CN104998496A - Electrostatic water washing dust removing apparatus - Google Patents
Electrostatic water washing dust removing apparatus Download PDFInfo
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- CN104998496A CN104998496A CN201410154662.4A CN201410154662A CN104998496A CN 104998496 A CN104998496 A CN 104998496A CN 201410154662 A CN201410154662 A CN 201410154662A CN 104998496 A CN104998496 A CN 104998496A
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- liquid phase
- phase labyrinth
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- labyrinth
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 238000005406 washing Methods 0.000 title claims abstract description 19
- 239000000428 dust Substances 0.000 title abstract description 17
- 239000007791 liquid phase Substances 0.000 claims abstract description 60
- 239000007788 liquid Substances 0.000 claims abstract description 54
- 238000009825 accumulation Methods 0.000 claims description 15
- 239000012071 phase Substances 0.000 claims description 14
- 238000001179 sorption measurement Methods 0.000 claims description 13
- 239000013049 sediment Substances 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 8
- 239000004065 semiconductor Substances 0.000 claims description 7
- 230000008021 deposition Effects 0.000 claims description 6
- 239000004020 conductor Substances 0.000 claims description 5
- 238000003958 fumigation Methods 0.000 claims description 4
- 230000009469 supplementation Effects 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 abstract description 19
- 230000000694 effects Effects 0.000 abstract description 9
- 238000010521 absorption reaction Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 4
- 241000196324 Embryophyta Species 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000005457 optimization Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 240000002853 Nelumbo nucifera Species 0.000 description 2
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 2
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000241 respiratory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
Landscapes
- Separation Of Particles Using Liquids (AREA)
- Electrostatic Separation (AREA)
Abstract
The invention relates to an electrostatic water washing dust removing apparatus, which comprises a housing, wherein the housing is provided with a gas inlet pipe and a gas exhaust pipe, a liquid phase labyrinth is arranged inside the housing, the gas inlet of the liquid phase labyrinth is communicated with the gas inlet pipe, the gas outlet is communicated with the gas exhaust pipe, at least the partial liquid phase labyrinth is immersed in a liquid, the liquid phase labyrinth is formed by straggeredly arranging a plurality of horizontally arranged separation plates, at least the facing-water surfaces of the separation plates are provided with a bristle layer, the upper portion of the liquid phase labyrinth gas inlet is provided with a negative ion device, the discharge electrode in the negative ion device is connected with the positive electrode of a power supply, and the liquid phase labyrinth is an electric conduction body and is connected with the negative electrode of the power supply or the ground. According to the present invention, the wet absorption way is used and the liquid phase labyrinth structure is matched, such that the dust in the air is effectively absorbed, and the indoor absorbable particles are reduced; and particularly the liquid phase labyrinth structure is used so as to prolong the contact time of the air and the liquid, and the negative ion device structure is matched so as to well adsorb the particles into the liquid, such that the dust removing effect is improved.
Description
Technical field
The present invention relates to the field of dedusting and control haze, especially a kind of electrostatic water washing dedust device.
Background technology
Under the weather condition that dust is larger, such as, under haze weather, indoor often dust is a lot, and affect the respiratory health of people, especially this situation of high building is even more serious.
The existing air purifier mode of filtering that adopts carrys out dust out more, Problems existing is, this filtration filter disc is difficult to filter short grained dust, the such as small particle of pm2.5 and following grade, the lung that still can enter into human body accumulates, and has a strong impact on healthy.And adopt more accurate filter disc can filter tiny particle, but this also produces new technical problem, more accurate filter disc is easy to be blocked by dust or fine particle thing, and the cost frequently changing filter disc is higher, and the filter disc changed cannot recycle, and causes new environmental pollution.
Use filter disc, especially more accurate filter disc, along with the prolongation windage of time strengthens gradually, energy consumption is higher, or scavenging efficiency reduces.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of electrostatic water washing dedust device, and can remove the dust in air, elimination efficiency is high, and energy consumption is low, and consumables cost is low.
For solving the problems of the technologies described above, the technical solution adopted in the present invention is: a kind of electrostatic water washing dedust device, comprise housing, housing is provided with air inlet pipe and blast pipe, liquid phase labyrinth is provided with in housing, the air inlet in liquid phase labyrinth is communicated with air inlet pipe, and gas outlet is communicated with blast pipe, and described liquid phase labyrinth is immersed in liquid at least in part;
Be provided with negative ion device on the top of liquid phase labyrinth air inlet, the discharge electrode in negative ion device is connected with the positive pole of power supply, and described liquid phase labyrinth is electric conductor, and liquid phase labyrinth is connected with the negative pole of power supply or/and the direct ground connection in liquid phase labyrinth.
Described liquid phase labyrinth is formed by multiple horizontally disposed dividing plate interlaced arrangement, is at least provided with bristle layer at the upstream face of dividing plate.
Described liquid phase labyrinth is general frame structure, is provided with oscillator at the outer wall of liquid phase labyrinth framework, is also provided with multiple flexible member for supporting.
Described blast pipe is also communicated with liquid back pipe, and liquid back pipe is communicated with sediment accumulation area, is provided with sloping plate deposition district at sediment accumulation area, and the bottom of sediment accumulation area is provided with scum pipe, and the top of slag accumulation area is communicated with liquid phase labyrinth by liquid return hole.
Also be provided with gas phase labyrinth, the import in gas phase labyrinth is connected with the gas outlet in liquid phase labyrinth, and the outlet in gas phase labyrinth is communicated with blast pipe;
In described gas phase labyrinth, multiple horizontal baffle interlaced arrangement composition first order labyrinth, multiple vertical baffle interlaced arrangement becomes labyrinth, the second level, is at least provided with adsorption layer in the windward side of horizontal baffle and vertical baffle.
In liquid phase labyrinth, be also provided with shower nozzle, shower nozzle is communicated with the position of housing near bottom with pump by pipeline, or is communicated with the position bottom liquid back pipe.
Also be provided with condensing unit, the heat exchanger fin of condensing unit is placed in blast pipe, and heat exchanger fin is connected with the cold pole of semiconductor chilling plate, and the thermoae of semiconductor chilling plate is connected with heat abstractor.
Described heat abstractor is air-cooled or water cooling plant;
Be provided with shower nozzle in liquid phase labyrinth or case top, shower nozzle is communicated with below the liquid level of liquid in housing with pump by pipeline;
Described water cooling plant and pipeline connection, utilize shower nozzle circulating fluid to lower the temperature;
Pipeline is also communicated with liquid supplementation pipe.
Described air inlet pipe or blast pipe are connected with new blower fan;
The entrance of air inlet pipe reaches outside body of wall.
Also fumigation device is provided with in blast pipe.
A kind of electrostatic water washing dedust device provided by the invention, by adopting the mode of liquid adsorption, coordinating the structure in liquid phase labyrinth, effectively having adsorbed the dust in air, decrease indoor adsorbable particle content.Especially adopt the structure in liquid phase labyrinth, extend the time of contact of air and liquid, play good dustproof function, compared with filter type of the prior art, indoor dust removing effects of the present invention is better, and energy consumption is low, and almost no material consumption, reduces use cost.Coordinate the structure of negative ion device, liquid phase labyrinth suitable for reading, the particle entered in air is become positively charged lotus, and liquid phase labyrinth is connected or ground connection with negative pole, thus can better particle is adsorbed onto in liquid, raising dust removing effects.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the invention will be further described:
Fig. 1 is overall structure schematic diagram of the present invention.
Fig. 2 is the overall structure schematic diagram of another embodiment of the present invention.
Fig. 3 is the structural representation in liquid phase labyrinth in the present invention.
In figure: body of wall 1, new blower fan 2, air inlet pipe 3, gas phase labyrinth 4, vertical baffle 41, horizontal baffle 42, shower nozzle 5, pipeline 6, water cooling plant 7, semiconductor chilling plate 8, liquid phase labyrinth 9, dividing plate 91, bristle layer 92, air inlet 93, gas outlet 94, oscillator 95, flexible member 96, heat exchanger fin 10, blast pipe 11, liquid return hole 12, liquid back pipe 13, sloping plate deposition district 14, sediment accumulation area 15, scum pipe 16, housing 17, pump 18, liquid supplementation pipe 19, negative ion device 20.
Detailed description of the invention
Embodiment 1:
As in Fig. 2, a kind of electrostatic water washing dedust device, comprises housing 17, and housing 17 is provided with air inlet pipe 3 and blast pipe 11, and described air inlet pipe 3 or blast pipe 11 are connected with new blower fan 2; Run to promote air.
Be provided with liquid phase labyrinth 9 in housing 17, the air inlet in liquid phase labyrinth 9 is communicated with air inlet pipe 3, and gas outlet is communicated with blast pipe 11;
Described liquid phase labyrinth 9 is immersed in liquid at least in part.Structure thus, extends the path exchanged between air and water, improves dust removing effects.
The scheme optimized is as in Fig. 2, and described liquid phase labyrinth 9 is formed by multiple horizontally disposed dividing plate 91 interlaced arrangement, is at least provided with bristle layer 92 at the upstream face of dividing plate 91.By the bristle layer 92 arranged, the bristle in multiple bristle layer 92 is pricked a bubble, which increases the contact area between air and water, further enhance dust removing effects.Bristle layer in this example adopts the structure of the firm thorn in similar thread gluing, preferably adopts nylon plastic(s) material.Upstream face in this example refers to the bottom surface of each dividing plate 91, when bubble rises, and the bottom surface meeting of each dividing plate 91 and bubble contact.
The scheme of further optimization is as in Fig. 2, negative ion device 20 is provided with on the top of liquid phase labyrinth 9 air inlet, discharge electrode in negative ion device 20 is connected with the positive pole of power supply, and described liquid phase labyrinth 9 is electric conductor, and liquid phase labyrinth 9 is connected with the negative pole of power supply or/and liquid phase labyrinth 9 directly ground connection.Structure thus, by the discharge electrode in negative ion device 20, its structure is of the prior art, comprise conductor, conductor is provided with multiple discharge electrode, the discharge electrode be connected with positive source makes to be become positively charged lotus by the particle at this place, and liquid phase labyrinth is connected with power cathode, or directly ground connection, or be connected with negative pole and ground connection simultaneously, thus the liquid making liquid phase labyrinth comprise in it becomes negative pole, utilize the gravitation of both positive and negative polarity to make liquid can better adsorption particle thing, this be especially effective for the particle compared with small particle diameter.Preferably, the supply voltage of use does not make air produce ionization.
The scheme of further optimization is as in Fig. 2,3, described liquid phase labyrinth 9 is general frame structure, movable is arranged in housing 17, air inlet pipe 3 is communicated with air inlet 93, gas outlet 94 is communicated with blast pipe 11, being provided with oscillator 95 at the outer wall of liquid phase labyrinth 9 framework, being also provided with multiple flexible member 96 for supporting, such as rubber column.By the vibration of oscillator 95, preferably adopt piezoelectric-type ultrasonic oscillator, make the general frame vibration at high speed in liquid phase labyrinth 9, thus drive the liquid at high speed in it to vibrate, make liquid produce " cavitation " effect; After combining with the structure of the bristle layer 92 preferably arranged, further increase the contact area of air and liquid, make the dust in air adsorb by liquid.Preferred further, in blast pipe 11, be provided with particle somascope, this is existing in prior art, oscillator 95 start and stop are controlled by particle somascope, when detecting that particle content then starts oscillator 95 higher than threshold values, otherwise do not start, to reduce energy consumption and noise.
The scheme of further optimization as shown in Figure 2, described blast pipe 11 is also communicated with liquid back pipe 13, liquid back pipe 13 is communicated with from the position bottom housing 17 with sediment accumulation area 15, sloping plate deposition district 14 is provided with at sediment accumulation area 15, the bottom of sediment accumulation area 15 is provided with scum pipe 16, and the top of slag accumulation area 15 is communicated with liquid phase labyrinth 9 by liquid return hole 12.Structure thus, utilizes the circulation of liquid to make the particle of absorption precipitated, to increase the adsorption capacity of liquid, avoids the particle adsorbed to form secondary pollution after saturation.During use, air through adsorption cleaning is drained into blast pipe 11 from gas outlet 94, now may to carry under one's arms in air draught partially liq, gas-water separation is carried out at liquid back pipe 13, gas enters into blast pipe 11, liquid then enters into sediment accumulation area 15 downwards, after liquid level raises herein, liquid upwards flows with lower speed, precipitate through sloping plate deposition district 14, now in sloping plate deposition district 14, carry out Separation of Solid and Liquid, liquid upwards enters liquid phase labyrinth 9 through liquid return hole 12 and carries out air adsorption, the solid of particle is then downward, be deposited in sediment accumulation area 15, discharge from scum pipe 16 through valve.After have employed this structure, significantly extend the interval time changing liquid.
In the scheme further optimized, see Fig. 1, be provided with shower nozzle 5 in liquid phase labyrinth 9 or housing 17 top, shower nozzle 5 is communicated with below the liquid level of liquid in housing 17 with pump 18 by pipeline 6; In figure for ease of observe be communicated with the position of liquid back pipe 13, also can be communicated with in the position of liquid return hole 12.Shower nozzle 5 is arranged in the rising passway in liquid phase labyrinth 9 in this example, this further enhances the effect of spraying and dedusting.
For avoiding indoor humidity excessive, be also provided with condensing unit, see Fig. 1 at blast pipe 11.The heat exchanger fin 10 of condensing unit is placed in blast pipe 11, and heat exchanger fin 10 is connected with the cold pole of semiconductor chilling plate 8, and the thermoae of semiconductor chilling plate 8 is connected with heat abstractor.Described heat abstractor is air-cooled or water cooling plant; Structure thus, the moisture after purification in gas is met condensation and is formed water at heat exchanger fin 10 place, thus avoids indoor humidity too high.
Preferred scheme is as in Fig. 1, and described water cooling plant is communicated with pipeline 6, utilizes shower nozzle circulating fluid to lower the temperature; Structure thus, improves the cooling effect of heat abstractor, also utilizes the circulation power of shower nozzle.
Pipeline 6 is also communicated with liquid supplementation pipe 19.Structure thus, is convenient to the liquid level liquid make-up according to liquid.
The entrance of air inlet pipe 3 reaches outside body of wall 1.Structure thus, is convenient to introduce new wind outdoor, after device purifying and dedusting of the present invention, be sent to each room, preferably, in the position away from air inlet pipe, arranges exhaust apparatus, to form circulation, guarantees the pure and fresh cleaning of room air.The present invention also can with other indoor air handlers, the device of such as photocatalyst and so on combinationally uses to reach better effect.Owing to present invention employs the mode of circulating air, new wind supplements sufficient, and air is changed very fast, and the matching requirements for this kind of removal harmful organic substance gas is not high.
Also fumigation device is provided with in blast pipe 11.Utilize the air-flow evaporation stacte in blast pipe 11, improve air quality further.Fumigation device in this example is prior art, preferably adopts the structure in container liquid or solid essential oil being placed on hollow out ventilation.
Embodiment 2:
On the basis of embodiment 1, as shown in fig. 1, be also provided with gas phase labyrinth 4, the import in gas phase labyrinth 4 is connected with the gas outlet in liquid phase labyrinth 9 structure optimized further, and the outlet in gas phase labyrinth 4 is communicated with blast pipe 11;
In described gas phase labyrinth 4, multiple horizontal baffle 42 interlaced arrangement composition first order labyrinth, multiple vertical baffle 41 interlaced arrangement becomes labyrinth, the second level, is at least provided with adsorption layer in the windward side of horizontal baffle 42 and vertical baffle 41.Structure thus, realizes the supplementary absorption to particulate in air, and be also conducive to reducing the drop in air simultaneously, thus reduce the humidity of air-out, this structure also reduces windage.Adsorption layer in this example can adopt band fabric villous, to improve the contact area with air.The structure in gas phase labyrinth proposes a kind of new thinking, namely utilizes the mode of centrifugal absorption and non-filtered, and adsorption layer is convenient to cleaning, and compared with filter screen, service life significantly extends.
The multistage labyrinth structure that the horizontal baffle 42 arranged and vertical baffle 41 combine, its core is the number of times adding turning, turn each time, under centrifugal action, some dust of capital or drop are centrifuged power and are thrown to adsorption layer, thus adsorbed by adsorption layer, this structure can adsorb to fall most larger-diameter particle in advance, such as, be greater than the particle of PM10.And compared to filter screen, adsorption layer is convenient to repeated washing, therefore service life is longer, and windage is less.
The above embodiments are only the preferred technical solution of the present invention; and should not be considered as restriction of the present invention; the technical scheme that protection scope of the present invention should be recorded with claim, the equivalents comprising technical characteristic in the technical scheme of claim record is protection domain.Namely the equivalent replacement within the scope of this improves, also within protection scope of the present invention.
Claims (10)
1. an electrostatic water washing dedust device, comprise housing (17), housing (17) is provided with air inlet pipe (3) and blast pipe (11), it is characterized in that: in housing (17), be provided with liquid phase labyrinth (9), the air inlet in liquid phase labyrinth (9) is communicated with air inlet pipe (3), gas outlet is communicated with blast pipe (11), and described liquid phase labyrinth (9) is immersed in liquid at least in part.
2. a kind of electrostatic water washing dedust device according to claim 1, is characterized in that: described liquid phase labyrinth (9) is formed by multiple horizontally disposed dividing plate (91) interlaced arrangement, is at least provided with bristle layer (92) at the upstream face of dividing plate (91).
3. a kind of electrostatic water washing dedust device according to claim 2, it is characterized in that: described liquid phase labyrinth (9) is general frame structure, being provided with oscillator (95) at the outer wall of liquid phase labyrinth (9) framework, being also provided with multiple flexible member (96) for supporting.
4. a kind of electrostatic water washing dedust device according to claim 1, it is characterized in that: described blast pipe (11) is also communicated with liquid back pipe (13), liquid back pipe (13) is communicated with sediment accumulation area (15), sloping plate deposition district (14) is provided with at sediment accumulation area (15), the bottom of sediment accumulation area (15) is provided with scum pipe (16), and the top of slag accumulation area (15) is communicated with liquid phase labyrinth (9) by liquid return hole (12).
5. a kind of electrostatic water washing dedust device according to claim 4, is characterized in that: be also provided with gas phase labyrinth (4), and the import of gas phase labyrinth (4) is connected with the gas outlet of liquid phase labyrinth (9), and the outlet of gas phase labyrinth (4) is communicated with blast pipe (11);
In described gas phase labyrinth (4), multiple horizontal baffle (42) interlaced arrangement composition first order labyrinth, multiple vertical baffle (41) interlaced arrangement becomes labyrinth, the second level, is at least provided with adsorption layer in the windward side of horizontal baffle (42) and vertical baffle (41).
6. a kind of electrostatic water washing dedust device according to claim 5, it is characterized in that: in liquid phase labyrinth (9), be also provided with shower nozzle (5), shower nozzle (5) is communicated with the position of housing (17) near bottom with pump (18) by pipeline (6), or is communicated with the position near liquid back pipe (13) bottom.
7. a kind of electrostatic water washing dedust device according to claim 1, it is characterized in that: be also provided with condensing unit, the heat exchanger fin (10) of condensing unit is placed in blast pipe (11), heat exchanger fin (10) is connected with the cold pole of semiconductor chilling plate (8), the thermoae connection with heat abstractor of semiconductor chilling plate (8).
8. a kind of electrostatic water washing dedust device according to claim 7, is characterized in that: described heat abstractor is air-cooled or water cooling plant;
Be provided with shower nozzle (5) in liquid phase labyrinth (9) or housing (17) top, shower nozzle (5) is communicated with below the liquid level of housing (17) interior liquid with pump (18) by pipeline (6);
Described water cooling plant is communicated with pipeline (6), utilizes shower nozzle circulating fluid to lower the temperature;
Pipeline (6) is also communicated with liquid supplementation pipe (19).
9. a kind of electrostatic water washing dedust device according to claim 1, is characterized in that: described air inlet pipe (3) or blast pipe (11) are connected with new blower fan (2);
The entrance of air inlet pipe (3) reaches outside body of wall (1);
Also fumigation device is provided with in blast pipe (11).
10. a kind of electrostatic water washing dedust device according to claim 1, it is characterized in that: be provided with negative ion device (20) on the top of liquid phase labyrinth (9) air inlet, discharge electrode in negative ion device (20) is connected with the positive pole of power supply, described liquid phase labyrinth (9) is electric conductor, and liquid phase labyrinth (9) are connected with the negative pole of power supply or/and liquid phase labyrinth (9) directly ground connection.
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 |
Applications Claiming Priority (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 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104998496A true CN104998496A (en) | 2015-10-28 |
| CN104998496B CN104998496B (en) | 2019-05-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410154662.4A Active CN104998496B (en) | 2014-04-17 | 2014-04-17 | Static Electric Water washes dust-extraction unit |
Country Status (1)
| Country | Link |
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| CN (1) | CN104998496B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664632A (en) * | 2016-01-26 | 2016-06-15 | 梁小利 | Efficient treatment device for industrial waste gas |
| CN106000646A (en) * | 2016-06-08 | 2016-10-12 | 深圳奇滨科技开发有限公司 | Water soluble dust removing device |
| CN106351694A (en) * | 2016-10-19 | 2017-01-25 | 河北科技大学 | Tunnel dust removal method |
| CN106474862A (en) * | 2016-11-11 | 2017-03-08 | 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 |
| CN112452085A (en) * | 2020-10-30 | 2021-03-09 | 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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2014
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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 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664632A (en) * | 2016-01-26 | 2016-06-15 | 梁小利 | Efficient treatment device for industrial waste gas |
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| 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 |
| CN112452085A (en) * | 2020-10-30 | 2021-03-09 | 武汉慕都环境科技有限公司 | Automatic dust removal control system and method |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104998496B (en) | 2019-05-17 |
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