CN104998496B - Static Electric Water washes dust-extraction unit - Google Patents
Static Electric Water washes dust-extraction unit Download PDFInfo
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- CN104998496B CN104998496B CN201410154662.4A CN201410154662A CN104998496B CN 104998496 B CN104998496 B CN 104998496B CN 201410154662 A CN201410154662 A CN 201410154662A CN 104998496 B CN104998496 B CN 104998496B
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- liquid phase
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- phase labyrinth
- labyrinth
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Abstract
A kind of Static Electric Water washes dust-extraction unit, including shell, and shell is equipped with air inlet pipe and exhaust pipe, is equipped with liquid phase labyrinth in shell, the air inlet in liquid phase labyrinth is connected to air inlet pipe, and gas outlet is connected to exhaust pipe；The liquid phase labyrinth is at least partially submerged in liquid.The liquid phase labyrinth is formed by multiple horizontally disposed partition interlaced arrangements, at least bristle layer is equipped in the upstream face of partition, in liquid phase labyrinth, the top of air inlet is equipped with negative ion device, the anode connection of discharge electrode and power supply in negative ion device, the liquid phase labyrinth is electric conductor, the cathode connection of liquid phase labyrinth and power supply or ground connection.The mode that the present invention is adsorbed by using wet type cooperates the structure in liquid phase labyrinth, has effectively adsorbed the dust in air, reduced indoor adsorbable particulate matter.In particular by the structure in liquid phase labyrinth, the time of contact of air and liquid is extended, cooperates the structure of negative ion device that preferably particulate matter can be adsorbed onto liquid, improves dust removing effects.
Description
Technical field
The present invention relates to dedustings and the field of prevention and treatment haze, especially a kind of Static Electric Water to wash dust-extraction unit.
Background technique
Under the biggish weather condition of dust, such as under haze weather, there are many indoor often dust, influence the respiratory tract of people
Health, especially high building such case are even more serious.
Existing air purifier mostly uses the mode of filtering to remove dust, the problem is that, this filtering filter
Piece is difficult to filter short grained dust, such as the small particle of pm2.5 and following level, can still enter lung's product of human body
It deposits, seriously affects health.And tiny particulate matter can be filtered using more accurate filter disc, but this also generates new skill
Art problem, more accurate filter disc is easy to be blocked by dust or tiny particles content, and frequently replaces the higher cost of filter disc, and more
The filter disc changed can not be recycled, and cause new environmental pollution.
Using filter disc, especially more accurate filter disc, as the extension windage of time is gradually increased, energy consumption is higher, or
Scavenging efficiency reduces.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of Static Electric Waters to wash dust-extraction unit, can remove the ash in air
Dirt, elimination efficiency is high, and low energy consumption, and consumables cost is low.
In order to solve the above technical problems, the technical scheme adopted by the invention is that: a kind of Static Electric Water washes dust-extraction unit, including
Shell, shell are equipped with air inlet pipe and exhaust pipe, and liquid phase labyrinth is equipped in shell, and the air inlet and air inlet pipe in liquid phase labyrinth connect
Logical, gas outlet is connected to exhaust pipe, and the liquid phase labyrinth is at least partially submerged in liquid；
In liquid phase labyrinth, the top of air inlet is equipped with negative ion device, the anode of discharge electrode and power supply in negative ion device
Connection, the liquid phase labyrinth are electric conductor, and the cathode connection of liquid phase labyrinth and power supply or/and liquid phase labyrinth are directly grounded.
The liquid phase labyrinth is formed by multiple horizontally disposed partition interlaced arrangements, is at least equipped in the upstream face of partition
Bristle layer.
The liquid phase labyrinth is integral frame structure, and in liquid phase labyrinth, the outer wall of frame is equipped with oscillator, is additionally provided with multiple
Elastic element for bearing.
The exhaust pipe is also connected to liquid back pipe, and liquid back pipe is connected to sediment accumulation area, is equipped in sediment accumulation area oblique
Plate settling zone, the bottom of sediment accumulation area are equipped with scum pipe, and the top of slag accumulation area is connected to by liquid return hole with liquid phase labyrinth.
Be additionally provided with gas phase labyrinth, the import in gas phase labyrinth is connect with the gas outlet in liquid phase labyrinth, the outlet in gas phase labyrinth with
Exhaust pipe connection；
In the gas phase labyrinth, multiple horizontal baffle interlaced arrangements form first order labyrinth, and multiple vertical baffles interlock
It is arranged to second level labyrinth, is at least equipped with adsorption layer in the windward side of horizontal baffle and vertical baffle.
Spray head is additionally provided in liquid phase labyrinth, spray head is connected to shell close to the position of bottom by pipeline and pump, or
It is connected to the position close to liquid back pipe bottom.
Be additionally provided with condensing unit, the heat exchanger fin of condensing unit is placed in exhaust pipe, heat exchanger fin and semiconductor chilling plate it is cold
Pole connection, the thermoae of semiconductor chilling plate are connect with radiator.
The radiator is air-cooled or water cooling plant；
It is equipped with spray head in liquid phase labyrinth or case top, spray head is by pipeline and pumps and connects below the liquid level of liquid in shell
It is logical；
The water cooling plant and pipeline connection is cooled down using spray head circulating liquid；
Pipeline is also connected to liquid supplementation pipe.
The air inlet pipe or exhaust pipe is connect with new blower；
The entrance of air inlet pipe reaches except wall.
Fumigation device is additionally provided in exhaust pipe.
A kind of Static Electric Water provided by the invention washes dust-extraction unit, by using the mode of liquid adsorption, cooperates liquid phase labyrinth
Structure, effectively adsorbed the dust in air, reduced indoor adsorbable particle content.In particular by liquid phase labyrinth
Structure, extend the time of contact of air and liquid, play good dustproof function, with filter type phase in the prior art
More preferably than, indoor dust removing effects of the invention, and low energy consumption, and almost no material consumption, reduces use cost.Cooperate negative ion device
Structure, suitable for reading in liquid phase labyrinth make the particulate matter to get into the air become positively charged lotus, and liquid phase labyrinth is connect with cathode or
Person's ground connection improves dust removing effects so as to which preferably particulate matter is adsorbed onto liquid.
Detailed description of the invention
Present invention will be further explained below with reference to the attached drawings and examples:
Fig. 1 is overall structure diagram of the invention.
Fig. 2 is the overall structure diagram of another embodiment of the present invention.
Fig. 3 is the structural schematic diagram in liquid phase labyrinth in the present invention.
In figure: wall 1, new blower 2, air inlet pipe 3, gas phase labyrinth 4, vertical baffle 41, horizontal baffle 42, spray head 5, pipeline
6, water cooling plant 7, semiconductor chilling plate 8, liquid phase labyrinth 9, partition 91, bristle layer 92, air inlet 93, gas outlet 94, oscillator 95,
Elastic element 96, heat exchanger fin 10, exhaust pipe 11, liquid return hole 12, liquid back pipe 13, sloping plate deposition district 14, sediment accumulation area 15, deslagging
Pipe 16, shell 17, pump 18, liquid supplementation pipe 19, negative ion device 20.
Specific embodiment
Embodiment 1:
In Fig. 2, a kind of Static Electric Water washes dust-extraction unit, including shell 17, and shell 17 is equipped with air inlet pipe 3 and exhaust pipe
11, the air inlet pipe 3 or exhaust pipe 11 are connect with new blower 2；To push air to run.
Liquid phase labyrinth 9 is equipped in shell 17, the air inlet in liquid phase labyrinth 9 is connected to air inlet pipe 3, gas outlet and exhaust pipe 11
Connection；
The liquid phase labyrinth 9 is at least partially submerged in liquid.Thus structure is extended and is exchanged between air and water
Path, improve dust removing effects.
In the scheme such as Fig. 2 of optimization, the liquid phase labyrinth 9 is formed by multiple horizontally disposed 91 interlaced arrangements of partition,
At least bristle layer 92 is equipped in the upstream face of partition 91.By the bristle layer 92 of setting, pierce the bristle in multiple bristle layers 92
Relieving stagnant Qi bubble, which increase the contacts area between air and water, further enhance dust removing effects.Bristle layer in this example uses
The structure just pierced in similar thread gluing, it is preferred to use nylon plastic(s) material.Upstream face in this example refers under each partition 91
Bottom surface, when bubble rises, the bottom surface meeting of each partition 91 and bubble contact.
In the scheme such as Fig. 2 advanced optimized, in liquid phase labyrinth the top of 9 air inlet be equipped with negative ion device 20, bear from
The anode connection of discharge electrode and power supply in sub-device 20, the liquid phase labyrinth 9 are electric conductor, liquid phase labyrinth 9 and power supply
Cathode connection or/and liquid phase labyrinth 9 are directly grounded.Thus structure, by the discharge electrode in negative ion device 20, structure is existing
Have in technology, including conductor, multiple discharge electrodes are equipped on conductor, the discharge electrode connecting with positive pole makes by this
Particulate matter becomes positively charged lotus, and liquid phase labyrinth is connect with power cathode, is perhaps directly grounded or is connect and connect with cathode simultaneously
Ground adsorbs liquid preferably using the gravitation of positive and negative anodes so that liquid phase labyrinth be made to include that the liquid in it becomes cathode
Particulate matter, this is particularly effective the particulate matter compared with small particle.Preferably, the supply voltage used does not make air generate electricity
From.
The scheme such as Fig. 2 that advanced optimize, in 3, the liquid phase labyrinth 9 is integral frame structure, movable to be mounted on
In shell 17, air inlet pipe 3 is connected to air inlet 93, and gas outlet 94 is connected to exhaust pipe 11, and in liquid phase labyrinth, the outer wall of 9 frame is set
There is oscillator 95, is additionally provided with multiple elastic elements 96 for bearing, such as rubber column.Pass through the vibration of oscillator 95, it is preferred to use
Piezoelectric-type ultrasonic oscillator, makes the general frame vibration at high speed in liquid phase labyrinth 9, so that the liquid at high speed in it be driven to vibrate, makes liquid
Body generates " cavitation " effect；After the structure for the bristle layer 92 being preferably provided with combines, air and liquid are further improved
Contact area adsorbs the dust in air by liquid.It is further preferred that being provided with particulate matter inspection in exhaust pipe 11
Instrument, this be it is existing in the prior art, 95 start and stop of oscillator are controlled by particulate matter somascope, when detecting particle content height
Then start oscillator 95 in threshold values, otherwise do not start, to reduce energy consumption and noise.
The scheme advanced optimized is as shown in Figure 2, and the exhaust pipe 11 is also connected to liquid back pipe 13, liquid back pipe 13 from
Position close to 17 bottom of shell is connected to sediment accumulation area 15, is equipped with sloping plate deposition district 14, sediment heap in sediment accumulation area 15
The bottom in product area 15 is equipped with scum pipe 16, and the top of slag accumulation area 15 is connected to by liquid return hole 12 with liquid phase labyrinth 9.Thus it ties
Structure is deposited the particulate matter of absorption using the circulation of liquid, to increase the adsorption capacity of liquid, the particulate matter of absorption is avoided to exist
Secondary pollution is formed after saturation.In use, the air by adsorption cleaning is drained into exhaust pipe 11 from gas outlet 94, air at this time
Partially liq may be carried under one's arms in air-flow, carry out gas-water separation in liquid back pipe 13, gas enters exhaust pipe 11, liquid then downwards into
Enter to sediment accumulation area 15, after liquid level herein increases, liquid is flowed up with lower speed, by sloping plate deposition district 14 into
Row precipitating, is separated by solid-liquid separation in sloping plate deposition district 14 at this time, and liquid passes upward through liquid return hole 12 and enters the progress of liquid phase labyrinth 9
The solid of air adsorption, particulate matter is then downward, is deposited in sediment accumulation area 15, is discharged from scum pipe 16 through valve.Using this
After structure, the interval time of replacement liquid is substantially extended.
In the scheme further optimized, referring to Fig. 1, spray head 5 is equipped at the top of liquid phase labyrinth 9 or shell 17, spray head 5 is logical
Cross pipeline 6 and pump 18 be connected to below the liquid level of liquid in shell 17；It is to connect with the position of liquid back pipe 13 in order to facilitate observation of in figure
It is logical, it is also possible to be connected in the position of liquid return hole 12.Spray head 5 is arranged in the rising passway in liquid phase labyrinth 9 in this example, this into
One step enhances the effect of spraying and dedusting.
To avoid indoor humidity excessive, it is additionally provided with condensing unit in exhaust pipe 11, referring to Fig. 1.The heat exchange of condensing unit
Piece 10 is placed in exhaust pipe 11, and heat exchanger fin 10 is connect with the cold pole of semiconductor chilling plate 8, semiconductor chilling plate 8 it is thermoae with it is scattered
Thermal connection.The radiator is air-cooled or water cooling plant；Thus structure, the moisture after purification in gas are changing
Water is condensed into the cold at backing 10, to avoid indoor humidity excessively high.
As shown in figure 1, the water cooling plant is connected to preferred scheme with pipeline 6, is cooled down using spray head circulating liquid；Thus
Structure improves the cooling effect of radiator, also utilizes the circulation power of spray head.
Pipeline 6 is also connected to liquid supplementation pipe 19.Thus structure, convenient for supplementing liquid according to the liquid level of liquid.
The entrance of air inlet pipe 3 reaches except wall 1.Thus structure is convenient for from outdoor introducing fresh air, through dress of the invention
Each room is sent to after setting purifying and dedusting, it is preferred that in the position far from air inlet pipe, exhaust apparatus is set, to form circulation,
Ensure the pure and fresh cleaning of room air.The present invention can also be with the device of other indoor air handlers, such as photocatalyst etc
It is applied in combination to reach better effect.Since present invention employs the modes of circulation air, fresh air supplement is sufficient, air replacement
Comparatively fast, of less demanding for the device of this kind of removal harmful organic substance gas.
Fumigation device is additionally provided in exhaust pipe 11.Stacte is evaporated using the air-flow in exhaust pipe 11, further increases sky
Makings amount.Fumigation device in this example is the prior art, it is preferred to use liquid or solid essential oil is placed on to the appearance of hollow out ventilation
Structure in device.
Embodiment 2:
On the basis of embodiment 1, the structure advanced optimized is as shown in fig. 1, is additionally provided with gas phase labyrinth 4, gas phase fan
The import in palace 4 is connect with the gas outlet in liquid phase labyrinth 9, and the outlet in gas phase labyrinth 4 is connected to exhaust pipe 11；
In the gas phase labyrinth 4, multiple 42 interlaced arrangements of horizontal baffle form first order labyrinth, multiple vertical baffles 41
Interlaced arrangement is at least equipped with adsorption layer in the windward side of horizontal baffle 42 and vertical baffle 41 at second level labyrinth.Thus structure,
It realizes and the supplement of particulate in air is adsorbed, while being also beneficial to reduce the drop in air, so that the humidity of outlet air is reduced,
The structure also reduces windage.Adsorption layer in this example can be used with fabric villous, to improve the contact surface with air
Product.The structure in gas phase labyrinth proposes a kind of new thinking, i.e., in the way of non-filtered using centrifugation absorption, adsorption layer is convenient for clearly
It washes, compared with strainer, service life substantially extends.
The multistage labyrinth structure of horizontal baffle 42 and vertical baffle 41 combination of setting, core are to increase turning
Number is turned each time, under the action of the centrifugal force, all can some dust or drop adsorption layer is thrown to by centrifugal force, thus
It is adsorbed layer absorption, this structure can adsorb most larger-diameter particulate matter in advance, be greater than the particle of PM10
Object.And compared to strainer, adsorption layer is convenient for repeated washing, therefore service life is longer, and windage is smaller.
The above embodiments are only the preferred technical solution of the present invention, and are not construed as limitation of the invention, this hair
Bright protection scope should be with the technical solution of claim record, technical characteristic in the technical solution recorded including claim
Equivalents are protection scope.Equivalent replacement i.e. within this range is improved, also within protection scope of the present invention.
Claims (6)
1. a kind of Static Electric Water washes dust-extraction unit, including shell (17), shell (17) is equipped with air inlet pipe (3) and exhaust pipe (11),
It is characterized in that: being equipped with liquid phase labyrinth (9) in shell (17), the air inlet of liquid phase labyrinth (9) is connected to air inlet pipe (3), gas outlet
It is connected to exhaust pipe (11), the liquid phase labyrinth (9) is at least partially submerged in liquid；
The liquid phase labyrinth (9) is formed by multiple horizontally disposed partition (91) interlaced arrangements, at least meeting in partition (91)
The water surface is equipped with bristle layer (92)；
Negative ion device (20) are equipped on the top of liquid phase labyrinth (9) air inlet, discharge electrode and electricity in negative ion device (20)
The anode connection in source, the liquid phase labyrinth (9) is electric conductor, and liquid phase labyrinth (9) are connect with the cathode of power supply or/and liquid phase fan
Palace (9) is directly grounded；
It is additionally provided with gas phase labyrinth (4), the import of gas phase labyrinth (4) is connect with the gas outlet of liquid phase labyrinth (9), gas phase labyrinth (4)
Outlet be connected to exhaust pipe (11)；
In the gas phase labyrinth (4), multiple horizontal baffle (42) interlaced arrangements form first order labyrinth, multiple vertical baffles
(41) interlaced arrangement is at least equipped with adsorption layer in the windward side of horizontal baffle (42) and vertical baffle (41) at second level labyrinth；
It is additionally provided with condensing unit, the heat exchanger fin (10) of condensing unit is placed in exhaust pipe (11), heat exchanger fin (10) and semiconductor system
Cold (8) cold pole connection, thermoae being connect with radiator of semiconductor chilling plate (8).
2. a kind of Static Electric Water according to claim 1 washes dust-extraction unit, it is characterized in that: the liquid phase labyrinth (9) is whole
Body frame structure is equipped with oscillator (95) in the outer wall of liquid phase labyrinth (9) frame, is additionally provided with multiple elastic elements for bearing
(96).
3. a kind of Static Electric Water according to claim 1 washes dust-extraction unit, it is characterized in that: the exhaust pipe (11) also with return
Liquid pipe (13) connection, liquid back pipe (13) are connected to sediment accumulation area (15), are equipped with sloping plate deposition district in sediment accumulation area (15)
(14), the bottom of sediment accumulation area (15) is equipped with scum pipe (16), and the top of slag accumulation area (15) passes through liquid return hole (12) and liquid
Phase labyrinth (9) connection.
4. a kind of Static Electric Water according to claim 1 washes dust-extraction unit, it is characterized in that: being additionally provided in liquid phase labyrinth (9)
Spray head (5), spray head (5) is connected to shell (17) close to the position of bottom by pipeline (6) and pump (18), or returns liquid with close
Manage the position connection of (13) bottom.
5. a kind of Static Electric Water according to claim 1 washes dust-extraction unit, it is characterized in that: the radiator be it is air-cooled or
Water cooling plant；
Spray head (5) are equipped at the top of liquid phase labyrinth (9) or shell (17), spray head (5) passes through pipeline (6) and pump (18) and shell
(17) it is connected to below the liquid level of interior liquid；
The water cooling plant is connected to pipeline (6), is cooled down using spray head circulating liquid；
Pipeline (6) is also connected to liquid supplementation pipe (19).
6. a kind of Static Electric Water according to claim 1 washes dust-extraction unit, it is characterized in that: the air inlet pipe (3) or exhaust
Pipe (11) is connect with new blower (2)；
The entrance of air inlet pipe (3) reaches except wall (1)；
Fumigation device is additionally provided in exhaust pipe (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410154662.4A CN104998496B (en) | 2014-04-17 | 2014-04-17 | Static Electric Water washes dust-extraction unit |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410154662.4A CN104998496B (en) | 2014-04-17 | 2014-04-17 | Static Electric Water washes dust-extraction unit |
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| CN104998496A CN104998496A (en) | 2015-10-28 |
| CN104998496B true CN104998496B (en) | 2019-05-17 |
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| CN201410154662.4A Active CN104998496B (en) | 2014-04-17 | 2014-04-17 | Static Electric Water washes dust-extraction unit |
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Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107158864B (en) * | 2016-01-26 | 2019-04-23 | 浙江朗泰环境工程有限公司 | A kind of industrial waste gas high-efficient treatment device |
| CN106000646B (en) * | 2016-06-08 | 2018-08-21 | 深圳奇滨科技开发有限公司 | A kind of water-soluble dust-extraction unit |
| CN106351694A (en) * | 2016-10-19 | 2017-01-25 | 河北科技大学 | Tunnel dust removal method |
| CN106474862B (en) * | 2016-11-11 | 2018-08-21 | 江苏大学 | A kind of dedusting and purifying device |
| CN109999595A (en) * | 2019-04-30 | 2019-07-12 | 昆山新环境环保工程有限公司 | A kind of explosion-proof wet dust pelletizing system |
| CN112452085B (en) * | 2020-10-30 | 2022-07-15 | 武汉慕都环境科技有限公司 | Automatic dust removal control system and method |
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|---|---|---|---|---|
| EP0445766A1 (en) * | 1990-03-08 | 1991-09-11 | 2 E, akciová spolecnost | Process and device for separation of admixtures from air |
| CN2481982Y (en) * | 2001-02-23 | 2002-03-13 | 陈建华 | Smoke-eliminating dust-reducing device |
| CN202700355U (en) * | 2012-08-31 | 2013-01-30 | 宁波中瑞生物科技有限公司 | Fermentation tail gas treatment device |
| CN103933818A (en) * | 2014-04-17 | 2014-07-23 | 三峡大学 | Wet anion dust remover |
| CN203777885U (en) * | 2014-04-17 | 2014-08-20 | 三峡大学 | Wet anion dust collection device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0445766A1 (en) * | 1990-03-08 | 1991-09-11 | 2 E, akciová spolecnost | Process and device for separation of admixtures from air |
| CN2481982Y (en) * | 2001-02-23 | 2002-03-13 | 陈建华 | Smoke-eliminating dust-reducing device |
| CN202700355U (en) * | 2012-08-31 | 2013-01-30 | 宁波中瑞生物科技有限公司 | Fermentation tail gas treatment device |
| CN103933818A (en) * | 2014-04-17 | 2014-07-23 | 三峡大学 | Wet anion dust remover |
| CN203777885U (en) * | 2014-04-17 | 2014-08-20 | 三峡大学 | Wet anion dust collection device |
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| CN104998496A (en) | 2015-10-28 |
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Effective date of registration: 20190314 Address after: 436000 Baoye Industrial Park, Pioneering Avenue, Gedian Economic Development Zone, Huarong District, Ezhou City, Hubei Province Applicant after: Hubei Baoye Construction Industrialization Co., Ltd. Address before: 443000 mailbox 00800016, 47 Fusui Road, Xiling District, Yichang City, Hubei Province Applicant before: Hu Yong |
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