CN204494657U - Hypergravity air conditioner - Google Patents
Hypergravity air conditioner Download PDFInfo
- Publication number
- CN204494657U CN204494657U CN201420861551.2U CN201420861551U CN204494657U CN 204494657 U CN204494657 U CN 204494657U CN 201420861551 U CN201420861551 U CN 201420861551U CN 204494657 U CN204494657 U CN 204494657U
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- Prior art keywords
- cooling fluid
- bucket
- heat exchange
- air
- hypergravity
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Abstract
The utility model discloses a kind of hypergravity air conditioner, comprise the heat exchange bucket that upper end has opening, heat exchange bucket is provided with air-intake device, cooling air exhaust apparatus and cooling fluid storage device, be provided with in described heat exchange bucket and can the cooling fluid that cooling fluid storage device is carried carried out discrete, the hypergravity cooling fluid atomising device of atomization, the utility model adopts such scheme, utilize hypergravity atomising device that cooling fluid is sheared dispersion and form high-speed motion liquid mist, the air that the countercurrent screw produced with heat exchange bucket and air-intake device moves directly contacts unique flow behavior, by strengthening cooling fluid and air heat transfer area, increase relative velocity, increase the number of times that contacts with each other, achieve cooling fluid and Efficient air caloic exchanges.
Description
Technical field
The utility model relates to a kind of air conditioner, relates to a kind of hypergravity air conditioner specifically, is applicable to the various industrialized agricultures such as vegetables, fruit tree, flowers, herding.
Background technology
At present, in the various industrialized agricultures such as vegetables, fruit tree, flowers, herding, under the environment of sweltering heat in summer, the temperature of general employing air conditioner to indoor is lowered the temperature, its operation principle is that outdoor fresh air sends into indoor continuously after vaporizing type air conditioner filters and lowers the temperature, and by indoor with outside the higher turbid air discharge chamber of peculiar smell, dust, temperature, make indoor temperature be reduced, improve the oxygen content of air, improve air quality.Therefore, vaporizing type air conditioner can reach the double effects of cooling and ventilation.
At present, in order to increase cooling-down effect, multilayer corrugated fiber applications as laminates is added in air conditioner inside--wet curtain, when unsaturated air flows through porous, moistening wet curtain surface, large quantity of moisture evaporates, the sensible heat embodied by temperature in air is converted into evaporation latent heat, thus reduces the temperature of air self.There is good water absorbing properties and ventilation, filtering function.
But this structure has following defect:
One is that in wet curtain air conditioner, wet curtain paper surface area is also enough large, on wet curtain paper moisture film and air exchange area few, affect heat exchange effect.
Two is because wet curtain paper needs a large amount of cooling waters moistening, fully can not evaporate, waste a large amount of water resources.
Three is high to water quality requirement, and wet curtain paper is afraid of that sun, easily fouling, life-span are short, the hole of the dust in air also easily on the wet curtain of blocking.
Utility model content
Problem to be solved in the utility model is the above-mentioned defect in order to overcome traditional air conditioner, provides one to economize on resources, and can ensure again the hypergravity air conditioner of good cooling effect.
In order to solve the problem, the utility model by the following technical solutions:
A kind of hypergravity air conditioner, comprise the heat exchange bucket that upper end has opening, heat exchange bucket is provided with air-intake device, cooling air exhaust apparatus and cooling fluid storage device, is provided with in described heat exchange bucket and the cooling fluid that cooling fluid storage device is carried can be carried out hypergravity cooling fluid atomising device that is discrete, atomization.
Below the further optimization of the utility model to such scheme:
Hypergravity cooling fluid atomising device comprise be arranged in heat exchange bucket and be in transmission connection with power set get rid of bucket, get rid of bucket to be communicated with cooling fluid storage device, described getting rid of in bucket is filled with filament shape filler, get rid of bucket when rotating under the effect of power set, the cooling fluid through filament shape filler can be carried out disperseing, being atomized.Form fine droplet, absorb the heat in air, the air of turnover heat exchange bucket is cooled.
Further optimization: cooling air exhaust apparatus comprises the side that is arranged on heat exchange bucket and is positioned at the axial flow blower getting rid of barrel lower position.
Further optimization: cooling fluid storage device comprise the side that is arranged on heat exchange bucket and with the feed pipe getting rid of bucket inside and be communicated with.
Power set comprise the motor of the opening part being arranged on heat exchange bucket, and described motor is provided with power output shaft, the lower end of described power output shaft with get rid of bucket and be connected.
Air-intake device comprises some blades of the upper end open position being arranged on heat exchange bucket, and the air of heat exchange bucket outside is also led in heat exchange bucket by some blade rotation directions.Blade is horizontal by 25 ° of angles, and the rotation direction of blade is contrary with cooling fluid atomising device rotation direction.
The position of axial flow blower inside heat exchange bucket is provided with air inlet, and at air inlet, place is provided with shutter.
The position of the outside side near lower end of heat exchange bucket is provided with the liquid level gauge for observing the liquid level in heat exchange bucket.For observing the liquid level in heat exchange bucket, and control drain pipe discharge at any time in order to ensure that the liquid level in heat exchange bucket is in optimum state.
The utility model adopts such scheme, utilize hypergravity atomising device that cooling fluid is sheared dispersion and form high-speed motion liquid mist, the air that the countercurrent screw produced with heat exchange bucket and air-intake device moves directly contacts unique flow behavior, by strengthening cooling fluid and air heat transfer area, increase relative velocity, increase the number of times that contacts with each other, achieve cooling fluid and Efficient air caloic exchanges.
The utility model adopts such scheme, has the following advantages:
1, oblique air intake is adopted can to improve the flow velocity of air, improve the swap time of air and cooling fluid.
2, employing gets rid of fog-forming technique outside bucket, the favourable raising droplet flight time, directly improves the swap time of air and cooling fluid.
3, adopt axial flow blower air-breathing air draft technology, can mass air flow rate be increased, and make liquid mist interface produce certain negative pressure, be conducive to the evaporation of liquid mist.
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of hypergravity air conditioner in the utility model embodiment;
Accompanying drawing 2 is the top view of accompanying drawing 1;
Accompanying drawing 3 is the fundamental diagram of hypergravity cooling fluid atomising device in the utility model embodiment.
In figure: 1-motor; 2-motor cabinet; 3-power output shaft; 4-feed pipe; 5-liquid feed valve; 6-heat exchange bucket; 7-filler; 8-gets rid of bucket; 9-drain pipe; 10-supporting leg; 11-air inlet; 12-axial flow blower; 13-blade; 14-liquid level gauge; 15-shutter.
Detailed description of the invention
Embodiment, as shown in Figure 1 and Figure 2, hypergravity air conditioner, comprise the heat exchange bucket 6 that upper end has opening, lower end is provided with drain pipe 9, the bottom of heat exchange bucket 6 is supported by supporting leg 10, heat exchange bucket 6 is provided with air-intake device, cooling air exhaust apparatus and cooling fluid storage device, the hypergravity cooling fluid atomising device that the cooling fluid that cooling fluid storage device is carried can be carried out disperseing, being atomized is installed in described heat exchange bucket 6.
Hypergravity cooling fluid atomising device comprise be arranged in heat exchange bucket 6 and be in transmission connection with power set get rid of bucket 8, get rid of bucket 8 to be communicated with cooling fluid storage device, described getting rid of in bucket 8 is filled with filler 7, the excircle getting rid of bucket 8 is provided with stainless (steel) wire, get rid of bucket 8 when rotating under the effect of power set, the cooling fluid through filler 7 can be carried out disperseing, be atomized, formation fine droplet, absorb the heat in air, the air of turnover heat exchange bucket 6 is cooled.
Filler is as the pith of super gravity field cooling fluid atomising device, the rotor dosing filler of the utility model employing adopts center to be cooling fluid storage device, the circumferencial direction of cooling fluid storage device is filler, has larger difference with traditional rotor or rotating disk:
One is the thin liquidus sprayed by spray hole, directly contacts with the filler of High Rotation Speed, and thin liquidus is in filling surface diffusion or broken.
Two is that cooling fluid is accelerated motion in filler due to super gravity field effect, and the high shear force of filler is divided into the liquid film of certain linear velocity, brin and drop cooling fluid.
Three is huge surface area of filler, and when contacting with cooling fluid, liquid phase is dispersed into film or fine droplet further, and pole improves the phase contact area of cooling fluid with adding.
The performance quality of filler directly affects super gravity field cooling fluid atomising device dynamic balance, equation, nebulization efficiency and service life.For filling-material structure, the material of filling-material structure, percent opening, aperture, thickness, the series of parameters such as space and bulk density can affect the equation performance such as thickness of the film-formation result of liquid in filler, film forming.
At present, to filling-material structure research less, mainly concentrate on silk screen and porous material in bulk, but silk screen and Porous materials balance in bulk poor, long-term running can cause density inside and outside filler to differ to causing, and has a strong impact on all even mist formation effect of liquid flow movement.
For strengthening filler is to the equation such as dispersion, shearing of cooling fluid, take into full account the series of parameters such as filler balance, life-span, intensity, percent opening, aperture, thickness, space, density and cost, choosing in filler and structure, using for reference hairbrush production technology and technique.Material is chosen the filament that rigidity is strong, and it is be placed on well by filament alignment in circular mould that structure adopts, and then adopts injection moulding filament and circular base plate to be fused into one, is placed on and gets rid of in bucket 8.
Cooling air exhaust apparatus comprises the side that is arranged on heat exchange bucket 6 and is positioned at the axial flow blower 12 getting rid of bucket 8 lower position.
Cooling fluid storage device comprise the side that is arranged on heat exchange bucket 6 and with the feed pipe 4 getting rid of bucket 8 inside and be communicated with.Feed pipe 4 is provided with liquid feed valve 5.
Feed pipe 4 is fixed on air conditioner shell, and the hydrojet end of feed pipe 4 is provided with several needle-like spray orifices, and feed pipe 4 does not move with the rotation of getting rid of bucket.
Cooling fluid flies out from getting rid of bucket from entering hypergravity atomising device to formation mist droplet, mainly contains three processes.
Process one: cooling fluid is sprayed by several needle-like spray orifices on feed pipe, and cooling fluid extrudes spray orifice by hydraulic pressure, is 1.5-2.5mm jet from spray orifice ejection diameter, achieves the refinement first to cooling fluid.
Process two: after filler receives spray orifice jet, cooling fluid spreads thinning at filling surface further, and cooling fluid jet permeates in filler with pressure itself.After cooling fluid jet approximately passes through the filler of about 10mm, all reach the angular speed identical with filler, cooling fluid at this moment mainly exists with the form of liquid film.
Process three: cooling fluid jet is filled catch completely after, High Rotation Speed together with filler, constantly accelerates outwardly, continuous filled shearing splitting, forms mist droplet and is pulled out away from and gets rid of bucket.
Find out from three processes above, the link of the most crux of cooling fluid atomization quality, in the 3rd process, is the significant shear power shattering process that cooling fluid is produced by super gravity field.Have rigidity filament owing to adopting in packing box, the diameter of silk is several microns, and packing box radial direction has hundreds of root filament.Cooling fluid, under hypergravity effect, is passed through filament and is tamped layer, will repeatedly be sheared, the droplet that final formation is small.
Suppose, cooling fluid is passed through filament and is tamped layer and can effectively shear for about 30 times (liquid-drop diameter is less than filament diameter can not be divided to a certain extent) again, and so cooling fluid is split into more than 10 hundred million parts.If drop mass is 1mg when cooling fluid caught by filler.
So,
× π ×
× ρ=
× π ×
× ρ
=1mg
diameter when drop filler is caught,
for diameter when drop flies away from filler;
Calculate:
=1.24mm,
=1.24 ×
mm
Can find out that cooling fluid is in super gravity field, after filling out the shearing of filament packing layer, the diameter of the liquid droplet of formation reaches micron order.Drop large like this forms enough large total heat transfer surface area, improves cooling fluid and air heat and mass efficiency.
Power set comprise the motor 1 of the opening part being arranged on heat exchange bucket 6, and described motor 1 is provided with power output shaft 3, the lower end of described power output shaft 3 with get rid of bucket 8 and be connected.
Air-intake device comprises the some blades 13 of the upper end open position being arranged on heat exchange bucket 6, every sheet blade two fixing points, makes blade horizontal by about 25 ° of angles.The rotation direction of blade is contrary with cooling fluid atomising device rotation direction, so just forces air to make helical flow in bucket.Which adds the swap time of water smoke and air, too increase the path of exchange simultaneously.
The position of axial flow blower 12 inside heat exchange bucket 6 is provided with air inlet 11, and at air inlet 11, place is provided with shutter 15.
The position of the outside side near lower end of heat exchange bucket 6 is provided with the liquid level gauge 14 for observing the liquid level in heat exchange bucket 6.For observing the liquid level in heat exchange bucket 6, and control drain pipe 9 discharges to ensure that the liquid level in heat exchange bucket 6 is in optimum state at any time.
The utility model adopts such scheme, as shown in Figure 3, during work, turns on the power switch and liquid feed valve 5, and alternating current generator 1 starts to rotate under transducer drive, and rotating speed is adjustable at 900-1390 rev/min, and drives hypergravity cooling fluid atomising device High Rotation Speed.
Cooling fluid is led to after supercooled liquid feeding device first carries out refinement, broken further on the filler being ejected into cooling fluid atomising device equably.
Cooling fluid filled 7 seizure in very short time realize synchronous axial system, under High Rotation Speed cooling fluid atomising device produces the effect of about 140g ~ 330g super gravity field, constantly do accelerated motion, through filament shape filler in cooling fluid accelerated motion, cooling fluid is often through a filament shape filler, filament shape filler is just sheared cooling fluid, cooling fluid is sheared through filament shape filler hundreds of, cooling fluid is first with shaped liquid film, again with liquidus shape, after become fine drop, the movement velocity arriving drop during cooling fluid atomising device edge reaches 14 ~ 20.4 meter per seconds, last drop is radially dished out by cooling fluid atomising device stainless (steel) wire and is formed tiny liquid mist.
Axial flow blower 12 adopts rotating speed 2900rpm, air quantity 6000
/ h, blast 260pa, power 0.75kw.Axial flow blower;
Adopt negative inspiratory pressure mode, air, through some blades 13 rotation direction of the upper end open position of heat exchange bucket 6, forces air to make helical flow in bucket.The reverse mist layer through being formed by cooling fluid of the air molecule of helical flow, achieves fully contacting of air molecule and cooling fluid, completes cooling and air, High Efficiency Thermal mass transter.
The utility model adopts such scheme, has the following advantages:
1, adopt hypergravity atomization technique, cooling fluid can be dispersed into micron-sized drop, form enough large total heat transfer surface area, cooling fluid and air heat and mass efficiency improve 2-3 orders of magnitude.
2, adopt hypergravity atomization technique, the movement velocity of cooling fluid droplet can be made to reach 14 ~ 20.4 meter per seconds, can not be taken away by high velocity air.
3, oblique air intake is adopted can to improve the flow velocity of air, improve the swap time of air and cooling fluid.
4, employing gets rid of fog-forming technique outside bucket, the favourable raising droplet flight time, directly improves the swap time of air and cooling fluid.
5, adopt large power shaft flow fan air-breathing air draft technology, can mass air flow rate be increased, and make cooling fluid interface produce certain negative pressure, be conducive to the evaporation of water smoke.
6, hypergravity heat exchange process, the consumption of the cooling fluid that can make greatly reduces, and has saved a large amount of resources.
In above-described embodiment, described cooling fluid both can adopt conventional chilling liquid, and water also can be adopted as cooling fluid.
Claims (10)
1. a hypergravity air conditioner, comprises the heat exchange bucket (6) that upper end has opening, heat exchange bucket (6)
On air-intake device, cooling air exhaust apparatus and cooling fluid storage device are installed, it is characterized in that: be provided with in described heat exchange bucket (6) and the cooling fluid that cooling fluid storage device is carried can be carried out the hypergravity cooling fluid atomising device that disperses, be atomized.
2. hypergravity air conditioner according to claim 1, is characterized in that: hypergravity cooling fluid atomising device comprise be arranged in heat exchange bucket (6) and be in transmission connection with power set get rid of bucket (8), get rid of bucket (8) and be communicated with cooling fluid storage device.
3. hypergravity air conditioner according to claim 2, is characterized in that: described in get rid of in bucket (8) and be filled with filler (7), get rid of bucket (8) when rotating under the effect of power set, the cooling fluid through filler (7) can be carried out disperseing, being atomized.
4. the hypergravity air conditioner according to Claims 2 or 3, is characterized in that: cooling air exhaust apparatus comprises the side that is arranged on heat exchange bucket (6) and is positioned at the axial flow blower (12) getting rid of bucket (8) lower position.
5. hypergravity air conditioner according to claim 4, is characterized in that:
Cooling fluid storage device comprise the side that is arranged on heat exchange bucket (6) and with the feed pipe (4) getting rid of bucket (8) inside and be communicated with.
6. hypergravity air conditioner according to claim 5, is characterized in that:
Power set comprise the motor (1) of the opening part being arranged on heat exchange bucket (6), described motor (1) are provided with power output shaft (3), the lower end of described power output shaft (3) with get rid of bucket (8) and be connected.
7. hypergravity air conditioner according to claim 6, is characterized in that:
Air-intake device comprises the some blades (13) of the upper end open position being arranged on heat exchange bucket (6), and the air of heat exchange bucket outside can be led in heat exchange bucket (6) by some blades (13).
8. hypergravity air conditioner according to claim 7, is characterized in that:
Blade (13) is horizontal by 25 ° of angles, and the rotation direction of blade (13) is contrary with cooling fluid atomising device rotation direction.
9. hypergravity air conditioner according to claim 8, is characterized in that:
Axial flow blower (12) is provided with air inlet (11) near the position of heat exchange bucket (6) inner side, is provided with shutter (15) at air inlet (11) place.
10. hypergravity air conditioner according to claim 9, is characterized in that:
The position of the outside side near lower end of heat exchange bucket (6) is provided with the liquid level gauge (14) for observing the liquid level in heat exchange bucket (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861551.2U CN204494657U (en) | 2014-12-31 | 2014-12-31 | Hypergravity air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861551.2U CN204494657U (en) | 2014-12-31 | 2014-12-31 | Hypergravity air conditioner |
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| Publication Number | Publication Date |
|---|---|
| CN204494657U true CN204494657U (en) | 2015-07-22 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420861551.2U Expired - Fee Related CN204494657U (en) | 2014-12-31 | 2014-12-31 | Hypergravity air conditioner |
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| Country | Link |
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| CN (1) | CN204494657U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104534596A (en) * | 2014-12-31 | 2015-04-22 | 山东中昊重工科技有限公司 | Super-gravity air conditioner |
-
2014
- 2014-12-31 CN CN201420861551.2U patent/CN204494657U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104534596A (en) * | 2014-12-31 | 2015-04-22 | 山东中昊重工科技有限公司 | Super-gravity air conditioner |
| CN104534596B (en) * | 2014-12-31 | 2017-08-29 | 山东忠昊重工科技有限公司 | A kind of hypergravity air conditioner |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CGPU | Change to patent or to utility model | ||
| CU01 | Correction of utility model patent |
Correction item: First patent holder Correct: Shandong loyal Heavy Industry Technology Co., Ltd. False: SHANDONG ZHONGHAO HEAVY TECHNOLOGY CO., LTD. Number: 29 Page: The title page Volume: 31 |
|
| CU03 | Correction of utility model patent gazette |
Correction item: First patent holder Correct: Shandong loyal Heavy Industry Technology Co., Ltd. False: SHANDONG ZHONGHAO HEAVY TECHNOLOGY CO., LTD. Number: 29 Volume: 31 |
|
| ERR | Gazette correction | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150722 Termination date: 20151231 |
|
| EXPY | Termination of patent right or utility model |