所述换流齿片的斜面与所述内层上游流道内的所述基础齿片的斜面之间可以形成面向所述内外换流口的V型道。Optionally, the slope of the commutation gear at the inner and outer commutation ports can be arranged face to face with the slope of the basic tooth in the inner upstream flow channel, and the slopes of the internal and external commutation ports A V-shaped channel facing the inner and outer commutation ports may be formed between the slope of the commutation gear and the slope of the basic gear in the inner upstream channel.
可选地,所述外内换流口处的所述换流齿片的斜面可以与所述内层下游流道内的所述基础齿片的斜面面对面设置,所述外内换流口处的所述换流齿片的斜面与所述内层下游流道内的所述基础齿片的斜面之间可以形成面向所述外内换流口的V型道。Optionally, the slope of the commutation tooth at the outer and inner commutation port can be arranged face to face with the slope of the basic tooth in the inner layer downstream channel, and the slope of the outer and internal commutation port A V-shaped channel facing the outer and inner commutation ports may be formed between the slope of the commutation gear and the slope of the basic gear in the inner downstream channel.
可选地,在所述隔板的长度方向上,所述换流口的中心可以位于隔板的二分之一至三分之二处。Optionally, in the length direction of the partition, the center of the flow change port may be located at one-half to two-thirds of the partition.
本申请提供一种光纤激光器,该光纤激光器可以包括被散热件和上述散热组件,所述流道可以与所述被散热件连接,且所述外层流道可以位于所述内层流道的远离所述被散热件的一侧。The present application provides a fiber laser. The fiber laser may include a heat dissipation component and the above heat dissipation assembly. The flow channel may be connected to the heat dissipation component, and the outer flow channel may be located at the inner layer of the flow channel The side away from the part to be dissipated.
可选地,所述被散热件可以形成所述流道的一侧壁。Optionally, the heat-dissipated part may form a side wall of the flow channel.
可选地,所述流道可以包括多个沿所述被散热件的宽度方向依次设置的折线型管道,同一折线型管道的一部分可以靠近所述被散热件设置,所述折线型管道的另一部分可以远离所述被散热件设置。Optionally, the flow channel may include a plurality of folded-line pipes sequentially arranged along the width direction of the heat-dissipated part, a part of the same folded-line pipe may be arranged close to the heat-dissipated part, and another part of the folded-line pipe may be disposed close to the heat-dissipated part. A part may be disposed away from the heat-dissipated member.
应当理解,前述的一般描述和接下来的具体实施方式两者均是为了举例和说明的目的并且未必限制本公开。并入并构成说明书的一部分的附图示出本公开的主题。同时,说明书和附图用来解释本公开的原理。It is to be understood that both the foregoing general description and the following detailed description are for purposes of illustration and description and are not necessarily restrictive of the disclosure. The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate subject matter of the present disclosure. Meanwhile, the specification and drawings serve to explain the principles of the present disclosure.
附图说明Description of drawings
为了更清楚地说明本申请具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本申请的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific embodiments of the present application or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the description of the specific embodiments or prior art. Obviously, the accompanying drawings in the following description The drawings are some implementations of the present application, and those skilled in the art can obtain other drawings based on these drawings without creative work.
图1为本申请实施例的散热组件的结构示意图;FIG. 1 is a schematic structural diagram of a heat dissipation assembly according to an embodiment of the present application;
图2为如图1所示的散热组件的分解图;FIG. 2 is an exploded view of the heat dissipation assembly shown in FIG. 1;
图3为图1所示的散热组件中隔板的结构示意图;Fig. 3 is a structural schematic diagram of a partition in the heat dissipation assembly shown in Fig. 1;
图4为图1所示的散热组件中基础齿片和换流齿片的结构示意图;Fig. 4 is a structural schematic diagram of the basic tooth piece and the commutation tooth piece in the heat dissipation assembly shown in Fig. 1;
图5为1所示的散热组件中内层流道内的流体的流动路径示意图;FIG. 5 is a schematic diagram of the flow path of the fluid in the inner layer flow channel in the heat dissipation assembly shown in 1;
图6为1所示的散热组件中外层流道内的流体的流动路径示意图。FIG. 6 is a schematic diagram of the flow path of the fluid in the outer channel in the heat dissipation assembly shown in FIG. 1 .
图标:10-隔板;20-内层流道;30-外层流道;40-内层挡板;50-外层挡板;60-内外换流口;70-外内换流口;80-基础齿片;90-换流齿片;100-被散热件;21-内层上游流道;22-内层下游流道;31-外层上游流道;32-外层下游流道;41-内层上挡板;42-内层下挡板;43-内层中挡板;51-外层上挡板;52-外层下挡板;53-外层中挡板。Icon: 10-baffle; 20-inner flow channel; 30-outer flow channel; 40-inner baffle; 50-outer baffle; 80-basic tooth piece; 90-converter tooth piece; 100-radiated parts; 21-upstream flow channel of inner layer; 22-downstream flow channel of inner layer; 31-upstream flow channel of outer layer; 32-downstream flow channel of outer layer 41-inner upper baffle; 42-inner lower baffle; 43-inner middle baffle;
具体实施方式Detailed ways
下面将结合附图对本申请的技术方案进行清楚、完整地描述,显然,所描述的实施例是本申请一部分实施例,而不是全部的实施例。The technical solutions of the present application will be clearly and completely described below in conjunction with the accompanying drawings. Apparently, the described embodiments are some of the embodiments of the present application, not all of them.
通常在此处附图中描述和显示出的本申请实施例的组件可以以各种不同的配置来布置和设计。因此,以下对在附图中提供的本申请的实施例的详细描述并非旨在限制要求保护的本申请的范围,而是仅仅表示本申请的选定实施例。The components of the embodiments of the application generally described and shown in the figures herein may be arranged and designed in a variety of different configurations. Accordingly, the following detailed description of the embodiments of the application provided in the accompanying drawings is not intended to limit the scope of the claimed application, but merely represents selected embodiments of the application.
基于本申请中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本申请保护的范围。Based on the embodiments in this application, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of this application.
在本申请的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of this application, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, use a specific orientation construction and operation, therefore should not be construed as limiting the application. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.
在本申请的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本申请中的具体含义。In the description of this application, it should be noted that unless otherwise specified and limited, the terms "installation", "connection", and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it may be mechanically connected or electrically connected; it may be directly connected or indirectly connected through an intermediary, and it may be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in this application in specific situations.
需要说明的是,本申请实施例提供的散热件可以但不局限用于对光纤盘散热,还可以用于对电源等其他需要散热的部件进行散热;可以但不局限用于光纤激光器,还可以用于其他设备装置上。It should be noted that the heat sink provided in the embodiment of the present application can be used, but not limited, to dissipate heat from fiber optic disks, and can also be used to dissipate heat from power supplies and other components that require heat dissipation; it can be used, but not limited to, fiber lasers, and can also Used for other equipment.
需要说明的是,流道的长度方向也为介质的输送方向,也即在流道的长度方向上,流道的一端为介质进入端,流道的另一端为介质流出端,介质的输送方向即为由介质进入端指向介质流出端。It should be noted that the length direction of the flow channel is also the conveying direction of the medium, that is, in the length direction of the flow channel, one end of the flow channel is the medium inlet end, and the other end of the flow channel is the medium outflow end. That is, from the medium inlet end to the medium outflow end.
如图1至图6所示,本申请提供一种散热组件,该散热组件可以包括流道,流道可以包括并列设置的内层流道20和外层流道30;在流道的长度方向上,内层流道20可以包括至少两个间隔设置的内层子流道(至少两个内层子流道相互独立,彼此之间不能够直接连通),外层流道30可以包括至少两个间隔设置的外层子流道(至少两个外层子流道相互独立,彼此之间不能够直接连通);在流道的长度方向上,相邻设置的内层子流道和外层子流道可以相互连通,且相互连通的内层子流道和外层子流道可以位于不同位置,具体地,流道的一端可以为介质进入端,流道的另一端可以为介质流出端,沿介质进入端至介质流出端的介质输送方向上,一个内层子流道可以和与该内层子流道相邻的且位于该内层子流道下游的外层子流道连通,一个外层子流道可以和与该外层子流道相邻的且位于该外层子流道下游的内层子流道连通,流道可以用于与被散热件连接,且外层流道可以位于内层流道的远离被散热件的一侧。As shown in Figures 1 to 6, the present application provides a heat dissipation assembly, which may include a flow channel, and the flow channel may include an inner layer flow channel 20 and an outer layer flow channel 30 arranged side by side; in the length direction of the flow channel Above, the inner layer channel 20 may include at least two inner layer sub-channels arranged at intervals (at least two inner layer sub-channels are independent of each other and cannot be directly communicated with each other), and the outer layer channel 30 may include at least two Outer layer sub-channels arranged at intervals (at least two outer layer sub-channels are independent of each other and cannot be directly connected to each other); in the length direction of the flow channel, the adjacently arranged inner layer sub-channels and the outer layer The sub-channels can be connected to each other, and the interconnected inner layer sub-channels and outer layer sub-channels can be located in different positions, specifically, one end of the flow channel can be the medium inlet end, and the other end of the flow channel can be the medium outflow end , along the medium conveying direction from the medium inlet end to the medium outflow end, one inner layer sub-channel can communicate with the outer layer sub-channel adjacent to the inner layer sub-channel and located downstream of the inner layer sub-channel, one The outer layer sub-channel can communicate with the inner layer sub-channel adjacent to the outer layer sub-channel and located downstream of the outer layer sub-channel, the flow channel can be used to connect with the heat sink, and the outer layer of the sub-channel It can be located on the side of the inner flow channel away from the part to be radiated.
为方便描述,在介质输送方向上,可以定义位于最上游也即位于介质进入端的一个内层子流道为第一内层子流道,其他内层子流道依次排序,可以定义位于最上游也即位于介质进入端的一个外层子流道为第一外层子流道,其他外层子流道依次排序;在介质输送方向上,第一外层子流道与第二内层子流道可以相邻且连通,且第二内层子流道可以位于第一外层子流道的下游,第一内层子流道与第二外层子流道可以相邻且连通,且第二外层子流道可以位于第一内层子流道的下游,以此类推。For the convenience of description, in the medium conveying direction, an inner layer sub-channel located at the most upstream, that is, at the medium inlet end, can be defined as the first inner layer sub-channel, and other inner layer sub-channels are sorted in sequence, and can be defined as being located at the most upstream That is to say, one outer layer sub-channel located at the medium inlet end is the first outer layer sub-channel, and the other outer layer sub-channels are arranged sequentially; in the medium conveying direction, the first outer layer sub-channel and the second inner layer sub-channel The channels can be adjacent and communicated, and the second inner layer sub-channel can be located downstream of the first outer layer sub-channel, the first inner layer sub-channel can be adjacent to and communicate with the second outer layer sub-channel, and the second The second outer sub-channel may be located downstream of the first inner sub-channel, and so on.
在使用本实施例提供的散热组件时,可以将本实施例提供的散热组件与被散热件100连接,内层流道20可以贴在被散热件100的板面,外层流道30可以设置在内层流道20的远离被散热件100的一侧;在流道的至少一端可以设置流体动力源,流体动力源使得冷却介质由流道的介质进入端分别进入内层流道20和外层流道30内。在介质输送方向上,介质首先可以进入第一内层子流道和第一外层子流道,然后介质可以由第一内层子流道流入下游的第二外层子流道,同理,介质可以由第一外层子流道进入下游的第二内层外流道,以此类推,直至介质由介质流出端流出,在此过程中,内层流道20内的介质可以与外层流道30的介质进行交换;靠近被散热件100的内层流道20内的介质换热量大,与被散热件100的温差较小,远离被散热件100的外层流道30内的介质相较于内层流道20内的介质换热量小,与被散热件100的温差较大,内层流道20的介质可以与外层流道30的介质进行交换,则外层流道30的介质进入内层流道20后,又可以与下游的被散热件100实现大换热量,使得被散热件100的散热量大、降温大,从而可以使被散热件100的靠近介质流出端的部分的换热量大,散热量大,降温多,温度低,进而可以减小被散热件100两端的温差,有利于改善被散热件100的散热均匀性和温度均匀性。当被散热件为光纤盘时,自然可以使光纤盘的靠近介质流出端的部分的换热量大,散热量大,降温多,温度低,进而 可以减小,进而可以减小光纤盘两端的温差,有利于改善光纤盘的散热均匀性和温度均匀性。When using the heat dissipation assembly provided in this embodiment, the heat dissipation assembly provided in this embodiment can be connected to the heat sink 100, the inner flow channel 20 can be attached to the plate surface of the heat sink 100, and the outer flow channel 30 can be set The side of the inner layer flow channel 20 away from the heat sink 100; at least one end of the flow channel can be provided with a fluid power source, and the fluid power source makes the cooling medium enter the inner layer flow channel 20 and the outer layer respectively from the medium inlet end of the flow channel. In the laminar flow channel 30. In the medium conveying direction, the medium can first enter the first inner layer sub-channel and the first outer layer sub-channel, and then the medium can flow from the first inner layer sub-channel into the downstream second outer layer sub-channel, similarly , the medium can enter the downstream second inner outer flow channel from the first outer layer sub-channel, and so on until the medium flows out from the medium outflow end, during this process, the medium in the inner layer flow channel 20 can be connected with the outer layer The medium in the flow channel 30 is exchanged; the medium in the inner flow channel 20 close to the heat sink 100 has a large heat transfer amount, and the temperature difference with the heat sink 100 is small, and the medium in the outer flow channel 30 far away from the heat sink 100 Compared with the medium in the inner layer flow channel 20, the heat exchange rate of the medium is smaller, and the temperature difference with the heat sink 100 is larger. The medium in the inner layer flow channel 20 can exchange with the medium in the outer layer flow channel 30, and the outer layer flow After the medium in the channel 30 enters the inner layer channel 20, it can realize a large amount of heat exchange with the downstream heat sink 100, so that the heat dissipation of the heat sink 100 is large, and the temperature drop is large, so that the heat sink 100 can be close to the medium. The portion at the outflow end has large heat transfer, large heat dissipation, large cooling, and low temperature, thereby reducing the temperature difference between the two ends of the heat sink 100, which is beneficial to improving the heat dissipation uniformity and temperature uniformity of the heat sink 100. When the heat-dissipated part is an optical fiber disc, it can naturally make the part of the optical fiber disc close to the medium outflow end have a large heat transfer, large heat dissipation, more cooling, and low temperature, which can be reduced, and then the temperature difference between the two ends of the optical fiber disc can be reduced. , which is conducive to improving the heat dissipation uniformity and temperature uniformity of the optical fiber disk.
其中,流体动力源可以根据流体的属性来选择,例如:流体为气体时,流体动力源可以为风机,可以在介质进入端设置吹风机,或者可以在介质流出端设置抽风机,或者可以既在介质进入端设置吹风机又在介质流出端设置抽风机;流体为液体时,可以设置泵等动力件。Among them, the fluid power source can be selected according to the properties of the fluid, for example: when the fluid is gas, the fluid power source can be a fan, a blower can be set at the medium inlet end, or an exhaust fan can be set at the medium outflow end, or both can be installed in the medium A blower is set at the inlet end and an exhaust fan is set at the medium outflow end; when the fluid is liquid, a pump and other power parts can be set.
可选地,内层子流道的数量可以与外层子流道的数量相同设置,方便加工,有利于介质更换流道,更有利于被散热件100的散热均匀性。Optionally, the number of sub-channels in the inner layer can be set to be the same as the number of sub-channels in the outer layer, which facilitates processing, facilitates the replacement of channels for the medium, and is more conducive to the uniformity of heat dissipation of the heat sink 100 .
在上述实施例基础之上,内层子流道的数量可以为三个、四个或者五个等等,相应的,外层子流道的数量可以为三个、四个或者五个等等。在介质输送方向上,第一外层子流道可以与第二内层子流道相邻且连通,且第二内层子流道可以位于第一外层子流道的下游;第一内层子流道可以与第二外层子流道相邻且连通,且第二外层子流道可以位于第一内层子流道的下游;第二外层子流道可以与第三内层子流道相邻且连通,且第三内层子流道可以位于第二外层子流道的下游;第二内层子流道与第三外层子流道可以相邻且连通,且第三外层子流道可以位于第二内层子流道的下游,依此类推,此时,介质的两条流通路径可以均呈波浪形。On the basis of the above embodiments, the number of sub-channels in the inner layer can be three, four or five, etc., and correspondingly, the number of sub-channels in the outer layer can be three, four, or five, etc. . In the conveying direction of the medium, the first outer layer sub-channel may be adjacent to and communicated with the second inner layer sub-channel, and the second inner layer sub-channel may be located downstream of the first outer layer sub-channel; The layer sub-channel can be adjacent to and communicated with the second outer layer sub-channel, and the second outer layer sub-channel can be located downstream of the first inner layer sub-channel; the second outer layer sub-channel can be connected to the third inner layer sub-channel. The layer sub-channels are adjacent and connected, and the third inner layer sub-channel may be located downstream of the second outer layer sub-channel; the second inner layer sub-channel and the third outer layer sub-channel may be adjacent and communicated, And the third outer layer sub-channel can be located downstream of the second inner layer sub-channel, and so on, at this time, the two flow paths of the medium can both be wave-shaped.
可选的,内层子流道的数量可以为两个,外层子流道的数量可以为两个,在介质输送方向上,第一外层子流道可以与第二内层子流道相邻且连通,且第二内层子流道可以位于第一外层子流道的下游;第一内层子流道可以与第二外层子流道相邻且连通,且第二外层子流道可以位于第一内层子流道的下游,此时,被散热件100的上游部分(靠近介质进入端的部分)可以与第一内层子流道相对应,被散热件100的下游部分(靠近介质流出端的部分)可以与第二内层子流道相对应;第一内层子流道内的介质可以转入第二外层子流道后直接流至介质流出端,第一外层子流道内的介质可以转入第二内层子流道后直接流至介质流出端,这种结构,一方面使得流道的结构简单,另一方面第一外层子流道内的介质换热量少,与被散热件100的下游部分仍存在较大温差,能够较大程度上与被散热件100的下游部分进行换热,能够更进一步的使被散热件100的下游部分散热多,降温多,更进一步改善被散热件100的散热均匀性和温度均匀性。Optionally, the number of sub-channels in the inner layer can be two, and the number of sub-channels in the outer layer can be two. In the medium conveying direction, the first outer layer sub-channel can be connected to the second inner layer sub-channel. Adjacent and communicated, and the second inner layer sub-channel can be located downstream of the first outer layer sub-channel; the first inner layer sub-channel can be adjacent to and communicated with the second outer layer sub-channel, and the second outer layer sub-channel can The layer sub-channel may be located downstream of the first inner layer sub-channel. At this time, the upstream part of the heat sink 100 (the part near the medium inlet end) may correspond to the first inner layer sub-channel, and the heat sink 100 The downstream part (the part close to the medium outflow end) can correspond to the second inner layer sub-channel; the medium in the first inner layer sub-channel can be transferred to the second outer layer sub-channel and then directly flow to the medium outflow end, the first The medium in the outer layer sub-channel can be transferred to the second inner layer sub-channel and then directly flow to the medium outflow end. This structure, on the one hand, makes the structure of the channel simple, and on the other hand, the medium in the first outer layer sub-channel The amount of heat exchange is small, and there is still a large temperature difference with the downstream part of the radiated part 100, which can exchange heat with the downstream part of the radiated part 100 to a large extent, and can further make the downstream part of the radiated part 100 dissipate more heat. , the temperature is lowered more, and the heat dissipation uniformity and temperature uniformity of the heat sink 100 are further improved.
其中,内层流道20和外层流道30的结构形式可以为多种,例如:流道可以包括多个沿被散热件100的宽度方向依次设置的折线型管道,同一折线型管道的一部分可以靠近被散热件100设置,该部分即形成内层流道20,该折线型管道的另一部分可以远离被散热件100设置,该部分即形成外层流道30,根据内层流道20和外层流道30的具体数量来设置折线形管道的拐角数量。Wherein, the structural forms of the inner layer flow channel 20 and the outer layer flow channel 30 can be various, for example: the flow channel can include a plurality of zigzag pipes arranged in sequence along the width direction of the heat sink 100, a part of the same zigzag pipe It can be arranged close to the heat dissipation part 100, and this part forms the inner layer flow channel 20. The other part of the folded line pipe can be arranged away from the heat dissipation part 100, and this part forms the outer layer flow channel 30. According to the inner layer flow channel 20 and The specific number of the outer flow channels 30 is used to set the number of corners of the zigzag pipeline.
作为一种可选方案,如图1至图4所示,流道内可以设有隔板10,隔板10可以将流道分隔形成内层流道20和外层流道30;隔板10的两侧可以分别连接有挡板,挡板的远离隔板10的侧部可以均与流道的内壁抵接,内层流道20内的挡板可以将内层流道20分隔成至少两个内层子流道,外层流道30内的挡板可以将外层流道30分隔成至少两个外层子流道;隔板10上可以设有至少两个换流口,内层子流道和外层子流道可以通过换流口连通。As an alternative, as shown in Figures 1 to 4, a partition 10 can be provided in the flow channel, and the partition 10 can separate the flow channel to form an inner layer flow channel 20 and an outer layer flow channel 30; The two sides can be respectively connected with baffles, and the side of the baffle away from the partition 10 can all abut against the inner wall of the flow channel, and the baffle in the inner layer flow channel 20 can divide the inner layer flow channel 20 into at least two The inner layer sub-channel, the baffle plate in the outer layer channel 30 can divide the outer layer channel 30 into at least two outer layer sub-channels; The flow channel and the sub-channel of the outer layer can be communicated through the commutation port.
本实施例中,隔板10的两侧可以均设置挡板,也即内层流道20内可以设置内层挡板40,外层流道30内可以设置外层挡板50;在流道的厚度方向上,内层挡板40的一侧可以与隔板10连接,内层挡板40的另一侧可以与内层流道20的内壁抵接,在流道的宽度方向上,内层挡板40的两侧可以分别与内层流道20的相应的内壁抵接;同理,在流道的厚度方向上,外层挡板50的一侧可以与隔板10连接,外层挡板50的另一侧可以与外层流道30的内壁抵接,在流道的宽度方向上,外层挡板50的两侧可以分别与外层流道30的相应的外壁抵接。In this embodiment, baffles can be set on both sides of the partition 10, that is, an inner baffle 40 can be set in the inner flow channel 20, and an outer baffle 50 can be set in the outer flow channel 30; In the thickness direction of the inner layer baffle 40, one side of the inner layer baffle 40 can be connected with the partition 10, and the other side of the inner layer baffle 40 can be in contact with the inner wall of the inner layer flow channel 20. In the width direction of the flow channel, the inner Both sides of the layer baffle plate 40 can abut against the corresponding inner wall of the inner layer flow channel 20 respectively; similarly, in the thickness direction of the flow channel, one side of the outer layer baffle plate 50 can be connected with the partition plate 10, and the outer layer The other side of the baffle 50 may be in contact with the inner wall of the outer channel 30 , and in the width direction of the channel, both sides of the outer baffle 50 may be in contact with corresponding outer walls of the outer channel 30 .
内层挡板40可以将内层流道20分隔成至少两个内层子流道(例如:当沿流道的长度方向,隔板10上可以间隔设有两个内层挡板40时,内层子流道可以为三个,相应的,隔板10上可以间隔设有两个外层挡板50,外层子流道可以为三个;同理,内层挡板40和外层挡板50可以均为三个时,内层子流道和外层子流道可以均为四个)。The inner layer baffle plate 40 can divide the inner layer flow channel 20 into at least two inner layer sub-channels (for example: when two inner layer baffle plates 40 can be arranged at intervals along the length direction of the flow channel, There can be three inner layer sub-flow channels, correspondingly, two outer layer baffles 50 can be arranged at intervals on the dividing plate 10, and there can be three outer layer sub-flow channels; in the same way, the inner layer baffles 40 and the outer layer When there can be three baffle plates 50, there can be four sub-channels in the inner layer and four sub-channels in the outer layer).
这种结构流道结构进一步简单;另一方面,在流道的宽度方向上,隔板10的一侧的内层子流道可以为连续的,隔板10的另一侧的外层子流道也可以为连续的,则能够在被散热件100的宽度方向上,内层子流道与被散热件100可以连续抵接,从而可以使内层子流道与被散热件100的换热均匀,同理,外层流道30与内层流道20的换热均匀。可选的,内层子流道的宽度不小于被散热件100的宽度,外层子流道的宽度与内层子流道的宽度相同。The flow channel structure of this structure is further simple; on the other hand, in the width direction of the flow channel, the inner sub-flow channel on one side of the partition 10 can be continuous, and the outer layer sub-flow on the other side of the partition 10 The channel can also be continuous, then in the width direction of the radiated part 100, the inner layer sub-channel and the radiated part 100 can be continuously abutted, so that the heat exchange between the inner layer sub-channel and the radiated part 100 can be improved. Uniform, similarly, the heat exchange between the outer layer flow channel 30 and the inner layer flow channel 20 is uniform. Optionally, the width of the inner layer sub-channel is not smaller than the width of the heat sink 100 , and the width of the outer layer sub-channel is the same as that of the inner layer sub-channel.
具体地,挡板可以包括上挡板、下挡板以及连接在上挡板和下挡板之间的中挡板;在隔板10的宽度方向上,相邻两个换流口中,一个换流口的上游可以设有上挡板,另一个换流口的下游可以设有下挡板,相邻两个换流口之间可以设有中挡板,且对于同一个换流口,在流道的长度方向上,换流口的一侧可以设置上挡板,换流口的另一侧可以设置下挡板。较佳的,挡板可以设置在换流口的边沿处。Specifically, the baffle may include an upper baffle, a lower baffle, and a middle baffle connected between the upper baffle and the lower baffle; An upper baffle can be provided upstream of the flow opening, a lower baffle can be provided downstream of the other flow opening, and a middle baffle can be provided between two adjacent flow openings, and for the same flow opening, the In the length direction of the flow channel, an upper baffle may be provided on one side of the flow change port, and a lower baffle may be provided on the other side of the flow change port. Preferably, the baffle can be arranged at the edge of the commutation port.
也可以理解为,内层挡板40可以包括内层上挡板41、内层下挡板42和内层中挡板43,内层中挡板43的一端可以与内层上挡板41连接,内层中挡板43的另一端可以与内层下挡板42连接;外层挡板50可以包括外层上挡板51、外层下挡板52和外层中挡板53,外层中挡板53的一端可以与外层上挡板51连接,外层中挡板53的另一端可以与外层下挡板52连接;在隔板10的宽度方向上,相邻的两个换流口中,在内层流道20内,第一换流口的上边沿(沿介质输送方向,上游的方向为上)可以设置一个内层上挡板41,第二换流口 的下边沿可以设置内层下挡板42,内层中挡板43可以设置在该两个换流口之间,相应的,在外层流道30内,第一换流口的下边沿可以设置外层下挡板52,第二换流口的上边沿可以设置外层上挡板51,外层中挡板53可以设置在该两个换流口之间,挡板的中挡板可以将相邻两个换流口在流道的宽度方向上隔离开来,也即内层挡板40可以至少包括一个Z字型板段,外层挡板50可以至少包括一个Z字型板段。It can also be understood that the inner baffle 40 can include an upper inner baffle 41 , an inner lower baffle 42 and an inner middle baffle 43 , and one end of the inner middle baffle 43 can be connected to the inner upper baffle 41 , the other end of the baffle plate 43 in the inner layer can be connected with the lower baffle plate 42 of the inner layer; One end of the middle baffle 53 can be connected with the upper baffle 51 of the outer layer, and the other end of the middle baffle 53 of the outer layer can be connected with the lower baffle 52 of the outer layer; In the flow port, in the inner layer flow channel 20, an upper inner layer baffle 41 can be provided on the upper edge of the first flow change port (along the medium conveying direction, the upstream direction is upward), and the lower edge of the second flow change port can be The inner lower baffle 42 is set, and the inner middle baffle 43 can be arranged between the two commutation ports. Correspondingly, in the outer channel 30, the lower edge of the first commutation port can be provided with an outer lower baffle Plate 52, the upper edge of the second commutation port can be provided with an outer upper baffle 51, an outer middle baffle 53 can be arranged between the two commutation ports, and the middle baffles of the baffles can be placed between two adjacent The diverter ports are isolated in the width direction of the flow channel, that is, the inner baffle 40 may include at least one Z-shaped plate segment, and the outer baffle 50 may include at least one Z-shaped plate segment.
位于换流口上边沿的上挡板可以阻止介质通过相应的换流口,位于换流口的下边沿的下挡板可以促使介质通过相应的换流口;从而可以使内层子流道内的介质改变途径通过第二换流口流入相应的外层子流道内;可以使外层子流道内的介质通过第一换流口流入相应的内层子流道;也即,相邻两个换流口中的一个可以为用于内层子流道的介质转入外层子流道的内外换流口60,另一个可以为用于外层子流道的介质转入内层子流道的外内换流口70,这就实现了内层流道20的介质和外层流道30的介质相互交换。The upper baffle located on the upper edge of the commutation port can prevent the medium from passing through the corresponding commutation port, and the lower baffle located on the lower edge of the commutation port can promote the medium to pass through the corresponding commutation port; thus, the medium in the inner sub-channel can Change the way to flow into the corresponding outer sub-channel through the second commutation port; the medium in the outer sub-channel can flow into the corresponding inner sub-channel through the first commutation port; that is, two adjacent commutation channels One of the mouths can be the internal and external commutation port 60 for the medium used in the inner layer sub-channel to transfer to the outer layer sub-channel, and the other can be the outer port 60 for the medium used in the outer layer sub-channel to transfer to the inner layer sub-channel. The inner commutation port 70 realizes the mutual exchange of the medium of the inner layer flow channel 20 and the medium of the outer layer flow channel 30 .
其中,可以采用换流口的翻边作为隔板10的一侧的上挡板或者下挡板,隔板10的另一侧的挡板可以通过焊接、螺纹连接或者黏胶粘接固定在隔板10或者流道的内壁上。Wherein, the flange of the diverter port can be used as the upper baffle or the lower baffle on one side of the partition 10, and the baffle on the other side of the partition 10 can be fixed on the partition by welding, threaded connection or adhesive bonding. Plate 10 or the inner wall of the flow channel.
隔板10一侧的挡板的数量可以与换流口在流道的长度方向上的数量相等,例如:在流道的长度方向上,换流口的数量可以为两个时,内层挡板40的数量可以为两个,则内层子流道的数量可以为三个,外层挡板50的数量可以为两个,外层子流道的数量可以为三个等,以此类推。The number of baffles on one side of the separator 10 can be equal to the number of flow change ports in the length direction of the flow channel, for example: in the length direction of the flow channel, when the number of flow change ports can be two, the inner layer block The number of plates 40 can be two, then the number of inner layer sub-runners can be three, the number of outer layer baffles 50 can be two, the number of outer layer sub-runners can be three, etc., and so on .
作为一种可选方案,内层子流道的数量可以为两个,外层子流道的数量可以为两个,即内层挡板40的数量和外层挡板50的数量可以均为一个,相应的,在流道的长度方向上,换流口的数量可以为一个(在流道的宽度方向上的同一位置,也即在流道的长度方向上,一个换流口无与其正对设置的另一个换流口),隔板10的两侧可以各设有一个挡板,内层子流道可以为两个,一个可以为内层上游流道21,另一个可以为内层下游流道22,外层子流道的数量可以为两个,一个可以为外层上游流道31,另一个可以为外层下游流道32。相应的有益效果在上文中已描述,在此不再赘述。As an alternative, the number of sub-channels in the inner layer can be two, and the number of sub-channels in the outer layer can be two, that is, the number of inner baffles 40 and the number of outer baffles 50 can be both One, correspondingly, in the length direction of the flow channel, the number of commutation ports can be one (at the same position in the width direction of the flow channel, that is, in the length direction of the flow channel, one commutation port has no positive For another flow change port provided), a baffle plate can be provided on both sides of the partition plate 10, and there can be two inner layer sub-flow channels, one can be the inner layer upstream flow channel 21, and the other can be the inner layer For the downstream flow channel 22 , the number of the outer layer sub-channels may be two, one may be the outer layer upstream flow channel 31 , and the other may be the outer layer downstream flow channel 32 . The corresponding beneficial effects have been described above and will not be repeated here.
其中,在流道的宽度方向上,换流口的数量可以为两个,也即设置一个内外换流口60和一个外内换流口70;或者换流口的数量可以为四个,一个内外换流口60和一个外内换流口70可以相互交替设置等。Wherein, in the width direction of the runner, the quantity of the flow change port can be two, that is, one inner and outer flow change port 60 and one outer and inner flow change port 70 are set; or the number of flow change ports can be four, one The inner and outer commutation ports 60 and one outer and inner commutation port 70 may be arranged alternately with each other.
作为一种可选方案,换流口的数量可以为三个,其中一个可以为内外换流口60,另外两个可以为外内换流口70,内外换流口60可以位于两个外内换流口70之间;内层上游流道21可以通过内外换流口60与外层上游流道31连通,外层上游流道31可以通过外内换流口70与内层下游流道22连通。As an optional solution, the number of commutation ports can be three, one of which can be the inner and outer commutation ports 60, and the other two can be the outer and inner commutation ports 70, and the inner and outer commutation ports 60 can be located in the two outer and inner commutation ports. Between the commutation ports 70; the inner upstream channel 21 can communicate with the outer upstream channel 31 through the inner and outer commutation ports 60, and the outer upstream channel 31 can communicate with the inner downstream channel 22 through the outer and inner commutation ports 70 connected.
本实施例中,内层上游流道21的介质可以向位于中部的内外换流口60聚集,且通过 内外换流口60进入外层下游流道32,介质进入外层下游流道32后又向外层下游流道32的各个方向扩散,介质整体向介质流出端输送;外层上游流道31的介质可以在内往外换流口处分成两路,一路介质可以通过一个外内换流口70介入内层下游流道22,另外一路介质可以通过另外一个外内换流口70进入内层下游流道22,两路介质可以在内层下游流道22汇合,共同与被散热件100的下游部分换热,这种结构能够使外层上游流道31的较低温介质快速进入内层下游流道22,加快该部分介质与被散热件100的换热,从而提高被散热件100的散热效率。In this embodiment, the medium in the upstream channel 21 of the inner layer can gather toward the internal and external commutation ports 60 located in the middle, and enter the downstream channel 32 of the outer layer through the internal and external commutation ports 60, and the medium enters the downstream channel 32 of the outer layer and then Diffuse in all directions of the downstream flow channel 32 of the outer layer, and the medium is transported to the medium outflow end as a whole; the medium of the upstream flow channel 31 of the outer layer can be divided into two paths at the inner-to-outer flow port, and the medium of one line can pass through an outer-inner flow port 70 intervenes in the downstream channel 22 of the inner layer, and the other channel of medium can enter the downstream channel 22 of the inner layer through another outer-inner commutation port 70, and the two channels of media can merge into the downstream channel 22 of the inner layer, and together with the heat sink 100 Heat exchange in the downstream part, this structure can make the lower temperature medium in the outer layer upstream flow channel 31 quickly enter the inner layer downstream flow channel 22, speed up the heat exchange between this part of the medium and the radiated part 100, thereby improving the heat dissipation of the radiated part 100 efficiency.
其中,可以根据需要设置换流口在隔板10上的位置,例如:换流口的中心可以位于隔板10的二分之一至三分之二处(例如:二分之一、十二分之七或者三分之二等),完成装配后,换流口与隔板10的介质进入端的距离可以为隔板10长度的二分之一至三分之二。外层上游流道31内的介质在输送过程中也会有换热,温度会有增加,上述结构能够保障被散热件100的散热效果。Wherein, the position of the diversion port on the partition plate 10 can be set as required, for example: the center of the diversion port can be located at one-half to two-thirds of the partition plate 10 (for example: one-half, twelve Seven-thirds or two-thirds, etc.), after the assembly is completed, the distance between the commutation port and the medium inlet end of the partition plate 10 can be one-half to two-thirds of the length of the partition plate 10. The medium in the upstream channel 31 of the outer layer will also exchange heat during transportation, and the temperature will increase. The above structure can ensure the heat dissipation effect of the heat sink 100 .
如图2至图6所示,在上述实施例基础之上,可选地,散热组件还可以包括设置在内层子流道内的多个基础齿片80,基础齿片80的长度方向可以与流道的长度方向相同,多个基础齿片80可以沿流道的宽度方向间隔设置;基础齿片80的靠近换流口的一端可以呈斜面设置,且在流道的厚度方向上,基础齿片80的靠近隔板10的一侧可以远离换流口设置。As shown in Figures 2 to 6, on the basis of the above-mentioned embodiments, optionally, the heat dissipation assembly may also include a plurality of basic tooth pieces 80 arranged in the inner sub-flow channel, and the length direction of the basic tooth pieces 80 may be consistent with the The length direction of the flow channel is the same, and a plurality of basic tooth pieces 80 can be arranged at intervals along the width direction of the flow channel; the end of the basic tooth piece 80 close to the commutation port can be arranged on a slope, and in the thickness direction of the flow channel, the basic tooth A side of the sheet 80 close to the separator 10 may be disposed away from the commutation port.
本实施例中,在内层流道20内可以设置基础齿片80,在流道的厚度方向上,基础齿片80的一侧可以与内层子流道的一侧内壁连接,基础齿片80的另一侧可以与内层子流道的另一侧内壁连接,相邻两个基础齿片80之间可以形成介质流通通道;多个基础齿片80能够提高内层子流道的强度,还能够增加介质的换热面积,从而提高换热效率,还能够扰乱介质的流动方向,使得介质紊流,提高换热效果,从而提高被散热件的散热效果。在基础齿片80的靠近换流口的一端可以设置斜面,从而多个基础齿片80能够在换流口处形成豁口,使得多个介质流通通道相互连通,从而能够使得介质能够汇集或者向四处扩散。In this embodiment, a basic tooth piece 80 can be provided in the inner layer flow channel 20, and in the thickness direction of the flow channel, one side of the basic tooth piece 80 can be connected with the inner wall of one side of the inner layer sub-flow channel, and the basic tooth piece The other side of 80 can be connected with the inner wall of the other side of the inner layer sub-channel, and a medium flow channel can be formed between two adjacent basic tooth pieces 80; multiple basic tooth pieces 80 can improve the strength of the inner layer sub-channel , It can also increase the heat exchange area of the medium, thereby improving the heat exchange efficiency, and can also disturb the flow direction of the medium, making the medium turbulent, improving the heat exchange effect, thereby improving the heat dissipation effect of the heat sink. A slope can be set at the end of the basic tooth piece 80 near the commutation port, so that a plurality of basic tooth plates 80 can form gaps at the commutation port, so that multiple medium circulation channels can communicate with each other, so that the medium can be collected or flowed around. diffusion.
如图2至图6所示,在上述实施例基础之上,可选地,内层子流道的与换流口正对的位置可以设有多个换流齿片90,换流齿片90的长度方向可以与流道的长度方向相同,沿流道的宽度方向,多个换流齿片90可以间隔设置;换流齿片90的靠近隔板10的侧部可以呈斜面设置,且在流道的厚度方向上,换流齿片90的远离隔板10的一侧可以远离挡板设置(具体地,沿介质输送方向:在内层流道内,内外换流口的下边沿可以设置内层下挡板,外内换流口的上边沿可以设置内层上挡板;在外层流道内,内外换流口的上边沿可以设置外层上挡板,在外内换流口的下边沿可以设置外层下挡板)。本实施例中,换流齿片90能够提高内层流道20的位于换流口处的强度,提高换流口处的换热效果,换流齿片90可以 呈斜面设置,也即多个换流齿片90的一侧豁口设置,则可以实现介质的汇集或者扩散。As shown in Fig. 2 to Fig. 6, on the basis of the above-mentioned embodiments, optionally, a plurality of commutation teeth 90 may be provided at the position of the inner layer sub-channel facing the commutation port, and the commutation teeth The length direction of 90 can be the same as the length direction of the flow channel, along the width direction of the flow channel, a plurality of commutation teeth 90 can be arranged at intervals; the side of the commutation teeth 90 close to the separator 10 can be arranged on a slope, and In the thickness direction of the flow channel, the side of the commutation tooth piece 90 away from the partition plate 10 can be set away from the baffle plate (specifically, along the medium conveying direction: in the inner layer flow channel, the lower edges of the inner and outer commutation ports can be set Inner layer lower baffle plate, inner layer upper baffle plate can be set on the upper edge of outer and inner commutation port; The outer lower baffle can be set). In this embodiment, the commutation gear 90 can improve the strength of the inner channel 20 at the commutation port and improve the heat exchange effect at the commutation port. The notch on one side of the commutation tooth 90 can realize the collection or diffusion of the medium.
具体地,如图5所示,内外换流口60处的换流齿片90的斜面可以与内层上游流道21内的基础齿片80的斜面面对面设置,两者之间形成V型道,V型道的开口可以面向内外换流口60;如图6所示,外内换流口70处的换流齿片90的斜面可以与内层下游流道22内的基础齿片80的斜面面对面设置,两者之间可以形成V型道,V型道的开口可以面向外内换流口70。Specifically, as shown in FIG. 5 , the slope of the commutation gear 90 at the inner and outer commutation ports 60 can be arranged face to face with the slope of the basic gear 80 in the inner upstream channel 21 , forming a V-shaped channel between the two. , the opening of the V-shaped channel can face the inner and outer commutation ports 60; as shown in FIG. The inclined surfaces are arranged facing each other, and a V-shaped channel can be formed between them, and the opening of the V-shaped channel can face the outer-inner commutation port 70 .
本申请的实施例还提供了一种光纤激光器,该光纤激光器可以包括被散热件100和上述任一技术方案的散热组件,流道可以与被散热件100连接,且外层流道30可以位于内层流道20的远离被散热件100的一侧。本实施例中的光纤激光器可以包括上述任一技术方案的散热组件,因而,具有该散热组件的全部有益技术效果,在此,不再赘述。The embodiment of the present application also provides a fiber laser. The fiber laser can include a heat sink 100 and a heat dissipation assembly of any of the above-mentioned technical solutions. The flow channel can be connected to the heat sink 100, and the outer flow channel 30 can be located at The side of the inner flow channel 20 away from the heat sink 100 . The fiber laser in this embodiment may include the heat dissipation component of any of the above technical solutions, and thus has all the beneficial technical effects of the heat dissipation component, which will not be repeated here.
其中,流道可以独立包括多个首尾依次连接的侧板,流道作为一个独立部件可以安装在被散热件100上。Wherein, the flow channel may independently include a plurality of side plates connected end to end in sequence, and the flow channel may be installed on the heat sink 100 as an independent component.
作为一种可选方案,被散热件100可以形成流道的一侧壁,也即流道的一个侧板可以为被散热件100,则内层流道20内的介质可以直接与被散热件100接触,可以提高换热效率和换热效果,从而提高被散热件100的散热效率和散热效果。例如:被散热件100可以为光纤盘,流道可以与光纤盘连接,且光纤盘可以直接作为流道的一侧壁。As an alternative, the heat-dissipated part 100 can form a side wall of the flow channel, that is, one side plate of the flow channel can be the heat-dissipated part 100, and the medium in the inner layer flow channel 20 can directly contact the heat-dissipated part The 100 contact can improve the heat exchange efficiency and heat exchange effect, thereby improving the heat dissipation efficiency and heat dissipation effect of the radiated part 100 . For example, the heat-dissipated part 100 may be a fiber optic disk, the flow channel may be connected to the fiber optic disk, and the fiber optic disk may directly serve as a side wall of the flow channel.
最后应说明的是:以上各实施例仅用以说明本申请的技术方案,而非对其限制;尽管参照前述各实施例对本申请进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本申请各实施例技术方案的范围。在此处所提供的说明书中,说明了大量具体细节。然而,能够理解,本申请的实施例可以在没有这些具体细节的情况下实践。在一些实例中,并未详细示出公知的方法、结构和技术,以便不模糊对本说明书的理解。此外,本领域的技术人员能够理解,尽管在此的一些实施例包括其它实施例中所包括的某些特征而不是其它特征,但是不同实施例的特征的组合意味着处于本申请的范围之内并且形成不同的实施例。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present application, and are not intended to limit it; although the application has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present application. scope. In the description provided herein, numerous specific details are set forth. However, it is understood that the embodiments of the application may be practiced without these specific details. In some instances, well-known methods, structures and techniques have not been shown in detail in order not to obscure the understanding of this description. In addition, those skilled in the art will appreciate that although some embodiments herein include some features included in other embodiments but not others, combinations of features from different embodiments are meant to be within the scope of the present application. And form different embodiments.
工业实用性Industrial Applicability
本申请涉及光纤激光器散热技术领域,尤其是涉及一种散热组件及光纤激光器。所述散热组件,包括:流道,流道包括并列设置的内层流道和外层流道;在流道的长度方向上,内层流道包括至少两个间隔设置的内层子流道,外层流道包括至少两个间隔设置的外层子流道;在流道的长度方向上,相邻设置的内层子流道和外层子流道相互连通,且相互连通的内层子流道和外层子流道位于不同位置。本发明本申请提供的散热组件可以使被散热件的靠近介质流出端的部分的换热量大,散热量大,降温多,温度低,进而可以减小被散热 件两端的温差,有利于改善被散热件的散热均匀性和温度均匀性。The present application relates to the technical field of fiber laser heat dissipation, in particular to a heat dissipation component and a fiber laser. The heat dissipation assembly includes: a flow channel, the flow channel includes an inner layer flow channel and an outer layer flow channel arranged side by side; in the length direction of the flow channel, the inner layer flow channel includes at least two inner layer sub-channels arranged at intervals , the outer layer flow channel includes at least two outer layer sub-channels arranged at intervals; in the length direction of the flow channel, the adjacent inner layer sub-channels and outer layer sub-channels communicate with each other, and the interconnected inner layer Sub-runners and outer sub-runners are in different positions. The heat dissipation assembly provided by the present invention can make the part of the heat-dissipated part close to the medium outflow end have a large heat transfer amount, a large heat dissipation, a large temperature drop, and a low temperature, thereby reducing the temperature difference between the two ends of the heat-dissipated part, which is conducive to improving Heat dissipation uniformity and temperature uniformity of the heat sink.
此外,可以理解的是,本申请的散热组件及光纤激光器是可以重现的,并且可以应用在多种工业应用中。例如,本申请的散热组件及光纤激光器可以用于任何需要散热的领域。In addition, it can be understood that the heat dissipation assembly and fiber laser of the present application are reproducible and can be applied in various industrial applications. For example, the heat dissipation assembly and the fiber laser of the present application can be used in any field requiring heat dissipation.

Claims (15)

  1. 一种散热组件,其特征在于,包括:流道,所述流道包括并列设置的内层流道和外层流道;在所述流道的长度方向上,所述内层流道包括至少两个间隔设置的内层子流道,所述外层流道包括至少两个间隔设置的外层子流道,相邻设置的所述内层子流道和所述外层子流道相互连通,且相互连通的所述内层子流道和所述外层子流道位于不同位置。A heat dissipation assembly, characterized in that it includes: a flow channel, the flow channel includes an inner layer flow channel and an outer layer flow channel arranged side by side; in the length direction of the flow channel, the inner layer flow channel includes at least Two inner layer sub-channels arranged at intervals, the outer layer channel includes at least two outer layer sub-channels arranged at intervals, the adjacently arranged inner layer sub-channels and the outer layer sub-channels are mutually The inner layer sub-channels and the outer layer sub-channels that communicate with each other are located at different positions.
  2. 根据权利要求1所述的散热组件,其特征在于,所述流道内设有隔板,所述隔板将所述流道分隔形成所述内层流道和所述外层流道;所述隔板的两侧分别连接有挡板,所述挡板的远离所述隔板的侧部均与所述流道的内壁抵接,所述内层流道内的所述挡板将所述内层流道分隔成至少两个所述内层子流道,所述外层流道内的所述挡板将所述外层流道分隔成至少两个所述外层子流道;所述隔板上设有至少两个换流口,所述内层子流道和所述外层子流道通过所述换流口连通。The heat dissipation assembly according to claim 1, wherein a baffle is provided in the flow channel, and the baffle separates the flow channel to form the inner layer flow channel and the outer layer flow channel; Baffles are respectively connected to both sides of the partition, and the sides of the baffles far away from the partition are in contact with the inner wall of the flow channel, and the baffles in the inner layer flow channel connect the The inner channel is divided into at least two inner sub-channels, and the baffle in the outer channel divides the outer channel into at least two outer sub-channels; At least two diversion ports are arranged on the separator, and the inner layer sub-channel and the outer layer sub-channel are communicated through the diversion ports.
  3. 根据权利要求2所述的散热组件,其特征在于,所述内层子流道的数量与所述外层子流道的数量是相同的。The heat dissipation assembly according to claim 2, wherein the number of the inner layer sub-channels is the same as the number of the outer layer sub-channels.
  4. 根据权利要求2或3所述的散热组件,其特征在于,所述挡板包括上挡板、下挡板以及连接在所述上挡板和所述下挡板之间的中挡板;在所述隔板的宽度方向上,相邻两个所述换流口中,一个所述换流口的上游设有所述上挡板,另一个所述换流口的下游设有下挡板,相邻两个所述换流口之间设有中挡板,且对于同一个所述换流口,在流道的长度方向上,换流口的一侧设置上挡板,换流口的另一侧设置下挡板。The heat dissipation assembly according to claim 2 or 3, wherein the baffle includes an upper baffle, a lower baffle, and a middle baffle connected between the upper baffle and the lower baffle; In the width direction of the separator, among the two adjacent diversion ports, the upper baffle is provided upstream of one diversion port, and the lower baffle is provided downstream of the other diversion port, An intermediate baffle is provided between two adjacent flow ports, and for the same flow port, in the length direction of the flow channel, an upper baffle is provided on one side of the flow port, and an upper baffle is provided on one side of the flow port. The other side is provided with a lower baffle.
  5. 根据权利要求2至4中的任一项所述的散热组件,其特征在于,所述散热组件还包括设置在所述内层子流道内的多个基础齿片,所述基础齿片的长度方向与所述流道的长度方向相同,多个所述基础齿片沿所述流道的宽度方向间隔设置;所述基础齿片的靠近所述换流口的一端呈斜面设置,且在所述流道的厚度方向上,所述基础齿片的靠近所述隔板的一侧远离所述换流口设置。The heat dissipation assembly according to any one of claims 2 to 4, characterized in that, the heat dissipation assembly further comprises a plurality of basic tooth pieces arranged in the inner layer sub-channel, and the length of the basic tooth pieces is The direction is the same as the length direction of the flow channel, and a plurality of the basic tooth pieces are arranged at intervals along the width direction of the flow channel; In the thickness direction of the flow channel, the side of the basic tooth piece close to the partition plate is arranged away from the commutation port.
  6. 根据权利要求5所述的散热组件,其特征在于,在所述流道的厚度方向上,所述基础齿片的一侧与所述内层子流道的一侧内壁连接,所述基础齿片的另一侧与所述内层子流道的另一侧内壁连接,相邻两个基础齿片之间形成介质流通通道。The heat dissipation assembly according to claim 5, characterized in that, in the thickness direction of the flow channel, one side of the basic tooth piece is connected to the inner wall of one side of the inner layer sub-flow channel, and the basic tooth The other side of the sheet is connected to the inner wall of the other side of the sub-channel in the inner layer, and a medium circulation channel is formed between two adjacent basic tooth sheets.
  7. 根据权利要求5或6所述的散热组件,其特征在于,所述内层子流道的与所述换流口正对的位置设有多个换流齿片,所述换流齿片的长度方向与所述流道的长度方向相同,沿所述流道的宽度方向,多个所述换流齿片间隔设置;所述换流齿片的靠近所述隔板的侧部呈斜面设置,且在所述流道的厚度方向上,所述换流齿片的远离所述隔板的一侧远离所述挡板设置。The heat dissipating assembly according to claim 5 or 6, characterized in that, a plurality of commutation teeth are provided at the position of the inner layer sub-channel facing the commutation port, and the commutation teeth are The length direction is the same as the length direction of the flow channel, and along the width direction of the flow channel, a plurality of the commutation teeth are arranged at intervals; the sides of the commutation teeth close to the partition are arranged on an inclined plane , and in the thickness direction of the flow channel, the side of the commutation tooth piece away from the separator is arranged away from the baffle.
  8. 根据权利要求7所述的散热组件,其特征在于,在所述流道的长度方向上,所述换流口的数量为一个,在所述流道的宽度方向上,所述换流口的数量为多个;所述隔板的两侧各设有一个所述挡板,所述内层子流道为两个,一个为内层上游流道,另一个为内层下游流道,所述外层子流道的数量为两个,一个为外层上游流道,另一个为外层下游流道。The heat dissipation assembly according to claim 7, characterized in that, in the length direction of the flow channel, the number of the flow change ports is one, and in the width direction of the flow channel, the number of the flow change ports is The number is multiple; each side of the partition is provided with a baffle plate, and the inner layer sub-flow channel is two, one is the inner layer upstream flow channel, and the other is the inner layer downstream flow channel, so The number of sub-channels in the outer layer is two, one is the upstream channel of the outer layer, and the other is the downstream channel of the outer layer.
  9. 根据权利要求8所述的散热组件,其特征在于,换流口的数量为三个,其中一个为内外换流口,另外两个为外内换流口,所述内外换流口位于两个所述外内换流口之间;所述内层上游流道通过所述内外换流口与所述外层上游流道连通,所述外层上游流道通过所述外内换流口与所述内层下游流道连通。The heat dissipation assembly according to claim 8, characterized in that, there are three commutation ports, one of which is an internal and external commutation port, and the other two are external and internal commutation ports, and the internal and external commutation ports are located between two between the outer and inner commutation ports; the inner upstream channel communicates with the outer upstream channel through the inner and outer commutation ports, and the outer upstream channel communicates with the outer upstream channel through the outer and inner commutation ports The downstream channel of the inner layer is connected.
  10. 根据权利要求9所述的散热组件,其特征在于,所述内外换流口处的所述换流齿片的斜面与所述内层上游流道内的所述基础齿片的斜面面对面设置,所述内外换流口处的所述换流齿片的斜面与所述内层上游流道内的所述基础齿片的斜面之间形成面向所述内外换流口的V型道。The heat dissipation assembly according to claim 9, characterized in that, the inclined surface of the commutation tooth at the inner and outer commutation ports is arranged face to face with the inclined surface of the basic tooth in the upstream channel of the inner layer, so A V-shaped channel facing the inner and outer commutation ports is formed between the slope of the commutation gear at the inner and outer commutation ports and the slope of the basic tooth in the inner upstream channel.
  11. 根据权利要求9或10所述的散热组件,其特征在于,所述外内换流口处的所述换流齿片的斜面与所述内层下游流道内的所述基础齿片的斜面面对面设置,所述外内换流口处的所述换流齿片的斜面与所述内层下游流道内的所述基础齿片的斜面之间形成面向所述外内换流口的V型道。The heat dissipation assembly according to claim 9 or 10, characterized in that, the slope of the commutation tooth at the outer and inner commutation ports faces the slope of the basic tooth in the downstream channel of the inner layer It is set that a V-shaped channel facing the outer and inner commutation ports is formed between the slope of the commutation tooth at the outer and inner commutation port and the slope of the basic tooth in the inner layer downstream channel .
  12. 根据权利要求9所述的散热组件,其特征在于,在所述隔板的长度方向上,所述换流口的中心位于所述隔板的二分之一至三分之二处。The heat dissipation assembly according to claim 9, characterized in that, in the length direction of the partition, the center of the flow opening is located at one-half to two-thirds of the partition.
  13. 一种光纤激光器,其特征在于,包括被散热件和根据权利要求1-12中的任一项所述的散热组件,所述流道与所述被散热件连接,且所述外层流道位于所述内层流道的远离所述被散热件的一侧。A fiber laser, characterized in that it includes a heat sink and the heat dissipation assembly according to any one of claims 1-12, the flow channel is connected to the heat sink, and the outer flow channel It is located on the side of the inner flow channel away from the heat sink.
  14. 根据权利要求13所述的光纤激光器,其特征在于,所述被散热件形成所述流道的一侧壁。The fiber laser according to claim 13, wherein the heat-dissipated member forms a side wall of the flow channel.
  15. 根据权利要求13或14所述的散热组件,其特征在于,所述流道包括多个沿所述被散热件的宽度方向依次设置的折线型管道,同一折线型管道的一部分靠近所述被散热件设置,所述折线型管道的另一部分远离所述被散热件设置。The heat dissipating assembly according to claim 13 or 14, wherein the flow channel comprises a plurality of broken-line pipes arranged in sequence along the width direction of the heat-dissipated part, and a part of the same broken-line pipe is close to the heat-dissipated part. The other part of the zigzag pipe is set away from the heat sink.
PCT/CN2021/134479 2021-09-27 2021-11-30 Heat dissipation assembly and fiber laser WO2023045073A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202111138742.7 2021-09-27
CN202111138742.7A CN113783086A (en) 2021-09-27 2021-09-27 Heat dissipation assembly and optical fiber laser

Publications (1)

Publication Number Publication Date
WO2023045073A1 true WO2023045073A1 (en) 2023-03-30

Family

ID=78853922

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2021/134479 WO2023045073A1 (en) 2021-09-27 2021-11-30 Heat dissipation assembly and fiber laser

Country Status (2)

Country Link
CN (1) CN113783086A (en)
WO (1) WO2023045073A1 (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5508883A (en) * 1992-04-10 1996-04-16 International Business Machines Corporation Air mixer cool plate
CN1591699A (en) * 2003-08-28 2005-03-09 株式会社东芝 Radiator and radiating method
JP2005203466A (en) * 2004-01-14 2005-07-28 Fuji Electric Fa Components & Systems Co Ltd Heatsink
CN101922870A (en) * 2010-08-31 2010-12-22 东南大学 Dividing wall type heat exchanger
JP2013016681A (en) * 2011-07-05 2013-01-24 Koito Mfg Co Ltd Heat radiation member and heat radiation mechanism
CN106098656A (en) * 2015-04-27 2016-11-09 发那科株式会社 Radiator
CN107532865A (en) * 2015-04-17 2018-01-02 株式会社电装 Heat exchanger

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1605220B1 (en) * 2003-02-27 2009-11-11 Laserfront Technologies, Inc. Heat sunk, laser module, laser device, and laser-processing device
CN203225449U (en) * 2013-05-16 2013-10-02 熊英 Cooling device of optical fiber laser
WO2019018446A1 (en) * 2017-07-17 2019-01-24 Fractal Heatsink Technologies, LLC Multi-fractal heat sink system and method
CN213586758U (en) * 2020-11-20 2021-06-29 江苏杰源智能制造有限公司 Heat dissipation tooth
CN215645409U (en) * 2021-09-27 2022-01-25 北京热刺激光技术有限责任公司 Heat dissipation assembly and optical fiber laser

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5508883A (en) * 1992-04-10 1996-04-16 International Business Machines Corporation Air mixer cool plate
CN1591699A (en) * 2003-08-28 2005-03-09 株式会社东芝 Radiator and radiating method
JP2005203466A (en) * 2004-01-14 2005-07-28 Fuji Electric Fa Components & Systems Co Ltd Heatsink
CN101922870A (en) * 2010-08-31 2010-12-22 东南大学 Dividing wall type heat exchanger
JP2013016681A (en) * 2011-07-05 2013-01-24 Koito Mfg Co Ltd Heat radiation member and heat radiation mechanism
CN107532865A (en) * 2015-04-17 2018-01-02 株式会社电装 Heat exchanger
CN106098656A (en) * 2015-04-27 2016-11-09 发那科株式会社 Radiator

Also Published As

Publication number Publication date
CN113783086A (en) 2021-12-10

Similar Documents

Publication Publication Date Title
KR100950689B1 (en) Plate type heat exchanger
WO2014059773A1 (en) Heat exchanger plate, heat exchanger, and enclosure of communication base station
CN216121199U (en) Cooling heat sink and stacked array applied to high-power semiconductor light source chip
CN112577342A (en) Heat exchange plate and heat exchanger
WO2023045073A1 (en) Heat dissipation assembly and fiber laser
CN215645409U (en) Heat dissipation assembly and optical fiber laser
JP7432742B2 (en) Heat exchanger
TWI489742B (en) Linear motor air-cooling structure
CN213026252U (en) Liquid cooling plate for battery pack
TWM623183U (en) Liquid cooling device and cooling equipment
US10663845B2 (en) Color wheel device and projector
KR101163995B1 (en) Oilcooler
JP4075413B2 (en) Plate heat exchanger
JPH08291990A (en) Heat-exchanger element
CN214384464U (en) Heat exchange plate and heat exchanger
JP2011119555A (en) Heat sink using bent louver-like heat dissipation unit
JP2007085594A (en) Cross flow core type plate heat exchanger
CN113078764A (en) Motor liquid cooling structure
KR20060061472A (en) Plate having 3-dimensional microchannel and heat exchanger using it
CN220172239U (en) Liquid cooling plate and energy storage device
CN114630566B (en) Multilayer reposition of redundant personnel liquid cooling board
CN215221912U (en) Motor liquid cooling structure
CN217036305U (en) Heat dissipation plate and fiber laser of parallel multi-fluid channel flow equalizing structure
JP2001041109A (en) Exhaust heat exchanger
JP4522725B2 (en) heatsink

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 21958185

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205A DATED 08/07/2024)