CN109539844A - A kind of heat pipe runner combined type full heat recovery device and method - Google Patents
A kind of heat pipe runner combined type full heat recovery device and method Download PDFInfo
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- CN109539844A CN109539844A CN201811459046.4A CN201811459046A CN109539844A CN 109539844 A CN109539844 A CN 109539844A CN 201811459046 A CN201811459046 A CN 201811459046A CN 109539844 A CN109539844 A CN 109539844A
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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
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F12/00—Use of energy recovery systems in air conditioning, ventilation or screening
- F24F12/001—Use of energy recovery systems in air conditioning, ventilation or screening with heat-exchange between supplied and exhausted air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
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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
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/56—Heat recovery units
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- Life Sciences & Earth Sciences (AREA)
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- Thermal Sciences (AREA)
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Abstract
The invention discloses a kind of heat pipe runner combined type full heat recovery devices, including box shell, front housing, back cabinet and heat pipe wheel set assembly, front housing is equipped with fresh inlet channel and wind exhausting outlet channel, back cabinet is equipped with fresh air exit passageway and air draft intake channel, the front side wall of box shell is equipped with fresh inlet and wind exhausting outlet, and the rear wall of box shell is equipped with fresh air outlet and air draft import；Heat pipe wheel set assembly includes runner, annular heat pipe and driving motor, and runner includes wheel shell and muti-piece fin, and wheel shell inner space is separated into multiple fin air ducts by muti-piece fin；The outer surface of annular heat pipe is equipped with heat tube moisture material layer, and the outer surface of fin is equipped with fin dehumidifying material layer, is connected with the transmission belt being connected across on wheel shell on the output shaft of driving motor；The invention also discloses a kind of heat pipe runner combined type total heat recovery methods.Invention enhances heat transfer process, improve Exposure degree efficiency, can be realized the total heat recovery under summer and winter condition.
Description
Technical field
The invention belongs to heat recovery technology fields, and in particular to a kind of heat pipe runner combined type full heat recovery device and side
Method.
Background technique
Indoor air quality becomes the focus of scholar's research in recent years, and indoor air quality is to people's lives and work shadow
Sound is very big.Bad indoor air quality and sick building syndrome has direct association, it can lead to people's disease incidence
Rate surges, and dizzy, out of strength, working efficiency is low.Influence indoor air quality because being known as: do not supplement it is enough it is outdoor newly
Wind, the air pollution that building itself generates, the air pollution etc. that physical activity generates.Therefore to improve indoor air quality,
Most direct, most effective measure first is that guaranteeing indoor enough fresh air volumes.For the specific fresh air volume of specific environment set,
So that indoor air quality is met hygienic requirements, however meet hygienic requirements with regard to inevitable requirement fresh air volume substantial increase, increases new
Air quantity, that is, new wind load, has also just increased accordingly air conditioning energy consumption.And air conditioning energy consumption has accounted for the 40%~60% of building energy consumption, fresh air
Load can increase to the 40% of total refrigeration duty, and so big energy consumption just generates direct contradiction with energy-saving and emission-reduction fundamental state policy, so
The full heat recovery device of research and development air draft has become an important direction of scientific rersearch for fresh air pretreatment.
The rotary-type heat regenerator of core material is made because of its presence by noninflammability hygroscopic material or the material with hygroscopicity coating
Biggish thermal contact resistance, and recuperation of heat has periodically, the other side cannot be transferred heat in time, thus heat exchanger effectiveness
It is severely impacted, while the wet exchange efficiency that heat exchange influences also is affected.Heat pipe is a kind of superconducting heat transfer element, is led
Thermal energy power is more than the capacity of heat transmission of any known metal, however a series of heat pipe-type heat regenerator being made of heat pipes can only recycle
Air sensible cannot recycle air latent heat.
Summary of the invention
In view of the above-mentioned deficiencies in the prior art, the technical problem to be solved by the present invention is that providing a kind of heat pipe runner
Combined type full heat recovery device, structure is simple, and design rationally, enhances heat transfer process, improves Exposure degree efficiency, can
Realize the total heat recovery under summer and winter condition, it is practical, convenient for promoting the use of.
In order to solve the above technical problems, the technical solution adopted by the present invention is that: a kind of heat pipe runner combined type total heat recovery
Device including box shell, is arranged in the front housing of front side in box shell, the back cabinet being arranged on rear side of in box shell and is arranged in box shell
The heat pipe wheel set assembly of middle position is provided with fresh inlet channel and wind exhausting outlet channel on the front housing, after described
The fresh air exit passageway being oppositely arranged with fresh inlet channel and the row being oppositely arranged with wind exhausting outlet channel are provided on casing
Wind inlet channel is provided with the fresh inlet being oppositely arranged with fresh inlet channel on the front side wall of the box shell and goes out with air draft
The wind exhausting outlet that mouthful channel is oppositely arranged is provided with the fresh air being oppositely arranged with fresh air exit passageway on the rear wall of the box shell
Outlet and the air draft import that is oppositely arranged with air draft intake channel, fresh inlet channel and fresh air exit passageway institute in the box shell
It is fresh air area in region, air draft intake channel and wind exhausting outlet channel region are exhaust zone in the box shell；The heat pipe
Wheel set assembly includes runner, annular heat pipe and provides the driving motor of power for rotating for runner, and the runner includes annular
Wheel shell and the uniformly distributed muti-piece fin in wheel shell is dissipated around with the geometric center of wheel shell, fin described in muti-piece will take turns
Shell inner space is separated into multiple fin air ducts, and each fin air duct is by the adjacent fin of two panels and is clipped in
One section of wheel shell between the adjacent fin of two panels surrounds, and the fin air duct is in fresh air area connection fresh inlet channel and newly
Wind exit passageway and flushing channel, the fin air duct are connected to wind exhausting outlet channel and air draft intake channel in exhaust zone,
The annular heat pipe is laid along the axial direction of runner in multilayer in wheel shell, and every layer of annular heat pipe includes more and lay in concentric circles
Annular heat pipe, every annular heat pipe is interspersed on fin；Heat tube moisture material is provided on the outer surface of the annular heat pipe
The bed of material is provided with fin dehumidifying material layer on the outer surface of the fin, is connected with bridging on the output shaft of the driving motor
Transmission belt on wheel shell.
A kind of above-mentioned heat pipe runner combined type full heat recovery device is provided with front housing round hole on the front housing,
The preceding subregion partition for front housing round hole to be divided into two 180 ° of sector channels is provided in the front housing round hole,
180 ° of sector channels on the upside of preceding subregion partition are fresh inlet channel, and 180 ° of sectors on the downside of preceding subregion partition are logical
Road is wind exhausting outlet channel.
A kind of above-mentioned heat pipe runner combined type full heat recovery device, the thickness of the preceding subregion partition are more than or equal to any
Maximum distance between adjacent two pieces of fins.
A kind of above-mentioned heat pipe runner combined type full heat recovery device is additionally provided with flushing channel on the back cabinet, institute
Flushing channel is stated to be connected with air draft intake channel.
A kind of above-mentioned heat pipe runner combined type full heat recovery device is provided with back cabinet round hole on the back cabinet,
Subregion after being provided with first for back cabinet round hole to be divided into two 180 ° of sector channels in the back cabinet round hole
Partition is provided with for 180 ° of sector channels to be divided into 165 ° in 180 ° of sector channels after first on the upside of subregion partition
Subregion partition after the second of sector channel and 15 ° of sector channels is positioned at 180 ° of sector channels after first on the downside of subregion partition
Air draft intake channel, 165 ° of sector channels are fresh air exit passageway, and 15 ° of sector channels are flushing channel, described the
The intercommunicating pore being provided on subregion partition below flushing channel after one, the flushing channel and air draft intake channel pass through company
Through-hole is connected.
A kind of above-mentioned heat pipe runner combined type full heat recovery device, the thickness of subregion partition is more than or equal to after described first
Maximum distance between two pieces of fins of arbitrary neighborhood.
A kind of above-mentioned heat pipe runner combined type full heat recovery device, the annular heat pipe include shell and are arranged in shell
On capping, be provided with heat pipe wicks on the inner surface of the shell, the shell inner cavity is vacuum chamber, in the vacuum chamber
Filled with heat-pipe working medium.
A kind of above-mentioned heat pipe runner combined type full heat recovery device, the fin and wheel shell are all made of aluminum alloy materials system
At the shell is made of red copper material, and the heat tube moisture material layer is coated in the appearance of shell using dip-coating method
On face, the fin dehumidifying material layer is coated on the outer surface of fin using dip-coating method.
A kind of above-mentioned heat pipe runner combined type full heat recovery device, the heat tube moisture material layer use dip-coating method
Detailed process on outer surface coated in shell are as follows:
Step A1, annular heat pipe is immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to annular
The surface of heat pipe carries out ungrease treatment of deoiling；
Step A2, after pulling annular heat pipe out of sodium hydroxide solution out, annular heat pipe table is cleaned with distilled water and ethyl alcohol
Face, then it is placed in drying in oven；
Step A3, silica gel particle is coated on by annular heat pipe surface using aqueous compound adhesive, is impregnated into silica solution after drying
In 1 hour~5 hours, later take out drying, repeat 3~8 times；
Step A4, annular heat pipe is immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, makes chlorination
Lithium is sufficiently submerged in silica gel particle duct, then is placed in drying in oven；
Step A5, annular heat pipe is put into temperature is 30 DEG C, humidity is that lyolysis is forced in the climatic chamber of 90%RH
12h, then it is placed in drying in oven；
The fin dehumidifying material layer is coated in the detailed process on the outer surface of fin using dip-coating method are as follows:
Step B1, fin is immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to the table of fin
Face carries out ungrease treatment of deoiling；
Step B2, after pulling fin out of sodium hydroxide solution out, fin surface is cleaned with distilled water and ethyl alcohol, then be placed in
Drying in oven；
Step B3, silica gel particle is coated on by fin surface using aqueous compound adhesive, it is small that 1 is impregnated into silica solution after drying
When~5 hours, drying is taken out later, is repeated 3~8 times；
Step B4, fin is immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, fills lithium chloride
Divide and be immersed in silica gel particle duct, then is placed in drying in oven；
Step B5, fin is put into pressure lyolysis 12h in the climatic chamber that temperature is 30 DEG C, humidity is 90%RH, then
It is placed in drying in oven.
The invention also discloses a kind of method and steps simply, it is convenient to realize, it is complete under summer and winter condition to can be realized
Recuperation of heat, practical, convenient for popularization and use heat pipe runner combined type total heat recovery method, this method include summer operating mode and
Two kinds of situations of winter condition, under summer operating mode, fresh air area is evaporator section, and exhaust zone is condensation segment, and under winter condition, fresh air area is
Condensation segment, exhaust zone are evaporator section；By after heat-pipe working medium water vapor, water vapour is run to annular the evaporator section of the annular heat pipe
Heat pipe condenser section releases heat in condensation segment and is condensed into liquid, and liquid water is aspirated by heat pipe wicks in heat pipe wicks
The evaporator section of annular heat pipe is flowed back under effect, vaporization of being heated again, so on circulate；When driving motor rotates counterclockwise,
Runner is driven to rotate counterclockwise by transmission belt, the annular heat pipe and fin slowly rotate under the drive of wheel shell, accelerate
Exchange process of the heat-pipe working medium water between evaporator section and condensation segment, improves heat exchange efficiency；Runner constantly rotates, and fresh air passes through
The fresh air area of runner, simultaneously inversely by the exhaust zone of runner, fresh air and air draft are alternately reverse by turning in this way for air draft
Wheel, when fin air duct has just been transferred to fresh air area from exhaust zone, fresh air and air draft mixed airflow in fin air duct enter
Flushing channel drains into outdoor；
Wherein, under summer operating mode, when the lower room air of temperature and humidity passes through the fin air duct of corresponding portion,
Annular heat pipeline section in corresponding fin air duct is cooled, and fin dehumidifying material layer and heat tube moisture material layer are due to water steaming
Gas partial pressure is poor, releases partial moisture contained therein, and in a flash under, is just in contact with exhaust airflow, cooled ring
Shape hot pipe section and fin dehumidifying material layer after drying and heat tube moisture material layer just take turns and go to fresh air area, the fresh sky with entrance
Gas phase contact, then the fresh air of high temperature and humidity is just able to cool down and dry, i.e., first carries out before carrying out other heat and wet treatments
It precools and dries in advance；
Summer Fresh air handing process are as follows: the fresh air that the fresh inlet enters removes moist wood by the fin on fin outer surface
Heat tube moisture material layer on the bed of material and annular heat pipe outer surface, fin dehumidifying material layer and heat tube moisture material layer are heated and add
Wet, the fin dehumidifying material layer and heat tube moisture material layer of heating exchange heat with the heat-pipe working medium water in corresponding portion shell,
Heat-pipe working medium water is heated vaporization, to take away fresh air heat, then the outdoor fresh air of high temperature and humidity obtains cooling down and dry, through new
It is standby to enter other air conditioner heats behind wind outlet；
Summer Air exhaust process are as follows: the air draft that the air draft import enters removes moist wood by the fin on fin outer surface
Heat tube moisture material layer on the bed of material and annular heat pipe outer surface, fin dehumidifying material layer and heat tube moisture material layer are cooled and go
Wet, cooling fin dehumidifying material layer and heat tube moisture material layer exchange heat with the water vapour in corresponding portion shell, and water steams
Vapour is condensed liquefaction, to take away exhaust cold, then air draft is discharged through wind exhausting outlet after being heated humidification or sets into other
It is standby；
Wherein, under winter condition, the fresh air of outdoor low temperature drying needs to recycle the hot and wet of indoor exhaust wind, works as winter
Annular when the higher room air of temperature and humidity passes through the fin air duct of corresponding portion, in corresponding fin air duct
Hot pipe section is heated, and fin dehumidifying material layer and heat tube moisture material layer adsorb institute in air due to water vapor partial pressure differential
The partial moisture contained, and in a flash under, be just in contact with exhaust airflow, the fin after the annular heat pipeline section being heated and moisture absorption
Dehumidifying material layer and heat tube moisture material layer just take turns and go to fresh air area, are in contact with the fresh air of entrance, then low temperature drying
Fresh air be just able to warming and humidifying, i.e., before carrying out other heat and wet treatments first carry out preheating and pre-humidifying；
Winter Air exhaust process are as follows: the air draft that the air draft import enters removes moist wood by the fin on fin outer surface
Heat tube moisture material layer on the bed of material and annular heat pipe outer surface, fin dehumidifying material layer and heat tube moisture material layer are heated and add
Wet, the fin dehumidifying material layer and heat tube moisture material layer of heating exchange heat with the working-medium water in corresponding portion shell, heat pipe
Working-medium water is heated vaporization, to take away air draft heat, then air draft is cooled down dry after through wind exhausting outlet drain into outdoor；
Winter Fresh air handing process are as follows: the fresh air that the fresh inlet enters removes moist wood by the fin on fin outer surface
Heat tube moisture material layer on the bed of material and annular heat pipe outer surface, fin dehumidifying material layer and heat tube moisture material layer are cooled and go
Wet, cooling fin dehumidifying material layer and heat tube moisture material layer exchange heat with the water vapour in corresponding portion shell, and water steams
Vapour is condensed liquefaction, to take away fresh air cooling capacity, then the outdoor fresh air of low temperature drying obtains warming and humidifying, after fresh air exports
It is standby into other air conditioner heats.
Compared with the prior art, the present invention has the following advantages:
1, heat pipe runner combined type full heat recovery device of the invention, the device utilize indoor discharge air and outdoor introduction
Fresh air carry out sensible heat and latent heat exchange and recycle the energy, and then reach energy saving and keep draughty purpose,
Fresh air preheating can be humidified by pre-cooling of fresh air and dehumidifying in summer in winter, have and recycle efficient, installation simply, just
In maintenance, easily controllable, equipment investment return period are short the advantages that.
2, heat pipe runner combined type full heat recovery device of the invention, multiple groups annular heat pipe be interspersed in fin air duct it
Between, annular heat pipe is superconducting heat transfer element, so enhancing heat transfer process, improves Exposure degree efficiency.
3, heat pipe runner combined type full heat recovery device of the invention will be coated in fin and annular heat pipe table except wet stock
Face forms fin dehumidifying material layer and heat tube moisture material layer, due to except there are steam partial pressures between wet stock and air
Power is poor, so realizing wet transmitting between two kinds of fluids.
4, heat pipe runner combined type full heat recovery device of the invention, annular heat pipe slowly turn under driving motor effect
It is dynamic, exchange efficiency of the heat-pipe working medium water between evaporator section and condensation segment is accelerated, to improve heat exchange efficiency.
5, heat pipe runner combined type full heat recovery device of the invention, with annular heat pipe Exposure degree, fin removes wet stock
Layer and heat tube moisture material layer recovery of latent heat, every heat pipe self-contained heat exchange system, recycling are efficiently, compact-sized；It is returned with ordinary hot
The honeycomb air duct for receiving runner is compared, and fin air duct is larger without the problem of resulting in blockage.
6, heat pipe runner combined type full heat recovery device of the invention, by the way that flushing channel is arranged, when fin air duct
When being just transferred to fresh air area from exhaust zone, fresh air and air draft mixed airflow in fin air duct are able to enter flushing channel and drain into
It is outdoor.
7, the method and step of heat pipe runner combined type total heat recovery method of the invention is simple, and it is convenient to realize, can be realized
Total heat recovery under summer and winter condition, it is practical, convenient for promoting the use of.
In conclusion improving Exposure degree efficiency invention enhances heat transfer process, summer and winter work can be realized
Total heat recovery under condition, it is practical, convenient for promoting the use of.
Below by drawings and examples, technical scheme of the present invention will be described in further detail.
Detailed description of the invention
Fig. 1 is the perspective view of heat pipe runner combined type full heat recovery device of the present invention.
Fig. 2 is the decomposition texture schematic diagram of heat pipe runner combined type full heat recovery device of the present invention.
Fig. 3 is the structural schematic diagram of heat pipe wheel set assembly of the present invention.
Fig. 4 is main view of the Fig. 3 of the present invention in addition to driving motor and belt.
Fig. 5 is the connection relationship diagram of annular heat pipe of the present invention and fin.
Fig. 6 is the fragmentary cross-sectional view of heat pipe wheel set assembly of the present invention.
Fig. 7 be back cabinet of the present invention, after first after subregion partition and second subregion partition connection relationship diagram.
Fig. 8 is the structural schematic diagram of annular heat pipe of the present invention.
Description of symbols:
1-box shell；2-wind exhausting outlets；3-front housings；
4-back cabinets；5-runners；5-1-wheel shell；
5-2-fin；5-3-fin air duct；5-4-fin dehumidifying material layer；
6-transmission belts；7-driving motors；8-preceding subregion partitions；
The outlet of 9-fresh airs；10-air draft imports；11-box shells；
12-fins；13-annular heat pipes；13-1-shell；
13-2-capping；13-3-heat pipe wicks；13-4-vacuum chamber；
13-5-heat tube moisture material layer；14-fresh inlet channels；
15-wind exhausting outlet channels；16-air draft intake channels；17-fresh air exit passageways；
18-flushing channels；Subregion partition after 19-the first；Subregion partition after 20-the second；
21-intercommunicating pores.
Specific embodiment
As shown in FIG. 1 to FIG. 8, heat pipe runner combined type full heat recovery device of the invention, including box shell 11, setting are in case
The front housing 3 of front side, the back cabinet 4 being arranged on rear side of in box shell 11 and the heat that middle position in box shell 11 is set in shell 11
Pipe wheel set assembly is provided with fresh inlet channel 14 and wind exhausting outlet channel 15 on the front housing 3, sets on the back cabinet 4
It is equipped with the fresh air exit passageway 17 being oppositely arranged with fresh inlet channel 14 and the air draft being oppositely arranged with wind exhausting outlet channel 15
Intake channel 16, be provided on the front side wall of the box shell 11 fresh inlet 1 being oppositely arranged with fresh inlet channel 14 and with
The wind exhausting outlet 2 that wind exhausting outlet channel 15 is oppositely arranged is provided with and fresh air exit passageway 17 on the rear wall of the box shell 11
The fresh air outlet 9 being oppositely arranged and the air draft import 10 that is oppositely arranged with air draft intake channel 16, in the box shell 11 fresh air into
Mouth channel 14 and 17 region of fresh air exit passageway are fresh air area, air draft intake channel 16 and wind exhausting outlet in the box shell 11
15 region of channel is exhaust zone；The heat pipe wheel set assembly includes runner 5, annular heat pipe 13 and mentions for rotating for runner
For the driving motor 7 of power, the runner 5 is included the wheel shell 5-1 of annular and is dissipated around with the geometric center of wheel shell 5-1
The inner space wheel shell 5-1 is separated into multiple fins by the even muti-piece fin 5-2 being laid in wheel shell 5-1, fin 5-2 described in muti-piece
Fin air duct 5-3, each fin air duct 5-3 adjacent with two panels is clipped in by the adjacent fin 5-2 of two panels
One section of wheel shell 5-1 between 5-2 is surrounded, and the fin air duct 5-3 is connected to fresh inlet channel 14 and fresh air in fresh air area
Exit passageway 17 and flushing channel 18, the fin air duct 5-3 exhaust zone be connected to wind exhausting outlet channel 15 and air draft into
Mouth channel 16, the annular heat pipe 13 are laid along the axial direction of runner 5 in multilayer in wheel shell 5-1, and every layer of annular heat pipe 13 wraps
The more annular heat pipes 13 laid in concentric circles are included, every annular heat pipe 13 is interspersed on fin 5-2；The annular heat pipe 13
Outer surface on be provided with heat tube moisture material layer 13-5, be provided on the outer surface of the fin 5-2 fin dehumidifying material layer
5-4 is connected with the transmission belt 6 being connected across on wheel shell 5-1 on the output shaft of the driving motor 7.
When it is implemented, the shape of the wheel shell 5-1 is circular ring shape.Fin 5-2 is used for stationary annular heat pipe 13, annular heat
Pipe 13 exchanges heat for strengthening fluid.Heat tube moisture material layer 13-5 and fin dehumidifying material layer 5-4 and air draft air-flow or new general mood
Not only Exchange of apparent heat had occurred between stream but also has carried out wet transmitting.
In the present embodiment, as shown in Fig. 2, front housing round hole is provided on the front housing 3, the front housing round hole
It is inside provided with the preceding subregion partition 8 for front housing round hole to be divided into two 180 ° of sector channels, is located at preceding subregion partition 8
180 ° of sector channels of upside are fresh inlet channel 14, and 180 ° of sector channels positioned at preceding 8 downside of subregion partition go out for air draft
Mouth channel 15.
In the present embodiment, the thickness of the preceding subregion partition 8 is more than or equal to the maximum between two pieces of fin 5-2 of arbitrary neighborhood
Distance.
Due to current partition partition 8 thickness be less than adjacent two pieces of fin 5-2 between maximum distance when, fresh air air-flow and
Air draft air-flow will be mixed in the corresponding fin air duct 5-3 of preceding subregion partition 8, cause the intersection of fresh air and air draft
Pollution, therefore, the thickness of preceding subregion partition 8 is set greater than equal to the maximum distance between two pieces of fin 5-2 of arbitrary neighborhood,
It can be avoided the cross contamination of fresh air and air draft.
In the present embodiment, as shown in Fig. 2, be additionally provided with flushing channel 18 on the back cabinet 4, the flushing channel 18 with
Air draft intake channel 16 is connected.
In the present embodiment, as shown in Figure 2 and Figure 7, back cabinet round hole, the back cabinet are provided on the back cabinet 4
Subregion partition 19 after being provided with first for back cabinet round hole to be divided into two 180 ° of sector channels in round hole, is located at
It is provided in 180 ° of sector channels of 19 upside of subregion partition after first and leads to for 180 ° of sector channels to be divided into 165 ° of sectors
Subregion partition 20 after the second of road and 15 ° of sector channels, 180 ° of sector channels of 19 downside of subregion partition are row after first
Wind inlet channel 16,165 ° of sector channels are fresh air exit passageway 17, and 15 ° of sector channels are flushing channel 18, institute
Be provided on subregion partition 19 after stating first the intercommunicating pore 21 positioned at the lower section of flushing channel 18, the flushing channel 18 and air draft into
Mouth channel 16 is connected by intercommunicating pore 21.
When it is implemented, the flushing channel 18 is positioned at the upper right side of subregion partition 19 after first.Since fin air is logical
When road 5-3 enters fresh air area from exhaust zone, fin air duct 5-3 retains foul atmosphere air draft, so fin air duct 5-3
A small gangs of fresh air air-flow purging is first passed through, the shallow bid mixed airflow after purging cannot be sent into interior, therefore enter flushing channel
18, enter air draft intake channel 16 using intercommunicating pore 21, send to be mixed with air draft to outdoor；It can prevent from arranging on a small quantity in this way
Wind incorporation fresh air enters the room.
In the present embodiment, the thickness of subregion partition 19 is more than or equal between two pieces of fin 5-2 of arbitrary neighborhood after described first
Maximum distance.
When being less than the maximum distance between adjacent two pieces of fin 5-2 due to the thickness of the subregion partition 19 after first, fresh air
Air-flow and air draft air-flow will be mixed after first in the corresponding fin air duct 5-3 of subregion partition 19, cause fresh air
Therefore the thickness of subregion partition 19 after first is set greater than equal to two pieces of fins of arbitrary neighborhood with the cross contamination of air draft
Maximum distance between 5-2 can be avoided the cross contamination of fresh air and air draft.
In the present embodiment, as shown in Figure 6 and Figure 8, the annular heat pipe 13 includes shell 13-1 and is arranged in shell 13-1
On capping 13-2, be provided with heat pipe wicks 13-3 on the inner surface of the shell 13-1, the inner cavity the shell 13-1 is true
Heat-pipe working medium is filled in cavity 13-4, the vacuum chamber 13-4.
When it is implemented, the heat-pipe working medium is water.
The presence of the heat pipe wicks 13-3 can guarantee that the heat-pipe working medium in annular heat pipe 13 quickly sets up circulation,
Accelerate the starting speed of annular heat pipe 13；Heat-pipe working medium after condensation is collected to heat pipe wicks 13-3 through shell 13-1,
Under the swabbing action of heat pipe wicks 13-3, the evaporator section of annular heat pipe 13 is flowed back into again.
In the present embodiment, the fin 5-2 and wheel shell 5-1 are all made of aluminum alloy materials and are made, and the shell 13-1 is used
Red copper material is made, and the heat tube moisture material layer 13-5 is coated on the outer surface of shell 13-1 using dip-coating method, institute
Fin dehumidifying material layer 5-4 is stated using dip-coating method coated on the outer surface of fin 5-2.
In the present embodiment, the heat tube moisture material layer 13-5 is coated in the outer surface of shell 13-1 using dip-coating method
On detailed process are as follows:
Step A1, annular heat pipe 13 is immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to ring
The surface of shape heat pipe 13 carries out ungrease treatment of deoiling；
Step A2, after pulling annular heat pipe 13 out of sodium hydroxide solution out, annular heat pipe is cleaned with distilled water and ethyl alcohol
13 surfaces, then it is placed in drying in oven；
Step A3, silica gel particle is coated on by 13 surface of annular heat pipe using aqueous compound adhesive, it is molten is impregnated into silicon after drying
1 hour~5 hours in glue, drying is taken out later, is repeated 3~8 times；
The wet stock that removes of dehumidifying material layer 13-5 uses silica gel particle, except the adhesive of wet stock and 13 surface of annular heat pipe
Aqueous compound adhesive is selected, aqueous compound adhesive replaces organic solvent with water, compared with solvent type compound adhesive asepsis environment-protecting；
Step A4, annular heat pipe 13 is immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, makes chlorine
Change lithium to be sufficiently submerged in silica gel particle duct, then is placed in drying in oven；
Step A5, annular heat pipe 13 is put into temperature is 30 DEG C, humidity is that lyolysis is forced in the climatic chamber of 90%RH
12h, then it is placed in drying in oven；
By step A5, it can be avoided lithium chloride solution and overflow corrosion annular heat pipe 13；
The fin dehumidifying material layer 5-4 is using dip-coating method coated in the detailed process on the outer surface of fin 5-2
Are as follows:
Step B1, fin 5-2 is immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to fin
The surface of 5-2 carries out ungrease treatment of deoiling；
Step B2, after pulling fin 5-2 out of sodium hydroxide solution out, the surface fin 5-2 is cleaned with distilled water and ethyl alcohol,
It is placed in drying in oven again；
Step B3, silica gel particle is coated on by the surface fin 5-2 using aqueous compound adhesive, is impregnated into silica solution after drying
1 hour~5 hours, drying is taken out later, is repeated 3~8 times；
The wet stock that removes of dehumidifying material layer 13-5 uses silica gel particle, except wet stock and the adhesive on the surface fin 5-2 select
With aqueous compound adhesive, aqueous compound adhesive replaces organic solvent with water, compared with solvent type compound adhesive asepsis environment-protecting；
Step B4, fin 5-2 is immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, makes chlorination
Lithium is sufficiently submerged in silica gel particle duct, then is placed in drying in oven；
Step B5, fin 5-2 is put into pressure lyolysis 12h in the climatic chamber that temperature is 30 DEG C, humidity is 90%RH,
It is placed in drying in oven again.
By step B5, it can be avoided lithium chloride solution and overflow corrosion fin 5-2.
Heat pipe runner combined type total heat recovery method of the invention, including two kinds of situations of summer operating mode and winter condition, summer
Under season operating condition, fresh air area is evaporator section, and exhaust zone is condensation segment, and under winter condition, fresh air area is condensation segment, and exhaust zone is evaporation
Section；By after heat-pipe working medium water vapor, water vapour is run to 13 condensation segment of annular heat pipe, cold the evaporator section of the annular heat pipe 13
Solidifying section releases heat and is condensed into liquid, and liquid water is by heat pipe wicks 13-3, under heat pipe wicks 13-3 swabbing action
The evaporator section of annular heat pipe 13 is flowed back into, vaporization of being heated again, so on circulate；When driving motor 7 rotates counterclockwise, pass through
Transmission belt 6 drives runner 5 to rotate counterclockwise, and the annular heat pipe 13 and fin 5-2 are slowly rotated under the drive of wheel shell 5, are added
Fast exchange process of the heat-pipe working medium water between evaporator section and condensation segment, improves heat exchange efficiency；Runner 5 constantly rotates, newly
Wind passes through the fresh air area of runner 5, and air draft inversely passes through the exhaust zone of runner 5 simultaneously, and fresh air and air draft are alternately inverse in this way
To by runner 5, fresh air and row when fin air duct 5-3 has just been transferred to fresh air area from exhaust zone, in fin air duct 5-3
Wind mixed airflow enters flushing channel 18 and drains into outdoor；
Wherein, under summer operating mode, the lower room air of temperature and humidity passes through the fin air duct 5-3 of corresponding portion
When, 13 sections of annular heat pipe in corresponding fin air duct 5-3 are cooled, and fin dehumidifies material layer 5-4 and heat tube moisture material
Bed of material 13-5 releases partial moisture contained therein due to water vapor partial pressure differential, and in a flash under, just with exhaust airflow phase
Contact, cooled 13 sections of annular heat pipe are just taken turns with the fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 after drying
Go to fresh air area, be in contact with the fresh air of entrance, then the fresh air of high temperature and humidity be just able to cooling dry, i.e., into
It first carries out precooling and drying in advance before other heat and wet treatments of row；
Summer Fresh air handing process are as follows: the fresh air that the fresh inlet 1 enters is removed by the fin on the outer surface fin 5-2
Heat tube moisture material layer 13-5 on 13 outer surface moist wood bed of material 5-4 and annular heat pipe, fin dehumidifying material layer 5-4 and heat pipe remove
Moist wood bed of material 13-5 is heated humidification, the fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 and corresponding portion of heating
Heat-pipe working medium water in shell 13-1 exchanges heat, and heat-pipe working medium water is heated vaporization, to take away fresh air heat, then high temperature
The outdoor fresh air of high humidity obtains cooling and dries, and it is standby to enter other air conditioner heats behind fresh air outlet 9；
Summer Air exhaust process are as follows: the air draft that the air draft import 10 enters is removed by the fin on 12 outer surface of fin
Heat tube moisture material layer 13-5 on 13 outer surface moist wood bed of material 5-4 and annular heat pipe, fin dehumidifying material layer 5-4 and heat pipe remove
Moist wood bed of material 13-5 is cooled to dry, cooling fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 and corresponding portion
Water vapour in shell 13-1 exchanges heat, and water vapour is condensed liquefaction, to take away exhaust cold, then air draft be heated plus
Other equipment are discharged or entered after wet through wind exhausting outlet 2；
Wherein, under winter condition, the fresh air of outdoor low temperature drying needs to recycle the hot and wet of indoor exhaust wind, works as winter
When the higher room air of temperature and humidity passes through the fin air duct 5-3 of corresponding portion, in corresponding fin air duct 5-3
13 sections of annular heat pipe be heated, fin dehumidify material layer 5-4 and heat tube moisture material layer 13-5 due to steam partial pressure
Difference adsorbs partial moisture contained in air, and in a flash under, is just in contact with exhaust airflow, the annular heat pipe being heated
13 sections are just taken turns with the fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 after moisture absorption and go to fresh air area, new with entrance
Fresh air is in contact, and then the fresh air of low temperature drying is just able to warming and humidifying, i.e., before carrying out other heat and wet treatments first
Carry out preheating and pre-humidifying；
Winter Air exhaust process are as follows: the air draft that the air draft import 10 enters is by the fin on the outer surface fin 5-2
The heat tube moisture material layer 13-5 to dehumidify on material layer 5-4 and 13 outer surface of annular heat pipe, fin dehumidifying material layer 5-4 and heat pipe
Dehumidifying material layer 13-5 is heated humidification, the fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 of heating and corresponding portion
The working-medium water being in charge of in shell 13-1 exchanges heat, and heat-pipe working medium water is heated vaporization, to take away air draft heat, then air draft quilt
Cool down and drains into outdoor through wind exhausting outlet 2 after drying；
Winter Fresh air handing process are as follows: the fresh air that the fresh inlet 1 enters is removed by the fin on the outer surface fin 5-2
Heat tube moisture material layer 13-5 on 13 outer surface moist wood bed of material 5-4 and annular heat pipe, fin dehumidifying material layer 5-4 and heat pipe remove
Moist wood bed of material 13-5 is cooled to dry, cooling fin dehumidifying material layer 5-4 and heat tube moisture material layer 13-5 and corresponding portion
Water vapour in shell 13-1 exchanges heat, and water vapour is condensed liquefaction, to take away fresh air cooling capacity, the then room of low temperature drying
Outer fresh air obtains warming and humidifying, and it is standby to enter other air conditioner heats behind fresh air outlet 9.
The above is only presently preferred embodiments of the present invention, is not intended to limit the invention in any way, it is all according to the present invention
Technical spirit any simple modification to the above embodiments, change and equivalent structural changes, still fall within skill of the present invention
In the protection scope of art scheme.
Claims (10)
1. a kind of heat pipe runner combined type full heat recovery device, it is characterised in that: including box shell (11), setting in box shell (11)
Back cabinet (4) and setting of the front housing (3), setting of front side on rear side of box shell (11) is interior are in box shell (11) interior middle position
Heat pipe wheel set assembly, is provided with fresh inlet channel (14) and wind exhausting outlet channel (15) on the front housing (3), it is described after machine
Be provided on shell (4) the fresh air exit passageway (17) being oppositely arranged with fresh inlet channel (14) and with wind exhausting outlet channel (15)
The air draft intake channel (16) being oppositely arranged is provided on the front side wall of the box shell (11) opposite with fresh inlet channel (14)
The fresh inlet (1) of setting and the wind exhausting outlet (2) being oppositely arranged with wind exhausting outlet channel (15), the rear side of the box shell (11)
It is provided with the fresh air outlet (9) being oppositely arranged with fresh air exit passageway (17) on wall and is oppositely arranged with air draft intake channel (16)
Air draft import (10), the interior fresh inlet channel (14) of the box shell (11) and fresh air exit passageway (17) region are fresh air
Area, the interior air draft intake channel (16) of the box shell (11) and wind exhausting outlet channel (15) region are exhaust zone；The heat pipe
Wheel set assembly includes runner (5), annular heat pipe (13) and provides the driving motor (7) of power for rotating for runner, and described turn
Wheel (5) is included the wheel shell (5-1) of annular and is dissipated around with the geometric center of wheel shell (5-1) uniformly distributed at wheel shell (5-1)
The inner space wheel shell (5-1) is separated into multiple fin air ducts by interior muti-piece fin (5-2), fin (5-2) described in muti-piece
(5-3), each fin air duct (5-3) is by the adjacent fin of two panels (5-2) and is clipped in the adjacent fin (5- of two panels
2) one section of wheel shell (5-1) between surrounds, the fin air duct (5-3) fresh air area connection fresh inlet channel (14) with
Fresh air exit passageway (17) and flushing channel (18), the fin air duct (5-3) are connected to wind exhausting outlet channel in exhaust zone
(15) with air draft intake channel (16), the annular heat pipe (13) is in laminates along the axial direction of runner (5) in wheel shell (5-1)
If every layer of annular heat pipe (13) includes the more annular heat pipes (13) laid in concentric circles, every annular heat pipe (13) is worn
It is inserted on fin (5-2)；Heat tube moisture material layer (13-5), the fin are provided on the outer surface of the annular heat pipe (13)
It is provided with fin dehumidifying material layer (5-4) on the outer surface of (5-2), is connected with bridging on the output shaft of the driving motor (7)
Transmission belt (6) on wheel shell (5-1).
2. a kind of heat pipe runner combined type full heat recovery device described in accordance with the claim 1, it is characterised in that: the front housing
(3) it is provided with front housing round hole on, is provided in the front housing round hole for front housing round hole to be divided into two
The preceding subregion partition (8) of 180 ° of sector channels, being located at 180 ° of sector channels on the upside of preceding subregion partition (8) is fresh inlet channel
(14), being located at 180 ° of sector channels on the downside of preceding subregion partition (8) is wind exhausting outlet channel (15).
3. a kind of heat pipe runner combined type full heat recovery device according to claim 2, it is characterised in that: the preceding subregion
The thickness of partition (8) is more than or equal to the maximum distance between two pieces of fins (5-2) of arbitrary neighborhood.
4. a kind of heat pipe runner combined type full heat recovery device described in accordance with the claim 1, it is characterised in that: the back cabinet
(4) it is additionally provided on flushing channel (18), the flushing channel (18) is connected with air draft intake channel (16).
5. a kind of heat pipe runner combined type full heat recovery device according to claim 4, it is characterised in that: the back cabinet
(4) it is provided with back cabinet round hole on, is provided in the back cabinet round hole for back cabinet round hole to be divided into two
Subregion partition (19) after the first of 180 ° of sector channels are set in 180 ° of sector channels on the upside of subregion partition (19) after first
Subregion partition (20) after being equipped with second for 180 ° of sector channels to be divided into 165 ° of sector channels and 15 ° of sector channels, position
180 ° of sector channels after first on the downside of subregion partition (19) are air draft intake channel (16), and 165 ° of sector channels are new
Wind exit passageway (17), 15 ° of sector channels are flushing channel (18), are provided with position on subregion partition (19) after described first
Intercommunicating pore (21) below flushing channel (18), the flushing channel (18) and air draft intake channel (16) pass through intercommunicating pore
(21) it is connected.
6. a kind of heat pipe runner combined type full heat recovery device according to claim 5, it is characterised in that: after described first
The thickness of subregion partition (19) is more than or equal to the maximum distance between two pieces of fins (5-2) of arbitrary neighborhood.
7. a kind of heat pipe runner combined type full heat recovery device described in accordance with the claim 1, it is characterised in that: the annular heat
Pipe (13) includes the capping (13-2) on shell (13-1) of shell (13-1) and setting, on the inner surface of the shell (13-1)
It is provided with heat pipe wicks (13-3), the shell inner cavity (13-1) is vacuum chamber (13-4), is filled out in the vacuum chamber (13-4)
Filled with heat-pipe working medium.
8. a kind of heat pipe runner combined type full heat recovery device according to claim 7, it is characterised in that: the fin
(5-2) and wheel shell (5-1) are all made of aluminum alloy materials and are made, and the shell (13-1) is made of red copper material, the heat pipe
Dehumidifying material layer (13-5) is coated on the outer surface of shell (13-1) using dip-coating method, the fin dehumidifying material layer
(5-4) is using dip-coating method coated on the outer surface of fin (5-2).
9. a kind of heat pipe runner combined type full heat recovery device according to claim 8, it is characterised in that: the heat pipe removes
The moist wood bed of material (13-5) is using dip-coating method coated in the detailed process on the outer surface of shell (13-1) are as follows:
Step A1, annular heat pipe (13) are immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to annular
The surface of heat pipe (13) carries out ungrease treatment of deoiling；
Step A2, after pulling annular heat pipe (13) out of sodium hydroxide solution out, annular heat pipe is cleaned with distilled water and ethyl alcohol
(13) surface, then it is placed in drying in oven；
Step A3, silica gel particle is coated on by annular heat pipe (13) surface using aqueous compound adhesive, is impregnated into silica solution after drying
In 1 hour~5 hours, later take out drying, repeat 3~8 times；
Step A4, annular heat pipe (13) are immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, makes chlorination
Lithium is sufficiently submerged in silica gel particle duct, then is placed in drying in oven；
Step A5, annular heat pipe (13) is put into temperature is 30 DEG C, humidity is that lyolysis is forced in the climatic chamber of 90%RH
12h, then it is placed in drying in oven；
Fin dehumidifying material layer (5-4) is using dip-coating method coated in the detailed process on the outer surface of fin (5-2)
Are as follows:
Step B1, fin (5-2) is immersed into 60s in the sodium hydroxide solution that substance withdrawl syndrome is 0.1mol/L, to fin (5-
2) surface carries out ungrease treatment of deoiling；
Step B2, after pulling fin (5-2) out of sodium hydroxide solution out, the surface fin (5-2) is cleaned with distilled water and ethyl alcohol,
It is placed in drying in oven again；
Step B3, silica gel particle is coated on by the surface fin (5-2) using aqueous compound adhesive, is impregnated into after drying 1 in silica solution
Hour~5 hours, drying is taken out later, is repeated 3~8 times；
Step B4, fin (5-2) is immersed in the lithium chloride solution that mass fraction is 45% 6 hours~10 hours, makes lithium chloride
It is sufficiently submerged in silica gel particle duct, then is placed in drying in oven；
Step B5, fin (5-2) is put into pressure lyolysis 12h in the climatic chamber that temperature is 30 DEG C, humidity is 90%RH, then
It is placed in drying in oven.
10. a kind of heat pipe runner combined type total heat recovery method using device as described in claim 1, which is characterized in that should
Method includes two kinds of situations of summer operating mode and winter condition, and under summer operating mode, fresh air area is evaporator section, and exhaust zone is condensation segment,
Under winter condition, fresh air area is condensation segment, and exhaust zone is evaporator section；The evaporator section of the annular heat pipe (13) is by heat-pipe working medium water
After vaporization, water vapour is run to annular heat pipe (13) condensation segment, is released heat in condensation segment and is condensed into liquid, liquid water by
Heat pipe wicks (13-3) flow back into the evaporator section of annular heat pipe (13), again under heat pipe wicks (13-3) swabbing action
Heated vaporization, so on circulate；When driving motor (7) rotates counterclockwise, drive runner (5) counterclockwise by transmission belt (6)
Rotation, the annular heat pipe (13) and fin (5-2) slowly rotate under the drive of wheel shell (5), accelerate heat-pipe working medium water and exist
Exchange process between evaporator section and condensation segment, improves heat exchange efficiency；Runner (5) constantly rotates, and fresh air passes through runner (5)
Fresh air area, the reverse exhaust zone for passing through runner (5), fresh air and air draft alternately inversely pass through runner in this way simultaneously for air draft
(5), when fin air duct (5-3) has just been transferred to fresh air area from exhaust zone, the fresh air and air draft in fin air duct (5-3) are mixed
Conjunction air-flow enters flushing channel (18) and drains into outdoor；
Wherein, under summer operating mode, the lower room air of temperature and humidity passes through the fin air duct (5-3) of corresponding portion
When, annular heat pipe (13) section in corresponding fin air duct (5-3) is cooled, and fin dehumidifies material layer (5-4) and heat pipe
Dehumidifying material layer (13-5) releases partial moisture contained therein due to water vapor partial pressure differential, and in a flash under, just with row
Wind air is in contact, cooled annular heat pipe (13) section and fin dehumidifying material layer (5-4) and heat tube moisture material after drying
The bed of material (13-5) just takes turns and goes to fresh air area, is in contact with the fresh air of entrance, then the fresh air of high temperature and humidity is just able to
Cooling is dried, i.e., first carries out precooling and drying in advance before carrying out other heat and wet treatments；
Summer Fresh air handing process are as follows: the fresh air that the fresh inlet (1) enters is removed by the fin on the outer surface fin (5-2)
Heat tube moisture material layer (13-5) on the moist wood bed of material (5-4) and annular heat pipe (13) outer surface, fin dehumidify material layer (5-4)
Humidification, fin dehumidifying material layer (5-4) of heating and heat tube moisture material layer are heated with heat tube moisture material layer (13-5)
(13-5) exchanges heat with the heat-pipe working medium water in corresponding portion shell (13-1), and heat-pipe working medium water is heated vaporization, thus band
Fresh air heat is walked, then the outdoor fresh air of high temperature and humidity obtains cooling down and dry, and enters other air conditioner heats after fresh air exports (9)
It is standby；
Summer Air exhaust process are as follows: the air draft that the air draft import (10) enters is removed by the fin on fin (12) outer surface
Heat tube moisture material layer (13-5) on the moist wood bed of material (5-4) and annular heat pipe (13) outer surface, fin dehumidify material layer (5-4)
It is cooled and dries with heat tube moisture material layer (13-5), cooling fin dehumidifying material layer (5-4) and heat tube moisture material layer
(13-5) exchanges heat with the water vapour in corresponding portion shell (13-1), and water vapour is condensed liquefaction, so that it is cold to take away air draft
Amount, then air draft, which is heated, is discharged through wind exhausting outlet (2) or enters other equipment after humidification；
Wherein, under winter condition, the fresh air of outdoor low temperature drying needs to recycle the hot and wet of indoor exhaust wind, works as winter temperature
When passing through fin air duct (5-3) of corresponding portion with the higher room air of humidity, in corresponding fin air duct (5-3)
Annular heat pipe (13) section be heated, fin dehumidifies material layer (5-4) and heat tube moisture material layer (13-5) due to vapor
Partial pressure is poor, adsorbs partial moisture contained in air, and in a flash under, be just in contact with exhaust airflow, the ring being heated
Fin dehumidifying material layer (5-4) and heat tube moisture material layer (13-5) after shape heat pipe (13) section and moisture absorption are just taken turns and go to fresh air
Area is in contact with the fresh air of entrance, and then the fresh air of low temperature drying is just able to warming and humidifying, that is, is carrying out other heat
Preheating and pre-humidifying are first carried out before wet process；
Winter Air exhaust process are as follows: the air draft that the air draft import (10) enters is by the fin on the outer surface fin (5-2)
The heat tube moisture material layer (13-5) to dehumidify on the outer surface material layer (5-4) and annular heat pipe (13), fin dehumidifying material layer (5-
4) and heat tube moisture material layer (13-5) is heated humidification, fin dehumidifying material layer (5-4) of heating and heat tube moisture material layer
(13-5) exchanges heat with the working-medium water in corresponding portion shell (13-1), and heat-pipe working medium water is heated vaporization, thus the row of taking away
Wind-heat amount, then air draft is cooled down dry after through wind exhausting outlet (2) drain into outdoor；
Winter Fresh air handing process are as follows: the fresh air that the fresh inlet (1) enters is removed by the fin on the outer surface fin (5-2)
Heat tube moisture material layer (13-5) on the moist wood bed of material (5-4) and annular heat pipe (13) outer surface, fin dehumidify material layer (5-4)
It is cooled and dries with heat tube moisture material layer (13-5), cooling fin dehumidifying material layer (5-4) and heat tube moisture material layer
(13-5) exchanges heat with the water vapour in corresponding portion shell (13-1), and water vapour is condensed liquefaction, to take away new air-cooled
Amount, then the outdoor fresh air of low temperature drying obtains warming and humidifying, and it is standby to enter other air conditioner heats after fresh air exports (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811459046.4A CN109539844B (en) | 2018-11-30 | 2018-11-30 | Heat pipe and runner combined type total heat recovery device and method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811459046.4A CN109539844B (en) | 2018-11-30 | 2018-11-30 | Heat pipe and runner combined type total heat recovery device and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109539844A true CN109539844A (en) | 2019-03-29 |
| CN109539844B CN109539844B (en) | 2020-02-04 |
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ID=65852114
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811459046.4A Active CN109539844B (en) | 2018-11-30 | 2018-11-30 | Heat pipe and runner combined type total heat recovery device and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112097442A (en) * | 2019-06-18 | 2020-12-18 | 青岛海尔智能技术研发有限公司 | Airflow dehumidification module for refrigeration and freezing device and refrigeration and freezing device |
| CN114505996A (en) * | 2022-02-12 | 2022-05-17 | 高文强 | Water-soluble polyethylene film heat setting equipment |
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| CN206543512U (en) * | 2017-02-14 | 2017-10-10 | 袁一军 | A kind of efficient heat transfer mass transfer system of utilization runner |
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| JPS52140055A (en) * | 1976-05-18 | 1977-11-22 | Ebara Corp | Rotating type heat exchanger |
| US4405013A (en) * | 1979-01-10 | 1983-09-20 | Gadelius K.K. | Rotary type heat pipe heat exchanger |
| CN2300839Y (en) * | 1997-04-14 | 1998-12-16 | 刘宗源 | Moisture absorption runner |
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| Publication number | Publication date |
|---|---|
| CN109539844B (en) | 2020-02-04 |
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