CN205549935U - Wet -type electric precipitation secondary absorption tower - Google Patents
Wet -type electric precipitation secondary absorption tower Download PDFInfo
- Publication number
- CN205549935U CN205549935U CN201620240866.4U CN201620240866U CN205549935U CN 205549935 U CN205549935 U CN 205549935U CN 201620240866 U CN201620240866 U CN 201620240866U CN 205549935 U CN205549935 U CN 205549935U
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- wet
- dust
- tower body
- absorption tower
- esp
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Abstract
The utility model discloses a wet -type electric precipitation secondary absorption tower, including the tower body, the tower body top has flue gas entry, its characterized in that: in the tower body from the top down guide plate, one -level shower, wet -type electricity dust collector, second grade shower set gradually and be used for separation large granule smoke and dust and adsorb the dust particle droplet lead the electric purification grid, the tower body bottom is provided with sewage port. The utility model discloses the electric purification grid of leading newly -increased on the basis on present wet -type electric precipitation absorption tower makes gas carry out the secondary dust removal. The increase should purify the grid, can ensure to export flue gas <= 5mgM3 after the high concentration flue gas is through this equipment.
Description
Technical field
This utility model relates to dedusting technology field, is specifically related to a kind of wet-esp two-level absorption tower.
Background technology
Nowadays the more of dedusting technology is exactly bag-type dust and electric precipitation, and electric precipitation can be divided into again dry type, half dry type
With wet type these three.Wet electrical dust precipitator is identical with dry electric precipitation device operation principle, is all to bear to electric field space conveying direct current
High pressure, is ionized by space gases, in flue gas after dust granules and droplet charging particle under the effect of electric field force, moves to receive
Dirt pole plate (colelctor electrode), thus it is collected in dust collector pole surface.Dry electric precipitation device utilizes vibration dust-cleaning mode to collect
Dust shakes off in ash bucket, and wet electrical dust precipitator is then by collecting the droplet granule in flue gas, is formed on dust collector pole surface
Overflow and dust is flushed in ash bucket (water ash bucket).Wet electrical dust precipitator is different from dry electric precipitation device maximum, is cigarette
The difference of gas working medium, dry electric precipitation device flue gas is dry flue gas, and flue-gas temperature is higher, is substantially free of droplet in flue gas.And wet type
Electric cleaner is wet saturated flue gas, and flue-gas temperature is relatively low, containing substantial amounts of droplet in flue gas.Wet electrical dust precipitator is generally arranged at
After wet desulphurization device, saturated flue gas is carried after desulfurization a large amount of water droplet, captured when by high voltage electric field, it is possible to reduce stone
The probability that cream rain is formed.Having preferable effect simultaneously for collecting fine particle PM2.5, acid mist etc., smoke dust discharge concentration can
To reach≤10 milligrams/cubic metre.
Summary of the invention
This utility model purpose is to provide one to remove than existing wet dust removal absorption tower dust removing effects more preferable wet type electricity
Dirt two-level absorption tower.
This utility model for achieving the above object, adopts the following technical scheme that
A kind of wet-esp two-level absorption tower, including tower body, described tower body top has smoke inlet, and its feature exists
In: be disposed with from top to bottom in described tower body deflector, one-level shower, Wet type electric dust-removing device, two grades of showers and
For intercepting bulky grain flue dust and adsorbing the conduction purification grid of grit droplet；Sewage mouth it is provided with bottom tower body.
It is further characterized by described conduction and purifies grid is electro-conductive glass steel grating plate, has the square of regular distribution
Shape and square space.
Preferred: described Wet type electric dust-removing device includes high-tension porcelain insulator, electric discharge coil holder, many discharge lines, dust legs and weighs
Hammer；Described high-tension porcelain insulator is arranged on electric discharge coil holder two ends, is used for connecting high-tension electricity；Described many discharge lines one end are evenly distributed on
On electric discharge coil holder, the other end hangs with weight；It is provided with dust leg in every discharge lines.
Described one-level shower and the NaOH solution that spray liquid is 5% of two grades of showers.
The advantage of this utility model wet-esp two-level absorption tower:
1, use novel corrosion-resistant composite as dust leg, modular construction, honeycomb arrangement, can effectively utilize sky
Between, Flow Field Distribution uniform.Corrosion-resistant, electric discharge strength is stable, makes equipment voltage, electric current be in higher parameter, thus ensures relatively
Good dust removing effects.
2, novel corrosion resistant composite is used to make electric precipitation (mist) device structure flexible arrangement, it is possible to adapt to current complexity
Transformation place, can individually be arranged in desulfurizing tower and export at clean gas flue, it is possible to be arranged in desulfurizing tower tower top, or be individually arranged in
The vacant lot that power plant's site condition allows.
Need not spray into continuously alkaline water when 3, running, rely on electric field region to collect flue fog drip, formed in dust leg
Overflow, reaches the purpose of gravity flow deashing.
4, wet electrical dust precipitator is one of current state-of-the-art PM2.5 control technology, can reach following performance indications:
Power consumption little (300,000 ten million unit power consumption≤300 kilowatt), resistance low (≤350 handkerchief)
Subparticle removal efficiency is high.PM2.5 concentration of emission≤1.5mg/M3, granular material discharged concentration≤10mg/M3.
Aerosol and sulfur trioxide removal efficiency 60%.
Heavy metal Hg removal efficiency about 40%.
Droplet clearance 85%.
5, newly-increased conduction purification grid makes gas carry out final dusting.Increase this purification grid, it can be ensured that high concentration
Flue gas is by exiting flue gas≤5mg/M after this equipment3 。
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Detailed description of the invention
As shown in Figure 1: from top to bottom, flue gas passes through deflector 2 to the smoke inlet 10 at flue gas tower body 1 top, makes gas equal
Even distribution.Being sprayed by one-level shower 3, spray uses the NaOH solution of 5% again, enters back into dedusting region by wet type electricity
Dust arrester carries out dedusting.Described Wet type electric dust-removing device includes high-tension porcelain insulator 4, electric discharge coil holder 5, many discharge lines 6, dust legs
11 and weight 7；Described high-tension porcelain insulator 4 is arranged on electric discharge coil holder 3 two ends, is used for connecting high-tension electricity；Described many discharge lines 6 one end
Being evenly distributed on electric discharge coil holder 3, the other end hangs with weight 7；It is provided with dust leg 11 in every discharge lines 6.At high-tension electricity
Under effect, in dust leg 11, create corona current and electric field intensity.Under the effect of electric field force, the grit in gas completes
Charged, mobile, sedimentation, flushing process, in gas, charged grit moves to dust leg 11, and gas is detained in dust leg 11, transports
Row obtains dedusting, gas outlet of finally going directly, be absorbed in the grit of dust leg 11 wall by the flushing of spray liquid after, pass through wet type
The sewage mouth 9 of dedusting absorption tower is discharged.Through the flue gas of Wet type electric dust-removing device after two grades of showers 3 spray, the most past
Under by conduction purify grid 8, carry out final dusting.It is electro-conductive glass steel grating plate that conduction purifies grid 8, uses molded
Technique make with the many rectangle of regular distribution, the polyester sheets in square space, there is the mechanical characteristics of the two-way same sex.Should
Conduction purifies grid 8 and can intercept bulky grain flue dust and adsorb certain grit droplet, and the grit of absorption can pass through spray liquid
Rinse to dirty.Sewage sewage mouth bottom absorption tower is discharged.
This utility model is through final dusting, it can be ensured that high-concentration fume is by exiting flue gas≤5mg/ after this equipment
M3。
Claims (4)
1. a wet-esp two-level absorption tower, including tower body, described tower body top has smoke inlet, it is characterised in that:
It is disposed with deflector, one-level shower, Wet type electric dust-removing device, two grades of showers in described tower body from top to bottom and uses
In intercepting bulky grain flue dust and adsorbing the conduction purification grid of grit droplet；Sewage mouth it is provided with bottom tower body.
Wet-esp two-level absorption tower the most according to claim 1, it is characterised in that: described conduction purifies grid for leading
Electricity glass fiber reinforced grid-like panel, has rectangle and the square space of regular distribution.
Wet-esp two-level absorption tower the most according to claim 1 and 2, it is characterised in that: described wet-esp fills
Put and include high-tension porcelain insulator, electric discharge coil holder, many discharge lines, dust leg and weight；Described high-tension porcelain insulator is arranged on electric discharge coil holder two
End, is used for connecting high-tension electricity；Described many discharge lines one end are evenly distributed on electric discharge coil holder, and the other end hangs with weight；Every
Dust leg it is provided with in discharge lines.
Wet-esp two-level absorption tower the most according to claim 1 and 2, it is characterised in that: described one-level shower and
The spray liquid of two grades of showers is the NaOH solution of 5%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620240866.4U CN205549935U (en) | 2016-03-25 | 2016-03-25 | Wet -type electric precipitation secondary absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620240866.4U CN205549935U (en) | 2016-03-25 | 2016-03-25 | Wet -type electric precipitation secondary absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205549935U true CN205549935U (en) | 2016-09-07 |
Family
ID=56815621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620240866.4U Expired - Fee Related CN205549935U (en) | 2016-03-25 | 2016-03-25 | Wet -type electric precipitation secondary absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205549935U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512667A (en) * | 2016-12-31 | 2017-03-22 | 江苏博际环境工程科技有限公司 | Wet-type variable-flow flue gas purification and downward wet-type static electricity combined ultralow flue gas emission device |
| CN106733185A (en) * | 2016-12-31 | 2017-05-31 | 江苏博际环境工程科技有限公司 | A kind of downstriker wet static dedusting demisting flue gas minimum discharge device |
| CN107470027A (en) * | 2017-08-23 | 2017-12-15 | 广州熠森能环保科技有限公司 | Function modoularization exhaust gas cleaner and domestic garbage disposer |
| CN108722094A (en) * | 2018-08-01 | 2018-11-02 | 南京龙源环保有限公司 | A kind of final dusting equipment for detaching fine particle dust in tail gas |
-
2016
- 2016-03-25 CN CN201620240866.4U patent/CN205549935U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512667A (en) * | 2016-12-31 | 2017-03-22 | 江苏博际环境工程科技有限公司 | Wet-type variable-flow flue gas purification and downward wet-type static electricity combined ultralow flue gas emission device |
| CN106733185A (en) * | 2016-12-31 | 2017-05-31 | 江苏博际环境工程科技有限公司 | A kind of downstriker wet static dedusting demisting flue gas minimum discharge device |
| CN107470027A (en) * | 2017-08-23 | 2017-12-15 | 广州熠森能环保科技有限公司 | Function modoularization exhaust gas cleaner and domestic garbage disposer |
| CN108722094A (en) * | 2018-08-01 | 2018-11-02 | 南京龙源环保有限公司 | A kind of final dusting equipment for detaching fine particle dust in tail gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160907 Termination date: 20210325 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |