CN207140661U - A kind of fountain is atomized potted landscape - Google Patents
A kind of fountain is atomized potted landscape Download PDFInfo
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- CN207140661U CN207140661U CN201720855732.8U CN201720855732U CN207140661U CN 207140661 U CN207140661 U CN 207140661U CN 201720855732 U CN201720855732 U CN 201720855732U CN 207140661 U CN207140661 U CN 207140661U
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- fountain
- sprayer unit
- spout
- atomization
- water
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Abstract
The utility model discloses a kind of fountain to be atomized potted landscape, the present apparatus includes sprayer unit, fountain apparatus, landscape device, water vat, diving pipeline, immersible pump, air compressor, sprayer unit of the present utility model makes the atomization of liquid and the smashing principle of drop using compressed air, present apparatus applied fluid mechanics principle, using compressed air as power, effect of the water smoke through jet is ejected into air rapidly, the globule is changed into gaseous state from liquid, it is absolute to space progress uniformly to be humidified without water droplet, press dirt, hydrojet, electrostatic can be eliminated in humidification, and the simple and convenient connection working media of control can work, energy consumption is low, atomizing effect is good, cost is cheap.
Description
Technical field
The utility model belongs to family's humidification device field, more particularly to a kind of fountain atomization potted landscape.
Background technology
With the arriving in summer, room air is dried further.Drying is the formidable enemy of health, and it can not only make one internal water
It is a large amount of to be lost in, cause tight skin, dry mouth and parching tongue, harelip, excessive internal heat etc., moreover it is possible to cause the breathing problems such as influenza.Room air
Drying can also damage to implements such as furniture, floor, household electrical appliances, reduce service life.In current in the market, indoor potted landscape
Individual character different expressions, it is fascinating, but function phase is to poor in the application of family.As for the potted landscape used among family not
Only there is the function that the beautiful scenery for making us pleasing will also be advantageous to health, so can just there is the effect made something perfect even more perfect.
Ultrasonic humidifying is in the market humidification method the most universal, and its intensity is big, and humidification is uniform, and humidification efficiency is high；Energy-conservation, power saving；
Long service life；Humidity autobalance, anhydrous automatic protection；Have the functions such as medical treatment atomization, cold compress bath face, cleaning jewellery concurrently.
For sprayer unit, atomization is to evaluate the mostly important index of its practical value.The mist of sprayer unit
Change performance, not only decide the distribution of droplet drop-size distribution, and be related to the aerial discharge capacity of liquid mist, it is directly affected
Air wetting effect.When studying the atomization of sprayer unit, it is necessary first to the broken mechanism of droplet is theoretically analyzed,
Droplet motion analysis and its influence factor are studied, finds out the principal element for influenceing droplet sizes and uniformity；Secondly, for spraying
The mobility status of device flow field, the design requirement of nozzle and the flow parameter of image atomization are found out, and find rational numerical value
Derivation algorithm.
The content of the invention
The shortcomings that the utility model overcomes in the prior art, there is provided a kind of fountain is atomized potted landscape.
In order to solve the above-mentioned technical problem, the utility model is achieved through the following technical solutions：
A kind of fountain is atomized potted landscape, including sprayer unit, fountain apparatus, landscape device, water vat, diving pipeline, latent
Water pump, air compressor；Diving pipeline is connected with immersible pump, and air compressor is connected by pipeline with sprayer unit, spraying dress
Put, fountain apparatus, landscape device arranged adjacent be in water vat；
Wherein, sprayer unit includes outer, top cylinder, baffle plate, tube wall, cone tank, base, water on upper cover body, cylinder
Pipe, shrinkage type jet pipe, inlet opening, conical pipe, buckle, conical cavity, nebulization chamber and dispersive nozzle, sprayer unit are in integrally cylinder
Shape, is divided into top tube structure and lower cylinder structure, and the two is suspended on cylinder on outer by upper cover body, and passes through buckle
Connection；
Top tube structure is made up of upper cover body, top cylinder, baffle plate and shrinkage type jet pipe, and upper cover body is arranged at top cylinder
The top of body, the bottom of top cylinder set baffle plate and shrinkage type jet pipe；Nebulization chamber is formed between baffle plate and shrinkage type jet pipe,
Shrinkage type jet pipe is the bell-mouth structure of air that upper end is tightened up, and lower section is entrance, and top is outlet, and the inlet diameter is 2-8mm, is gone out
The a diameter of 0.1-0.3mm of mouth, top are that dispersive nozzle lower cylinder structure is made up of conical pipe, water pipe and cone tank, conical pipe
It is arranged in cone tank, water pipe is arranged at the lower section of cone tank, in the inside of tube wall, is provided with above the upper edge of cone tank
(it is to provide water source for humidification that it, which is acted on, and hole will exceed tapered kerve, be advantageous to making full use of for water for inlet opening.Bottom is set
The water in pipe can be placed in higher water level to be fully used for tapered groove)；
Wherein, fountain apparatus include spout block, spout, spout connecting seat, interface block, interface, center con and
Horizontal pipeline, center con are provided at both ends with horizontal pipeline, and the upper end of center con is provided with interface, the interface
Upper end is provided with interface block, and horizontal pipeline is provided at both ends with spout connecting seat, and the upper end of spout connecting seat is provided with spout,
The upper end of the spout is provided with spout block；
In the above-mentioned technical solutions, a kind of sprayer unit of described fountain atomization potted landscape utilizes lightweight material system
Into total quality 10-20kg.
In the above-mentioned technical solutions, described landscape device is decoration artificial hillock or other ornamental landscapes, for being arranged in
Indoor purifying indoor environment.
In the above-mentioned technical solutions, the height of described top tube structure is the 1/3-1/2 of overall sprayer unit height.
In the above-mentioned technical solutions, ball float is provided with the outer wall of described sprayer unit, for device to be flown at into water
Face, it is allowed to fluctuate with the increase and decrease of water level.
In the above-mentioned technical solutions, the fogdrop diameter formed in described nebulization chamber is at 3-8 μm.
In the above-mentioned technical solutions, the size of described fountain atomising device is：Long 50-70cm, wide 30-50cm, high 30-
50cm。
In the above-mentioned technical solutions, the inlet diameter of the shrinkage type jet pipe is 4-6mm, outlet diameter 0.1-0.2mm.
Compared with prior art, the beneficial effects of the utility model are：Sprayer unit of the present utility model is using pressure
Contracting air makes the atomization of liquid and the smashing principle of drop, present apparatus applied fluid mechanics principle, using compressed air as power,
Effect of the water smoke through jet is ejected into air rapidly, and the globule is changed into gaseous state from liquid, and definitely equal without water droplet is carried out to space
Even humidification, pressure dirt, hydrojet, can eliminate electrostatic in humidification, and control simple and convenient connection working media to work, energy
Consume low, atomizing effect is good, and cost is cheap.
Brief description of the drawings
Fig. 1 is sprayer unit overall structure diagram in the utility model.
Fig. 2 is the utility model sprayer unit lower cylinder planar structure schematic diagram.
Fig. 3 is the utility model sprayer unit top cylinder planar structure schematic diagram.
Fig. 4 is shrinkage type jet pipe sectional perspective structural representation in the utility model.
Fig. 5 is fountain apparatus structural representation in the utility model.
Fig. 6 is the utility model overall structure diagram.
1 is upper cover body, and 2 be outer on cylinder, and 3 be top cylinder, and 4 be baffle plate, and 5 be tube wall, and 6 be cone tank, and 7 be bottom
Seat, 8 be water pipe, and 9 be shrinkage type jet pipe, and 10 be inlet opening, and 11 be conical pipe, and 12 be buckle, and 13 be conical cavity, and 14 be atomization chamber
Room, 15 be spout, and 16 be spout block, and 17 be dispersive nozzle, and 18 be spout connecting seat, and 19 be interface block, and 20 be interface, 21
Centered on connector, 22 be horizontal pipeline, and 23 be sprayer unit, and 24 be landscape device, and 25 be fountain apparatus, and 26 be snorkle
Road, 27 be water vat, and 28 be air compressor.
Embodiment
The utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings：
As shown in FIG., a kind of fountain atomization potted landscape, including sprayer unit, fountain apparatus, landscape device, water vat,
Diving pipeline, immersible pump, air compressor composition；Diving pipeline is connected with immersible pump, and air compressor passes through pipeline and spraying
Device is connected, and sprayer unit, fountain apparatus, landscape device arranged adjacent are in water vat；
Wherein, sprayer unit includes outer, top cylinder, baffle plate, tube wall, cone tank, base, water on upper cover body, cylinder
Pipe, shrinkage type jet pipe, inlet opening, conical pipe, buckle, conical cavity, nebulization chamber and dispersive nozzle, sprayer unit are in integrally cylinder
Shape, is divided into top tube structure and lower cylinder structure, and the two is suspended on cylinder on outer by upper cover body, and passes through buckle
Connection；
Top tube structure is made up of upper cover body, top cylinder, baffle plate and shrinkage type jet pipe, and upper cover body is arranged at top cylinder
The top of body, the bottom of top cylinder set baffle plate and shrinkage type jet pipe；Nebulization chamber is formed between baffle plate and shrinkage type jet pipe,
Shrinkage type jet pipe is the bell-mouth structure of air that upper end is tightened up, and lower section is entrance, and top is outlet, and the inlet diameter is 5mm, outlet
A diameter of 0.2mm, top are that dispersive nozzle lower cylinder structure is made up of conical pipe, water pipe and cone tank, and conical pipe is arranged at
In cone tank, water pipe is arranged at the lower section of cone tank, in the inside of tube wall, is provided with above the upper edge of cone tank into water
Hole；
Wherein, fountain apparatus include spout block, spout, spout connecting seat, interface block, interface, center con and
Horizontal pipeline, center con are provided at both ends with horizontal pipeline, and the upper end of center con is provided with interface, the interface
Upper end is provided with interface block, and horizontal pipeline is provided at both ends with spout connecting seat, and the upper end of spout connecting seat is provided with spout,
The upper end of the spout is provided with spout block；
In the above-mentioned technical solutions, a kind of sprayer unit of described fountain atomization potted landscape utilizes lightweight material system
Into total quality 20kg.
In the above-mentioned technical solutions, ball float is provided with the outer wall of described sprayer unit, for device to be flown at into water
Face, it is allowed to fluctuate with the increase and decrease of water level.
In the above-mentioned technical solutions, the fogdrop diameter formed in described nebulization chamber is at 5 μm.
In the above-mentioned technical solutions, the size of described fountain atomising device is：Long 60cm, wide 40cm, high 40cm.
Sprayer unit principle of device：
There is mass transport problem for air compression.Momentum or energy transmission are carried out in the fluid of half component.Production
The reason for raw this transmission is due to occur local velocity or temperature difference in flow field, so that the fluid in high speed or high-temperature area
It is the speed of fluid or temperature has the trend gradually balanced by kinetic energy or energy transmission to low velocity or low temperature area, and quality
Transmission is carried out in the multicomponent mixture that gas, liquid and soluble solids etc. are formed, when one kind in mixture
Or various ingredients are in flow field when there is local concentration difference, each component is relative and mixture, from high concentration region by mass transfer
To the trend of low concentration region, the concentration of a component in flow field is set gradually to balance.
From the viewpoint of engineering, mass transfer generally occurs on the interface of each component, Gu as gas-solid, gas-liquid, liquid-
One of which.Turbulent flow (or) eddy diffusion, in turbulent motion, fluid particle except with when move in addition to, also have random
Fluctuation campaign, this motion has similarity with molecular motion, but substantially then identical, the latter is that the structure of matter is consolidated
Have, and the former still has caused by flow behavior, it is similar with momentum and energy transmission.The random fluctuation of speed and concentration can be significantly
The efficiency of raising mass transfer or drastically enhanced diffustion ability, it is generally recognized that these fluctuation campaigns have close with the whirlpool motion in turbulent flow
Relation is cut, therefore eddy diffusion is also known as by the caused diffusion coefficient of fluctuation campaign., be from because amount of turbulence is a kind of complicated flowing
Theoretical or experiment determines that the Universality between eddy diffusivity and time-average flow amount is highly difficult up, because it is not only right
Difference flowing has different values, even if to same flowing, also has different values from the time in different positions.
The transmission of the design principle and quality of compressed air sprayer unit also has close relationship.
Compressed air does not expand completely in nozzle, and jet is for free expanding jet.
With air momentum-exchange, heat exchange occur for jet.Because effluxvelocity is larger, and jet expansion upstream airflow has
Disturbance, tangential section is unstable, whirlpool occurs on the section, and these whirlpools do irregular motion in flowing, thus send out
Transverse momentum exchange, heat exchange between raw micelle, so as to form turbulent jet boundary layer.It is rapid with the increase of outlet distance
After laminar boundary layer constantly increases, the axis speed of jet constantly declines, and drops to subsonic speed from supersonic speed, supersonic jet decays to Asia
After velocity of sound, no shock wave parallel jet can be regarded as.
With surrounding static air momentum-exchange occurs for jet during exercise, and air is constantly involved in jet mixing area, plus super
Velocity of sound jet is in certain radial penetrating air, and therefore, jet just has lateral velocity, but compared with longitudinal velocity, lateral velocity
Very little, so, streamline near jet-core region is close to parallel, it is believed that effluxvelocity vertically, which can characterize, entirely penetrates
The velocity characteristic of stream.
Spout state
Gaseous state in compressor can be considered stagnation state：
According to isentropic procedure energy equation：
Wherein：k:Isentropic index air is 1.4R:Gas constant air is 287J/ (kg.k)
Or
Or
Relation between the parameter and stagnation parameter of section：
Formula (3-5) is rewritten as：
Had by formula (3-7)：
According to isentropic procedure equation p/ ρk=C, state equation p/ ρ=RT and formula (3-7), export：
Critical condition：
Obtained according to energy equation (3-6)：
Above formula shows, during the insulation flow of gas, with the increase of air velocity, local velocity of sound reduces, and works as gas
Stream is accelerated to limit velocity vmaxWhen, local velocity of sound drops to zero；And when air velocity by stagnation to zero when, local velocity of sound is then
Rise to stagnation velocity of sound C0.Therefore, air velocity have it is small become big and local velocity of sound from large to small during, must occur
Air velocity v is exactly equal to local velocity of sound C, i.e. Ma=1 state.Namely design state.
Ma=1 is substituted into formula (3-7)~formula (3-10) respectively, can be obtained：
For k=1.4 gas：
Nozzle pressure
By differential equation of motion formulaWith velocity of sound formula：
Formula (3-11) is substituted into the differential expression of isentropic procedure equation：
Write ideal gas state equation p/ ρ=RT as differential expressions, obtained：
Bring formula (3-11) and (3-12) into above formula, arrange：
Formula (3-11)~(3-13) shows：Air velocity v change is always opposite with parameter ρ, p, T change.V increases along journey
Greatly, ρ, p, T must reduce along journey, and v reduces along journey, then ρ, p, T must be along Cheng Zeng great.
Therefore, for nozzle has sizable gas flow rate, then a smaller pressure is needed.
Accumulate nozzle exit
Analyze variation relation of the flow parameter with channel cross-sectional area A.
Formula (3-11) is substituted into the differential equation of continuity equationArrange：
It can be drawn by formula (3-14) to draw a conclusion：
1. subsonic airflow (Ma ＜ 1), now (1-Ma2) ＞ 0, dA and dv contrary signs, i.e. channel cross-sectional area reduces along journey, speed
Degree will be along Cheng Zeng great；Channel cross-sectional area will reduce along Cheng Zeng great, speed along journey.
2. supersonic flow (Ma ＞ 1), now (1-Ma2) ＜ 0, dA and dv jack per lines, i.e. channel cross-sectional area reduces along journey, speed
Degree will reduce along journey；Channel cross-sectional area will be along Cheng Zeng great along Cheng Zeng great, speed.
3. subsonic airflow (Ma=1), now (1-Ma2)=0, dA=0, illustrate the velocity of sound can only appear on pipeline maximum or
At minimum cross section.When channel cross-sectional area is along Cheng Zeng great, the speed of subsonic airflow will reduce along journey, can not in maximum section part
The velocity of sound can be reached；The speed of supersonic flow will be also impossible to reach the velocity of sound along Cheng Zeng great, maximum section part.Therefore, the velocity of sound is not
It possibly be present at maximum section part.However, when channel cross-sectional area subtracts small along journey, the speed of subsonic airflow will along Cheng Zeng great,
Flow velocity reaches maximum at minimum cross section,
The velocity of sound is likely to be breached under certain condition；The speed of supersonic flow will reduce along journey, the flow velocity at minimum cross section
Reach minimum value, the minimum value may also reach the velocity of sound under certain conditions.Therefore, velocity of sound flowing is only possible to appear in minimum
Section part.
Therefore, jet can regard the jet that the aperture of some disposal one unlimited minor radius close from jet exit is sprayed as
Flowing, the sectional area of spout should be set to very little area.
The effect of jet pipe is the enthalpy drop of gas to be most sufficiently converted into kinetic energy.According to jet pipe upstream and downstream gas pressure ratio
Difference, jet pipe can be divided into supersonic nozzle (Laval nozzle) and subsonic effuser (shrinking shape jet pipe) two classes.Work as pressure ratioWhen, supersonic airstream can obtain using Laval nozzle；Work as pressure ratioWhen, adopt
Subsonic speed or velocity of sound air-flow are can obtain with shape jet pipe is shunk.
The type compressors of PARI BOY 037 are used as needed, its relevant parameter is respectively：Electric current 0.5A, power 50w, pressure
Strong 1.3Bar=0.13MPa, 2700~3250L/min=162 of air demand~195m3/h。
To water inlet section and delivery port section, jet pipe speed and flow are asked in examination.
Nozzle exit section is ρe、Pe、Te, inlet section ρ0、P0、T0。
According to energy equation：Then：
According to state equation：
Utilize isentropic conditions：
Therefore, formula (4-1) can also be write as：
Then mass flow：
Mass flow Q is discussedmWith the change of pressure：
Ⅰp0=pbBecause jet pipe both ends are not flowed without pressure difference, gas, Qm=0, back pressure pe=pb。
Ⅱp0>pb>p*Gas reduces through shrink nozzle, pressure along journey, back pressure pe=pb〉p*.Flow velocity along Cheng Zeng great, but
Fail to reach velocity of sound v in pipe exite＜ C0.Nozzle exit flow rate can be calculated by formula (4-2) and formula (4-3).
Ⅲp0>pb=p*Gas reaches the velocity of sound, v in outlet after collapsible tube acceleratese=C*, i.e. Ma=1.Now, outlet speed
Degree reaches maximum vemax, the big maximum Q of flowmmax.Back pressure pe=pb=p*.By formula, obtain：
The Peak Flow Rate v of shrink nozzle Outlet Section can be obtained by substituting the above in formula (3-11) and (3-12)emaxAnd jet pipe
Interior biggest quality flow Qmmax, i.e.,：
Ⅳp0>p*>pbBecause subsonic airflow through shrink nozzle can not possibly reach supersonic speed, therefore air-flow is in outside nozzle
Speed be still the velocity of sound, vemax=C*, the pressure in exit is still critical pressure, pe=p*〉pb.Now, because shrink nozzle exports
Section part has reached critical condition, and the outer existing pressure difference disturbance of Outlet Section can not possibly countercurrently propagate into jet pipe, thus air-flow from
The pressure p exported out*It is down to back pressure pbProcess can only be completed outside jet pipe, here it is mass flow QmNot exclusively according to formula (4-
3) basic reason of change.
Determine critical parameter and critical cross-section size
Critical parameter：
Critical pressure is：p*=0.528p0=0.528 × 0.13=0.06864MPa
Critical-temperature is：T*=0.833T0=0.833 × 293=244.069K
Critical density is：
Critical speed is：
Sectional dimension：
According to PARI BOY sprayer unit nozzle entries a diameter of 5mm, outlet diameter 0.2mm, data are set according to this
Meter calculates.
Therefore, from shrinkage type jet pipe.
In summary, gas must reach the velocity of sound after collapsible tube accelerates in exit, it can thus be concluded that：
Shrink nozzle exit reaches the velocity of sound, i.e. critical condition, ve=C*。
ve=C*=313.16m/s
ρe=ρ*=0.979kg/m3
Outlet spouts jet atomization mechanism
With air momentum-exchange, heat exchange occur for jet.Because effluxvelocity is larger, and jet expansion upstream airflow has
Disturbance, tangential section is unstable, whirlpool occurs on the section, and these whirlpools do irregular motion in flowing, thus send out
Transverse momentum exchange, heat exchange between raw micelle, so as to form turbulent jet boundary layer.Disturbance and exchange of kinetic energy cause liquid
Vents face is risen to along the duct at jet pipe both ends, because air-flow is very big, liquid is mapped on the baffle plate above spout, hits and adds
Speed atomization.
Fountain principle and workflow
Principle is a conservation of momentum, from large radius pipeline to minor radius pipeline, produces the change of a speed, rushes at and deviate from
The direction on ground.The speed of large radius is driven by pump, and the speed in minor radius is original speed, with momentum transformation speed.Need
One infinitesimal of selection calculates the conservation of momentum, can so obtain a speed, this speed is muzzle velocity, is then exactly on one
Throwing campaign, this is preferable situation, is not rubbed, without wind.The block of fountain and base are linked together, afterwards shape
Into the moulding of fountain, whole fountain and immersible pump are linked together, the function of fountain can be realized by being powered.Before turn on pump, inhale
Entering must be hydraulically full in pipe and pump.After turn on pump, impeller rotates at a high speed, and liquid therein rotates, centrifuged together with blade
In the presence of power, fly away from impeller and outwards project, the liquid of the injection speed in pump case diffuser casing is gradually slack-off, and pressure gradually increases
Add, then from pump discharge, discharge pipe outflow.Now, at blade center due to liquid be thrown toward around and formed both be not it is free
Again without the vacuum low-pressure area of liquid, the liquid in liquid pool flows into pump, liquid gas in the presence of the atmospheric pressure of pond face through suction line
Body is exactly so continuously to be pumped up from liquid pool and continuously flowed out from discharge pipe.
Interface and spout Components Shape
Interface and spout are the most important components of fountain apparatus, which determine the shape of fountain.Interface and spout are screw thread
Connection.Surrounding at interface thread stamps aperture, when immersible pump by transverse connecting pipe and perpendicular connecting tube is transported to water to connect
When mouth and spout threaded connection place.Water is located between the cooperation that interface and spout are reserved is rushed to by the aperture of interface thread surrounding,
Even is outwards gushed out by spout.Interface and spout degree of cooperation, and at interface thread surrounding aperture position by testing
Know.To ensure thread size precision in processing, ensure that the profile of interface and spout wants the requirement attractive in appearance for adapting to landscape.
The utility model is described in detail above, but the content is only preferred embodiment of the present utility model,
It is not to be regarded as being used to limit practical range of the present utility model.All equivalent changes made according to present utility model application scope with
Improve etc., all should still it belong within patent covering scope of the present utility model.
Claims (8)
1. a kind of fountain is atomized potted landscape, it is characterised in that：Including sprayer unit, fountain apparatus, landscape device, water vat, latent
Water lines, immersible pump, air compressor；Diving pipeline is connected with immersible pump, and air compressor passes through pipeline and sprayer unit phase
Even, sprayer unit, fountain apparatus, landscape device arranged adjacent are in water vat；
Wherein, sprayer unit includes outer, top cylinder, baffle plate, tube wall, cone tank, base, water pipe, receipts on upper cover body, cylinder
Miniature jet pipe, inlet opening, conical pipe, buckle, conical cavity, nebulization chamber and dispersive nozzle, sprayer unit are integrally cylindrical in shape, and are divided into
Top tube structure and lower cylinder structure, the two is suspended on cylinder on outer by upper cover body, and by snapping connection；
Top tube structure is made up of upper cover body, top cylinder, baffle plate and shrinkage type jet pipe, and upper cover body is arranged at top cylinder
Top, the bottom of top cylinder set baffle plate and shrinkage type jet pipe；Nebulization chamber is formed between baffle plate and shrinkage type jet pipe, is shunk
Type jet pipe is the bell-mouth structure of air that upper end is tightened up, and lower section is entrance, and top is outlet, and the inlet diameter is 2-8mm, and outlet is straight
Footpath is 0.1-0.3mm, and top is that dispersive nozzle lower cylinder structure is made up of conical pipe, water pipe and cone tank, and conical pipe is set
In in cone tank, water pipe is arranged at the lower section of cone tank, in the inside of tube wall, is provided with above the upper edge of cone tank into water
Hole；
Wherein, fountain apparatus includes spout block, spout, spout connecting seat, interface block, interface, center con and level
Pipeline, center con are provided at both ends with horizontal pipeline, and the upper end of center con is provided with interface, the upper end of the interface
Interface block is provided with, horizontal pipeline is provided at both ends with spout connecting seat, and the upper end of spout connecting seat is provided with spout, described
The upper end of spout is provided with spout block.
A kind of 2. fountain atomization potted landscape according to claim 1, it is characterised in that：A kind of described fountain atomization basin
The total quality of the sprayer unit of scape structure is 10-20kg.
A kind of 3. fountain atomization potted landscape according to claim 1, it is characterised in that：Described landscape device is decoration
Artificial hillock or other ornamental landscapes, for being arranged in indoor purifying indoor environment.
A kind of 4. fountain atomization potted landscape according to claim 1, it is characterised in that：Described top tube structure
Highly it is the 1/3-1/2 of overall sprayer unit height.
A kind of 5. fountain atomization potted landscape according to claim 1, it is characterised in that：The outer wall of described sprayer unit
On be provided with ball float, for device to be flown at into the water surface, be allowed to fluctuate with the increase and decrease of water level.
A kind of 6. fountain atomization potted landscape according to claim 1, it is characterised in that：The shape in described nebulization chamber
Into fogdrop diameter at 3-8 μm.
A kind of 7. fountain atomization potted landscape according to claim 1, it is characterised in that：Described fountain atomising device
Size is：Long 50-70cm, wide 30-50cm, high 30-50cm.
A kind of 8. fountain atomization potted landscape according to claim 1, it is characterised in that：The entrance of the shrinkage type jet pipe
A diameter of 4-6mm, outlet diameter 0.1-0.2mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720855732.8U CN207140661U (en) | 2017-07-14 | 2017-07-14 | A kind of fountain is atomized potted landscape |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720855732.8U CN207140661U (en) | 2017-07-14 | 2017-07-14 | A kind of fountain is atomized potted landscape |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207140661U true CN207140661U (en) | 2018-03-27 |
Family
ID=61675200
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720855732.8U Expired - Fee Related CN207140661U (en) | 2017-07-14 | 2017-07-14 | A kind of fountain is atomized potted landscape |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207140661U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108838015A (en) * | 2018-07-25 | 2018-11-20 | 安徽远锦文化环境艺术工程有限公司 | A kind of rockery Assembled rotary cascade fountain |
-
2017
- 2017-07-14 CN CN201720855732.8U patent/CN207140661U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108838015A (en) * | 2018-07-25 | 2018-11-20 | 安徽远锦文化环境艺术工程有限公司 | A kind of rockery Assembled rotary cascade fountain |
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