CN206252970U - Water power dust pelletizing system - Google Patents
Water power dust pelletizing system Download PDFInfo
- Publication number
- CN206252970U CN206252970U CN201621289580.1U CN201621289580U CN206252970U CN 206252970 U CN206252970 U CN 206252970U CN 201621289580 U CN201621289580 U CN 201621289580U CN 206252970 U CN206252970 U CN 206252970U
- Authority
- CN
- China
- Prior art keywords
- water
- dust pelletizing
- pelletizing system
- water tank
- power dust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model discloses a kind of water power dust pelletizing system, include water tank, the side of the water tank is provided with salt storeroom, the top connection water inlet pipe of the water tank, the bottom connection mozzle of the water tank, the end of the mozzle is evenly arranged with multiple waterfog heads, and metallic conductor is provided with the waterfog head, and the metallic conductor connects external circuit.The utility model being capable of purify air, reduction air contamination, consumption of the reduction to electric energy；The purpose of energy-saving and emission-reduction is reached, can be used to process the pernicious gas produced in industrial production；Secondary pollution is not resulted in during sorption enhanced.
Description
Technical field
The utility model is related to a kind of dust arrester, more particularly to a kind of water power dust pelletizing system.
Background technology
Field is manufactured in industrial production, links can all produce substantial amounts of dust or waste gas, for a long time in this environmental work
People easily suffer from all kinds of heart and lung diseases, serious harm worker's is healthy.And dust or waste gas are easily reduced production ring
The visibility in border, increases all kinds of accident occurrence risks.
At present, existing cleaner mainly has sack cleaner, cyclone dust collectors, high-voltage electrostatic dust separator, gravity to sink
Drop deduster etc., these cleaners do not adapt to the dedusting of the strong dusty gas of high temperature high humidity, corrosivity, and service life is not
It is long, safeguard inconvenient, one-time investment is larger, and does not reach state environmental emissioning standard etc..
Traditional air cleaning effect is bad, and noise is big, and the dust isolated is it is also possible to secondary pollution, traditional
Water cleaner can greatly increase air humidity, and industrial equipment and workman's body are all had a certain impact, and, in tradition
In electrostatic precipitation system, the dust of attraction can be adsorbed on object around and is difficult to clean off because itself is powered, on collecting plate
Dust needs to be removed by the way of shaking.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of water power dust pelletizing system, and it being capable of purify air, reduction
Air contamination, reduces the consumption to electric energy, can be used to process the pernicious gas produced in industrial production in sorption enhanced not
Secondary pollution can be caused.
In order to solve the above-mentioned technical problem, the utility model provides a kind of water power dust pelletizing system, includes water tank, described
The side of water tank is provided with salt storeroom, and the top connection water inlet pipe of the water tank, the bottom of the water tank connects mozzle,
The end of the mozzle is evenly arranged with multiple waterfog heads, and metallic conductor, the metal are provided with the waterfog head
Conductor connects external circuit.
Further, the salt storeroom is sodium chloride storeroom.
Further, the top of the water tank is provided with water inlet, and the water inlet is connected with water inlet pipe, in the water inlet
Filter is provided with pipe.
Further, the bottom of the water tank is provided with delivery port, and the delivery port is connected with mozzle, in the water conservancy diversion
Liquid electrostatic generator is provided with pipe.
Further, be evenly arranged with becket on the metallic conductor, each described becket respectively with each water smoke
Shower nozzle is corresponding.
Further, the metallic conductor is connected by insulated conductor with external circuit.
Further, the surface of the metallic conductor and insulated conductor scribbles insulated paint.
Further, the bottom of the water tank is also associated with tank.
Further, it is provided with insulation water pipe between the water tank and tank.
Further, the external circuit includes power circuit, boost module, control system, connection circuit and transformer, institute
State power circuit and control system to be electrically connected with, the control system is also electrically connected with transformer, the control system also with
Boost module is electrically connected with, and high-voltage output end and the metallic conductor of the boost module are electrically connected with.
The utility model being capable of purify air, reduction air contamination, consumption of the reduction to electric energy；Reach energy-saving and emission-reduction
Purpose, can be used to process the pernicious gas produced in industrial production；Secondary pollution is not resulted in during sorption enhanced.
Brief description of the drawings
Fig. 1 is the utility model water power dust pelletizing system structural representation one；
Fig. 2 is the utility model water power dust pelletizing system structural representation two；
Fig. 3 is the utility model external circuit structure chart.
In figure, 1. water tank, 2. water inlet, 3. delivery port, 4. sodium chloride storeroom, 5, mozzle, 6. waterfog head, 7. gold
Belong to ring, 8. insulated conductor, 9. external circuit, 91. power circuits, 92. boost modules, 93. control circuits, 94. connection circuits, 95.
Transformer, 10. tank, 11. insulation water pipes, 12. filters, 13. liquid electrostatic generators.
Specific embodiment
The utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings, so that those skilled in the art
The utility model can be better understood from and can be practiced, but illustrated embodiment is not as to restriction of the present utility model.
As shown in Figure 1 to Figure 3, it is a kind of water power dust pelletizing system of the utility model, includes water tank 1, the one of the water tank 1
Side is provided with the salt storeroom of the salt formed by active metals such as potassium, calcium, sodium, is sodium chloride storeroom 4, institute in the present embodiment
The top connection water inlet pipe of water tank 1 is stated, the bottom of the water tank 1 connects mozzle 5, and the end of the mozzle 5 is uniformly arranged
There are multiple waterfog heads 6, metallic conductor is provided with the waterfog head 6, the metallic conductor connects external circuit 9.
The top of the water tank is provided with water inlet 2, and the water inlet 2 is connected with water inlet pipe, is set on the water inlet pipe
It is equipped with filter 12.
The bottom of the water tank 1 is provided with delivery port 3, and the delivery port 3 is connected with mozzle 5, on the mozzle 5
It is provided with liquid electrostatic generator 13.This liquid electrostatic generator 13 can form an electric field, make current in the effect of electric field
Lower polarization, enhancing water smoke is by charged effect.Becket 7 is evenly arranged with the metallic conductor, each described becket 7 is distinguished
Each waterfog head 6 is corresponding.The metallic conductor is connected by insulated conductor 8 with external circuit 9.The metallic conductor and insulation
The surface of wire 8 scribbles insulated paint.The bottom of the water tank 1 is also associated with tank 10.Between the water tank 1 and tank 10
It is provided with insulation water pipe 11.Water tank 1 supplies charged water by insulation water pipe 11 to tank 10, and current flow through invest wall from top to bottom
The tank 10 of wall, forms flowing water layer, adsorbs and take away the molten impurity of institute.
Operation principle of the present utility model is：First to water filling in the water tank 1 of water power dust pelletizing system, current first pass around into
The filter 12 of water pipe is filtered, and removes the insoluble impurities in water, and then sodium chloride storeroom produces NaCl solution, makes molten
Ion is rich in liquid.Delivery port 3 connects mozzle 5, and the end of mozzle 5 is equipped with waterfog head 6, can be by NaCl solution with vaporific
Outwards sprinkling.
Becket 7 is provided with the utility model at waterfog head 6, is connected with external circuit 9 by insulated conductor 8, and gold
Category conductor scribbles insulated paint with the surface of insulated conductor 8, for protection circuit.The utility model external circuit 9 is that high-pressure modular is integrated
System, the magnitude of voltage that can be produced is about 60,000 volts of high pressures of (60KV).
This high-pressure modular integrated system is by power circuit 91, boost module 92, control system 93, connection circuit 94 and transformation
Device 95 is constituted.Power circuit 91 is electrically connected with control system 93, and control system 93 is also electrically connected with transformer 95, control system
System 93 is also connected with boost module 92, and the high-voltage output end of boost module 92 is connected with metallic conductor.Can be by the direct current liter of 3-6V
Height arrives 60KV or so, but will not people, animal be caused any harm with (power is small).
When current flow into waterfog head 6, solution occurs polarization phenomena because of the high voltage electric field around becket, in solution
Na+(sodium ion) or Cl-(chlorion) is assembled because of the effect of electric field to different directions；Solution after polarization is through shower nozzle with vaporific spray
Go out, this process makes to be rich in Na in electric charge on water smoke band, i.e. water smoke+And Cl-)。
During motion, the impurity of suspension in air can be actively attracted because itself is powered, and (traditional water smoke is removed water smoke
Dirt device is then less efficient relative to electrostatic attraction by the globule being stained with to inhale and reach the purpose of dedusting to dust), because the globule is powered thus meeting
By externally electric discharge, discharge process produces a small amount of O3(ozone) and OH-(hydroxide ion), the harmful substance (SO of absorption2、NO、
NO2Deng) immerse in the solution rich in NaOH and neutralization reaction occurs with it, generate innocuous substance；Reach dedusting, purify air
Effect.The O for producing simultaneously3Also disinfection (note can be played a part of：Rich in NaOH it is relative to liquid juice in solution
Speech, will not to external world cause corrosiveness).Afterwards, these adsorbed impurity can fall within ground because of deadweight, reach udst separation
The effect of air.Meanwhile, absorbed heat when water smoke evaporates, the temperature of waste gas can be reduced, add again by molecular thermalmotion is reduced
Fast dust coagulation.
Meanwhile, water tank 1 supplies charged water by insulation water pipe 11 to tank 10, and current flow through invest wall from top to bottom
Tank, forms flowing water layer, adsorbs and take away the molten impurity of institute.
The utility model utilizes water polarized charged in the electric field, adsorbs the industrial waste gas of discharge；In the suction of charged drop
Under drawing, pernicious gas and inhalable solid particle are close to one because electric field force is acted on actively to liquid drop movement with drop,
Because electrical body is the water with strong adhesion, therefore the dust for holding will not cause itself to take electricity of the same race because being contacted with electrical body
Lotus and separation.In conventional electrostatic dust pelletizing system, the dust of attraction can be difficult to because on itself band Electro Sorb around object
Remove, and dust on collecting plate needs to be removed by the way of shaking；And the advantage of this system is using sprinkling
Charged liquid dust suction, then falls within accumulation area under deadweight；And corrosiveness of the liquid to collecting plate can be reduced.
The utility model also has with advantages below：
1) conventional electrostatic dust arrester, is using the powered dust adsorbed with this in air of battery lead plate, adsorbed dust
Not only it is difficult to clean off, can also influences dust removing effects；Or (liquid is in itself to dust to utilize suction-operated of the fog-like liquid to dust
Absorption) purpose of dedusting is reached, its is less efficient.And the utility model is powered come dust suction dedusting by water smoke, not only solve
Battery lead plate impaired problem, also greatly improves efficiency of dust collection.
2) conventional electrostatic dust pelletizing system is to adsorb the harmful substance in air；And this device contains in can utilizing water smoke
Alkaline matter neutralize the pernicious gas in waste gas.
3) for traditional dust pelletizing system, this system increases cooling function newly.
4) use of electric energy is reduced；From Kelvin drip electrification principle, make liquid powered using device positive feedback,
Few electric energy need to be consumed.
5) to the overcoming of coal-dust explosion hidden danger, (in closing space, burning of the combustion property suspension in explosion limit can be led
Chemical explosion is caused, during dust is captured, though there is a small amount of dust not in contact with water smoke, due to being full of water in apparatus body
Droplet, humidity is larger, thus can avoid coal-dust explosion).
6) (there are two kinds of space charges in electric cleaner simultaneously, one kind is gas ion to overcoming for high-voltage corona obturation
Electric charge, a kind of is the electric charge of powered grit.The movement velocity of powered grit is significantly larger than due to the movement velocity of gas ion,
So the corona current of the dust-contained airflow for passing through deduster is smaller than clean gas.If gas dust content is very high, can make
The corona current of electric cleaner drastically declines, and may level off to zero when serious, and corona blocking occurs.And in water fog charge dedusting
In device, due to charged water spray meeting adsorption of dust particle, therefore corona blocking is not susceptible to).
7) overcoming (when the ratio resistance of dust is less than 10 to inverse corona10During Ω cm, ratio resistance to the operation of deduster and
Performance is almost without harmful effect；When ratio resistance is between 1010Ω~1011When between Ω cm, spark rate increases, operating voltage
Reduce；When ratio resistance is higher than 1011During Ω cm, occur electric spark in dust and dust layer, that is, produce obvious inverse corona.Anti- electricity
Dizzy generation can cause corona current density to substantially reduce, and then severe jamming particle charged and trapping.Charged water spray dedusting
Device uses charged water spray adsorption of dust particle, can substantially reduce its ratio resistance, so as to effectively contain the generation of inverse corona).
Embodiment described above is only the preferred embodiment lifted to absolutely prove the utility model, the utility model
Protection domain not limited to this.Equivalent substitute or change that those skilled in the art are made on the basis of the utility model
Change, within protection domain of the present utility model.Protection domain of the present utility model is defined by claims.
Claims (10)
1. a kind of water power dust pelletizing system, it is characterised in that include water tank, the side of the water tank is provided with salt storeroom,
The top connection water inlet pipe of the water tank, the bottom connection mozzle of the water tank, the end of the mozzle is evenly arranged with
Multiple waterfog heads, are provided with metallic conductor at the waterfog head, the metallic conductor connects external circuit.
2. water power dust pelletizing system according to claim 1, it is characterised in that the salt storeroom is sodium chloride storage
Room.
3. water power dust pelletizing system according to claim 1, it is characterised in that the top of the water tank is provided with water inlet,
The water inlet is connected with water inlet pipe, and filter is provided with the water inlet pipe.
4. water power dust pelletizing system according to claim 1, it is characterised in that the bottom of the water tank is provided with delivery port,
The delivery port is connected with mozzle, and liquid electrostatic generator is provided with the mozzle.
5. water power dust pelletizing system according to claim 1, it is characterised in that be evenly arranged with metal on the metallic conductor
Ring, each described becket is corresponding with each waterfog head respectively.
6. water power dust pelletizing system according to claim 5, it is characterised in that the metallic conductor by insulated conductor with it is outer
Circuit is connected.
7. water power dust pelletizing system according to claim 6, it is characterised in that the surface of the metallic conductor and insulated conductor
Scribble insulated paint.
8. water power dust pelletizing system according to claim 1, it is characterised in that the bottom of the water tank is also associated with tank.
9. water power dust pelletizing system according to claim 8, it is characterised in that be provided between the water tank and tank absolutely
Edge water pipe.
10. water power dust pelletizing system according to claim 1, it is characterised in that the external circuit includes power circuit, boosting
Module, control system, connection circuit and transformer, the power circuit are electrically connected with control system, and the control system is also
With transformer be electrically connected with, the control system also with boost module be electrically connected with, the high-voltage output end of the boost module with
Metallic conductor is electrically connected with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621289580.1U CN206252970U (en) | 2016-11-29 | 2016-11-29 | Water power dust pelletizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621289580.1U CN206252970U (en) | 2016-11-29 | 2016-11-29 | Water power dust pelletizing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206252970U true CN206252970U (en) | 2017-06-16 |
Family
ID=59027844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621289580.1U Expired - Fee Related CN206252970U (en) | 2016-11-29 | 2016-11-29 | Water power dust pelletizing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206252970U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113041767A (en) * | 2021-04-02 | 2021-06-29 | 刘森 | High-efficiency electro-hydraulic dust removal method and system for dust-containing flue gas |
-
2016
- 2016-11-29 CN CN201621289580.1U patent/CN206252970U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113041767A (en) * | 2021-04-02 | 2021-06-29 | 刘森 | High-efficiency electro-hydraulic dust removal method and system for dust-containing flue gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170616 Termination date: 20171129 |