CN207584952U - High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system - Google Patents
High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system Download PDFInfo
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- CN207584952U CN207584952U CN201720693640.4U CN201720693640U CN207584952U CN 207584952 U CN207584952 U CN 207584952U CN 201720693640 U CN201720693640 U CN 201720693640U CN 207584952 U CN207584952 U CN 207584952U
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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
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- 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]
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Abstract
High-efficiency cold-hot provided by the utility model is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, including compressor, media lines, wind turbine and expansion valve, which further includes imports the return air in constant temperature and humidity space that fresh air mixes and constant temperature and humidity air after cool-down dehumidification and heat temperature raising sends the cycle gas pipeline in constant temperature and humidity space back to again again；The media lines of refrigerant return are equipped with cool-down dehumidification component between compressor and expansion valve, and the media lines that refrigerant exports between compressor and expansion valve are equipped with heat temperature raising component；Cool-down dehumidification component by the heat absorption for mixing air inlet and is conveyed to heat temperature raising component by recuperation of heat at air inlet through compressor, the cold absorption for recycling cold wind in gas pipeline is conveyed to cool-down dehumidification component by heat temperature raising component by cold recovery again, heat temperature raising is carried out before air-supply, successively reciprocation cycle to after the temperature and temperature for reaching requirement, finally blow into constant temperature and humidity space.
Description
【Technical field】
The utility model is related to air-conditioning technique more particularly to the double receipts energy-saving constant-temperature constant wetting air conditioner processing systems of high-efficiency cold-hot
System.
【Background technology】
At present, energy crisis has become the problem of whole world concern, can be by the natural energy resources of human use increasingly
It is few, but demand of the mankind to natural energy resources is increasing, and countries in the world are all carrying out Energy restructuring, with to greatest extent
The utilization of the existing energy is saved, and mitigates the environmental pollution increasingly aggravated.
Constant-temperature constant-humidity air-conditioner processor belongs to auxiliary producting energy in industrial enterprise's (such as pharmacy, electronic enterprise) produces
Equipment, it is ensured that surrounding air is in stable humiture, ensures the quality of production product.At traditional constant-temperature constant-humidity air-conditioner
Reason machine, dehumidifying and heating are mutually independent spare system using a set of, handpiece Water Chilling Units are needed removed except temperature in dehumidifying
It is wet, it heats up after the humidity of requirement is reached, then by heating equipment (such as boiler, electrical heating), until after the temperature of requirement,
Being transported to again needs the workshop of constant temperature and humidity.One side cool-down dehumidification, on the other hand heat temperature raising again, is unidirectional output,
It is not utilized by energy regenerating and rationally fully, there are larger energy losses.
【Utility model content】
The utility model provides a kind of loss that can reduce energy, improves the efficiency of energy utilization of equipment, reaches energy saving
The high-efficiency cold-hot for the effect that lowers consumption is double to receive energy-saving constant-temperature constant wetting air conditioner processing system.
In order to realize above-mentioned purpose of utility model, the technical solution adopted in the utility model is：
High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, including compressor, media lines, wind turbine and expansion
Valve, which further includes imports fresh air mixing and after cool-down dehumidification and heat temperature raising again by the return air in constant temperature and humidity space
Constant temperature and humidity air send the cycle gas pipeline in constant temperature and humidity space back to again；Refrigerant returns between the compressor and expansion valve
The media lines of stream are equipped with to be arranged side by side with cycle gas pipeline will recycle return air importing in gas pipeline by refrigeration
The mixing air inlet that fresh air is formed exports the cool-down dehumidification component of cold wind by cool-down dehumidification；It is cold between the compressor and expansion valve
The media lines of matchmaker's output are equipped with to be arranged side by side to recycle in gas pipeline by evaporation with cycle gas pipeline and flow through
Cold wind by heat temperature raising output constant temperature and humidity air heat temperature raising component；The compressor is by refrigerant by low-temp low-pressure shape
State is changed into high-temperature high-pressure state, and heating agent is changed into low temperature by the expansion valve by high-temperature high-pressure state；The drop
Warm dehumidifying component by the heat absorption for mixing air inlet and is conveyed to heat temperature raising component by recuperation of heat at air inlet through compressor,
The cold absorption for recycling cold wind in gas pipeline is conveyed to cool-down dehumidification component by heat temperature raising component by cold recovery again, is being sent
Heat temperature raising is carried out before wind, successively reciprocation cycle to after the temperature and temperature for reaching requirement, finally air-supply is empty to constant temperature and humidity
Between in；The excessive heat that the wind turbine is set at heat temperature raising component and is recycled to heat temperature raising component, which is evacuated, carrys out dynamic
Wind pushing temperature in cycle gas pipeline is adjusted to keep constant.
Preferably, the cool-down dehumidification component is exchanges pipeline structure.
Preferably, the cool-down dehumidification component includes the multigroup condenser coil connected with media lines and with recycling appendix
Multigroup first wind path coil pipe of road connection, multigroup condenser coil and multigroup cross-superimposed arrangement of first wind path coil pipe.
Preferably, the heat temperature raising component is exchanges pipeline structure.
Preferably, the heat temperature raising component includes the multigroup evaporation coil connected with media lines and with recycling appendix
Multigroup second wind path coil pipe of road connection, multigroup evaporation coil and multigroup cross-superimposed arrangement of second wind path coil pipe.
Preferably, the wind turbine is frequency conversion fan.
Preferably, the expansion valve is electric expansion valve.
The beneficial effects of the utility model are：
The utility model will be replaced mounted on mixing blast pipe to the traditional air conditioner processor between ajutage, be removed
Original refrigeration system equipment and heat temperature raising system equipment, replace with cool-down dehumidification component and heat temperature raising component, and pacify
It fills individual power distribution equipment and supplies power supply to energy-saving equipment, realize energy-saving.
Cool-down dehumidification component will be mixed the heat absorption entered the wind and be conveyed to through compressor at air inlet by recuperation of heat to be added
Hot temperature rising module enters the wind mixing and carries out cool-down dehumidification, heat temperature raising component will be recycled in gas pipeline again by cold recovery
The cold absorption of cold wind is conveyed to cool-down dehumidification component, i.e., cold wind in pipeline is carried out heat temperature raising, heated before air-supply
Heating, successively reciprocation cycle to after the temperature and temperature for reaching requirement, finally blow into constant temperature and humidity space；Meanwhile wind
The excessive heat that machine is set at heat temperature raising component and is recycled to heat temperature raising component evacuated come dynamic regulation cycle it is defeated
Wind pushing temperature is kept constant in feed channel, and the system is made to realize cold and hot double receipts under multi-ensuring, energy utilization rate is improved, reduces
Operating cost.
Compared with prior art, it has the following advantages：
(1) without additional two sets of cold-heating systems
Cool-down dehumidification component built in the system and heat temperature raising component, the difference with traditional equipment maximum are two components
Independent unidirectional system, but two-way interconnection, cool-down dehumidification component can by the heat absorption in air and pass to plus
Hot temperature rising module so as to fulfill the cooling of air, goes out moisture in the hollow air elutriation of temperature-fall period and reaches effect on moisture extraction；Heat temperature raising group
The heat passed over is then released to air by part, and to air heat temperature raising, in heating up process, heat temperature raising component will
Cold absorption in air simultaneously returns to cool-down dehumidification component, makes system always in efficient benign cycle, final to realize
The double energy-saving effects received of high-efficiency cold-hot.
(2) it is efficient
Due to using the double power-saving technologies received of high-efficiency cold-hot, on the one hand reducing two sets of cold and hot systems attached by traditional equipment
The energy loss that system equipment is brought in energy transport, another aspect traditional equipment are needed in cool-down dehumidification using cold
Water dispenser group cools down air cooling, while by water chilling unit system in the heat dissipation of air to extraneous air, this portion
Heat is divided not to be recycled recycling, is wasted；Meanwhile after air reaches the humidity of requirement, and need by adding
Hot equipment carries out it heat temperature raising, while the cold of air is discharged into extraneous air again, this part cold does not have
To recycling, energy is wasted again.
Cold and hot double receipts of the system high efficiency, have prevented the energy dissipation that traditional equipment unidirectionally exports completely.
(3) energy consumption is saved
It is efficient due to the system, compared with traditional equipment, more than 40% energy consumption can be saved.
【Description of the drawings】
Fig. 1 is the structure principle chart of the utility model.
Specific embodiment of the present utility model is described in more detail below in conjunction with attached drawing.
【Specific embodiment】
High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing systems, as shown in Figure 1, including compressor 1, media lines 2,
Frequency conversion fan 3 and electric expansion valve 4, which further includes imports fresh air b mixing simultaneously again by the return air a in constant temperature and humidity space
Constant temperature and humidity air after cool-down dehumidification and heat temperature raising sends the cycle gas pipeline 5 in constant temperature and humidity space back to again.
Wherein, it is equipped on the media lines 2 of refrigerant return with recycling appendix between compressor 1 and electric expansion valve 4
Road 5 is arranged side by side will recycle the mixing air inlet c of return air a importing fresh airs b formation in gas pipeline 5 by cooling by refrigeration
The cool-down dehumidification component 6 of dehumidifying output cold wind d；On the media lines 2 that refrigerant exports between compressor 1 and electric expansion valve 4
It is risen equipped with being arranged side by side with cycle gas pipeline 5 by evaporation by the cold wind d flowed through in gas pipeline 5 is recycled by heating
The heat temperature raising component 7 of temperature output constant temperature and humidity air.
During work, refrigerant is changed into high-temperature high-pressure state by compressor 1 by low temperature, and electric expansion valve 4 will be warm
Matchmaker is changed into low temperature by high-temperature high-pressure state；Cool-down dehumidification component 6 will be mixed by recuperation of heat at air inlet and be entered the wind
Heat absorption and be conveyed to heat temperature raising component 7 through compressor 1, i.e., mixing enter the wind carry out cool-down dehumidification, heat temperature raising group
The cold absorption for recycling cold wind in gas pipeline 5 is conveyed to cool-down dehumidification component 6 by part 7 by cold recovery again, i.e., in pipeline
Cold wind carries out heat temperature raising, and heat temperature raising is carried out before air-supply, successively reciprocation cycle to after the temperature and temperature for reaching requirement,
It finally blows into constant temperature and humidity space；Moreover, frequency conversion fan 3 is set at heat temperature raising component 7 and to heat temperature raising component 7
Recycling excessive heat evacuate come dynamic regulation recycle gas pipeline 5 in wind pushing temperature keep constant, under multi-ensuring
The system is made to realize cold and hot double receipts, energy utilization rate is improved, reduces operating cost.
In the system, cool-down dehumidification component includes connecting with media lines to exchange pipeline structure, the cool-down dehumidification component
Multigroup condenser coil and with multigroup first wind path coil pipe for connect of cycle gas pipeline, multigroup condenser coil and multigroup first wind
The cross-superimposed arrangement of road coil pipe；Heat temperature raising component is also to exchange pipeline structure, which includes and media lines
Multigroup evaporation coil of connection and with multigroup second wind path coil pipe for connect of cycle gas pipeline, multigroup evaporation coil and multigroup the
The two cross-superimposed arrangements of wind path coil pipe.
Embodiment described above is the preferred embodiment for the utility model, and the reality of the utility model is not limited with this
Apply range, all equivalence changes made according to the shape of the utility model, construction and principle should all be covered by the guarantor of the utility model
In the range of shield.
Claims (7)
1. high-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing systems, including compressor, media lines, wind turbine and expansion valve,
It is characterized in that：
The system is further included imports fresh air mixing and through cool-down dehumidification and heat temperature raising again by the return air in constant temperature and humidity space
Constant temperature and humidity air afterwards sends the cycle gas pipeline in constant temperature and humidity space back to again；
The media lines of refrigerant return are equipped with to be arranged side by side with cycle gas pipeline and pass through between the compressor and expansion valve
Refrigeration will recycle return air in gas pipeline and import the mixing air inlet of fresh air formation by the cooling of cool-down dehumidification output cold wind
Dehumidifying component；
The media lines that refrigerant exports between the compressor and expansion valve, which are equipped with to be arranged side by side with cycle gas pipeline, to be passed through
Evaporation is by the cold wind flowed through in cycle gas pipeline by the heat temperature raising component of heat temperature raising output constant temperature and humidity air；
Refrigerant is changed into high-temperature high-pressure state by the compressor by low temperature, and the expansion valve is by heating agent by high temperature height
Pressure condition is changed into low temperature；
The cool-down dehumidification component will be mixed the heat absorption entered the wind and be conveyed to through compressor at air inlet by recuperation of heat to be added
The cold absorption for recycling cold wind in gas pipeline is conveyed to cooling by cold recovery again and removed by hot temperature rising module, heat temperature raising component
Wet component carries out heat temperature raising before air-supply, successively reciprocation cycle to after the temperature and temperature for reaching requirement, finally air-supply is arrived
In constant temperature and humidity space；
The excessive heat that the wind turbine is set at heat temperature raising component and is recycled to heat temperature raising component, which is evacuated, carrys out dynamic
Wind pushing temperature in cycle gas pipeline is adjusted to keep constant.
2. high-efficiency cold-hot according to claim 1 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Cool-down dehumidification component is exchanges pipeline structure.
3. high-efficiency cold-hot according to claim 2 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Cool-down dehumidification component includes the multigroup condenser coil connected with media lines and multigroup first wind connected with cycle gas pipeline
Road coil pipe, multigroup condenser coil and multigroup cross-superimposed arrangement of first wind path coil pipe.
4. high-efficiency cold-hot according to claim 1 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Heat temperature raising component is exchanges pipeline structure.
5. high-efficiency cold-hot according to claim 4 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Heat temperature raising component includes the multigroup evaporation coil connected with media lines and multigroup second wind connected with cycle gas pipeline
Road coil pipe, multigroup evaporation coil and multigroup cross-superimposed arrangement of second wind path coil pipe.
6. high-efficiency cold-hot according to claim 1 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Wind turbine is frequency conversion fan.
7. high-efficiency cold-hot according to claim 1 is double to receive energy-saving constant-temperature constant wetting air conditioner processing system, which is characterized in that described
Expansion valve is electric expansion valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720693640.4U CN207584952U (en) | 2017-06-14 | 2017-06-14 | High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720693640.4U CN207584952U (en) | 2017-06-14 | 2017-06-14 | High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system |
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| Publication Number | Publication Date |
|---|---|
| CN207584952U true CN207584952U (en) | 2018-07-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720693640.4U Active CN207584952U (en) | 2017-06-14 | 2017-06-14 | High-efficiency cold-hot is double to receive energy-saving constant-temperature constant wetting air conditioner processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110513905A (en) * | 2019-07-26 | 2019-11-29 | 浙江大学宁波理工学院 | A kind of cold-hot combined supply system based on open type absorbent circulation |
-
2017
- 2017-06-14 CN CN201720693640.4U patent/CN207584952U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110513905A (en) * | 2019-07-26 | 2019-11-29 | 浙江大学宁波理工学院 | A kind of cold-hot combined supply system based on open type absorbent circulation |
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