CN204051312U - Atomization dust-collecting equipment - Google Patents
Atomization dust-collecting equipment Download PDFInfo
- Publication number
- CN204051312U CN204051312U CN201420405158.2U CN201420405158U CN204051312U CN 204051312 U CN204051312 U CN 204051312U CN 201420405158 U CN201420405158 U CN 201420405158U CN 204051312 U CN204051312 U CN 204051312U
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- CN
- China
- Prior art keywords
- device body
- exhaust gas
- collecting equipment
- gas entrance
- kuppe
- 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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- 238000000889 atomisation Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000004458 analytical method Methods 0.000 claims abstract description 8
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 5
- 239000010959 steel Substances 0.000 claims abstract description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 abstract description 12
- 239000000428 dust Substances 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 abstract description 6
- 239000002912 waste gas Substances 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 abstract description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 3
- 239000004568 cement Substances 0.000 abstract description 2
- 239000003245 coal Substances 0.000 abstract description 2
- 230000005611 electricity Effects 0.000 abstract description 2
- 229910052742 iron Inorganic materials 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 3
- 238000002663 nebulization Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 238000010616 electrical installation Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Landscapes
- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model discloses atomization dust-collecting equipment, the side of device body is provided with exhaust gas entrance, at least one Fans is provided with in this exhaust gas entrance, the side of blower fan is exhaust gas entrance, the opposite side genesis analysis that the opposite side of blower fan is provided with kuppe device body has catch net mechanism, form closed mixed flow room between this catch net mechanism and kuppe, this space, mixed flow room and at least one air compressor machine pipeline UNICOM, be provided with water fog generator in device body.1, waste gas and water smoke hang time reached for 2 seconds, made the collision adsorption probability of micronic dust and water droplet in air improve more than hundred times; 2, device possesses interception function, reaches the object catching micronic dust; 3, the device scope of application is extensive, and the method is not only applicable to high pollution discharge unit, as enterprises such as coal electricity, iron and steel, cement, chemical industry, shipbuildings; 4, energy consumption is low; 5, low cost of manufacture; 6, purification efficiency is high, and clearance reaches 91%, benzene 49%, toluene 72%, dimethylbenzene 87.5%, sulfur dioxide 37%, nitrogen oxide 89%.
Description
Technical field
The utility model relates to the technical field of industrial nebulization dust system, a kind of specifically can the nebulization dust unit of modular organization, particularly its unit internal structure.
Background technology
Conventional wet dust collection method mainly adopts Water spray natural subsidence mode, and the water droplet particle that the method is sprayed, generally at 60 ~ 150 microns, then relies on dust in water droplet and air to collide, is adsorbed in water droplet, directly brings sewage discharge into.
Summary of the invention
The purpose of this utility model is to provide atomization dust-collecting equipment, and the water fog generator in device makes water fogging, and water fog particle reaches 10 microns-15 microns, makes the aerial density of water droplet increase by 25 times, thus makes the corresponding raising of seizure micronic dust ability.
To achieve these goals, the technical solution of the utility model is: atomization dust-collecting equipment, it comprises device body, the side of described device body is provided with exhaust gas entrance, at least one Fans is provided with in this exhaust gas entrance, the side of blower fan is exhaust gas entrance, the opposite side genesis analysis that the opposite side of blower fan is provided with kuppe device body has catch net mechanism, closed mixed flow room is formed between this catch net mechanism and kuppe, this space, mixed flow room and air compressor machine pipeline UNICOM, be provided with water fog generator in device body.
The utility model discloses atomization dust-collecting equipment, 1, device arranges mixed flow room, make waste gas and water smoke hang time reach 2-3 second, 0.2 second of naturally landing than water droplet increases by 10 times, and binomial measure makes the collision adsorption probability of micronic dust and water droplet in air improve more than hundred times.2, device possesses interception function, above-mentioned binomial measure reaches the object catching micronic dust, if but let alone evaporation and reenter air, appoint and so can not reach purification object, tackle medium overstocked, cause process exhaust gas flow to reduce, Long-Time Service will produce clogging (as ceramic material, active carbon, fiber cloth, Electrostatic Absorption etc.).Medium is crossed rare, cannot fully intercept and capture.The interception medium that this device adopts can ensure that being subject to processing waste gas can smooth and easyly for a long time pass through, and can make again more than 95% water smoke be caught, collect.Interception material adopts chemical fibre net or 304 stainless (steel) wires of three layers of waterproof, corrosion resistant, and filter opening diameter reaches 0.5 millimeter-0.8 millimeter, the longitude and latitude spacing of filter opening 1.0 millimeters-1.8 millimeters.3, the device scope of application is extensive, and the method is not only applicable to high pollution discharge unit, as enterprises such as coal electricity, iron and steel, cement, chemical industry, shipbuildings.Because of the unrestricted characteristic of its large discharge so also very effective to regional space, every public building possessing consentrated air supply system such as such as office building, hotel, hospital, market, school, gymnasium etc. all obtains pure air by this device.Even after miniaturization to indoor family all very applicable (current family type all adopts electrostatic, active carbon, filter cloth, micropore ceramics to make filter material, and Long-Time Service is diminishing efficiency not only, even produces secondary pollution).4, energy consumption is low, because the filtration interception mode air drag adopted is little, is only 5.6 kilowatts, water consumption 100 liters with this device process 15000 cubes of ms/h of waste gas power consumptions.Such as 1000 square metres of factory building every day (8 hours) energy consumptions are no more than 50.00 yuans (except family types).Be really " environmental protection is energy-conservation again ".Because all equipment all can recycle for a long time, the maintaining expense of equipment is extremely low, does not substantially exist.5, low cost of manufacture, owing to adopting particular form, structure, becomes hundred times and improves treatment effect, so also can correspondingly reduce at double in exhaust-gas treatment unit cost.Necessary accessories Jun Shi domestic enterprise matured product used in device production process, price advantage is apparent.6, purification efficiency is high, now detect through First proof machine that single treatment Removal efficiency of particulate matter reaches 91%, benzene 49%, toluene 72%, dimethylbenzene 87.5%, sulfur dioxide 37%, nitrogen oxide 89%, sampling Airflow amount is 8000 cubes ms/h, and current proof machine is as promoted at double through reforming processing ability.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Fig. 2 is the utility model nebulization dust process chart
detailed description of the invention
With reference to the accompanying drawings, the utility model is described further.
Wherein:
1, device body;
2, exhaust gas entrance;
3, blower fan;
4, kuppe;
5, catch net mechanism;
6, mixed flow room;
7, air compressor machine;
8, water fog generator;
9, electric box;
10, clean air outlet.
The utility model is atomization dust-collecting equipment, it comprises device body 1, it is different from prior art and is: the side of described device body 1 is provided with exhaust gas entrance 2, at least one Fans 3 is provided with in this exhaust gas entrance 2, the side of blower fan 3 is exhaust gas entrance 2, the opposite side genesis analysis that the opposite side of blower fan 3 is provided with kuppe 4 device body 1 has catch net mechanism 5, closed mixed flow room 6 is formed between this catch net mechanism 5 side and kuppe 4, catch net mechanism 5 opposite side forms clean air outlet 10, this space, mixed flow room 6 and air compressor machine 7 pipeline UNICOM, water fog generator 8 is provided with in device body 1, compressed air can promote the absorption of water fog particle and floating dust, the effect of cohesion.
In the specific implementation, described water fog generator 8 is arranged in mixed flow room 6 or is arranged in kuppe 4, the water fog particle that water fog generator 8 generator occurs 10 microns-15 microns, the mode of water fog generator 8 is that 3 kilograms of-8 kilograms of pressure-airs blow and spray current and cause water smoke to occur.
In the specific implementation, described catch net mechanism 5 is made up of the fleece of at least three layers of genesis analysis or the stainless (steel) wire of at least three layers of genesis analysis, and above-mentioned two kinds of materials all have the characteristic of waterproof, corrosion resistant, adopts framework plug in construction, is easy to regular maintenance.
In the specific implementation, described web surface is distributed with filter opening, 0.5 millimeter-0.8 millimeter, the position, aperture of filter opening, the longitude and latitude spacing between filter opening 1.0 millimeters-1.8 millimeters.
In the specific implementation, according to actual conditions, some device bodies 1 can transverse direction or vertical modularization superposition, form rectangular distribution, matrix can be single or multiple lift.
In the specific implementation, the electrical installation such as above-mentioned blower fan, air compressor machine, water fog generator is all connected with electric box 9 electric wiring of device body.
This device can install impinger at air inlet and air outlet, in use to carry out on-line monitoring, early warning, run to improve Automated condtrol, when specially treated being carried out to waste gas as needed interpolation chemical liquid for some, also can realize quantified controlling.
Above content is in conjunction with concrete preferred embodiment further detailed description of the utility model, can not assert that the utility model is specifically implemented to be confined to these explanations above-mentioned.For the utility model person of an ordinary skill in the technical field, without departing from the concept of the premise utility, some simple deduction or replace can also be made, all should be considered as belonging to protection domain of the present utility model.
Claims (5)
1. atomization dust-collecting equipment, it comprises device body (1), it is characterized in that: the side of described device body (1) is provided with exhaust gas entrance (2), at least one Fans (3) is provided with in this exhaust gas entrance (2), the side of blower fan (3) is exhaust gas entrance (2), the opposite side genesis analysis that the opposite side of blower fan (3) is provided with kuppe (4) device body (1) has catch net mechanism (5), closed mixed flow room (6) is formed between this catch net mechanism (5) and kuppe (4), this mixed flow room (6) space platform air compressor machine (7) pipeline UNICOM, water fog generator (8) is provided with in device body (1).
2. atomization dust-collecting equipment according to claim 1, is characterized in that: described water fog generator (8) is arranged in mixed flow room (6) or is arranged in kuppe (4), the water fog particle that water fog generator (8) generator occurs 10 microns-15 microns.
3. atomization dust-collecting equipment according to claim 1, is characterized in that: described catch net mechanism (5) is made up of the fleece of at least three layers of genesis analysis or the stainless (steel) wire of at least three layers of genesis analysis.
4. atomization dust-collecting equipment according to claim 3, is characterized in that: described web surface is distributed with filter opening, 0.5 millimeter-0.8 millimeter, the position, aperture of filter opening, the longitude and latitude spacing between filter opening 1.0 millimeters-1.8 millimeters.
5. atomization dust-collecting equipment according to claim 1, is characterized in that: described some device bodies (1) can transverse direction or vertical modularization superposition, form rectangular distribution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420405158.2U CN204051312U (en) | 2014-07-22 | 2014-07-22 | Atomization dust-collecting equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420405158.2U CN204051312U (en) | 2014-07-22 | 2014-07-22 | Atomization dust-collecting equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204051312U true CN204051312U (en) | 2014-12-31 |
Family
ID=52192907
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420405158.2U Expired - Fee Related CN204051312U (en) | 2014-07-22 | 2014-07-22 | Atomization dust-collecting equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204051312U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104083971A (en) * | 2014-07-22 | 2014-10-08 | 顾宝君 | Atomized dust removing device and dust removing process thereof |
-
2014
- 2014-07-22 CN CN201420405158.2U patent/CN204051312U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104083971A (en) * | 2014-07-22 | 2014-10-08 | 顾宝君 | Atomized dust removing device and dust removing process thereof |
| CN104083971B (en) * | 2014-07-22 | 2016-08-31 | 顾宝君 | Atomization dust-collecting equipment and dust collecting process thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190528 Address after: 201399 No. 4, 451 Zhonglu Park, Nanhui Industrial Park, Shanghai Patentee after: BOA (SHANGHAI) BELLOWS TECHNOLOGY CO., LTD. Address before: 201716 No. 25, Lane 588, Liantang Road, Liantang Industrial Park, Qingpu District, Shanghai Patentee before: Gu Baojun |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141231 Termination date: 20200722 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |