CN110132036A - A kind of method that accumulation of heat penetrates through dimensionally-optimised design - Google Patents
A kind of method that accumulation of heat penetrates through dimensionally-optimised design Download PDFInfo
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- CN110132036A CN110132036A CN201910164688.XA CN201910164688A CN110132036A CN 110132036 A CN110132036 A CN 110132036A CN 201910164688 A CN201910164688 A CN 201910164688A CN 110132036 A CN110132036 A CN 110132036A
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- heat
- pipe
- storage heater
- vertical
- vertical pipe
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
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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
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Central Heating Systems (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention provides a kind of methods that accumulation of heat penetrates through dimensionally-optimised design, including storage heater, the evaporation ends of heat pipe are arranged in storage heater, the storage heater is arranged in heat source, the container on evaporation ends top is arranged in the condensation end of heat pipe, the evaporation ends include the more evaporation tubes extended downwardly, pipe copper pipe is set between the adjacent evaporation tube, pipe copper pipe takes under type to be such as designed: the distance at the center apart from storage heater is S, the size of pipe copper pipe is set according to following rule: C (S), then C ' (S) > 0.The present invention is reached as soon as possible in fluid thermal histories by thermal balance by that can guarantee to the optimization design for taking pipe copper tube size.
Description
Technical field
The present invention relates to a kind of storage heater technology more particularly to a kind of storage heaters of Novel structure.
Background technique
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 known as the heat transfer element of " heat pipe ", it takes full advantage of heat-conduction principle and phase transformation is situated between
The heat of thermal objects is transmitted to outside heat source rapidly by the quick thermal transport property of matter through heat pipe, and the capacity of heat transmission is more than to appoint
The capacity of heat transmission of what known metal.
The industries such as aerospace, military project were widely used in front of hot pipe technique, since being introduced into radiator manufacturing, so that
People change the mentality of designing of traditional heat sinks, get rid of the list for obtaining more preferable heat dissipation effect by high air quantity motor merely
One radiating mode makes radiator obtain satisfied heat transfer effect using hot pipe technique, opens heat dissipation industry new world.At present
Heat pipe is widely used in various heat exchange equipments, including nuclear power field, such as the UTILIZATION OF VESIDUAL HEAT IN of nuclear power etc..
In the prior art, the shape of heat pipe affects the endotherm area of evaporation ends, therefore general evaporation ends heat absorption range ratio
It is smaller, it sometimes needs that multiple heat pipes are arranged in heat source to meet heat absorption demand；And more evaporation ends there are when, it is each
Evaporation ends can generate the non-uniform phenomenon of heat absorption because the position in heat source is different.
In view of the above-mentioned problems, the present invention is improved on the basis of invention in front, a kind of new heat pipe knot is provided
Structure makes full use of heat source, reduces energy consumption, improves exploitation effect.
Summary of the invention
The present invention provides a kind of new heat pipe structures, extend the heat absorption range of evaporation ends, energy saving.
To achieve the goals above, technical scheme is as follows:
A kind of heat pipe, including vertical portion, horizontal component and vertical pipe, wherein the bottom end of vertical portion is connected to horizontal part
Point, direction of the horizontal component from the bottom end of vertical portion away from vertical portion extends, and the horizontal component lower part connects
Lead to multiple vertical pipes, wherein vertical pipe is the evaporation ends of heat pipe, and vertical portion is the condensation end of heat pipe.
Preferably, the horizontal component is flat tube structure, vertical pipe is circular tube structure.
Preferably, horizontal component is square structure.
Preferably, the vertical pipe is multiple rows of, wherein adjacent two rows are to be staggered in arrangement.
Preferably, the center of circle of vertical pipe and two closed on the vertical pipe center of circle of adjacent row constitute isosceles triangle, institute
State vertical pipe the center of circle be located at isosceles triangle apex angle point position.
Preferably, the outer diameter of vertical pipe is d, the distance between adjacent vertical pipe center of circle of same row is L, vertical pipe
It is A that 3 center of circle and two closed on the vertical pipe center of circle of adjacent row, which constitute the apex angle of isosceles triangle, then meets claimed below:
Sin (A)=a-b*Ln (d/L), wherein Ln is logarithmic function, and a, b are parameters, meets following require:
0.095<a<0.105,0.29<b<0.31；0.1<d/L<0.7.
Preferably, gradually becoming smaller with d/L, a is increasing, and b is increasing.
Preferably, 15 ° < A < 80 °.
Preferably, 20 ° < A < 40 °.
Preferably, 0.2 < d/L < 0.5.
Compared with prior art, the present invention has the advantage that:
1) structure of the evaporation ends of opposite heat tube of the present invention is improved, and the evaporation ends of heat pipe are extended to farther side
To so that the endotherm area of the evaporation ends of heat pipe increases, can expanding in this way in the case where not changing the condensation end volume of heat pipe
The heat absorption range of big heat pipe, can be absorbed the heat of heat source distalmost end.Heat pipe evaporation ends and condensation in compared with the existing technology
End is consistent size, can be improved 40% or more heat exchange efficiency.The volume and occupied area of heat exchanger are reduced simultaneously, so that
It is compact-sized.
2) communicating pipe is arranged in adjacent evaporation ends in the present invention, pressure can be caused different in the heated difference of vertical pipe
In the case of, the fluid in evaporation ends that pressure can be made big quickly flows to the small evaporation ends of pressure, to keep whole pressure
Power is balanced, avoids hot-spot or supercooling.
3) research of a large amount of numerical simulation and experiment has been carried out, distributed architecture of the opposite heat tube in storage heater has carried out most
Excellent structure, and the best relative formula that heat pipe is distributed is obtained by research, the distribution of heat pipe is further increased, reaches optimal
Heat absorption reduces cost.
4) communicating pipe is arranged in the present invention between adjacent heat pipe, realizes that the pressure between heat pipe is balanced, heat exchange is balanced.
Detailed description of the invention
Fig. 1 is heat pipe structure schematic diagram of the present invention.
Fig. 2 is schematic diagram of the Fig. 1 from bottom.
Fig. 3 is the heat pipe partial structural diagram of present invention setting communicating pipe.
Fig. 4 is heat pipe specific embodiment structural schematic diagram of the present invention.
Fig. 5 is the structural schematic diagram that communicating pipe is arranged between the heat pipe of the present invention of Fig. 4.
Fig. 6 is the partial enlargement mark schematic diagram of Fig. 2.
In figure: 8 communicating pipe of 1 vertical portion, 2 horizontal component, 3 vertical pipe, 4 storage heater, 5 cold source, 7 communicating pipe of 6 heat source 9 container
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 heat pipe, including vertical portion 1, horizontal component 2 and vertical pipe 3, wherein the bottom end of vertical portion 1 is connected to horizontal
Part 2, direction of the horizontal component 2 from the bottom end of vertical portion 1 away from vertical portion 1 extend, the horizontal component 2
Lower part is connected to multiple vertical pipes 3, and wherein vertical pipe 3 is the evaporation ends of heat pipe, and vertical portion 1 is the condensation end of heat pipe.
Heat pipe of the present invention absorbs heat in operation, by vertical pipe 3 from heat source, then the fluid in vertical pipe 3 into
Row evaporation, enters vertical portion by horizontal component, then rejects heat to cold source in vertical portion, fluid carries out cold
It is solidifying, vertical pipe 3 is entered back by the effect of gravity.
The structure of the evaporation ends by the way that heat pipe is arranged of opposite heat tube of the present invention is improved, and the evaporation ends of heat pipe are extended
To farther direction, in the case where not changing the condensation end volume of heat pipe, so that the endotherm area of the evaporation ends of heat pipe increases,
The heat absorption range that heat pipe can be expanded in this way, can be absorbed the heat of heat source distalmost end.Heat pipe in compared with the existing technology steams
Originator and condensation end are consistent size, can be improved 45% or more heat exchange efficiency.The volume of condensation end is reduced simultaneously and is accounted for
Ground area, so that compact-sized.
In addition, evaporation ends of the present invention by the multiple vertical pipes 3 of setting as heat pipe, so that each vertical pipe 3 is used as one
The absorption of heat is added in each and every one independent absorbing pipe, also increases the endotherm area of integral heat pipe evaporation ends.
Preferably, the heat source can be soil or boiler exhaust gas etc..
Preferably, the cold source is water or air.
Preferably, the horizontal component 2 is flat tube structure, vertical pipe 3 is circular tube structure.By the way that horizontal component is arranged
For flat tube structure, the distribution of vertical pipe 3 can be increased, further increase the absorption of heat.
Further preferably, horizontal component 2 is square structure.
Preferably, as shown in Fig. 2, the vertical pipe 3 is multiple rows of, wherein adjacent two rows are to be staggered in arrangement.Pass through mistake
Column arrangement, can be further improved the caloric receptivity of heat pipe.
Preferably, vertical pipe 3 is located at the extended line of the middle line of the center of circle connecting line segment of the adjacent upright pipe 3 of adjacent row
On.I.e. two closed on vertical pipe, 3 center of circle in the center of circle of vertical pipe 3 and adjacent row constitutes isosceles triangle, the vertical pipe
The center of circle is located at the position of the point of isosceles triangle apex angle.
Preferably, as shown in figure 3, communicating pipe 8 is arranged between at least two adjacent vertical pipes 3.It finds under study for action,
During vertical section heat absorption, it may appear that the absorption heat of the absorbing pipe of different location is different, leads to the pressure between vertical pipe 3
Power or temperature are different, will lead to straightened portion pipe 3 in this way and are heated excessively high, cause the lost of life, once a vertical pipe 3 occurs
Problem may cause the problem of entire heat pipe is not available.The present invention is set by largely studying in adjacent vertical pipe
Communicating pipe 8 is set, can make the vertical pipe 3 that pressure is big in the case where vertical pipe is heated different to cause pressure different
Interior fluid quickly flows to the small vertical pipe 3 of pressure, to keep integral pressure balanced, avoids hot-spot or supercooling.
Preferably, multiple communicating pipes 8 are arranged between adjacent vertical pipe 3 from 3 lower part of vertical pipe to 3 top of vertical pipe.
By the way that multiple communicating pipes are arranged, fluid continuous counterpressure in heat absorption evaporation process is enabled to, guarantees entire vertical pipe
Interior pressure is balanced.
Preferably, constantly reducing the distance between adjacent communicating pipe 8 from 3 lower part of vertical pipe to 3 top of vertical pipe.This
Purpose is in order to which more communicating pipes are arranged, because of flowing up with fluid, fluid is constantly heated, as fluid is continuous
It is heated, it is heated more and more uneven in different thermal-collecting tubes, therefore by above-mentioned setting, can guarantee in process fluid flow
In reach as soon as possible pressure equilibrium.
Preferably, from 3 lower part of vertical pipe to 3 top of vertical pipe, the distance between adjacent communicating pipe ever-reduced width
It spends increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent in process fluid flow to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, from 3 lower part of vertical pipe to 3 top of vertical pipe, the diameter of communicating pipe 8 is continuously increased.This purpose be for
Setting guarantees bigger connection area, because of flowing up with fluid, fluid is constantly heated, as fluid is continuous
It is heated, it is heated more and more uneven in different thermal-collecting tubes, therefore by above-mentioned setting, it can guarantee in process fluid flow
Reach pressure equilibrium as soon as possible.
Preferably, the ever-increasing amplitude of the diameter of communicating pipe 8 is increasingly from 3 lower part of vertical pipe to 3 top of vertical pipe
Greatly.Be found through experiments that, above-mentioned setting, can guarantee in process fluid flow it is more excellent faster reach pressure equilibrium.This
It is the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Fig. 4 illustrates a kind of heat pipe using system, preferably, as shown in figure 4, the vertical pipe 3 of heat pipe is arranged in accumulation of heat
In device 4.The storage heater 4 is arranged in heat source.The heat source can be geothermal energy.
Preferably, the fusing point of heat-storing material is 60-80 degrees Celsius in the storage heater 4, preferably 65 degrees Celsius.
Preferably, the heat-storing material in the storage heater 4 is paraffin.
The present invention can be got up the heat storage in heat source 6 by setting storage heater 4, and because of the heat of storage heater
It melts bigger, therefore more heats can be stored, therefore heat pipe can more fully utilize the heat of dry heat source 6, and
Because storage heater is arranged, storage heater and 6 contact area of heat source are bigger, and can greatly reduce between heat pipe and heat source 6
Thermal contact resistance, easy for installation, endothermic effect will be much better than heat pipe and individually be placed in heat source 6.Therefore pass through setting storage heater
The heat absorption efficiency of heat pipe can be greatly improved.It is found through experiments that, by the way that storage heater is arranged, the heating of 15-20% can be improved
Efficiency can further save the energy.
Preferably, the heat source is the geothermal energy of xeothermic rock stratum, the cold source is water, and heat pipe is used for the exploitation of shale gas
Middle heating water generates steam, introduces steam into rammell to carry out the exploitation of shale gas.
Preferably, the cross section of the storage heater 4 is square structure, the cross-sectional area of the storage heater 4 is greater than cold source
The cross-sectional area of the container 9 at place.It is greater than the cross-sectional area of the container 9 where cold source by the cross-sectional area of storage heater 4, it can be with
The further heat exchange area for increasing storage heater and heat source 6, and more heats can be stored, further satisfaction heating is wanted
It asks.
Preferably, the cross-sectional area of the storage heater 4 and container 9 is square structure.The side length of storage heater 4, which is greater than, to be held
The side length of device 9.
Preferably, the cross-sectional area of the storage heater 4 is 10-26 times of 9 cross-sectional area of container, preferably 18 times.
Preferably, from the center of storage heater 4 to the direction of the outer wall of storage heater, the storage of the heat-storing material in storage heater 4
Thermal energy power gradually dies down.
Gradually changing for the heat storage capacity of heat-storing material is taken, can be further improved heat storage capacity, it is vertical to can be realized
Pipe 3 is evenly heated.Because more arriving storage heater outer wall, then because directly being contacted with heat source, temperature highest herein, accumulation of heat
Material can be directly heated, and after heat-storing material is by abundant accumulation of heat, heat can be transmitted to the inside of storage heater.Pass through storage heater
The variation of the heat storage capacity of heat-storing material, it is ensured that, can be inside by heat at once after external heat-storing material reaches accumulation of heat saturation
Portion's transmitting guarantees that inside also stores heat.In this way, different location of the vertical pipe 3 in storage heater can sufficiently absorb heat, avoid
Heat pipe overheat, the heat absorption of some heat pipes not enough, guarantees that the heat absorption of integral heat pipe is uniform, avoids part superheated steam from damaging, cause
Product it is difficult in maintenance.It is arranged in this way, the service life that can be heat pipe entirety reaches identical.Make cold source also whole simultaneously
Body homogeneous heating.
Preferably, from the center of storage heater 4 to the outer wall direction of storage heater 4, the heat storage capacity of heat-storing material gradually subtracts
Weak amplitude gradually increases.By experiment and numerical simulation discovery, this set is taken, can be further improved the heat absorption of heat pipe
The uniformity.
Preferably, communicating pipe, 8 quantity was continuously increased from the center of storage heater 4 to the outer wall direction of storage heater 4.This mesh
Be in order to which more communicating pipes are arranged because amount of stored heat is most closer to the outer wall direction of storage heater 4, fluid is heated also more,
Steam pressure in vertical pipe 3 is also bigger, therefore by above-mentioned setting, can guarantee to reach as soon as possible in fluid thermal histories
Pressure is balanced.
Preferably, from the center of storage heater 4 to the outer wall direction of storage heater 4, communicating pipe the ever-increasing amplitude of 8 quantity
It is increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent in fluid thermal histories to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
As preferably from the center of storage heater 4 to the outer wall direction of storage heater 4, the diameter of communicating pipe 8 is continuously increased.This mesh
Be in order to be arranged and guarantee bigger connection area because amount of stored heat is most closer to the outer wall direction of storage heater 4, fluid by
Heat is also more, and the steam pressure in vertical pipe 3 is also bigger, therefore by above-mentioned setting, can guarantee in fluid thermal histories to the greatest extent
Fast reaches pressure equilibrium.
Preferably, from the center of storage heater 4 to the outer wall direction of storage heater 4, the ever-increasing width of the diameter of communicating pipe 8
It spends increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent in process fluid flow to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Accumulation of heat paraffin is loaded in storage heater.Paraffin class phase change heat storage material have latent heat of phase change it is high, almost without
Surfusion, melt when steam pressure is low, be not susceptible to chemical reaction and chemical stability preferably, without mutually separate and corrosion
The advantages such as property and price are low, become the first choice of heat-storing material.Paraffin embeds vertical pipe 3.Vertical pipe 3, which absorbs, comes from storage heater
The heat of interior paraffin realizes the heating to cold source in top vertical portion heat release.
Pass through numerical simulation and experiment discovery, the distance between vertical pipe 3, between distance and adjacent row including same row
Distance cannot be too small, it is too small to will lead to that heat pipe distribution is excessive, cause the caloric receptivity of every heat pipe insufficient, it is excessive to will lead to heat pipe
Distribution is very little, causes heat pipe to overheat, therefore the application sums up by a large amount of numerical simulation and experiment and carrys out heat pipe vertical pipe 3
The distribution of the optimization of distribution, the deficiency so that heat pipe can neither recept the caloric, and it is excessive to recept the caloric.
As shown in fig. 6, the outer diameter of vertical pipe 3 is d, the distance between adjacent 3 center of circle of vertical pipe of same row is L, is erected
It is A that the center of circle of straight tube 3 and two closed on vertical pipe, 3 center of circle of adjacent row, which constitute the apex angle of isosceles triangle, then meets following
It is required that:
Sin (A)=a-b*Ln (d/L), wherein Ln is logarithmic function, and a, b are parameters, meets following require:
0.095<a<0.105,0.29<b<0.31；
Further preferably, the a=0.1016, b=0.3043.
Preferably, gradually becoming smaller with d/L, a is increasing, and b is increasing.
Preferably, 15 ° < A < 80 °.
Further preferably, 20 ° < A < 40 °.
0.1 < d/L < 0.7, further preferably, 0.2 < d/L < 0.5.
Above-mentioned empirical equation is obtained by a large amount of numerical simulations and experiment, the structure obtained by above-mentioned relation formula, energy
It is enough to realize the heat pipe structure optimized, and pass through verification experimental verification, error is substantially within 3%.
The heat absorption capacity 900-1100W of heat pipe, further preferably 1000W；
100-120 degrees Celsius of the temperature of heat source, further preferably 110 DEG C.
Heat pipe horizontal component shown in Fig. 2 is preferably square, side length be 400-600 millimeters, further preferably 500
Millimeter.
3 outside diameter d of vertical pipe is 9-12 millimeters, further preferably 11mm.
Preferably, as shown in figure 4, including two heat pipes in the system, the horizontal component 2 of described two heat pipes divides
Do not extend by two symmetrical heat pipes of setting towards opposite direction, can absorb heat in different directions, meet the need of heat exchange
It asks.
Preferably, as shown in figure 5, communicating pipe 7 is arranged between the vertical pipe 3 of two heat pipes adjacent to each other.By setting
Communicating pipe is set, can be even to avoid uneven heating between heat pipe, it realizes that the pressure between heat pipe is balanced, avoids between different heat pipes
Defect caused by uneven heating is even.
Preferably, constantly reducing the distance between adjacent communicating pipe 7 from 3 lower part of vertical pipe to 3 top of vertical pipe.This
Purpose is in order to which more communicating pipes are arranged, because of flowing up with fluid, fluid is constantly heated, as fluid is continuous
It is heated, it is heated more and more uneven in different heat pipes, therefore by above-mentioned setting, can guarantee in process fluid flow
Reach pressure equilibrium as soon as possible.
Preferably, from 3 lower part of vertical pipe to 3 top of vertical pipe, the distance between adjacent communicating pipe 7 ever-reduced width
It spends increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent in process fluid flow to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, from 3 lower part of vertical pipe to 3 top of vertical pipe, the diameter of communicating pipe 7 is continuously increased.This purpose be for
Setting guarantees bigger connection area, because of flowing up with fluid, fluid is constantly heated, as fluid is continuous
It is heated, it is heated more and more uneven in different heat pipes, therefore by above-mentioned setting, it can guarantee in process fluid flow to the greatest extent
Fast reaches pressure equilibrium.
Preferably, the ever-increasing amplitude of the diameter of communicating pipe 7 is increasingly from 3 lower part of vertical pipe to 3 top of vertical pipe
Greatly.Be found through experiments that, above-mentioned setting, can guarantee in process fluid flow it is more excellent faster reach pressure equilibrium.This
It is the optimal mode of communicating got and largely studying pressure changes in distribution rule.
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 (2)
1. the evaporation ends of a kind of method that accumulation of heat penetrates through dimensionally-optimised design, including storage heater, heat pipe are arranged in storage heater, institute
Storage heater is stated to be arranged in heat source, the condensation end of heat pipe is arranged in the container on evaporation ends top, the evaporation ends include more to
Pipe copper pipe is arranged between the adjacent evaporation tube for the evaporation tube of lower extension, and pipe copper pipe takes under type to be such as designed:
The distance at the center apart from storage heater is S, and the size of pipe copper pipe is set according to following rule: C (S), then C ' (S) > 0.
2. the method for optimization design as described in claim 1, which is characterized in that then C " (S) > 0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201910164688.XA CN110132036B (en) | 2018-02-13 | 2018-02-13 | Method for optimally designing heat storage through size |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201810148416.6A CN108225070B (en) | 2018-02-13 | 2018-02-13 | A kind of heat pipe that internal pressure distribution is balanced |
| CN201910164688.XA CN110132036B (en) | 2018-02-13 | 2018-02-13 | Method for optimally designing heat storage through size |
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| CN110132036A true CN110132036A (en) | 2019-08-16 |
| CN110132036B CN110132036B (en) | 2020-10-30 |
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| CN201910164728.0A Active CN110220403B (en) | 2018-02-13 | 2018-02-13 | Method for coherent diameter distribution of multi-heat-pipe heat accumulator |
| CN201910164675.2A Active CN110132035B (en) | 2018-02-13 | 2018-02-13 | Method for distributing coherent number of multi-heat-pipe heat accumulator |
| CN201810148416.6A Active CN108225070B (en) | 2018-02-13 | 2018-02-13 | A kind of heat pipe that internal pressure distribution is balanced |
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| CN201810148416.6A Active CN108225070B (en) | 2018-02-13 | 2018-02-13 | A kind of heat pipe that internal pressure distribution is balanced |
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- 2018-02-13 CN CN201910164675.2A patent/CN110132035B/en active Active
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- 2018-02-13 CN CN201910164688.XA patent/CN110132036B/en active Active
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| WO2013025640A2 (en) * | 2011-08-12 | 2013-02-21 | Mcalister Technologies, Llc | Geothermal energization of a non-combustion chemical reactor and associated systems and methods |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN110132035B (en) | 2020-10-30 |
| CN108225070B (en) | 2019-06-11 |
| CN110220403B (en) | 2020-10-30 |
| CN110132036B (en) | 2020-10-30 |
| CN110132035A (en) | 2019-08-16 |
| CN110220403A (en) | 2019-09-10 |
| CN108225070A (en) | 2018-06-29 |
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