CN207350743U - A kind of turbulent flow cold and heat recovery device - Google Patents
A kind of turbulent flow cold and heat recovery device Download PDFInfo
- Publication number
- CN207350743U CN207350743U CN201721423693.0U CN201721423693U CN207350743U CN 207350743 U CN207350743 U CN 207350743U CN 201721423693 U CN201721423693 U CN 201721423693U CN 207350743 U CN207350743 U CN 207350743U
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- air
- condensation chamber
- evaporation cavity
- air outlet
- air inlet
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- 238000011084 recovery Methods 0.000 title claims abstract description 33
- 238000009833 condensation Methods 0.000 claims abstract description 72
- 230000005494 condensation Effects 0.000 claims abstract description 72
- 238000001704 evaporation Methods 0.000 claims abstract description 71
- 230000008020 evaporation Effects 0.000 claims abstract description 71
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 239000005030 aluminium foil Substances 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 238000002309 gasification Methods 0.000 claims description 3
- 238000012864 cross contamination Methods 0.000 abstract description 6
- 230000001932 seasonal effect Effects 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 description 10
- 238000009826 distribution Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 125000001475 halogen functional group Chemical group 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005373 pervaporation Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
A kind of turbulent flow cold and heat recovery device, carries out recuperation of heat for the inlet air to user terminal and air draft, condensation chamber and evaporation cavity is respectively formed with recover, fresh air air inlet, fresh air outlet, air draft air inlet and air draft air outlet are equipped with turbulent cold and heat recovery device；Condensation chamber is equipped with condensation chamber air inlet and condensation chamber air outlet, evaporation cavity is equipped with evaporation cavity air inlet and evaporation cavity air outlet, fresh air air inlet is respectively connected to evaporation cavity air inlet and condensation chamber air outlet by pipeline, fresh air outlet is respectively connected to evaporation cavity air outlet and condensation chamber air inlet by pipeline, air draft air inlet is respectively connected to condensation chamber air inlet and evaporation cavity air outlet by pipeline, and air draft air outlet is respectively connected to condensation chamber air outlet and evaporation cavity air inlet by pipeline.A kind of turbulent cold and heat recovery device of the utility model, there is provided Various Seasonal user terminal is entered with the cold of discharge and being separately recovered for heat, while avoid the cross contamination of fresh air and air draft, fully ensure that the cleannes of fresh air.
Description
Technical field
The utility model belongs to air-conditioning equipment field, and in particular to a kind of turbulent flow cold and heat recovery device.
Background technology
Since deficiency is realized in the environmental protection and energy saving of technical merit finite sum, cause the energy regenerating wretched insufficiency of space air draft or return
Debit's formula is incorrect, causes the waste and some cross contaminations of the energy.
Currently for the energy regenerating of space air draft, there are following shortcoming：
1. present space air draft, is expelled directly out mostly, is not recycled for the energy of air draft, cause the wave of the energy
Take.
2. some heat reclamation devices, there are certain requirements for use condition and occasion, while in heat recycle process, air draft with
Fresh air can be in contact, and cause cross contamination.
The patent application of Application No. 201210288759.5, discloses a kind of heat reclamation device, has in heat regenerator
Fin version, heat regenerator top have blast pipe to be connected with main box, and pneumatic operated valve, recuperation of heat are respectively housed in blast pipe upper and lower part
Device lower part is equipped with discharge pipe, and flow-mixing blower fan is housed in discharge pipe, and the outlet of flow-mixing blower fan is connected with auxiliary box body.
The patent application of Application No. 2016100699867, discloses a kind of turbulent-flow heat-exchanging device, includes housing, housing
Inside it is provided with the Heated container for accommodating cold fluid and the zone of heat liberation set along Heated container outer wall, the hot fluid leads to
Hot fluid inlet and hot fluid outlet ports are provided with road, is provided with grid in zone of heat liberation, grid and Heated container outer wall it
Between formed with narrow slit, flow into zone of heat liberation formed with turbulent chamber, hot fluid between grid from hot fluid inlet, passing through hot-fluid
Turbulent flow is produced in turbulent intracavitary during body passage, then is flowed out from hot fluid outlet ports.
The patent application of Application No. 2016109469485, discloses a kind of heating stove turbulent flow air distribution combustion device, including disorderly
Stream air register and the fire-banking device on turbulent air register top is arranged at, fire-banking device and turbulent air register are Split type structure, turbulent air distribution
Device is included with solar or lunar halo and turbulent wind distributing hole, and some rows of turbulent wind distributing hole point are evenly arranged in on solar or lunar halo inner wall, and turbulent air distribution
Angle is less than 180 ° between any two in hole, and air distribution ring outer wall both sides connect secondary air distribution air inlet, the inner and outer wall with solar or lunar halo it
Between form annular passage, annular passage connects the air inlet of two secondary air distributions.
Utility model content
To solve problem above, provide cold and heat recovery to the user, meet that cold and heat is separately recovered in Various Seasonal,
The cross contamination of fresh air and air draft is avoided at the same time, fully ensures that the cleannes of fresh air, it is cold that the utility model provides a kind of turbulent flow
Heat regenerator, its technical solution are specific as follows：
A kind of turbulent flow cold and heat recovery device, recuperation of heat is carried out for the inlet air to user terminal and air draft, it is characterised in that：
Condensation chamber (1) and evaporation cavity (2) are respectively formed with the turbulent cold and heat recovery device,
Be equipped with the turbulent cold and heat recovery device fresh air air inlet (3), fresh air outlet (4), air draft air inlet (5) with
Air draft air outlet (6)；
Condensation chamber air inlet (7) and condensation chamber air outlet (8) are equipped with the condensation chamber (1),
Evaporation cavity air inlet (9) and evaporation cavity air outlet (10) are equipped with the evaporation cavity (2),
The fresh air air inlet (3) is respectively connected to evaporation cavity air inlet (9) and condensation chamber air outlet (8) by pipeline,
The fresh air outlet (4) is respectively connected to evaporation cavity air outlet (10) and condensation chamber air inlet (7) by pipeline,
The air draft air inlet (5) is respectively connected to condensation chamber air inlet (7) and evaporation cavity air outlet (10) by pipeline,
The air draft air outlet (6) is respectively connected to condensation chamber air outlet (8) and evaporation cavity air inlet (9) by pipeline,
On the pipeline of fresh air air inlet (3) and evaporation cavity air inlet (9),
On the pipeline of fresh air air inlet (3) and condensation chamber air outlet (8),
On the pipeline of fresh air outlet (4) and evaporation cavity air outlet (10),
On the pipeline of fresh air outlet (4) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and evaporation cavity air outlet (10),
On the pipeline of air draft air outlet (6) and condenser air outlet (8) and air draft air outlet (6) and evaporation cavity air inlet
(9) on pipeline, it is respectively equipped with air-valve.
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
The condensation chamber (1) is accommodated with evaporation cavity (2) by housing (11) is unified；
The condensation chamber (1) is arranged on the surface of evaporation cavity,
Demarcation strip (12) is equipped between the condensation chamber (1) and evaporation cavity (2).
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
In housing, the top of condensation chamber sets the working medium manifold (13) being arranged along the horizontal and changed with what working medium manifold was connected
Heat pipe bundle (14),
The heat-exchanging tube bundle (14) along housing, in longitudinal direction through condensation chamber and evaporation cavity, array arrangement,
Needle-valve (15) is equipped with the working medium manifold (13).
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
The heat-exchanging tube bundle (14) is made of inner screw thread copper pipe.
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
Described runs through the condensation chamber heat-exchanging tube bundle that array is arranged with evaporation cavity along housing in longitudinal direction, wherein every heat exchange
Pipe takes the shape of the letter U to be set with inverted U-shaped slitless connection formula, is formed working medium gasification and is risen and the lower solidifying passage of liquefaction.
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
Insulating layer is equipped with described housing (3) periphery.
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
Fenestration fin is uniformly arranged all over the body in the heat-exchanging tube bundle (14).
A kind of turbulent cold and heat recovery device according to the present utility model, it is characterised in that：
The fenestration fin is aluminium foil fin.
A kind of turbulent cold and heat recovery device of the utility model, there is provided Various Seasonal enters user terminal the cold with discharge
With being separately recovered for heat, while the cross contamination of fresh air and air draft is avoided by accordingly setting, fully ensure that the cleaning of fresh air
Degree.
Brief description of the drawings
Fig. 1 is the overall structure diagram of the utility model；
Fig. 2 is the summer operation schematic diagram of the utility model；
Fig. 3 is the winter operating diagram of the utility model.
In figure, 1 is condensation chamber；2 be evaporation cavity；3 be fresh air air inlet；4 be fresh air outlet；5 be air draft air inlet；6
For air draft air outlet；7 be condensation chamber air inlet；8 be condensation chamber air outlet；9 be evaporation cavity air inlet；10 be evaporation cavity outlet air
Mouthful；11 be housing；12 be demarcation strip；13 be working medium manifold；14 be heat-exchanging tube bundle；15 be needle-valve.
Embodiment
In the following, a kind of turbulent cold and heat recovery device of the utility model is made according to specification drawings and specific embodiments into
One step illustrates.
A kind of turbulent cold and heat recovery device as shown in Figure 1, 2, 3, recuperation of heat is carried out for the inlet air to user terminal and air draft,
Condensation chamber (1) and evaporation cavity (2) are respectively formed with the turbulent cold and heat recovery device,
Be equipped with the turbulent cold and heat recovery device fresh air air inlet (3), fresh air outlet (4), air draft air inlet (5) with
Air draft air outlet (6)；
Condensation chamber air inlet (7) and condensation chamber air outlet (8) are equipped with the condensation chamber (1),
Evaporation cavity air inlet (9) and evaporation cavity air outlet (10) are equipped with the evaporation cavity (2),
The fresh air air inlet (3) is respectively connected to evaporation cavity air inlet (9) and condensation chamber air outlet (8) by pipeline,
The fresh air outlet (4) is respectively connected to evaporation cavity air outlet (10) and condensation chamber air inlet (7) by pipeline,
The air draft air inlet (5) is respectively connected to condensation chamber air inlet (7) and evaporation cavity air outlet (10) by pipeline,
The air draft air outlet (6) is respectively connected to condensation chamber air outlet (8) and evaporation cavity air inlet (9) by pipeline,
On the pipeline of fresh air air inlet (3) and evaporation cavity air inlet (9),
On the pipeline of fresh air air inlet (3) and condensation chamber air outlet (8),
On the pipeline of fresh air outlet (4) and evaporation cavity air outlet (10),
On the pipeline of fresh air outlet (4) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and evaporation cavity air outlet (10),
On the pipeline of air draft air outlet (6) and condenser air outlet (8) and air draft air outlet (6) and evaporation cavity air inlet
(9) on pipeline, it is respectively equipped with air-valve.
Wherein,
The condensation chamber (1) is accommodated with evaporation cavity (2) by housing (11) is unified；
The condensation chamber (1) is arranged on the surface of evaporation cavity,
Demarcation strip (12) is equipped between the condensation chamber (1) and evaporation cavity (2).
Wherein,
In housing, the top of condensation chamber sets the working medium manifold (13) being arranged along the horizontal and changed with what working medium manifold was connected
Heat pipe bundle (14),
The heat-exchanging tube bundle (14) along housing, in longitudinal direction through condensation chamber and evaporation cavity, array arrangement,
Needle-valve (15) is equipped with the working medium manifold (13).
Wherein,
The heat-exchanging tube bundle (14) is made of inner screw thread copper pipe.
Wherein,
Described runs through the condensation chamber heat-exchanging tube bundle that array is arranged with evaporation cavity along housing in longitudinal direction, wherein every heat exchange
Pipe takes the shape of the letter U to be set with inverted U-shaped slitless connection formula, is formed working medium gasification and is risen and the lower solidifying passage of liquefaction.
Wherein,
Insulating layer is equipped with described housing (3) periphery.
Wherein,
Fenestration fin is uniformly arranged all over the body in the heat-exchanging tube bundle (14).
Wherein,
The fenestration fin is aluminium foil fin.
The course of work：
Summer condition：Fresh air enters evaporation cavity by connecting fresh air air inlet and the pipeline of evaporation cavity air inlet, into steaming
The fresh air of hair chamber passes through evaporation cavity, and the liquid heat transferring medium exchanged in heat pipe bundle is heated, and is vaporized, new air temperature drop
Low, the fresh air after temperature reduction, user's space is sent into by the pipeline for connecting evaporation cavity air outlet and fresh air outlet；By user
The air draft of discharge to be held, enters condensation chamber by connecting air draft air inlet and the pipeline of condensation chamber air inlet, condensation chamber is passed through in air draft,
Gaseous state heat transferring medium in exchange heat pipe bundle is cooled down, and makes its liquefaction, temperature of outgoing air rise, the air draft after temperature rise, leads to
The pipeline of connection condensation chamber air outlet and air draft air outlet is crossed, is discharged via air draft air outlet.
Winter condition；Fresh air enters condensation chamber by connecting fresh air air inlet and the pipeline of condensation chamber air outlet, and entrance is cold
The fresh air of solidifying chamber passes through condensation chamber, and the gaseous state heat transferring medium exchanged in heat pipe bundle is cooled down, and makes its liquefaction, new air temperature liter
Height, the fresh air after temperature rise, user's space is sent into by the pipeline for connecting condensation chamber air outlet and fresh air outlet；By user
The air draft of discharge is held, enters evaporation cavity by connecting air draft air inlet and the pipeline of evaporation cavity air outlet, air draft is through pervaporation
Chamber, the liquid heat transferring medium exchanged in heat pipe bundle are heated, are vaporized, and temperature of outgoing air reduces, the air draft after temperature reduction,
By connecting the pipeline of evaporation cavity air inlet and air draft air outlet, discharged via air draft air outlet.
In above procedure, the change of working medium turns to：Hot wind is heated by evaporation cavity, exchange hot working fluid, and working medium heat absorption is steamed
Send out as gas, rise to condensation chamber, hot wind is radiated by exchanging hot working fluid, and temperature reduces；Cold wind exchanges thermal technology by condensation chamber
Matter is cooled down, and working medium heat dissipation is condensed into liquid, flows back to the evaporation cavity of lower part, cold wind is heated by gaseous heat-exchange working medium, temperature
Rise.
A kind of turbulent cold and heat recovery device of the utility model, there is provided Various Seasonal enters user terminal the cold with discharge
With being separately recovered for heat, while the cross contamination of fresh air and air draft is avoided by accordingly setting, fully ensure that the cleaning of fresh air
Degree.And the heat-exchanging tube bundle can carry out suitability laying according to different working condition requirements, working medium can be according to different operating mode need
Seek the variety exchanging for carrying out suitability.
Claims (8)
1. a kind of turbulent flow cold and heat recovery device, recuperation of heat is carried out for the inlet air to user terminal and air draft, it is characterised in that：
Condensation chamber (1) and evaporation cavity (2) are respectively formed with the turbulent cold and heat recovery device,
Fresh air air inlet (3), fresh air outlet (4), air draft air inlet (5) and air draft are equipped with the turbulent cold and heat recovery device
Air outlet (6)；
Condensation chamber air inlet (7) and condensation chamber air outlet (8) are equipped with the condensation chamber (1),
Evaporation cavity air inlet (9) and evaporation cavity air outlet (10) are equipped with the evaporation cavity (2),
The fresh air air inlet (3) is respectively connected to evaporation cavity air inlet (9) and condensation chamber air outlet (8) by pipeline,
The fresh air outlet (4) is respectively connected to evaporation cavity air outlet (10) and condensation chamber air inlet (7) by pipeline,
The air draft air inlet (5) is respectively connected to condensation chamber air inlet (7) and evaporation cavity air outlet (10) by pipeline,
The air draft air outlet (6) is respectively connected to condensation chamber air outlet (8) and evaporation cavity air inlet (9) by pipeline,
On the pipeline of fresh air air inlet (3) and evaporation cavity air inlet (9),
On the pipeline of fresh air air inlet (3) and condensation chamber air outlet (8),
On the pipeline of fresh air outlet (4) and evaporation cavity air outlet (10),
On the pipeline of fresh air outlet (4) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and condensation chamber air inlet (7),
On the pipeline of air draft air inlet (5) and evaporation cavity air outlet (10),
On the pipeline of air draft air outlet (6) and condenser air outlet (8) and air draft air outlet (6) and evaporation cavity air inlet (9)
Pipeline on, be respectively equipped with air-valve.
A kind of 2. turbulent cold and heat recovery device according to claim 1, it is characterised in that：
The condensation chamber (1) is accommodated with evaporation cavity (2) by housing (11) is unified；
The condensation chamber (1) is arranged on the surface of evaporation cavity,
Demarcation strip (12) is equipped between the condensation chamber (1) and evaporation cavity (2).
A kind of 3. turbulent cold and heat recovery device according to claim 2, it is characterised in that：
In housing, the top of condensation chamber the working medium manifold (13) being arranged along the horizontal and the heat exchanger tube connected with working medium manifold are set
Beam (14),
The heat-exchanging tube bundle (14) along housing, in longitudinal direction through condensation chamber and evaporation cavity, array arrangement,
Needle-valve (15) is equipped with the working medium manifold (13).
A kind of 4. turbulent cold and heat recovery device according to claim 3, it is characterised in that：
The heat-exchanging tube bundle (14) is made of inner screw thread copper pipe.
A kind of 5. turbulent cold and heat recovery device according to claim 3, it is characterised in that：
Described runs through the condensation chamber heat-exchanging tube bundle that array is arranged with evaporation cavity along housing in longitudinal direction, wherein every heat exchanger tube is in
U-shaped is set with inverted U-shaped slitless connection formula, is formed working medium gasification and is risen and the lower solidifying passage of liquefaction.
A kind of 6. turbulent cold and heat recovery device according to claim 2, it is characterised in that：
Insulating layer is equipped with described housing (11) periphery.
A kind of 7. turbulent cold and heat recovery device according to claim 3, it is characterised in that：
Fenestration fin is uniformly arranged all over the body in the heat-exchanging tube bundle (14).
A kind of 8. turbulent cold and heat recovery device according to claim 7, it is characterised in that：
The fenestration fin is aluminium foil fin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721423693.0U CN207350743U (en) | 2017-10-31 | 2017-10-31 | A kind of turbulent flow cold and heat recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721423693.0U CN207350743U (en) | 2017-10-31 | 2017-10-31 | A kind of turbulent flow cold and heat recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207350743U true CN207350743U (en) | 2018-05-11 |
Family
ID=62353730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721423693.0U Expired - Fee Related CN207350743U (en) | 2017-10-31 | 2017-10-31 | A kind of turbulent flow cold and heat recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207350743U (en) |
-
2017
- 2017-10-31 CN CN201721423693.0U patent/CN207350743U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180511 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |