CN208493628U - A kind of oblique cutting type smoke duster - Google Patents
A kind of oblique cutting type smoke duster Download PDFInfo
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- CN208493628U CN208493628U CN201820521190.5U CN201820521190U CN208493628U CN 208493628 U CN208493628 U CN 208493628U CN 201820521190 U CN201820521190 U CN 201820521190U CN 208493628 U CN208493628 U CN 208493628U
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- expansion chamber
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Abstract
The utility model discloses a kind of oblique cutting type smoke dusters.It mainly include water supplying pipe, expansion chamber, water curtain water spray group;The water supplying pipe is divided into water main and water supply pipe, and water main is parallel with expansion chamber, and water supply pipe is vertically connected on water main;The expansion chamber is divided into inlet portion, enlarged portion and contraction flow region;The water curtain water spray group is arranged in expansion chamber, is divided into four groups;First, second group of setting is arranged in inlet portion, third group in enlarged portion, and the 4th group of setting is in contraction flow region;First, second group every group by three row's sparge pipe groups at third group is by five row's sparge pipe groups at the 4th row is by row's sparge pipe groups at the above-mentioned every row's sparge pipe of four groups of water curtains water spray group installs five vortex injectors;The sparge pipe is connected with water supply pipe;The enlarged portion height of expansion chamber is higher than inlet portion, and contraction flow region is contour with enlarged portion, and width is less than enlarged portion.The utility model is especially pronounced for the removal effect of soot dust granule object, can in scavenging 90% or more soot dust granule.
Description
Technical field
The present invention relates to a kind of oblique cutting type smoke dusters, belong to factory's environmental protection machinery.
Background technique
Factory's dedusting generally uses gallet water curtain dust collector, and by cylinder lower part along being introduced tangentially into, rotation rises dusty gas,
Grit is acted on by centrifugal force and is separated, and is thrown to cylinder inboard wall, is adsorbed by cylinder inboard wall flowing water film layer, on earth with water flow
Portion's cone, draws off through dust-exhausting port.The formation of water film is by being arranged in the several nozzles in the top of cylinder, water being sprayed onto device along tangential
Wall.
This deduster structure is simple, and metal consumption is small, water consumption is small, the disadvantage is that larger, the difficult arrangement of height, and
There is water phenomenon in actual motion, easily causes air-introduced machine band water, and cause draught fan impeller perishable.
But with the continuous improvement of environmental protection standard, smoke emissioning concentration control is increasingly stringenter, " boiler atmosphere pollution row
Put standard " GB 13271-2014 is instead of GB13271-2001, and particulate matter is by original 250mg/m3It is reduced to 80mg/m3(other refer to
It is smaller to mark sulfur dioxide, nitrogen oxides, mercury and other compounds contents, energy qualified discharge), only using gallet water curtain dust collector
Qualified discharge can be maintained reluctantly, and discharged gas fume particulate matter about 70mg/m3 has been approached concentration of emission limit value.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of oblique cutting type smoke dusters, solve traditional deduster and set
Standby difficult arrangement, the deficiency of dust removing effects difference.
In order to solve the above-mentioned technical problem, a kind of following technical scheme: oblique cutting type smoke duster is used, it is main to wrap
Include water supplying pipe, expansion chamber, water curtain water spray group;The water supplying pipe is divided into water main and water supply pipe, water main and expansion chamber
In parallel, water supply pipe is vertically connected on water main;The expansion chamber is divided into inlet portion, enlarged portion and contraction flow region;The water
Curtain water spray group is arranged in expansion chamber, is divided into four groups;First water curtain water spray group, the second water curtain water spray group are arranged in inlet portion, the
The setting of three water curtain water spray groups is arranged in enlarged portion, the 4th water curtain water spray group in contraction flow region;First water curtain water spray group, the spray of the second water curtain
Every group of water group by three row's sparge pipe groups at third water curtain water spray group is by five row's sparge pipe groups at the 4th water curtain water spray group is by a row
Sparge pipe groups are at the above-mentioned every row's sparge pipe of four groups of water curtains water spray group installs five vortex injectors;The sparge pipe with for moisture
Pipe is connected;
The enlarged portion height of the expansion chamber is higher than inlet portion, and contraction flow region is contour with enlarged portion, and width is less than enlarged portion.
The sparge pipe is connect with water supply pipe by wired hose, and valve is additionally provided between wired hose and water supply pipe
Door.
The vortex injector installation direction is backwards to flow of flue gas direction.
The vortex injector spray angle is 120 °.
The vortex injector material is 316L stainless steel.
Three water supply pipes connecting with inlet portion and enlarged portion are vertically arranged, and the water supply pipe connecting with contraction flow region is
It is horizontally disposed.
The invention belongs to wet scrubber, it is to make boiler smoke and water close contact, is touched using the inertia of water droplet and particle
The device for hitting other effect arrested particles or increasing particle, it is bulky grain that grit, which is collided with water droplet and agglomerated after shape contacts, and
It is taken away by water flow, more with the contact area of dusty gas, drop diameter is smaller, and water droplet is more, and collision agglutination efficiency is higher;When
The density of grit, partial size and relative velocity are bigger, and collision agglutination efficiency is higher.The present invention is capable of increasing contact of the water with flue gas
Area and density, partial size and the relative velocity for increasing grit.The present invention is especially pronounced for the removal effect of soot dust granule object,
Can in scavenging 90% or more soot dust granule, in " emission standard of air pollutants for boilers " GB13271-2014 standard
Grain object requires limit value by original 250mg/m380 mg/m3 are down to, by test, after the present invention, in the flue dust of discharge
Grain object content is by using 68.9mg/m3 of former gallet water curtain dust collector to be down to 27.0 mg/m3.
Detailed description of the invention
Fig. 1 is left view structure chart of the present invention.
Fig. 2 is Figure 1A-A cross-sectional view.
Fig. 3 is Figure 1B-B cross-sectional view.
Fig. 4 is Fig. 1 C-C cross-sectional view.
Fig. 5 is overlooking structure figure of the present invention.
Specific embodiment
Above-mentioned attached graph laplacian is as follows: expansion chamber 20, water main 11, water supply pipe 12, wired hose 13, valve 14;
Inlet portion 21, enlarged portion 22, contraction flow region 23;First water curtain water spray group 31, the second water curtain water spray group 32, third water curtain water spray group
33, the 4th water curtain water spray group 34, sparge pipe 35, vortex injector 36.
As shown in Figure 1, shown in Figure 5, the invention mainly comprises 20, four groups of water main 11, water supply pipe 12, expansion chamber water curtain sprays
Water group 31,32,33,34
As shown in Figure 1, the water supplying pipe is divided into water main 11 and water supply pipe 12, water main 11 is arranged in expansion chamber
It is parallel with expansion chamber 20 by the of 20;Water supply pipe 12 is connected on water main 11, vertical with water main 11.
As shown in Figure 1, shown in Figure 5, the expansion chamber 20 is square structure, is divided into three parts, and three parts are sequentially connected, point
Not Wei inlet portion 21, enlarged portion 22 and contraction flow region 23, enlarged portion 22 and inlet portion 21 are with wide, but height is higher than inlet portion 21,
Contraction flow region 23 and enlarged portion 22 are with height, but width is less than enlarged portion 22, and position is located at one close to water main 11
Side.
As Figure 1-Figure 5, the water curtain water spray group 31,32,33,34 is arranged inside expansion chamber 20, is divided into four groups;
In inlet portion 21, third water curtain water spray group 33 is arranged in enlarged portion for first water curtain water spray group 31, the setting of the second water curtain water spray group 32
22, the 4th water curtain water spray group 34 is arranged in contraction flow region 23;First water curtain water spray group 31, the second 32 every groups of water curtain water spray group are by three rows
Sparge pipe 35 forms, and the sparge pipe 35 is laterally setting, and every row's sparge pipe 35 installs five vortex injectors 36, the first water curtain
Water spray group 31 and the second water curtain water spray group 32 install 30 vortex injectors 36 altogether;Third water curtain water spray group 33 is sprayed water by five rows
Pipe 35 forms, and the sparge pipe 35 is laterally setting, and every row's sparge pipe 35 installs five vortex injectors 36, installs 25 altogether
A vortex injector 36;4th water curtain water spray group 34 is made of a sparge pipe 35, and the sparge pipe 35 is vertically arranged, water spray
There are five vortex injectors 36 for the installation of pipe 35;Above-mentioned four groups of water curtain water sprays group 3 installs 60 vortex injectors 36 altogether;It is described
Sparge pipe 35 is connect with water supply pipe 12 by wired hose 13, is additionally provided with valve between wired hose 13 and water supply pipe 12
14;Three water supply pipes 12 connecting with inlet portion 21 and enlarged portion 22 are vertically arranged, connect with contraction flow region 23 for moisture
Pipe 12 is horizontally disposed.Above-mentioned water main 11, water supply pipe 12 and sparge pipe 35 are all made of stainless steel tube.Using wired hose
13 connections, convenient for being checked sparge pipe 35 and vortex injector 36, being repaired.
As shown in Figure 1,36 spray regime of vortex injector is conical hollow, spray angle is 120 °, and material used is
316L, the arrangement and setting of vortex injector 36 ensure its spraying covering area overlapping, realize entirely section injection by spraying uniformly,
Comprehensively covering, can be generated under large-scale flow rate and pressure be evenly distributed, droplet size be medium spraying water curtain bigger than normal, increasing
Big flue gas and spraying contact area, big flow nozzle have big and smooth circulation road.The injection installation of vortex injector 36
Direction is backwards to flow of flue gas direction, and can reduce flue gas air inducing influences it, guarantees that the shape of water curtain is complete.
The principle of the present invention is such that in deduster there are two types of the ways of contact of gas and liquid, with preparatory dispersion
It is bubbled when the water contact of (atomization or moisture film) or gas impact water curtain, to form small water droplet or water mist.When gas is close to water
When drop, since the circular air film of water droplet acts on, gas streamline will change flow direction around water droplet, and motion profile becomes bent from straight line
Line, and partial size greatly and the big grit of density then tries hard to keep original streamline and with water droplet collision, grit and water droplet shape of colliding connects
Cohesion is bulky grain after touch, and is taken away by water flow, it is clear that bigger with the contact area of dusty gas, drop diameter is smaller, water droplet
More, collision agglutination efficiency is higher;When the density of grit, partial size and relative velocity are bigger, collision agglutination efficiency is higher.
Therefore, the design of this deduster mainly increases the contact area of water and flue gas and increases the density of grit, grain
Diameter and relative velocity.
Working condition of the invention is such that flue gas is discharged into expansion chamber 20 from boiler, first passes around inlet portion 21,
Inlet portion 21 is equipped with the first water curtain water spray group 31, the second water curtain water spray group 32, at this time smoke movement fast speed, rapidly with water
Mist collision agglutination;Enlarged portion 22 is subsequently entered, the inner space of enlarged portion 22 is the largest, and the third in enlarged portion 22 is arranged in
The vortex injector 36 that water curtain water spray group 33 is installed is also at most that smoke movement speed slows down at this time, therefore increases spray
Area contacts flue gas further with water mist and achievees the purpose that remove wherein particulate matter;Last flue gas enters contraction flow region 23, receives
The water mist that the 4th water curtain water spray group 34 that contracting portion 23 is installed is formed is full of whole cross section, forms comprehensive no dead angle spray, passes through
The air-flow of contraction flow region 23 causes air velocity to be promoted because of space contraction, and the water mist sprayed by vortex injector 36 is in high-speed flow
Impact under, be further atomized into smaller droplet, and the relative velocity of gas, liquid, solid (grain dirt) three-phase is all very big, makes them
It is sufficiently mixed.So far, 90% or more soot dust granule has been removed.
In practical operation, can according to the case where flue gas adjust 1-60 vortex injector 36 opening and closing situation, or with
Group or row are the opening and closing situation that unit adjusts every group or every row.
In practical operation, the present invention is also able to cooperate original granite water film dust tower and uses, by raw ramie stone water film dedusting tower
All dismountings are only used as to prevent air-introduced machine the de- mist device with water for internal setting.The remaining flue dust after dedusting in the present invention
After grain, water mist, dust-laden tangent enter granite water film dust tower, is formed and rotate upward contour stealth, due to different-grain diameter
Between grit or droplet, under the action of different inertia force, the biggish dust-laden drop of partial size is condensed into mutual making contact,
It under the action of gravity, inertia force, centrifugal force, separates from air-flow, is flowed down along king-tower wall, to reach its de- mist effect
Fruit reduces, prevents air-introduced machine band water.
Claims (7)
1. a kind of oblique cutting type smoke duster mainly includes water supplying pipe, expansion chamber (20), water curtain water spray group, it is characterised in that:
The water supplying pipe is divided into water main (11) and water supply pipe (12), and water main (11) is parallel with expansion chamber (20), for moisture
Pipe (12) is vertically connected on water main (11);The expansion chamber (20) is divided into inlet portion (21), enlarged portion (22) and contraction
Portion (23);The water curtain water spray group setting is divided into four groups in expansion chamber (20);First water curtain water spray group (31), the second water curtain
Water spray group (32) setting is arranged in inlet portion (21), third water curtain water spray group (33) in enlarged portion (22), the 4th water curtain water spray group
(34) it is arranged in contraction flow region (23);First water curtain water spray group (31), every group of the second water curtain water spray group (32) are by three row's sparge pipes
(35) it forms, third water curtain water spray group (33) is made of five row's sparge pipes (35), and the 4th water curtain water spray group (34) is sprayed water by one
(35) composition is managed, the above-mentioned every row's sparge pipe (35) of four groups of water curtains water spray group installs five vortex injectors (36);The sparge pipe
(35) it is connected with water supply pipe (12).
2. a kind of tiltedly cutting type smoke duster as described in claim 1, it is characterised in that: the expansion of the expansion chamber (20)
Portion (22) is highly higher than inlet portion (21), and contraction flow region (23) and enlarged portion (22) are contour, and width is less than enlarged portion (22).
3. a kind of tiltedly cutting type smoke duster as claimed in claim 2, it is characterised in that: the sparge pipe (35) and water supply
It is in charge of (12) to connect by wired hose (13), valve (14) is additionally provided between wired hose (13) and water supply pipe (12).
4. a kind of tiltedly cutting type smoke duster as claimed in claim 3, it is characterised in that: vortex injector (36) peace
Filling direction is backwards to flow of flue gas direction.
5. a kind of tiltedly cutting type smoke duster as claimed in claim 4, it is characterised in that: vortex injector (36) spray
Firing angle degree is 120 °.
6. a kind of tiltedly cutting type smoke duster as claimed in claim 5, it is characterised in that: vortex injector (36) material
Matter is 316L stainless steel.
7. a kind of tiltedly cutting type smoke duster as claimed in claim 6, it is characterised in that: with inlet portion (21) and enlarged portion
(22) three water supply pipes (12) connected are vertically arranged, and the water supply pipe (12) connecting with contraction flow region (23) sets for level
It sets.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820521190.5U CN208493628U (en) | 2018-04-13 | 2018-04-13 | A kind of oblique cutting type smoke duster |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820521190.5U CN208493628U (en) | 2018-04-13 | 2018-04-13 | A kind of oblique cutting type smoke duster |
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Publication Number | Publication Date |
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CN208493628U true CN208493628U (en) | 2019-02-15 |
Family
ID=65296403
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CN201820521190.5U Expired - Fee Related CN208493628U (en) | 2018-04-13 | 2018-04-13 | A kind of oblique cutting type smoke duster |
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CN (1) | CN208493628U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108355433A (en) * | 2018-04-13 | 2018-08-03 | 广西农垦糖业集团星星制糖有限公司 | A kind of oblique cutting type smoke duster |
-
2018
- 2018-04-13 CN CN201820521190.5U patent/CN208493628U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108355433A (en) * | 2018-04-13 | 2018-08-03 | 广西农垦糖业集团星星制糖有限公司 | A kind of oblique cutting type smoke duster |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address | ||
CP03 | Change of name, title or address |
Address after: 536015 Guangxi sugar group Xingxing Sugar Co., Ltd., Fucheng Town, Yinhai District, Beihai City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi sugar group Xingxing Sugar Co.,Ltd. Address before: 536000 the Guangxi Zhuang Autonomous Region Beihai Yinhai Fucheng Guangxi Nongken sugar group Xingxing Sugar Co., Ltd. Patentee before: GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP XINGXING SUGAR PRODUCTION Co.,Ltd. |
|
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190215 |