CN206410586U - A kind of efficient heat conducting tube of inner surface enhanced type - Google Patents
A kind of efficient heat conducting tube of inner surface enhanced type Download PDFInfo
- Publication number
- CN206410586U CN206410586U CN201621400049.7U CN201621400049U CN206410586U CN 206410586 U CN206410586 U CN 206410586U CN 201621400049 U CN201621400049 U CN 201621400049U CN 206410586 U CN206410586 U CN 206410586U
- Authority
- CN
- China
- Prior art keywords
- heat conducting
- efficient heat
- conducting tube
- surface enhanced
- enhanced type
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a kind of efficient heat conducting tube of inner surface enhanced type, the radial direction extension along the body of material including body and on the body and the body inner surface around body helically state extension the internal thread rib being integrally constituted with the body, the groove along the internal-rib bearing of trend interval shape distribution is provided with the top of the internal thread rib, in the bottom of the groove provided with the channel structure intersected and be interconnected.The utility model can significantly increase the area on intraductal heat exchange surface;Improve tube fluid flow regime simultaneously, destroy the boundary layer of flow surface, making the turbulence level of fluid further increases, to reduce heat transfer resistance.
Description
Technical field
The heat-exchange tube technical field that the utility model belongs in air-conditioning, refrigeration system, and in particular to a kind of inner surface is strong
The efficient heat conducting tube of change, it is adaptable to evaporate the heat-transfer pipe that the intraductal heat exchange performance of operating mode or condensing condition is strengthened.
Background technology
The heat exchange tube inner structure of evaporator or condensation in prior art is typically:It is machined and in body
Along the length direction helical form internal-rib that spirally state is constituted and is integrally constituted with body of body on inwall.This band
The heat exchanger tube for having internal-rib can make the fluid formation turbulent condition in pipe, effectively improve the coefficient of heat transfer in pipe, improve evaporation or
Condensation heat transfer performance.
However, currently available technology patents and patent applicationss scheme is due to only in the inner wall surface processing spiral of body
Rib, does not form three-dimensional internal rib formations, and only the two-dimensional shapes such as internal-rib height, size and fat or thin degree are provided.When reinforcing is passed
When strengthening insufficient outside heating pipe, i.e., in the case that intraductal heat exchange performance is the heat transfer bottleneck of heat-transfer pipe complex heat transfer performance, this
Plant structure has augmentation of heat transfer effect to tube fluid heat convection.But with the development of efficient heat conducting tube pipe peri-procedural techniques,
Heat transfer outside a tube performance has no longer been heat transfer bottleneck, reviews the process technology in pipe and does not obtain very big development in recent years, because
The augmentation of heat transfer effect of this original two-dimentional screw thread internal rib formations can not reach gratifying effect, and such case is necessary
Improved.
The content of the invention
Task of the present utility model is that providing one kind not only contributes to significantly increase intraductal heat exchange surface area but also be conducive to changing
Kind tube fluid flow regime, destroys the boundary layer of flow surface, making the turbulence level of fluid further increases, to reduce heat transfer
The efficient heat conducting tube of thermal resistance.In the evaporator or condenser of the applicable Large Central Air Conditioning System water chiller of this heat-transfer pipe.
What task of the present utility model was performed by, a kind of efficient heat conducting tube of inner surface enhanced type, including body
And the material on the body along the body radial direction extension and the body inner surface around body
Helically the internal thread rib being integrally constituted with the body of state extension, edge is provided with the top of the internal thread rib
The groove of the internal-rib bearing of trend interval shape distribution.
Further, in the bottom of the groove provided with the channel structure intersected and be interconnected.
Further, the height of the internal thread rib is 0.1 ㎜ -1.0 ㎜ and/or quantity is 8-75 bars and/or spiral
10 ° -70 ° of angle.
Further, the depth and/or width of the groove are 0.05 ㎜ -0.5 ㎜.
Further, the helical angle and the angle of the groove of the internal thread rib are at an acute angle.
Further, the depth and/or width of the channel structure are 0.01 ㎜ -0.2 ㎜.
Further, the depth and width of the channel structure of two intersections are equal or unequal.
Further, the angle of the channel structure of two intersections is acute angle or right angle.
Further, it is additionally provided with the outer surface of body integral and radial direction of along body extends with body
Helically state three-dimensional or multidimensional outer fin.
Further, the height of the outer fin is 0.5 ㎜ -1.5 ㎜, and outer fin pitch is 0.3 ㎜ -1 ㎜.
Beneficial effect:Compared with prior art, it has the advantages that the utility model:
The efficient heat conducting tube of the utility model inner surface enhanced type is due to the top of the internal thread rib in heat transfer pipe internal surface
The reinforcing unit that there is the channel structure for intersecting connected state to constitute by groove and bottom portion of groove is devised, thus can be shown
Write the area on increase intraductal heat exchange surface;Be conducive to improving tube fluid flow regime using this structure simultaneously, destroy fluid
The boundary layer on surface, making the turbulence level of fluid further increases, to reduce heat transfer resistance;The outer surface of body has simultaneously
The outer fin of three-dimensional or multidimensional also greatly improves heat transfer outside a tube effect.
Brief description of the drawings
The utility model is described in detail below by drawings and Examples.But the utility model is not limited to the present embodiment.
Fig. 1 is dimensional structure diagram of the present utility model.
Fig. 2 is inner surface of tube body expanded schematic diagram of the present utility model shown in Fig. 1.
Embodiment
A kind of efficient heat conducting tube of inner surface enhanced type, including body 1 and material on body 1 are along body 1
Radial direction extends and around body, helically state extension is integrally constituted with body 1 in the inner surface of body 1
Internal thread rib 2.It is preferred that, the quantity of the internal thread rib 2 is 8-75 bars, 10 ° -70 ° of spiral angle.
The groove 21 along the internal-rib bearing of trend interval shape distribution is provided with the top of internal thread rib 2, in the groove
21 bottom, which has, to intersect and interconnected channel structure 211.The helical angle of the internal thread rib 2 and the internal thread rib
The angle for the groove 21 that 2 top is distributed with interval shape is at an acute angle.The depth and width for two channel structures 211 intersected can phase
Deng or it is unequal, its angle is acute angle or right angle.
The utility model is because the top design of the internal thread rib 2 in heat transfer pipe internal surface is by groove 21 and groove 21
The reinforcing unit of the composition of channel structure 211 with intersection connected state of bottom, thus intraductal heat exchange table can be significantly increased
The area in face;Due to there is internal thread rib 2 in inside pipe wall, not only internal surface area is considerably increased compared to slippery inner surface while can
Change the mode of flow of fluid, making fluid, helically line flows along body direction, and fluid is in turbulent condition, strengthens heat convection
Effect.Fluid during fluid interchange fluid flow direction part, when fluid motion to the bottom of a certain laminated rib, fluid
Just have a flowing to climb and cross the process of internal thread rib, this process can be such that fluid fully contacts with tube wall, but simultaneously
The flow resistance of fluid can be increased, therefore, in order to reach suitable flow resistance, the internal thread rib 2 of the present utility model
Highly it is 0.1 ㎜ -1.0 ㎜.
Due to the effect of the structure of groove 21 on the internal thread rib 2, fluid can change side local flow direction, this mistake
Journey destroys the boundary layer of fluid, is conducive to fluid fully to be contacted with groove surfaces, increases local convection heat transfer effect.Flow part
Body, which climbs, will smoothly flow to after certain altitude and by groove, while increase Local Heat Transfer, the resistance of flow of fluid also by
Suitably reduce, if in the case that heat exchanger tube is large number of in set heat exchange device, for reducing unit water resistance, reducing water
Pump work consumption is highly beneficial.In the bottom of groove 21 there is the channel structure 211 intersected and be interconnected can also increase simultaneously
Part heat exchange surface area and the boundary layer for flowing local failure fluid, further increase tube fluid heat convection effect.For
Reach in rational circulation and the contact area and less flow resistance of groove, the present embodiment, the depth of groove 21 is
0.05 ㎜ -0.5 ㎜, width is 0.05 ㎜ -0.5 ㎜;The depth of channel structure 211 be 0.01 ㎜ -0.2 ㎜, width be 0.01 ㎜ -
0.2㎜。
The utility model be additionally included in body 1 outer surface have with body 1 it is integral and along the radius side of body 1
To the three-dimensional or the outer fin 3 of multidimensional for extending helically state, the height of the outer fin 3 is 0.5 ㎜ -1.5 ㎜, outer fin pitch
For 0.3 ㎜ -1 ㎜.
The three-dimensional or the outer fin 3 of multidimensional that the outer surface of body 1 has have larger benefit for lifting heat transfer outside a tube.
After condenser uses such heat-transfer pipe, the three-dimensional and multidimensional structure of outer fin 3 can be generally processed into as reinforcing condensation effect
Zigzag, these structures for reinforcing condensing heat-exchange it is highly beneficial, while can also increase the heat exchange surface area outside pipe, enhanced tube
Outer heat transfer effect.After evaporator uses such heat-transfer pipe, the three-dimensional and multidimensional structure of outer fin 3 can generally be processed into phase interaction
With interconnected opening structure, these structures exchange heat highly beneficial for reinforcing explosive evaporation.
Embodiment described above is only that preferred embodiment of the present utility model is described, not to this practicality
New spirit and scope are defined.On the premise of the utility model design concept is not departed from, this area ordinary person couple
The all variations and modifications that the technical solution of the utility model is made, all should drop into protection domain of the present utility model, this reality
With new claimed technology contents, all record in detail in the claims.
Claims (10)
1. a kind of efficient heat conducting tube of inner surface enhanced type, including body(1)And by the body(1)On material along institute
State body(1)Radial direction extension and in the body(1)Inner surface around body helically state extension with
The body(1)The internal thread rib being integrally constituted(2), it is characterised in that:In the internal thread rib(2)Top be provided with along
The groove of the internal-rib bearing of trend interval shape distribution(21).
2. the efficient heat conducting tube of inner surface enhanced type according to claim 1, it is characterised in that:In the groove(21)'s
Bottom is provided with the channel structure intersected and be interconnected(211).
3. the efficient heat conducting tube of inner surface enhanced type according to claim 1, it is characterised in that:The internal thread rib(2)
Height be 0.1 ㎜ -1.0 ㎜ and/or quantity is 10 ° -70 ° of 8-75 bars and/or spiral angle.
4. a kind of efficient heat conducting tube of inner surface enhanced type according to claim 1, it is characterised in that:The groove(21)
Depth and/or width be 0.05 ㎜ -0.5 ㎜.
5. the efficient heat conducting tube of the inner surface enhanced type according to any one of Claims 1-4, it is characterised in that:In described
Screw thread rib(2)Helical angle and the groove(21)Angle it is at an acute angle.
6. the efficient heat conducting tube of inner surface enhanced type according to claim 2, it is characterised in that:The channel structure
(211)Depth and/or width be 0.01 ㎜ -0.2 ㎜.
7. the efficient heat conducting tube of inner surface enhanced type according to claim 2, it is characterised in that:The groove of two intersections
Road structure(211)Depth and width it is equal or unequal.
8. the efficient heat conducting tube of inner surface enhanced type according to claim 2, it is characterised in that:The groove of two intersections
Road structure(211)Angle be acute angle or right angle.
9. the efficient heat conducting tube of inner surface enhanced type according to claim 1, it is characterised in that:In body(1)Appearance
Face is additionally provided with and body(1)It is integral and along body(1)Radial direction extension helically state three-dimensional or multidimensional
Outer fin(3).
10. the efficient heat conducting tube of inner surface enhanced type according to claim 9, it is characterised in that:The outer fin(3)Height
Spend for 0.5 ㎜ -1.5 ㎜, outer fin pitch is 0.3 ㎜ -1 ㎜.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621400049.7U CN206410586U (en) | 2016-12-20 | 2016-12-20 | A kind of efficient heat conducting tube of inner surface enhanced type |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621400049.7U CN206410586U (en) | 2016-12-20 | 2016-12-20 | A kind of efficient heat conducting tube of inner surface enhanced type |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206410586U true CN206410586U (en) | 2017-08-15 |
Family
ID=59549661
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621400049.7U Expired - Fee Related CN206410586U (en) | 2016-12-20 | 2016-12-20 | A kind of efficient heat conducting tube of inner surface enhanced type |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206410586U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106767099A (en) * | 2016-12-20 | 2017-05-31 | 江苏萃隆精密铜管股份有限公司 | A kind of efficient heat conducting tube of inner surface enhanced type |
-
2016
- 2016-12-20 CN CN201621400049.7U patent/CN206410586U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106767099A (en) * | 2016-12-20 | 2017-05-31 | 江苏萃隆精密铜管股份有限公司 | A kind of efficient heat conducting tube of inner surface enhanced type |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101532798B (en) | Reinforced heat transfer element of truncated cylindrical surface wing type vortex generator | |
WO2017101235A1 (en) | Enhanced high-efficiency spiral tube heat exchanger | |
CN201034436Y (en) | Dual-reinforced evaporating heat transfer tube | |
CN103063072A (en) | Heat-exchange tube | |
CN203100513U (en) | Heat-exchanger tube | |
CN104870926B (en) | Evaporation heat transfer pipe with hollow cavity | |
CN206410586U (en) | A kind of efficient heat conducting tube of inner surface enhanced type | |
CN103791754A (en) | Efficient heat exchange tube used for condenser | |
CN104903673A (en) | Evaporation heat transfer tube | |
CN107990778A (en) | Efficient inner screw thread copper pipe | |
CN107091587B (en) | Heat exchange device based on graphene heat exchange tube-wet curtain paper | |
CN207797862U (en) | Efficient inner screw thread copper pipe | |
CN106767099A (en) | A kind of efficient heat conducting tube of inner surface enhanced type | |
CN102997740A (en) | Novel reinforced tube for boiling and heat exchange in tube | |
CN106643262A (en) | Efficient heat transfer pipe with evaporating function and condensing function | |
CN206410589U (en) | A kind of efficient heat conducting tube of evaporative condenser Jian Gu Xing | |
CN203534300U (en) | Gravity assisted heat pipe with spiral groove | |
CN203037125U (en) | Double-sided reinforced heat exchange tube | |
CN203687732U (en) | Efficient heat exchange tube for condenser | |
CN102735089A (en) | Heat transfer pipe, and heat and mass transfer equipment having heat transfer pipe | |
CN205580277U (en) | Discontinuous outer trapezoidal ribbed pipe of indulging | |
CN201138153Y (en) | Heat exchanging tube for condenser | |
CN209068809U (en) | A kind of new-type full-liquid type evaporating heat-exchanging pipe | |
CN203310170U (en) | Evaporative condenser | |
CN202329345U (en) | Novel strengthening pipe for boiling heat exchange in duct |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170815 Termination date: 20201220 |