CN101539384A - Fins for serial fin type heat exchanger - Google Patents

Fins for serial fin type heat exchanger Download PDF

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Publication number
CN101539384A
CN101539384A CN200910020384A CN200910020384A CN101539384A CN 101539384 A CN101539384 A CN 101539384A CN 200910020384 A CN200910020384 A CN 200910020384A CN 200910020384 A CN200910020384 A CN 200910020384A CN 101539384 A CN101539384 A CN 101539384A
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CN
China
Prior art keywords
fin
fin body
disturbance
heat exchanger
pore
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN200910020384A
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Chinese (zh)
Inventor
蒋积良
宋晓兵
张永健
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG GUANGDA MACHINE MANUFACTURING Co Ltd
Original Assignee
SHANDONG GUANGDA MACHINE MANUFACTURING Co Ltd
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 SHANDONG GUANGDA MACHINE MANUFACTURING Co Ltd filed Critical SHANDONG GUANGDA MACHINE MANUFACTURING Co Ltd
Priority to CN200910020384A priority Critical patent/CN101539384A/en
Publication of CN101539384A publication Critical patent/CN101539384A/en
Pending legal-status Critical Current

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Abstract

The invention discloses fins for a serial fin type heat exchanger. A fin body between pipe holes is provided with a first disturbance protrusion, thereby improving the rigidity of the fin body and playing a disturbance role in media which flow through the surface of the fin body, and turbulent heat transfer is arisen so as to ensure that the surface heat transfer coefficient of the fins is greatly improved. But at the same time, large numbers of medium vortex turbulent flow clusters are formed so as to increase the pressure loss when the media pass through a core body. The side face of the first disturbance protrusion is provided with a notch which is communicated with both sides of the fin body so as to ensure that partial media enter the other side of the fin body through the notch, thereby solving the technical problem of the vortex turbulent flow clusters and further improving the heat exchange efficiency of the fins.

Description

The fin of sheet string type heat exchanger
Technical field
The present invention relates to the heat exchanger technical field, relate in particular to a kind of fin of sheet string type heat exchanger.
Background technology
As shown in Figure 7 and Figure 8, the fin of existing sheet string type heat exchanger is to be provided with some pores on each fin, is provided with the pore flange in pore one side.Wherein, the shape of fin has a significant impact the heat exchange performance tool of heat exchanger.At present, generally the fin form of Cai Yonging has flat shape, and MEDIA FLOW is out-of-date to form laminar flow layer along fin surface, can not form the better turbulent layer of heat-transfer effect, and the surface coefficient of heat transfer of fin is lower, and heat exchange effect is relatively poor.
Summary of the invention
Technical problem to be solved by this invention provides a kind of fin of simple in structure, sheet string type heat exchanger that heat exchange efficiency significantly improves.
For solving the problems of the technologies described above, technical scheme of the present invention is: the fin of sheet string type heat exchanger, comprise fin body, described fin body is provided with the pore to fin body one side flanging, described fin body between the described pore is provided with the first disturbance projection, and the side of the described first disturbance projection is provided with the otch that is communicated with described fin body both sides.
As optimized technical scheme, the described first disturbance projection is towards the flange direction of pore, and the height of the described first disturbance projection is equal to or less than the height of pore flange.
As to improvement of the technical scheme, the described first disturbance projection is the bucking ladder shape
As to further improvement in the technical proposal, the periphery of described pore is provided with the second disturbance projection, and the side of the described second disturbance projection is provided with the otch that is communicated with described fin body both sides.
As to further improvement in the technical proposal, the described second disturbance projection is towards the flange direction of pore, and the height of the described second disturbance projection is equal to or less than the height of pore flange.
As to further improvement in the technical proposal, the described second disturbance projection is curved.
As to further improvement in the technical proposal, the edge of described fin body is provided with the corrugated bending.
Owing to adopted technique scheme, described fin body between the described pore is provided with the first disturbance projection, not only improved the rigidity of described fin body, and the medium on the described fin body surface of flowing through played the flow-disturbing effect, turbulent flow heat transfer has appearred, thereby the surface coefficient of heat transfer of fin is improved greatly, but formed a large amount of medium eddying turbulence groups simultaneously, increased the pressure loss when medium passes through core body; But the side of the described first disturbance projection is provided with the otch that is communicated with described fin body both sides, makes the part medium enter described fin body opposite side by otch, has then solved the technical barrier of eddying turbulence group, and the heat exchange efficiency of fin is further improved.
Description of drawings
Fig. 1 is the structural representation of the embodiment of the invention one;
Fig. 2 is the vertical view of Fig. 1, shows the corrugated bending at fin body edge;
Fig. 3 be the A-A of Fig. 1 to view, show the structure of the first disturbance projection;
The B-B of Fig. 4 Fig. 1 shows the otch of the first disturbance projection to view;
The structural representation of Fig. 5 embodiment of the invention two;
The C-C of Fig. 6 Fig. 1 shows the structure of the second disturbance projection to view;
Fig. 7 is the structural representation of background technology fin;
Fig. 8 is that the D-D of Fig. 7 is to view.
The specific embodiment
Embodiment one:
As shown in Figure 1, the fin of sheet string type heat exchanger, comprise fin body 1, described fin body is provided with the pore 2 to a side flanging of fin body 1, described fin body 1 between the described pore 2 is provided with the first disturbance projection 3, the side of the described first disturbance projection 3 is provided with the otch 31 of the both sides that are communicated with described fin body 1, in the present embodiment, each described first disturbance projection 3 has two otch 31, and otch 31 is separately positioned on the media flow direction, reduced the generation of eddying turbulence group.
As shown in Figure 3, the described first disturbance projection 3 is towards the flange direction of pore 2, and the height of the described first disturbance projection 3 further reduces the resistance that medium passes through less than the height of pore flange 21, thereby improves the heat exchange efficiency of fin.
As shown in Figure 4, the described first disturbance projection 3 is the bucking ladder shape, has improved the manufacturability of present embodiment and the rigidity of fin; As can be seen from Figure 2, the edge of described fin body 1 is provided with corrugated bending 4, makes the medium of turnover fin that turbulent flow take place, thereby as improving replenishing of heat exchange efficiency of fins.
Embodiment two:
Present embodiment and embodiment one are basic identical, and difference is: the periphery of described pore 2 is provided with the second disturbance projection 5, and the side of the described second disturbance projection 5 is provided with the otch 51 that is communicated with described fin body 1 both sides.
The described second disturbance projection 5 is towards the flange direction of pore 2, and the height of the described second disturbance projection 5 is less than the height of pore flange 21.
In the present embodiment, described second disturbance projection 5 is curved, around described pore 2 uniform settings.
Present embodiment has strengthened the intensity of pore on the one hand, prevents the damage of fin in fin serial connection technical process, has further strengthened the generation of medium turbulent flow simultaneously, and the heat exchange efficiency of fin is improved greatly.
More than only be for example to best mode for carrying out the invention for example, protection scope of the present invention is as the criterion with the content of claim, any equivalence techniques conversion of making based on technical clarification of the present invention all should be within protection scope of the present invention.
The present invention can be widely used in the technical field of heat exchangers such as the charge air cooler, oil cooler of engine, and the raising of heat exchange efficiency can significantly reduce the volume of heat exchanger, thereby has significantly reduced the use of material, has technique effect significantly.

Claims (7)

1. the fin of sheet string type heat exchanger, comprise fin body, described fin body is provided with the pore to fin body one side flanging, it is characterized in that: the described fin body between the described pore is provided with the first disturbance projection, and the side of the described first disturbance projection is provided with the otch that is communicated with described fin body both sides.
2. the fin of sheet string type heat exchanger as claimed in claim 1 is characterized in that: the described first disturbance projection is towards the flange direction of pore, and the height of the described first disturbance projection is equal to or less than the height of pore flange.
3. the fin of sheet string type heat exchanger as claimed in claim 1 is characterized in that: the described first disturbance projection is the bucking ladder shape.
4. as the fin of claim 1,2 or 3 described sheet string type heat exchangers, it is characterized in that: the periphery of described pore is provided with the second disturbance projection, and the side of the described second disturbance projection is provided with the otch that is communicated with described fin body both sides.
5. the fin of sheet string type heat exchanger as claimed in claim 4 is characterized in that: the described second disturbance projection is towards the flange direction of pore, and the height of the described second disturbance projection is equal to or less than the height of pore flange.
6. the fin of sheet string type heat exchanger as claimed in claim 5 is characterized in that: the described second disturbance projection is curved.
7. the fin of sheet string type heat exchanger as claimed in claim 6 is characterized in that: the edge of described fin body is provided with the corrugated bending.
CN200910020384A 2009-04-23 2009-04-23 Fins for serial fin type heat exchanger Pending CN101539384A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200910020384A CN101539384A (en) 2009-04-23 2009-04-23 Fins for serial fin type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200910020384A CN101539384A (en) 2009-04-23 2009-04-23 Fins for serial fin type heat exchanger

Publications (1)

Publication Number Publication Date
CN101539384A true CN101539384A (en) 2009-09-23

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN200910020384A Pending CN101539384A (en) 2009-04-23 2009-04-23 Fins for serial fin type heat exchanger

Country Status (1)

Country Link
CN (1) CN101539384A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102162705A (en) * 2011-03-25 2011-08-24 兰州交通大学 Combined curved-surface vortex generator-type round fin-tube heat exchanger
CN104329977A (en) * 2014-10-27 2015-02-04 浙江开尔新材料股份有限公司 Rotary air preheater heat transfer corrugated plate with interrupted holes and processing method for rotary air preheater heat transfer corrugated plate
CN104979308A (en) * 2015-07-14 2015-10-14 哈尔滨精方电力设备科技有限公司 High-efficiency cooling sheet
CN106152854A (en) * 2015-03-31 2016-11-23 丹佛斯微通道换热器(嘉兴)有限公司 Fin and heat exchanger
CN106679484A (en) * 2017-03-02 2017-05-17 珠海格力电器股份有限公司 Fin, heat exchanger and air-conditioner

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102162705A (en) * 2011-03-25 2011-08-24 兰州交通大学 Combined curved-surface vortex generator-type round fin-tube heat exchanger
CN102162705B (en) * 2011-03-25 2012-08-15 兰州交通大学 Combined curved-surface vortex generator-type round fin-tube heat exchanger
CN104329977A (en) * 2014-10-27 2015-02-04 浙江开尔新材料股份有限公司 Rotary air preheater heat transfer corrugated plate with interrupted holes and processing method for rotary air preheater heat transfer corrugated plate
CN104329977B (en) * 2014-10-27 2016-04-13 浙江开尔新材料股份有限公司 Rotary regenerative air preheater heat transfer corrugated plating with flow-disturbing hole and processing method thereof
CN106152854A (en) * 2015-03-31 2016-11-23 丹佛斯微通道换热器(嘉兴)有限公司 Fin and heat exchanger
CN106152854B (en) * 2015-03-31 2018-11-30 丹佛斯微通道换热器(嘉兴)有限公司 Fin and heat exchanger
CN104979308A (en) * 2015-07-14 2015-10-14 哈尔滨精方电力设备科技有限公司 High-efficiency cooling sheet
CN106679484A (en) * 2017-03-02 2017-05-17 珠海格力电器股份有限公司 Fin, heat exchanger and air-conditioner

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Open date: 20090923