CN206160347U - Temperature regulation energy conversion device - Google Patents
Temperature regulation energy conversion device Download PDFInfo
- Publication number
- CN206160347U CN206160347U CN201621197298.0U CN201621197298U CN206160347U CN 206160347 U CN206160347 U CN 206160347U CN 201621197298 U CN201621197298 U CN 201621197298U CN 206160347 U CN206160347 U CN 206160347U
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- China
- Prior art keywords
- evaporimeter
- conversion device
- energy conversion
- input
- condenser
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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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/40—Geothermal heat-pumps
Abstract
The utility model relates to a temperature regulation energy conversion device, including closed basic station room and basic station room thermoregulation mechanism, room thermoregulation mechanism in basic station is including setting up the evaporimeter in basic station room upper end to and set up underground the condenser in the deep well, the evaporimeter output passes through the tube coupling with the condenser input, be equipped with the booster pump on the pipeline, the cover has the insulating tube on the pipeline, the condenser output passes through the capillary with the evaporimeter input and is connected, the evaporimeter is the vacuum seal return circuit with the closed -loop that the condenser formed, be filled with the medium that adjusts the temperature in the vacuum seal return circuit. Compared with the prior art the cooling has, the intensification process need not to use air conditioning equipment to go on, the power consumption is little, the low characteristics of operation installation cost.
Description
Technical field
The utility model is related to a kind of energy conversion device, specifically a kind of temperature adjustment energy conversion device.
Background technology
Base station be public mobile communication base station be radio station a kind of form, refer in certain area of radio coverage
In, believe radio station by carrying out the transceiving of information transmission between mobile switching center, with mobile telephone terminal, typically
All supporting setting base station room where base station is set.
Base station room in use, is needed its internal temperature control in suitable scope.Under normal circumstances, summer
No more than 29 DEG C, winter temperature cannot be below 10 DEG C to temperature in the room of base station, can otherwise affect normally using for electric elements.
But in actual use, summer temp can be risen to more than 30 DEG C, and in the winter time in the presence of heat-insulation layer in the room of base station
Temperature can typically maintain more than 10 DEG C in the room of base station, and less than 10 DEG C can be down under minority harsh climate, thus can be to electrical equipment unit
The normal use of part impacts, and prevents base station room from giving full play to its effect.In order to overcome high temperature and low temperature environment to base station
The adverse effect that room is caused, presently mainly carries out auxiliary temperature-reducing intensification by installing air-conditioning equipment in the room of base station, but this
The defect that kind of mode is present is:Air-conditioning equipment needs to run without interruption, and power consumption is big, and operation installation cost is high, is unfavorable for extensively
Carrying out promote and use.
Utility model content
The utility model proposes a kind of temperature adjustment energy conversion device.
What the technical solution of the utility model was realized in:A kind of temperature adjustment energy conversion device, it is characterised in that:
Including closed base station room and base station room thermoregulation mechanism;Base station room thermoregulation mechanism includes being arranged on the room of base station
The evaporimeter at end, and the condenser being arranged in Deep Underground, the evaporimeter output end is with condenser input by pipe
Road connects, and the pipeline is provided with booster pump, on the pipeline insulating tube is cased with;The condenser output end is input into evaporimeter
End is connected by capillary;The closed-loop path that the evaporimeter and condenser are formed is vacuum tightness loop, the vacuum tightness
Filled with temperature control medium in loop.
Used as preferred technical scheme, the volume in closed base station room is 2-3 cube.
Used as preferred technical scheme, the insulating tube is polyurethane thermal pipe.
Used as preferred technical scheme, the capillary inner diameter is 0.8 ~ 2mm.
Used as preferred technical scheme, the temperature control medium is fluoro trichloromethane.
Used as preferred technical scheme, the condenser is coil-like, and described coil pipe one end is input, and the other end is defeated
Go out end.
As preferred technical scheme, demarcation strip is equipped with the evaporimeter, the demarcation strip will be deposited inside evaporimeter
Storage space is divided into the input space and output space, and between the input space and output space passage is communicated with.
Used as preferred technical scheme, the input space is provided with input port, and the height of the input port is empty higher than input
The height of interior liquid level.
As a result of above-mentioned technical proposal, the utility model has beneficial effect following prominent:
The suction exothermic process that temperature-fall period is fully relied in temperature control medium vapour-liquid transfer process is carried out, as long as temperature is beyond drop
Warm medium boiling temperature, is vaporized process automatically.Heat exchange of the temperature-rise period by temperature control medium in cyclic process is carried out,
Cooling, temperature-rise period are carried out without using air-conditioning equipment, take full advantage of geothermal energy resources, and power consumption seldom, runs installation cost
It is low, beneficial to widely being promoted and used.
Description of the drawings
In order to be illustrated more clearly that the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, before creative labor is not paid
Put, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is the utility model overall structure diagram.
Fig. 2 is the utility model evaporation structure schematic diagram.
Fig. 3 is that temperature control medium flows to schematic diagram in the utility model evaporimeter.
In figure:1- closeds base station room;2- evaporimeters;3- condensers;4- pipelines;5- capillaries;6- booster pumps;7- is input into
Mouthful;8- demarcation strips;The 9- input spaces;10- exports space.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
As shown in figure 1, the utility model includes closed base station room 1 and base station room thermoregulation mechanism.The closed
The volume in base station room 1 is 2-3 cube.
Base station room thermoregulation mechanism includes being arranged on the evaporimeter 2 of base station room upper end, and is arranged on underground depth
Condenser 3 in well.The output end of the evaporimeter 2 is connected with the input of condenser 3 by pipeline 4, and the pipeline 4 is provided with increasing
Press pump 6, the effect of booster pump 6 is to promote circulation.Insulating tube is cased with the pipeline 4, the insulating tube is polyurethane thermal pipe,
The effect of insulating tube is to avoid thermal loss, affects cooling temperature rise effect.The output end of the condenser 3 and the input of evaporimeter 2
Connected by capillary 5, the internal diameter of the capillary 5 is 0.8 ~ 2mm.The closed-loop path that the evaporimeter 2 is formed with condenser 3 is
Vacuum tightness loop, filled with temperature control medium in the vacuum tightness loop, in prioritization scheme, the temperature control medium is a fluorine trichlorine
Methane.23.7 DEG C of the boiling temperature of fluoro trichloromethane, in summer when the temperature in the room of base station is higher than 23.7 DEG C, evaporimeter 2
Interior temperature control medium vaporization, absorbs the heat of surrounding air, makes the temperature drop in the room of base station, while the temperature control medium after vaporization
Volumetric expansion, the air pressure in vacuum tightness loop is raised, and adds the effect of booster pump 6, forces the temperature control medium Jing pipes after vaporization
Road 4 enters the condenser 3 being arranged in Deep Underground, because well temperature maintains essentially in 18 DEG C throughout the year, so high-temperature gas
The temperature control medium of form can condense to the cold after into condenser 3, and from gaseous state liquid is changed into, while discharging heat.It is temporarily stored in
Liquid temperature control medium in condenser 3, under the collective effect that vacuum tightness loop has air pressure and booster pump 6, along capillary
The Returning evaporimeter 2 of pipe 5 completes one cycle process.Before temperature reaches 29 DEG C of critical-temperatures in the room of base station, dropped in advance
Temperature, it is to avoid temperature affects equipment operation more than 29 DEG C.When base station room is in weather more cold winter, temperature control medium due to
23.7 DEG C of boiling temperature is not reached, so temperature control medium is in all the time liquid condition, in the presence of booster pump 6 temperature adjustment is promoted
Medium in vacuum tightness loop interior circulation, when temperature control medium is recycled to condenser 3, because well temperature maintains essentially in 18
DEG C, so water temperature can pass to temperature control medium by heat transfer, raise temperature control medium temperature, temperature control medium is by heat through following
Annulus is to evaporimeter 2, then heat is shed by evaporimeter 2, so as to realize thermogenic action.Temperature-fall period fully relies on temperature control medium
Suction exothermic process in vapour-liquid transfer process is carried out, and temperature control medium vapour-liquid transfer process does not need compressor to act on cooling
Medium, as long as temperature exceeds temperature-reducing medium boiling temperature, is vaporized process automatically.And without the need for manually carrying out regular high temperature detector
Survey to check temperature whether beyond 29 DEG C.Heat exchange of the temperature-rise period by temperature control medium in cyclic process is carried out, cooling,
Temperature-rise period is carried out without using air-conditioning equipment, and seldom, operation installation cost is low for power consumption, beneficial to widely being promoted and made
With.
In order to increase the heat exchange area of condenser 3 and water or surrounding air, the condenser 3 can be it is coil-like,
Described coil pipe one end is input, and the other end is output end.
As shown in Figure 2,3, demarcation strip 8 is provided with the evaporimeter, the demarcation strip 8 divides evaporimeter internal storage space
The input space 9 and output space 10 are divided into, between the input space 9 and output space 10 passage is communicated with.The separation
The inwall adjacent with the input space 9 of plate 8 is provided with heat-insulation layer.The input space 9 is provided with input port 7, the height of the input port 7
Height of the degree higher than liquid level in the input space 9.The memory space inside evaporimeter is separated by demarcation strip 8, makes evaporation
The medium of vaporization separates, the air pressure in the input space 9 when volumetric expansion air pressure increase needs output through demarcation strip 8 in device
Reduce, while the height of input port 9 is higher than the height for exporting liquid level in space 10, the two collective effect avoids gas in evaporimeter
Press through height and liquid medium press-in input port 7 is produced into refluence.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc. should be included in the utility model
Protection domain within.
Claims (8)
1. a kind of temperature adjustment energy conversion device, it is characterised in that:Including closed base station room and base station room temperature adjuster
Structure;Base station room thermoregulation mechanism includes being arranged on the evaporimeter of base station room upper end, and is arranged in Deep Underground
Condenser, the evaporimeter output end is connected with condenser input by pipeline, and the pipeline is provided with booster pump, the pipe
Insulating tube is cased with road;The condenser output end is connected with evaporimeter input by capillary;The evaporimeter and condensation
The closed-loop path that device is formed is vacuum tightness loop, filled with temperature control medium in the vacuum tightness loop.
2. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:Closed base station room
Volume be 2-3 cube.
3. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:The insulating tube is poly- ammonia
Ester insulating tube.
4. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:The capillary inner diameter is
0.8~2mm。
5. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:The temperature control medium is one
Fluoro trichloromethane.
6. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:The condenser is coil pipe
Shape, described coil pipe one end is input, and the other end is output end.
7. according to a kind of temperature adjustment energy conversion device described in claim 1, it is characterised in that:It is all provided with the evaporimeter
There is demarcation strip, evaporimeter internal storage space is divided into the input space and output space, the input space by the demarcation strip
Passage is communicated with and output space between.
8. according to a kind of temperature adjustment energy conversion device described in claim 7, it is characterised in that:The input space is provided with
Input port, the height of the input port is higher than the height of liquid level in the input space.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621197298.0U CN206160347U (en) | 2016-11-07 | 2016-11-07 | Temperature regulation energy conversion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621197298.0U CN206160347U (en) | 2016-11-07 | 2016-11-07 | Temperature regulation energy conversion device |
Publications (1)
Publication Number | Publication Date |
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CN206160347U true CN206160347U (en) | 2017-05-10 |
Family
ID=58658237
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201621197298.0U Active CN206160347U (en) | 2016-11-07 | 2016-11-07 | Temperature regulation energy conversion device |
Country Status (1)
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CN (1) | CN206160347U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109812901A (en) * | 2019-03-25 | 2019-05-28 | 陈国锋 | A kind of air-conditioner temperature regulation unit using high-low pressure conversion |
-
2016
- 2016-11-07 CN CN201621197298.0U patent/CN206160347U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109812901A (en) * | 2019-03-25 | 2019-05-28 | 陈国锋 | A kind of air-conditioner temperature regulation unit using high-low pressure conversion |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20180904 Address after: 271100 1 1 Yuntai Mountain Road, Laiwu high tech Zone, Shandong Patentee after: Shandong Yi Hui Intelligent Technology Co., Ltd. Address before: 271100 Shanghai Pearl Garden E5, Laicheng District, Laiwu, Shandong Patentee before: Wei Shucheng |