CN112484180B - Air conditioner - Google Patents

Air conditioner Download PDF

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Publication number
CN112484180B
CN112484180B CN201910860682.6A CN201910860682A CN112484180B CN 112484180 B CN112484180 B CN 112484180B CN 201910860682 A CN201910860682 A CN 201910860682A CN 112484180 B CN112484180 B CN 112484180B
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medium
liquid
energy storage
outlet
heat exchanger
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CN112484180A (en
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大森宏
周宏亮
刘和成
岳宝
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Midea Group Co Ltd
Guangdong Midea White Goods Technology Innovation Center Co Ltd
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Midea Group Co Ltd
Guangdong Midea White Goods Technology Innovation Center Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F5/00Air-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
    • F24F5/0007Air-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
    • F24F5/001Compression cycle type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F13/00Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
    • F24F13/30Arrangement or mounting of heat-exchangers

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Central Heating Systems (AREA)

Abstract

The present invention provides an air conditioner, comprising: a first medium circuit in which a pump is provided, the pump being adapted to driving a flow of a first medium in the first medium circuit; the liquid collector is provided with an inlet and an outlet, the liquid collector is communicated with the first medium loop through the inlet and the outlet, the liquid collector is adapted to carry out gas-liquid separation on the first medium flowing through the liquid collector, and the position of the outlet is higher than the liquid suction port of the pump. The air conditioner that this scheme provided, the liquid trap can carry out gas-liquid separation to the first medium in the first medium return circuit, separates out the bubble in the first medium, reduces the bubble content in the first medium, promotes the heat exchange efficiency of the stability of water pump operation and first medium.

Description

Air conditioner
Technical Field
The invention relates to the field of air conditioners, in particular to an air conditioner.
Background
In the existing air conditioner, a liquid collector is connected in a medium loop of the air conditioner and used for carrying out gas-liquid separation on a medium in the medium loop, however, in the structure, the liquid collector needs to be established under the condition that the medium in the medium loop is in a circulating state when the liquid collector carries out gas-liquid separation, the working efficiency of the liquid collector has limitation, and the use requirement is difficult to meet.
Disclosure of Invention
In order to solve at least one of the above technical problems, an object of the present invention is to provide an air conditioner.
To achieve the above object, an embodiment of the present invention provides an air conditioner including: a first medium circuit in which a pump is provided, the pump being adapted to driving a flow of a first medium in the first medium circuit; a liquid trap having an inlet and an outlet, the liquid trap being in communication with the first medium circuit via the inlet and the outlet, the liquid trap being adapted to perform gas-liquid separation of the first medium flowing therethrough, wherein the outlet is located higher than a liquid suction port of the pump.
In the air conditioner provided by the above embodiment of the invention, the inlet and the outlet of the liquid trap are respectively communicated with the first medium loop, so that the liquid trap is connected into the first medium loop through the inlet and the outlet of the liquid trap, and thus, the liquid trap can perform gas-liquid separation on the first medium in the first medium loop to separate bubbles in the first medium, and reduce the content of bubbles in the first medium, thereby improving the operation stability of the water pump and the heat exchange efficiency of the first medium, and improving the operation energy efficiency of the air conditioner, wherein the outlet of the liquid trap is set higher than the liquid suction port of the pump in the first medium loop, so that the bubbles in the first medium in the pump can automatically float into the liquid trap by using a vapor-liquid density difference under the condition that the first medium in the first medium loop is in a static state or a slow flow state, so that the liquid trap still has a good gas-liquid separation effect under the condition that the first medium in the first medium loop is in a static state or a slow flow state And the functional requirements of the product can be further met.
In addition, the air conditioner in the above embodiment provided by the present invention may further have the following additional technical features:
in the above technical solution, the liquid trap is provided with a filling port adapted for allowing a first medium to enter the liquid trap, and the filling port is communicated with the first medium circuit via the liquid trap, so that the first medium entering along the filling port is injected into the first medium circuit via the liquid trap.
In this scheme, set up the filler on the liquid trap to fill notes first medium in to first medium return circuit for user or assembly personnel via the filler, it is more simple and convenient to use.
In any of the above technical solutions, the filling port is provided at the top of the liquid trap.
In this scheme, set up the filler and be located the top of liquid trap, can reduce the weeping risk nature from the filler like this, and the operation of filling first medium is also more convenient.
In any of the above technical solutions, the liquid trap is provided with a blocking member that blocks the filling port, wherein the blocking member is integrally or partially constructed as an elastic wall.
In the scheme, the sealing piece is arranged to seal the filling opening, so that the first medium loop can be prevented from leaking from the filling opening, wherein the whole or part of the sealing piece is arranged to be the elastic wall, so that the elastic wall can absorb the fluctuation energy in the first medium loop through elastic deformation, and the pressure fluctuation in the first medium loop is avoided, for example, the elastic wall can be used for buffering and offsetting the pressure fluctuation in the first medium loop caused by the start-stop operation of the pump, thereby reducing the pressure fluctuation in the first medium loop and preventing the pressure fluctuation from damaging the components in the first medium loop.
In any one of the above technical solutions, an inner cavity is formed inside the liquid trap, an arc-shaped portion is configured on a side wall of the inner cavity, and the inlet and/or the outlet are/is arranged along a tangential direction of the arc-shaped portion.
In this scheme, at the lateral wall structure arc portion of inner chamber, make at least one of the entry of liquid trap and the export set up along the tangential of arc portion, if make the entry of liquid trap along the tangential setting of arc portion, like this, enter into the surface of the first medium tangential contact arc portion in the inner chamber of liquid trap along the entry, make first medium can form the vortex efficiently under the water conservancy diversion effect of arc portion, play the effect similar "cyclone separator", thereby carry out gas-liquid separation efficiently, reduce the gas content in the first medium, improve the heat conductivity of first medium, strengthen the heat transfer ability of first medium.
If again, the export that makes the liquid trap sets up along the tangential of arc portion, like this, first medium after the arc portion pitch arc water conservancy diversion can be thrown away from the export along the tangential of arc portion under the inertial action, can further strengthen the vortex and form the effect, promote gas-liquid separation efficiency, and design like this also makes the flowing back efficiency of liquid trap higher, can prevent that gas from dissolving into again, further reduces the gas content rate in the first medium, improves the heat conductivity of first medium, strengthens the heat transfer ability of first medium.
In any of the above technical solutions, the position of the outlet is lower than the position of the inlet, or the position of the outlet is flush with the position of the inlet.
In this scheme, the position that sets up the export is less than the position of entry, or with the position parallel and level of entry, can reduce the probability that gas melts into in the liquid again like this, further reduces the gas content in the first medium, improves the heat conductivity of first medium, strengthens the heat transfer ability of first medium.
In any of the above technical solutions, the first medium circuit includes a first heat exchanger and an energy storage device, the first heat exchanger, the energy storage device, the liquid trap and the pump are connected via a pipeline to form a circuit, and the inlet is communicated with the first heat exchanger, and the outlet is communicated with the pump.
In this scheme, set up first heat exchanger and energy storage device and form first medium return circuit via the pipe connection, like this, after first medium absorbed the heat or the cold volume of the continuous deposit in the energy storage device, accessible first heat exchanger releases to realize heating or refrigeration to the environment in the environment, simple structure has, get cold and get the effectual advantage of heat, and through locating liquid trap and pump in the return circuit of first heat exchanger and energy storage device formation via the pipe connection, make liquid trap and pump form a part of this return circuit, and like this, combine the gas-liquid separation effect of liquid trap, more do benefit to and realize getting cold and getting hot high efficiency and the diversification of operational mode, and wherein, the heat or the cold volume of first medium are got from the energy storage device, can realize shifting the peak and filling valley power consumption, realize the optimal utilization of the energy, and the use that produces is also more convenient. The inlet of the liquid collector is connected with the first heat exchanger, the outlet of the liquid collector is connected with the pump, so that the liquid collector is connected in series between the first heat exchanger and the pump, meanwhile, the pump drives the liquid in the first heat exchanger to enter the liquid collector, the liquid is pumped into the energy storage device through the pump after passing through the liquid collector, and returns to the first heat exchanger again after heat exchange with the energy storage material is completed in the energy storage device, so that liquid circulation is completed, wherein the liquid in the liquid collector flows to the pump and further drives the liquid in the energy storage device to flow to the first heat exchanger, so that the gas content of the first medium entering the energy storage device is low, the energy release of the energy storage device is more efficient, the cold or heat release efficiency of the energy storage device is improved, and quick cold or heat supply is realized.
In any of the above technical solutions, the position of the inlet is higher than the position of the medium outlet of the first heat exchanger.
In the scheme, the position of the inlet is higher than the position of the medium outlet of the first heat exchanger, so that bubbles in the first medium in the first heat exchanger can automatically float up to the liquid collector by utilizing the vapor-liquid density difference under the condition that the first medium in the first medium loop is in a static state or in a slow flowing state, the liquid collector still has a good gas-liquid separation effect under the condition that the first medium in the first medium loop is in the static state or in the slow flowing state, and the functional requirements of products can be further met.
In any of the above technical solutions, the energy storage device includes a cavity, a first flow path and an energy storage material, an accommodation space is formed in the cavity, the first flow path and the energy storage material are accommodated in the accommodation space, the first flow path exchanges heat with the energy storage material, and the first flow path and the first heat exchanger are formed in the same loop.
In the scheme, the cavity is arranged to accommodate the first flow path and the energy storage material, so that the energy storage material can efficiently release cold or heat to the first medium through the first flow path, the cold or heat release efficiency of the energy storage device is improved, and rapid cold or heat supply is realized.
In any one of the above technical solutions, a second flow path is provided in the energy storage device, and the air conditioner further includes: and the second medium loop comprises a compressor, a second heat exchanger, a throttling device and the second flow path, and the compressor, the second heat exchanger, the throttling device and the second flow path are connected through pipelines to form a loop.
In this scheme, compressor, second heat exchanger, throttling arrangement and second flow path form the return circuit via the pipe connection, and wherein, the second flow path is located in the energy storage equipment for the cold volume or the heat accessible second medium that refrigerate or heat production in the second medium return circuit release for energy storage material to accumulate high-efficiently via the second flow path, promote energy storage efficiency, and save energy storage consuming time.
Additional aspects and advantages of the invention will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
Drawings
The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:
FIG. 1 is a schematic view showing a partial structure of an air conditioner according to an embodiment of the present invention;
FIG. 2 is a schematic perspective view of a liquid trap according to one embodiment of the present invention;
FIG. 3 is a schematic top view of the accumulator shown in FIG. 2;
FIG. 4 is a schematic side view of the accumulator shown in FIG. 2;
fig. 5 is a schematic diagram of a partial structure of an air conditioner according to an embodiment of the present invention.
Wherein, the correspondence between the reference numbers and the component names in fig. 1 and 5 is:
100 first medium loop, 110 first heat exchanger, 1102 medium inlet, 1101 medium outlet, 111 first fan, 120 energy storage device, 121 cavity, 122 first flow path, 123 energy storage material, 200 pump, 210 liquid suction port, 220 liquid discharge port, 300 liquid trap, 310 inlet, 320 outlet, 330 filling port, 340 blocking piece, 350 inner cavity, 351 arc part, 400 second medium loop, 410 compressor, 420 second heat exchanger, 421 second fan, 430 throttling device, 440 second flow path, 460 four-way valve.
Detailed Description
In order that the above objects, features and advantages of the present invention can be more clearly understood, a more particular description of the invention will be rendered by reference to the appended drawings. It should be noted that the embodiments of the present invention and features of the embodiments may be combined with each other without conflict.
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention, however, the present invention may be practiced in other ways than those specifically described herein, and therefore the scope of the present invention is not limited by the specific embodiments disclosed below.
An air conditioner according to some embodiments of the present invention will be described below with reference to fig. 1 to 5.
As shown in fig. 1, an embodiment of the present invention provides an air conditioner, including: a first medium circuit 100 and a liquid collector 300, in particular, a pump 200 is arranged in the first medium circuit 100, the pump 200 being adapted to drive the flow of the first medium in the first medium circuit 100; the liquid trap 300 has an inlet 310 and an outlet 320, the liquid trap 300 being in communication with the first medium circuit 100 via the inlet 310 and the outlet 320, the liquid trap 300 being adapted to perform gas-liquid separation of the first medium flowing therethrough, wherein the outlet 320 is located higher than the liquid suction port 210 of the pump 200.
It should be noted that the position of the outlet 320 is higher than the liquid suction port 210 of the pump 200, which can be specifically understood in combination with the scene that when the product is placed on a bearing surface such as the ground, a table, etc. for use, the height of the outlet 320 from the bearing surface is higher than the height of the liquid suction port 210 of the pump 200 from the bearing surface in the direction perpendicular to the bearing surface.
And it is understood that the height of the outlet 320 from the bearing surface may be specifically understood as the height of the center of the outlet 320 from the bearing surface, and the height of the liquid suction port 210 of the pump 200 from the bearing surface may be specifically understood as the height of the center of the liquid suction port 210 from the bearing surface; alternatively, the height of the outlet 320 from the bearing surface may be specifically understood as the height of the top end of the outlet 320 from the bearing surface, and the height of the liquid suction port 210 of the pump 200 from the bearing surface may be specifically understood as the height of the top end of the liquid suction port 210 from the bearing surface; alternatively, the height of the outlet 320 from the carrying surface may be specifically understood as the height of the bottom end of the outlet 320 from the carrying surface, and the height of the liquid suction port 210 of the pump 200 from the carrying surface may be specifically understood as the height of the bottom end of the liquid suction port 210 from the carrying surface.
In the air conditioner provided by the above embodiment of the present invention, the inlet 310 and the outlet 320 of the liquid trap 300 are respectively communicated with the first medium circuit 100, so that the liquid trap 300 is connected to the first medium circuit 100 through the inlet 310 and the outlet 320 thereof, and thus, the first medium in the first medium circuit 100 can be subjected to gas-liquid separation by the liquid trap 300 to separate bubbles from the first medium, so as to reduce the content of bubbles in the first medium, thereby improving the stability of the operation of the water pump and the heat exchange efficiency of the first medium, and improving the operation energy efficiency of the air conditioner, wherein the outlet 320 of the liquid trap 300 is arranged higher than the liquid suction port 210 of the pump 200 in the first medium circuit 100, so that the bubbles in the first medium in the pump 200 can be automatically floated into the liquid trap 300 by using a difference in vapor-liquid density when the first medium in the first medium circuit 100 is in a static state or in a slow flow state, the liquid collector 300 still has a good gas-liquid separation effect under the condition that the first medium in the first medium circuit 100 is in a static state or in a slow flow state, and can further meet the functional requirements of products.
Example 1:
as shown in fig. 2, in addition to the features of the above embodiment, the present embodiment further defines: the liquid trap 300 is provided with a fill port 330, the fill port 330 being adapted to allow the first medium to enter the liquid trap 300, wherein the fill port 330 communicates with the first medium circuit 100 via the liquid trap 300, so that the first medium entering along the fill port 330 is injected into the first medium circuit 100 via the liquid trap 300. This may facilitate filling of the first medium into the first medium circuit 100 via the fill port 330 by a user or assembler, which may be simpler and more convenient to use.
Further, as shown in fig. 2 and 3, a fill port 330 is provided at the top of the liquid trap 300. This reduces the risk of leakage from the fill port 330 and makes the operation of filling the first medium more convenient.
Further, as shown in fig. 1, the liquid trap 300 is provided with a stopper 340, and the stopper 340 blocks the filler neck 330. Leakage of the first medium circuit 100 from the fill port 330 can be avoided.
Still further, the blocking piece 340 is constructed wholly or partially as an elastic wall. In this way, the elastic wall elastic deformation can be used to absorb the fluctuation energy in the first medium circuit 100 and avoid the pressure fluctuation in the first medium circuit 100, for example, the elastic wall elastic deformation is used to buffer and cancel the pressure fluctuation in the first medium circuit 100 caused by the start-stop operation of the pump 200, so as to reduce the pressure fluctuation in the first medium circuit 100 and prevent the pressure fluctuation from damaging the components in the first medium circuit 100.
In more detail, as shown in fig. 2 and 3, the liquid trap 300 includes a cylindrical hollow cavity, one axial end of the hollow cavity is a top end, and the other axial end of the hollow cavity is a bottom end, wherein a filling port 330 is formed at the top end of the hollow cavity and is communicated with the inside of the hollow cavity, and the blocking member 340 includes a cover body, and the cover body is screwed, clamped or hooped with the upper portion of the hollow cavity, so that the cover body covers the filling port 330, in a specific embodiment, a top wall of the cover body is disposed opposite to the filling port 330, wherein the cover body is a rubber cover or the top wall of the cover body is a rubber wall, and the top wall of the cover body can be deformed to counteract pressure fluctuation in the first medium circuit 100 caused in part by start-stop operation of the pump 200 in the first medium circuit 100.
Example 2:
as shown in fig. 3, in addition to the features of the above embodiment, the present embodiment further defines: the interior of liquid trap 300 is formed with an inner chamber 350, the sidewall of inner chamber 350 is configured with an arc 351, and at least one of inlet 310 of liquid trap 300 and outlet 320 of liquid trap 300 is disposed tangentially to arc 351.
It is worth noting that at least one of the inlet 310 of the liquid trap 300 and the outlet 320 of the liquid trap 300 is arranged tangentially to the arc 351, it being understood macroscopically that either the inlet 310 or the outlet 320 extends generally tangentially to the arc 351, or macroscopically that either the centerline of the inlet 310 or the centerline of the outlet 320 extends generally tangentially to the arc 351 or generally parallel to the tangent of the arc 351, without strictly requiring that either the inlet 310 or the outlet 320 be absolutely tangential to the arc 351, and in fact, it may be permissible for either the inlet 310 or the outlet 320 to be slightly offset or angled from the tangent of the arc 351.
For example, as shown in fig. 3, the inlet 310 of the liquid trap 300 is arranged along the tangential direction of the arc-shaped portion 351, so that the first medium entering the inner cavity 350 of the liquid trap 300 along the inlet 310 tangentially contacts the surface of the arc-shaped portion 351, so that the first medium can efficiently form a vortex under the flow guiding effect of the arc-shaped portion 351 to play a role similar to a "vortex separator", thereby efficiently performing gas-liquid separation, reducing the gas content in the first medium, improving the heat conductivity of the first medium, and enhancing the heat exchange capability of the first medium.
For another example, as shown in fig. 3, the outlet 320 of the liquid collector 300 is arranged along the tangential direction of the arc-shaped portion 351, so that the first medium after being guided by the arc of the arc-shaped portion 351 can be thrown out from the outlet 320 along the tangential direction of the arc-shaped portion 351 under the action of inertia, the vortex forming effect can be further enhanced, the gas-liquid separation efficiency is improved, the liquid drainage efficiency of the liquid collector 300 is higher due to the design, the gas can be prevented from being dissolved again, the gas content in the first medium is further reduced, the heat conductivity of the first medium is improved, and the heat exchange capacity of the first medium is enhanced.
In more detail, as shown in fig. 3, the liquid trap 300 includes a cylindrical hollow cavity, the inside of the hollow cavity is formed as a cylindrical inner chamber 350, half of the sidewall of the inner chamber 350 is formed as a first semicircular arc wall surface formed as an arc part 351, and the other half of the sidewall of the inner chamber 350 is formed as a second semicircular arc wall surface on which the inlet 310 and the outlet 320 are disposed and are respectively approximately tangent to the first semicircular arc wall surface.
Example 3:
as shown in fig. 4, in addition to the features of the above embodiment, the present embodiment further defines: the outlet 320 of the liquid trap 300 is located lower than the inlet 310 of the liquid trap 300.
It should be noted that, when the product is placed on a supporting surface such as the ground, a table, etc. for use, the central line or center of the outlet 320 is lower than the central line or center of the inlet 310 in a direction perpendicular to the supporting surface.
In more detail, as shown in fig. 4, the distance between the center line of the outlet 320 and the center line of the inlet 310 is h, the value of h is greater than 0mm, and the position of the center line of the inlet 310 is higher than that of the center line of the outlet 320. Therefore, the probability of gas re-melting into liquid can be reduced, the gas content in the first medium is further reduced, the heat conductivity of the first medium is improved, and the heat exchange capacity of the first medium is enhanced.
Of course, the present invention is not limited to this, and in other embodiments, the skilled person may also design the position of the outlet 320 to be flush with the position of the inlet 310, or the position of the center line of the inlet 310 to be at the same level as the position of the center line of the outlet 320, according to the requirement.
Example 4:
as shown in fig. 5, in addition to the features of the above embodiment, the present embodiment further defines: the first medium circuit 100 includes a first heat exchanger 110, an accumulator 120, the first heat exchanger 110, the accumulator 120, an accumulator 300, and a pump 200 are connected via pipes to form a circuit, and wherein an inlet 310 of the accumulator 300 is communicated with the first heat exchanger 110, and an outlet 320 of the accumulator 300 is communicated with the pump 200. Like this, after first medium absorbed the heat or the cold volume of continuous deposit in energy storage device 120, accessible first heat exchanger 110 releases the environment in and realizes heating or refrigeration to the environment, has simple structure, get cold and get hot effectual advantage, and combine the gas-liquid separation effect of liquid trap 300, more do benefit to and realize getting cold and getting hot high efficiency and the diversification of operational mode, and wherein, the heat or the cold volume of first medium are got from energy storage device 120, can realize shifting the peak and fill in the valley power consumption, realize the optimal utilization of the energy, and the use that produces is also more convenient.
And through the design, the first medium loop is formed as follows: the circulating loop of the first heat exchanger 110, the liquid collector 300, the pump 200, the energy storage device 120 and the first heat exchanger 110 is characterized in that the pump 200 drives the liquid in the first heat exchanger 110 to enter the liquid collector 300, the liquid is pumped into the energy storage device 120 through the pump 200 after passing through the liquid collector 300, the liquid returns to the first heat exchanger 110 after heat exchange with energy storage materials is completed in the energy storage device 120, and therefore liquid circulation is completed, wherein the liquid in the liquid collector 300 flows to the pump 200 and further drives the liquid in the energy storage device 120 to flow to the first heat exchanger 110, so that the gas content of the first medium entering the energy storage device 120 is low, the energy release of the energy storage device 120 is more efficient, the cold or heat release efficiency of the energy storage device 120 is improved, and quick cold or heat supply is realized.
Further, it will be appreciated that a heat exchanger, in particular the first heat exchanger 110, will generally have a medium inlet 1102 adapted for the medium to enter the heat exchanger, and a discharge medium outlet 1101 adapted for the medium to exit the heat exchanger, as shown in fig. 1, the inlet 310 of the accumulator 300 being located at a higher level than the medium outlet 1101 of the first heat exchanger 110. In this way, when the first medium in the first medium circuit 100 is in a static state or in a slow flow state, bubbles in the first medium in the first heat exchanger 110 may automatically float up to the liquid trap 300 by using a vapor-liquid density difference, so that the liquid trap 300 still has a good gas-liquid separation effect when the first medium in the first medium circuit 100 is in the static state or in the slow flow state, and the functional requirements of the product can be further satisfied.
It is worth noting that the position of the inlet 310 of the liquid collector 300 is higher than the position of the medium outlet 1101 of the first heat exchanger 110, which can be specifically understood in combination with the scenario that, when the product is placed on a bearing surface such as the ground, a table top, or the like for use, the height of the inlet 310 from the bearing surface is higher than the height of the medium outlet 1101 of the first heat exchanger 110 from the bearing surface in a direction perpendicular to the bearing surface.
And it is to be understood that the height of the inlet 310 from the load-supporting surface may be specifically understood as the height of the center of the inlet 310 from the load-supporting surface, and the height of the medium outlet 1101 of the first heat exchanger 110 from the load-supporting surface may be specifically understood as the height of the center of the medium outlet 1101 of the first heat exchanger 110 from the load-supporting surface; alternatively, the height of the inlet 310 from the load-supporting surface may be specifically understood as the height of the top end of the inlet 310 from the load-supporting surface, and the height of the medium outlet 1101 of the first heat exchanger 110 from the load-supporting surface may be specifically understood as the height of the top end of the medium outlet 1101 of the first heat exchanger 110 from the load-supporting surface; alternatively, the height of the inlet 310 from the bearing surface may be specifically understood as the height of the bottom end of the inlet 310 from the bearing surface, and the height of the medium outlet 1101 of the first heat exchanger 110 from the bearing surface may be specifically understood as the height of the bottom end of the medium outlet 1101 of the first heat exchanger 110 from the bearing surface.
Further, as shown in fig. 1 and 5, the pump 200 is connected to the accumulator 300 and the energy storage means 120, and as shown in fig. 1, the pump 200 sucks liquid from the accumulator 300 and discharges the liquid to the energy storage means 120, so that the first medium is discharged from the accumulator 300 into the energy storage means 120 in the L direction. Thus, the gas content of the first medium entering the energy storage device 120 is low, the energy release of the energy storage device 120 is more efficient, the cold release or heat release efficiency of the energy storage device 120 is improved, and rapid cold supply or heat supply is realized.
More specifically, as shown in fig. 5, the pump 200 has a liquid suction port 210 and a liquid discharge port 220, wherein the liquid suction port 210 communicates with the liquid trap 300, the liquid discharge port 220 communicates with the energy storage means 120, and the pump 200 sucks liquid from the liquid trap 300 and discharges the liquid to the energy storage means 120 when operated. The purpose of driving the first medium is achieved.
Further, as shown in fig. 5, the energy storage device 120 includes a cavity 121, a first flow path 122 and an energy storage material 123, an accommodation space is formed in the cavity 121, the first flow path 122 and the energy storage material 123 are accommodated in the accommodation space, the first flow path 122 exchanges heat with the energy storage material 123, and the first flow path 122 and the first heat exchanger 110 are formed in the same loop. The energy storage material 123 releases cooling or heat to the first medium efficiently through the first flow path 122, so that the cooling or heat release efficiency of the energy storage device 120 is improved, and rapid cooling or heating is realized.
Further, as shown in fig. 5, a second flow path 440 is provided in the energy storage device 120, the air conditioner further includes a second medium circuit 400, the second medium circuit 400 includes a compressor 410, a second heat exchanger 420, a throttling device 430, and a second flow path 440, and the compressor 410, the second heat exchanger 420, the throttling device 430, and the second flow path 440 are connected via a pipeline to form a circuit. The second flow path 440 is disposed in the energy storage device 120, so that the cold or heat generated by cooling or heating in the second medium circuit 400 can be efficiently released to the energy storage material 123 through the second flow path 440 for storage, thereby improving the energy storage efficiency and saving the energy storage time.
In more detail, the second flow path 440 is located in the accommodating space of the cavity 121 of the energy storage device 120 and is in heat transfer engagement with the energy storage material 123. Further, the first flow path 122 and the second flow path 440 are immersed in the energy storage material 123 and contact the energy storage material 123 to exchange heat.
Furthermore, cavity 121 is the bilayer structure including shell and inner bag, and the inner bag closes encloses accommodation space, and the shell forms the inner bag outside in order to protect the inner bag, is equipped with the strengthening rib on the shell and strengthens.
The first heat exchanger 110 is disposed on the upper side of the casing, the casing supports the first heat exchanger 110, the pump 200 is disposed on the upper side of the casing, the pump 200 is supported by the casing, the liquid trap 300 is disposed on the first heat exchanger 110 or on the side of the first heat exchanger 110, the outlet 320 of the liquid trap 300 is positioned higher than the liquid suction port 210 of the pump 200, and the inlet 310 is positioned higher than the medium outlet 1101 of the first heat exchanger 110.
The specific embodiment is as follows:
the air conditioner may be a mobile air conditioner, and of course, the air conditioner may also be an integrated window air conditioner or a split air conditioner, wherein the air conditioner includes components such as an energy storage device 120, a first heat exchanger 110, a first fan 111, a second heat exchanger 420, a second fan 421, a compressor 410, a first flow path 122, a second flow path 440, a liquid trap 300, a throttling device 430, and a pump 200.
In more detail, as shown in fig. 5, the air conditioner is formed with an air conditioning system, and the air conditioning system includes a first medium circuit 100 and a second medium circuit 400, wherein the air conditioner is provided with an energy storage device 120, and one or more heat exchangers are arranged in a cavity 121 of the energy storage device 120, for example, one heat exchanger is arranged in the energy storage device 120 and includes a first flow path 122 and a second flow path 440, or, for example, as shown in fig. 5, a plurality of heat exchangers are arranged in the energy storage device 120, specifically, two heat exchangers are arranged in the energy storage device 120, one of the two heat exchangers has the first flow path 122, and the other has the second flow path 440. The energy storage material 123 is disposed in the energy storage device 120, and the energy storage material 123 is configured to exchange heat with a heat exchanger (specifically, the first flow path 122 and the second flow path 440) in the energy storage device 120 and store heat (cold) released by the heat exchanger.
The first medium circuit 100 includes a first heat exchanger 110 and a first flow path 122, and the first heat exchanger 110 and the first flow path 122 are connected in series via a pipe to form a circuit.
The second medium circuit 400 includes a compressor 410, a second heat exchanger 420, a throttling device 430, and a second flow path 440, and the compressor 410, the second heat exchanger 420, the throttling device 430, and the second flow path 440 are connected in series via piping to form a circuit.
A first medium flows through the first medium circuit 100, a second medium flows through the second medium circuit 400, and the first medium and the second medium may be the same medium or different media.
Further, a pump 200 is provided in the first medium circuit 100 for driving the first medium to flow.
Further, the first heat exchanger 110 is provided with a first fan 111 for driving the air flow to exchange heat therewith. The second heat exchanger 420 is provided with a second fan 421 for driving the air flow to exchange heat therewith.
For example, the first medium is water or other coolant.
For example, the second medium is a refrigerant.
For example, the energy storage material is water.
When the cold storage mode is operated, in the second medium loop 400, a second medium enters the compressor 410, after the compressor 410 compresses the second medium, the second medium is sent to the second heat exchanger 420, the second medium exchanges heat with the environment through the second heat exchanger 420 in the second heat exchanger 420 to realize condensation, the condensed second medium enters the throttling device 430 to be throttled, then the throttled second medium enters the second flow path 440 of the energy storage device 120 to be evaporated, wherein cold energy released by evaporation is stored in the energy storage material 123, and finally, the evaporated second medium returns to the compressor 410 to realize circulation.
In the cooling mode, in the first medium circuit 100, the first medium releases heat to the energy storage material 123 in the first flow path 122 of the energy storage device 120, the first medium after heat release enters the first heat exchanger 110, and absorbs heat of the environment through the first heat exchanger 110 in the first heat exchanger 110, so that cooling of the environment is realized, and the first medium after heat absorption returns to the first flow path 122 of the energy storage device 120 again to release heat, thereby completing a cycle.
On the contrary, when the heat storage mode is operated, in the second medium circuit 400, the second medium discharged from the compressor 410 enters the second flow path 440 of the energy storage device 120, so that the second medium releases heat to the energy storage material 123 through the second flow path 440, so that the energy storage material 123 absorbs heat and stores the heat, accordingly, the second medium is condensed through heat release, the condensed second medium enters the throttling device 430 for throttling treatment, then, the throttled second medium enters the second heat exchanger 420 for evaporation, wherein the cold released by evaporation is released to the environment, and finally, the evaporated second medium returns to the compressor 410 to realize circulation.
In the heating mode, in the first medium circuit 100, the first medium absorbs heat from the energy storage material 123 in the first flow path 122 of the energy storage device 120, the first medium after absorbing heat enters the first heat exchanger 110, and releases heat to the environment through the first heat exchanger 110 in the first heat exchanger 110, so that heat is supplied to the environment, and the first medium after releasing heat returns to the first flow path 122 of the energy storage device 120 again to absorb heat, thereby completing the cycle.
For example, as shown in fig. 3, a four-way valve 460 is provided in the second medium circuit 400, and the cold storage mode and the heat storage mode can be switched by the four-way valve 460. Of course, the air conditioning system may not be provided with the four-way valve 460 according to the specific demand.
Here, by providing the liquid trap 300 in the first medium circuit 100 and positioning the outlet 320 of the liquid trap 300 higher than the liquid suction port 210 of the pump 200, bubbles in the first medium circuit 100 can rise along the pipe of the first medium circuit 100 due to a gas-liquid density difference when the first medium circuit 100 stops standing, and thus are collected in the liquid trap 300.
The accumulator 300 is provided with an inlet 310, an outlet 320 and a fill port 330. The fill port 330 can facilitate filling of the first medium into the first medium circuit 100. The fill port 330 is sealed with a rubber cap, the top of which can deform to counteract pressure fluctuations in the first medium circuit 100 caused in part by the start and stop operation of the pump 200 of the first medium circuit 100.
The inlet 310 and the outlet 320 of the liquid collector 300 are tangent to the wall surface of the liquid collector 300, and a vortex is formed in the liquid collector 300 in the circulation process of the first medium, so that the function similar to that of a vortex separator is achieved, bubbles contained in the first medium are separated, the gas content in the first medium is reduced, the heat conductivity of the first medium is improved, and the heat exchange capacity of the first medium is enhanced.
The position of the pump 200 in the first medium circuit 100 is located above the energy storage device 120, below the outlet 320 of the liquid trap 300, the first medium in the liquid trap 300 is pumped into the first flow path 122 of the energy storage device 120 through the pump 200 to exchange heat with the energy storage material, the first medium with a lower temperature directly enters the first heat exchanger 110 to exchange heat with the external environment after coming out of the first flow path 122 of the energy storage device 120, and the first medium with a higher temperature after absorbing heat flows into the liquid trap 300. It is worth mentioning that the first medium cannot pass through the pump 200 after entering the energy storage device 120 for cooling, so as to prevent the cryogenic fluid from passing through the pump 200 and causing the problem of surface condensation of the pump 200.
In the present invention, the terms "first", "second", and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance; the term "plurality" means two or more unless expressly limited otherwise. The terms "mounted," "connected," "fixed," and the like are to be construed broadly, and for example, "connected" may be a fixed connection, a removable connection, or an integral connection; "coupled" may be direct or indirect through an intermediary. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "left", "right", "front", "rear", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the referred device or unit must have a specific direction, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention.
In the description herein, the description of the terms "one embodiment," "some embodiments," "specific embodiments," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (8)

1. An air conditioner, comprising:
a first medium circuit in which a pump is provided, the pump being adapted to driving a flow of a first medium in the first medium circuit;
a liquid trap having an inlet and an outlet, the liquid trap being in communication with the first medium circuit via the inlet and the outlet, the liquid trap being adapted to perform gas-liquid separation of the first medium flowing therethrough, wherein the outlet is located higher than a liquid suction port of the pump;
the first medium loop comprises a first heat exchanger and an energy storage device, the first heat exchanger, the energy storage device, the liquid collector and the pump are connected through pipelines to form a loop, the inlet is communicated with the first heat exchanger, and the outlet is communicated with the pump;
the outlet is located lower than the inlet or is located flush with the inlet.
2. The air conditioner according to claim 1,
the liquid trap is provided with a filling port suitable for allowing a first medium to enter the liquid trap, and the filling port is communicated with the first medium circuit through the liquid trap, so that the first medium entering along the filling port is injected into the first medium circuit through the liquid trap.
3. The air conditioner according to claim 2,
the top of the liquid collector is provided with the filling port.
4. The air conditioner according to claim 2 or 3,
the liquid trap is provided with a sealing piece which seals and blocks the filling opening, wherein the whole or part of the sealing piece is an elastic wall.
5. The air conditioner according to any one of claims 1 to 3,
an inner cavity is formed inside the liquid collector, an arc-shaped part is formed on the side wall of the inner cavity, and the inlet and/or the outlet are/is arranged along the tangential direction of the arc-shaped part.
6. The air conditioner according to any one of claims 1 to 3,
the inlet is located at a higher position than the medium outlet of the first heat exchanger.
7. The air conditioner according to any one of claims 1 to 3,
the energy storage device comprises a cavity, a first flow path and an energy storage material, wherein an accommodating space is formed in the cavity, the first flow path and the energy storage material are accommodated in the accommodating space, the first flow path exchanges heat with the energy storage material, and the first flow path and the first heat exchanger are formed in the same loop.
8. The air conditioner according to any one of claims 1 to 3, wherein a second flow path is provided in the energy storage device, the air conditioner further comprising:
and the second medium loop comprises a compressor, a second heat exchanger, a throttling device and the second flow path, and the compressor, the second heat exchanger, the throttling device and the second flow path are connected through pipelines to form a loop.
CN201910860682.6A 2019-09-11 2019-09-11 Air conditioner Active CN112484180B (en)

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