CN107906998A - A kind of high-performance condensing heat-exchanging pipe based on biomimetic features - Google Patents
A kind of high-performance condensing heat-exchanging pipe based on biomimetic features Download PDFInfo
- Publication number
- CN107906998A CN107906998A CN201711021902.3A CN201711021902A CN107906998A CN 107906998 A CN107906998 A CN 107906998A CN 201711021902 A CN201711021902 A CN 201711021902A CN 107906998 A CN107906998 A CN 107906998A
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- China
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- biomimetic features
- exchanging pipe
- condensing heat
- heat
- hydrophobic
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Links
- 230000003592 biomimetic effect Effects 0.000 title claims abstract description 44
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 28
- 230000003075 superhydrophobic effect Effects 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 7
- 238000009826 distribution Methods 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 238000009833 condensation Methods 0.000 abstract description 26
- 230000005494 condensation Effects 0.000 abstract description 26
- 239000007788 liquid Substances 0.000 abstract description 11
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000000889 atomisation Methods 0.000 abstract 1
- 238000001694 spray drying Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 239000011049 pearl Substances 0.000 description 10
- 230000008569 process Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 241000219357 Cactaceae Species 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002086 nanomaterial Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
Landscapes
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Geometry (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of high-performance condensing heat-exchanging pipe based on biomimetic features, is a kind of high-performance condensing heat-exchanging pipe based on biomimetic features, for draining vapor or organic vapor high-efficiency condensation and in time condensate liquid.The condensing heat-exchanging pipe includes the heat exchanger tube base tube (1) with hydrophobic micro-channel structure, the super hydrophobic base (2) being arranged on heat exchanger tube base tube (1) surface, the hydrophobic micro-channel structure (4) being distributed in the super hydrophobic base (2) and the needle-shaped hydrophilic biomimetic features (3) being distributed on the hydrophobic micro-channel structure (4).The heat exchanger tube base tube handled by the spray drying technology based on ultrasonic atomization effectively improves the surface property of material, reduces surface energy, and more stable pearl condensation is formed in heat exchange pipe surface;The liquid pearl that the hydrophobic micro-channel of distribution on the condensation surfaces can will be moved to the needle-shaped hydrophilic biomimetic features root guides in time, ensures being smoothed out for condensation cycle.
Description
Technical field
The present invention relates to a kind of high-efficiency condensation heat exchanger tube for being widely used in the fields such as the energy, electronics, refrigeration, and in particular to
Be a kind of to improve the high-performance condensing heat-exchanging pipe based on biomimetic features that designs of condensing heat-exchange efficiency.
Background technology
Steam condensation heat transfer process is widely present in the industrial circles such as the energy, chemical industry, refrigeration, and steam condensation can produce big
Latent heat is measured, therefore the recycling of latent heat is particularly significant for energy-saving and emission-reduction.In refrigeration industry, using the condensation of condensation efficiency higher
Device can reduce condenser area, save material.In addition, when in steam there are during incoagulable gas, can liquid film or drop with
One layer of air film is formed between mixed gas so that resistance to mass tranfer is added between steam and gas-liquid interface or condenser wall, sternly
Condensing heat-exchange performance is weakened again.In conclusion condensation efficiency is improved, the heat in high efficiente callback steam condensation process, to me
State's industrial expansion and promotion energy-saving and emission-reduction are of great significance.
According to surface of solids microstructure and wetting characteristics, steam condensation can be divided into film condensation and pearl condensation.Pearl
Condensation is a kind of more efficient heat transfer type relative to film condensation, its condensation coefficient improves 1-2 number than film condensation
Magnitude.Heat transfer area can be greatly reduced in the realization of pearl condensation, and very big income is obtained in terms of economy and environment.It is but actual
On, pearl condensation be it is a kind of comprising drop coring, growth, merging, depart from dynamic circulation process, have Analysis On Multi-scale Features and
By multifactor impact.Pearl condenses the surface condition for being largely dependent upon heat exchanger tube, is industrially a kind of relatively difficult to achieve
And unstable condensate form.
Cactus is efficiently catchmented using the super hydrophilic material for the thorn structure for being distributed in stem surface, due to the point of needle-shaped thorn
End section radius is less than root section radius so that droplet is constantly transported under the action of laplace pressure difference to bore spine root
It is dynamic.After droplet is assembled in root, transmitted along the backbone groove with hydrophobic wax top layer, and assemble other droplets by its band
Walk, so as to complete a circulation of catchmenting.
Exchange tube surface is using one of major technique that process for treating surface is raising condensing heat-exchange efficiency, generally use
Pod road adds the modes such as low rib to increase heat exchange area, while condensation water is more easily discharged under the action of surface tension,
The thickness of condensate film is reduced, so as to achieve the purpose that to strengthen condensing heat-exchange.But the condensing mode that above method is realized is equal
For film condensation, condensate film is attached to one thermal resistance of formation on tube wall so that the gas for needing to condense can not direct contacting pipe
Wall, causes cooling energy recovery still relatively low, and the room for promotion for strengthening condensing heat-exchange is limited.
The content of the invention
Technical problem:The technical problem to be solved by the present invention is to solve the above shortcomings of the prior art and to provide one kind
High-performance condensing heat-exchanging pipe based on biomimetic features, the heat exchanger tube imitate the water collecting process of cactus, can greatly improve condensation and change
Hot coefficient, achievees the purpose that high efficient heat exchanging, while enhances the stability of heat exchange structure, improves industrial promotion price
Value.
Technical solution
Technical solution:To achieve the above object, a kind of high-performance condensing heat-exchanging pipe based on biomimetic features of the invention is adopted
Technical solution:The condensing heat-exchanging pipe includes the heat exchanger tube base tube with hydrophobic micro-channel structure, is arranged on heat exchanger tube base tube
Super hydrophobic base on surface, the hydrophobic micro-channel structure being distributed in the super hydrophobic base and is distributed in the hydrophobic microflute
Needle-shaped hydrophilic biomimetic features in road structure.
The cast of the heat exchanger tube base tube is pipe, elliptical tube, rectangular channel, round rectangle passage, drop shaped tube, flat tube
Or porous flat pipe.
The material of the heat exchanger tube base tube is copper, carbon steel, stainless steel, aluminium or nano-porous structure are ceramic.
The equivalent outside diameter of the heat exchanger tube base tube is 2-200mm, internal equivalent diameter 1-200mm.
The heat exchanger tube base tube outer wall has hydrophobic micro-channel structure, and the width of the hydrophobic micro-channel structure is
0.1-10mm, depth 0.1-5mm.
The hydrophobic micro-channel structure is linked together each needle-shaped hydrophilic biomimetic features with certain distribution mode, its point
Mode for cloth depends on the arrangement mode of needle-shaped hydrophilic biomimetic features and the disposing way of condensing heat-exchanging pipe;If condensing heat-exchanging pipe is put
Mode is put to be horizontal, then hydrophobic micro-channel structure should try one's best is distributed along the circumferencial direction of heat exchanger tube base tube;If condensing heat-exchanging pipe
Disposing way is vertical, then hydrophobic micro-channel structure should try one's best axially is distributed along heat exchanger tube base tube.
The super hydrophobic base has micro-nano binary surface texture, and roll angle is less than 6 degree.
The needle-shaped hydrophilic biomimetic features with random unordered or be equally spacedly arranged in super hydrophobic base, wherein, between waiting
It is divided into in-line arrangement and fork two kinds of structures of row away from arrangement, and the spacing of adjacent needle-shaped hydrophilic biomimetic features is 0.5-40mm.
The pipe axle clamp angle beta of the needle-shaped hydrophilic biomimetic features and heat exchanger tube base tube is 0-90 °, length 0.1-30mm.
Beneficial effect:The present invention uses above-mentioned technical proposal, has the following advantages that compared with prior art:
1st, the present invention uses a kind of super hydrophobic base with micro nano structure, its surface has the small spy of rolling resistance
Point, is conducive to drop rolling, and under the conditions of certain vapor flow rate, condensing droplet is easier to come off from heat exchange pipe surface, more has
Beneficial to the exclusion of condensate liquid.
2nd, in the presence of incoagulable gas, the micro nano structure of super hydrophobic base layer captures incoagulable gas, so as to subtract
The small contact area of substrate and liquid, make the surface of solids reduce the viscous force of drop, reaches the obvious heat transfer resistance that reduces
Purpose.
3rd, the present invention uses needle-shaped hydrophilic biomimetic features, and hydrophilic material can improve condensation speed with rapid acquiring vapour molecule
Rate, while its laplace pressure produced shortens the accumulation process of small liquid pearl, and constantly to bore spine root motion.In small liquid pearl
Motion process in accelerate droplet aggregation, very big facilitation is played to condensation process.
4th, heat exchanger tube base tube of the invention has hydrophobic micro-channel structure, can utilize the effect of gravity so that needle-shaped
The liquid pearl of hydrophilic biomimetic features root aggregation glides along groove and assembles other small liquid pearls, shortens liquid pearl and departs from condensing surface
Time, ensures to condense being normally carried out for cyclic process.
Brief description of the drawings
Fig. 1 is the heat exchanger tube table that needle-shaped hydrophilic biomimetic features are equally spacedly distributed in a manner of the row of pitching in super hydrophobic base
Face schematic diagram.
Fig. 2 is that the heat exchanger tube that needle-shaped hydrophilic biomimetic features are equally spacedly distributed in a manner of the row of pitching in super hydrophobic base is horizontal
Schematic cross-section.
Have in figure:Heat exchanger tube base tube 1, super hydrophobic base 2, needle-shaped hydrophilic biomimetic features 3, hydrophobic micro-channel structure 4.
Embodiment
Further described in detail below in conjunction with the accompanying drawings:
As shown in Figure 1, the present invention be with hydrophobic micro-channel heat exchanger tube base tube surface prepare super hydrophobic base and
The needle-shaped hydrophilic biomimetic features being distributed in the super hydrophobic base.It is hydrophilic in condensing heat-exchange pipe surface based on biomimetic features
Property region and super-hydrophobicity region organically combine, needle-shaped hydrophilic biomimetic features are equally spacedly distributed in super-hydrophobic in a manner of the row of pitching
In substrate.Hydrophobic micro-channel structure is closed according to the arrangement mode of needle-shaped hydrophilic biomimetic features and the disposing way of condenser
The distribution of reason.
In addition, needle-shaped hydrophilic biomimetic features can by it is random it is unordered in a manner of or in-line arrangement in the way of be arranged in super hydrophobic base
On.
Above in the arrangement mode of needle-shaped hydrophilic biomimetic features, the pipe axle clamp of needle-shaped hydrophilic biomimetic features and heat exchanger tube base tube
Angle beta is 0-90 °, and length 0.1-30mm, the spacing of adjacent needle-shaped hydrophilic biomimetic features is 0.5-40mm.
The cast of the heat exchanger tube base tube of the present invention is pipe, elliptical tube, rectangular channel, round rectangle passage, drop shaped tube, flat
Pipe or porous flat pipe, the material of heat exchanger tube base tube is that copper, carbon steel, stainless steel, aluminium or nano-porous structure are ceramic, heat exchanger tube base tube
Equivalent outside diameter be 2-200mm, internal equivalent diameter 1-200mm.The width for the hydrophobic micro-channel structure being distributed on heat exchanger tube base tube
Spend for 0.1-10mm, depth 0.1-5mm.
As shown in Fig. 2, when needle-shaped hydrophilic biomimetic features are equally spacedly distributed in super hydrophobic base in a manner of the row of pitching,
As viewed from axial, it can be found that the distribution density of needle-shaped hydrophilic biomimetic features is higher, preferable condensation effect can be reached.
Heat exchanger tube disposing way in figure is horizontal, therefore hydrophobic micro-channel should try one's best and divide along the circumferencial direction of pipe
Cloth;If the disposing way of heat exchanger tube is vertical, hydrophobic micro-channel should try one's best axially to be distributed along pipe.Ensure condensing droplet energy
Drain glibly under the effect of gravity.
Claims (9)
1. a kind of high-performance condensing heat-exchanging pipe based on biomimetic features, it is characterised in that the condensing heat-exchanging pipe is included with hydrophobic
The heat exchanger tube base tube (1) of micro-channel structure, the super hydrophobic base (2) being arranged on heat exchanger tube base tube (1) surface, is distributed in described
Hydrophobic micro-channel structure (4) in super hydrophobic base (2) and it is distributed in needle-shaped hydrophilic imitative on the hydrophobic micro-channel structure (4)
Raw structure (3).
2. the high-performance condensing heat-exchanging pipe according to claim 1 based on biomimetic features, it is characterised in that the heat exchange
The cast of pipe base tube (1) is pipe, elliptical tube, rectangular channel, round rectangle passage, drop shaped tube, flat tube or porous flat pipe.
3. the high-performance condensing heat-exchanging pipe according to claim 1 or 2 based on biomimetic features, it is characterised in that described
The material of heat exchanger tube base tube (1) is copper, carbon steel, stainless steel, aluminium or nano-porous structure are ceramic.
4. the high-performance condensing heat-exchanging pipe according to claim 3 based on biomimetic features, it is characterised in that the heat exchange
The equivalent outside diameter of pipe base tube (1) is 2-200mm, internal equivalent diameter 1-200mm.
5. the high-performance condensing heat-exchanging pipe according to claim 4 based on biomimetic features, it is characterised in that the heat exchange
Pipe base tube (1) outer wall has hydrophobic micro-channel structure (4), and the width of the hydrophobic micro-channel structure (4) is 0.1-10mm, deep
Spend for 0.1-5mm.
6. the high-performance condensing heat-exchanging pipe according to claim 5 based on biomimetic features, it is characterised in that described hydrophobic micro-
Channel structure (4) is linked together each needle-shaped hydrophilic biomimetic features (3) with certain distribution mode, its distribution mode depends on
The arrangement mode of needle-shaped hydrophilic biomimetic features (3) and the disposing way of condensing heat-exchanging pipe;If condensing heat-exchanging pipe disposing way is
Horizontal, then hydrophobic micro-channel structure (4) should be tried one's best is distributed along the circumferencial direction of heat exchanger tube base tube (1);If condensing heat-exchanging pipe is put
Mode is put to be vertical, then hydrophobic micro-channel structure (4) should be tried one's best axially is distributed along heat exchanger tube base tube (1).
7. the high-performance condensing heat-exchanging pipe according to claim 1 based on biomimetic features, it is characterised in that described is super thin
Water base bottom (2) has micro-nano binary surface texture, and roll angle is less than 6 degree.
8. the high-performance condensing heat-exchanging pipe according to claim 6 based on biomimetic features, it is characterised in that the needle-shaped parent
Water biomimetic features (3) with random unordered or be equally spacedly arranged in super hydrophobic base (2), wherein, equidistantly arrangement is divided into suitable
Row and fork two kinds of structures of row, and the spacing of adjacent needle-shaped hydrophilic biomimetic features (3) is 0.5-40mm.
9. the high-performance condensing heat-exchanging pipe according to claim 8 based on biomimetic features, it is characterised in that the needle-shaped parent
The pipe axle clamp angle beta of water biomimetic features (3) and heat exchanger tube base tube (1) is 0-90 °, length 0.1-30mm.
Priority Applications (1)
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CN201711021902.3A CN107906998B (en) | 2017-10-27 | 2017-10-27 | High-performance condensation heat exchange tube based on bionic structure |
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CN201711021902.3A CN107906998B (en) | 2017-10-27 | 2017-10-27 | High-performance condensation heat exchange tube based on bionic structure |
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CN107906998A true CN107906998A (en) | 2018-04-13 |
CN107906998B CN107906998B (en) | 2020-05-19 |
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Cited By (14)
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CN108844261A (en) * | 2018-05-21 | 2018-11-20 | 哈尔滨工业大学 | A kind of fiber tube composite construction for inner surface evaporative condenser |
CN109059604A (en) * | 2018-06-15 | 2018-12-21 | 上海交通大学 | A kind of unstable wave intensified condenser tube and production method based on close and distant water spacer |
CN109099540A (en) * | 2018-06-14 | 2018-12-28 | 东南大学 | A kind of radiation appliance reducing indoor air humidity |
CN109612291A (en) * | 2019-01-26 | 2019-04-12 | 广州航海学院 | Strengthen the apparatus and method of condensing heat-exchange |
CN109707004A (en) * | 2019-01-18 | 2019-05-03 | 长春理工大学 | Biomimetic features with mist capacity gauge |
CN109855438A (en) * | 2019-03-27 | 2019-06-07 | 常州大学 | High-performance flexible cryosurface and preparation method thereof based on carbon nanomaterial film |
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CN111207618A (en) * | 2020-01-15 | 2020-05-29 | 郑州轻工业大学 | Boiling enhanced heat exchange tube with inserted bionic enhanced cone |
CN111530220A (en) * | 2020-04-30 | 2020-08-14 | 南京碳环生物质能源有限公司 | Condensation treatment method and device for removing siloxane component in biomass gas |
CN111549856A (en) * | 2020-04-02 | 2020-08-18 | 天津大学 | Self-driven planarization mist liquid drop directional collection structure |
CN111964503A (en) * | 2020-08-26 | 2020-11-20 | 南京航空航天大学 | Three-dimensional patterned surface for enhancing dropwise condensation |
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CN102538542A (en) * | 2011-12-30 | 2012-07-04 | 西安交通大学 | Flue gas condensation-type heat transfer pipe with bionic structure |
CN103359684A (en) * | 2013-06-26 | 2013-10-23 | 西安交通大学 | Hydrophobic surface, preparation method and application thereof in dropwise condensation heat transfer |
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CN106892399A (en) * | 2015-12-21 | 2017-06-27 | 华中科技大学 | A kind of bionical moisture condensation and collection structure and preparation method thereof |
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CN102538542A (en) * | 2011-12-30 | 2012-07-04 | 西安交通大学 | Flue gas condensation-type heat transfer pipe with bionic structure |
CN103359684A (en) * | 2013-06-26 | 2013-10-23 | 西安交通大学 | Hydrophobic surface, preparation method and application thereof in dropwise condensation heat transfer |
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CN108844261A (en) * | 2018-05-21 | 2018-11-20 | 哈尔滨工业大学 | A kind of fiber tube composite construction for inner surface evaporative condenser |
CN109099540A (en) * | 2018-06-14 | 2018-12-28 | 东南大学 | A kind of radiation appliance reducing indoor air humidity |
CN109059604A (en) * | 2018-06-15 | 2018-12-21 | 上海交通大学 | A kind of unstable wave intensified condenser tube and production method based on close and distant water spacer |
CN109707004A (en) * | 2019-01-18 | 2019-05-03 | 长春理工大学 | Biomimetic features with mist capacity gauge |
CN109612291A (en) * | 2019-01-26 | 2019-04-12 | 广州航海学院 | Strengthen the apparatus and method of condensing heat-exchange |
CN109855438A (en) * | 2019-03-27 | 2019-06-07 | 常州大学 | High-performance flexible cryosurface and preparation method thereof based on carbon nanomaterial film |
CN110943265B (en) * | 2019-05-07 | 2024-04-26 | 吉林大学 | Preparation of battery thermal management device coupled with novel bionic heat pipe and bidirectional heat flow control method |
CN110943265A (en) * | 2019-05-07 | 2020-03-31 | 吉林大学 | Preparation and bidirectional heat flow control method of battery heat management device coupled with novel bionic heat pipe |
CN110552397A (en) * | 2019-08-06 | 2019-12-10 | 天津大学 | Functional interface for capturing and directionally collecting mist droplets in self-driven manner |
CN111207618A (en) * | 2020-01-15 | 2020-05-29 | 郑州轻工业大学 | Boiling enhanced heat exchange tube with inserted bionic enhanced cone |
CN111549856A (en) * | 2020-04-02 | 2020-08-18 | 天津大学 | Self-driven planarization mist liquid drop directional collection structure |
CN111530220A (en) * | 2020-04-30 | 2020-08-14 | 南京碳环生物质能源有限公司 | Condensation treatment method and device for removing siloxane component in biomass gas |
CN112144608A (en) * | 2020-08-12 | 2020-12-29 | 江苏大学 | Bionic blade integrating self-transportation and permeation of water absorption |
CN112144608B (en) * | 2020-08-12 | 2021-11-23 | 江苏大学 | Bionic blade integrating self-transportation and permeation of water absorption |
CN111964503A (en) * | 2020-08-26 | 2020-11-20 | 南京航空航天大学 | Three-dimensional patterned surface for enhancing dropwise condensation |
CN111964503B (en) * | 2020-08-26 | 2022-03-25 | 南京航空航天大学 | Three-dimensional patterned surface for enhancing dropwise condensation |
CN115060087A (en) * | 2022-03-10 | 2022-09-16 | 华南理工大学 | Heat exchange surface capable of quickly removing condensed liquid drops and preparation method and application thereof |
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