CN101813352A - Jet-type air conditioner - Google Patents
Jet-type air conditioner Download PDFInfo
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- CN101813352A CN101813352A CN200910116258A CN200910116258A CN101813352A CN 101813352 A CN101813352 A CN 101813352A CN 200910116258 A CN200910116258 A CN 200910116258A CN 200910116258 A CN200910116258 A CN 200910116258A CN 101813352 A CN101813352 A CN 101813352A
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Abstract
The invention discloses a jet-type air conditioner which comprises a liquid storage tank (1), a condenser (8), an evaporator (5), a heat regenerator (3), a ejector (6) and a circulating pump (9), wherein the jet orifice (15) of the ejector (6) is in pipe connection with the outlet of the circulating pump (9), and the inlet of the circulating pump (9) is in pipe connection with the liquid storage tank (1); a first outlet (11) of the heat regenerator (3) is in pipe connection with a second inlet (12) of the heat regenerator (3), and the evaporator (5) and an expansion valve (4) are respectively connected with a pipeline in series; a first inlet (10) of the heat regenerator (3) is in pipe connection with the liquid storage tank (1), and a second outlet (13) of the heat regenerator (3) is in pipe connection with the suction inlet of the ejector (6); the outlet (14) of the jet device (6), the condenser (8), a non-return valve (7) and the liquid storage tank (1) are in pipe connection sequentially; and refrigerating media are stored in the liquid storage tank (1) and the pipeline. The invention has obvious energy-saving effect.
Description
Technical field
The present invention relates to a kind of air-conditioner, particularly a kind ofly add the injection type air-conditioner that injector device is a power with circulating pump.
Background technology
Present family mainly is to adopt the mode of both vapor compression to freeze with air-conditioner, is called the steam compressing air conditioner device.Its kind of refrigeration cycle is: liquid refrigerant enters evaporimeter and vaporization heat absorption in evaporimeter through capillary or expansion valve step-down, becomes low-pressure steam, thereby produces refrigeration effect; And after low-pressure steam is inhaled into compressor, be compressed into high temperature and high pressure steam again by consuming mechanical power.High temperature and high pressure steam enters condenser again, heat release in condenser, is condensed into highly pressurised liquid; Highly pressurised liquid is again by capillary or expansion valve, is that the liquid-vapor mixture of low-temp low-pressure is got back to evaporimeter by throttling expansion again, thereby finishes a refrigeration work circulation.
And to keep kind of refrigeration cycle, just must constantly consume a large amount of mechanical energy by compressor.
In the steam compressing air conditioner device, the mechanical energy of compressor not only will provide kind of refrigeration cycle needed kinetic energy, also to roll up the interior energy of cold-producing medium, make cold-producing medium constantly become high temperature and high pressure steam from low temperature and low pressure steam, these heat energy that are transformed from mechanical energy are released in condenser with the heat energy that imports into from evaporimeter.As seen, in the steam compressing air conditioner device, have greatly mechanical energy be used as used heat or idle work slatterns, the utilization ratio of its energy is quite low.
Summary of the invention
Purpose of the present invention just provides a kind ofly can efficiently utilize mechanical energy, adds the injection type air-conditioner that injector device is a power with circulating pump.
The technical solution used in the present invention is: injection type air-conditioner, and it comprises fluid reservoir, condenser, evaporimeter, regenerator, injector and circulating pump, and the jet of injector is connected with the circulating-pump outlet pipe, and the inlet of circulating pump is connected with the fluid reservoir pipe; Pipe connects between regenerator first outlet and second inlet, is serially connected with evaporimeter and expansion valve on the pipeline respectively; First inlet of regenerator is connected with the fluid reservoir pipe, and second outlet is connected with the suction inlet pipe of injector; The outlet of injector, condenser, check valve, fluid reservoir are managed connection successively; Contain refrigerant in fluid reservoir and the pipeline.
Adopt technique scheme, a part of liquid refrigerating medium in the fluid reservoir flows out by the pressurized injector that enters of circulating pump from fluid reservoir, jet expansion step-down, expansion at injector, form the ultrahigh speed fluid, near its suction chamber jet expansion causes high vacuum, refrigerant in the evaporimeter is constantly evaporated under the effect of pressure reduction, form Low Temperature Steam and enter suction chamber, be involved in mixing chamber by the ultrahigh speed fluid of jet expansion then.Like this, vapour, liquid two fluid streams mix and slow down, boost at mixing chamber, mix vapour-liquid stream (perhaps supersaturated vapor) and enter the condenser cooling, form liquid working substance and flow back to fluid reservoir; Another part liquid refrigerating working medium in the fluid reservoir then constantly enters evaporimeter by expansion valve or capillary under the effect of pressure reduction, replenish the refrigeration working medium that is evaporated in the evaporimeter, forms the working medium circulation.Evaporimeter and condenser can pass through flowing of refrigerant like this, play the effect to environment temperature reduction and heating.
In order to make sordid refrigerant not influence work, on first inlet of circulating pump and fluid reservoir and regenerator and the pipeline between the fluid reservoir, be serially connected with filter respectively.
The invention has the beneficial effects as follows: because the present invention uses circulating pump rather than compressor to provide power as kind of refrigeration cycle, and the kinetic energy and the potential energy of circulating pump work the time only increasing cold-producing medium, almost do not increase the interior energy of cold-producing medium, mechanical energy does not slattern as used heat or idle work greatly, so under the identical situation of refrigerating capacity, the power that the present invention is consumed in kind of refrigeration cycle is more much smaller than the power that steam compressing air conditioner device consumed, power approximately has only 1/2nd of steam compressing air conditioner device, and energy-saving effect is obvious.
Description of drawings
Fig. 1 connection diagram of the present invention.
Fig. 2 is the emitter construction schematic diagram.
Among the figure, 1, fluid reservoir, 2, filter, 3, regenerator, 4, expansion valve, 5, evaporimeter, 6, injector, 7, check valve, 8, condenser, 9, circulating pump, 10, first inlet, 11, first outlet, 12, second inlet, 13, second outlet, 14, outlet, 15, jet, 16, suction inlet, 17, mixing chamber, 18, the throat mouth, 19, the diffusion chamber, 20, suction chamber, 21, housing, 22, main burner, 23, inferior nozzle.
The specific embodiment
The present invention is described in further detail below in conjunction with description of drawings.
Injection type air-conditioner of the present invention, as shown in Figure 1, it comprises and is used for fluid reservoir 1, condenser 8, evaporimeter 5, regenerator 3, injector 6 and the circulating pump 9 of storage medium, and the jet 15 of injector 6 is connected with circulating pump 9 outlets, and the inlet of circulating pump 9 is connected with fluid reservoir 1 pipe; Pipe connects between regenerator 3 first outlets 11 and second inlet 12, is serially connected with evaporimeter 5 and expansion valve 4 on the pipeline respectively; First inlet 10 of regenerator 3 is connected with fluid reservoir 1 pipe, and second outlet 13 is connected with suction inlet 16 pipes of injector 6; The outlet 14 of injector 6, condenser 8, check valve 7, fluid reservoir 1 are managed connection successively; Contain refrigerant in fluid reservoir 1 and the pipeline.The refrigerant of present embodiment is high for fluorine chlorine.Circulating pump 9 and fluid reservoir 1 and regenerator 3 first the inlet 10 and fluid reservoir 1 between pipeline on be serially connected with filter 2 respectively.
Injector is ripe prior art, its structure as shown in Figure 2, it comprises housing 21, main burner 22 and inferior nozzle 23, an end of injector is a jet 15, the other end is outlet 14, the side is provided with suction inlet 16.Main burner 22 and time nozzle 23 are located at respectively in the two ends inner chamber of housing 21, are provided with suction chamber 20 between main burner 22 and the inferior nozzle 23.The passage of main burner 22 and time nozzle 23 is respectively equipped with mixing chamber 17, throat mouth 18 and diffusion chamber 19.
Regenerator also is ripe prior art, and coiled regenerator, tubular type regenerator in parallel, poling formula regenerator and bushing type regenerator are generally arranged, and regenerator is provided with first inlet, 10, second inlet, 12, first outlet, 11 and second outlet 13.
Circulating pump is the high pressure glandless motor pump, and the character of looking cold-producing medium can adopt diaphragm type or non-diaphragm pump.
Claims (2)
1. injection type air-conditioner, it is characterized in that it comprises fluid reservoir [1], condenser [8], evaporimeter [5], regenerator [3], injector [6] and circulating pump [9], the jet [15] of injector [6] is connected with circulating pump [9] outlet, and the inlet of circulating pump [9] is connected with fluid reservoir [1] pipe; Pipe connects between regenerator [3] first outlets [11] and second inlet [12], is serially connected with evaporimeter [5] and expansion valve [4] on the pipeline respectively; First inlet [10] of regenerator [3] is connected with fluid reservoir [1] pipe, and second outlet [13] is connected with the suction inlet pipe of injector [6]; The outlet [14] of injector [6], condenser [8], check valve [7], fluid reservoir [1] are managed connection successively; Contain refrigerant in fluid reservoir [1] and the pipeline.
2. injection type air-conditioner according to claim 1 is characterized in that being serially connected with filter [2] respectively on the pipeline between first inlet [10] and the fluid reservoir [1] of circulating pump [9] and fluid reservoir [1] and regenerator [3].
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200910116258A CN101813352A (en) | 2009-02-25 | 2009-02-25 | Jet-type air conditioner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200910116258A CN101813352A (en) | 2009-02-25 | 2009-02-25 | Jet-type air conditioner |
Publications (1)
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CN101813352A true CN101813352A (en) | 2010-08-25 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN200910116258A Pending CN101813352A (en) | 2009-02-25 | 2009-02-25 | Jet-type air conditioner |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108413637A (en) * | 2018-02-28 | 2018-08-17 | 中国科学院力学研究所 | A kind of industrial smoke waste heat recovery and dehumidification system |
CN108507212A (en) * | 2018-03-29 | 2018-09-07 | 重庆大学 | Jet stream two-phase heat exchange pump auxiliary system |
CN114698345A (en) * | 2022-04-11 | 2022-07-01 | 湖南创化低碳环保科技有限公司 | Jet type cooling system for chip and photovoltaic panel |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87101531A (en) * | 1987-04-06 | 1988-10-19 | 张洪玉 | Energy saving refrigeration installation for miniature cold storage |
CN2177621Y (en) * | 1993-12-23 | 1994-09-21 | 西安交通大学 | Energy-saving air-conditioner for vehicle and ship |
CN2191996Y (en) * | 1994-05-06 | 1995-03-15 | 坂田(天津)交通器材有限公司 | Jet-type air conditioner for vehicle and ship |
EP1607697A2 (en) * | 2004-06-09 | 2005-12-21 | Chen, Kuo-mei | Atomized liquid jet refrigeration system |
CN201355100Y (en) * | 2009-02-25 | 2009-12-02 | 王海 | Ejection-type air conditioner |
-
2009
- 2009-02-25 CN CN200910116258A patent/CN101813352A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87101531A (en) * | 1987-04-06 | 1988-10-19 | 张洪玉 | Energy saving refrigeration installation for miniature cold storage |
CN2177621Y (en) * | 1993-12-23 | 1994-09-21 | 西安交通大学 | Energy-saving air-conditioner for vehicle and ship |
CN2191996Y (en) * | 1994-05-06 | 1995-03-15 | 坂田(天津)交通器材有限公司 | Jet-type air conditioner for vehicle and ship |
EP1607697A2 (en) * | 2004-06-09 | 2005-12-21 | Chen, Kuo-mei | Atomized liquid jet refrigeration system |
CN201355100Y (en) * | 2009-02-25 | 2009-12-02 | 王海 | Ejection-type air conditioner |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108413637A (en) * | 2018-02-28 | 2018-08-17 | 中国科学院力学研究所 | A kind of industrial smoke waste heat recovery and dehumidification system |
CN108413637B (en) * | 2018-02-28 | 2019-02-26 | 中国科学院力学研究所 | A kind of recycling of industrial smoke waste heat and dehumidification system |
CN108507212A (en) * | 2018-03-29 | 2018-09-07 | 重庆大学 | Jet stream two-phase heat exchange pump auxiliary system |
CN108507212B (en) * | 2018-03-29 | 2021-05-14 | 重庆大学 | Jet flow two-phase heat exchange pump auxiliary system |
CN114698345A (en) * | 2022-04-11 | 2022-07-01 | 湖南创化低碳环保科技有限公司 | Jet type cooling system for chip and photovoltaic panel |
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Application publication date: 20100825 |