CN206391788U - Fountain inertial dust separator - Google Patents
Fountain inertial dust separator Download PDFInfo
- Publication number
- CN206391788U CN206391788U CN201621469675.1U CN201621469675U CN206391788U CN 206391788 U CN206391788 U CN 206391788U CN 201621469675 U CN201621469675 U CN 201621469675U CN 206391788 U CN206391788 U CN 206391788U
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- China
- Prior art keywords
- housing
- dust separator
- fountain
- air inlet
- inertial dust
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Abstract
The utility model discloses a kind of fountain inertial dust separator, including housing, dedusting chamber is provided with the housing, air inlet is provided with the side wall of the housing, the top of the housing is connected with discharge pipe, the bottom of the housing is provided with sewage draining exit, shower is installed on the housing of the air inlet, one end of the shower is stretched into the housing and is connected with nozzle component, spray control device is installed, the dedusting intracavitary is provided with multiple towards the nozzle component and the baffle plate for arrangement of falling successively on the shower;Flue gas need to first carry out spray process when entering inertial dust separator, and dust can be made to be combined with water and improve its settling efficiency;The utility model is simple to operate, only needs periodically by ash bucket deashing, operation, maintenance cost are low.
Description
Technical field
The utility model is related to a kind of cleaner, more particularly to a kind of inertial dust collection used cooperatively with water deduster
Device.
Background technology
The dust removal mechanism of water deduster is mainly drop and intergranular inertial collision and interception function.Impact type water dedusting
Device design parameter:It is adapted to 5 μm of particle diameter > grit;Efficiency of dust collection:> 95% (dust size is bigger, and efficiency of dust collection is higher);
Gas flow rate:10-20m/s;Gas liquid ratio:10-50L/m3;Equipment resistance:P=1200~2000Pa.
For the easy scale deposition of the larger flue gas of dust concentration, causing can not after water-level gauge (ball float) fouling in water dedusting
Dust Capacity is more in normal operation, deduster, changes water and deashing and just causes that equipment operation is obstructed or fume emission does not reach not in time
The problems such as mark.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of high fountain inertia of easy to operate, efficiency of dust collection
Deduster.
In order to solve the above technical problems, the technical solution of the utility model is:Fountain inertial dust separator, including housing,
It is provided with the housing on dedusting chamber, the side wall of the housing and is provided with air inlet, the top of the housing is connected with air-out
Pipe, the bottom of the housing, which is provided with sewage draining exit, the housing of the air inlet, is provided with shower, the shower
One end stretch into the housing and be connected with nozzle component, the shower spray control device is installed, the dedusting
Intracavitary is provided with multiple towards the nozzle component and the baffle plate for arrangement of falling successively.
As a kind of perferred technical scheme, the nozzle component includes multiple towards the baffle plate setting and radial
The nozzle of distribution.
As a kind of perferred technical scheme, the nozzle component is towards being provided with spray on the housing of air inlet side
Mouth backplate.
As a kind of perferred technical scheme, the spray control device includes the spray electricity being arranged on the shower
Magnet valve.
As a kind of perferred technical scheme, the baffle plate includes the baffle body being vertically arranged, the baffle body
Top is vertically installed with the anti-outflow flanging extended towards the air inlet.
As a kind of perferred technical scheme, the lower edge of two baffle plates farthest from the air inlet is intended to be less than institute
State the lower edge of air inlet.
By adopting the above-described technical solution, fountain inertial dust separator, including housing, dedusting is provided with the housing
Air inlet is provided with chamber, the side wall of the housing, the top of the housing is connected with discharge pipe, and the bottom of the housing is set
Have and shower is installed on sewage draining exit, the housing of the air inlet, one end of the shower is stretched into the housing
And be connected with nozzle component, the shower spray control device is installed, the dedusting intracavitary is provided with multiple towards institute
State nozzle component and the baffle plate for arrangement of falling successively;Flue gas need to first carry out spray process when entering inertial dust separator, can make dust
Combined with water and improve its settling efficiency;The utility model is simple to operate, only needs ash bucket deashing, operation, maintenance expense periodically
With low.
Brief description of the drawings
The following drawings is only intended to, in doing the utility model schematic illustration and explanation, not limit model of the present utility model
Enclose.Wherein:
Fig. 1 is the structural representation of the utility model embodiment;
In figure:11- housings;12- dedusting chambers;13- air inlets;14- discharge pipes;15- sewage draining exits;21- showers;22- sprays
Mouth;23- nozzle guards;24- spraying electromagnetic valves;3- baffle plates.
Embodiment
With reference to the accompanying drawings and examples, the utility model is expanded on further.In the following detailed description, only by saying
Bright mode describes some one exemplary embodiments of the present utility model.Undoubtedly, one of ordinary skill in the art can be with
Recognize, can be with a variety of modes to described in the case of without departing from spirit and scope of the present utility model
Embodiment is modified.Therefore, accompanying drawing and description are inherently illustrative, rather than for limiting the protection of claim
Scope.
As shown in figure 1, fountain inertial dust separator, including housing 11, dedusting chamber 12 is provided with the housing 11, it is described
Air inlet 13 is provided with the side wall of housing 11, the top of the housing 11 is connected with discharge pipe 14, the bottom of the housing 11
It is provided with the housing 11 at sewage draining exit 15, the air inlet 13 and shower 21 is installed, one end of the shower 21
Stretch into the housing 11 and be connected with nozzle component, the nozzle component includes multiple nozzles 22 radially distributed, institute
Nozzle component is stated towards nozzle guard 23 is provided with the housing 11 of the side of air inlet 13, nozzle guard 23 can use angle
Steel.Spray control device is installed, the spray control device includes being arranged on the shower 21 on the shower 21
Spraying electromagnetic valve 24, be provided with the dedusting chamber 12 it is multiple towards the nozzle component and the baffle plate 3 for arrangement of falling successively,
The baffle plate 3 includes the body of baffle plate 3 being vertically arranged, and the top of the body of baffle plate 3 is vertically installed with towards the air inlet
The anti-outflow flanging of 13 extensions, the lower edge of two baffle plates 3 farthest from the air inlet 13 is intended to be less than the air inlet
13 lower edge.
In the present embodiment, the installation site and quantity of nozzle component:Flue gas need to first be sprayed when entering inertial dust separator
Pouring is handled, and dust can be made to be combined with water and improve its settling efficiency, specific nozzle component is arranged at inertial dust separator smoke inlet,
And provided with protection devices such as angle steel;
In the present embodiment, the specific required quantity of nozzle 22 is then set according to air quantity and spray head parameter, and nozzle 22 exists
The anglec of rotation of nozzle 22 can be changed during setting, make its effect for not only acting as humidification gas also have cleaning to close on the double of baffle plate 3
Recast is used;
In the present embodiment, flue gas can change the flow trace of dust, be dropped by Action of Gravity Field when spraying at baffle plate 3
Into ash bucket, efficiency of dust collection is improved, the installation number of baffle plate 3 typically sets 5-10, set with specific reference to air force, air quantity
Bigger, the number of baffle plate 3 is also increased as;
The installation site of baffle plate 3 and shape:First of baffle plate 3 (thickness of slab 10mm) is set at the rear side 0.2-0.3m of nozzle 22,
Direct surrounding is welded on the housing 11 of inertial dust separator (shape is designed according to inertial dust separator inner shape).The second to four
Road baffle plate 3 be then arranged between the rear side of first baffle plate 3, baffle plate 3 be spaced in 0.3-0.5m or so (specific interval according to air quantity and
The size of inertial dust separator is determined), baffle plate 3 is bending tabular, can effectively intercept because air current flow direction changes and caused by
Grain beyond the region of objective existence stream, the size of top fold is in 0.05m or so, and the upper horizontal position of rear side baffle 3 is the horizontal centre of front side baffle plate 3
Or at position more on the upper side.5th road and baffle plate 3 afterwards, which are then spaced, increases to 0.5-0.8m, and shape is still direct for bending plate
It is welded on inertial dust separator housing 11.In addition, the vertical size of baffle plate 3 is then to ensure the lower horizontal of last twice baffle plate 3
On the basis of position is less than the lower horizontal height of inertial dust separator air inlet 13.
The utility model is added before impact type water deduster according to dust characteristic, fluid motion feature etc..Enter in deduster
Mouth, into the larger particulate matter of particle diameter, slow down the horizontal movement of dust added with spray equipment, spray droplet with dust perikinetic aggregation
Speed, (dust of 20-50 μm of particle diameter is applied to, equipment resistance is in 300-800Pa, efficiency of dust collection with common inertial dust separator
50-70%) compare, the dust of 5-20 μm of particle diameter, efficiency of dust collection > 85%, powder can be trapped added with the inertial dust separator of spray equipment
Dirt is discharged in dust collecting trough through ash bucket on the downside of inertial dust separator, and supernatant after precipitation is also recycled.
Fountain inertial dust separator (efficiency of dust collection > 85%) is used as primary dust removing device, the utility model (efficiency of dust collection
95%) as two-stage dust removal device, then efficiency of dust collection when running simultaneously is:
η=1- (1- η1)(1-η2)=1-0.15 × 0.05=99.25%
If deduster need to only reach 99% efficiency of dust collection, the efficiency of dust collection for only needing water deduster is 93.3%.
The design greatly alleviates the operating load and increase deashing and exchange water cycle of follow-up water deduster, reduces water
The operating cost of deduster.Improved inertial dust separator investment and operating cost are relatively low, but can reduce the concentration of emission of flue gas
Used with the cost of overhaul in later stage.Fountain inertial dust separator small volume, designed size is carried out with specific reference to exhaust gas volumn and containing Dust Capacity,
Water spray is with exhaust gas volumn ratio in 7.5*10-5—9.0*10-5L/m3Most preferably.
The determination of inertial dust separator appearance and size, it is 10m/s, pipe that flue gas, which enters flue gas flow rate after fountain inertial dust separator,
Road internal diameter is d, then grit is in the time that vertical direction is fallen on the downside of pipeline from top:Then horizontal direction flue gas is transported
Dynamic distance is:L=v0T (does not consider that smoke flow resistance loses), v0:Flue gas horizontal direction speed, l:Inertial dust separator air-flow
The length in direction, m;Original width when inertial dust separator flue gas has just enter into is:The size of ash bucket is then dense according to flue gas
Degree, efficiency of dust collection, deashing time determine the volume of ash bucket.
The present embodiment is applied to before impact type water deduster, and the dust of removal about 85%, reduction are handled as primary dust removing
The operating load of water deduster, it is ensured that flue gas qualified discharge.
The utility model has the following advantages that:
1st, equipment design is simple, low manufacture cost;
2nd, equipment operation is simple, only needs ash bucket deashing periodically, the dust on baffle plate 3 be with plate at vapor coagulate
Drippage enters ash bucket and removed after knot;
3rd, handled suitable for the dust that flue gas content is larger or moisture vapor amount is larger;
4th, operation, maintenance cost are low, only need to change nozzle 22;
5th, the gas flow rate in equipment is 2-3m/s;
6th, the coagulation that equipment is only handled as water deduster or other Wet smokes.
Description of the present utility model is provided for the sake of example and description, and is not exhaustively or by originally
Utility model is limited to disclosed form.Many modifications and variations are obvious for the ordinary skill in the art.
Selection and description embodiment are, in order to more preferably illustrate principle of the present utility model and practical application, and to make the common skill of this area
Art personnel are it will be appreciated that the utility model is so as to design the various embodiments with various modifications suitable for special-purpose.
Claims (6)
1. being provided with dedusting chamber in fountain inertial dust separator, including housing, the housing, it is provided with the side wall of the housing
Air inlet, the top of the housing is connected with discharge pipe, and the bottom of the housing is provided with sewage draining exit, it is characterised in that:It is described
Shower is installed, one end of the shower is stretched into the housing and is connected with jet head sets on the housing of air inlet
Spray control device is installed on part, the shower, the dedusting intracavitary be provided with it is multiple towards the nozzle component and according to
The baffle plate of secondary whereabouts arrangement.
2. fountain inertial dust separator as claimed in claim 1, it is characterised in that:The nozzle component includes multiple towards institute
The nozzle stated baffle plate setting and radially distributed.
3. fountain inertial dust separator as claimed in claim 1, it is characterised in that:The nozzle component is towards air inlet side
The housing on nozzle guard is installed.
4. fountain inertial dust separator as claimed in claim 1, it is characterised in that:The spray control device includes being arranged on
Spraying electromagnetic valve on the shower.
5. fountain inertial dust separator as claimed in claim 1, it is characterised in that:The baffle plate includes the baffle plate being vertically arranged
Body, the top of the baffle body is vertically installed with the anti-outflow flanging extended towards the air inlet.
6. the fountain inertial dust separator as described in claim 1 to 5 any claim, it is characterised in that:From the air intake
The lower edge of two farthest baffle plates of mouth is intended to the lower edge less than the air inlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621469675.1U CN206391788U (en) | 2016-12-29 | 2016-12-29 | Fountain inertial dust separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621469675.1U CN206391788U (en) | 2016-12-29 | 2016-12-29 | Fountain inertial dust separator |
Publications (1)
Publication Number | Publication Date |
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CN206391788U true CN206391788U (en) | 2017-08-11 |
Family
ID=59517549
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CN201621469675.1U Active CN206391788U (en) | 2016-12-29 | 2016-12-29 | Fountain inertial dust separator |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107344054A (en) * | 2017-08-29 | 2017-11-14 | 张久明 | A kind of apparatus and method of recyclable soot dust granule thing |
CN108261889A (en) * | 2018-01-18 | 2018-07-10 | 深圳市天得环境科技有限公司 | The exhaust-gas treatment spray system of easy care |
CN109224736A (en) * | 2018-09-27 | 2019-01-18 | 南通航运职业技术学院 | A kind of dust-extraction unit of imitative nasal cavity structure |
CN109647099A (en) * | 2019-01-25 | 2019-04-19 | 福州东旭光电科技有限公司 | Box cullet deduster |
CN110115899A (en) * | 2019-05-06 | 2019-08-13 | 山东钢铁集团有限公司 | Round steel continuous casting line fire cuts machine region mobile type dust collector and its application method |
-
2016
- 2016-12-29 CN CN201621469675.1U patent/CN206391788U/en active Active
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107344054A (en) * | 2017-08-29 | 2017-11-14 | 张久明 | A kind of apparatus and method of recyclable soot dust granule thing |
CN107344054B (en) * | 2017-08-29 | 2023-11-28 | 张久明 | Device and method capable of recycling smoke dust particles |
CN108261889A (en) * | 2018-01-18 | 2018-07-10 | 深圳市天得环境科技有限公司 | The exhaust-gas treatment spray system of easy care |
CN108261889B (en) * | 2018-01-18 | 2021-06-15 | 深圳市天得一环境科技有限公司 | Waste gas treatment spraying system easy to maintain |
CN109224736A (en) * | 2018-09-27 | 2019-01-18 | 南通航运职业技术学院 | A kind of dust-extraction unit of imitative nasal cavity structure |
CN109647099A (en) * | 2019-01-25 | 2019-04-19 | 福州东旭光电科技有限公司 | Box cullet deduster |
CN110115899A (en) * | 2019-05-06 | 2019-08-13 | 山东钢铁集团有限公司 | Round steel continuous casting line fire cuts machine region mobile type dust collector and its application method |
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