CN109373792B - Heat pipe with optimally designed included angle of free end face - Google Patents
Heat pipe with optimally designed included angle of free end face Download PDFInfo
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- CN109373792B CN109373792B CN201811388096.8A CN201811388096A CN109373792B CN 109373792 B CN109373792 B CN 109373792B CN 201811388096 A CN201811388096 A CN 201811388096A CN 109373792 B CN109373792 B CN 109373792B
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- 230000008020 evaporation Effects 0.000 claims abstract description 9
- 238000001704 evaporation Methods 0.000 claims abstract description 9
- 238000005485 electric heating Methods 0.000 claims description 40
- 239000012530 fluid Substances 0.000 claims description 30
- 230000005494 condensation Effects 0.000 claims description 8
- 238000009833 condensation Methods 0.000 claims description 8
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 238000013461 design Methods 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 description 24
- 238000012546 transfer Methods 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000007667 floating Methods 0.000 description 4
- 238000005086 pumping Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000013529 heat transfer fluid Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000000191 radiation effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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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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- 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
- F28D15/06—Control arrangements therefor
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- Sustainable Development (AREA)
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- 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 heat pipe which comprises a lower collecting pipe, an upper collecting pipe, a coil pipe and a return pipe, wherein the coil pipe is communicated with the lower collecting pipe and the upper collecting pipe, the lower collecting pipe is an evaporation end, and an included angle c formed by a plane where a first free end is located and a plane where a central line of the lower collecting pipe and a central line of the upper collecting pipe are located is 40-65 degrees; the plane of the second free end forms an included angle b of 55-65 degrees with the plane of the central lines of the lower header and the upper header. According to the invention, through the design of the preferable included angle, the vibration of the free end is optimal, and thus the heat exchange efficiency is optimal.
Description
Technical Field
The invention belongs to the field of heat pipes, and particularly relates to a coil pipe heat pipe.
Background
The heat pipe technology is a heat transfer element called a heat pipe invented by George Grover (George Grover) of national laboratory of Los Alamos (Los Alamos) in 1963, fully utilizes the heat conduction principle and the rapid heat transfer property of a phase change medium, quickly transfers the heat of a heating object to the outside of a heat source through the heat pipe, and the heat conduction capability of the heat transfer element exceeds the heat conduction capability of any known metal.
The heat pipe technology is widely applied to the industries of aerospace, military industry and the like, and since the heat pipe technology is introduced into the radiator manufacturing industry, the design idea of the traditional radiator is changed for people, the single heat radiation mode that a high-air-volume motor is used for obtaining a better heat radiation effect is avoided, the heat pipe technology is adopted for enabling the radiator to obtain a satisfactory heat exchange effect, and a new place in the heat radiation industry is opened up. At present, the heat pipe is widely applied to various heat exchange devices, including the field of nuclear power, such as the utilization of waste heat of nuclear power.
The heat pipe in the prior art is in a static state in the heat exchange process, only depends on the heat dissipation of the condensation end of the heat pipe, and the improvement of a plurality of inventions is only the improvement of the structure of the enhanced heat transfer of the condensation end. On the other hand, the prior art cannot realize automatic temperature control, so that the heat exchange efficiency of the heat pipe is low.
Aiming at the problems, the invention provides a novel heat pipe, thereby solving the problems of low heat exchange coefficient and uneven heat exchange under the condition of heat exchange of the heat pipe.
Disclosure of Invention
The present invention provides a new heat pipe to solve the above-mentioned technical problems.
In order to achieve the purpose, the technical scheme of the invention is as follows:
a heat pipe comprising a lower header, an upper header, a heat exchange tube bundle and a return tube, the heat exchange tube bundle being in communication with the lower header and the upper header, the lower header being an evaporator end, the condenser end comprising an upper header, the fluid being evaporated by thermal absorption in the lower header and condensed in the upper header, the condensed fluid passing through the return tube back to the lower header; the return pipe is connected with the positions of the two side ends of the lower header and the upper header, and the lower header is internally provided with an electric heating device; the heat pipe also includes a temperature control system for controlling the temperature of the vapor within the heat pipe.
Preferably, a temperature sensor is arranged in the heat exchange tube bundle and is used for measuring the temperature of steam generated in the heat exchange tube bundle; the heating rod is electrified for heating, and after being heated, the fluid is quickly atomized in a vacuum state and is filled in each coil pipe, the upper collecting pipe and the lower collecting pipe; when the temperature measured by the temperature sensor reaches a preset first temperature, the temperature controller controls the heating device to stop heating, and when the temperature measured by the temperature sensor is lower than a preset second temperature, the temperature controller controls the heating rod to heat.
Preferably, the first temperature and the second temperature are the same.
Preferably, the first temperature is 5-20 degrees celsius higher than the second temperature.
Preferably, the first temperature is 8-13 degrees celsius higher than the second temperature.
Preferably, the electric heating device is an electric heating rod.
Preferably, the electric heating means is located at a position between the middle position and the bottom of the lower header.
Preferably, the number of the coil pipes is multiple, and the multiple coil pipes are in a parallel structure.
Preferably, the inner diameter of the lower header is R1, the inner diameter of the upper header is R2, the outer diameter of the heat exchange tube is D, the distance between the center lines of the adjacent heat exchange tubes is L, and the following relations are satisfied:
10 (R1/R2) = a-b Ln (5D/L), where Ln is a logarithmic function, a, b are coefficients,
wherein 17.03< a <18.12,9.15< b < 10.11;
55mm<R1<100mm；95mm<R2<145mm；
25mm<D<80mm；40mm<L<120mm；
0.45<R1/R2<0.88；
0.5<D/L<0.7。
preferably, a =17.54 and b = 9.68.
Preferably, the central lines of the plurality of circular arc-shaped heat exchange tubes are circular arcs of concentric circles.
Preferably, the return pipe connects the lower header and the upper header at positions of both side ends thereof.
Preferably, the concentric circles are circles centered on the center of the cross section of the upper header.
Preferably, the pipe diameter of the lower header is smaller than that of the upper header.
Preferably, the inner diameter of the lower header is R1, and the inner diameter of the upper header is R2, so that 0.45< R1/R2< 0.88.
Preferably, the number of the coil pipes is multiple, and the multiple coil pipes are in a parallel structure.
Preferably, the distance between adjacent heat exchange tubes becomes larger as the distance from the center of the lower header becomes larger.
Compared with the prior art, the plate heat exchanger and the heat exchange pipe wall thereof have the following advantages:
1) through setting up controlling means for can satisfy actual need more in the use of heat pipe, the user can control the application temperature of heat pipe as required, has avoided the overheated or the supercooling phenomenon that traditional heat pipe's unable fine temperature control produced, has further realized the automation of heat pipe equipment and the extensive of application.
2) The invention provides a novel electric heating heat pipe, which is characterized in that an electric heating device is arranged in the heat pipe, and heat exchange is carried out by utilizing electric energy, so that the single application range of the traditional heat pipe and the limitation of a heat source are avoided, the application field of the heat pipe is wider, the purposes of environmental protection and energy saving can be achieved, and the utilization efficiency of the heat pipe is improved.
3) Through the change of the heating power and the structural size of the electric heating rod, the heating efficiency is further improved, and the heat exchange efficiency of the heat pipe is improved.
4) The invention provides a coil pipe type heat pipe structure for the first time, and through the arrangement of the coil pipe, the heat exchange fluid can generate volume expansion after being heated, and the free end of the coil pipe is induced to generate vibration. Thereby causing the surrounding fluid to form further turbulent flow and further enhancing heat transfer.
5) The invention further improves the heat exchange effect of the heat pipe by setting the pipe diameter of the heat exchange pipe of the coil pipe and the distance between the pipe intervals and the central line of the lower collecting pipe.
6) The invention optimizes the optimal relationship of the parameters of the heat pipe through a large number of tests, thereby further improving the heat exchange efficiency.
Drawings
Fig. 1 is a schematic front view of a heat pipe apparatus.
Fig. 2 is a cross-sectional view a-a in fig. 1.
Fig. 3 is a dimensional schematic of the structure of fig. 2.
Fig. 4 is a schematic structural view of the arrangement of the electric heating apparatus of fig. 1.
Fig. 5 is a schematic diagram of the optimized structure in fig. 4.
Fig. 6 is a schematic view of the structure of an electric heating apparatus in a parabolic cross-sectional shape.
In the figure: 1. the device comprises a lower header 2, an upper header 3, a coil pipe 4, a heat exchange pipe 5, a return pipe 6, a free end 7, a free end 8, an electric heating device, a 9 vacuumizing device and a 10 power supply.
Detailed Description
The following detailed description of embodiments of the invention refers to the accompanying drawings.
In this document, "/" denotes division and "×", "denotes multiplication, referring to formulas, if not specifically stated.
It is an object of the present invention to provide an electrically heated heat pipe, such as shown in fig. 4-6.
A heat pipe comprises a lower header 1, an upper header 2, a heat exchange tube bundle and a return pipe 5, wherein the heat exchange tube bundle is communicated with the lower header 1 and the upper header 2, the lower header 1 is an evaporation end, the condensation end comprises the upper header 2, fluid is subjected to heat absorption evaporation in the lower header 1 and is condensed in the upper header 2, and the condensed fluid returns to the lower header 1 through the return pipe; the return pipe is connected with the positions of the two side ends of the lower collecting pipe 1 and the upper collecting pipe 2, and an electric heating device 8 is arranged in the lower collecting pipe 1; the heat pipe also includes a temperature control system for controlling the temperature of the vapor within the heat pipe.
The lower header 1, the upper header 2 and the heat exchange tube bundle of the heat pipe form a channel for fluid circulation. The upper collecting pipe 2 is provided with a vacuum-pumping pipe 9, the vacuum pump vacuumizes the inner cavities of the lower collecting pipe 1, the upper collecting pipe 2 and the heat exchange pipe bundle through the vacuum-pumping port pipe 9, then a proper amount of heat transfer fluid is filled through the vacuum-pumping pipe 9, and the heat transfer fluid finally flows into the lower collecting pipe 1. And after the injection amount of the thermal fluid to be transmitted reaches the standard capacity, sealing the vacuumizing tube 9.
Preferably, an electric heating device 8 is arranged in the lower header 1, and the electric heating device 8 is used for heating the fluid in the lower header 1. The fluid absorbs electric heat to evaporate in the lower header 1, after heat exchange is carried out between at least one part of the coil 3 and the upper header 2, the fluid is condensed in the upper header 2, and the condensed fluid returns to the lower header 1 through the return pipe 5.
Preferably, the electrical heating means 8 are preferably circular in cross-section.
Preferably, the electric heating means 8 is an electric heating rod.
Preferably, the electric heating device 8 is located below the middle position of the lower header 1, i.e. the electric heating device is located at a position between the middle position and the bottom of the lower header.
Preferably, the distance between the central line of the electric heating device 8 and the central line of the lower header is 1/4-1/3 of the tube inner radius of the lower header 1.
Experiments show that the position can achieve the optimal heating effect, so that the optimal heat exchange effect is achieved.
Preferably, the heat pipe further comprises a temperature control system for controlling the temperature of the vapour within the heat pipe. And a temperature sensor is arranged in the heat exchange tube bundle and is used for measuring the temperature of steam generated in the coil. The heating rod is electrified for heating, and the heated fluid is rapidly atomized in a vacuum state and is filled in each heat exchange tube bundle, the upper collecting tube 2 and the lower collecting tube 1. When the temperature measured by the temperature sensor reaches a preset first temperature, the temperature controller controls the heating device to stop heating, and when the temperature measured by the temperature sensor is lower than a preset second temperature, the temperature controller controls the heating rod to heat.
Preferably, the first temperature and the second temperature are the same.
Preferably, the first temperature is 5-20 degrees celsius higher than the second temperature. Preferably 8-13 degrees celsius.
Preferably, the electric heating device 8 continuously reduces the heat generating power from the middle part (for example, M position in fig. 5) of the lower header 1 to the two ends (for example, E, F position in fig. 5) of the lower header. Namely, the heating power of the middle part of the electric heating device 8 is the highest, and the heating power of the two ends is the lowest.
Preferably, the heat generating power of the electric heating device is continuously reduced more and more from the middle of the lower header 1 to the two ends of the lower header.
Through the optimized design, the heat exchange efficiency can be further improved. Through the experiment discovery, can improve heat exchange efficiency through above-mentioned setting.
Preferably, the electric heating device 8 is divided into a plurality of sections, and the heat generating power of the electric heating devices of the different sections is continuously reduced from the middle part (for example, M position in fig. 5) of the lower header 1 to the two ends (for example, E, F position in fig. 5) of the lower header. Namely, the heating power of the middle part of the electric heating device 8 is the highest, and the heating power of the two ends is the lowest.
Preferably, the heat generating power of the electric heating devices of different sections is continuously reduced more and more from the middle part of the lower header 1 to the two ends of the lower header 1.
Through the optimized design, on one hand, the processing is convenient, and the heat exchange efficiency can be further improved. Experiments show that the heat exchange efficiency can be improved by about 15% by the arrangement.
Fig. 5 shows a structure in which the electric heating device 8 is divided into a plurality of segments.
The electric heating device adopts a resistance heating mode.
Preferably, the electric heating device is a rod-shaped resistor. Preferably, the number is one or more.
Preferably, the electric heating device is a resistance wire. Preferably, the number is one or more.
Preferably, the electric heating devices (preferably one or more rod-shaped resistors or one or more resistance wires) are arranged from the middle part of the lower header 1 to the two ends of the lower header, and the outer diameter of the electric heating devices is larger, namely the electric heating devices are thicker. Namely, the middle part of the electric heating device is the thinnest, and the two ends are the thickest. For example, as shown in fig. 5 and 6, by the above-mentioned optimized arrangement, the heating powers of different positions of the electric heating device are different, thereby improving the efficiency of electric heating.
Preferably, the outer diameter of the electric heating apparatus becomes larger from the middle of the lower header 1 to both ends of the lower header.
By adopting the change of the outer diameter, the resistance in the middle is the largest, the heating rate is the largest, the fluid is evaporated, the heating rate is gradually reduced towards the two ends, and the cold fluid flows down from the two ends, so that the heat exchange efficiency of the heat pipe is improved.
Experiments show that the optimal arrangement enables the utilization efficiency of electric heating to be highest, enables the heat pipe to achieve the best electric heating utilization efficiency, and can improve the heat utilization rate by about 10%.
Preferably, the external shape of the electric heating device is parabolic, as shown in fig. 6.
Preferably, the fluid is water.
Further preferably, the heat exchange tube bundle is a coil, and the description of the heat pipe with the coil is as follows:
as shown in fig. 1, the heat pipe includes a lower header 1, an upper header 2, a coil 3 and a return pipe 5, the coil 3 is communicated with the lower header 1 and the upper header 2, the lower header 1 is an evaporation end, the condensation end includes the upper header 2 and at least a part of the coil 3, the fluid is evaporated by heat absorption in the lower header 1, after heat exchange is performed between at least a part of the coil 3 and the upper header 2, the fluid is condensed in the upper header 2, and the condensed fluid returns to the lower header 1 through the return pipe 5.
Preferably, the coil 3 is one or more, for example, fig. 1 illustrates a plurality of coils 3.
As shown in fig. 1, the upper header 2 is located at an upper portion of the lower header 1.
As shown in fig. 2, each coil 3 comprises a plurality of heat exchange tubes 4 of circular arc shape, the ends of adjacent heat exchange tubes 4 are communicated, the plurality of heat exchange tubes 4 are formed into a serial structure, and the ends of the heat exchange tubes 4 are formed into tube free ends 6, 7.
The heat pipes, when in operation, exchange heat with other fluids through the upper header 2 and the coil 3. Other fluids may exchange heat with only a portion of the coil 3, for example the portion of coil 3 in fig. 2 connected to the lower header 1 does not participate in heat exchange.
Preferably, the part not participating in heat exchange is an adiabatic end. That is, the heat pipe includes an evaporation end, a condensation end and an adiabatic end, wherein the evaporation end is the lower header 1, the adiabatic end is a part of the coil 3 connected with the lower header 1, and the rest is the condensation end.
Preferably, only the lower header 1 is used as the evaporation end, the upper header 2 and the coil are used as the condensation end, and there is no adiabatic end.
The invention provides a heat pipe with a novel structure.A coil pipe is arranged, heat exchange fluid can expand in volume after being heated, so that steam is formed, and the volume of the steam is far greater than that of water, so that the formed steam can flow in the coil pipe in a rapid impact manner. Because of volume expansion and steam flowing, the free ends 6 and 7 of the coil 1 can be induced to vibrate, the vibration is transmitted to the surrounding heat exchange fluid by the free ends 6 and 7 of the heat exchange tubes in the vibrating process, and the fluid can also generate disturbance with each other, so that the surrounding heat exchange fluid forms disturbed flow, a boundary layer is damaged, and the purpose of enhancing heat transfer is achieved.
Experiments show that compared with the heat pipe which is always in a standing state in the prior art, the heat exchange efficiency is improved by 25-35%.
Preferably, the lower header 1, the upper header 2 and the coil 3 are all of a circular tube structure.
Preferably, the return pipe 5 connects the lower header 1 and the upper header 2 at positions of both side ends. Therefore, the flow path of the fluid in the upper header 2 is ensured to be long, the heat exchange time can be further prolonged, and the heat exchange efficiency is improved.
Preferably, the heat exchange tube 4 is a flexible heat exchange tube. The heat exchange tube 4 is provided with the elastic heat exchange tube, so that the turbulent flow of the free end can be further increased, and the heat exchange coefficient can be further improved.
Preferably, the center lines of the plurality of circular arc-shaped heat exchange tubes 4 are circular arcs of concentric circles.
Preferably, the concentric circles are circles centered on the center of the upper header 2. I.e. the heat exchange tubes 4 of the coil 3 are arranged around the central line of the upper header 2.
As shown in fig. 2, the heat exchanger tube 4 is not a complete circle but a mouth is left, thereby forming a free end of the heat exchanger tube. The angle of the arc of the mouth part is 70-120 degrees, namely the sum of included angles b and c in figure 3 is 70-120 degrees.
Preferably, the pipe diameter of the lower header 1 is smaller than that of the upper header 2.
The lower header has an internal diameter of R1 and the upper header has an internal diameter of R2, preferably 0.45< R1/R2< 0.88.
Through the arrangement, the heat transfer can be further enhanced, and the heat exchange efficiency is improved by 8-15%.
Preferably, the distance between the adjacent heat exchange tubes 4 becomes larger as it becomes farther from the center of the upper header 2. For example, as shown in fig. 2, the distance between the heat exchange tubes BC is larger than the distance between AB and the distance between the heat exchange tubes CD is larger than the distance between BC in the radial direction centered on the center of the upper header 2.
Preferably, the distance between the adjacent heat exchange tubes 4 is continuously increased to a larger and larger extent.
Through the preferred setting, can further improve heat exchange efficiency, increase the homogeneity of the heat distribution of heat transfer. Experiments show that the heat exchange efficiency can be improved by 8-12% by the arrangement.
Preferably, the heat exchange tubes 4 have a larger diameter as they are farther from the center of the upper header 2.
Preferably, the diameter of the heat exchange tube 4 is continuously increased to a larger and larger extent.
Through the preferable arrangement, the heat exchange efficiency can be further improved, and the uniformity of heat exchange is increased. Experiments show that the heat exchange efficiency can be improved by about 10% by the arrangement.
Preferably, as shown in fig. 1, the number of the coil pipes 4 is plural, and the plural coil pipes 4 are in a parallel structure.
In tests, it was found that the distance relationship between the lower header 1, the upper header 2 and the heat exchange tubes 4 can have an influence on the heat exchange efficiency and uniformity. If the distance between the heat exchange tubes 4 is too large, the heat exchange efficiency is poor, the distance between the heat exchange tubes 4 is too small, the heat exchange tubes 4 are distributed too densely, the heat exchange efficiency can be influenced, the pipe diameters of the collecting pipes and the heat exchange tubes influence the volume of contained liquid or steam, and the vibration of the free ends 6 and 7 can be influenced, so that the heat exchange is influenced. Therefore, the sizes of the pipe diameters of the lower header 1 and the upper header 2 have a certain relation with the distance between the heat exchange pipes 4.
The invention provides an optimal size relation summarized by test data of a plurality of heat pipes with different sizes. Starting from the maximum heat exchange amount in the heat exchange effect, nearly 200 forms are calculated. The dimensional relationship is as follows:
the inner diameter of the lower header is R1, the inner diameter of the upper header is R2, the outer diameter of the heat exchange tube is D, the distance between the center lines of the adjacent heat exchange tubes is L, and the following relations are satisfied:
10 (R1/R2) = a-b Ln (5D/L), where Ln is a logarithmic function, a, b are coefficients,
wherein 17.03< a <18.12,9.15< b < 10.11;
55mm<R1<100mm；95mm<R2<145mm；
25mm<D<80mm；40mm<L<120mm；
0.45< R1/R2< 0.88; preferably 0.5-0.8, more preferably 0.59< R1/R2< 0.71;
0.5< D/L < 0.7; preferably 0.58< D/L < 0.66.
Preferably, 17.32< a <17.72,9.45< b < 9.91;
further preferably, a =17.54 and b = 9.68.
Preferably, the number of heat exchange tubes is 3 to 5, preferably 3 or 4.
Preferably, the value of a is continuously increased and the value of b is continuously decreased with the increase of R1/R2. Through the change, the structural parameters of the heat pipe are optimized and reasonable, and the calculated data are accurate.
The distance between the central lines of the lower collecting pipe 1 and the upper collecting pipe 2 is 320-380 mm; preferably 340-.
Preferably, the radius of the heat exchange tube is preferably 10-40 mm; preferably 15 to 35mm, more preferably 20 to 30 mm.
If the diameters of the adjacent heat exchange tubes are different, the diameter D of each heat exchange tube is the average value of the diameters of the adjacent heat exchange tubes.
Further preferably, the central lines of the heat exchange tubes 4 of the same coil are positioned on the same plane. Preferably, the plane is perpendicular to the plane formed by the centerlines of the lower header 1 and the upper header 2. Preferably, the planes formed by the center lines of the different coiled heat exchange tubes 4 are parallel to each other.
Further preferably, the distance between adjacent coils 3 is 2.8-3.6 times the outer diameter of the coiled heat exchange tube 4. The distance between adjacent coils 3 is calculated as the distance between the planes in which the center lines of the coiled heat exchange tubes 4 lie.
Further preferably, if the diameters of the heat exchange tubes of the coil are different, the average value of the diameters of the heat exchange tubes of the same coil is taken as the average diameter of the coil. For example, the average of the heat exchange tubes a-D as shown in fig. 2. The diameter of two adjacent coils 3 is then averaged to calculate the distance of the adjacent coils.
Preferably, the ends of the heat exchange tubes at the free ends 6, 7 of the same side are aligned in the same plane, with the extension of the ends (or the plane in which the ends lie) passing through the midline of the lower header 1, as shown in fig. 3.
Preferably, as shown in fig. 2, the inner heat exchange tubes of the coil 3 have first ends connected to the upper header 2 and second ends connected to one ends of the adjacent outer heat exchange tubes, the outermost heat exchange tubes of the coil 3 have one ends connected to the lower header 1, and the ends of the adjacent heat exchange tubes are connected to each other, thereby forming a serial structure.
Preferably, a plane on which a line connecting centers of the lower header 1 and the upper header 2 is located is a vertical direction.
As shown in fig. 3, the plane of the first end 6 forms an angle c of 40-65 degrees with the plane of the central lines of the lower header 1 and the upper header 2.
The plane in which the second end 7 is located forms an angle b of 55-65 degrees with the plane in which the centre lines of the lower header 1 and the upper header 2 are located.
Through the design of the preferable included angle, the vibration of the free end is optimal, and therefore the heat exchange efficiency is optimal.
As shown in fig. 2, the number of the heat exchange tubes 4 of the coil is 4, and the heat exchange tubes A, B, C, D are communicated. Of course, the number is not limited to four, and a plurality of the connecting structures are the same as those in fig. 2.
The floating type solar water heater comprises a plurality of floating coil pipes 1, a lower collecting pipe 1 and an upper collecting pipe 2, wherein the floating coil pipes 3 are arranged in parallel, and the floating coil pipes 1 are respectively and independently connected with the lower collecting pipe 1 and the upper collecting pipe 2.
Although the present invention has been described with reference to the preferred embodiments, it is not limited thereto. Various changes and modifications may be effected therein by one skilled in the art without departing from the spirit and scope of the invention as defined in the appended claims.
Claims (2)
1. A heat pipe comprises a lower collecting pipe, an upper collecting pipe, a coil pipe and a return pipe, wherein the coil pipe is communicated with the lower collecting pipe and the upper collecting pipe, the lower collecting pipe is an evaporation end, a condensation end comprises the upper collecting pipe and at least one part of the coil pipe, fluid is subjected to heat absorption evaporation in the lower collecting pipe, after heat exchange is carried out between at least one part of the coil pipe and the upper collecting pipe, the fluid is condensed in the upper collecting pipe, and the condensed fluid returns to the lower collecting pipe through the return pipe; the number of the coil pipes is one or more, each coil pipe comprises a plurality of circular arc-shaped heat exchange pipes, the end parts of the adjacent heat exchange pipes are communicated, so that the plurality of heat exchange pipes form a series structure, the end parts of the heat exchange pipes form a first free end and a second free end, and an electric heating device is arranged in the lower collecting pipe; the device is characterized in that an included angle c formed by a plane where the first free end is located and a plane where the central lines of the lower header and the upper header are located is 40-65 degrees; an included angle b formed by a plane where the second free end is located and a plane where the central lines of the lower header and the upper header are located is 55-65 degrees;
the central lines of the plurality of arc-shaped heat exchange tubes are arcs of concentric circles; the concentric circles are circles taking the center of the cross section of the upper header as the center of a circle;
the inner diameter of the lower header is R1, the inner diameter of the upper header is R2, the outer diameter of the heat exchange tube is D, the distance between the center lines of the adjacent heat exchange tubes is L, and the following relations are satisfied:
10 (R1/R2) = a-b Ln (5D/L), where Ln is a logarithmic function, a, b are coefficients,
wherein 17.03< a <18.12,9.15< b < 10.11;
55mm<R1<100mm；95mm<R2<145mm；
25mm<D<80mm；40mm<L<120mm；
0.45<R1/R2<0.88；
0.5<D/L<0.7。
2. the heat pipe of claim 1 wherein a plane in which a line connecting centers of the lower header and the upper header is located is a vertical direction.
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| CN109990262B (en) * | 2018-03-09 | 2020-12-04 | 浙江伊鑫纺织科技股份有限公司 | Auxiliary heating steam generator |
| CN110906772B (en) * | 2019-01-29 | 2021-02-09 | 青岛乾福圣耀商贸有限公司 | Gravity heat pipe with variable spacing |
| CN109631640B (en) * | 2019-01-29 | 2020-04-10 | 青岛佰腾科技有限公司 | Design method of gravity heat pipe for heating fumigation-washing liquid medicine |
| CN113701533B (en) * | 2019-04-23 | 2022-07-01 | 山东大学 | Mirror symmetry loop heat pipe design method |
| CN112146494B (en) * | 2019-06-28 | 2022-02-11 | 山东大学 | Rotational symmetry's control by temperature change vibration loop heat pipe |
| CN112129093B (en) * | 2020-04-29 | 2021-08-10 | 山东大学 | A hot water steam switches heating device for donkey-hide gelatin is distinguished and is detected |
| CN112432535B (en) * | 2020-11-27 | 2022-08-30 | 巨野百林化学有限公司 | Unit type heat exchange device for chemical production |
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| SU1657927A1 (en) * | 1989-06-08 | 1991-06-23 | Московский энергетический институт | Heat transfer device |
| CN201000293Y (en) * | 2006-10-27 | 2008-01-02 | 姚新安 | Hot pipe type heat radiator |
| CN102361522B (en) * | 2011-10-21 | 2015-10-28 | 重庆仪表材料研究所 | A kind of variable cross-section termination not armoured heating heater and preparation method thereof |
| CN102946653A (en) * | 2012-12-07 | 2013-02-27 | 深圳晶蓝地光电科技有限公司 | Variable cross-section high temperature furnace heating body |
| CN203085514U (en) * | 2012-12-20 | 2013-07-24 | 华南理工大学 | IGBT module heat radiator based on loop heat pipe |
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| US20160061532A1 (en) * | 2014-09-02 | 2016-03-03 | Aavid Thermalloy, Llc | Evaporator and condenser section structure for thermosiphon |
| CN204649044U (en) * | 2015-05-18 | 2015-09-16 | 华南理工大学 | A kind of follow-on ultra-thin loop circuit heat pipe |
| CN205228243U (en) * | 2015-11-04 | 2016-05-11 | 天津商业大学 | Flat loop heat pipe |
| CN205156393U (en) * | 2015-11-16 | 2016-04-13 | 江苏太阳宝新能源有限公司 | Fused salt heat absorber |
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