CN208887043U - A kind of heat source recovery device - Google Patents
A kind of heat source recovery device Download PDFInfo
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- CN208887043U CN208887043U CN201821624700.8U CN201821624700U CN208887043U CN 208887043 U CN208887043 U CN 208887043U CN 201821624700 U CN201821624700 U CN 201821624700U CN 208887043 U CN208887043 U CN 208887043U
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- heat pipe
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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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- Central Air Conditioning (AREA)
Abstract
The utility model relates to a kind of air conditioning and cleaning system, in particular to a kind of heat source recovery device, including air inlet unit and exhaust fan unit;It enters the wind unit and is equipped with fresh air section, initial effect filtering section, heat pipe table cold and heat recovery section, evaporator section, maintenance section, heat pipe secondary heat-recovery section, surface cooling section, bringing-up section, condensing units section, medium efficiency filtration section and humidifier section;Exhaust fan unit is equipped with initial effect filtering section, washing spray section, recuperation of heat exhausting section of heat pipe, oxidation sterilizing section, active carbon fillter section, compression condensation section and exhaust blower section.The utility model recycles coil pipe by setting multiple-effect circulation, including the heat pipe table cold and heat recovery section before evaporator section is arranged in, the heat pipe secondary heat-recovery section that is arranged in after evaporator section, the heat pipe after washing spray section is arranged in and once recycles exhausting section;The temperature difference in exhaust fan unit in exhaust gas and Fresh air handling units is efficiently used, so that the heat source of exhaustion section is fully used, further saves the energy.
Description
Technical field
The utility model relates to a kind of air conditioning and cleaning system, in particular to a kind of heat source recovery device.
Background technique
In recent years, air-conditioning market competition was more and more fierce, and the requirement to air-conditioning regulation performance is also higher and higher, air conditioning
Main control include air quality, air themperature, air humidity and wind speed etc..
The control of air quality is compared from however effective method is to be set using outdoor fresh air to room air
It changes or dilutes, that is, sucking outdoor fresh air, indoor exhaust air is discharged.For being under high humidity environment in existing aeration device
Fresh air, the general moisture by condensing tube condensation fresh air achievees the purpose that fresh air dehumidification, and dehumidification by condensation can make newly
The temperature of wind declines to a great extent, generally can be lower than indoor required preference temperature, to need using electric heating or other heating sides
Formula enters back into interior after the fresh air after dehumidification by condensation to be heated to suitable temperature, using exhaust fan unit that indoor exhaust gas is direct
Discharge is outdoor, does not carry out effective recycling and reusing to indoor exhaust gas, there are problems that high energy consumption.
Utility model content
In order to overcome the defects of the prior art described above, the technical problem to be solved by the utility model is to provide a kind of heat
Source recyclable device, using the temperature difference of the fresh air in exhaust gas in exhaust fan unit and air inlet unit, the principle solution recycled using coil pipe
In the certainly existing fresh air system using compressor principle the problem of energy waste.
In order to solve the above-mentioned technical problem, the technical solution adopted in the utility model are as follows: a kind of heat source recovery device, including
Enter the wind unit and exhaust fan unit;
The air inlet unit includes along the sequentially connected fresh air section of fresh inlet end to fresh air outlet extreme direction, primarily efficient filter
Section, heat pipe table cold and heat recovery section, evaporator section, maintenance section, heat pipe secondary heat-recovery section, surface cooling section, bringing-up section, condensing units
Section, medium efficiency filtration section and humidifier section;The heat pipe table cold and heat recovery section is equipped with heat pipe coil pipe, and the heat pipe secondary heat-recovery section is set
There is second heat pipe dish pipe;
The exhaust fan unit include along air draft input end to the sequentially connected air draft initial effect filtering section of wind exhausting outlet extreme direction,
Spray section, heat-recovery section of heat pipe, oxidation sterilizing section, active carbon fillter section, compression condensation section and exhaust blower section are washed, it is described
Heat-recovery section of heat pipe is equipped with a heat pipe coil pipe;
The heat pipe coil pipe of the heat pipe table cold and heat recovery section, a heat pipe coil pipe of heat-recovery section of heat pipe and heat pipe two
The second heat pipe dish pipe of secondary heat-recovery section forms the heat recovery circuit of closed loop, and ethylene glycol solution is equipped in heat recovery circuit and is pumped.
The utility model has the beneficial effects that: by setting multiple-effect circulation recycle coil pipe, including setting evaporator section it
The heat pipe secondary heat-recovery section that preceding heat pipe table cold and heat recovery section, is arranged in after evaporator section is arranged after washing spray section
Heat-recovery section of heat pipe;The temperature difference in exhaust fan unit in exhaust gas and Fresh air handling units is efficiently used, the heat source of exhaustion section is made
It is fully used, further saves the energy.
Detailed description of the invention
Fig. 1 show a kind of structural schematic diagram of heat source recovery device;
Fig. 2 show a kind of partial enlarged view of the air inlet unit heat pipe secondary heat-recovery section of heat source recovery device;
Fig. 3 show a kind of partial enlarged view of the air inlet unit evaporator section of heat source recovery device;
Label declaration:
1, unit is entered the wind;
11, fresh air section;
12, initial effect filtering section;121, primary filter;
13, heat pipe table cold and heat recovery section;
14, evaporator section;141, mouth is crimped in refrigerant;142, refrigerant low-voltage interface;143, device for drying and filtering;144, electric
Sub- expansion valve;
15, heat pipe secondary heat-recovery section;151, check valve;152, ethylene glycol outlet end;153, ethylene glycol input end;154,
Electronic ratio triple valve;155, check valve;
16, surface cooling section;161, chilled water water return outlet;162, refrigerant high pressure interface;
17, bringing-up section;
18, condensing units section;181, check valve;
19, fan section;110, medium efficiency filtration section;111, humidifier section;112, wind outlet section;113, medium effeciency filter;
2, exhaust fan unit;
21, initial effect filtering section;
22, spray section is washed;221, spray pump is washed;
23, heat-recovery section of heat pipe;231, ethylene glycol solution pumps;
24, oxidation sterilizing section;25, active carbon fillter section;26, active carbon fillter section;
27, compression condensation section;271, electric expansion valve;272, compressor;273, check valve;
28, exhaust blower section;
29, exhaustion section;
3, heat pipe liquid back pipe;
4, heat pipe liquid supply pipe.
Specific embodiment
For technology contents, the objects and the effects that the utility model is described in detail, below in conjunction with embodiment and match
Attached drawing is closed to be explained.
The design of the utility model most critical is: utilizing the temperature of the fresh air in exhaust gas in exhaust fan unit and air inlet unit
Difference solves the problems, such as energy waste in the existing fresh air system using compressor principle using the principle that coil pipe recycles.
It please refers to shown in Fig. 1 to Fig. 3, a kind of heat source recovery device of the utility model, including air inlet unit 1 and air draft
Unit 2;
The air inlet unit includes exporting the sequentially connected fresh air section 11 of extreme direction along fresh inlet end to fresh air, just imitating
Filter section 12, heat pipe table cold and heat recovery section 13, evaporator section 14, maintenance section, heat pipe secondary heat-recovery section 15, surface cooling section 16, bringing-up section
17, condensing units section 18, medium efficiency filtration section 110 and humidifier section 111;The heat pipe table cold and heat recovery section is equipped with heat pipe coil pipe,
The heat pipe secondary heat-recovery section is equipped with second heat pipe dish pipe;
The exhaust fan unit includes along air draft input end to the sequentially connected air draft initial effect filtering section of wind exhausting outlet extreme direction
21, spray section 22, heat-recovery section 23 of heat pipe, oxidation sterilizing section 24, active carbon fillter section 25,27 and of compression condensation section are washed
Exhaust blower section 28, heat-recovery section of the heat pipe are equipped with a heat pipe coil pipe;
The heat pipe coil pipe of the heat pipe table cold and heat recovery section 13, a heat pipe coil pipe of heat-recovery section 23 of heat pipe and heat
The second heat pipe dish pipe for managing secondary heat-recovery section 15 forms the heat recovery circuit of closed loop, and it is molten that ethylene glycol is equipped in heat recovery circuit
Liquid pump 231.
The working principle of above-mentioned heat source recovery device: after fresh air dehumidification work, fresh air goes successively to heat pipe secondary heat
After exhausting section 15 and surface cooling section 16 carry out heat exchange, into bringing-up section 17 and condensing units section 18, heat fresh air, due to removing
Air and evaporation coil after wet have carried out heat exchange, and air themperature is lower than indoor required temperature, needs to be heated to preference temperature
After enter back into interior, be passed through in the condensing units coil pipe in condensing units section 18 be by compressor 272 compress after high pressure
Refrigerant releases a large amount of heat since compressor 272 compresses refrigerant, and the refrigerant temperature in this section is high, by removing
Fresh air after wet supercooling carries out heat exchange by the Duan Shiyu condensing units coil pipe, is warmed to room temperature, using medium efficiency filtration section
113 further filterings and humidifier section 111 enter the room after handling.
As can be seen from the above description, the utility model has the beneficial effects that: setting multiple-effect circulation recycles coil pipe, including setting
Before evaporator section heat pipe table cold and heat recovery section, evaporator section 14 is set after heat pipe secondary heat-recovery section 15, setting exist
Recuperation of heat exhausting section of heat pipe after washing spray section;It efficiently uses in exhaust fan unit 2 in exhaust gas and Fresh air handling units
Temperature difference makes the heat source of exhaustion section be fully used, further saves the energy.
Further, the second heat pipe dish pipe of one end and heat pipe secondary heat-recovery section 15 of a heat pipe coil pipe into
The connection of mouth end, the outlet end of the second heat pipe dish pipe of the heat pipe secondary heat-recovery section 15 and the heat of heat pipe table cold and heat recovery section 13
The input end of pipe dish pipe connects, the outlet end of the heat pipe coil pipe of the heat pipe table cold and heat recovery section 13 and a heat pipe coil pipe
The other end connection.
As can be seen from the above description, by the way that three heat pipe heat-recovery sections are linked together, convenient for the transmitting of unit inner heat source and
It is recycled.
Further, one end and the heat pipe secondary heat of a heat pipe coil pipe is arranged in the ethylene glycol solution pump 231
Between the input end of the second heat pipe dish pipe of exhausting section 15.
As can be seen from the above description, by the way that ethylene glycol solution is arranged between a heat pipe coil pipe and heat pipe secondary heat-recovery section
Pump convenient for conveying ethylene glycol solution and accelerates flow velocity.
Further, the second heat pipe dish pipe of one end and heat pipe secondary heat-recovery section 15 of a heat pipe coil pipe into
Mouth end passes through heat pipe liquid supply pipe 4 and connects.
As can be seen from the above description, by setting heat pipe liquid supply pipe, convenient for reducing ethylene glycol solution efficiency in transmission process
Consumption.
Further, the outlet end of the heat pipe coil pipe of the heat pipe table cold and heat recovery section 13 and a heat pipe coil pipe
The other end is connected by heat pipe liquid back pipe 3.
As can be seen from the above description, quickly being recycled by setting heat pipe liquid back pipe 3 convenient for ethylene glycol solution.
Further, the second heat pipe dish pipe of the heat pipe secondary heat-recovery section 15 include straight tube branch, coil pipe branch and
Electronic ratio triple valve 154, electronic ratio triple valve 154 include first interface, second interface and third interface, and described first connects
Mouth is connect with the input end of the second heat pipe dish pipe of heat pipe secondary heat-recovery section, the second interface and straight tube branch one end
Connection, the third interface are connect with coil pipe branch one end, and the straight tube branch other end and the coil pipe branch other end connect
It connects.
As can be seen from the above description, by the way that electronic ratio triple valve is arranged, convenient for control the flow velocity of ethylene glycol solution, flow and
Flow direction.
Further, the straight tube branch road is equipped with check valve 155.
As can be seen from the above description, by setting check valve, convenient for preventing ethylene glycol solution from flowing back to electronic ratio triple valve
154。
Further, the coil pipe branch road is equipped with check valve.
As can be seen from the above description, by setting check valve, convenient for preventing ethylene glycol solution from flowing back to second heat pipe dish pipe.
It please refers to shown in Fig. 1 to Fig. 3, the embodiments of the present invention one are as follows:
A kind of heat source recovery device provided by the utility model, including air inlet unit 1 and exhaust fan unit 2;
The air inlet unit 1 includes along fresh inlet end to fresh air outlet extreme direction sequentially connected fresh air section 11, just effect
Fillter section 12, heat pipe table cold and heat recovery section 13, evaporator section 14, maintenance section, heat pipe secondary heat-recovery section 15, surface cooling section 16, heating
Section 17, condensing units section 18, medium efficiency filtration section 110, humidifier section 111 and wind outlet section 112;The heat pipe table cold and heat recovery section 13
Equipped with heat pipe coil pipe, the heat pipe secondary heat-recovery section 15 is equipped with second heat pipe dish pipe, ethylene glycol input end 153, ethylene glycol and goes out
Mouth end 152;The maintenance section, which is equipped in refrigerant low-voltage interface 142 and refrigerant, crimps mouth 141;The evaporator section is equipped with evaporation
The input end of coil pipe, the evaporation coil is equipped with device for drying and filtering 143 and electric expansion valve 144;The surface cooling section 16 is equipped with cold
Freeze water water return outlet 161 and refrigerant high pressure interface 162;The initial effect filtering section 12 is equipped with primary filter 121;It was imitated in described
It filters section 110 and is equipped with medium effeciency filter 113;
The exhaust fan unit 2 include along air draft input end to the sequentially connected initial effect filtering section 21 of wind exhausting outlet extreme direction,
Wash spray section 22, heat-recovery section 23 of heat pipe, oxidation sterilizing section 24, active carbon fillter section 25, active carbon fillter section 26,
Compression condensation section 27, exhaust blower section 28 and exhaustion section 29, the washing spray section 22 are equipped with washing spray pump 221;The heat pipe
One time heat-recovery section is equipped with a heat pipe coil pipe;The compression condensation section includes electric expansion valve 271, fluid reservoir, compressor
272, check valve 273 and compression condensation coil pipe;
The heat pipe coil pipe of the heat pipe table cold and heat recovery section, a heat pipe coil pipe of heat-recovery section of heat pipe and heat pipe two
The second heat pipe dish pipe of secondary heat-recovery section forms the heat recovery circuit of closed loop, and ethylene glycol solution is equipped in heat recovery circuit and is pumped
231, the outlet end of the ethylene glycol solution pump is connect with heat pipe liquid supply pipe 4, and the input end and heat pipe of ethylene glycol solution pump return liquid
Pipe 3 connects;
The input end of the second heat pipe dish pipe of one end and heat pipe secondary heat-recovery section of heat pipe coil pipe is connect, institute
State the input end of the outlet end of the second heat pipe dish pipe of heat pipe secondary heat-recovery section and the heat pipe coil pipe of heat pipe table cold and heat recovery section
Connection, the outlet end of the heat pipe coil pipe of the heat pipe table cold and heat recovery section is connect with the other end of a heat pipe coil pipe;
The secondary of one end of a heat pipe coil pipe and heat pipe secondary heat-recovery section is arranged in ethylene glycol solution pump
Between the input end of heat pipe coil pipe;
The input end of the second heat pipe dish pipe of one end and heat pipe secondary heat-recovery section of heat pipe coil pipe passes through heat
The connection of pipe liquid supply pipe;
The outlet end of the heat pipe coil pipe of the heat pipe table cold and heat recovery section and the other end of a heat pipe coil pipe pass through
The connection of heat pipe liquid back pipe;
The second heat pipe dish pipe of the heat pipe secondary heat-recovery section includes straight tube branch, coil pipe branch and electronic ratio threeway
Valve 154, electronic ratio triple valve 154 include first interface, second interface and third interface, the first interface and heat pipe secondary
The input end of the second heat pipe dish pipe of heat-recovery section connects, and the second interface is connect with straight tube branch one end, and described the
Three interfaces are connect with coil pipe branch one end, and the straight tube branch other end is connect with the coil pipe branch other end;
The straight tube branch and coil pipe branch road are equipped with check valve 155 and check valve 151.
The variation of the temperature of fresh air is specific as follows in above-mentioned heat source recovery device:
Such as summer outdoor fresh air temperature is 36 DEG C, it is cold by initial effect filtering section 12 and heat pipe table into after air inlet unit 1
After heat-recovery section 13, the temperature of fresh air is down to 26 DEG C;After 14 dehumidification by condensation of evaporator section, new air temperature is down to 12 DEG C;By
After heat pipe secondary heat-recovery section 15, new air temperature rises to 17 DEG C;After bringing-up section 17 and condensing units section 18, new air temperature
Rise to 21 DEG C;Indoor new air temperature is finally putting at 22~23 DEG C;
Such as indoor exhaust gas temperature is 23~25 DEG C, into after exhaust fan unit 2, is sprayed by initial effect filtering section and washing
Section, the temperature of exhaust gas are down to 18~21 DEG C;After heat-recovery section of superheater tube and oxidation sterilizing section, the temperature of exhaust gas rises to 25
~29 DEG C, finally discharge is outdoor.
The variation of ethylene glycol temperature in above-mentioned heat source recovery device is specific as follows:
The ethylene glycol temperature of heat-recovery section 21 of heat pipe outflow is flowed at 21~23 DEG C from heat pipe secondary heat-recovery section 15
Ethylene glycol temperature out flows into the ethylene glycol temperature of heat pipe table cold and heat recovery section 13 at 17~23 DEG C, flows back to heat at 17~21 DEG C
The ethylene glycol temperature of Guan Yici heat-recovery section 21 is at 24~28 DEG C.
In conclusion a kind of heat source recovery device provided by the utility model, setting multiple-effect circulation recycles coil pipe, including sets
Set before evaporator section heat pipe table cold and heat recovery section, evaporator section 14 is set after heat pipe secondary heat-recovery section 15, setting
In recuperation of heat exhausting section of heat pipe after washing spray section;It efficiently uses in exhaust fan unit in exhaust gas and Fresh air handling units
Temperature difference makes the heat source of exhaustion section be fully used, further saves the energy.
The above description is only the embodiments of the present invention, and therefore it does not limit the scope of the patent of the utility model, all
Equivalents made based on the specification and figures of the utility model are applied directly or indirectly in relevant technology neck
Domain is also included in the patent protection scope of the utility model.
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821624700.8U CN208887043U (en) | 2018-10-08 | 2018-10-08 | A kind of heat source recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821624700.8U CN208887043U (en) | 2018-10-08 | 2018-10-08 | A kind of heat source recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208887043U true CN208887043U (en) | 2019-05-21 |
Family
ID=66515092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821624700.8U Expired - Fee Related CN208887043U (en) | 2018-10-08 | 2018-10-08 | A kind of heat source recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208887043U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112594831A (en) * | 2020-12-29 | 2021-04-02 | 福建瑞博恩环境科技有限公司 | Split type heat pipe heat recovery fresh air unit |
-
2018
- 2018-10-08 CN CN201821624700.8U patent/CN208887043U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112594831A (en) * | 2020-12-29 | 2021-04-02 | 福建瑞博恩环境科技有限公司 | Split type heat pipe heat recovery fresh air unit |
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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: 20190521 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |