CN201589470U - Air-cooled evaporator for air source heat pump and liquid distributing system - Google Patents
Air-cooled evaporator for air source heat pump and liquid distributing system Download PDFInfo
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- CN201589470U CN201589470U CN2010201056444U CN201020105644U CN201589470U CN 201589470 U CN201589470 U CN 201589470U CN 2010201056444 U CN2010201056444 U CN 2010201056444U CN 201020105644 U CN201020105644 U CN 201020105644U CN 201589470 U CN201589470 U CN 201589470U
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Abstract
The utility model discloses an air-cooled evaporator for air source heat pump and a liquid distributing system, wherein the air-cooled evaporator has the characteristics of sufficient evaporation and high heat exchange efficiency. The air-cooled evaporator comprises an evaporator main body (1) and an axial flow fan (4) arranged on the evaporator main body. The liquid distributing system comprises a liquid distributor (3) and a plurality of capillary liquid distributing pipes (2) connected on the liquid distributor. The other end of each capillary liquid distributing pipe (2) is respectively connected to each evaporator in the evaporator main body (1). A distance is formed between the evaporators on both sides at the lower part of the evaporator main body (1). A section of the evaporator main body (1) along a longitudinal axis takes a shape of inverted trapezoid. The lengths of the capillary liquid distributing pipes (2) are gradually lengthened with decrease of an airflow speed along an inclined plane from top to bottom and the length of each capillary liquid distributing pipe is matched with linear distribution of the airflow speed. The bottom of the air-cooled evaporator of the utility model is not provided with an airflow dead zone. Each path of liquid refrigerant of the whole air-cooled evaporator is sufficiently evaporated.
Description
Technical field
The utility model relates to the air-cooled evaporimeter of a kind of air source heat pump and divides liquid systems.
Background technology
Air source heat pump is a kind of efficient energy conversion device, and it absorbs heat from air in the winter time, and by compressor work, it is heat of high temperature that the low-temperature heat quantity of air is promoted, and this heat is used for building winter heating and health hot water.Energy-conservation along with country, as to reduce discharging situation development, this efficient heat energy conversion equipment more and more obtain paying attention to and using.But because air source heat pump efficient decay under the low temperature condition in the winter time, wherein one of greatest factor is air-cooled evaporimeter because the separatory inequality time, it is inhomogeneous that the wind speed of air-cooled evaporimeter is crossed in circulation of air, causes air-cooled evaporator effectiveness low, and the heating effect of heat pump descends.The air-cooled evaporimeter of present air source heat pump normally " V " font arranges that top is provided with axial flow blower 4 (as shown in Figure 1), is characterized in this air-cooled evaporation structure compactness, and the refrigerating system coolant line arrangement is simple.But because this air-cooled evaporimeter " V " font arranges, the air stream of the top and the bottom by this evaporimeter is inhomogeneous.The heat transfer intensity of refrigerant and air is big in the air velocity height on the air-cooled evaporimeter of " V " type 1 top wherein, evaporimeter, and refrigerant fully evaporates, and is not with liquid.And form one " V air-flow dead band " in the lower part of air-cooled evaporimeter 1, and as a-quadrant among the figure, air velocity is low, and refrigerant and air heat transfer intensity are little in the heat exchanger, and refrigerant can not fully evaporate, and band liquid phenomenon is arranged.In addition, the length of each road capillary separating tube 2 of air-cooled evaporimeter 1 is equally long, vapour, the flow resistance of liquid two-phase refrigerant in capillary separating tube 2 after knockout 3 mixes and distributes are identical, its flow is also identical, cause the air-cooled evaporimeter of this " V " type lower part because air-flow is little, inadequate another key factor of refrigerant evaporation.Because the refrigerant evaporation in the air-cooled evaporimeter is insufficient, the heating effect of unit is poor, simultaneously, owing to there is not the liquid refrigerants of evaporation to suck compressor, cause the compressor liquid hammer, influenced the security and the reliability of compressor, compressor is with the liquid operation for a long time, its short in service life, and this is the difficult problem that the air source heat pump of the air-cooled evaporimeter of " V " type at present faces.
The utility model content
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, provides a kind of and evaporates the air-cooled evaporimeter abundant, that heat exchange efficiency is high and divide liquid systems.
The technical scheme that the utility model adopted is: the branch liquid systems of some the capillary separating tubes that the utility model comprises vaporizer body, is positioned at the axial flow blower on described vaporizer body top and comprises knockout and draws from knockout, the other end of described some capillary separating tubes is connected to each the road evaporimeter in the vaporizer body respectively, be provided with a segment distance between the evaporimeter of both sides, described vaporizer body bottom, the described vaporizer body longitudinally cross sectional shape of axis is down trapezoidal shape.
The branch liquid systems that comprises the knockout and some the capillary separating tubes of drawing is distributed to the capillary separating tube with the refrigerant in the pipeline and is entered each road evaporimeter on the vaporizer body, the length that is connected in some capillary separating tubes on the described vaporizer body is elongated gradually along with reducing of air velocity from top to bottom, and its separately length and the linear distribution of air velocity be complementary.Be that the separatory capillary is the shortest, branch liquid measure maximum is the air-cooled evaporimeter top first via, and the separatory capillary is the longest, the branch liquid measure is minimum to be a road of air-cooled base of evaporator, and middle separatory capillary pipe length is linear distribution.
The caliber of described some capillary separating tubes is identical.
The beneficial effects of the utility model are: owing to be provided with a segment distance between the evaporimeter of both sides, described vaporizer body bottom, the described vaporizer body longitudinally cross sectional shape of axis is down trapezoidal shape, so the air-cooled evaporimeter face velocity of this structure is linear distribution along air-cooled evaporimeter height, bottom air stream face velocity at air-cooled evaporimeter still satisfies the heat exchange requirement simultaneously, and comparing existing air-cooled evaporimeter does not have " V air-flow dead band ".Because the fluid on-way resistance is directly proportional with length under identical caliber condition, the separatory capillary pipe length is short, and the resistance that vapour, liquid two-phase refrigerant pass through is little, and its flow is big, and what be complementary with it is the cold evaporimeter of a transportation work style big by air velocity, that heat transfer intensity is big; Separating tube length is long, and the resistance that vapour, liquid two-phase refrigerant pass through is big, and its flow is little, and what be complementary with it is the road evaporimeter little by air velocity, that heat transfer intensity is little.According to the above-mentioned air-flow linear distribution that is down the air-cooled evaporimeter of trapezoidal shape, corresponding separatory capillary pipe length with tool also is linear distribution, the refrigerant that makes each road knockout of air-cooled evaporimeter distribute like this can both evaporate fully, realizes that whole air-cooled evaporimeter efficiently moves.
Description of drawings
Fig. 1 is the structural representation of the air-cooled evaporimeter of existing " V " type;
Fig. 2 is a structural representation of the present utility model.
The specific embodiment
As shown in Figure 2, the utility model comprises vaporizer body 1, be positioned at the axial flow blower 4 on described vaporizer body 1 top and some the capillary separating tubes 2 of drawing from knockout 3, the other end of described some capillary separating tubes 2 is connected to each the road evaporimeter in the vaporizer body 1 respectively, be provided with a segment distance between the evaporimeter of both sides, described vaporizer body 1 bottom, the described vaporizer body 1 longitudinally cross sectional shape of axis is down trapezoidal shape, the air-cooled evaporimeter face velocity of this structure is linear distribution along air-cooled evaporimeter height, while is in the bottom of air-cooled evaporimeter, i.e. B zone in the drawings, air stream face velocity still satisfies the heat exchange requirement, there be not " V air-flow dead band ", whole air-cooled evaporator effectiveness is not fully exerted, and the heating efficiency of air source heat pump is improved.
In addition, the length that is connected in some capillary separating tubes 2 on the described vaporizer body 1 is optimized design, elongated gradually from top to bottom along with reducing of air velocity, and its separately length and the linear distribution of air velocity be complementary.
The wind-cooled evaporator of above-mentioned inverted trapezoidal shape and the combination of the separatory capillary of optimization are so that wind-cooled evaporator heat transfer intensity and air velocity, the branch liquid measure is complementary, improved like this heat exchange efficiency of whole wind-cooled evaporator, part can both fully be evaporated with its underpart refrigerant on the wind-cooled evaporator, and the identical degree of superheat is arranged, guaranteed that the steam state refrigerant that enters compressor is not with liquid, service life and the security of compressor have been improved, it is low to have solved present " V " type wind-cooled evaporator air source heat pump winter operation efficient, the difficult problem of compressor liquid hammer, characteristics and advantages of the present utility model is embodied in:
1, the cross section is the wind-cooled evaporator of inverted trapezoidal so that air-flow is even by the speed of this evaporimeter, is linear distribution, does not have the air-flow dead band in the wind-cooled evaporator bottom, and whole wind-cooled evaporator efficient is not fully exerted, and improves the air source heat pump heating efficiency;
2, according to the wind-cooled evaporator air-flow characteristic distributions of cross section inverted trapezoidal, determine knockout and separatory separatory ability capillaceous, so that the heat transfer intensity of each road evaporimeter and its minute liquid measure be complementary, the liquid refrigerants on each road of whole wind-cooled evaporator is fully evaporated, have the identical degree of superheat, guarantee that the steam state refrigerant advances compressor and is not with liquid, improved air source heat pump compressor safety and reliability.
Claims (3)
1. air-cooled evaporimeter of air source heat pump, comprise vaporizer body (1), be positioned at the axial flow blower (4) on described vaporizer body (1) top, some capillary separating tubes (2) are connected to each the road evaporimeter in the vaporizer body (1) respectively, it is characterized in that: be provided with a segment distance between the evaporimeter of described vaporizer body (1) both sides, bottom, described vaporizer body (1) the longitudinally cross sectional shape of axis is down trapezoidal shape.
2. branch liquid systems that is complementary with the air-cooled evaporimeter of the described air source heat pump of claim 1, it is characterized in that: comprise knockout (3) and some the capillary separating tubes (2) of drawing by knockout (3), the other end of described some capillary separating tubes (2) is connected to respectively on the described vaporizer body (1), the length of described some capillary separating tubes (2) is elongated gradually along with reducing of air velocity from top to bottom along the inclined-plane of above-mentioned vaporizer body (1) both sides of falling trapezoidal shape, and its separately length and the linear distribution of air velocity be complementary.
3. minute liquid systems according to claim 2 is characterized in that: described some capillary separating tubes (2) caliber separately is identical.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010201056444U CN201589470U (en) | 2010-01-28 | 2010-01-28 | Air-cooled evaporator for air source heat pump and liquid distributing system |
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CN2010201056444U CN201589470U (en) | 2010-01-28 | 2010-01-28 | Air-cooled evaporator for air source heat pump and liquid distributing system |
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CN201589470U true CN201589470U (en) | 2010-09-22 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105352146A (en) * | 2015-12-01 | 2016-02-24 | 四川天地汇能环保科技有限公司 | Grid-plate-type V-shaped heat exchange device |
CN106839525A (en) * | 2015-12-07 | 2017-06-13 | 同方人工环境有限公司 | The wind heat exchanger structure and its control method of a kind of air cooled heat pump modular chiller |
CN108518896A (en) * | 2018-05-23 | 2018-09-11 | 南京佳力图机房环境技术股份有限公司 | A kind of air conditioner in machine room evaporator and air conditioner in machine room |
CN114623629A (en) * | 2022-04-16 | 2022-06-14 | 哈尔滨工业大学 | Equal-dryness dry evaporator with cyclone separation single-phase liquid equalizing hole throttling function |
-
2010
- 2010-01-28 CN CN2010201056444U patent/CN201589470U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105352146A (en) * | 2015-12-01 | 2016-02-24 | 四川天地汇能环保科技有限公司 | Grid-plate-type V-shaped heat exchange device |
CN105352146B (en) * | 2015-12-01 | 2019-02-05 | 四川天地汇能环保科技有限公司 | A kind of Turbogrid plates Formula V type heat-exchanger rig |
CN106839525A (en) * | 2015-12-07 | 2017-06-13 | 同方人工环境有限公司 | The wind heat exchanger structure and its control method of a kind of air cooled heat pump modular chiller |
CN108518896A (en) * | 2018-05-23 | 2018-09-11 | 南京佳力图机房环境技术股份有限公司 | A kind of air conditioner in machine room evaporator and air conditioner in machine room |
CN108518896B (en) * | 2018-05-23 | 2024-04-19 | 南京佳力图机房环境技术股份有限公司 | Computer lab air conditioner evaporimeter and computer lab air conditioner |
CN114623629A (en) * | 2022-04-16 | 2022-06-14 | 哈尔滨工业大学 | Equal-dryness dry evaporator with cyclone separation single-phase liquid equalizing hole throttling function |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100922 Termination date: 20140128 |