CN108362150B - A kind of loop circuit heat pipe and its heat-exchanger rig of via area height change - Google Patents
A kind of loop circuit heat pipe and its heat-exchanger rig of via area height change Download PDFInfo
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- CN108362150B CN108362150B CN201810246205.6A CN201810246205A CN108362150B CN 108362150 B CN108362150 B CN 108362150B CN 201810246205 A CN201810246205 A CN 201810246205A CN 108362150 B CN108362150 B CN 108362150B
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- air
- heat pipe
- pipeline
- loop circuit
- evaporation ends
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/04—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with tubes having a capillary structure
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/10—Geothermal energy
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- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
Abstract
The present invention provides a kind of anti-gravity loop circuit heat pipes, the heat pipe includes evaporation ends and condensation end, the evaporation ends are located at condensation end top, described evaporation ends a part was arranged in the fluid ascent stage, in at least part of the evaporation ends of fluid ascent stage, capillary wick is set, capillary wick center setting condensation end flows to the pipeline of evaporation ends, the pipeline is flexible pipe, through-hole is set on the pipeline tube wall, pipeline between through-hole and capillary wick by being connected to, along on height ascent direction, the diameter of the through-hole is increasing.The present invention is increasing by through-hole, so that connection area is increasing, it is ensured that the pressure of capillary wick on the whole is balanced, avoids local pressure excessive, causes damages.
Description
Technical field
The present invention relates to a kind of heat pipe and utilize the heat-exchanger rig of heat pipe.
Background technique
In the prior art, heat pipe is typically all the circulation for relying on gravity to realize heat pipe, but such heat pipe is only suitable for lower part
The case where heat absorption top heat release, goes not being applicable in for the heat absorption lower part heat release of opposite top.Therefore such situation, the present invention are directed to
By being improved capillary structure, structure is invented and has improved antigravity heat pipe.
In application in front, applicant has applied for anti-gravity loop circuit heat pipe, and the heat pipe includes evaporation ends and condensation end,
The evaporation ends are located at condensation end top, and described evaporation ends a part is arranged in the fluid ascent stage, in the evaporation of fluid ascent stage
Capillary wick is arranged in at least part at end, and capillary wick center setting condensation end flows to the pipeline of evaporation ends.But this heat pipe pipeline
Connection between capillary wick is to maintain consistent in the height direction, but finds under study for action, such situation is be easy to cause
Local pressure is excessive, and the service life of opposite heat tube generates loss.
In view of the above-mentioned problems, the present invention is improved on the basis of invention in front, a kind of new loop heat is provided
Pipe and its heat-exchanger rig, the present invention is increasing by through-hole, so that connection area is increasing, it is ensured that capillary wick is whole
On pressure it is balanced, avoid local pressure excessive, cause damages.
Summary of the invention
The present invention provides a kind of new loop circuit heat pipes and its heat-exchanger rig, and the present invention is increasing by through-hole, so that
It is increasing to be connected to area, it is ensured that capillary wick pressure on the whole is balanced, avoids local pressure excessive, cause damages to
Solve the technical issues of front occurs.
To achieve the goals above, technical scheme is as follows:
A kind of anti-gravity loop circuit heat pipe, the heat pipe include evaporation ends and condensation end, and the evaporation ends are located on condensation end
Capillary is arranged in the fluid ascent stage, at least part of the evaporation ends of fluid ascent stage in portion, evaporation ends a part setting
Core, capillary wick center setting condensation end flow to the pipeline of evaporation ends, and the pipeline is flexible pipe, is arranged on the pipeline tube wall logical
Hole, pipeline between through-hole and capillary wick by being connected to, and along on height ascent direction, the diameter of the through-hole is increasing.
Preferably, the increasing amplitude of the diameter of the through-hole constantly increases along on height ascent direction.
Preferably, through-hole is round or diamond shape.
Preferably, the capillary wick extends to condensation end.
A kind of heat-exchanger rig, including blower fan apparatus, air inlet passageway, air outlet passage, loop circuit heat pipe and water storage are cold
Solidifying room, which is characterized in that the water storage condensation chamber is arranged in soil heat sink, and the outlet of air inlet passageway, air outlet slit are logical
The entrance in road is connected to water storage condensation chamber, and air is introduced into the mistake of water storage condensation chamber by the blower fan apparatus from air inlet passageway
Cheng Zhongyu evaporation ends exchange heat, and condensation end gives heat transfer to external soil heat sink, and the loop circuit heat pipe is mentioned-above ring
Road heat pipe.
Preferably, the blower fan apparatus includes vertical wind machine, planetary gear speed increaser and helical blade, vertical-shaft wind
Machine utilizes wind energy, and planetary gear speed increaser and helical blade is driven to suck air.
Preferably, the inlet tube of helical blade lower end connection water storage condensation chamber, the water storage condensation chamber connect inlet tube
Position start diameter and become larger, then diameter starts to become smaller.
Preferably, the evaporation ends of loop circuit heat pipe are mounted on water storage condensation chamber inlet tube, the condensation end winding of loop circuit heat pipe
Outside condensation chamber, and external soil directly contacts.
Preferably, capillary wick is arranged at least part of the evaporation ends, to realize the effect of antigravity heat pipe.
Preferably, air inlet passageway is exactly the inlet tube of condensation chamber, entering for condensation chamber is arranged in air outlet passage
Mouth pipe, the hot-air of the cold air precooled air import of air outlet slit.
Preferably, the inlet tube of condensation chamber is arranged in evaporation ends, at least part of evaporation ends is filled with capillary wick, hair
Thin core center setting condensation end flows to the pipeline of evaporation ends, and the outside wall surface of evaporation ends is around the longitudinal vertical fin of setting.
Preferably, air outlet passage be arranged between the vertical fin of adjacent two and with two adjacent vertical wings
Piece contact.
Preferably, evaporation ends flow direction condensation end pipeline be arranged between the vertical fin of adjacent two and with it is adjacent
Two vertical fin contacts.
The pipeline be it is multiple, the air outlet passage be multiple, the quantity phase of the pipeline and air outlet passage
Deng.
Further preferably, the pipeline is arranged between adjacent air outlet passage, and the air outlet passage 4 exists
Between adjacent pipeline 9.
Further preferably, 9 center of pipeline is identical as adjacent 4 centre distance of air outlet passage；The air goes out
Mouth 4 center of channel is identical as adjacent 9 centre distance of air pipe line.
Preferably, the radius of air outlet passage 4 is R, the radius of pipeline 9 is r, and the angle between adjacent fins is A,
Meet claimed below:
Sin (A)=a*LN (r/R)+b, wherein LN is logarithmic function, and a, b are parameters,
Wherein 0.330 < a < 0.340,0.73 <b < 0.74；
15°<A<25°；
0.24<r/R<0.5；
Further preferably, 0.26 < r/R < 0.38.
Compared with prior art, the present invention has the advantage that:
1) present invention is increasing by the pipeline in capillary wick and the connection through-hole between capillary wick, so that connection area
It is increasing, it is ensured that the pressure of capillary wick on the whole is balanced, avoids local pressure excessive, causes damages.
2) it forces humid air to reach dew point using the temperature difference of ground air and underground, gets rid of the dependence to electricity, it can
It is truly realized zero-emission, no pollution.
3) for loop circuit heat pipe as efficient heat transfer tool, principle is simple, compact-sized, can effectively increase air heat-exchange face
Product, significantly improves cooling efficiency.
4) loop circuit heat pipe condenser is wrapped in outside condensation chamber, is come into full contact with external soil, and opposite heat tube evaporation ends are increased
The heat dissipation of air improves cooling efficiency.
5) it is consumed without secondary energy sources, wind-force is as daily power, and system uses vertical-shaft wind used for wind power generation
Machine avoids influence of the wind direction to wind energy conversion system, can collect the wind that all directions are come, solar-cell motor can under calm condition
Entry impeller rotation is driven, this sampling device can accomplish continuous service.Accomplish wind light mutual complementing on definite meaning.
Detailed description of the invention
Fig. 1 is overall structure diagram of the invention.
Fig. 2 is vertical axis windmill schematic diagram of the invention.
Fig. 3 is planetary gear speed increaser cross-sectional view of the invention.
Fig. 4 is impeller top view of the invention.
Fig. 5 is under ground portion view of the invention.
Fig. 6 is condensation chamber cross-sectional view of the invention.
Fig. 7 is the sectional view of A-A in Fig. 6.
Fig. 8 is the structural schematic diagram of heat pipe of the invention.
Fig. 9 is the structural schematic diagram that multiple evaporation ends of the invention flow to condensation end pipeline (descending branch).
Figure 10 is the pipeline jointing construction schematic diagram of present invention setting capillary wick position.
Appended drawing reference is as follows: 1 blower, 2 planetary gears, 3 helical blades, 4 air outlet passages, and 5 air intlets are logical
Road, 6 loop circuit heat pipe evaporation ends, 7 condensation chambers, 8 loop circuit heat pipe condensation ends, 9 evaporation ends flow to condensation end pipeline (descending branch), and 10 is cold
Solidifying end flows to evaporation ends pipeline, 11 condensation chamber inlet tubes, 12 fins, 13 capillary wicks
Specific embodiment
Specific embodiments of the present invention will be described in detail with reference to the accompanying drawing.
Herein, if without specified otherwise, it is related to formula, "/" indicates that division, "×", " * " indicate multiplication.
Specific embodiments of the present invention will be described in detail with reference to the accompanying drawing.
A kind of anti-gravity loop circuit heat pipe, as shown in figure 8, the heat pipe includes evaporation ends 6 and condensation end 8, the evaporation ends 6
Positioned at 8 top of condensation end, 6 a part setting of the evaporation ends in the fluid ascent stage, the fluid ascent stage evaporation ends at least
A part setting capillary wick 13, as shown in Figure 10.
Preferably, evaporation ends include that evaporation ends flow to condensation end pipeline (descending branch) 9, ascent stage two parts.Wherein make
To be preferred, setting condensation end flows to evaporation ends pipeline 10 in the ascent stage.
As shown in Figure 1, a kind of loop circuit heat pipe air water fetching device, including blower fan apparatus 1, air inlet passageway 5, air go out
Mouth channel 4, loop circuit heat pipe and water storage condensation chamber 7, the water storage condensation chamber 7 are arranged in soil heat sink, and the loop circuit heat pipe is
Antigravity heat pipe, the outlet of air inlet passageway 5, the entrance of air outlet passage 4 are connected to water storage condensation chamber, the blower dress
Set 1 air is introduced water storage condensation chamber 7 from air inlet passageway 5 during exchange heat with evaporation ends 6, condensation end 8 will
Heat transfer gives external soil heat sink.
The present invention provides a kind of air water fetching devices of the loop circuit heat pipe of Novel structure, by the way that loop circuit heat pipe conduct is arranged
Efficient heat transfer tool, principle is simple, compact-sized, significantly improves cooling efficiency.And the present invention utilizes ground air and underground
The temperature difference of soil forces humid air to reach dew point, gets rid of the dependence to electricity, can be truly realized zero-emission, no pollution.
Preferably, at least part of the evaporation ends 6 of loop circuit heat pipe is mounted on 7 inlet of water storage condensation chamber.
Preferably, 7 inlet tube of condensation chamber, the air inlet passageway are arranged between the condensation chamber 7 and blower fan apparatus 1
5 at least part are arranged in 7 inlet tube of condensation chamber, and at least part of 7 inlet tube of condensation chamber is arranged in external soil heat sink
In.By making sky so set, the air in air inlet passageway 5 can be made directly to participate in the heat exchange of external soil heat sink
Gas is further cooling under the collective effect of soil and loop circuit heat pipe, improves cooling effect.
Further preferably, the blower fan apparatus 1 includes vertical wind machine, planetary gear speed increaser 2 and helical blade 3, vertically
Axis wind energy conversion system utilizes wind energy, and planetary gear speed increaser 2 and helical blade 3 is driven to suck air.
Preferably, vertical wind machine 1 is located at top, lower part is successively planetary gear speed increaser 2 and helical blade 3, described
Helical blade 3 is connected to 7 inlet tube of condensation chamber, so that outside air is introduced into condensation chamber 7.
Further preferably, the inlet tube of condensation chamber 7 is exactly air inlet passageway.
Preferably, as shown in Figure 1, the water storage condensation chamber 7 from connection inlet tube position it is downward, be just initially diameter
It becomes larger, diameter starts to gradually become smaller after then having arrived certain position.Be conducive to air in condensation indoor moveable, complete gas
Circulation, and increase gas and condense the heat exchange efficiency between locular wall
Preferably, the evaporation ends 6 of loop circuit heat pipe are mounted on water storage condensation chamber inlet tube, the condensation end 8 of loop circuit heat pipe is twined
It is around in outside condensation chamber, and external soil directly contacts.Loop circuit heat pipe condenser is wrapped in outside condensation chamber, is filled with external soil
Tap touching, increases the heat dissipation of opposite heat tube evaporation ends air, improves cooling efficiency.
Preferably, capillary wick 13 is arranged at least part of the evaporation ends 6, capillary force provides working medium reflux and follows
The power of ring, while the working medium amount of reflux being made to reach the demand of heat transfer, to realize the effect of antigravity heat pipe.
By be arranged capillary wick 13, and capillary wick 13 because itself be arranged in evaporation ends so that in the ascent stage 6 of evaporation ends
Naturally flow resistance is generated, so that the steam natural that evaporation ends generate flows to the small pipeline 9 of resistance, so as to form bob-weight
Power heat pipe.
Preferably, the capillary wick 13 was positioned only in the ascent stage of evaporation ends, as being preferably provided at the ascent stage
A part in.Such as shown in Fig. 6, Figure 10.
Preferably, at least part of air outlet passage 4 is arranged in the inlet tube of condensation chamber, air outlet slit it is cold
The hot-air of air precooling air intlet.By the heat exchange of exit gas and inlet gas, heat transfer effect is further realized, is increased
The condensation efficiency of water.
Preferably, the ascent stage of evaporation ends is filled with hair as shown in fig. 7, the inlet tube of condensation chamber is arranged in evaporation ends
Thin core 13, to provide sufficiently large capillary force, 13 center of capillary wick setting condensation end flows to the pipeline 10 of evaporation ends, by such
Pipeline 10 (in without capillary wick) is set, it is possible to reduce the fluid resistance of pipeline improves antigravity shape so that working medium reflux is more smooth
Heat-transfer capability under state, the ascent stage outside wall surface of evaporation ends increase heat exchange area, improve around the longitudinal vertical fin 12 of setting
With the heat exchange efficiency of air.
Pipeline 10 is gas or liquid line, realizes a flexible arrangement, both caliber was smaller, was easily bent.Loop circuit heat pipe
Principle is, if vaporizer side and pipeline 10 are steam pipe line, then principle is the heated internal working medium evaporation of evaporator, and steam is along evaporation
Device upper outlet enters pipeline 10, then flow to lower loop around pipeline, with soil contact start condense, when steam all condense
Afterwards, evaporator is returned to by the effect of evaporator capillary wick capillary force, to realize the circulation of working medium.
Preferably, pipeline 10 is flexible pipe.
Preferably, being connected between pipeline 10 and capillary wick 13.By connection, can be realized capillary wick 13 and pipeline 10 it
Between fluid circulation so that liquid is by capillary wick uphill process, if generate biggish pressure because of heat absorption, such as
Possibly even there is bubble, then it can be by pipeline 10 come the pressure of balanced evaporator section, to guarantee the equilibrium of pressure.
Further there is choosing, it is more next along area is connected on height ascent direction, between the pipeline 10 and capillary wick 13
It is bigger.Because with the rising of height, because fluid is constantly heated, the pressure of generation can be increasing, therefore by continuous
Increased connection area, it is ensured that the pressure of capillary wick 13 on the whole is balanced, avoids local pressure excessive, causes damages.
Further preferably, more next along area is connected on height ascent direction, between the pipeline 10 and capillary wick 13
Bigger amplitude constantly increases.It is found through experiments that, the amplitude for taking connection area increasing constantly increases, Neng Goujin
One step realizes that the pressure inside capillary wick is balanced, improves the service life of product.
Preferably, through-hole is arranged in 10 tube wall of pipeline, pipeline 10 between through-hole and capillary wick 13 by being connected to.It is further excellent
Choosing, through-hole are round or diamond shape.
Further preferably, along on height ascent direction, the diameter (or nominal diameter) of the through-hole is increasing.Mainly
Reason is increasing by through-hole, so that connection area is increasing, it is ensured that the pressure of capillary wick 13 on the whole is balanced, keeps away
It is excessive to exempt from local pressure, causes damages.
Further preferably, along on height ascent direction, diameter (or nominal diameter) increasing amplitude of the through-hole
It is continuous to increase.The main cause amplitude variation increasing by through-hole, so that it is continuous to be connected to the increasing amplitude of area
Increase, the pressure that can be further realized inside capillary wick is balanced, improves the service life of product.
Further preferably, along on height ascent direction, the distribution density of through-hole is identical.
Further preferably, along on height ascent direction, the distribution density of the through-hole is increasing.Main cause passes through
Through-hole distribution density is increasing, so that connection area is increasing, it is ensured that the pressure of capillary wick 13 on the whole is balanced, keeps away
It is excessive to exempt from local pressure, causes damages.
Further preferably, along on height ascent direction, the increasing amplitude of the distribution density of the through-hole constantly increases
Add.The main cause amplitude variation increasing by through-hole distribution density, so that it is continuous to be connected to the increasing amplitude of area
Increase, the pressure that can be further realized inside capillary wick is balanced, improves the service life of product.
Further preferably, along on height ascent direction, the diameter (or nominal diameter) of each through-hole is identical.
Further preferably, the capillary wick 13 extends to condensation end, directly to suct the liquid of condensation end.Into one
Step improves the circulation ability of antigravity heat pipe.
Further preferably, along on height ascent direction, the caliber of the pipeline 10 is increasing.Because with height
Rising because fluid is constantly heated, the pressure of generation can be increasing, therefore passes through the pipe of ever-increasing pipeline 10
Diameter, it is ensured that the pressure of capillary wick 13 and evaporation ends on the whole is balanced, avoids local pressure excessive, causes damages.
Further preferably, along on height ascent direction, the increasing amplitude of 10 caliber of pipeline constantly increases
Add.It is found through experiments that, the amplitude for taking caliber increasing constantly increases, and can further realize capillary wick and evaporation
Pressure inside end is balanced, improves the service life of product.
Preferably, capillary wick is distributed along short transverse, as shown in Fig. 6.Further preferably, along height decline side
To the capillary force of the capillary wick gradually increases.It is more proximate to condensation end, capillary force is bigger.It is found through experiments that, takes such
Mode can further increase the suction to liquid, can be improved 20% or more suction under identical cost, to improve
Heat transfer effect.
By further analyzing, preliminary reason may be as the capillary force close to condensation end is increasing, so that condensation
The liquid at end can be quickly drawn onto capillary wick, and liquid is constantly flowed to evaporation ends.In flow process, liquid is not
Disconnected heat absorption, then because temperature caused by absorbing heat increases, density becomes smaller, therefore because of variable density reason, the hair for needing it
Thin power obviously becomes smaller, therefore is also easy for up inhaling in the case where capillary force is small.Above-mentioned reason is that the present inventor passes through
What a large amount of experiment and research obtained, the common knowledge of non-this field.
Further preferably, along height descent direction, the amplitude that the capillary force of the capillary wick gradually increases is increasing.
It is found through experiments that, takes such mode, the suction to liquid can be further increased, it can be further under identical cost
The suction for improving 8% or so, to improve heat transfer effect.
Preferably, as shown in Figure 10, the caliber that the heat pipe position of capillary wick is arranged is greater than the heat pipe for being not provided with capillary wick
The caliber of position.
Further preferably, as shown in Figure 10, it is described setting capillary wick heat pipe position pipe and be not provided with capillary wick
Caliber change between the pipe of heat pipe position is consecutive variations.It is further preferred that straight line changes.The pipe of Large Diameter Pipeline position
Pipe with tubule warp in junction is connected by contractibility.The variation of the caliber of contractibility is linear change.
Preferably, air outlet passage 4 is arranged between the vertical fin 12 of adjacent two and erects with adjacent two
Straight fins 12 contact.Pass through such setting, it is possible to reduce the mechanism of the independent support air outlet passage 4 of setting, so that structure
Compact, the cold air of exit passageway can be exchanged heat by pipeline and fin, kept the cold degree of fin, enhanced heat transfer effect.
Preferably, evaporation ends flow direction condensation end pipeline 9 be arranged between the vertical fin of adjacent two and with it is adjacent
Two vertical fin contacts.Pass through such setting, it is possible to reduce the mechanism of the independent support air outlet passage 4 of setting makes
Must be compact-sized, the steam in pipeline can reduce system overall thermal resistance, avoid on ground by pipeline to the of short duration a small amount of heat transfer of fin
Steam superheating is generated in the case of the antigravity of face in evaporator, to slow down the temperature oscillation phenomenon in heat pipe start-up course.
Further preferably, the pipeline 9 than air outlet passage 4 closer to the outer wall of evaporation ends pipeline so that above-mentioned
Two diabatic processes can be achieved at the same time, and play respective action.
Further preferably, the diameter of the pipeline 9 is less than air outlet passage 4.
Preferably, along the condensation end pipeline 9 that multiple evaporation ends flow directions can be set, as shown in Fig. 7,9.Pass through setting
Multiple pipelines 9 can make evaporation ends inhale thermogenetic steam and enter condensation end by multiple pipelines 9, further augmentation of heat transfer,
And the evaporation because the fluid in heat pipe absorbs heat, cause volume to increase, by the way that multiple pipelines 9 are arranged, can further alleviate pressure
Power improves heat transfer effect.
Further preferably, the vertical fin extends through the center of circle of the inlet tube of condensation chamber, the evaporation ends ascent stage
The inlet tube of the pipeline and condensation chamber center of circle having the same.
Preferably, the pipeline 9 be it is multiple, between the center of circle and evaporation ends ascent stage pipeline of the multiple pipeline 9
Apart from identical.
Further preferably, per one pipeline 9 of setting between adjacent two vertical fins 12.The pipeline 9 is in parallel
Structure.
Preferably, the air outlet passage 4 is multiple, the center of circle of the multiple air outlet passage 4 and evaporation ends
The distance between ascent stage pipeline is identical, so that Temperature Distribution is more uniform between fin, and above-mentioned heat transfer effect is become apparent from.
Further preferably, per one air outlet passage 4 of setting between adjacent two vertical fins 12.The air outlet passage 4
It is parallel-connection structure.
Further preferably, the pipeline 9 be it is multiple, the air outlet passage 4 be it is multiple, the pipeline 9 goes out with air
The quantity in mouth channel 4 is equal.
Further preferably, the pipeline 9 is arranged between adjacent air outlet passage 4, the air outlet passage 4
Between adjacent pipeline 9.Further preferably, 9 center of pipeline is identical as adjacent 4 centre distance of air outlet passage；
4 center of air outlet passage is identical as adjacent 9 centre distance of air pipe line.Adjacent sky is arranged in the i.e. described pipeline 9
The centre of gas exit passageway 4, the air outlet passage 4 is among adjacent pipeline 9.I.e. as shown in figure 8, where pipeline 9
The first line between the center of circle and the center of circle of evaporation ends 6, between adjacent 4 center of circle of air outlet passage and the center of circle of evaporation ends 6
The first line, third line are formed, the first angle formed between the first line and the second line is equal to the first line and third
The second angle formed between line.Similarly, the 4th between the center of circle where air outlet passage 4 and the center of circle of evaporation ends 6
Line, forms the 5th line, the 6th line between adjacent 9 center of circle of pipeline and the center of circle of evaporation ends 6, the 4th line and the 5th connect
The third angle formed between line is equal to the 4th angle formed between the 4th line and the 6th line.Namely in circumferential direction
On, pipeline 9 and exit passageway 4 are uniformly distributed.
Pass through above-mentioned setting, it is ensured that pipeline 9 and air outlet passage 4 carry out the uniform of cooling to inlet air, keep away
Exempt from local income inequality, leads to effect variation of fetching water.
It, can not in numerical simulation and it was found that, the caliber of air outlet passage 4 and pipeline 9 difference cannot be too big
Too small, the distance for causing very much air outlet passage 4 and pipeline 9 to be distributed greatly is too far, leads to the sky between channel 4 and pipeline 9
Gas heat exchange is bad, causes overall heat exchange uneven, and the distance for causing air outlet passage 4 and pipeline 9 to be distributed if too small is too close,
The air heat-exchange of the air and/or the outer wall close to evaporation ends 6 that lead to the outer wall close to air inlet passageway 5 is bad, causes whole
Air heat-exchange in body air inlet passageway 5 is uneven；Same reason, the angle between adjacent fins 12 cannot be too big, too
It will lead to that distribution fin is few, and heat transfer effect is excessively bad if big, also result in air outlet passage 4 and quantity that pipeline 9 is distributed
Very little, cause heat exchange unevenly and heat transfer effect is bad, similarly, the angle between adjacent fins 12 cannot be too small, too small
Words cause fin distribution too close, and flow resistance increases, and the caliber of air outlet passage 4 and pipeline 9 is not much different, but he
Differ greatly with the exchange capability of heat of homalographic, therefore heat exchange is uneven in such cases, causes heat transfer effect bad.Therefore it needs
Optimal size relationship is determined by a large amount of numerical simulation and its experiment.
The radius of air outlet passage 4 is R, and the radius of pipeline 9 is r, and the angle between adjacent fins is A, is met following
It is required that:
Sin (A)=a*LN (r/R)+b, wherein LN is logarithmic function, and a, b are parameters,
Wherein 0.330 < a < 0.340,0.73 <b < 0.74；
15°<A<25°；
0.24<r/R<0.5；Further preferably, 0.26 < r/R < 0.38.
Above-mentioned empirical equation is to be obtained by a large amount of numerical simulations and experiment, and pass through verification experimental verification, and error is substantially
Within 3.2.
Preferably, 3 < the R < 10mm；1.5 < the r < 4.0mm；
Further preferably, the heat pipe caliber for capillary wick position being arranged is 30-40mm, further preferably 32mm；
Further preferably, the heat pipe caliber for being not provided with capillary wick position is 5.0-6.4mm；
Further preferably, it is 5.0-6.4mm that condensation end, which flows to the caliber of the pipeline of evaporation ends,；
Further preferably, 5 caliber of air inlet passageway is 80-200mm；It is preferred that 120-150mm；
Further preferably, the vertical direction length of fin is 780-1500mm, preferably 1200mm；The length that fin longitudinally extends
Degree accounts for the 95% of 6 outer diameter of evaporation ends and 4 internal diameter difference of air outlet passage.The overall heat exchange ability of fin significantly mentions under this length
Height, the coefficient of heat transfer are and relatively small to the effect of the broken ring in boundary layer and the influence of fluid flow effect also in suitable range
The case where for caliber change, takes the mean values of caliber to calculate.For example, about 9 pipeline changes, then
Caliber is averaged using pipeline 9 to calculate.
External wind drives vertical axis windmill 1 as shown in the figure to rotate, and wind energy transformation is mechanical energy.Wind energy conversion system passes through planetary gear
Speed changer 2 drives coaxial air inlet helical blade 3 to rotate, and filtered extraneous humid air is sucked condensation chamber.Air inlet air port design
It is the revolving body with decrement mouth for maintaining pressure.The continued operation of impeller increases intracavity gas pressure, humid air it is exhausted
Humidity is increased.The biggish air of absolute humidity is entered under the continuous action of air pressure by the relatively narrow inlet channel of bore
Underground condensation chamber.Extraneous hot-air first in the inlet channel 5 with outdoor cooler air is being discharged into outlet passageway
It exchanges heat, exhaust gas is allowed to take away partial heat, the metal outer wall contacted with soil also has thermally conductive function, and the two collective effect is completed
Air precooling.After air initially enters condensation chamber, relatively warm air first slow transits through loop heat pipe evaporator fin channels, with loop
Medium completes heat exchange in heat pipe, and own temperature significantly reduces, and when reaching dew point, vapor starts to liquefy, in fin surface shape
At droplet.Surplus air gos deep into water storage condensation chamber 7, by cavity metal outer wall and extraneous soil heat exchange, while being condensed into liquid
Drop.As liquid water is built up, hot-air is gradually decreased with outer wall contact area, and major refrigeration is mentioned by loop circuit heat pipe at this time
For.The evaporation ends 6 of the loop circuit heat pipe absorb the heat of hot-air, and liquid refrigerant is flashed to gaseous state, then passes through condensation chamber
Heat is conducted to external soil by the loop circuit heat pipe condensation end 8 being externally wrapped with, and gaseous working medium is made to be condensed into liquid, and anti-gravity ring
Road heat pipe has the characteristics that liquid reflux can be made.Under lasting wind-force, the water resource in extraneous humid air will be constantly
It is collected into water storage condensation chamber, is cooled rapidly, be discharged away after being condensed out liquid water.What vertical axis windmill 1 generated
Electric energy is stored in battery, and electric energy supplies the fresh water of electronic water pump extraction accumulation, and storage is on the ground in water tank.
The present invention condenses to water vapor in air by wind energy, soil heat sink and loop circuit heat pipe when fetching water
Condensation water intaking, not only solves dependence of traditional solar energy absorption method to solar energy, adapts to more regions and weather condition, accomplish
No secondary energy sources consumption, also solves the not high enough problem of prior art transfer efficiency.
Preferably, wind energy conversion system, is transferred to the revolving speed of impeller by planetary gear speed increaser connection vertical axis windmill and impeller
Amplification, makes outside air enter tank interior faster, increases intake to a certain extent, while improving the pressure in pipeline.
Preferably, preparing loop heat pipe capillary core using powder metallurgy process.Before starting, the evaporator of loop circuit heat pipe
It is full of working medium in capillary wick, additional cavity and perfusion tube, and is in two phases in steam channel, condenser and steam pipe.
Cooling chamber position using soil it is cooling supplemented by, the collaboration heat exchange mode based on anti-gravity loop circuit heat pipe, can mention significantly
High-altitude air cooling speed improves water yield.
Preferably, loop circuit heat pipe condensation end is wrapped in outside condensation chamber, increase heat dissipation area.
Preferably, exhaust pipe is placed in the intake channel, to achieve the purpose that air precooling.
Although the present invention has been disclosed in the preferred embodiments as above, present invention is not limited to this.Any art technology
Personnel can make various changes or modifications, therefore protection scope of the present invention is answered without departing from the spirit and scope of the present invention
When being defined by the scope defined by the claims..
Claims (9)
1. a kind of loop circuit heat pipe air water fetching device, including blower fan apparatus, air inlet passageway, air outlet passage, loop heat
Pipe and water storage condensation chamber, which is characterized in that the water storage condensation chamber is arranged in soil heat sink, the outlet of air inlet passageway,
The entrance of air outlet passage is connected to water storage condensation chamber, and air is introduced water storage from air inlet passageway by the blower fan apparatus
It exchanges heat during condensation chamber with evaporation ends, condensation end gives heat transfer to external soil heat sink, and the loop circuit heat pipe is anti-
Gravity loop circuit heat pipe, the loop circuit heat pipe include evaporation ends and condensation end, and the evaporation ends are located at condensation end top, the evaporation
End a part setting is in the fluid ascent stage, at least part setting capillary wick of the evaporation ends of fluid ascent stage, capillary wick
Heart setting condensation end flows to the pipeline of evaporation ends, and the pipeline is flexible pipe, through-hole is arranged on the pipeline tube wall, pipeline passes through
It is connected between through-hole and capillary wick, along on height ascent direction, the diameter of the through-hole is increasing；
The evaporation ends of loop circuit heat pipe are mounted in water storage condensation chamber inlet tube, and the condensation end of loop circuit heat pipe is wound in outside condensation chamber
Portion, and external soil directly contact.
2. loop circuit heat pipe air water fetching device as described in claim 1, which is characterized in that along on height ascent direction, institute
The increasing amplitude of diameter for stating through-hole constantly increases.
3. loop circuit heat pipe air water fetching device as claimed in claim 1 or 2, which is characterized in that through-hole is round or diamond shape.
4. loop circuit heat pipe air water fetching device as described in claim 1, which is characterized in that the capillary wick extends to condensation
End.
5. loop circuit heat pipe air water fetching device as described in claim 1, which is characterized in that air inlet passageway is exactly condensation chamber
Inlet tube, air outlet passage is arranged in the inlet tube of condensation chamber, the heat of the cold air precooled air import of air outlet slit
Air.
6. loop circuit heat pipe air water fetching device as described in claim 1, which is characterized in that entering for condensation chamber is arranged in evaporation ends
In mouth pipe, at least part of evaporation ends is filled with capillary wick, and capillary wick center setting condensation end flows to the pipeline of evaporation ends, steams
The outside wall surface of originator is around the longitudinal vertical fin of setting.
7. loop circuit heat pipe air water fetching device as described in claim 1, which is characterized in that air outlet passage is arranged adjacent
Two vertical fins between and with two adjacent vertical fin contacts.
8. loop circuit heat pipe air water fetching device as claimed in claim 7, which is characterized in that adjacent sky is arranged in the pipeline
Between gas exit passageway, the air outlet passage is between adjacent pipeline.
9. loop circuit heat pipe air water fetching device as claimed in claim 8, which is characterized in that the pipeline center and adjacent sky
Gas exit passageway centre distance is identical；The air outlet passage center is identical as adjacent air pipe line centre distance.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910186515.8A CN110094893B (en) | 2018-01-31 | 2018-03-23 | Design method for communication size of water lifting device |
| CN201910183189.5A CN110094892B (en) | 2018-01-31 | 2018-03-23 | Design method of device for extracting water from air by loop heat pipe |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2018100981138 | 2018-01-31 | ||
| CN201810098113 | 2018-01-31 |
Related Child Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910186515.8A Division CN110094893B (en) | 2018-01-31 | 2018-03-23 | Design method for communication size of water lifting device |
| CN201910183189.5A Division CN110094892B (en) | 2018-01-31 | 2018-03-23 | Design method of device for extracting water from air by loop heat pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108362150A CN108362150A (en) | 2018-08-03 |
| CN108362150B true CN108362150B (en) | 2019-03-29 |
Family
ID=63000779
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910183189.5A Expired - Fee Related CN110094892B (en) | 2018-01-31 | 2018-03-23 | Design method of device for extracting water from air by loop heat pipe |
| CN201910186515.8A Expired - Fee Related CN110094893B (en) | 2018-01-31 | 2018-03-23 | Design method for communication size of water lifting device |
| CN201810246205.6A Expired - Fee Related CN108362150B (en) | 2018-01-31 | 2018-03-23 | A kind of loop circuit heat pipe and its heat-exchanger rig of via area height change |
| CN201810247015.6A Expired - Fee Related CN108489309B (en) | 2018-01-31 | 2018-03-23 | A kind of loop circuit heat pipe and its heat-exchanger rig of through-hole distribution density height change |
Family Applications Before (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910183189.5A Expired - Fee Related CN110094892B (en) | 2018-01-31 | 2018-03-23 | Design method of device for extracting water from air by loop heat pipe |
| CN201910186515.8A Expired - Fee Related CN110094893B (en) | 2018-01-31 | 2018-03-23 | Design method for communication size of water lifting device |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810247015.6A Expired - Fee Related CN108489309B (en) | 2018-01-31 | 2018-03-23 | A kind of loop circuit heat pipe and its heat-exchanger rig of through-hole distribution density height change |
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| CN (4) | CN110094892B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110617634B (en) * | 2019-03-14 | 2021-01-29 | 山东大学 | Distribution structure of capillary parts and solar heat collector thereof |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003194485A (en) * | 2001-12-27 | 2003-07-09 | Mitsubishi Electric Corp | Evaporator, loop heat pipe with built-in reservoir, and heat transport method |
| CN100552366C (en) * | 2006-09-15 | 2009-10-21 | 富准精密工业(深圳)有限公司 | Loop heat pipe |
| CN101398272A (en) * | 2007-09-28 | 2009-04-01 | 富准精密工业(深圳)有限公司 | Hot pipe |
| CN203454874U (en) * | 2013-06-27 | 2014-02-26 | 华南理工大学 | Anti-gravity loop heat pipe |
| CN103344145B (en) * | 2013-06-27 | 2016-01-06 | 华南理工大学 | A kind of there is liquid-sucking core runner loop circuit heat pipe and heat-transferring method and manufacture method |
| CN107345771A (en) * | 2016-05-05 | 2017-11-14 | 讯凯国际股份有限公司 | The heat-pipe apparatus of antigravity formula |
-
2018
- 2018-03-23 CN CN201910183189.5A patent/CN110094892B/en not_active Expired - Fee Related
- 2018-03-23 CN CN201910186515.8A patent/CN110094893B/en not_active Expired - Fee Related
- 2018-03-23 CN CN201810246205.6A patent/CN108362150B/en not_active Expired - Fee Related
- 2018-03-23 CN CN201810247015.6A patent/CN108489309B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN110094892A (en) | 2019-08-06 |
| CN110094892B (en) | 2020-12-18 |
| CN108362150A (en) | 2018-08-03 |
| CN108489309B (en) | 2019-04-19 |
| CN110094893B (en) | 2020-12-22 |
| CN110094893A (en) | 2019-08-06 |
| CN108489309A (en) | 2018-09-04 |
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