CN107144161A - The annular and separation device loop circuit heat pipe that spacing changes in a kind of short transverse - Google Patents
The annular and separation device loop circuit heat pipe that spacing changes in a kind of short transverse Download PDFInfo
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- CN107144161A CN107144161A CN201710294949.0A CN201710294949A CN107144161A CN 107144161 A CN107144161 A CN 107144161A CN 201710294949 A CN201710294949 A CN 201710294949A CN 107144161 A CN107144161 A CN 107144161A
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- Prior art keywords
- tedge
- separating device
- collector
- heat pipe
- heat
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Classifications
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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
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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
- F28D15/0266—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 separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers
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- Engineering & Computer Science (AREA)
- 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)
Abstract
The invention provides a kind of heat pipe, including evaporation collector, condensation collector, tedge and return duct, the tedge is connected with evaporation collector and condensation collector, the evaporation collector is located at bottom, the condensation collector is located at top, and the fluid absorbs heat in evaporation collector and evaporated, and enters condensation collector by tedge, condensed after being exchanged heat in condensation collector, the fluid of condensation returns to evaporation collector by return duct；Separating device is set in the tedge, set in same tedge and separating device is set in multiple separating devices, the tedge, multiple separating devices are set in same tedge, along the short transverse of tedge, the spacing between adjacent separating device constantly reduces.The present invention is changed by the spacing of separating device, when there is Gas- liquid two-phase flow in tedge, augmentation of heat transfer, while weakening the vibration of tedge, reduces noise level.
Description
Technical field
The invention belongs to heat pipe field, more particularly to a kind of heat exchange heat pipe.
Background technology
Hot pipe technique is George Ge Luofo of U.S. Los Alamos (Los Alamos) National Laboratory in 1963
One kind of (George Grover) invention is referred to as the heat transfer element of " heat pipe ", and it takes full advantage of heat-conduction principle and is situated between with phase transformation
The heat of thermal objects, is delivered to outside thermal source rapidly by the quick thermal transport property of matter through heat pipe, and its capacity of heat transmission, which exceedes, appoints
The capacity of heat transmission of what known metal.
The industries such as aerospace, military project are widely used in before hot pipe technique, since being introduced into radiator manufacturing so that
People change the mentality of designing of traditional heat sinks, have broken away from the high air quantity motor of simple dependence to obtain the list of more preferable radiating effect
One radiating mode, using hot pipe technique so that radiator obtains satisfied heat transfer effect, opens radiating industry new world.At present
Heat pipe is widely used in various heat transmission equipments, including nuclear power field, such as the UTILIZATION OF VESIDUAL HEAT IN of nuclear power.
On the one hand, heat pipe is in evaporation process, and inevitably carrying of liquids is in tedge, simultaneously as condensation end
Exothermic condensation so that there is liquid in condensation end, liquid also inevitably enters tedge, so that tedge
Interior fluid is liquid-vapor mixture, while the on-condensible gas that heat pipe can be produced because of aging in the process of running, on-condensible gas one
As rise to the condensation end on heat pipe top, the presence of on-condensible gas causes the pressure in condensation end of heat pipe to increase, and pressure causes
Liquid ramps up Bottomhole pressure.It greatly have impact on the efficiency of heat exchange.
On the other hand, condensation collector this section is exported to from tedge, because the space of this section becomes big suddenly, space
Change can cause the quick of gas to flow upwards out and assemble, therefore spatial variations can cause the vapour phase (vapour group) of aggregation from tedge
Position enters condensation collector, due to gas (vapour) liquid density contrast, and air mass leaves adapter position and will moved rapidly upward, and air mass is former empty
Between position the liquid of wall is pushed away while also by rapid resilience and hitting wall by air mass, form impingement phenomenon.Gas (vapour) liquid phase
More discontinuous, air mass aggregation is bigger, and Impact energy is bigger.Impingement phenomenon can cause larger noise to shake and mechanical shock, right
Equipment is damaged.
The present inventor also devises a kind of multitube separating device in above applying, shown in Figure 6.But such a dress
Put and find in operation, because be to be closely linked between pipe, therefore the space A formed between three pipes is relatively
It is small, because the convex arc that space A is three pipes is formed, therefore space A most of area stenosis, fluid can be caused to be difficult to enter
Pass through, cause fluid short, so as to have impact on the heat exchange of fluid, it is impossible to play good current stabilization effect.Simultaneously as above-mentioned knot
Together, manufacture is difficult for many tube combinations of structure.
In view of the above-mentioned problems, the present invention has carried out improving there is provided a kind of new heat pipe on the basis of above invention, from
And it is low and its problem of exchange heat uneven to solve the coefficient of heat transfer in the case of heat pipe heat exchanging.
The content of the invention
The invention provides a kind of new heat pipe, so as to solve the technical problem above occurred.
To achieve these goals, technical scheme is as follows：
A kind of heat pipe, including evaporation collector, condensation collector, tedge and return duct, the tedge and evaporation collector and
Condensation collector is connected, and the evaporation collector is located at bottom, and the condensation collector is located at top, and the fluid is in evaporation collector
Heat absorption evaporation, enters condensation collector by tedge, is condensed after being exchanged heat in condensation collector, and the fluid of condensation passes through backflow
Pipe returns to evaporation collector；Set in the tedge in separating device, same tedge and multiple separating devices are set, along upper
Spacing between the short transverse of riser, adjacent separating device constantly reduces.
Preferably, along the short transverse of tedge, the ever-reduced amplitude of spacing between adjacent separating device is got over
Come bigger.
Preferably, setting separating device in the tedge, the separating device includes core body and shell, the core body
It is arranged in shell, the shell is connected with heat exchange inside pipe wall, and the core body includes multiple concentric tubes and fin, the rib
Piece connects adjacent concentric tube.
Preferably, setting intercommunicating pore on the concentric tube and fin.
Preferably, the extended line of the fin passes through the center of circle of concentric tube.
Preferably, setting multiple separating devices in tedge, the height that distance rises tube inlet is H, adjacent separation dress
The distance between put is S, S=F1(H) following require, is met：
S’<0,S”>0。
Preferably, setting multiple separating devices in tedge, the height that distance rises tube inlet is H, separating device
Length is C, C=F2(H) following require, is met：
C’>0,C”>0。
Preferably, setting multiple separating devices in tedge, the height that distance rises tube inlet is H, separating device
Annular distance a diameter of D, D=F3(H) following require, is met：
D’<0,D”>0。
Preferably, the rising inside pipe wall sets groove, the shell of the separating device is arranged in groove, described outer
The inwall of shell and the aligning inner of tedge.
Preferably, tedge is welded for multi-segment structure, the junction of multi-segment structure sets separating device.
Preferably, the distance between adjacent separating device is S, the length of separating device is C, and the external diameter of heat exchanger tube is W,
The radius of neighboring concentric pipe is respectively R2And R1, wherein R2>R1, the radian of the circular arc between adjacent fin is h, is met as follows
It is required that：
S/C=a-b*LN (W/E)；
E=((h*R2 2-h*R1 2)/2)1/2；
Wherein LN is logarithmic function, and a, b is parameter, wherein 4.9<a<6.1,1.3<b<2.1；
The spacing of wherein separating device is with the distance between relative two ends of adjacent separating device；
34<W<58mm；
19<C<27mm；
50<S<70mm。
Preferably, a=5.42, b=1.72.
Compared with prior art, the present invention has the advantage that：
1) present invention is changed by the spacing of separating device, when there is Gas- liquid two-phase flow in tedge, augmentation of heat transfer,
Weaken the vibration of tedge simultaneously, reduce noise level.
2) the invention provides a kind of separating device of Novel structure, two-phase fluid is separated with respect to separating device
Into liquid and gas, liquid phase is divided into small liquid group, gas phase is divided into minute bubbles, suppresses the backflow of liquid phase, promotes gas phase suitable
Channel Group is moved, and plays a part of regime flow, the effect with vibration and noise reducing, improves heat transfer effect.Separate relative to multitube and fill
Put, further improve steady flow result, augmentation of heat transfer, and be simple to manufacture.
3) present invention, equivalent to inner area is added in tedge, enhances heat exchange by setting annular and separation device,
Improve heat transfer effect.
4) present invention is because vehicle repair major is split in the whole cross-section location of tedge, it is to avoid only
Tedge internal face is split, thus entirely rise realized on tube section expand liquid-vaqor interface and vapour phase boundary layer with it is cold
But the contact area of wall and strengthen disturbance, reduce noise and vibrations, enhance heat transfer.
5) present invention in tedge short transverse by setting distance, the length of separating device between adjacent separating device
The rule change of the parameter sizes such as degree, the external diameter of annular distance, so as to further reach steady flow result, reduces noise, improves heat exchange effect
Really.
6) present invention by the rule that exchanges heat caused by the change to annular and separation device parameters widely grind
Study carefully, in the case of flow resistance is met, realize the best relation formula of the effect of vibration and noise reducing.
Brief description of the drawings
Fig. 1 is the heat pipe structure schematic diagram of the present invention；
Fig. 2 is separating device cross-sectional structure schematic diagram of the present invention；
Fig. 3 is that separating device of the present invention arranges schematic diagram in tedge；
Fig. 4 is another schematic diagram that separating device of the present invention is arranged in tedge；
Fig. 5 is that separating device of the present invention arranges cross-sectional view in tedge；
Fig. 6 is that separating device of the present invention arranges radian scale diagrams in tedge；
Fig. 7 is the structural representation of the two-phase flow tube shell type heat exchanger in background technology.
In figure：1st, collector is evaporated, 2, condensation collector, 3, tedge, 4, separating device, 41 separating device shells, 42 annular distances,
43 fins, 44 concentric tubes, 5, return duct.
Embodiment
The embodiment to the present invention is described in detail below in conjunction with the accompanying drawings.
Herein, if without specified otherwise, being related to formula, "/" represents division, and "×", " * " represent multiplication.
A kind of heat pipe as shown in Figure 1, including evaporation collector 1, condensation collector 2, tedge 3 and return duct 5, it is described to rise
Pipe 3 is connected with evaporation collector 1 and condensation collector 2, and the evaporation collector 1 is located at bottom, and the condensation collector 2 is located at top,
Fluid heat absorption evaporation in evaporation collector 1, enters condensation collector 2 by tedge 3, is exchanged heat in condensation collector 2
After condense, the fluid of condensation returns to evaporation collector 1 by return duct 5.
As illustrated in figures 4-5, annular and separation device 4 is set in tedge 3.The structure of the annular and separation device 4 is shown in figure
3.As shown in figure 3, the separating device 4 includes core body and shell 41, the core body is arranged in shell 41, the shell with it is upper
Riser inwall is connected, and the core body includes multiple concentric tubes 44 and fin 43, and the fin 43 connects adjacent concentric tube
44.Limited between the concentric tube 44 that adjacent fin 43 and its fin 43 are connected and form annular distance 42.
The present invention sets annular and separation device in heat exchanger tube, by separating device by the liquid and gas in two-phase fluid
Separated, liquid phase is divided into small liquid group, gas phase is divided into minute bubbles, suppressed the backflow of liquid phase, promote the smooth stream of gas phase
It is dynamic, play a part of regime flow, the effect with vibration and noise reducing.Relative to multitube separating device, current stabilization is further improved
Effect, augmentation of heat transfer, and be simple to manufacture.
The present invention, equivalent to interior heat exchange area is added in heat exchanger tube, is enhanced and changed by setting annular and separation device
Heat, improves heat transfer effect.
The present invention is because all cross-section locations by gas-liquid two-phase in all heat exchanger tubes are split, so that whole
Gas-liquid interface and the segmentation of gas phase boundary and the contact area of cooling wall are realized on heat exchange tube section and strengthens disturbance, greatly
Big reduces noise and vibrations, enhances heat transfer.
Preferably, preferably, setting intercommunicating pore on the concentric tube 44 and/or fin 43.
Intercommunicating pore is set between adjacent annular distance, the connection between annular distance 42 is realized by intercommunicating pore.
By setting intercommunicating pore, it is ensured that interconnected between adjacent annular distance, pressure that can uniformly between annular distance,
So that the fluid of high pressure runner flows to low pressure, while can also further separate liquid and gas while flow of fluid, have
Beneficial to further stable two-phase flow.
Preferably, the extended line of the fin passes through the center of circle of concentric tube.
Preferably, being passed through in condensation collector 2 in the fluid in heat exchange pipeline, the heat exchange pipeline and condensation collector 2
Steam is exchanged heat.
Preferably, tedge 3 and evaporation collector 1 are all endothermic sections.
Preferably, along the flow direction (i.e. Fig. 2 short transverse) of fluid in tedge 3, tedge 3 is interior to set many
Individual separating device 4, from the entrance of tedge to the outlet of tedge, the distance between adjacent separating device is shorter and shorter.If away from
It is H from rising with a distance from tube inlet, the distance between adjacent separating device is S, S=F1(H), i.e. S is using height H as variable
Function, S ' is S first order derivative, meets following require：
S’<0；
Main cause is that carrier's liquid is understood in uphill process because of the gas in tedge, in uphill process, on
Riser is constantly heated, and causes the gas in biphase gas and liquid flow more and more, because the vapour phase in stream-liquid two-phase flow is more and more,
Exchange capability of heat in tedge can increase with vapour phase and weaken relatively, and vibrations and its noise also can be continuous with vapour phase increase
Increase.Therefore need the distance between the adjacent separating device of setting shorter and shorter.
In addition, condensation collector this section is exported to from tedge, because the space of this section becomes big, the change in space suddenly
The quick of gas can be caused to flow upwards out and assemble, therefore spatial variations can cause the vapour phase (vapour group) of aggregation from tedge position
Into condensation collector, due to gas (vapour) liquid density contrast, air mass leaves adapter position and will moved rapidly upward, and the former space bit of air mass
Put and the liquid of wall is pushed away while also by rapid resilience and hitting wall by air mass, form impingement phenomenon.Gas (vapour) liquid phase is more not
Continuously, air mass aggregation is bigger, and water hammer energy is bigger.Impingement phenomenon can cause larger noise to shake and mechanical shock, to equipment
Damage.Therefore in order to avoid the generation of this phenomenon, the distance between adjacent separating device now set is shorter and shorter,
So as to constantly separate gas phase and liquid phase in fluid delivery process, so as to reduce vibrations and noise to the full extent.
It is found through experiments that, by above-mentioned setting, vibrations and noise can be both reduced to the full extent, while can carry
High heat transfer effect.
Further preferably, from the entrance of tedge 3 to the outlet of tedge 3, the distance between adjacent separating device is more next
Shorter amplitude is continuously increased.That is S " is S second derivative, meets following require：
S”>0；
It is found through experiments that, by being arranged such, can further reduces by 9% or so vibrations and noise, improves simultaneously
7% or so heat transfer effect.
Preferably, the length of each separating device 4 keeps constant.
Preferably, in addition to the distance between adjacent separating device 4, separating device others parameter (such as length,
Caliber etc.) keep constant.
Preferably, along the short transverse of tedge 3, tedge 3 is interior to set multiple separating devices 4, from tedge 3
Entrance is to the outlet of tedge 3, and the length of separating device 4 is increasingly longer.I.e. the length of separating device is C, C=F2(X), C ' is
C first order derivative, meets following require：
C’>0。
Further preferably, from the entrance of tedge to the outlet of tedge, the length of separating device increasingly longer amplitude
It is continuously increased.That is C " is C second derivative, meets following require：
C”>0；
The change of the distance between for example adjacent separating device of specific reason is identical.
Preferably, the distance between adjacent separating device keeps constant.
Preferably, except the length of separating device is outside one's consideration, separating device others parameters (such as adjacent spacing, caliber
Deng) keep constant.
Preferably, along the short transverse of tedge 3, tedge 3 is interior to set multiple separating devices, from tedge 3
Entrance is to the outlet of tedge 3, and the hydraulic diameter of the annular distance 41 in different separating devices 4 is less and less.That is the ring of separating device
Hole hydraulic diameter is D, D=F3(X), D ' is D first order derivative, meets following require：
D’<0；
Preferably, from the entrance of tedge to the outlet of tedge, the annular distance hydraulic diameter of separating device is less and less
Amplitude be continuously increased.I.e.
D " is D second derivative, meets following require：
D”>0。
The change of the distance between for example adjacent separating device of specific reason is identical.
Preferably, the length of separating device and the distance of adjacent separating device keep constant.
Preferably, in addition to the annular distance hydraulic diameter of separating device, separating device others parameter (such as length, phase
The distance between adjacent separating device etc.) keep constant.
Further preferably, as shown in figure 3, the inside of the tedge 3 sets groove, the shell 42 of the separating device 4 is set
Put in groove.
Preferably, the aligning inner of the inwall of shell 42 and tedge 3.Pass through alignment so that tedge internal face table
Reached on face in approximately the same plane, it is ensured that surface it is smooth.
Preferably, the thickness of shell 42 is less than the depth of groove, it can so cause tedge internal face formation groove,
So as to carry out augmentation of heat transfer.
Further preferably, as shown in figure 4, tedge 3 is welded for multi-segment structure, the junction of multi-segment structure, which is set, to be divided
Every device 4.This mode causes being simple to manufacture for the tedge for setting separating device, cost reduction.
By analysis and experiment learn, the spacing between separating device can not be excessive, it is excessive if cause damping noise reduction
Effect it is bad, while can not be too small, it is too small if cause resistance excessive, similarly, the external diameter of annular distance can not it is excessive or
Too small, the effect for also resulting in damping noise reduction is bad or resistance is excessive, therefore the present invention is preferentially being expired by substantial amounts of experiment
The normal flow resistance of foot (total pressure-bearing is below 2.5Mpa, or the on-way resistance of single riser is less than or equal to 5Pa/M)
In the case of so that being optimal of damping noise reduction, arrange the optimal relation of parameters.
Preferably, preferably, the distance between adjacent separating device is S, the length of separating device is C, heat exchanger tube
External diameter be W, the radius of neighboring concentric pipe is respectively R2And R1, wherein R2>R1, the radian of the circular arc between adjacent fin is
H, meets following require：
S/C=a-b*LN (W/E)；
E=((h*R2 2-h*R1 2)/2)1/2；
Wherein LN is logarithmic function, and a, b is parameter, wherein 4.9<a<6.1,1.3<b<2.1；
34<W<58mm；
19<C<27mm；
50<S<70mm。
Preferably, 5.3<a<5.6,1.5<b<1.8.
Preferably, a=5.42, b=1.72.
The interval S of wherein separating device is with the distance between relative two ends of adjacent separating device；Above separate dress
The tail end put and the distance between front end of separating device below.Referring specifically to Fig. 4 mark.
Shell 41 actually is considered as into outermost concentric tube in above formula to participate in calculating together.
Radian h is with the radian of the medium line restriction of fin 43, referring to Fig. 6；The radius of concentric tube is respectively R2And R1Be with
The internal diameter of concentric tube and the average value of external diameter are calculated.
Preferably, rising length of tube L between 3000-5500mm.Further preferably, between 3500-4500mm.
By the preferred of the optimal geometric scale of above-mentioned formula, it can realize under the conditions of meeting normal flow resistance,
Damping noise reduction reaches optimum efficiency.
Further preferably, as W/R increase, a constantly reduce, b constantly increases.
For other parameters, the parameter such as tube wall, housing wall thickness is set according to normal standard.
Preferably, hot tube fluid is water.
Preferably, annular distance 42 extends in the whole length direction of separating device 4.I.e. the length of annular distance 42 is equal to separate and filled
Put 4 length.
Preferably, the caliber of the evaporation collector 1 is less than the caliber of condensation collector 2.
The internal diameter for evaporating collector is R1, and the internal diameter of condensation collector is R2, is used as preferably then 0.45<R1/R2<0.88.
, can further augmentation of heat transfer by above-mentioned setting, it is possible to increase more than 7% heat exchange efficiency.
Although the present invention is disclosed as above with preferred embodiment, the present invention is not limited to this.Any art technology
Personnel, without departing from the spirit and scope of the present invention, can make various changes or modifications, therefore protection scope of the present invention should
It is defined when by claim limited range.
Claims (9)
1. a kind of heat pipe, including evaporation collector, condensation collector, tedge and return duct, the tedge is with evaporating collector and cold
Aggegation pipe is connected, and the evaporation collector is located at bottom, and the condensation collector is located at top, and the fluid is inhaled in evaporation collector
Thermal evaporation, enters condensation collector by tedge, is condensed after being exchanged heat in condensation collector, the fluid of condensation passes through return duct
Return to evaporation collector；Characterized in that, setting separating device in the tedge, multiple separation dresses are set in same tedge
Put, along the short transverse of tedge, the spacing between adjacent separating device constantly reduces.
2. heat pipe as claimed in claim 1, it is characterised in that along the short transverse of tedge, between adjacent separating device
The ever-reduced amplitude of spacing it is increasing.
3. heat pipe as claimed in claim 1, it is characterised in that separating device, the separating device are set in the tedge
Including core body and shell, the core body is arranged in shell, and the shell is connected with heat exchange inside pipe wall, and the core body includes
Multiple concentric tubes and fin, the fin connect adjacent concentric tube.
4. heat pipe as claimed in claim 3, it is characterised in that intercommunicating pore is set on the concentric tube and fin.
5. heat pipe as claimed in claim 3, it is characterised in that the extended line of the fin passes through the center of circle of concentric tube.
6. heat pipe as claimed in claim 2, it is characterised in that the rising inside pipe wall sets groove, the separating device
Shell is arranged in groove, the inwall of the shell and the aligning inner of tedge.
7. heat pipe as claimed in claim 6, it is characterised in that tedge is welded for multi-segment structure, the company of multi-segment structure
Meet place and separating device is set.
8. heat pipe as claimed in claim 3, it is characterised in that the distance between adjacent separating device is S, the length of separating device
Spend for C, the external diameter of heat exchanger tube is W, and the radius of neighboring concentric pipe is respectively R2And R1, wherein R2>R1, between adjacent fin
The radian of circular arc is h, meets following require：
S/C=a-b*LN (W/E)；
E=((h*R2 2-h*R1 2)/2)1/2；
Wherein LN is logarithmic function, and a, b is parameter, wherein 4.9<a<6.1,1.3<b<2.1；
The spacing of wherein separating device is with the distance between relative two ends of adjacent separating device；
34<W<58mm；
19<C<27mm；
50<S<70mm。
9. heat pipe as claimed in claim 8, it is characterised in that a=5.42, b=1.72.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810488378.9A CN108827045B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of uniform pressure |
| CN201710294949.0A CN107144161B (en) | 2017-04-28 | 2017-04-28 | The annular and separation device loop circuit heat pipe of spacing variation in a kind of short transverse |
| CN201810489936.3A CN108827047B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe |
| CN201810489115.XA CN108827046B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of multi-segment structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710294949.0A CN107144161B (en) | 2017-04-28 | 2017-04-28 | The annular and separation device loop circuit heat pipe of spacing variation in a kind of short transverse |
Related Child Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810489115.XA Division CN108827046B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of multi-segment structure |
| CN201810488378.9A Division CN108827045B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of uniform pressure |
| CN201810489936.3A Division CN108827047B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107144161A true CN107144161A (en) | 2017-09-08 |
| CN107144161B CN107144161B (en) | 2018-07-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810489115.XA Expired - Fee Related CN108827046B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of multi-segment structure |
| CN201810489936.3A Expired - Fee Related CN108827047B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe |
| CN201810488378.9A Expired - Fee Related CN108827045B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of uniform pressure |
| CN201710294949.0A Expired - Fee Related CN107144161B (en) | 2017-04-28 | 2017-04-28 | The annular and separation device loop circuit heat pipe of spacing variation in a kind of short transverse |
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| CN201810489115.XA Expired - Fee Related CN108827046B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of multi-segment structure |
| CN201810489936.3A Expired - Fee Related CN108827047B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe |
| CN201810488378.9A Expired - Fee Related CN108827045B (en) | 2017-04-28 | 2017-04-28 | A kind of loop circuit heat pipe of uniform pressure |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109489270A (en) * | 2018-08-05 | 2019-03-19 | 青岛鑫众合贸易有限公司 | A kind of trough type solar heat-collector system at stabilising arrangement interval |
| CN110806024A (en) * | 2018-08-05 | 2020-02-18 | 青岛鑫众合贸易有限公司 | Trough type solar heat collector system with size of stabilizing device |
| CN111238273A (en) * | 2017-08-03 | 2020-06-05 | 山东大学 | Rod-fin loop heat pipe with variable distance |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107131781B (en) * | 2017-05-09 | 2018-10-19 | 山东大学 | A kind of variation of length can not condensing body annular and separation device heat exchanger |
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- 2017-04-28 CN CN201810488378.9A patent/CN108827045B/en not_active Expired - Fee Related
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| CN2901053Y (en) * | 2006-04-29 | 2007-05-16 | 林国策 | Small low pressure steam boiler |
| CN101639374A (en) * | 2009-08-26 | 2010-02-03 | 姚贤卿 | Multiphase flow rectifying device |
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| CN111238273A (en) * | 2017-08-03 | 2020-06-05 | 山东大学 | Rod-fin loop heat pipe with variable distance |
| CN109489270A (en) * | 2018-08-05 | 2019-03-19 | 青岛鑫众合贸易有限公司 | A kind of trough type solar heat-collector system at stabilising arrangement interval |
| CN109489270B (en) * | 2018-08-05 | 2020-02-18 | 青岛鑫众合贸易有限公司 | Trough type solar heat collector system with interval stabilizing devices |
| CN110806024A (en) * | 2018-08-05 | 2020-02-18 | 青岛鑫众合贸易有限公司 | Trough type solar heat collector system with size of stabilizing device |
| CN110806024B (en) * | 2018-08-05 | 2020-08-28 | 伟迈云科技股份有限公司 | Trough type solar heat collector system with size of stabilizing device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108827047A (en) | 2018-11-16 |
| CN107144161B (en) | 2018-07-13 |
| CN108827046A (en) | 2018-11-16 |
| CN108827047B (en) | 2019-05-07 |
| CN108827046B (en) | 2019-05-07 |
| CN108827045B (en) | 2019-05-07 |
| CN108827045A (en) | 2018-11-16 |
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