CN105135766A - Bi-directional spiral flash vessel applied to air-supplementing and enthalpy-increasing heat pump air-conditioning system - Google Patents
Bi-directional spiral flash vessel applied to air-supplementing and enthalpy-increasing heat pump air-conditioning system Download PDFInfo
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Abstract
The invention discloses a bi-directional spiral flash vessel applied to an air-supplementing and enthalpy-increasing heat pump air-conditioning system. The flash vessel comprises a barrel body, the barrel body comprises an upper-segment barrel body, an intermediate-segment barrel body and a lower-segment barrel body from top to bottom, an air outlet pipe is arranged on the side wall of the upper-segment barrel body, a first cooling agent inlet and outlet pipe and a second cooling agent inlet and outlet pipe which extend to an inner cavity of the barrel body are arranged on the side wall of the lower-segment barrel body, the portions, inserted into the barrel body, of the first cooling agent inlet and outlet pipe and the second cooling agent inlet and outlet pipe are spiral copper pipe portions both of which spirally extend upward clockwise or anticlockwise, and the two spiral copper pipe portions are assembled in a coiled mode so as to jointly form a gas-liquid separation device. By means of the bi-directional spiral flash vessel, the limit of unidirectional flow of an existing flash vessel is broken through, the bi-directional flowability is achieved, the air-supplementing and enthalpy-increasing system can be greatly simplified, meanwhile, the gas-liquid separation effect of the flash vessel is guaranteed and improved, and the bi-directional spiral flash vessel is applicable to an application occasion where the installation height of the flash vessel is limited and the specific value between the height and the diameter is small.
Description
Technical field
The present invention relates to the air-conditioning system that low-temperature air-compensation air increases enthalpy, be specifically related to a kind of bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system.
Background technology
Existing heat pump type air conditioning system runs at low temperature environment, still there is heating capacity decay, heating efficiency reduces, compressor exhaust temperature raises problems such as causing system cloud gray model unreliable, thus limits the promoting the use of in north cold area of heat pump air conditioner.And tonifying Qi enthalpy increasing heat pump air-conditioning system is due to its good low temperature adaptability, be applied to the fields such as low temperature domestic air conditioning, air conditioning for automobiles gradually.
The existing tonifying Qi with flash tank increases enthalpy system, and its flash tank has three mouths: gas-liquid mixed refrigerant entrance, liquid refrigerant outlet, tonifying Qi outlet.Its maximum shortcoming is this flash vessel is one-way flow, has requirement to the flow direction of cold-producing medium.But tonifying Qi increases the low-temperature heating performance that enthalpy can not only promote heat pump type air conditioning system, also the high-temperature refrigeration performance of air-conditioning system can be promoted, so when a set of heat pump type air conditioning system refrigeration and heat all need to use flash vessel to carry out tonifying Qi time, just relate to the switching problem of refrigerating/heating pattern, now to ensure the one-way of flash vessel flowing, then at least need separately to add four magnetic valves to control, increase the complexity of system.
Being applied in domestic air conditioning more than the current increasing of the tonifying Qi with flash vessel enthalpy system, when being applied to car air-conditioner as coach air conditioner, facing again the problem that installation dimension is limited.For flash vessel design, in order to ensure the effect of gas-liquid separation, flash vessel height and diameter ratio generally should be 4 ~ 6.But coach air conditioner is for height dimension unusual sensitivity again, and height and diameter ratio can only reach about 2 at most, and gas-liquid separation effect is difficult to guarantee.
In sum, how the tonifying Qi of band flash tank is increased the occasion that enthalpy system is applied to limited height, as in coach air conditioner, promote the low-temperature heating performance of air-conditioning system, ensure the terseness of system and the gas-liquid separation effect of flash vessel again, be the problem that those skilled in the art are badly in need of solving simultaneously.
Summary of the invention
For above-mentioned technical problem, the present invention aims to provide a kind of bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system, to improve the flash vessel gas-liquid separation effect of height-limited system, realizes the two-way flow of cold-producing medium simultaneously, simplifies tonifying Qi and increases enthalpy system.
Technical solution of the present invention is:
A kind of bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system, comprise cylindrical shell, described cylindrical shell from top to bottom comprises epimere cylindrical shell, stage casing cylindrical shell and lower end barrel, the swept volume of common composition tank body, epimere cylinder lateral wall is provided with escape pipe, lower end barrel sidewall is provided with the first cold-producing medium inlet/outlet pipe and second refrigerant inlet/outlet pipe that extend to cylinder lumen, described first cold-producing medium inlet/outlet pipe and the second refrigerant inlet/outlet pipe part inserted in cylindrical shell are all clockwise or are all the spiral copper pipe portion of spiraling counterclockwise upwards, two spiral copper pipe portion coiling assemblings, common formation gas-liquid separation device, the bottom that described first cold-producing medium inlet/outlet pipe is positioned at below cylindrical shell liquid level is provided with some first oil return hole for back flow, the bottom that described second refrigerant inlet/outlet pipe is positioned at below cylindrical shell liquid level is respectively arranged with some second oil return hole for back flow, this programme had both achieved the two-way flow of cold-producing medium, flash vessel gas-liquid separation effect can be improved again under setting height(from bottom) limited situation, greatly simplify the complexity that tonifying Qi increases enthalpy system, structure is simple, volume is little, cost is low, especially the application scenario of tonifying Qi is all needed under being applicable to low-temperature heating and high-temperature refrigeration operating mode.
Further, the quantity of described first oil return hole for back flow is 2 ~ 5, its actual internal area sum is less than or equal to described first cold-producing medium inlet/outlet pipe cross-sectional flow area, the quantity of described second oil return hole for back flow is 2 ~ 5, its actual internal area sum is less than or equal to the cross-sectional flow area of second refrigerant inlet/outlet pipe, can flow in spiral copper pipe portion to ensure abundant gas-liquid mixed refrigerant, and flowed out, so that gas-liquid mixed refrigerant carries out gas-liquid separation under gravity by spiral copper pipe portion end.
Further, the described first cold-producing medium inlet/outlet pipe spiral copper pipe portion that is positioned at more than cylindrical shell liquid level having uniformly along journey and ranked first venthole and and ranked first fluid hole along body helix; The spiral copper pipe portion that described second refrigerant inlet/outlet pipe is positioned at more than cylindrical shell liquid level has one uniformly along journey and ranked second venthole and along body helix and ranked second fluid hole, this programme is by setting out pore and fluid hole in spiral copper pipe portion, make the cold-producing medium of gas-liquid mixed under the effect of spiral centrifugal power, export gaseous refrigerant and liquid refrigerant respectively by venthole and fluid hole, realize gas-liquid separation further.
Further, angle on skew back in the spiral copper pipe portion that described first venthole is arranged on the first cold-producing medium inlet/outlet pipe, be 30 ~ 60 ° of angles with horizontal direction, skew back inferior horn outside the spiral copper pipe portion that described first fluid hole is arranged on the first cold-producing medium inlet/outlet pipe is 30 ~ 60 ° of angles with horizontal direction; Angle on skew back in the spiral copper pipe portion that described second venthole is arranged on second refrigerant inlet/outlet pipe, be 30 ~ 60 ° of angles with horizontal direction, skew back inferior horn outside the spiral copper pipe portion that second fluid hole is arranged on second refrigerant inlet/outlet pipe, be 30 ~ 60 ° of angles with horizontal direction, this programme is by setting out the specific position of pore and fluid hole, the cold-producing medium of gas-liquid mixed is separated by centrifugal force in helical pipe, improves the gas-liquid separation effect of cold-producing medium further.
Further, the quantity of described first venthole, the first fluid hole, the second venthole, the second fluid hole is 4 ~ 10, the object of the liquid state that quantity described in this programme can meet and gaseous refrigerant centrifugation, is also unlikely to increase difficulty of processing and cost simultaneously.
Further, described first cold-producing medium inlet/outlet pipe is identical with the shape and structure of second refrigerant inlet/outlet pipe.
Further, the flash distillation dividing plate above the spiral copper pipe portion being positioned at the first cold-producing medium inlet/outlet pipe and second refrigerant inlet/outlet pipe is provided with in described cylindrical shell, described flash distillation dividing plate is evenly provided with the gas-liquid separation hole that diameter is 4 ~ 8, the flash distillation dividing plate of this programme can play certain partition effect to floating cold-producing medium drop, ensures that in escape pipe be all gaseous refrigerant.
Further, described flash distillation dividing plate is arranged on 2/3 ~ 4/5 place of cylindrical shell height, to ensure the effect of gas-liquid separation.
This programme can the spiral flash vessel of two-way flow by arranging, solve existing tonifying Qi enthalpy increasing heat pump air-conditioning system and problem is required to the one-way flow of cold-producing medium, when a set of heat pump type air conditioning system refrigeration or heat all need to use flash vessel to carry out tonifying Qi time, increase by four magnetic valves in addition without the need to the one-way because ensureing flash vessel flowing and carry out refrigerant flow direction control, make air-conditioning system when the switching of refrigerating/heating pattern, cold-producing medium can be two-way flow through flash vessel, tonifying Qi can not only promote the low-temperature heating performance of heat pump type air conditioning system when increasing enthalpy, also the high-temperature refrigeration performance of air-conditioning system can be promoted, greatly simplify the complexity of system, volume and cost.
Compared with prior art, the present invention is used for the bidirectional screw flash vessel of tonifying Qi enthalpy increasing heat pump air-conditioning system, by arranging oil return hole for back flow below first, second cold-producing medium inlet/outlet pipe liquid level, make first, second cold-producing medium inlet/outlet pipe both can as the inlet tube of gas-liquid mixed refrigerant, again can as the outlet of liquid refrigerant, flash vessel has two-way flow.Be spiral copper pipe by arranging cold-producing medium inlet/outlet pipe inner barrel simultaneously, and open a discharge pore, fluid hole along spiral copper pipe more than liquid level, make gas-liquid two-phase mix refrigerant carry out centrifugal force separate under the effect of spiral copper pipe.The spiral flash vessel invented can reach the centrifugal force effect that be separated dual with gravity, can improve and ensure the separating effect of gas-liquid two-phase cold-producing medium, be applicable to flash vessel setting height(from bottom) limited, height and the less application scenario of diameter ratio.
Accompanying drawing explanation
Fig. 1 is the bidirectional screw flash vessel structural representation of the embodiment of the present invention.
Fig. 2 is the first cold-producing medium inlet/outlet pipe perspective view of the embodiment of the present invention.
Fig. 3 is the second refrigerant inlet/outlet pipe perspective view of the embodiment of the present invention.
Fig. 4 is the top view of the flash distillation dividing plate of the embodiment of the present invention.
Fig. 5 is the tonifying Qi enthalpy increasing heat pump Air Conditioning Cycle schematic diagram applying the embodiment of the present invention.
Shown in figure: shown in figure: 1-cylindrical shell; 2-escape pipe; 3-first cold-producing medium inlet/outlet pipe; 4-second refrigerant inlet/outlet pipe; 5-flash distillation dividing plate; 101-tonifying Qi increases enthalpy compressor; 102-cross valve; 103-outdoor heat exchanger; 104-first electric expansion valve; 105-bidirectional screw flash vessel; 106-second electric expansion valve; 107-indoor heat exchanger; 108-gas-liquid separator; 109-magnetic valve; 11-epimere cylindrical shell; 12-middle-end cylindrical shell; 13-lower end barrel; 31-first oil return hole for back flow; 32-first venthole; 33-first fluid hole; 41-second oil return hole for back flow; 42-second venthole; 43-second fluid hole; 51-gas-liquid separation hole.
Detailed description of the invention
Be described in further detail object of the present invention below by specific embodiment, embodiment can not repeat one by one at this, but therefore this be not defined in following examples below in conjunction with accompanying drawing and the embodiment that specifically carries out an invention.
As shown in Figure 1, a kind of bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system, comprise cylindrical shell 1, described cylindrical shell 1 from top to bottom comprises epimere cylindrical shell 11, stage casing cylindrical shell 12 and lower end barrel 13, the swept volume of common composition tank body, epimere cylindrical shell 11 sidewall is provided with escape pipe 2, lower end barrel 13 sidewall is provided with the first cold-producing medium inlet/outlet pipe 3 and second refrigerant inlet/outlet pipe 4 that extend to cylindrical shell 1 inner chamber, described first cold-producing medium inlet/outlet pipe 3 and second refrigerant inlet/outlet pipe 4 part inserted in cylindrical shell 1 are all clockwise or are all the spiral copper pipe portion of spiraling counterclockwise upwards, two spiral copper pipe portion coiling assemblings, common formation gas-liquid separation device, the bottom that described first cold-producing medium inlet/outlet pipe 3 is positioned at below cylindrical shell 1 liquid level is provided with 2 ~ 5 the first oil return hole for back flow 31, the bottom that described second refrigerant inlet/outlet pipe 4 is positioned at below cylindrical shell 1 liquid level is respectively arranged with 2 ~ 5 the second oil return hole for back flow 41, in flash vessel, liquid refrigerant liquid level is generally 1/4 ~ 1/3 of flash vessel height overall, this programme had both achieved the two-way flow of cold-producing medium, flash vessel gas-liquid separation effect can be improved again under setting height(from bottom) limited situation, greatly simplify the complexity that tonifying Qi increases enthalpy system, structure is simple, volume is little, cost is low, especially the application scenario under low-temperature heating and high-temperature refrigeration operating mode is applicable to.
As shown in Figures 2 and 3, in the present embodiment, the actual internal area sum of described first oil return hole for back flow 31 is less than or equal to described first cold-producing medium inlet/outlet pipe 3 cross-sectional flow area, the actual internal area sum of described second oil return hole for back flow 41 is less than or equal to the cross-sectional flow area of second refrigerant inlet/outlet pipe 4, can flow in spiral copper pipe portion to ensure abundant gas-liquid mixed refrigerant, and flowed out, so that gas-liquid mixed refrigerant carries out gas-liquid separation under gravity by spiral copper pipe portion end.
In the present embodiment, the spiral copper pipe portion that described first cold-producing medium inlet/outlet pipe 3 is positioned at more than cylindrical shell 1 liquid level has 4 ~ 10 the first ventholes 32 and 4 ~ 10 the first fluid holes 33 along body helix uniformly along journey; The spiral copper pipe portion that described second refrigerant inlet/outlet pipe 4 is positioned at more than cylindrical shell 1 liquid level has 4 ~ 10 the second ventholes 42 and 4 ~ 10 the second fluid holes 43 along body helix uniformly along journey, and concrete data can be determined according to the pipe range of spiral copper pipe.This programme, by setting out pore and fluid hole in spiral copper pipe portion, makes the cold-producing medium of gas-liquid mixed under the effect of spiral centrifugal power, exports gaseous refrigerant and liquid refrigerant respectively by venthole and fluid hole, the gas-liquid separation realized further.
In the present embodiment, as further prioritization scheme, in the spiral copper pipe portion that described first venthole 32 is arranged on the first cold-producing medium inlet/outlet pipe 3 angle on skew back, and be 30 ~ 60 ° of angles with horizontal direction, the present embodiment is 45 °; Skew back inferior horn outside the spiral copper pipe portion that described first fluid hole 33 is arranged on the first cold-producing medium inlet/outlet pipe 3, be 30 ~ 60 ° of angles with horizontal direction, the present embodiment is 45 °; Angle on skew back in the spiral copper pipe portion that described second venthole 42 is arranged on second refrigerant inlet/outlet pipe 4, be 30 ~ 60 ° of angles with horizontal direction, the present embodiment is 45 °, skew back inferior horn outside the spiral copper pipe portion that second fluid hole 43 is arranged on second refrigerant inlet/outlet pipe 4, be 30 ~ 60 ° of angles with horizontal direction, the present embodiment is 45 °.This programme sets out the specific position of pore and fluid hole, because the flowing in spiral copper pipe of gas-liquid two-phase mix refrigerant can produce centrifugal force, the gaseous refrigerant that inertia force is less is gathered in the inner side of spiral copper pipe, and the liquid refrigerant that inertia force is larger is gathered in outside spiral copper pipe.Part gaseous refrigerant after centrifugal force separate flows out from the venthole at angle interior skew back, and some liquid refrigerant flows out from the fluid hole of outer skew back inferior horn, improves the gas-liquid separation effect of cold-producing medium further.
For simplifying processing, described first cold-producing medium inlet/outlet pipe 3 is identical with the shape and structure of second refrigerant inlet/outlet pipe 4.
As shown in Figure 1 and Figure 4, the flash distillation dividing plate 5 above the spiral copper pipe portion being positioned at the first cold-producing medium inlet/outlet pipe 3 and second refrigerant inlet/outlet pipe 4 is provided with in described cylindrical shell 1, described flash distillation dividing plate 5 is generally arranged on 2/3 ~ 4/5 place of cylindrical shell 1 height, between spiral copper pipe portion and gas outlet, described flash distillation dividing plate 5 is evenly provided with the gas-liquid separation hole 51 that diameter is 4 ~ 8, flash distillation dividing plate 5 mainly plays iris action to floating more aerial cold-producing medium drops, gaseous refrigerant can from the smooth and easy outflow in gas-liquid separation hole 51, ensure that the great majority that escape pipe 2 flows out are gaseous refrigerant.
The bidirectional screw flash vessel that the present embodiment provides by arranging oil return hole for back flow below first, second cold-producing medium inlet/outlet pipe liquid level, make first, second cold-producing medium inlet/outlet pipe both can as the inlet tube of gas-liquid mixed refrigerant, again can as the outlet of liquid refrigerant, flash vessel has two-way flow, solves the restriction of existing flash vessel one-way flow.The application of two-way flash vessel greatly can simplify tonifying Qi and increase enthalpy system.Be spiral copper pipe by arranging cold-producing medium inlet/outlet pipe inner barrel simultaneously, and open a discharge pore, fluid hole along spiral copper pipe more than liquid level, make gas-liquid two-phase mix refrigerant carry out centrifugal force separate under the effect of spiral copper pipe.Reach the centrifugal force effect that be separated dual with gravity, can improve and ensure the separating effect of gas-liquid two-phase cold-producing medium, greatly simplify the complexity of system, volume and cost, be applicable to flash vessel setting height(from bottom) limited, height and the less application scenario of diameter ratio.
As shown in Figure 5, a kind of tonifying Qi enthalpy increasing heat pump air-conditioning system adopting described bidirectional screw flash vessel, comprise tonifying Qi and increase enthalpy compressor 101, cross valve 102, outdoor heat exchanger 103, indoor heat exchanger 107, gas-liquid separator 108, it is characterized in that: also comprise bidirectional screw flash vessel, the escape pipe 2 of described bidirectional screw flash vessel increases the gas supplementing opening of enthalpy compressor 101 by pipeline successively connected electromagnetic valve 109 and tonifying Qi, first cold-producing medium inlet/outlet pipe 3 of described bidirectional screw flash vessel connects the first electric expansion valve 104 and outdoor heat exchanger 103 successively by pipeline, the second refrigerant inlet/outlet pipe 4 of described bidirectional screw flash vessel connects the second electric expansion valve 106 and indoor heat exchanger 107 successively by pipeline.
The tonifying Qi enthalpy increasing heat pump air-conditioning system of the present embodiment, carries out the switching of refrigerating/heating pattern by cross valve 102.When refrigeration mode runs, high-temperature high-pressure refrigerant increases enthalpy compressor 101 from tonifying Qi and enters into outdoor heat exchanger 103, carries out one-level throttling, then flow into bidirectional screw flash vessel 105 through the first electric expansion valve 104.Gas-liquid mixed refrigerant is in flash vessel after flash distillation, gaseous refrigerant increases enthalpy compressor 101 via tonifying Qi pipeline to tonifying Qi and carries out tonifying Qi, liquid refrigerant enters indoor heat exchanger 107 evaporation endothermic through the second electric expansion valve 106 two-step throttle, then flows back to tonifying Qi and increases enthalpy compressor 101.Heating mode operational process is similar, refers to Fig. 5.
Owing to have employed the flash vessel with two-way flow function, thus tonifying Qi increasing enthalpy system diagram greatly simplifies.Need the operating mode of carrying out tonifying Qi at low-temperature heating, high-temperature refrigeration etc., the gaseous refrigerant that bidirectional screw flash vessel 105 flashes off increases enthalpy compressor 101 via magnetic valve 109 pairs of tonifying Qi and carries out tonifying Qi.When heat pump type air conditioning system operates in the operating mode not needing tonifying Qi, the first electric expansion valve 104 standard-sized sheet, magnetic valve 109 cuts out.Now bidirectional screw flash vessel 105 as liquid storage fill with use, liquid refrigerant through the second electric expansion valve 106 throttling laggard enter indoor heat exchanger 107 evaporation endothermic.
When heat pump type air conditioning system operates in refrigeration mode, gas-liquid two-phase cold-producing medium enters from the first cold-producing medium inlet/outlet pipe 3, part mix refrigerant can flow out at the first oil return hole for back flow 31, and upwards flows along spiral copper pipe due to the very fast remaining mix refrigerant of refrigerant flow rates.The flowing in spiral copper pipe of gas-liquid two-phase mix refrigerant can produce centrifugal force, and the gaseous refrigerant that inertia force is less is gathered in the inner side of spiral copper pipe, and the liquid refrigerant that inertia force is larger is gathered in outside spiral copper pipe.Part gaseous refrigerant after centrifugal force separate flows out from first venthole 32 at angle interior skew back, and some liquid refrigerant flows out from the first fluid hole 33 of outer skew back inferior horn.In pipe, residue mix refrigerant sprays from the end of the first cold-producing medium inlet/outlet pipe 3, carries out gas-liquid separation under gravity.Isolated gaseous refrigerant and the gaseous refrigerant flashed off increase enthalpy compressor 101 via gas-liquid separation hole 51 and escape pipe 2 pairs of tonifying Qi and carry out tonifying Qi.And isolated liquid refrigerant flows out from the second oil return hole for back flow 41, flow to indoor heat exchanger 107 again through the second electric expansion valve 106 two-step throttle and carry out evaporation endothermic.So the effect of the last gas-liquid separation of bidirectional screw flash vessel 105 is the double effects that centrifugal force separate adds Gravity Separation, can improve and ensure the separation degree of gas-liquid refrigerant in flash vessel, and then ensure the job security of compressor.
When heat pump type air conditioning system operates in heating mode, gas-liquid two-phase mix refrigerant enters from second refrigerant inlet/outlet pipe 4, mix refrigerant at a high speed upwards flows along spiral copper pipe, under the influence of centrifugal force, gaseous refrigerant flows out from the second venthole 42, and liquid refrigerant flows out from the second fluid hole 43.In pipe, residue mix refrigerant is from the ejection of second refrigerant inlet/outlet pipe 4 end, carries out gas-liquid separation under gravity.The gaseous refrigerant be separated and flash off flows out from escape pipe 2 and carries out tonifying Qi to tonifying Qi increasing enthalpy compressor 101, and liquid phase refrigerant flows out from the first oil return hole for back flow 31, then flow into outdoor heat exchanger 103 via the first electric expansion valve 104 second throttle and carry out evaporation endothermic.
Can find out, the heat pump type air conditioning system that the present embodiment provides can not only improve gas-liquid and to be connected the separating effect of cold-producing medium, the heat exchange efficiency of raising system, and solve the restriction of existing flash vessel one-way flow, greatly simplify the structural complexity of system, especially setting height(from bottom) is applicable to limited, height and the less application scenario of diameter ratio.
The above embodiment of the present invention is only for example of the present invention is clearly described, and is not the restriction to embodiments of the present invention.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.All any amendments done within the spirit and principles in the present invention, equivalent to replace and improvement etc., within the protection domain that all should be included in the claims in the present invention.
Claims (8)
1. one kind is applied to the bidirectional screw flash vessel of tonifying Qi enthalpy increasing heat pump air-conditioning system, comprise cylindrical shell (1), it is characterized in that: described cylindrical shell (1) from top to bottom comprises epimere cylindrical shell (11), stage casing cylindrical shell (12) and lower end barrel (13), the swept volume of common composition tank body, epimere cylindrical shell (11) sidewall is provided with escape pipe (2), lower end barrel (13) sidewall is provided with the first cold-producing medium inlet/outlet pipe (3) and second refrigerant inlet/outlet pipe (4) that extend to cylindrical shell (1) inner chamber, described first cold-producing medium inlet/outlet pipe (3) and second refrigerant inlet/outlet pipe (4) part inserted in cylindrical shell (1) are all clockwise or are all the spiral copper pipe portion of spiraling counterclockwise upwards, two spiral copper pipe portion coiling assemblings, common formation gas-liquid separation device, the bottom that described first cold-producing medium inlet/outlet pipe (3) is positioned at below cylindrical shell (1) liquid level is provided with some first oil return hole for back flow (31), the bottom that described second refrigerant inlet/outlet pipe (4) is positioned at below cylindrical shell (1) liquid level is respectively arranged with some second oil return hole for back flow (41).
2. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 1, it is characterized in that: the quantity of described first oil return hole for back flow (31) is 2 ~ 5, its actual internal area sum is less than or equal to described first cold-producing medium inlet/outlet pipe (3) cross-sectional flow area, the quantity of described second oil return hole for back flow (41) is 2 ~ 5, and its actual internal area sum is less than or equal to the cross-sectional flow area of second refrigerant inlet/outlet pipe (4).
3. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 1, is characterized in that: the spiral copper pipe portion that described first cold-producing medium inlet/outlet pipe (3) is positioned at more than cylindrical shell (1) liquid level has one uniformly along journey and ranked first venthole (32) and along body helix and ranked first fluid hole (33); The spiral copper pipe portion that described second refrigerant inlet/outlet pipe (4) is positioned at more than cylindrical shell (1) liquid level has one uniformly along journey and ranked second venthole (42) and along body helix and ranked second fluid hole (43).
4. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 3, it is characterized in that: in the spiral copper pipe portion that described first venthole (32) is arranged on the first cold-producing medium inlet/outlet pipe (3) angle on skew back, be 30 ~ 60 ° of angles with horizontal direction, skew back inferior horn outside the spiral copper pipe portion that described first fluid hole (33) is arranged on the first cold-producing medium inlet/outlet pipe (3) is 30 ~ 60 ° of angles with horizontal direction; Angle on skew back in the spiral copper pipe portion that described second venthole (42) is arranged on second refrigerant inlet/outlet pipe (4), be 30 ~ 60 ° of angles with horizontal direction, skew back inferior horn outside the spiral copper pipe portion that second fluid hole (43) is arranged on second refrigerant inlet/outlet pipe (4) is 30 ~ 60 ° of angles with horizontal direction.
5. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 4, is characterized in that: the quantity of described first venthole (32), the first fluid hole (33), the second venthole (42), the second fluid hole (43) is 4 ~ 10.
6. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 1, is characterized in that: described first cold-producing medium inlet/outlet pipe (3) is identical with the shape and structure of second refrigerant inlet/outlet pipe (4).
7. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to any one of claim 1 to 6, it is characterized in that: in described cylindrical shell (1), be provided with the flash distillation dividing plate (5) above the spiral copper pipe portion being positioned at the first cold-producing medium inlet/outlet pipe (3) and second refrigerant inlet/outlet pipe (4), described flash distillation dividing plate (5) is evenly provided with the gas-liquid separation hole (51) that diameter is 4 ~ 8.
8. the bidirectional screw flash vessel being applied to tonifying Qi enthalpy increasing heat pump air-conditioning system according to claim 7, is characterized in that: described flash distillation dividing plate (5) is arranged on 2/3 ~ 4/5 place of cylindrical shell (1) height.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106482406A (en) * | 2016-10-25 | 2017-03-08 | 珠海格力电器股份有限公司 | Flash evaporation and compression centrifugal refrigerating machines |
| CN108502858A (en) * | 2018-04-27 | 2018-09-07 | 胡自然 | A kind of industrial nitric acid preparation system |
| WO2018186130A1 (en) * | 2017-04-05 | 2018-10-11 | 株式会社デンソー | Gas/liquid separator and refrigerant cycle device |
| CN110455020A (en) * | 2019-07-24 | 2019-11-15 | 海信（山东）空调有限公司 | A kind of flash evaporation, air-conditioning system with enthalpy increased through vapor injection and control method thereof |
| CN110836560A (en) * | 2019-11-07 | 2020-02-25 | 珠海格力电器股份有限公司 | Flash evaporator and air conditioning system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003265984A (en) * | 2002-03-18 | 2003-09-24 | Central Conveyor Kk | Gas liquid separator |
| CN2763760Y (en) * | 2004-12-16 | 2006-03-08 | 上海大洋制冷工程有限公司 | Gas-liquid separator with heat regenerator function |
| CN203719273U (en) * | 2014-02-18 | 2014-07-16 | 美的集团股份有限公司 | Flash evaporator and air conditioner |
| JP2015001367A (en) * | 2013-06-18 | 2015-01-05 | 三菱電機株式会社 | Gas-liquid separator, and air conditioner having the same mounted thereon |
| CN205066260U (en) * | 2015-09-13 | 2016-03-02 | 华南理工大学 | Be applied to two -way spiral flash vessel that tonifying qi increases enthalpy heat pump air conditioning system |
-
2015
- 2015-09-13 CN CN201510578738.0A patent/CN105135766B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003265984A (en) * | 2002-03-18 | 2003-09-24 | Central Conveyor Kk | Gas liquid separator |
| CN2763760Y (en) * | 2004-12-16 | 2006-03-08 | 上海大洋制冷工程有限公司 | Gas-liquid separator with heat regenerator function |
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