CN211012619U

CN211012619U - Two-stage crotch type fin and heat exchanger

Info

Publication number: CN211012619U
Application number: CN201921664079.2U
Authority: CN
Inventors: 卢楚鹏; 胡伟强
Original assignee: Guangdong Wanhe Thermal Energy Technology Co Ltd
Current assignee: Guangdong Wanhe Thermal Energy Technology Co Ltd
Priority date: 2019-09-30
Filing date: 2019-09-30
Publication date: 2020-07-14
Anticipated expiration: 2029-09-30

Abstract

The utility model discloses a second grade crotch type fin to a heat exchanger with this second grade crotch type fin is disclosed, wherein second grade crotch type fin includes the fin body, be provided with on the fin body: more than two openings are arranged in a linear arrangement; the heat exchange flow channel is arranged between any two adjacent openings and comprises a primary groove, a secondary groove and a tertiary groove which are sequentially communicated; wherein, the one end intercommunication of one-level recess is two the one end of second grade recess, at least one the other end intercommunication of second grade recess is two the one end of tertiary recess, the utility model discloses can improve the heat transfer effect that the flue gas flowed through the fin body effectively, reduce material consumption.

Description

Two-stage crotch type fin and heat exchanger

Technical Field

The utility model relates to a heat exchange equipment, in particular to second grade crotch type fin and heat exchanger.

Background

The fin flue gas heat exchanger is a device for exchanging heat by utilizing external high-temperature flue gas and low-temperature water, fins are important components, and play an important role in influencing the overall heat exchange effect, in the heat exchanger, cold medium circularly flows in a heat exchange tube and exchanges heat with a heat exchange tube wall, the fins exchange heat with the high-temperature flue gas, the laminar flow boundary greatly obstructs the heat exchange between the flue gas and the fins, flat heat exchange channels are formed between flat fins arranged by the existing uniform arrangement, and the efficiency is lower when the flue gas passes through the heat exchange channels.

SUMMERY OF THE UTILITY MODEL

The utility model discloses aim at solving one of the technical problem that exists among the prior art at least. Therefore, the utility model provides a second grade crotch type fin can improve the heat exchange efficiency of fin.

The utility model also provides a heat exchanger of having above-mentioned second grade crotch type fin.

According to the utility model discloses a second grade crotch type fin of first aspect embodiment, including the fin body, be provided with on the fin body: more than two openings are arranged in a linear arrangement; the heat exchange flow channel is arranged between any two adjacent openings and comprises a primary groove, a secondary groove and a tertiary groove which are sequentially communicated; one end of the first-stage groove is communicated with one end of the second-stage groove, and the other end of the at least one second-stage groove is communicated with one end of the third-stage groove.

According to the utility model discloses second grade crotch type fin has following beneficial effect at least: the fin body is provided with the opening for inserting the external heat exchange tube, and a heat exchange flow channel for improving the heat exchange effect is arranged between any two adjacent openings, specifically, when the smoke passes through the surface of the fin body, the first-stage groove, the second-stage groove and the third-stage groove improve the mutual mixing between high-temperature fluid and low-temperature fluid, so that the heat exchange effect is improved, especially, when the smoke passes through the second-stage groove from the first-stage groove, and passes through a bifurcation point when passing through the third-stage groove from the second-stage groove, the fluid can form secondary flow near the bifurcation point when passing through the bifurcation point, namely, the backflow and separation phenomena are generated, the mutual mixing of the high-temperature fluid and the low-temperature fluid is further improved, the secondary flow has higher strength even under the low Reynolds number, and the heat exchange effect of the smoke passing through the fin body can.

According to the utility model discloses a few embodiments, the other end of one-level recess is provided with the air intake, the other end of tertiary recess is provided with the air outlet. The flue gas directly enters into first recess from air intake department, after the second recess, flows from the air outlet department of third recess.

According to some embodiments of the utility model, still be provided with a plurality of through-hole on the fin body, the through-hole be located with two of one-level recess intercommunication between the second grade recess. The position between the two secondary grooves on the fin body belongs to a heat exchange weak area, and the through hole formed in the heat exchange weak area is favorable for damaging the viscous bottom layer and enhancing the mixing of the near-wall-surface low-temperature fluid and the main-stream high-temperature fluid, so that the heat exchange is enhanced, the material consumption can be reduced, and the manufacturing cost is saved.

According to some embodiments of the invention, the through-hole is oval. The oval through holes can further improve the mixing effect of the low-temperature fluid and the high-temperature fluid and strengthen heat exchange.

According to the utility model discloses a some embodiments, the through-hole is provided with a plurality ofly, and arbitrary two are adjacent along the extending direction of one-level recess distance is 6mm to 10mm between the through-hole. In this distance range, the disturbance generated by the previous through hole can be transmitted to the next through hole, so as to better improve the heat exchange effect.

According to some embodiments of the invention, the side of the opening has a flange. The external heat exchange tube inserted into the opening can be abutted against the turned edge, so that the structural stability of the fin body and the heat exchange tube is improved.

According to some embodiments of the present invention, the diameter of the primary groove is D1, the diameter of the secondary groove is D2, the diameter of the tertiary groove is D3, wherein the ratio of D1 to D2 is 0.6 to 0.9, and the ratio of D2 to D3 is 0.6 to 0.9. The diameters of the first groove, the second groove and the third groove are sequentially decreased progressively according to the proportion range, so that a good heat exchange effect is ensured.

According to some embodiments of the present invention, the length of the first-stage groove is H1, the length of the second-stage groove is H2, and the length of the third-stage groove is H3, wherein the ratio of H1 to H2 is 0.8 to 0.9, and the ratio of H2 to H3 is 0.8 to 0.9. The lengths of the first groove, the second groove and the third groove are sequentially decreased progressively according to the proportion range.

According to the utility model discloses a some embodiments, two contained angle between the second grade recess is a, is connected to any two of second grade recess contained angle between the tertiary recess is b, and wherein, an equals b. And the second groove extending from the first groove and the third groove extending from the second groove are diverged and diverged according to the same included angle.

According to the utility model discloses a heat exchanger of second aspect embodiment, including the heat exchange tube, still include the above-mentioned that a plurality of block align to grid set up second grade crotch type fin, on the second grade crotch type fin the trompil is used for supplying the heat exchange tube passes, arbitrary piece second grade crotch type fin the one-level recess the second grade recess with the degree of depth of tertiary recess is h, and arbitrary two are adjacent distance between the second grade crotch type fin is d, and wherein, the ratio of h and d is 0.35 to 0.5.

According to the utility model discloses a heat exchanger has following beneficial effect at least: utilize above-mentioned second grade crotch type fin to arrange the setting, form a flue gas passageway between two second grade crotch type fins, when the flue gas passes through flue gas passageway, partial flue gas can flow into to the heat transfer runner in, alternate the heat exchange tube at every trompil internal fixation, the one-level recess depth of every second grade crotch type fin, the second grade recess depth, tertiary recess depth homogeneous phase is the same, and convenient to process, and the one-level recess depth, the second grade recess depth, there is certain proportional relation tertiary recess depth and the distance between arbitrary two adjacent second grade crotch type fins, can obtain better heat transfer effect in this proportional design.

Drawings

The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

fig. 1 is a schematic structural diagram of a two-stage crotch-type fin according to an embodiment of the present invention.

A fin body 100,

Opening 200, primary groove 210, secondary groove 220, tertiary groove 230, and via 240.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary only for the purpose of explaining the present invention, and should not be construed as limiting the present invention.

In the description of the present invention, a plurality of means are one or more, a plurality of means are two or more, and the terms greater than, less than, exceeding, etc. are understood as not including the number, and the terms greater than, less than, within, etc. are understood as including the number.

In the description of the present invention, unless there is an explicit limitation, the words such as setting, installation, connection, etc. should be understood in a broad sense, and those skilled in the art can reasonably determine the specific meanings of the above words in combination with the specific contents of the technical solution.

Referring to fig. 1, in the heat exchanger, including a plurality of fins arranged uniformly, the heat exchange tube is inserted into the opening 200 of each fin to connect and fix the fin, the fin is connected with the heat exchange tube by welding, a heat exchange flow channel is punched on the fin, when the flue gas enters the flue gas channel, the high temperature flue gas and the surface of the fin and the heat exchange tube generate heat convection, and the heat is transferred to the low temperature water in the heat exchange tube by heat conduction and heat convection, the heat exchange flow channel includes a first-level groove 210, a second-level groove 220 and a third-level groove 230 arranged on the fin body 100, the connection of the first-level groove 210, the second-level groove 220, the third-level groove 230 and the fin body 100 is a fillet structure, so that the flue gas can be mixed at the connection, the cooperation degree of the local area velocity field and the temperature field is enhanced, thereby realizing low resistance, The depth of the third-stage groove 230 is set according to the distance between the two second-stage crotch-type fins, specifically, the depth of the first-stage groove 210, the depth of the second-stage groove 220, and the depth of the third-stage groove 230 of any two second-stage crotch-type fins are all h, the distance between any two adjacent second-stage crotch-type fins is d, and the ratio of h to d is 0.35 to 0.5, so that a good heat exchange effect can be achieved under the ratio, in some embodiments, the ratio is 0.4, and a best heat exchange effect can be achieved under the ratio.

The fin includes fin body 100, be provided with a plurality of trompil 200 along left right direction linear arrangement on fin body 100, be provided with the heat transfer runner between two arbitrary adjacent trompils 200, the heat transfer runner includes by the back one-level runner that sets gradually to the front, second grade runner and tertiary runner, the one-level runner is including setting up in the one-level recess 210 of fin body 100 bottom surface, the second grade runner is including connecting in two second grade recesses 220 of one-level recess 210 front end, tertiary runner is including connecting in two tertiary recesses 230 of any second grade recess 220 front end.

The fin body 100 is provided with openings 200 for inserting external heat exchange tubes, and a heat exchange flow channel for improving a heat exchange effect is provided between any two adjacent openings 200, specifically, when the flue gas passes through the surface of the fin body 100, the primary grooves 210, the secondary grooves 220 and the tertiary grooves 230 improve the mutual mixing between the high-temperature fluid and the low-temperature fluid, thereby improving the heat exchange effect, particularly when the flue gas passes through the secondary flow channel from the primary flow channel from back to front and passes through a bifurcation point when passing through the tertiary flow channel from the secondary flow channel, the fluid can form secondary flow near the bifurcation point when passing through the bifurcation point, namely, the reflux and separation phenomena are generated, the mutual mixing of the high-temperature fluid and the low-temperature fluid is further improved, the secondary flow has high strength even at a low reynolds number, and the heat exchange effect of the flue gas flowing through the fin body 100 can be effectively improved.

In some embodiments, the extension of the primary grooves 210, the secondary grooves 220, and the tertiary grooves 230 may be bent, which also improves the heat exchange effect of the flue gas flowing through the fin body 100.

In this embodiment, the other end of the first-stage groove 210 is provided with an air inlet, and the other end of the third-stage groove 230 is provided with an air outlet. The flue gas directly enters into one-level recess 210 from the air inlet, after second grade recess 220, flows out from the air outlet of tertiary recess 230, and the other end of tertiary recess 230 extends to the heat exchange tube and keeps away from the party of one-level recess 210 simultaneously, and this structure forms the tapered runner and can guide fluid to pipe back wake vortex district and converge, has effectually inhibited the development of pipe back wake vortex to reduce the size in heat transfer weak area, and reduce and form the wake vortex because of the boundary layer separation and produce friction loss.

In this embodiment, the heat exchange flow channel further includes a through hole 240 disposed on the fin body 100, the center of the through hole 240 is located on the central line of the primary groove 210, and the through hole 240 is located in front of the primary groove 210. The position of the fin body 100 in front of the primary groove 210 belongs to a heat exchange weak area, and the through hole 240 arranged on the heat exchange weak area is beneficial to breaking a viscous bottom layer and enhancing the mixing of the low-temperature fluid close to the wall surface and the main high-temperature fluid, so that the heat exchange is enhanced, the material consumption can be reduced, and the manufacturing cost is saved.

In this embodiment, the through hole 240 has an oval shape. When smoke flows through the through holes 240 of the elliptical structure, the flow of the smoke on the fin body 100 belongs to low Reynolds number flow, and the viscous bottom layer has no obvious limit with the main flow.

In this embodiment, a plurality of through holes 240 are provided along the extending direction of the primary groove 210, and the distance between any two adjacent through holes 240 is 7 mm. At this distance, the disturbance generated by the previous through hole 240 can be transferred to the next through hole 240, so as to achieve a better heat exchange effect.

In this embodiment, the edge of the opening 200 has a flange, and the direction of the flange is the same as the direction of the recess. The peripheral heat exchange tube inserted into the opening 200 can be abutted to the turned edge and welded with the heat exchange tube by the turned edge, so that the heat exchange tube is more convenient and faster.

In this embodiment, the diameter of the primary groove 210 is D1, the diameter of the secondary groove 220 is D2, and the diameter of the tertiary groove 230 is D3, wherein D1 and D2 are 0.78, and D2 and D3 are 0.78. Further, the diameter of the secondary groove 220 is widened so as to increase the temperature gradient between the fluid in the secondary groove 220 and the heat exchange tube.

In this embodiment, the length of the primary groove 210 is H1, the length of the secondary groove 220 is H2, and the length of the tertiary groove 230 is H3, wherein H1 and H2 are 0.9, and H2 and H3 are 0.9. The distance between one end of the primary groove 210 far away from the secondary groove 220 and one side of the fin body 100 close to the primary groove 210 is 5 to 10 mm.

In this embodiment, an included angle between the two second grooves is a, an included angle between the two third grooves connected to any one of the second grooves is b, and a is equal to b and is equal to 50 degrees. And the second groove extending from the first groove and the third groove extending from the second groove are diverged and diverged according to the same included angle.

With the heat exchanger that conventional fin constitutes with the utility model discloses the heat exchanger that the second grade crotch type fin after the institutional advancement constitutes carries out contrast test, with on a rated power is 28 KW's hanging stove, obtains as following data shown in 1:

table 1:

as can be seen from the table above, in the heat exchanger of the invention, the single fin has higher heat exchange amount and lighter weight, which is beneficial to reducing the consumption of copper materials and reducing the cost.

The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art.

Claims

1. The utility model provides a two-stage crotch type fin which characterized in that: including fin body (100), be provided with on fin body (100):

more than two openings (200) which are arranged in a linear arrangement;

the heat exchange flow channel is arranged between any two adjacent openings (200), and comprises a primary groove (210), a secondary groove (220) and a tertiary groove (230) which are sequentially communicated;

one end of the primary groove (210) is communicated with one end of the two secondary grooves (220), and the other end of at least one secondary groove (220) is communicated with one end of the two tertiary grooves (230).

2. The two-stage crotch-type fin according to claim 1, wherein: the other end of the first-level groove (210) is provided with an air inlet, and the other end of the third-level groove (230) is provided with an air outlet.

3. The two-stage crotch-type fin according to claim 1, wherein: the fin body (100) is further provided with a plurality of through holes (240), and the through holes (240) are located between the two secondary grooves (220) communicated with the primary grooves (210).

4. The two-stage crotch-type fin according to claim 3, wherein: the through hole (240) is oval.

5. The two-stage crotch-type fin according to claim 3, wherein: the through holes (240) are arranged in a plurality of numbers along the extending direction of the primary groove (210), and the distance between any two adjacent through holes (240) is 6mm to 10 mm.

6. The two-stage crotch-type fin according to claim 1, wherein: the side of the opening hole (200) is provided with a flanging.

7. The two-stage crotch-type fin according to claim 1, wherein: the diameter of the primary groove (210) is D1, the diameter of the secondary groove (220) is D2, and the diameter of the tertiary groove (230) is D3, wherein the ratio of D1 to D2 is 0.6-0.9, and the ratio of D2 to D3 is 0.6-0.9.

8. The two-stage crotch-type fin according to claim 1, wherein: the length of the primary groove (210) is H1, the length of the secondary groove (220) is H2, and the length of the tertiary groove (230) is H3, wherein the ratio of H1 to H2 is 0.8-0.9, and the ratio of H2 to H3 is 0.8-0.9.

9. The two-stage crotch-type fin according to claim 1, wherein: an included angle between the two secondary grooves (220) is a, an included angle between the two tertiary grooves (230) connected to any one of the secondary grooves (220) is b, and a is equal to b.

10. A heat exchanger, characterized by: the heat exchange tube comprises a heat exchange tube and further comprises a plurality of secondary crotch-type fins which are uniformly arranged and are as claimed in any one of claims 1 to 9, the opening (200) in each secondary crotch-type fin is used for the heat exchange tube to penetrate, the depth of each primary groove (210), each secondary groove (220) and each tertiary groove (230) in each secondary crotch-type fin is h, the distance between any two adjacent secondary crotch-type fins is d, and the ratio of h to d is 0.35-0.5.