CN205227953U - Vapour and liquid separator and have its refrigerating cycle device, refrigerating system - Google Patents
Vapour and liquid separator and have its refrigerating cycle device, refrigerating system Download PDFInfo
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- CN205227953U CN205227953U CN201521041849.XU CN201521041849U CN205227953U CN 205227953 U CN205227953 U CN 205227953U CN 201521041849 U CN201521041849 U CN 201521041849U CN 205227953 U CN205227953 U CN 205227953U
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Abstract
The utility model discloses a vapour and liquid separator and have its refrigerating cycle device, refrigerating system. Vapour and liquid separator includes: barrel, low -pressure admission pipe, low pressure outlet duct and be suitable for the high -pressure pipeline of circulation refrigerant prescribe a limit to a separated space in the barrel. The one end of low -pressure admission pipe stretches into in order to emit into the refrigerant of treating gas -liquid separation in the separated space. The low pressure outlet duct stretches into in the separated space with the gaseous state refrigerant in the discharge separated space, and being located of low pressure outlet duct is equipped with the oil return opening in the part of separated space lower part. The high -voltage tube way has the heat transfer pipeline part that lies in separated space and carry out the heat transfer with the refrigerant with separated space, and heat transfer pipeline part feeds through with two mainstream ways respectively including two mainstream ways and a plurality of minutes flow paths, every both ends of dividing the flow path, and the tip on two mainstream ways do not stretches out the barrel and imports and exports in order to prescribe a limit to first exit and second. According to the utility model discloses a vapour and liquid separator has played subcooler, regenerator and gas -liquid separation's effect simultaneously.
Description
Technical field
The utility model relates to refrigerating field, especially relates to a kind of gas-liquid separator and has its freezing cycle device, refrigeration system.
Background technology
Existing air-conditioning vapour liquid separator is for realizing vapor-liquid separation, and mainly the unnecessary oil in compressor and refrigerant are stored, appropriate gaseous coolant and lubricating oil enter compressor and compresses.Under extreme operating condition, due to reasons such as temperature are low, the easy absorbing gas belt liquid of compressor, makes compressor occur the phenomenon of liquid hammer, causes the Performance And Reliability of compressor to reduce.And the fluid in vapour liquid separator comes from evaporimeter, the temperature of these fluids is lower, part cold cannot be utilized, cause waste.
Utility model content
The utility model is intended to solve one of technical problem in correlation technique at least to a certain extent.
For this reason, the utility model proposes a kind of gas-liquid separator, serve the effect of subcooler, regenerator and gas-liquid separation simultaneously.
The utility model also proposes a kind of freezing cycle device with above-mentioned gas-liquid separator.
The utility model also proposes a kind of refrigeration system with above-mentioned gas-liquid separator.
According to the gas-liquid separator of the utility model embodiment, comprising: cylindrical shell, in described cylindrical shell, limit separated space; Low-pressure inlet pipe, one end of described low-pressure inlet pipe extend in described separated space to enter the refrigerant treating gas-liquid separation; Low pressure escape pipe, described low pressure escape pipe extend into discharge the gaseous coolant in described separated space in described separated space, and the part being positioned at described separated space bottom of described low pressure escape pipe is provided with oil return opening; Be suitable for the pressure piping of circulation refrigerant, described pressure piping has and is positioned at described separated space to carry out the heat exchange pipeline part of heat exchange with the refrigerant of described separated space, described heat exchange pipeline part comprises two primary flow path and multiple points of streams, the two ends of each described point stream are communicated with described two primary flow path respectively, and the end of described two primary flow path is stretched out described cylindrical shell respectively and imported and exported to limit the first import and export and second.
According to the gas-liquid separator of the utility model embodiment, by being provided with pressure piping, refrigerant in pressure piping and the refrigerant in separated space carry out heat exchange, thus make gas-liquid separator serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of freezing cycle device, thus improve the refrigerating efficiency of compressor, improve the COP of freezing cycle device.
In embodiments more of the present utility model, in described low-pressure inlet pipe, be provided with bolster.
Particularly, a part of tube wall of described low-pressure inlet pipe bends inwards to limit described bolster after being separated with all the other tube walls.
In embodiments more of the present utility model, described low pressure escape pipe be positioned at described separated space and the part of the outlet side of contiguous described low pressure escape pipe is provided with return-air hole.
Alternatively, described pressure piping also comprises two current dividers, each described current divider has total head piece and multiple subflow mouth, and described two primary flow path are connected with described total head piece of described two current dividers respectively, and described multiple points of streams are connected with the subflow mouth of described two current dividers respectively.
In embodiments more of the present utility model, gas-liquid separator also comprises filter, and described filter is located at described oil return opening place.
In embodiments more of the present utility model, in described heat exchange pipeline part, overcoat has heat exchange fin.
In embodiments more of the present utility model, the bottom of described low-pressure inlet pipe extends downward beyond the inlet end of described low pressure escape pipe.
In embodiments more of the present utility model, the line of centres of the outlet side of described low pressure escape pipe and the inlet end of described low pressure escape pipe and, angle between the outlet side of described low pressure escape pipe and the line of centres of described low-pressure inlet pipe is A, described A > 0.
According to the freezing cycle device of the utility model embodiment, comprising: compressor, described compressor has exhaust outlet and gas returning port; Commutation assembly, described commutation assembly comprises the first valve port to the 4th valve port, described first valve port is communicated with one of them in the 3rd valve port with the second valve port, and described 4th valve port and described second valve port are communicated with another in described 3rd valve port, and described first valve port is connected with described exhaust outlet; Outdoor heat exchanger and indoor heat exchanger, the two ends of described outdoor heat exchanger are connected with the first end of first throttle device with described second valve port respectively, and the first end of described indoor heat exchanger is connected with described 3rd valve port; According to the gas-liquid separator of the utility model above-described embodiment, described first of described pressure piping is imported and exported and is connected with the second end of described first throttle device, described second of described pressure piping is imported and exported and is connected with the second end of described indoor heat exchanger, the upper end of described low-pressure inlet pipe is connected with described 4th valve port, and the outlet side of described low pressure escape pipe is connected with described gas returning port.
According to the freezing cycle device of the utility model embodiment, by being provided with gas-liquid separator, refrigerant in pressure piping and the refrigerant in separated space carry out heat exchange, thus make gas-liquid separator serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of freezing cycle device, thus improve the refrigerating efficiency of compressor, improve the COP of freezing cycle device.
Further, freezing cycle device also comprises auxiliary stream, and described auxiliary stream is connected with the outlet side of described pressure piping with described low pressure escape pipe respectively, and described auxiliary stream is in series with the second throttling arrangement and control valve.
According to the refrigeration system of the utility model embodiment, comprising: compressor, described compressor has exhaust outlet and gas returning port; Outdoor heat exchanger, the two ends of described outdoor heat exchanger are connected with the first end of described exhaust outlet with first throttle device respectively; Indoor heat exchanger and the gas-liquid separator according to the utility model above-described embodiment, described first of described pressure piping is imported and exported and is connected with the second end of described first throttle device, described second of described pressure piping is imported and exported and is connected with the first end of described indoor heat exchanger, the upper end of described low-pressure inlet pipe is connected with the second end of described indoor heat exchanger, and the outlet side of described low pressure escape pipe is connected with described gas returning port.
According to the refrigeration system of the utility model embodiment, by being provided with gas-liquid separator, refrigerant in pressure piping and the refrigerant in separated space carry out heat exchange, thus make gas-liquid separator serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of refrigeration system, thus improve the refrigerating efficiency of compressor, improve the COP of refrigeration system.
Further, refrigeration system also comprises auxiliary stream, and described auxiliary stream is connected with the outlet side of described pressure piping with described low pressure escape pipe respectively, and described auxiliary stream is in series with the second throttling arrangement and control valve.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the gas-liquid separator according to the utility model embodiment;
Fig. 2 is the schematic diagram of the gas-liquid separator according to another embodiment of the utility model;
Fig. 3 is the profile of an angle of gas-liquid separator according to the utility model embodiment;
Fig. 4 is the cooperation schematic diagram according to the pressure piping in the gas-liquid separator of the utility model embodiment and cylindrical shell;
Fig. 5 is the cooperation schematic diagram according to the pressure piping in the gas-liquid separator of another embodiment of the utility model and cylindrical shell;
Fig. 6 is the top view of the gas-liquid separator according to the utility model embodiment;
Fig. 7 is the schematic diagram of the low-pressure inlet pipe according to the utility model embodiment;
Fig. 8 is the sectional view of the low-pressure inlet pipe shown in Fig. 7;
Fig. 9 is the profile of the low pressure escape pipe according to the utility model embodiment;
Figure 10 is the schematic diagram of the freezing cycle device according to the utility model embodiment;
Figure 11 is the schematic diagram of the refrigeration system according to the utility model embodiment.
Reference numeral:
Gas-liquid separator 100,
Cylindrical shell 1, separated space 10,
Low-pressure inlet pipe 2, bolster 20, liquid outlet 21,
Low pressure escape pipe 3, oil return opening 30, return-air hole 31, inlet end 32, outlet side 33,
Pressure piping 4, heat exchange pipeline part 40, second are imported and exported and 41, first are imported and exported 42, primary flow path 401, point stream 402, current divider 43,
Filter 5,
Heat exchange fin 6, support 7,
Freezing cycle device 1000, refrigeration system 2000, compressor 200, exhaust outlet a, gas returning port b, commutation assembly 300, first valve port c, the second valve port d, the 3rd valve port e, the 4th valve port f, outdoor heat exchanger 400, indoor heat exchanger 500, first throttle device 600, second throttling arrangement 700, control valve 800, auxiliary stream 900.
Detailed description of the invention
Be described below in detail embodiment of the present utility model, the example of described embodiment is shown in the drawings.Be exemplary below by the embodiment be described with reference to the drawings, be intended to for explaining the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, it will be appreciated that, term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end " " interior ", " outward ", " clockwise ", " counterclockwise ", " axis ", " radial direction ", orientation or the position relationship of the instruction such as " circumference " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.
In addition, term " first ", " second " only for describing object, and can not be interpreted as instruction or hint relative importance or imply the quantity indicating indicated technical characteristic.Thus, be limited with " first ", the feature of " second " can express or impliedly comprise at least one this feature.In description of the present utility model, the implication of " multiple " is at least two, such as two, three etc., unless otherwise expressly limited specifically.
In the utility model, unless otherwise clearly defined and limited, the term such as term " installation ", " being connected ", " connection ", " fixing " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or integral; Can be mechanical connection, also can be electrical connection or each other can communication; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals or the interaction relationship of two elements, unless otherwise clear and definite restriction.For the ordinary skill in the art, the concrete meaning of above-mentioned term in the utility model can be understood as the case may be.
The gas-liquid separator 100 according to the utility model embodiment is described in detail below with reference to Fig. 1-Figure 10, gas-liquid separator 100 can be applied in freezing cycle device 1000 or refrigeration system 2000, freezing cycle device 1000 has refrigeration mode and heating mode, and refrigeration system 2000 has refrigeration mode.For the ease of being described the operation principle of gas-liquid separator 100, in the following description gas-liquid separator 100 is attached in freezing cycle device 1000 as example is described.
Freezing cycle device 1000 comprises compressor 200, outdoor heat exchanger 400, indoor heat exchanger 500, element such as commutation assembly 300 and first throttle device 600 etc., compressor 200 has exhaust outlet a and gas returning port b, commutation assembly 300 has the first valve port c to the 4th valve port f, first valve port c is connected with exhaust outlet a, second valve port d is connected with the first end of outdoor heat exchanger 400,3rd valve port e is connected with the first end of indoor heat exchanger 500, and the second end of outdoor heat exchanger 400 is connected with the first end of first throttle device 600.When freezing cycle device 1000 freezes, the first valve port c is communicated with the second valve port d and the 3rd valve port e is communicated with the 4th valve port f.When freezing cycle device 1000 heats, the first valve port c is communicated with the 3rd valve port e and the second valve port d is communicated with the 4th valve port f.
As Figure 1-Figure 4, according to the gas-liquid separator 100 of the utility model embodiment, comprising: cylindrical shell 1, low-pressure inlet pipe 2, low pressure escape pipe 3 and be suitable for the pressure piping 4 of refrigerant of circulating.Wherein, separated space 10 is limited in cylindrical shell 1, one end of low-pressure inlet pipe 2 extend in separated space 10 to enter the refrigerant treating gas-liquid separation, refrigerant is drained in separated space 10 from low-pressure inlet pipe 2, and the refrigerant be drained in separated space 10 carries out gas-liquid separation to isolate gaseous coolant and liquid refrigerants.In the example of Fig. 1-Fig. 3, Fig. 6, low-pressure inlet pipe 2 extend into downwards in separated space 10 from the top of cylindrical shell 1, but is understandable that, low-pressure inlet pipe 2 from the sidewall slope of cylindrical shell 1 or flatly can also extend in separated space 10.
Low pressure escape pipe 3 extend into discharge the gaseous coolant in separated space 10 in separated space 10, and the part being positioned at separated space 10 bottom of low pressure escape pipe 3 is provided with oil return opening 30.That is, low pressure escape pipe 3 has inlet end 32 and outlet side 33, and the inlet end 32 of low pressure escape pipe 3 is positioned at separated space 10, and the outlet side 33 of low pressure escape pipe 3 is positioned at outside cylindrical shell 1, and a part for low pressure escape pipe 3 is positioned at the bottom of separated space 10.Because gaseous coolant is generally positioned at the top of separated space 10, therefore the inlet end 32 of low pressure escape pipe 3 is preferably placed at the top of separated space 10.
Pressure piping 4 has and is positioned at separated space 10 to carry out the heat exchange pipeline part 40 of heat exchange with the refrigerant of separated space 10, heat exchange pipeline part 40 comprises two primary flow path 401 and multiple points of streams 402, the two ends of each point of stream 402 are communicated with two primary flow path 401 respectively, and the end of two primary flow path 401 is stretched out cylindrical shell 1 respectively and imported and exported 41 to limit the first import and export 42 and second.In other words, pressure piping 4 first extend in separated space 10 from cylindrical shell 1, and pressure piping 4 stretches out cylindrical shell 1 more afterwards, and entering into refrigerant in pressure piping 4 with pressure piping 4 is that refrigerant in flow path and separated space 10 carries out heat exchange.The refrigerant flowing to pressure piping 4 is introduced in one of them primary flow path 401, and refrigerant enters into multiple points of streams 402 afterwards, and the refrigerant then in multiple points of streams 402 discharges cylindrical shell 1 after convergeing to another primary flow path 401 again.Thus by making heat exchange pipeline part 40 comprise two primary flow path 401 and multiple points of streams 402, the heat exchange area of heat exchange pipeline part 40 can be increased, improve heat transfer effect.
Be understandable that, can select the quantity of point stream 402 according to actual conditions, shape and the circulation of multiple points of streams 402 can be the same or different.The shape of each point of stream 402 does not do concrete restriction, and such as each point of stream 402 can be formed as " U " shape substantially, or each point of stream 402 can comprise the bending bend extended.
Particularly, connector can be provided with to be fixed location to low pressure escape pipe 3 and pressure piping 4 in cylindrical shell 1, local welding can be carried out between low pressure escape pipe 3 and pressure piping 4 both to be fixed.More specifically, the caliber of the primary flow path 401 of pressure piping 4 can be less than the caliber of low pressure escape pipe 3, and the caliber of the primary flow path 401 of pressure piping 4 can be less than the caliber of low-pressure inlet pipe 2.
It should be noted that, " high pressure " and " low pressure " in description of the present utility model is comparatively speaking, only represent that the pressure of the refrigerant entered in pressure piping 4 is greater than the pressure of the refrigerant in low-pressure inlet pipe 2 and low pressure escape pipe 3, and do not represent concrete force value.
When gas-liquid separator 100 is applied to freezing cycle device 1000, as shown in Figure 9, first of pressure piping 4 is imported and exported 42 and is connected with the second end of first throttle device 600, second of pressure piping 4 is imported and exported 41 and is connected with the second end of indoor heat exchanger 500, low-pressure inlet pipe 2 is connected with the 4th valve port f, and low pressure escape pipe 3 is connected with gas returning port b.
During freezing cycle device 1000 refrigerating operaton, the refrigerant of the HTHP of discharging from the exhaust outlet a of compressor 200 is through outdoor heat exchanger 400 condensation, the refrigerant that heat exchanger 400 is discharged outdoor enters into reducing pressure by regulating flow in first throttle device 600, the refrigerant flowed out from first throttle device 600 flow in pressure piping 4, refrigerant in pressure piping 4 and the interior refrigerant stored of separated space 10 carry out heat exchange, refrigerant in pressure piping 4 is cooled further, improve the degree of superheat of the refrigerant stored in separated space 10, the refrigerant of the storage in gas-liquid separator 100 is by heating and gasifying.Refrigerant in pressure piping 4 after heat exchange is discharged to indoor heat exchanger 500 from the second import and export 41 and carries out heat exchange, the refrigerant of heat exchanger 500 discharge is discharged to the 3rd valve port e indoor, the refrigerant of discharging from the 4th valve port f is afterwards drained in separated space 10 by low-pressure inlet pipe 2, the refrigerant be drained in separated space 10 carries out gas-liquid separation, liquid refrigerants is stored in separated space 10, and gaseous coolant is discharged to gas returning port b to get back in compressor 200 from low pressure escape pipe 3.
During freezing cycle device 1000 heating operation, the refrigerant of discharging from the exhaust outlet a of compressor 200 is drained into indoor heat exchanger 500 and carries out condensation, the refrigerant that heat exchanger 500 is discharged indoor is imported and exported 41 by second and is entered in pressure piping 4, refrigerant in pressure piping 4 and the interior refrigerant stored of separated space 10 carry out heat exchange, refrigerant in pressure piping 4 is cooled further, be drained in outdoor heat exchanger 400 after the reducing pressure by regulating flow of first throttle device 600 from the refrigerant of pressure piping 4 discharge and carry out evaporation and heat-exchange, the refrigerant of heat exchanger 400 discharge is outdoor discharged to the second valve port d, the refrigerant of discharging from the 4th valve port f is afterwards drained in separated space 10 by low-pressure inlet pipe 2, the refrigerant be drained in separated space 10 carries out gas-liquid separation, liquid refrigerants is stored in separated space 10, gaseous coolant is discharged to gas returning port b to get back in compressor 200 from low pressure escape pipe 3.
No matter freezing cycle device 1000 freezes or heats, because refrigerant can carry a part of lubricating oil in the process of freezing cycle device 1000 Inner eycle, therefore be mixed with lubricating oil in the liquid refrigerants in separated space 10, the lubricating oil in separated space 10 can enter in low pressure escape pipe 3 and by gaseous coolant through oil return opening 30 and be carried to gas returning port b to get back in compressor 200.
It can thus be appreciated that, no matter freezing cycle device 1000 freezes or heats, refrigerant in pressure piping 4 all carries out heat exchange with the interior refrigerant stored of separated space 10, improve the degree of superheat of the refrigerant stored in separated space 10, make the refrigerant stored in separated space 10 by heating and gasifying, and then improve the mass dryness fraction of the refrigerant entering into compressor 200, effectively reduce the liquid hammer risk that compressor 200 absorbing gas belt liquid causes, therefore, for the refrigerant stored in gas-liquid separator 100
Gas-liquid separator 100 serves the function of regenerator, adds the degree of superheat of freezing cycle device 1000.
Refrigerant is further cooled in pressure piping 4, after improve the degree of supercooling of refrigerant, then enters into next element and carries out heat exchange.Therefore, for the refrigerant that outdoor heat exchanger 400 or indoor heat exchanger 500 are discharged, gas-liquid separator 100 serves the effect of subcooler, adds the degree of supercooling of freezing cycle device 1000.
Known in sum, gas-liquid separator 100 serves the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of freezing cycle device 1000, thus improve the refrigerating efficiency of compressor 200, improve the COP (CoefficientofPerformance of freezing cycle device 1000, heating energy efficiency ratio, the conversion ratio namely between energy and heat).
According to the gas-liquid separator 100 of the utility model embodiment, by being provided with pressure piping 4, refrigerant in refrigerant in pressure piping 4 and separated space 10 carries out heat exchange, thus make gas-liquid separator 100 serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of freezing cycle device 1000, thus improve the refrigerating efficiency of compressor 200, improve the COP of freezing cycle device 1000.
In further embodiment of the present utility model, as shown in Figure 2, in heat exchange pipeline part 40, overcoat has heat exchange fin 6.Thus heat exchange fin 6 can increase the heat exchange area of heat exchange pipeline part 40, the refrigerant in raising heat exchange pipeline part 40 and the heat exchange efficiency between the interior refrigerant stored of separated space 10, improve heat transfer effect.Particularly, heat exchange fin 6 can be multiple, is enclosed within heat exchange pipeline part 40 outside each heat exchange fin 6, can adopt and be fixed in any way between heat exchange fin 6 and heat exchange pipeline part 40.
The gas-liquid separator 100 according to the utility model specific embodiment is described in detail below with reference to Fig. 1, Fig. 3-Fig. 9.
As shown in Figure 1, comprise cylindrical shell 1, low-pressure inlet pipe 2, low pressure escape pipe 3 according to the gas-liquid separator 100 of the utility model embodiment and be suitable for the pressure piping 4 of refrigerant of circulating.Separated space 10 is limited in cylindrical shell 1.
The lower end of low-pressure inlet pipe 2 extend in separated space 10, and the upper end of low-pressure inlet pipe 2 is positioned at outside cylindrical shell 1.In order to avoid flinging the bottom of cylindrical shell 1 from low-pressure inlet pipe 2 refrigerant be drained in cylindrical shell 1, bolster 20 is provided with in low-pressure inlet pipe 2, bolster 20 can play the effect of the flow velocity of buffering refrigerant, and the refrigerant entered in low-pressure inlet pipe 2 enters in cylindrical shell 1 after the buffering of bolster 20.
As Fig. 3, shown in Fig. 7 and Fig. 8, bolster 20 is positioned at cylindrical shell 1, bend inwards to limit bolster 20 after a part of tube wall of low-pressure inlet pipe 2 is separated with all the other tube walls, that is, bolster 20 is bent inwards by a part of tube wall of low-pressure inlet pipe 2 and limits, because this section tubular wall and all the other tube walls of limiting the low-pressure inlet pipe 2 of bolster 20 are separated, the perisporium of therefore low-pressure inlet pipe 2 limits liquid outlet 21, the most of refrigerant entering into low-pressure inlet pipe 2 is drained in separated space 10 from liquid outlet 21 after the process flowed downward is buffered part 20 backstop.It is appreciated of course that, the structure of bolster 20 is not limited thereto, such as bolster 20 can also for the projection on multiple internal perisporium being located at low-pressure inlet pipe 2, and multiple projection is spaced apart on the length direction of low-pressure inlet pipe 2, as long as bolster 20 can play the flow velocity of buffering refrigerant.
Low pressure escape pipe 3 is formed as " U " shape substantially, low pressure escape pipe 3 first to extend into downwards in separated space 10 and extends downward the bottom of separated space 10, low pressure escape pipe 3 upwards bends the top extending to separated space 10 afterwards, the end being positioned at the low pressure escape pipe 3 on the top of separated space 10 is inlet end 32, and the end being positioned at the low pressure escape pipe 3 outside cylindrical shell 1 is outlet side 33.
The bending part place being positioned at separated space 10 of low pressure escape pipe 3 is provided with oil return opening 30, and the size of oil return opening 30 can be arranged according to actual conditions, and such as shown in Figure 9, the diameter of oil return opening 30 is the span of d, d is 0.5mm-5mm.
In order to prevent impurity from entering in low pressure escape pipe 3 by oil return opening 30, as shown in Figure 3 and Figure 9, gas-liquid separator 100 also comprises filter 5, and filter 5 is located at oil return opening 30 place.As shown in Figure 9, filter 5 can be screen pack, and screen pack 5 is located on low pressure escape pipe 3 by support 7.It is appreciated of course that filter 5 can also be formed as other filtrations.
As shown in Figure 3, the distance between the center line of the base section of low pressure escape pipe 3 and the diapire of separated space 10 is the span of B, distance B can be 5mm-50mm.As shown in Figure 3, the bottom of low-pressure inlet pipe 2 extends downward beyond the inlet end 32 of low pressure escape pipe 3.Thus the refrigerant entered in cylindrical shell 1 from low-pressure inlet pipe 2 can be avoided directly to be drained in low pressure escape pipe 3.As shown in Figure 3, the distance between the bottom face of low-pressure inlet pipe 2 and the air inlet end face of low pressure escape pipe 3 is H, distance H > 0.
As shown in Figure 3, low pressure escape pipe 3 be positioned at separated space 10 and the part of the outlet side 33 of contiguous low pressure escape pipe 3 is provided with return-air hole 31, that is, return-air hole 31 is located on low pressure escape pipe 3, return-air hole 31 is positioned at separated space 10, the outlet side 33 of the contiguous low pressure escape pipe 3 of return-air hole 31 is arranged, gaseous coolant in separated space 10 can enter in low pressure escape pipe 3 by return-air hole 31, namely the gaseous coolant in separated space 10 can enter in low pressure escape pipe 3 by return-air hole 31 and inlet end 32, thus the gas output of low pressure escape pipe 3 can be increased.Be understandable that, the quantity of return-air hole 31, the shape and size of each return-air hole 31 can set according to the actual requirements.
As shown in Figure 6, the line of centres L1 of the outlet side 33 of low pressure escape pipe 3 and the inlet end 32 of low pressure escape pipe 3 and, angle between the outlet side 33 of low pressure escape pipe 3 and the line of centres L2 of low-pressure inlet pipe 2 is A, described A > 0.That is, line of centres L1 is through the end face center of the end face center of the outlet side 33 of low pressure escape pipe 3 and the inlet end 32 of low pressure escape pipe 3, and line of centres L2 is through the center of the end face center of the outlet side 33 of low pressure escape pipe 3 and the top end face of low-pressure inlet pipe 2.In brief, formed by two mouths of pipe of low pressure escape pipe 3 between straight line and low-pressure inlet pipe 2 at an angle.
As shown in Figure 4 and Figure 5, heat exchange pipeline part 40 comprises two primary flow path 401, multiple points of streams 402 and two current dividers 43, the two ends of each point of stream 402 are communicated with two primary flow path 401 respectively, and the end of two primary flow path 401 is stretched out cylindrical shell 1 respectively and imported and exported 41 to limit the first import and export 42 and second.Each current divider 43 has total head piece and multiple subflow mouth, two primary flow path 401 are connected with total head piece of two current dividers 43 respectively, multiple points of streams 402 are connected with the subflow mouth of two current dividers 43 respectively, that is, each primary flow path 401 is connected by a current divider 43 with between multiple points of streams 402, thus makes the structure of heat exchange pipeline part 40 simple.It is appreciated of course that the annexation between each primary flow path 401 and multiple points of streams 402 is not limited thereto, such as each point of stream 402 can directly be welded in each primary flow path 401.
In the example of fig. 4, stream 402 is divided to be three.In the example of hgure 5, a point stream 402 is two, and current divider 43 can be triple valve.
Below with reference to Figure 10, the freezing cycle device 1000 according to the utility model embodiment is described.
As shown in Figure 10, according to the freezing cycle device 1000 of the utility model embodiment, comprise: compressor 200, outdoor heat exchanger 400, indoor heat exchanger 500, commutation assembly 300, first throttle device 600 and gas-liquid separator 100, compressor 200 has exhaust outlet a and gas returning port b, commutation assembly 300 has the first valve port c to the 4th valve port f, first valve port c is connected with exhaust outlet a, second valve port d is connected with the first end of outdoor heat exchanger 400, 3rd valve port e is connected with the first end of indoor heat exchanger 500, second end of outdoor heat exchanger 400 is connected with the first end of first throttle device 600.When freezing cycle device 1000 freezes, the first valve port c is communicated with the second valve port d and the 3rd valve port e is communicated with the 4th valve port f.When freezing cycle device 1000 heats, the first valve port c is communicated with the 3rd valve port e and the second valve port d is communicated with the 4th valve port f.
Preferably, commutation assembly 300 be cross valve, it is appreciated of course that the assembly 300 that commutates can also be formed as other structures, can realize commutating as long as have the first valve port c to the 4th valve port f.
First of pressure piping 4 is imported and exported 42 and is connected with the second end of first throttle device 600, second of pressure piping 4 is imported and exported 41 and is connected with the second end of indoor heat exchanger 500, the upper end of low-pressure inlet pipe 2 is connected with the 4th valve port f, and the outlet side 33 of low pressure escape pipe 3 is connected with gas returning port b.Alternatively, first throttle device 600 is the restricting element such as capillary or electric expansion valve.
It should be noted that, refrigerant circulation process during freezing cycle device 1000 refrigerating operaton and heating operation according to the utility model embodiment has been described in detail above-mentioned, just repeats no more here.
According to the freezing cycle device 1000 of the utility model embodiment, by being provided with gas-liquid separator 100, refrigerant in refrigerant in pressure piping 4 and separated space 10 carries out heat exchange, thus make gas-liquid separator 100 serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of freezing cycle device 1000, thus improve the refrigerating efficiency of compressor 200, improve the COP of freezing cycle device 1000.
As shown in Figure 10, in embodiments more of the present utility model, freezing cycle device 1000 also comprises auxiliary stream 900, and auxiliary stream 900 is connected with the outlet side 33 of low pressure escape pipe 3 with pressure piping 4 respectively, and auxiliary stream 900 is in series with the second throttling arrangement 700 and control valve 800.
Specifically, the first end of auxiliary stream 900 is connected between first throttle device 600 and pressure piping 4, and the second end of auxiliary stream 900 is connected between low pressure escape pipe 3 and gas returning port b, and control valve 800 can be stop valve or single-pass magnetic valve.Second throttling arrangement 700 plays the effect of reducing pressure by regulating flow, and alternatively, the second throttling arrangement 700 is capillary.
It can thus be appreciated that, when freezing cycle device 1000 freezes, control valve 800 is opened, and is drained in gas returning port b after the refrigerant of first throttle device 600 outflow can mix with the refrigerant of discharging from low pressure escape pipe 3 after the reducing pressure by regulating flow again of the second throttling arrangement 700.When freezing cycle device 1000 heats, control valve 800 can be in closed condition.Thus the temperature of the refrigerant being discharged to gas returning port b can be reduced; thus reduce the temperature of the refrigerant of discharging from the exhaust outlet a of compressor 200; avoid the temperature of the exhaust outlet a of compressor 200 too high and disadvantageous phenomenon is caused to compressor 200, playing the effect of protection compressor 200.
The refrigeration system 2000 according to the utility model embodiment is described in detail below with reference to Figure 11.
According to the refrigeration system 2000 of the utility model embodiment, comprising: compressor 200, outdoor heat exchanger 400, indoor heat exchanger 500, first throttle device 600 and gas-liquid separator 100, compressor 200 has exhaust outlet a and gas returning port b.The two ends of outdoor heat exchanger 400 are connected with the first end of first throttle device 600 with exhaust outlet a respectively.
First of pressure piping 4 is imported and exported 42 and is connected with the second end of first throttle device 600, second of pressure piping 4 is imported and exported 41 and is connected with the first end of indoor heat exchanger 500, the upper end of low-pressure inlet pipe 2 is connected with the second end of indoor heat exchanger 500, and the outlet side 33 of low pressure escape pipe 3 is connected with gas returning port b.
It should be noted that, refrigerant circulation process when refrigerant circulation process during refrigeration system 2000 refrigerating operaton according to the utility model embodiment is freezed with freezing cycle device 1000 is identical, and has been described in detail above-mentioned, just repeats no more here.
According to the refrigeration system 2000 of the utility model embodiment, by being provided with gas-liquid separator 100, refrigerant in refrigerant in pressure piping 4 and separated space 10 carries out heat exchange, thus make gas-liquid separator 100 serve the effect of subcooler, regenerator and gas-liquid separation simultaneously, add degree of supercooling and the degree of superheat of refrigeration system 2000, thus improve the refrigerating efficiency of compressor 200, improve the COP of refrigeration system 2000.
As shown in figure 11, in embodiments more of the present utility model, refrigeration system 2000 also comprises auxiliary stream 900, and auxiliary stream 900 is connected with the outlet side 33 of low pressure escape pipe 3 with pressure piping 4 respectively, and auxiliary stream 900 is in series with the second throttling arrangement 700 and control valve 800.
Specifically, the first end of auxiliary stream 900 is connected between first throttle device 600 and pressure piping 4, and the second end of auxiliary stream 900 is connected between low pressure escape pipe 3 and gas returning port b, and control valve 800 can be stop valve or check valve.When control valve 800 is check valve, check valve is one-way conduction on the direction from the first end of auxiliary stream 900 to the second end of auxiliary stream 900.Second throttling arrangement 700 plays the effect of reducing pressure by regulating flow, and alternatively, the second throttling arrangement 700 is capillary.
It can thus be appreciated that, be drained in gas returning port b after the refrigerant of first throttle device 600 outflow can mix with the refrigerant of discharging from low pressure escape pipe 3 after the reducing pressure by regulating flow again of the second throttling arrangement 700.Thus the temperature of the refrigerant being discharged to gas returning port b can be reduced; thus reduce the temperature of the refrigerant of discharging from the exhaust outlet a of compressor 200; avoid the temperature of the exhaust outlet a of compressor 200 too high and disadvantageous phenomenon is caused to compressor 200, playing the effect of protection compressor 200.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score can be that the first and second features directly contact, or the first and second features are by intermediary mediate contact.And, fisrt feature second feature " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or only represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " below " and " below " can be fisrt feature immediately below second feature or tiltedly below, or only represent that fisrt feature level height is less than second feature.
In the description of this description, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present utility model or example.In this manual, to the schematic representation of above-mentioned term not must for be identical embodiment or example.And the specific features of description, structure, material or feature can combine in one or more embodiment in office or example in an appropriate manner.In addition, when not conflicting, the feature of the different embodiment described in this description or example and different embodiment or example can carry out combining and combining by those skilled in the art.
Although illustrate and described embodiment of the present utility model above, be understandable that, above-described embodiment is exemplary, can not be interpreted as restriction of the present utility model, those of ordinary skill in the art can change above-described embodiment, revises, replace and modification in scope of the present utility model.
Claims (13)
1. a gas-liquid separator, is characterized in that, comprising:
Cylindrical shell, limits separated space in described cylindrical shell;
Low-pressure inlet pipe, one end of described low-pressure inlet pipe extend in described separated space to enter the refrigerant treating gas-liquid separation;
Low pressure escape pipe, described low pressure escape pipe extend into discharge the gaseous coolant in described separated space in described separated space, and the part being positioned at described separated space bottom of described low pressure escape pipe is provided with oil return opening;
Be suitable for the pressure piping of circulation refrigerant, described pressure piping has and is positioned at described separated space to carry out the heat exchange pipeline part of heat exchange with the refrigerant of described separated space, described heat exchange pipeline part comprises two primary flow path and multiple points of streams, the two ends of each described point stream are communicated with described two primary flow path respectively, and the end of described two primary flow path is stretched out described cylindrical shell respectively and imported and exported to limit the first import and export and second.
2. gas-liquid separator according to claim 1, is characterized in that, is provided with bolster in described low-pressure inlet pipe.
3. gas-liquid separator according to claim 2, is characterized in that, bends inwards to limit described bolster after a part of tube wall of described low-pressure inlet pipe is separated with all the other tube walls.
4. gas-liquid separator according to claim 1, is characterized in that, described low pressure escape pipe be positioned at described separated space and the part of the outlet side of contiguous described low pressure escape pipe is provided with return-air hole.
5. gas-liquid separator according to claim 1, it is characterized in that, described pressure piping also comprises two current dividers, each described current divider has total head piece and multiple subflow mouth, described two primary flow path are connected with described total head piece of described two current dividers respectively, and described multiple points of streams are connected with the subflow mouth of described two current dividers respectively.
6. gas-liquid separator according to claim 1, is characterized in that, also comprises filter, and described filter is located at described oil return opening place.
7. gas-liquid separator according to claim 1, is characterized in that, in described heat exchange pipeline part, overcoat has heat exchange fin.
8. gas-liquid separator according to claim 1, is characterized in that, the bottom of described low-pressure inlet pipe extends downward beyond the inlet end of described low pressure escape pipe.
9. gas-liquid separator according to claim 1, it is characterized in that, the line of centres of the outlet side of described low pressure escape pipe and the inlet end of described low pressure escape pipe and, angle between the outlet side of described low pressure escape pipe and the line of centres of described low-pressure inlet pipe is A, described A > 0.
10. a freezing cycle device, is characterized in that, comprising:
Compressor, described compressor has exhaust outlet and gas returning port;
Commutation assembly, described commutation assembly comprises the first valve port to the 4th valve port, described first valve port is communicated with one of them in the 3rd valve port with the second valve port, and described 4th valve port and described second valve port are communicated with another in described 3rd valve port, and described first valve port is connected with described exhaust outlet;
Outdoor heat exchanger and indoor heat exchanger, the two ends of described outdoor heat exchanger are connected with the first end of first throttle device with described second valve port respectively, and the first end of described indoor heat exchanger is connected with described 3rd valve port;
Gas-liquid separator according to any one of claim 1-9, described first of described pressure piping is imported and exported and is connected with the second end of described first throttle device, described second of described pressure piping is imported and exported and is connected with the second end of described indoor heat exchanger, the upper end of described low-pressure inlet pipe is connected with described 4th valve port, and the outlet side of described low pressure escape pipe is connected with described gas returning port.
11. freezing cycle devices according to claim 10, it is characterized in that, also comprise auxiliary stream, described auxiliary stream is connected with the outlet side of described pressure piping with described low pressure escape pipe respectively, and described auxiliary stream is in series with the second throttling arrangement and control valve.
12. 1 kinds of refrigeration systems, is characterized in that, comprising:
Compressor, described compressor has exhaust outlet and gas returning port;
Outdoor heat exchanger, the two ends of described outdoor heat exchanger are connected with the first end of described exhaust outlet with first throttle device respectively;
Indoor heat exchanger and the gas-liquid separator according to any one of claim 1-9, described first of described pressure piping is imported and exported and is connected with the second end of described first throttle device, described second of described pressure piping is imported and exported and is connected with the first end of described indoor heat exchanger, the upper end of described low-pressure inlet pipe is connected with the second end of described indoor heat exchanger, and the outlet side of described low pressure escape pipe is connected with described gas returning port.
13. refrigeration systems according to claim 12, is characterized in that, also comprise auxiliary stream, and described auxiliary stream is connected with the outlet side of described pressure piping with described low pressure escape pipe respectively, and described auxiliary stream is in series with the second throttling arrangement and control valve.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521041849.XU CN205227953U (en) | 2015-12-14 | 2015-12-14 | Vapour and liquid separator and have its refrigerating cycle device, refrigerating system |
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| CN201521041849.XU CN205227953U (en) | 2015-12-14 | 2015-12-14 | Vapour and liquid separator and have its refrigerating cycle device, refrigerating system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105605837A (en) * | 2015-12-14 | 2016-05-25 | 广东美的暖通设备有限公司 | Gas-liquid separator and refrigeration cycle device with same and refrigeration system with same |
| CN108317759A (en) * | 2018-01-09 | 2018-07-24 | 重庆美的通用制冷设备有限公司 | Refrigeration unit |
| CN108562476A (en) * | 2018-05-25 | 2018-09-21 | 北京海光仪器有限公司 | A kind of Separate System of Water-jet for the sample introduction that reacts for chemical evapn |
-
2015
- 2015-12-14 CN CN201521041849.XU patent/CN205227953U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105605837A (en) * | 2015-12-14 | 2016-05-25 | 广东美的暖通设备有限公司 | Gas-liquid separator and refrigeration cycle device with same and refrigeration system with same |
| CN108317759A (en) * | 2018-01-09 | 2018-07-24 | 重庆美的通用制冷设备有限公司 | Refrigeration unit |
| CN108562476A (en) * | 2018-05-25 | 2018-09-21 | 北京海光仪器有限公司 | A kind of Separate System of Water-jet for the sample introduction that reacts for chemical evapn |
| CN108562476B (en) * | 2018-05-25 | 2023-09-01 | 北京海光仪器有限公司 | Gas-liquid separation system for chemical vapor generation reaction sample injection |
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Granted publication date: 20160511 Termination date: 20201214 |