WO2014012287A1 - Air conditioning unit with filler coupling coil pipe evaporative type condenser - Google Patents
Air conditioning unit with filler coupling coil pipe evaporative type condenser Download PDFInfo
- Publication number
- WO2014012287A1 WO2014012287A1 PCT/CN2012/080022 CN2012080022W WO2014012287A1 WO 2014012287 A1 WO2014012287 A1 WO 2014012287A1 CN 2012080022 W CN2012080022 W CN 2012080022W WO 2014012287 A1 WO2014012287 A1 WO 2014012287A1
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- WO
- WIPO (PCT)
- Prior art keywords
- heat exchange
- air conditioning
- conditioning unit
- coil
- valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/0035—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using evaporation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/04—Condensers
-
- 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
- F28D5/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
- F28D5/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/041—Details of condensers of evaporative condensers
-
- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
- F28D1/0477—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/007—Condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
- F28F1/22—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally the means having portions engaging further tubular elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/08—Splashing boards or grids, e.g. for converting liquid sprays into liquid films; Elements or beds for increasing the area of the contact surface
- F28F25/087—Vertical or inclined sheets; Supports or spacers
-
- 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]
- Y02B30/54—Free-cooling systems
Definitions
- the invention relates to the field of air conditioning equipment, in particular to an air conditioning unit of a coil evaporative condenser.
- the coil for evaporative condenser used in the air-conditioning unit on the market is a transverse coil, which is cooled by spraying water on the outer surface of the coil, and uses circulating spray water to evaporate air to remove heat.
- the coil Since the cooling wind direction is perpendicular to the coil (that is, the cooling air passes through the plane space formed by each heat exchange tube and is perpendicular to the straight pipe section of the heat exchange tube), the coil has a windward side and a leeward side, and the leeward side Lack of air convection heat transfer reduces coil heat transfer efficiency.
- the effective heat exchange area of the transverse coil is small, the length of the coil to be used needs to be increased. The same as the H inch, due to the misalignment between the tubes and the tubes of the conventional transverse coil, there is no mechanical cleaning operation space, and there is also The disadvantage of being difficult to clean. Therefore, the lack of lateral coils greatly limits the use of evaporative condensers in air conditioning units.
- the purpose of the present invention is to overcome the shortcomings of the prior art and to provide an air conditioning unit with a packed coupling coil evaporative condenser to improve heat exchange efficiency.
- An air conditioning unit with a packed coupling coil evaporative condenser comprising a compressor, an evaporative condenser, a throttling device, an evaporator and a fan, the evaporative condenser comprising a coil heat exchanger, a cooling fan, and a cloth a water heater and a sump;
- the coil heat exchanger is composed of a plurality of heat exchange fins connected through an inlet header and an outlet header;
- the heat exchange fins include a coil and a filler, and the coil is provided with at least A piece of filler for guiding the spray cooling water from the upper heat exchange tube to the lower heat exchange tube.
- the coil is longitudinally disposed, that is, the cooling wind blown by the fan is along the straight tube of the coil
- the heat exchange tubes of the coil are S-shaped; the filler is disposed between the adjacent heat exchange tubes to connect the heat exchange tubes into a continuous water flow surface.
- the straight pipe sections adjacent to the heat exchange tubes are parallel to each other, and the pipe spacing of the straight pipe sections adjacent to the heat exchange pipes is the same, or the pipe spacing is from the upper layer receiving the spray cooling water to the shower cooling.
- the lower layer of water gradually becomes smaller.
- the straight pipe section of the heat exchange tube has a downward slope along the direction of liquid flow in the pipe.
- the length of the straight pipe section of the heat exchange tube is gradually increased from the upper layer which is first received by the cooling water spray to the lower layer which receives the spray cooling water.
- the heat exchange tube of the coil is S-shaped, and one or more pieces of the filler are disposed in a plane space formed by the heat exchange tube, and cooperate with the heat exchange tube Fixedly, continuously covering at least a portion of the surface of the plurality of heat exchange tubes.
- the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor
- the air outlet unit has a refrigeration cycle mode; the evaporative condenser is one or more parallel.
- the exhaust port of the compressor is connected to a gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through a throttling device, the gas pipe of the evaporator and the compressor
- the air inlet unit is connected, so the air conditioning unit has a refrigeration cycle mode and a heat pump cycle mode; the air conditioning unit is provided with a first refrigeration wide, a second refrigeration valve, a first heat pump wide and a second heat pump valve; the first refrigeration valve is disposed at a second refrigeration valve is disposed on a connecting line between the air inlet of the compressor and the gas pipe of the evaporator, and the first heat pump is disposed at the compressor.
- the second heat pump valve is disposed on the connecting pipe of the gas pipe of the evaporator and the gas pipe of the evaporating condenser.
- the exhaust port of the compressor is provided with a first commutation width
- the suction port of the compressor is provided with a second commutation width
- the two outlets of the first reversing valve are respectively connected with the evaporative condenser
- the gas pipe is connected to the gas pipe of the evaporator, and the two inlets of the second commutation are respectively connected with the gas pipe of the evaporative condenser and the gas pipe of the evaporator
- the heat pump and the second heat pump use an electric wide or manual valve
- the first and second reversing valves are electric or pneumatic two-position three-way reversing valves.
- the air conditioning unit is provided with a four-way valve, and the four interfaces of the four-way reversing valve are respectively connected to the compressor exhaust port, the gas pipe of the evaporative condenser, the gas pipe of the evaporator, and the compressor. Suction port Connected.
- the air conditioning unit is set to a split or multiple online mode.
- the working principle of the invention In the refrigeration cycle mode, when the refrigerant is compressed by the compressor into a high temperature and high pressure state, the refrigerant enters the evaporative condenser through the pipeline of the refrigeration system, and after the evaporative condenser, the gas in the high temperature and high pressure state is Cooling into a low-temperature and high-pressure liquid, and forming a low-temperature and low-pressure liquid through a throttling device to enter the evaporator to exchange heat with the air to obtain cold air, and then the refrigerant liquid evaporates and vaporizes in the evaporator and is sucked away by the compressor to complete the refrigeration cycle.
- the heat pump cycle mode when the refrigerant is compressed by the compressor into a high-temperature and high-pressure gas, the refrigerant enters the evaporator through the pipeline of the refrigeration system, and exchanges heat with the air to obtain hot air. At the same time, the gas in the high-temperature and high-pressure state is cooled.
- the low temperature and high pressure liquid is passed through a throttling device to form a low temperature and low pressure liquid into the evaporative condenser, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser and is sucked away by the compressor to complete the heat pump cycle mode.
- the invention adopts a packing-coupled serpentine coil evaporating condenser, which replaces the traditional air-cooling and water-cooling modes, and can further improve the heat exchange efficiency;
- the elbows at both ends of the longitudinal coil are placed in the airflow and cooling water sprinkling space to improve the effective utilization area of the coil;
- the evaporative condenser adopts a packing coupling longitudinal serpentine coil to make the cooling water flow through the surface of the upper heat exchange tube and then flow to the surface of the lower heat exchange tube under the guidance of the packing to realize the guiding water sowing and reduce the cooling water in the heat exchange.
- the dwell at the bottom of the tube reduces the phenomenon that the cooling water drifts backward or floats under the blowing of the cooling air, and at the same time increases the surface area of the evaporating heat transfer of the cooling water, thereby improving the heat exchange efficiency and reducing the usage of the heat exchange tubes.
- FIG. 1 is a schematic view showing the principle of a refrigeration cycle mode of an air conditioning unit of the present invention
- FIG. 2 is a schematic view of the principle of the air conditioning unit of the present invention
- 3 is a schematic view showing the principle of a heat pump cycle mode of the air conditioning unit of the present invention
- FIG. 4 is a schematic view showing the principle of using a plurality of evaporators in parallel in the air conditioning unit of the present invention
- Figure 5 is a schematic view showing the principle of using a two-position three-way reversing valve for the air conditioning unit of the present invention
- FIG. 6 is a schematic view showing the principle of using a four-way reversing valve for the air conditioning unit of the present invention
- Figure 7 is a schematic structural view of Embodiment 1 of the evaporative condenser of the present invention.
- Figure 8 is a partial cross-sectional view showing the A-A of the evaporative condenser of the present invention; the structure of the heat exchanger can be shown in the figure;
- Figure 9 is a schematic structural view of a heat exchange fin in the first embodiment of the evaporative condenser of the present invention
- Figure 10 is a cross-sectional view of the heat transfer fin of the first embodiment of the evaporative condenser of the present invention
- the cross-sectional direction corresponds to Figure 9 A-A direction
- Figure! 1 is a cross-sectional view of another heat exchange fin of the first embodiment of the evaporative condenser of the present invention; the cross-sectional direction corresponds to the A-A direction of FIG. 9;
- Figure! 2 is a schematic structural view of Embodiment 2 of the evaporative condenser of the present invention.
- Figure 3 is a schematic structural view of the heat exchange fins in the second embodiment of the evaporative condenser of the present invention
- 4 is a cross-sectional view taken along line A-A of the heat transfer fin shown in FIG. 7;
- Figure 15 is a schematic view showing another structure of the coil of the evaporative condenser of the present invention.
- Figure 16 is a schematic view showing another structure of the coil of the evaporative condenser of the present invention.
- Figure 17 is a schematic cross-sectional view showing an embodiment of the evaporative condenser of the present invention.
- Figure 18 is a schematic view showing the structure of the condenser fan placed in the front part of the heat exchanger according to the present invention.
- Figure 19 is a schematic view showing the structure of the condenser fan vertically placed in the present invention.
- Figure 20 is a schematic view showing the structure of a condenser fan placed vertically and using a double-group heat exchanger according to the present invention
- Figure 21 is a schematic view showing another structure of the present invention in which a condenser fan is vertically placed and a double-group heat exchanger is used.
- the air conditioning unit includes a compressor 1, an evaporative condenser 2, a throttling device 3, an evaporator 4, and a fan 5;
- the exhaust port 8 of the compressor is connected to the gas pipe 2a of the evaporative condenser, and the liquid pipe 2b of the evaporative condenser is connected to the liquid pipe 4a of the evaporator through a throttling device, the gas pipe 4b of the evaporator and the compressor
- the suction port 9 is connected.
- the evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling and will not be described in detail herein.
- the working principle of the invention When the refrigerant is compressed by the compressor 1 into a high temperature and high pressure state, the refrigerant enters the evaporative condenser 2 through the pipeline of the refrigeration system, and after passing through the evaporative condenser 2, the gas in the high temperature and high pressure state is cooled to a low temperature.
- the high-pressure liquid is formed into a low-temperature and low-pressure liquid through the throttling device 3 to enter the evaporator 4 to exchange heat with the air to obtain cold air, and then the refrigerant liquid evaporates and vaporizes in the evaporator 4 and is sucked away by the compressor 1 to complete the refrigeration. Loop mode.
- Example 2
- FIG. 2 is a schematic view showing the principle of the air conditioning unit of the present invention, which is different from the first embodiment in that the air conditioning unit is provided with a first refrigerating chamber 10, a second refrigerating valve 11, and a first heat pump valve 12. And a second heat pump valve 13; the first refrigerating valve 10 is disposed on a connecting line of the exhaust port 8 of the compressor and the gas pipe 2a of the evaporative condenser, and the second refrigerating valve 11 is disposed at the suction port 9 of the compressor On the connecting line with the gas pipe 4b of the evaporator, the first heat pump valve 12 is disposed on the connecting line of the exhaust port 8 of the compressor and the gas pipe 4b of the evaporator, and the second heat pump valve 13 is disposed at the compressor The suction port 9 is connected to the gas pipe 2a of the evaporative condenser.
- the air conditioning unit has a refrigeration cycle mode and a heat pump cycle mode.
- the evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling.
- the working principle of the invention When the heat pump is in the circulation mode, as shown in FIG. 3, the first heat pump width 12 and the second heat pump valve 13 are opened at this time, and the first cooling width 10 and the second refrigeration valve 11 are closed, and the refrigerant is discharged.
- the compressor 1 When the compressor 1 is compressed into a high-temperature and high-pressure gas, it enters the evaporator 4 from the refrigeration system pipe, exchanges heat with the air to obtain hot air, and then the high-temperature and high-pressure gas is cooled into a low-temperature high-pressure liquid, and is throttled by the throttling device 3
- the low-temperature low-pressure liquid is formed into the evaporative condenser 2, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser 2 and is sucked away by the compressor 1, completing the heat pump circulation mode.
- the evaporative condenser 2 employs a longitudinally disposed coil of filler coupling.
- Fig. 4 is a schematic view showing the principle of the air conditioning unit of the present invention in which a plurality of evaporators are connected in parallel, which is different from the embodiment i in that the evaporator 4 is connected in parallel by a plurality of evaporators. Also, the evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling.
- Example 4
- FIG. 5 is a schematic view showing the principle of the ffi two-position three-way reversing valve of the air conditioning unit of the present invention. Compared with the first embodiment, the difference is that the exhaust port 8 of the compressor 1 is provided with the first two.
- the suction port 9 of the compressor is provided with a second two-position three-way reversing valve 15; the first two-position three-way reversing the width of the two outlets respectively and the gas of the evaporative condenser
- the tube 2a is connected to the gas tube 4b of the evaporator, and the two inlets of the second two-position three-way switching valve 15 are connected to the gas tube 2a of the evaporative condenser and the gas tube 4b of the evaporator, respectively.
- FIG. 6 is a schematic view showing the principle of using a four-way reversing valve for the air conditioning unit of the present invention. Compared with the first embodiment, the difference is that the four interfaces of the four-way reversing width 16 are respectively arranged with the compressor.
- the gas port 8, the gas pipe 2a of the evaporative condenser, the gas pipe 4b of the evaporator, and the suction port 9 of the compressor are connected.
- the evaporative condenser 2 used in the above embodiment will be described in detail below.
- FIG. 7 and Figure 8 show the structure of the evaporative condenser 2 of the present invention, including a coil heat exchanger, a cooling fan 21, a water pump 22, a water distributor 23, a sump 24 and a frame 25;
- the heat exchange fins formed by the plurality of serpentine coils are connected by a mouthpiece header 28 and an outlet header 29.
- Each of the heat exchange fins includes a longitudinal serpentine (S-shaped) coil 26 and a packing 27 disposed between the planar spaces formed by the serpentine coils, and the packing and the coil form a tight fit structure, that is, the coupling therebetween Connected to form a segment structure.
- the coil is longitudinally disposed, that is, the cooling wind blown by the fan flows along the approximate length direction of the straight pipe section of the coil (the two do not need to be completely parallel); basically, the cooling wind is from each heat exchange fin
- the formed planar space is swept flat, and the coil 7 is provided with at least one piece of packing 8 for guiding the spray cooling water from the upper heat exchange tube to the lower heat exchange tube.
- the serpentine coil 26 is formed by continuous S-shaped bending of the heat exchange tubes, wherein the straight sections of the heat exchange tubes 261 are substantially parallel.
- the coil 26 can also be fitted with a packing and suitable for use in other forms within the evaporative condenser. Shape.
- the heat exchange tube of the serpentine coil 26 may be a copper tube, a stainless steel tube or a galvanized steel tube, etc., and the internal flow passage has a circular, elliptical, spiral, corrugated, and olive shape.
- the inner and outer surfaces of the serpentine coil 26 can adopt a smooth surface, preferably an enhanced heat transfer surface provided with internal and external threads, while the outer surface of the serpentine coil is provided with hydrophilic or anticorrosive. coating.
- Each serpentine coil has an inlet and an outlet for the flow passage.
- Figures 9 and 10 show the construction of the heat transfer fins, including the coil 26 and the packing 27, having a structure in which a piece of packing 27 is formed in continuous coupling with the coil 26.
- the filler of the one piece corresponds to the heat exchange tube 261 of the corresponding position coil, and a plurality of grooves 271 matched with the size are provided for accommodating the heat pipe.
- the above-mentioned piece of filler 27 completely covers one side surface of the heat transfer tube of the coil 26.
- the filler 27 is made of, but not limited to, a rubber material such as rubber (PVC, PP, PE, etc.), paper or aluminum foil, or copper foil.
- the filler 27 may be a flat plate filler having a smooth surface, or may be a one-way or multi-directional corrugated filler; the cross-sectional shape may be wavy, rectangular or oblong, wherein preferably one or both sides of the filler are formed.
- the undulating convex and concave surface facilitates the flow of the spray cooling water and increases the residence time of the cooling water on the surface of the filler, and correspondingly increases the evaporation heat exchange area.
- the packing 27 is two sheets which are fitted to each other on both side surfaces of the serpentine coil in a snap-fit manner to form a continuous coupling.
- the two sheets of filler 27 can enclose the heat exchange tubes 261 of the coils, or a certain gap can be left at the joint of the two sheets of filler 27, as shown in Fig. 11, the slit can allow a cooling water to flow through The surface of the heat exchange tube.
- the high temperature fluid enters the serpentine coil 26 through the inlet header 28, at which time the water pump 22 delivers the low temperature water in the sump 24 to the water distributor 23 at the top of the serpentine coil, and sprays it onto the serpentine tray through the nozzle.
- the outer surface of the tube forms a very thin water film.
- the fan 21 introduces a wind having a lower temperature and a relative humidity into the space where the evaporative condenser is located, and the heat exchanger and the heat exchanger and the filler 27 are passed through.
- the cooling water is subjected to sufficient heat exchange: part of the water in the water film absorbs heat and evaporates, and the rest falls into the sump 24, and the water supply pump 22 circulates, and the high temperature fluid is cooled to a low temperature fluid and then flows out from the outlet header 29.
- the present invention may also provide another type of evaporative condenser having a packing structure, including a coil heat exchanger, a fan 21, a water pump 22, a water distributor 23, a sump 24, and a frame 25;
- the heat exchanger is composed of a plurality of serpentine coils formed by a plurality of serpentine coils connected by an inlet header 28 and an outlet header 29.
- Each heat exchange fin includes a longitudinal serpentine (S-shaped) coil 26 and a packing 27, and the packing 27 is disposed in the adjacent heat exchange tube Between 20, a gap coupling is formed, that is, the gap between the heat exchange tubes 261 is filled by the filler 27 to connect the coil 26 and the filler 27 into a continuous water flow surface.
- the above-mentioned filler 27 can be fixed between the coil 26 and the packing 27 by welding, snapping or connecting means between the heat exchange tubes of the coil 26.
- the connecting member is a strap F, and one or more fixing holes are formed at the edge of the filler 27, and a strap is passed through the fixing hole to securely bind it to the corresponding heat exchange tube 261.
- the heat exchange tube of the coil is a circular tube or an elliptical tube
- the snapping mode may also be adopted, that is, the edge of the packing is set as a U-shaped groove to securely accommodate the heat exchange tube of the coil.
- the packing disposed between the adjacent heat exchange tubes may be one piece or a plurality of pieces.
- the coil in this embodiment can also adopt other structures.
- the straight pipe sections of the heat exchange tubes 261 of the coil 26 are parallel to each other, and the pipe pitch is gradually reduced from the upper layer to the lower layer. Accordingly, the radius of curvature of the curved portion of the heat exchange tube 261 is also gradually reduced, and the use of the filler 27 and the manner of connection with the coil 26 can be referred to the above embodiment.
- the upper heat exchange tube 261 first receives the sprayed cold water, and then flows from top to bottom to the lower heat exchange tube 261; when the high temperature refrigerant enters from the inlet and then flows out from the outlet, due to the upper layer of the in-line refrigeration
- the temperature of the agent is higher than the temperature of the next layer, so that the temperature of the water passing through the upper heat exchange tube 261 rises higher than the temperature of the water passing through the heat exchange tube 261 of the next layer, so that the filler 27 of the upper layer is lengthened. It is used to extend the heat exchange time of the cooling water in the filler 27.
- the coil of the structure can reduce the temperature difference between the lower heat exchange tube and the cooling water, thereby improving the heat exchange effect between the heat exchange tube and the cooling water, and is superior.
- the coil shown in Fig. 16 the straight section of the heat exchange tube 261 of the coil has a downward slope along the direction of liquid flow in the tube, and the liquid in the tube is a high temperature refrigerant.
- the high temperature refrigerant enters from the inlet, the refrigerant flows in a downward slope direction until the outlet flows out. Since the heat exchange tube 261 has a certain downward slope in the direction of flow, the coil more prominently reduces the pressure drop of the refrigerant from the inlet to the outlet.
- FIG. 17 is a schematic cross-sectional view showing another condenser of the present invention for adding a heat exchange filler, between the serpentine coils 26 and the heat exchanger in the heat exchanger.
- One or more pieces of filler 27' may be provided at the top or at the bottom of the heat exchanger.
- Fig. 20 shows that the evaporative condenser places the fan 21 vertically, and two sets of heat exchangers are disposed in the condenser.
- Figure 21 also shows another implementation of an evaporative condenser having two sets of heat exchangers.
- the heat exchange tubes of the heat exchanger used in this embodiment are not equal in length, that is, the length of the straight pipe section of the heat exchange tube 261 of the coil is from The upper layer to the next layer is gradually increased, wherein the upper heat exchange tube 261 first receives the spray cold water, and then flows from the top to the bottom to the lower heat exchange tube 261.
- the heat exchange fins provided in this embodiment are more suitable for evaporative condensers using two sets of heat exchangers. The difference from the embodiment shown in Fig.
- this embodiment can install a fan of a larger size and horsepower by changing the length of the straight pipe section of the heat exchange pipe 261 without changing the outer dimensions of the condenser.
- the fan 21 of the solid line part is the heat exchange tube piece provided by the embodiment, and the fan 21' of the broken line part is the heat exchange tube piece of the heat exchange tube of the equal length straight pipe section shown in FIG.
- the fan used in the former solid line
- the fan (dotted line) used in the latter which increases the air volume and thus improves the heat exchange effect.
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- Combustion & Propulsion (AREA)
- Other Air-Conditioning Systems (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Air Filters, Heat-Exchange Apparatuses, And Housings Of Air-Conditioning Units (AREA)
Description
本发明涉及空调设备领域, 特别涉及一种盘管蒸发式冷凝器的空调机组。 The invention relates to the field of air conditioning equipment, in particular to an air conditioning unit of a coil evaporative condenser.
^ 、采用蒸发式冷凝器向室外空气中放热并应用于空调机组中, 是实现高效、 稳定制冷的重要途径, 与水冷式冷凝器和风冷式冷凝器相比, 其换热效率高, 具有显著的节能减排前景。现阶段市场上空调机组中所用的蒸发式冷凝器用盘 管是横向盘管,通过对盘管外表面采用喷淋水进行冷却, 并利用循环的喷淋水 使空气蒸发带走热量。 由于冷却风向垂直于盘管(即冷却风从每个换热管片所 形成的平面空间穿过, 并与换热管的直管段垂直), 盘管会存在迎风面和背风 面, 在背风面缺乏空气对流换热, 降低了盘管换热效率。 另一方面, 由于横向 盘管有效换热面积小, 所配盘管长度则需加大, 同 H寸由于传统横向盘管的管与 管之间错位布置, 没有机械清洗的操作空间, 亦存在难清洗的缺点。 因此, 横 向盘管的不足极大地限制了蒸发式冷凝器在空调机组中的应用。 ^, using an evaporative condenser to release heat into the outdoor air and applied to the air conditioning unit is an important way to achieve efficient and stable cooling. Compared with water-cooled condensers and air-cooled condensers, the heat exchange efficiency is high. Has significant energy saving and emission reduction prospects. At present, the coil for evaporative condenser used in the air-conditioning unit on the market is a transverse coil, which is cooled by spraying water on the outer surface of the coil, and uses circulating spray water to evaporate air to remove heat. Since the cooling wind direction is perpendicular to the coil (that is, the cooling air passes through the plane space formed by each heat exchange tube and is perpendicular to the straight pipe section of the heat exchange tube), the coil has a windward side and a leeward side, and the leeward side Lack of air convection heat transfer reduces coil heat transfer efficiency. On the other hand, since the effective heat exchange area of the transverse coil is small, the length of the coil to be used needs to be increased. The same as the H inch, due to the misalignment between the tubes and the tubes of the conventional transverse coil, there is no mechanical cleaning operation space, and there is also The disadvantage of being difficult to clean. Therefore, the lack of lateral coils greatly limits the use of evaporative condensers in air conditioning units.
本 明的目的在于克服现有技术的缺点,提供一种带填料耦合盘管蒸发式 冷凝器的空调机组, 以提高换热效率。 The purpose of the present invention is to overcome the shortcomings of the prior art and to provide an air conditioning unit with a packed coupling coil evaporative condenser to improve heat exchange efficiency.
本发明的目的通过下述技术方案实现: The object of the invention is achieved by the following technical solution:
一种带填料耦合盘管蒸发式冷凝器的空调机组,包括压缩机、蒸发式冷凝 器、节流装置、蒸发器和风机,所述蒸发式冷凝器包括盘管换热器、冷却风机、 布水器和集水池;所述盘管换热器由多个换热管片通过进口集管和出口集管连 接组成; 所述换热管片包括盘管和填料,所述盘管设有至少一片用于引导喷淋 冷却水从上层换热管流向下层换热管的填料。 An air conditioning unit with a packed coupling coil evaporative condenser, comprising a compressor, an evaporative condenser, a throttling device, an evaporator and a fan, the evaporative condenser comprising a coil heat exchanger, a cooling fan, and a cloth a water heater and a sump; the coil heat exchanger is composed of a plurality of heat exchange fins connected through an inlet header and an outlet header; the heat exchange fins include a coil and a filler, and the coil is provided with at least A piece of filler for guiding the spray cooling water from the upper heat exchange tube to the lower heat exchange tube.
优选地,所述盘管纵向设置, 即所述风机吹入的冷却风沿所述盘管的直管 进一步地, 所述盘管的换热管 S形弯折; 所述填料设置于相邻的所述换热 管之间, 以将所述换热管连成一片连续的水流面。 Preferably, the coil is longitudinally disposed, that is, the cooling wind blown by the fan is along the straight tube of the coil Further, the heat exchange tubes of the coil are S-shaped; the filler is disposed between the adjacent heat exchange tubes to connect the heat exchange tubes into a continuous water flow surface.
进一步地, 相邻所述换热管的直管段相互平行,相邻所述换热管的直管段 的管间距相同,或者管间距从位于先接受喷淋冷却水的上层至后接受喷淋冷却 水的下层逐渐变小。 Further, the straight pipe sections adjacent to the heat exchange tubes are parallel to each other, and the pipe spacing of the straight pipe sections adjacent to the heat exchange pipes is the same, or the pipe spacing is from the upper layer receiving the spray cooling water to the shower cooling. The lower layer of water gradually becomes smaller.
优选地, 所述换热管的直管段具有沿管内液体流动方向的向下坡度。 还可选择地,所述换热管的直管段的长度从位于先接受冷却水喷淋的上层 至后接受喷淋冷却水的下层逐渐增加。 Preferably, the straight pipe section of the heat exchange tube has a downward slope along the direction of liquid flow in the pipe. Alternatively, the length of the straight pipe section of the heat exchange tube is gradually increased from the upper layer which is first received by the cooling water spray to the lower layer which receives the spray cooling water.
进一步地, 还可选择, 所述盘管的换热管 S形弯折, 一片或多片所述填料 设置在所述换热管形成的平面空间内, 且与所述换热管相互配合地固接, 连续 覆盖于多个所述换热管的至少一部分表面。 Further, optionally, the heat exchange tube of the coil is S-shaped, and one or more pieces of the filler are disposed in a plane space formed by the heat exchange tube, and cooperate with the heat exchange tube Fixedly, continuously covering at least a portion of the surface of the plurality of heat exchange tubes.
进一步地, 所述压缩机的排气口与蒸发式冷凝器的气体管连接, 蒸发式冷 凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机 的吸气口连接, 所述空调机组具有制冷循环模式; 所述蒸发式冷凝器为一个或 多个并联。 Further, the exhaust port of the compressor is connected to the gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through the throttling device, and the gas pipe of the evaporator and the suction of the compressor The air outlet unit has a refrigeration cycle mode; the evaporative condenser is one or more parallel.
可选择地, 所述压缩机的排气口与蒸发式冷凝器的气体管连接, 蒸发式冷 凝器的液体管通过节流装置与蒸发器的液体管连接,蒸发器的气体管与压缩机 的吸气口连接, 所以空调机组具有制冷循环模式和热泵循环模式; 所述空调机 组设置有第一制冷阔、第二制冷阀、 第一热泵阔和第二热泵阀; 第一制冷阀设 置在压缩机的排气口与蒸发式冷凝器的气体管的连接管路上,第二制冷阀设置 在压缩机的吸气口与蒸发器的气体管的连接管路上,第一热泵阔设置在压缩机 的排气口与蒸发器的气体管的连接管路上,第二热泵阀设置在压缩机的吸气口 与蒸发式冷凝器的气体管的连接管路上。 Optionally, the exhaust port of the compressor is connected to a gas pipe of the evaporative condenser, and the liquid pipe of the evaporative condenser is connected to the liquid pipe of the evaporator through a throttling device, the gas pipe of the evaporator and the compressor The air inlet unit is connected, so the air conditioning unit has a refrigeration cycle mode and a heat pump cycle mode; the air conditioning unit is provided with a first refrigeration wide, a second refrigeration valve, a first heat pump wide and a second heat pump valve; the first refrigeration valve is disposed at a second refrigeration valve is disposed on a connecting line between the air inlet of the compressor and the gas pipe of the evaporator, and the first heat pump is disposed at the compressor. The second heat pump valve is disposed on the connecting pipe of the gas pipe of the evaporator and the gas pipe of the evaporating condenser.
可选择地, 所述压缩机的排气口设有第一换向阔, 压缩机的吸气口设有第 二换向阔;第一换向阀的两个出口分别与蒸发式冷凝器的气体管和蒸发器的气 体管连接,第二换向阔的两个进口分别与蒸发式冷凝器的气体管和蒸发器的气 体管连接; 所述第一制冷阀、第二制冷阔、第一热泵阔和第二热泵阖釆用电动 阔或手动阀; 所述第一换向阀和第二换向阀为电动或气动的二位三通换向阀。 Optionally, the exhaust port of the compressor is provided with a first commutation width, and the suction port of the compressor is provided with a second commutation width; the two outlets of the first reversing valve are respectively connected with the evaporative condenser The gas pipe is connected to the gas pipe of the evaporator, and the two inlets of the second commutation are respectively connected with the gas pipe of the evaporative condenser and the gas pipe of the evaporator; the first refrigerating valve, the second refrigerating valve, and the first The heat pump and the second heat pump use an electric wide or manual valve; the first and second reversing valves are electric or pneumatic two-position three-way reversing valves.
可选择地,所述空调机组设置有四通换 阀, 四通换向阀的四个接口分别 与压縮机排气口、蒸发式冷凝器的气体管、蒸发器的气体管和压縮机的吸气口 连接。 Optionally, the air conditioning unit is provided with a four-way valve, and the four interfaces of the four-way reversing valve are respectively connected to the compressor exhaust port, the gas pipe of the evaporative condenser, the gas pipe of the evaporator, and the compressor. Suction port Connected.
可选择地, 所述空调机组设置为分体式或多联机模式。 Alternatively, the air conditioning unit is set to a split or multiple online mode.
本发明的工作原理: 当制冷循环模式时, 制冷剂经压缩机压縮后成高温高 压状态的气体时由制冷系统管道进入蒸发式冷凝器, 经过蒸发式冷凝器后, 高 温高压状态的气体被冷却成低温高压液体,并经节流装置形成低温低压液体进 入蒸发器中与空气进行热交换, 制取冷风, 然后在蒸发器中制冷剂液体蒸发汽 化并被压縮机吸走, 完成制冷循环模式; 当热泵循环模式时, 制冷剂经压缩机 压缩后成高温高压状态的气体时由制冷系统管道进入蒸发器,与空气进行热交 换, 制取热风, 同时, 高温高压状态的气体被冷却成低温高压液体, 并经节流 装置形成低温低压液体进入蒸发式冷凝器,然后在蒸发式冷凝器中制冷剂液体 蒸发汽化并被压缩机吸走, 完成热泵循环模式。 The working principle of the invention: In the refrigeration cycle mode, when the refrigerant is compressed by the compressor into a high temperature and high pressure state, the refrigerant enters the evaporative condenser through the pipeline of the refrigeration system, and after the evaporative condenser, the gas in the high temperature and high pressure state is Cooling into a low-temperature and high-pressure liquid, and forming a low-temperature and low-pressure liquid through a throttling device to enter the evaporator to exchange heat with the air to obtain cold air, and then the refrigerant liquid evaporates and vaporizes in the evaporator and is sucked away by the compressor to complete the refrigeration cycle. Mode; In the heat pump cycle mode, when the refrigerant is compressed by the compressor into a high-temperature and high-pressure gas, the refrigerant enters the evaporator through the pipeline of the refrigeration system, and exchanges heat with the air to obtain hot air. At the same time, the gas in the high-temperature and high-pressure state is cooled. The low temperature and high pressure liquid is passed through a throttling device to form a low temperature and low pressure liquid into the evaporative condenser, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser and is sucked away by the compressor to complete the heat pump cycle mode.
本发明相对于现有技术具有如下的优点及效果: The present invention has the following advantages and effects over the prior art:
1、 本发明采用填料耦合蛇形盘管蒸发式冷凝器, 取代传统的风冷和水冷 方式, 可迸一步提高换热效率; 1. The invention adopts a packing-coupled serpentine coil evaporating condenser, which replaces the traditional air-cooling and water-cooling modes, and can further improve the heat exchange efficiency;
2、 采用纵向盘管, 冷却风向与盘管长度方向一致, 不存在迎风面和背风 面, 减少换热盘管表面迎风面、 背风面及千点, 减少换热盘管结垢风险; 2. Longitudinal coil is adopted, the cooling wind direction is consistent with the length of the coil, there is no windward and leeward surface, the windward surface, the leeward surface and the thousand points of the heat exchange coil surface are reduced, and the risk of scaling of the heat exchange coil is reduced;
3、 纵向盘管两端弯头置于气流和冷却水播洒空间内, 提高盘管有效利用 面积; 3. The elbows at both ends of the longitudinal coil are placed in the airflow and cooling water sprinkling space to improve the effective utilization area of the coil;
4、 使用本蒸发式冷凝器清洁容易, 维护较为方便, 使用成本较低; 4. It is easy to clean with this evaporative condenser, it is convenient to maintain, and the use cost is low;
5、 本蒸发式冷凝器采用填料耦合纵 ^蛇形盘管, 使冷却水流经上层换热 管表面后在填料的引导下流向下层换热管表面, 实现引导播水, 减少冷却水在 换热管底部的停留, 减少冷却水在冷却空气的吹动下向后漂移或飞水的现象, 同时增大冷却水蒸发换热表面积, 达到提高换热效率、减少换热管使用量的作 用。 5. The evaporative condenser adopts a packing coupling longitudinal serpentine coil to make the cooling water flow through the surface of the upper heat exchange tube and then flow to the surface of the lower heat exchange tube under the guidance of the packing to realize the guiding water sowing and reduce the cooling water in the heat exchange. The dwell at the bottom of the tube reduces the phenomenon that the cooling water drifts backward or floats under the blowing of the cooling air, and at the same time increases the surface area of the evaporating heat transfer of the cooling water, thereby improving the heat exchange efficiency and reducing the usage of the heat exchange tubes.
图 1是本发明空调机组的制冷循环模式的原理示意图; 1 is a schematic view showing the principle of a refrigeration cycle mode of an air conditioning unit of the present invention;
图 2是本发明空调机组的原理示意图; 图 3是本发明空调机组的热泵循环模式的原理示意图; 2 is a schematic view of the principle of the air conditioning unit of the present invention; 3 is a schematic view showing the principle of a heat pump cycle mode of the air conditioning unit of the present invention;
图 4是本发明空调机组采用多个蒸发器并联的原理示意图; 4 is a schematic view showing the principle of using a plurality of evaporators in parallel in the air conditioning unit of the present invention;
图 5是本发明空调机组采用二位三通换向阀的原理示意图; Figure 5 is a schematic view showing the principle of using a two-position three-way reversing valve for the air conditioning unit of the present invention;
图 6是本发明空调机组采用四通换向阀的原理示意图; 6 is a schematic view showing the principle of using a four-way reversing valve for the air conditioning unit of the present invention;
图 7是本发明蒸发式冷凝器实施例一的结构示意图; Figure 7 is a schematic structural view of Embodiment 1 of the evaporative condenser of the present invention;
图 8是本发明蒸发式冷凝器的 A- A局部剖面示意图; 图中可示换热器的结 构; Figure 8 is a partial cross-sectional view showing the A-A of the evaporative condenser of the present invention; the structure of the heat exchanger can be shown in the figure;
图 9是本发明蒸发式冷凝器实施例一中的换热管片的结构示意图; 图 10是本发明蒸发式冷凝器实施例一中的换热管片的剖视图;剖视方向对 应于图 9的 A- A向; Figure 9 is a schematic structural view of a heat exchange fin in the first embodiment of the evaporative condenser of the present invention; Figure 10 is a cross-sectional view of the heat transfer fin of the first embodiment of the evaporative condenser of the present invention; the cross-sectional direction corresponds to Figure 9 A-A direction;
图!1是本发明本发明蒸发式冷凝器实施例一中另一种换热管片的剖视图; 剖视方向对应于图 9的 A- A向; Figure! 1 is a cross-sectional view of another heat exchange fin of the first embodiment of the evaporative condenser of the present invention; the cross-sectional direction corresponds to the A-A direction of FIG. 9;
图! 2是本发明蒸发式冷凝器实施例二的结构示意图; Figure! 2 is a schematic structural view of Embodiment 2 of the evaporative condenser of the present invention;
图! 3是本发明蒸发式冷凝器实施例二中的换热管片的结构示意图; 图! 4是图 7中所示换热管片的 A- A向剖视图; Figure 3 is a schematic structural view of the heat exchange fins in the second embodiment of the evaporative condenser of the present invention; 4 is a cross-sectional view taken along line A-A of the heat transfer fin shown in FIG. 7;
图 15是本发明蒸发式冷凝器的盘管的另一种结构示意图; Figure 15 is a schematic view showing another structure of the coil of the evaporative condenser of the present invention;
图 16是本发明蒸发式冷凝器的盘管的另一种结构示意图; Figure 16 is a schematic view showing another structure of the coil of the evaporative condenser of the present invention;
图 17是本发明蒸发式冷凝器实施例≡的剖面示意图; Figure 17 is a schematic cross-sectional view showing an embodiment of the evaporative condenser of the present invention;
图 18是本发明将冷凝器风机放置在换热器前部的结构示意图; Figure 18 is a schematic view showing the structure of the condenser fan placed in the front part of the heat exchanger according to the present invention;
图 19是本发明将冷凝器风机垂直放置的结构示意图; Figure 19 is a schematic view showing the structure of the condenser fan vertically placed in the present invention;
图 20是本发明将冷凝器风机垂直放置并采用双组换热器的结构示意图; 图 21是本发明将冷凝器风机垂直放置并采用双组换热器的另一结构示意 Figure 20 is a schematic view showing the structure of a condenser fan placed vertically and using a double-group heat exchanger according to the present invention; Figure 21 is a schematic view showing another structure of the present invention in which a condenser fan is vertically placed and a double-group heat exchanger is used.
下面结合实施例及 Pfi图对本发明作进一步详细的描述,但本发明的实施方 式不限于此。 The present invention will be further described in detail below with reference to the embodiments and the Pfi drawings, but the embodiments of the present invention are not limited thereto.
实施例 1 Example 1
图 1示出了本发明空调机组的制冷循环模式的原理示意图, 由图 1可见, 本 空调机组包括压缩机 1、 蒸发式冷凝器 2、 节流装置 3、 蒸发器 4和风机 5; 所述 压縮机的排气口 8与蒸发式冷凝器的气体管 2a连接, 蒸发式冷凝器的液体管 2b 通过节流装置与蒸发器的液体管 4a连接,蒸发器的气体管 4b与压縮机的吸气口 9连接。该蒸发式冷凝器 2采用了填料耦合的纵向设置的盘管,在此先不做详细 描述。 本发明的工作原理: 制冷剂经压縮机 1压缩后成高温高压状态的气体时由 制冷系统管道进入蒸发式冷凝器 2, 经过蒸发式冷凝器 2后, 高温高压状态的气 体被冷却成低温高压液体,并经节流装置 3形成低温低压液体进入蒸发器 4中与 空气进行热交换, 制取冷风, 然后在蒸发器 4中制冷剂液体蒸发汽化并被压縮 机 1吸走, 完成制冷循环模式。 实施例 2 1 is a schematic view showing the principle of a refrigeration cycle mode of an air conditioning unit of the present invention. As can be seen from FIG. 1, the air conditioning unit includes a compressor 1, an evaporative condenser 2, a throttling device 3, an evaporator 4, and a fan 5; The exhaust port 8 of the compressor is connected to the gas pipe 2a of the evaporative condenser, and the liquid pipe 2b of the evaporative condenser is connected to the liquid pipe 4a of the evaporator through a throttling device, the gas pipe 4b of the evaporator and the compressor The suction port 9 is connected. The evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling and will not be described in detail herein. The working principle of the invention: When the refrigerant is compressed by the compressor 1 into a high temperature and high pressure state, the refrigerant enters the evaporative condenser 2 through the pipeline of the refrigeration system, and after passing through the evaporative condenser 2, the gas in the high temperature and high pressure state is cooled to a low temperature. The high-pressure liquid is formed into a low-temperature and low-pressure liquid through the throttling device 3 to enter the evaporator 4 to exchange heat with the air to obtain cold air, and then the refrigerant liquid evaporates and vaporizes in the evaporator 4 and is sucked away by the compressor 1 to complete the refrigeration. Loop mode. Example 2
图 2示出了本发明空调机组的原理示意图, 与实施例 1相比较, 其不同之处 在于, 所述空调机组设置有第一制冷陶 10、 第二制冷阀 11、 第一热泵阀 12和第 二热泵阀 13 ; 第一制冷阀 10设置在压缩机的排气口 8与蒸发式冷凝器的气体管 2a的连接管路上, 第二制冷阀 11设置在压缩机的吸气口 9与蒸发器的气体管 4b 的连接管路上, 第一热泵阀 12设置在压缩机的排气口 8与蒸发器的气体管 4b的 连接管路上, 第二热泵阀 13设置在压缩机的吸气口 9与蒸发式冷凝器的气体管 2a的连接管路上。所以空调机组具有制冷循环模式和热泵循环模式。 同样, 该 蒸发式冷凝器 2采用了填料耦合的纵向设置的盘管。 本发明的工作原理: 当热泵循环模式时, 如图 3所示, 此时打开第一热泵 阔 12和第二热泵阀 13 , 关闭第一制冷阔 10和第二制冷阀 11, 制冷剂经压缩机 1 压缩后成高温高压状态的气体时由制冷系统管道进入蒸发器 4, 与空气进行热 交换, 制取热风, 然后高温高压状态的气体被冷却成低温高压液体, 并经节流 装置 3形成低温低压液体进入蒸发式冷凝器 2 , 然后在蒸发式冷凝器 2中制冷剂 液体蒸发汽化并被压縮机 1吸走, 完成热泵循环模式。 同样, 该蒸发式冷凝器 2 采 ffi了填料耦合的纵向设置的盘管。 实施例 3 2 is a schematic view showing the principle of the air conditioning unit of the present invention, which is different from the first embodiment in that the air conditioning unit is provided with a first refrigerating chamber 10, a second refrigerating valve 11, and a first heat pump valve 12. And a second heat pump valve 13; the first refrigerating valve 10 is disposed on a connecting line of the exhaust port 8 of the compressor and the gas pipe 2a of the evaporative condenser, and the second refrigerating valve 11 is disposed at the suction port 9 of the compressor On the connecting line with the gas pipe 4b of the evaporator, the first heat pump valve 12 is disposed on the connecting line of the exhaust port 8 of the compressor and the gas pipe 4b of the evaporator, and the second heat pump valve 13 is disposed at the compressor The suction port 9 is connected to the gas pipe 2a of the evaporative condenser. Therefore, the air conditioning unit has a refrigeration cycle mode and a heat pump cycle mode. Also, the evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling. The working principle of the invention: When the heat pump is in the circulation mode, as shown in FIG. 3, the first heat pump width 12 and the second heat pump valve 13 are opened at this time, and the first cooling width 10 and the second refrigeration valve 11 are closed, and the refrigerant is discharged. When the compressor 1 is compressed into a high-temperature and high-pressure gas, it enters the evaporator 4 from the refrigeration system pipe, exchanges heat with the air to obtain hot air, and then the high-temperature and high-pressure gas is cooled into a low-temperature high-pressure liquid, and is throttled by the throttling device 3 The low-temperature low-pressure liquid is formed into the evaporative condenser 2, and then the refrigerant liquid evaporates and vaporizes in the evaporative condenser 2 and is sucked away by the compressor 1, completing the heat pump circulation mode. Similarly, the evaporative condenser 2 employs a longitudinally disposed coil of filler coupling. Example 3
图 4示出了本发明空调机组采用多个蒸发器并联的原理示意图,与实施例 i 相比较, 其不同之处在于, 所述蒸发器 4采用多个蒸发器并联的方式。 同样, 该蒸发式冷凝器 2采用了填料耦合的纵向设置的盘管。 实施例 4 Fig. 4 is a schematic view showing the principle of the air conditioning unit of the present invention in which a plurality of evaporators are connected in parallel, which is different from the embodiment i in that the evaporator 4 is connected in parallel by a plurality of evaporators. Also, the evaporative condenser 2 employs a longitudinally disposed coil of a packing coupling. Example 4
图 5示出了本发明空调机组采 ffi二位三通换向阀的原理示意图,与实施例 1 相比较,其不同之处在于,所述压缩机 1的排气口 8设有第一二位三通换向阀 14 , 压缩机的吸气口 9设有第二二位三通换向阀 15 ; 第一二位三通换向阔 14的两个 出口分别与蒸发式冷凝器的气体管 2a和蒸发器的气体管 4b连接,第二二位三通 换向阀 15的两个进口分别与蒸发式冷凝器的气体管 2a和蒸发器的气体管 4b连 接。 实施例 5 FIG. 5 is a schematic view showing the principle of the ffi two-position three-way reversing valve of the air conditioning unit of the present invention. Compared with the first embodiment, the difference is that the exhaust port 8 of the compressor 1 is provided with the first two. a three-way reversing valve 14 , the suction port 9 of the compressor is provided with a second two-position three-way reversing valve 15; the first two-position three-way reversing the width of the two outlets respectively and the gas of the evaporative condenser The tube 2a is connected to the gas tube 4b of the evaporator, and the two inlets of the second two-position three-way switching valve 15 are connected to the gas tube 2a of the evaporative condenser and the gas tube 4b of the evaporator, respectively. Example 5
图 6示出了本发明空调机组采用四通换向阀的原理示意图,与实施例 1相比 较, 其不同之处在于,所述四通换向阔 16的四个接口分别与压缩机的排气口 8、 蒸发式冷凝器的气体管 2a、 蒸发器的气体管 4b和压缩机的吸气口 9连接。 对于上述实施例中所使用的蒸发式冷凝器 2, 下面进行详细说明。 6 is a schematic view showing the principle of using a four-way reversing valve for the air conditioning unit of the present invention. Compared with the first embodiment, the difference is that the four interfaces of the four-way reversing width 16 are respectively arranged with the compressor. The gas port 8, the gas pipe 2a of the evaporative condenser, the gas pipe 4b of the evaporator, and the suction port 9 of the compressor are connected. The evaporative condenser 2 used in the above embodiment will be described in detail below.
图 7、 图 8示出了本发明蒸发式冷凝器 2的结构, 包括盘管换热器、 冷却风 机 21、 水泵 22、 布水器 23、 集水池 24和框架 25 ; 所述换热器由多个蛇形盘管形 成的换热管片通过迸口集管 28和出口集管 29连接组成。每个换热管片包括纵向 蛇形 (S形) 盘管 26和填料 27, 填料设置在蛇形盘管形成的平面空间之间, 填 料和盘管形成一个紧密配合的结构, 即两者耦合连接, 形成管片结构。盘管纵 ^设置, 即所述风机吹入的冷却风沿所述盘管的直管段的大致长度方向(两者 并不需要完全平行)流动; 基本上就是冷却风从每个换热管片所形成的平面空 间平扫过, 所述盘管 7设有至少一片用于引导喷淋冷却水从上层换热管流向下 层换热管的填料 8。 Figure 7 and Figure 8 show the structure of the evaporative condenser 2 of the present invention, including a coil heat exchanger, a cooling fan 21, a water pump 22, a water distributor 23, a sump 24 and a frame 25; The heat exchange fins formed by the plurality of serpentine coils are connected by a mouthpiece header 28 and an outlet header 29. Each of the heat exchange fins includes a longitudinal serpentine (S-shaped) coil 26 and a packing 27 disposed between the planar spaces formed by the serpentine coils, and the packing and the coil form a tight fit structure, that is, the coupling therebetween Connected to form a segment structure. The coil is longitudinally disposed, that is, the cooling wind blown by the fan flows along the approximate length direction of the straight pipe section of the coil (the two do not need to be completely parallel); basically, the cooling wind is from each heat exchange fin The formed planar space is swept flat, and the coil 7 is provided with at least one piece of packing 8 for guiding the spray cooling water from the upper heat exchange tube to the lower heat exchange tube.
其中,蛇形盘管 26由换热管连续 S形弯曲而成,其中换热管 261的直线段大 致基本平行。该盘管 26也可以采用可安装填料并适用于蒸发冷凝器内的其它形 状。蛇形盘管 26的换热管可以采用铜管、 不锈钢管或镀锌钢管等, 其内部流道 的截面形状为圆形、 椭圆形、 螺旋形.、 波纹形和橄榄形等形状。 作为本领域人 员可以理解的是, 蛇形盘管 26内外表面可以采用光滑表面, 优选采用设有内、 外螺紋的强化传热表面, 同时所述蛇形盘管外表面设有亲水或防腐涂层。每个 蛇形盘管均设有流道的入口及出口。 Wherein, the serpentine coil 26 is formed by continuous S-shaped bending of the heat exchange tubes, wherein the straight sections of the heat exchange tubes 261 are substantially parallel. The coil 26 can also be fitted with a packing and suitable for use in other forms within the evaporative condenser. Shape. The heat exchange tube of the serpentine coil 26 may be a copper tube, a stainless steel tube or a galvanized steel tube, etc., and the internal flow passage has a circular, elliptical, spiral, corrugated, and olive shape. As can be understood by those skilled in the art, the inner and outer surfaces of the serpentine coil 26 can adopt a smooth surface, preferably an enhanced heat transfer surface provided with internal and external threads, while the outer surface of the serpentine coil is provided with hydrophilic or anticorrosive. coating. Each serpentine coil has an inlet and an outlet for the flow passage.
图 9、 10示出了换热管片的结构, 换包括盘管 26和填料 27, 具有由一片填 料 27与盘管 26形成连续耦合连接的结构。如图中所示, 该一片的填料对应相应 位置盘管的换热管 261, 设有相当数量与之大小配合的多条凹槽 271, 以用于容 置换热管。安装时, 只需将一片填料以卡合方式直接贴合于蛇形盘管的换热管 表面即可, 当然也可以辅助有其它的固定连接。 安装后, 上述一片填料 27将盘 管 26的换热管的一侧表面全部覆盖。 填料 27由但不限于橡塑 (PVC、 PP、 PE 等)、 纸质或铝箔、 铜箔等金属材料制成。 填料 27可以是一片表面平滑的平板 填料, 也可以是一片单向或多向的波紋型填料; 其截面形状可以是波浪形、 矩 形或长圆形, 其中优选填料的单侧或双侧形成有波浪形凸凹表面, 以利于喷淋 冷却水的流动, 并增加冷却水在填料表面的停留时间, 也相应增加了蒸发换热 面积。 Figures 9 and 10 show the construction of the heat transfer fins, including the coil 26 and the packing 27, having a structure in which a piece of packing 27 is formed in continuous coupling with the coil 26. As shown in the figure, the filler of the one piece corresponds to the heat exchange tube 261 of the corresponding position coil, and a plurality of grooves 271 matched with the size are provided for accommodating the heat pipe. When installing, it is only necessary to directly attach a piece of filler to the surface of the heat exchange tube of the serpentine coil in a snap-fit manner, and of course, it can also assist other fixed connections. After installation, the above-mentioned piece of filler 27 completely covers one side surface of the heat transfer tube of the coil 26. The filler 27 is made of, but not limited to, a rubber material such as rubber (PVC, PP, PE, etc.), paper or aluminum foil, or copper foil. The filler 27 may be a flat plate filler having a smooth surface, or may be a one-way or multi-directional corrugated filler; the cross-sectional shape may be wavy, rectangular or oblong, wherein preferably one or both sides of the filler are formed. The undulating convex and concave surface facilitates the flow of the spray cooling water and increases the residence time of the cooling water on the surface of the filler, and correspondingly increases the evaporation heat exchange area.
作为优选, 还可采用另一种填料与盘管的配合结构, 该填料 27为两片, 以 卡合方式相对贴合在蛇形盘管的两侧表面而形成连续耦合的形式。该两片填料 27可以将盘管的换热管 261完成包裹住, 也可以在两片填料 27的连接处留有一 定的缝隙, 如图 11中所示, 该缝隙可使一部冷却水流经换热管的表面。 Preferably, another type of filler and coiled structure may be used. The packing 27 is two sheets which are fitted to each other on both side surfaces of the serpentine coil in a snap-fit manner to form a continuous coupling. The two sheets of filler 27 can enclose the heat exchange tubes 261 of the coils, or a certain gap can be left at the joint of the two sheets of filler 27, as shown in Fig. 11, the slit can allow a cooling water to flow through The surface of the heat exchange tube.
工作时, 高温流体经进口集管 28进入蛇形盘管 26 , 此时水泵 22将集水池 24 中的低温水输送到蛇形盘管顶部的布水器 23,经喷嘴喷淋到蛇形盘管的外表面 形成很薄的水膜, 与此同时, 风机 21将温度及相对湿度较低的风引入蒸发式冷 凝器所在空间, 使其与换热器和流经换热器及填料 27的冷却水进行充分热交 换:, 水膜中部分水吸热后蒸发, 其余落入集水池 24, 供水泵 22循环用, 同时高 温的流体被冷却成低温流体后从出口集管 29流出。 During operation, the high temperature fluid enters the serpentine coil 26 through the inlet header 28, at which time the water pump 22 delivers the low temperature water in the sump 24 to the water distributor 23 at the top of the serpentine coil, and sprays it onto the serpentine tray through the nozzle. The outer surface of the tube forms a very thin water film. At the same time, the fan 21 introduces a wind having a lower temperature and a relative humidity into the space where the evaporative condenser is located, and the heat exchanger and the heat exchanger and the filler 27 are passed through. The cooling water is subjected to sufficient heat exchange: part of the water in the water film absorbs heat and evaporates, and the rest falls into the sump 24, and the water supply pump 22 circulates, and the high temperature fluid is cooled to a low temperature fluid and then flows out from the outlet header 29.
图 12-14中, 本发明还可以提供了另一种填料结构的蒸发式冷凝器, 包括 盘管换热器、 风机 21、 水泵 22、 布水器 23、 集水池 24和框架 25 ; 所述换热器由 多个蛇形盘管形成的换热管片通过进口集管 28和出口集管 29连接组成。每个换 热管片包括纵向蛇形 (S形) 盘管 26和填料 27, 填料 27设置于相邻的换热管的 20之间, 形成间隙耦合, 即通过填料 27填满换热管 261之间的缝隙, 以将所述 盘管 26与填料 27连成一片连续的水流面。关于连接方式, 盘管 26和填料 27之间 可以通过焊接、卡合方式或连接件,将上述的填料 27固定于与盘管 26的换热管 之间。 比如, 连接件为绑绳 F, 在填料 27的边缘打一个或多个固定孔, 用一根 绑绳穿过固定孔, 将其牢固地捆绑在相应的换热管 261上。 如果盘管的换热管 为圆形管或椭圆形管, 还可以选择采用卡合方式, 即将填料的边缘设置成 U型 槽, 以将盘管的换热管稳妥地容置于其中。设置于相邻换热管之间的填料可以 是一片, 也可以是多片。 12-14, the present invention may also provide another type of evaporative condenser having a packing structure, including a coil heat exchanger, a fan 21, a water pump 22, a water distributor 23, a sump 24, and a frame 25; The heat exchanger is composed of a plurality of serpentine coils formed by a plurality of serpentine coils connected by an inlet header 28 and an outlet header 29. Each heat exchange fin includes a longitudinal serpentine (S-shaped) coil 26 and a packing 27, and the packing 27 is disposed in the adjacent heat exchange tube Between 20, a gap coupling is formed, that is, the gap between the heat exchange tubes 261 is filled by the filler 27 to connect the coil 26 and the filler 27 into a continuous water flow surface. Regarding the connection method, the above-mentioned filler 27 can be fixed between the coil 26 and the packing 27 by welding, snapping or connecting means between the heat exchange tubes of the coil 26. For example, the connecting member is a strap F, and one or more fixing holes are formed at the edge of the filler 27, and a strap is passed through the fixing hole to securely bind it to the corresponding heat exchange tube 261. If the heat exchange tube of the coil is a circular tube or an elliptical tube, the snapping mode may also be adopted, that is, the edge of the packing is set as a U-shaped groove to securely accommodate the heat exchange tube of the coil. The packing disposed between the adjacent heat exchange tubes may be one piece or a plurality of pieces.
该实施例中的盘管还可以采 ^其它结构,比如如图 15所示的换热管片中, 盘管 26的换热管 261的直管段相互平行, 其管间距从上层往下层逐渐缩小, 相应地, 换热管 261的弯曲段的曲率半径也逐渐缩小, 填料 27的使用以及与 盘管 26的连接方式, 可参照上述实施例。 使用中, 上层的换热管 261先接受 喷淋冷水, 然后从上至向下流至位于下层的换热管 261 ; 当高温制冷剂从进口 进入而后从出口流出时, 由于上一层的管内制冷剂温度高于下一层的温度, 所 以每经过上一层换热管 261的水温升比经过下一层换热管 261的水温升更高, 故将上一层的填料 27加长, 用于延长填料 27中冷却水的换热时间。该结构的 盘管可降低下层换热管与冷却水的温差,从而提高换热管与冷却水的换热效果 方面, 更胜一筹。 可以选择地, 图 16示出的盘管, 盘管的换热管 261的直管 段具有沿管内液体流动方向的向下坡度, 该管内液体是高温制冷剂。当高温制 冷剂从进口进入后, 该制冷剂的流动是沿着向下坡度的方向, 直至出口流出。 由于换热管 261沿着流动的方向有一定的向下坡度,该盘管更为突出地降低了 制冷剂从进口到出口的压力降。 The coil in this embodiment can also adopt other structures. For example, in the heat exchange fins shown in FIG. 15, the straight pipe sections of the heat exchange tubes 261 of the coil 26 are parallel to each other, and the pipe pitch is gradually reduced from the upper layer to the lower layer. Accordingly, the radius of curvature of the curved portion of the heat exchange tube 261 is also gradually reduced, and the use of the filler 27 and the manner of connection with the coil 26 can be referred to the above embodiment. In use, the upper heat exchange tube 261 first receives the sprayed cold water, and then flows from top to bottom to the lower heat exchange tube 261; when the high temperature refrigerant enters from the inlet and then flows out from the outlet, due to the upper layer of the in-line refrigeration The temperature of the agent is higher than the temperature of the next layer, so that the temperature of the water passing through the upper heat exchange tube 261 rises higher than the temperature of the water passing through the heat exchange tube 261 of the next layer, so that the filler 27 of the upper layer is lengthened. It is used to extend the heat exchange time of the cooling water in the filler 27. The coil of the structure can reduce the temperature difference between the lower heat exchange tube and the cooling water, thereby improving the heat exchange effect between the heat exchange tube and the cooling water, and is superior. Alternatively, the coil shown in Fig. 16, the straight section of the heat exchange tube 261 of the coil has a downward slope along the direction of liquid flow in the tube, and the liquid in the tube is a high temperature refrigerant. When the high temperature refrigerant enters from the inlet, the refrigerant flows in a downward slope direction until the outlet flows out. Since the heat exchange tube 261 has a certain downward slope in the direction of flow, the coil more prominently reduces the pressure drop of the refrigerant from the inlet to the outlet.
为了获得更多的冷却水换热面积, 图 17示出了本发明另一个增加换热填 料的的冷凝器的剖面示意图,所述换热器中的蛇形盘管 26之间、换热器顶部或 换热器底部可设置有一片或多片填料 27'。 In order to obtain more cooling water heat exchange area, FIG. 17 is a schematic cross-sectional view showing another condenser of the present invention for adding a heat exchange filler, between the serpentine coils 26 and the heat exchanger in the heat exchanger. One or more pieces of filler 27' may be provided at the top or at the bottom of the heat exchanger.
图 18、 19示出了蒸发式冷凝器将风机 21放置在换热器前部(进风口)和风 机 21垂直放置。 18 and 19 show that the evaporative condenser places the fan 21 at the front of the heat exchanger (air inlet) and the fan 21 vertically.
图 20示出了蒸发式冷凝器将风机 21垂直放置,冷凝器内设置有 2组换热器。 图 21也示出了具有 2组换热器的蒸发式冷凝器的另一种实现方式。 本实 施例中所采用的换热器的换热管不等长,即盘管的换热管 261的直管段长度从 上一层到下一层逐渐增加, 其中, 上层的换热管 261先接受喷淋冷水, 然后从 上至向下流至位于下层的换热管 261。本实施例所提供的换热管片更适于采用 两组换热器的蒸发式冷凝器。 与图 20中所示实施例不同之处在于: 本实施例 可以在冷凝器外形尺寸不变的情况下,通过改变换热管 261的直管段的长度来 安装更大尺寸和马力的风机。 其中, 实线部分的风机 21为采用了本实施例所 提供的换热管片,虚线部分的风机 21 '为图 20中所示的具有等长直管段的换热 管的换热管片。相比较而言, 前者所使用的风机(实线) 比后者所使用的风机 (虚线) 的尺寸更大, 这样可加大风量, 从而提高换热效果。 Fig. 20 shows that the evaporative condenser places the fan 21 vertically, and two sets of heat exchangers are disposed in the condenser. Figure 21 also shows another implementation of an evaporative condenser having two sets of heat exchangers. The heat exchange tubes of the heat exchanger used in this embodiment are not equal in length, that is, the length of the straight pipe section of the heat exchange tube 261 of the coil is from The upper layer to the next layer is gradually increased, wherein the upper heat exchange tube 261 first receives the spray cold water, and then flows from the top to the bottom to the lower heat exchange tube 261. The heat exchange fins provided in this embodiment are more suitable for evaporative condensers using two sets of heat exchangers. The difference from the embodiment shown in Fig. 20 is that this embodiment can install a fan of a larger size and horsepower by changing the length of the straight pipe section of the heat exchange pipe 261 without changing the outer dimensions of the condenser. The fan 21 of the solid line part is the heat exchange tube piece provided by the embodiment, and the fan 21' of the broken line part is the heat exchange tube piece of the heat exchange tube of the equal length straight pipe section shown in FIG. In comparison, the fan used in the former (solid line) is larger than the fan (dotted line) used in the latter, which increases the air volume and thus improves the heat exchange effect.
值得注意的是, 以上所述仅为本发明的较佳实施例, 并非因此限定本发明 的专利保护范围, 本发明还可以部件进行材料和结构的改进, 或者是采 ^技术 等同物进行替换。 故凡运用本发明的说明书及图示内容所作的等效结构变化, 或直接或间接运用于其他相关技术领域均同理皆包含于本发明所涵盖的范围 内。 It is to be noted that the above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the invention. The invention may also be modified by materials or structures, or replaced by technical equivalents. Therefore, equivalent structural changes made by the description and illustration of the present invention, or directly or indirectly applied to other related technical fields, are included in the scope of the present invention.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210254000.5A CN103574964B (en) | 2012-07-20 | 2012-07-20 | A kind of air-conditioner set that coil pipe evaporative condenser is coupled with filler |
| CN201210254000.5 | 2012-07-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2014012287A1 true WO2014012287A1 (en) | 2014-01-23 |
Family
ID=49517879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2012/080022 Ceased WO2014012287A1 (en) | 2012-07-20 | 2012-08-13 | Air conditioning unit with filler coupling coil pipe evaporative type condenser |
Country Status (3)
| Country | Link |
|---|---|
| CN (1) | CN103574964B (en) |
| HK (1) | HK1181607A2 (en) |
| WO (1) | WO2014012287A1 (en) |
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| CN111059802A (en) * | 2019-12-16 | 2020-04-24 | 珠海格力电器股份有限公司 | A condensing device and an air conditioning system having the same |
| CN111284304A (en) * | 2020-03-27 | 2020-06-16 | 合肥天鹅制冷科技有限公司 | Air conditioning device with condensation and evaporation coupling |
| CN111473547A (en) * | 2019-01-23 | 2020-07-31 | 大金空调(上海)有限公司 | Heat exchanger assembly, evaporative cooling type heat pump unit and control method thereof |
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| CN114136027A (en) * | 2021-12-31 | 2022-03-04 | 深圳市英维克科技股份有限公司 | Evaporative condenser unit |
| CN116951716A (en) * | 2023-05-31 | 2023-10-27 | 苏州恒度环境系统有限公司 | Circulation evaporation type air conditioning system and control method thereof |
| CN119594589A (en) * | 2024-11-22 | 2025-03-11 | 珠海格力电器股份有限公司 | Refrigerating system, low-temperature preservation box, refrigerating control method and device and storage medium |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0719763A (en) * | 1993-07-07 | 1995-01-20 | Mitsubishi Plastics Ind Ltd | Cross flow type closed cooling tower and its operating method |
| CN2443268Y (en) * | 2000-10-07 | 2001-08-15 | 苏宇贵 | Heat pump type water-cooled outdoor set for split-air conditioner |
| CN101021390A (en) * | 2007-03-26 | 2007-08-22 | 上海理工大学 | Heat exchanging module of evaporating cooler used for drenching water mixed intensified cooling |
| CN201210028Y (en) * | 2008-05-19 | 2009-03-18 | 浙江金菱制冷工程有限公司 | Coil unit for reversed flow closed type cooling tower |
| CN201748558U (en) * | 2010-07-14 | 2011-02-16 | 清华大学 | Moisture adjusting device |
| CN201926217U (en) * | 2011-01-15 | 2011-08-10 | 颜汉兴 | An evaporative condenser |
| CN202709537U (en) * | 2012-07-20 | 2013-01-30 | 广州市华德工业有限公司 | Air conditioning unit with packing coupling coil pipe evaporative type condenser |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52100258U (en) * | 1976-01-27 | 1977-07-29 | ||
| US4693302A (en) * | 1984-12-28 | 1987-09-15 | Leonard Oboler | Heat exchanging apparatus for cooling and condensing by evaporation |
| US6883595B2 (en) * | 2002-04-12 | 2005-04-26 | Marley Cooling Technologies, Inc. | Heat exchange method and apparatus |
| KR20040082686A (en) * | 2003-03-20 | 2004-09-30 | 장인성 | heat-exchange plate comprising heat pipe and air cooling type condenser thereby |
| KR100622453B1 (en) * | 2006-05-31 | 2006-09-12 | 서종대 | Evaporative Cooling Heat Exchanger Unit |
| CN201909494U (en) * | 2010-12-06 | 2011-07-27 | 湖北东橙新能源科技有限公司 | Air-cooled type condenser spraying cooling device of central air-conditioning heat pump unit |
-
2012
- 2012-07-20 CN CN201210254000.5A patent/CN103574964B/en active Active
- 2012-08-13 WO PCT/CN2012/080022 patent/WO2014012287A1/en not_active Ceased
-
2013
- 2013-07-16 HK HK13108372.6A patent/HK1181607A2/en not_active IP Right Cessation
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0719763A (en) * | 1993-07-07 | 1995-01-20 | Mitsubishi Plastics Ind Ltd | Cross flow type closed cooling tower and its operating method |
| CN2443268Y (en) * | 2000-10-07 | 2001-08-15 | 苏宇贵 | Heat pump type water-cooled outdoor set for split-air conditioner |
| CN101021390A (en) * | 2007-03-26 | 2007-08-22 | 上海理工大学 | Heat exchanging module of evaporating cooler used for drenching water mixed intensified cooling |
| CN201210028Y (en) * | 2008-05-19 | 2009-03-18 | 浙江金菱制冷工程有限公司 | Coil unit for reversed flow closed type cooling tower |
| CN201748558U (en) * | 2010-07-14 | 2011-02-16 | 清华大学 | Moisture adjusting device |
| CN201926217U (en) * | 2011-01-15 | 2011-08-10 | 颜汉兴 | An evaporative condenser |
| CN202709537U (en) * | 2012-07-20 | 2013-01-30 | 广州市华德工业有限公司 | Air conditioning unit with packing coupling coil pipe evaporative type condenser |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109737528A (en) * | 2018-08-30 | 2019-05-10 | 新疆绿色使者空气环境技术有限公司 | Air conditioning device combining cross-flow multi-temperature evaporative refrigeration chiller and mechanical refrigeration |
| CN111473547A (en) * | 2019-01-23 | 2020-07-31 | 大金空调(上海)有限公司 | Heat exchanger assembly, evaporative cooling type heat pump unit and control method thereof |
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| CN112137538B (en) * | 2019-06-27 | 2024-04-30 | 青岛海尔洗碗机有限公司 | A dishwasher |
| CN111059802A (en) * | 2019-12-16 | 2020-04-24 | 珠海格力电器股份有限公司 | A condensing device and an air conditioning system having the same |
| CN111284304A (en) * | 2020-03-27 | 2020-06-16 | 合肥天鹅制冷科技有限公司 | Air conditioning device with condensation and evaporation coupling |
| CN111284304B (en) * | 2020-03-27 | 2024-05-03 | 合肥天鹅制冷科技有限公司 | Air conditioner with condensation and evaporation coupled together |
| CN113028534A (en) * | 2021-01-08 | 2021-06-25 | 于向阳 | Counterflow external cooling type indirect evaporative cooling air conditioner |
| CN114136027A (en) * | 2021-12-31 | 2022-03-04 | 深圳市英维克科技股份有限公司 | Evaporative condenser unit |
| CN116951716A (en) * | 2023-05-31 | 2023-10-27 | 苏州恒度环境系统有限公司 | Circulation evaporation type air conditioning system and control method thereof |
| CN119594589A (en) * | 2024-11-22 | 2025-03-11 | 珠海格力电器股份有限公司 | Refrigerating system, low-temperature preservation box, refrigerating control method and device and storage medium |
Also Published As
| Publication number | Publication date |
|---|---|
| HK1181607A2 (en) | 2013-11-08 |
| CN103574964B (en) | 2017-10-20 |
| CN103574964A (en) | 2014-02-12 |
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