CN207822768U - A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen - Google Patents
A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen Download PDFInfo
- Publication number
- CN207822768U CN207822768U CN201820001211.0U CN201820001211U CN207822768U CN 207822768 U CN207822768 U CN 207822768U CN 201820001211 U CN201820001211 U CN 201820001211U CN 207822768 U CN207822768 U CN 207822768U
- Authority
- CN
- China
- Prior art keywords
- desulfurization
- mist eliminator
- dust collection
- alkali
- collection column
- 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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- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 50
- 239000003513 alkali Substances 0.000 title claims abstract description 48
- 230000003009 desulfurizing Effects 0.000 title claims abstract description 46
- 239000000428 dust Substances 0.000 title claims abstract description 41
- 239000003595 mist Substances 0.000 claims abstract description 31
- 238000005507 spraying Methods 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims abstract description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000003546 flue gas Substances 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nODVweCcgaGVpZ2h0PSc4NXB4JyB2aWV3Qm94PScwIDAgODUgODUnPgo8IS0tIEVORCBPRiBIRUFERVIgLS0+CjxyZWN0IHN0eWxlPSdvcGFjaXR5OjEuMDtmaWxsOiNGRkZGRkY7c3Ryb2tlOm5vbmUnIHdpZHRoPSc4NS4wJyBoZWlnaHQ9Jzg1LjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMy4zJyB5PSc1My42JyBjbGFzcz0nYXRvbS0wJyBzdHlsZT0nZm9udC1zaXplOjIzcHg7Zm9udC1zdHlsZTpub3JtYWw7Zm9udC13ZWlnaHQ6bm9ybWFsO2ZpbGwtb3BhY2l0eToxO3N0cm9rZTpub25lO2ZvbnQtZmFtaWx5OnNhbnMtc2VyaWY7dGV4dC1hbmNob3I6c3RhcnQ7ZmlsbDojRTg0MjM1JyA+SDwvdGV4dD4KPHRleHQgeD0nMjguMicgeT0nNjIuOScgY2xhc3M9J2F0b20tMCcgc3R5bGU9J2ZvbnQtc2l6ZToxNXB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6I0U4NDIzNScgPjI8L3RleHQ+Cjx0ZXh0IHg9JzM1LjAnIHk9JzUzLjYnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjNweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
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- 238000011084 recovery Methods 0.000 claims description 23
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- 239000000706 filtrate Substances 0.000 claims description 7
- 239000003518 caustics Substances 0.000 claims description 5
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- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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[O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical group 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
Abstract
The utility model provides a kind of desulfurized dust collection column with silk screen and alkali kiln gas desulfurization dust-removal system, belongs to field of environment protection.This patent after steam-operating air inducing pull-over gear, increase desulfurized dust collection column before chimney, desulfurized dust collection column includes：Tower body, lower central position is provided with center rotary island in tower body, above the rotary island of center, desulfurization spraying layer is disposed in tower body from bottom to top, baffle type mist eliminator, baffle plate type demisting rinses layer, mesh mist eliminator, silk screen demisting rinses layer, the external desulfuration recycle pump of desulfurization spraying layer, alkali kiln gas sprays through desulfurization spraying layer and carries out desulfurization, most of water droplet is removed through baffle type mist eliminator, not only contain moisture in water droplet, also dissolved with sulfur dioxide etc., the particle dust in flue gas can also be removed, again through mesh mist eliminator, by in flue gas sicker and tiny water droplet removal, reach dedusting purpose.After this patent, flue dust arranges concentration outside, sulfur dioxide realizes qualified discharge, energy-saving and emission-reduction, and social benefit is apparent.
Description
Technical field
The utility model is related to environmental technology field, specifically a kind of desulfurized dust collection column and alkali stove cigarette with silk screen
Desulfurization dust pelletizing system.
Background technology
Alkali recovery boiler is the important equipment of slurrying enterprise chemical recovery system, is that the concentrated black liquid after being concentrated with pulping waste liquor is
The special boiler of fuel.The purpose of burning is to recycle the heat of alkali and organic component in pulping waste liquor, thus alkali collection pot
Stove is again simultaneously paper industry environmental protection and energy saving important equipment.
In use, generated alkali kiln gas is single to rely on electrostatic precipitator dedusting, cigarette to existing alkali recovery boiler
The nitrous oxides concentration of gas is less than 100 mg/m3, can qualified discharge, but sulfur dioxide in flue gas and dirt are transported in boiler excess load
When row, qualified discharge requirement can not achieve.
Invention content
The technical assignment of the utility model is in view of the deficiencies of the prior art, to provide a kind of desulfurized dust collection column with silk screen
And alkali kiln gas desulfurization dust-removal system, to solve in alkali kiln gas existing in the prior art, sulfur dioxide and dirt cannot rows up to standard
The problem of putting.
Technical solution adopted by the utility model to solve its technical problems is：
1, the utility model provides a kind of desulfurized dust collection column with silk screen, including：Tower body, lower central position in tower body
Be provided with center rotary island, center rotary island is conducive to circulating for alkali kiln gas, above the rotary island of center, in tower body from bottom to top according to
Secondary desulfurization spraying layer, baffle type mist eliminator, the baffle plate type demisting of being provided with rinses layer, mesh mist eliminator, the flushing of silk screen demisting
Layer,
The external desulfuration recycle pump of desulfurization spraying layer, alkali kiln gas sprays through desulfurization spraying layer and carries out desulfurization, through baffling
Board-like demister removes most of water droplet, not only contains moisture in water droplet, also dissolved with sulfur dioxide etc., can also go to a certain degree
Except the particle dust in flue gas, then through mesh mist eliminator, by flue gas sicker and tiny water droplet remove, reach dedusting mesh
's.
As the utility model it is further preferred that the desulfurization spraying layer is level Four, baffle type mist eliminator is two-stage,
Mesh mist eliminator is two-stage.
2, the utility model separately provides a kind of alkali kiln gas desulfurization dust-removal system, including：Zheng Fa Nong liquid bath, Ru Lu liquid
Cao, liquid heater, alkali recovery boiler, dissolving tank, filtrate filter, send caustic room, electrostatic precipitator, steam-operating air inducing dragging
Machine, above-mentioned desulfurized dust collection column, chimney, sode ash dissolving tank, primary air fan, two wind turbine, air preheater three times；
Zheng Fa Nong liquid bath, Ru Lu liquid bath, liquid heater, alkali recovery boiler, dissolving tank, filtrate filter, send it is severe
Chemical industry section is sequentially connected by pipeline；
Alkali recovery boiler, electrostatic precipitator, steam-operating air inducing pull-over gear, desulfurized dust collection column, chimney are sequentially connected by flue,
Form flue gas dust collecting system；
Primary air fan, two are connected after wind turbine is connected with air preheater three times, then by process pipelines with alkali recovery boiler,
Form the air feed system of alkali recovery boiler.
As the utility model it is further preferred that by alkali recovery boiler two three times air feed system air door channel increase,
So that black liquor fully burns, the generation of sulfur dioxide and flying dust is reduced from source.
As the utility model it is further preferred that one or two electrical field control systems of electrostatic precipitator are changed by industrial frequency control
It is controlled for high frequency, increases the efficiency of dust collection of electrostatic precipitator.
As the utility model it is further preferred that transformation steam-operating air inducing pull-over gear, its air door channel is increased, raising is drawn
Air quantity and wind pressure.
A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen of the utility model, with the prior art
It is compared to generated advantageous effect：
1, after steam-operating air inducing pull-over gear, increase desulfurized dust collection column, the external desulfuration recycle pump of desulfurization spraying layer, alkali before chimney
Kiln gas sprays through desulfurization spraying layer and carries out desulfurization, removes most of water droplet through baffle type mist eliminator, not only contains in water droplet
Moisture can also remove the particle dust in flue gas, then through mesh mist eliminator, by cigarette to a certain degree also dissolved with sulfur dioxide etc.
Sicker in gas and the removal of tiny water droplet, reach dedusting purpose.
2, it is directed to alkali kiln gas desulfurization dust-removal system,
First, optimization alkali recovery boiler two air feed system three times, the air door of the air feed system three times of alkali recovery boiler two is led to
Road increases so that black liquor fully burns, and the generation of sulfur dioxide and flying dust is reduced from source；
Second, one or two electrical field control systems of electrostatic precipitator are changed to high frequency control by industrial frequency control, increase electrostatic and remove
The efficiency of dust collection of dirt device；
Third, transformation steam-operating air inducing pull-over gear, its air door channel is increased, absorbing quantity and wind pressure are improved.
Fourth, after alkali kiln gas first passes through electrostatic precipitator dedusting, then by desulfurized dust collection column advanced treating, realize de-
It is sulphur, dust removal integrated, equipment investment is reduced, the flue gas after flue gas is up to standard passes through high-altitude after CEMS system detectio qualifications into chimney
Discharge.
The dirt discharge standard 20mg/Nm that concentration reaches the requirement of environmental protection administration of cities and counties is arranged after the utility model, outside flue dust
3, emission standards for sulfur dioxide 200mg/Nm3,39.81 tons of year emission reduction dirt or more, year 65.28 tons of reducing emission of sulfur dioxide or more, society
Meeting benefit is apparent.
Description of the drawings
Attached drawing 1 is the structure chart of the utility model alkali kiln gas desulfurization dust-removal system；
Attached drawing 2 is the structure chart of desulfurized dust collection column of the utility model with silk screen.
In figure, 1, Zheng Fa Nong liquid bath, 2, Ru Lu liquid bath, 3, liquid heater, 4, alkali recovery boiler, 5, dissolving tank,
6, filtrate filter, 7, send caustic room, 8, electrostatic precipitator, 9, steam-operating air inducing pull-over gear, 10, desulfurized dust collection column, 11, cigarette
Chimney, 12, sode ash dissolving tank, 13, primary air fan, 14, two wind turbines three times, 15, air preheater,
16, tower body, 17, center rotary island, 18, desulfurization spraying layer, the 1800, first desulfurization spraying layer, the 1801, second desulfurization spray
Drenching layer, 1802, third desulfurization spraying layer, the 1803, the 4th desulfurization spraying layer,
19, baffle type mist eliminator, the 1900, first baffle type mist eliminator, the 1901, second baffle type mist eliminator,
20, mesh mist eliminator, the 2000, first mesh mist eliminator, the 2001, second mesh mist eliminator,
21, baffle plate type demisting rinse layer, 22, silk screen demisting rinse layer.
Specific implementation mode
1-2 below in conjunction with the accompanying drawings, to a kind of desulfurized dust collection column and alkali kiln gas desulfurization with silk screen of the utility model
Dust pelletizing system is described in detail below.
Embodiment one
As shown in Fig. 1, the utility model separately provides a kind of alkali kiln gas desulfurization dust-removal system, including：Zheng Fa Nong liquid
Slot 1, Ru Lu 2, of liquid bath liquid heater 3, alkali recovery boiler 4, dissolving tank 4, filtrate filter 6, send caustic room 7, electrostatic
Deduster 8, steam-operating air inducing pull-over gear 9, desulfurized dust collection column 10, chimney 11, sode ash dissolving tank 12, primary air fan 13, two tertiary airs
Machine 14, air preheater 15；
Zheng Fa Nong liquid bath 1, Ru Lu 2, of liquid bath liquid heater 3, alkali recovery boiler 4, dissolving tank 4, filtrate filter
6, caustic room 7 is sent to be sequentially connected by pipeline；
Alkali recovery boiler 4, electrostatic precipitator 8, steam-operating air inducing pull-over gear, desulfurized dust collection column 10, chimney 11 by flue according to
It is secondary to be connected, form flue gas dust collecting system；
Primary air fan 13, two is after wind turbine 14 is connected with air preheater 15 three times, then passes through process pipelines and alkali collection pot
Stove 4 is connected, and forms the air feed system of alkali recovery boiler 4.
On the basis of the said structure, by alkali recovery boiler 4 two three times air feed system air door channel increase so that black liquor fills
Divided combustion reduces the generation of sulfur dioxide and flying dust from source.
On the basis of the said structure, one or two electrical field control systems of electrostatic precipitator 8 are changed to high frequency control by industrial frequency control
System increases the efficiency of dust collection of electrostatic precipitator 8.
On the basis of the said structure, transformation steam-operating air inducing pull-over gear 9, its air door channel is increased, and improves absorbing quantity and wind
Pressure.
The course of work of the present embodiment is described as follows：
The flue gas that alkali recovery boiler 4 generates, first passes through 8 dedusting of electrostatic precipitator, steam-operating air inducing pull-over gear 9 again send flue gas
To carrying out desulfurization and dedusting advanced treating in the desulfurizing tower 10 with silk screen, it is up to standard after flue gas into chimney 11, through CEMS system detectios
High air discharge after qualification.
Embodiment two
As shown in Fig. 2, the desulfurized dust collection column 10 of embodiment one is a kind of desulfurized dust collection column 10 with silk screen, including：
Tower body 16, lower central position is provided with center rotary island 17 in tower body 16, and center rotary island 17 is conducive to the recycle stream of alkali kiln gas
It is dynamic, it is disposed with desulfurization spraying layer 18, baffle type mist eliminator 19, folding from bottom to top in 17 top of center rotary island, tower body 16
Flowing plate formula demisting rinses layer, mesh mist eliminator 20, silk screen demisting and rinses layer 21,
18 external desulfuration recycle pump of the desulfurization spraying layer, alkali kiln gas is sprayed through desulfurization spraying layer 18 carries out desulfurization, warp
Baffle type mist eliminator 19 removes most of water droplet, and moisture is not only contained in water droplet, can also be certain also dissolved with sulfur dioxide etc.
Degree removes the particle dust in flue gas, then through mesh mist eliminator 20, by flue gas sicker and tiny water droplet remove, reach
To dedusting purpose.
In Fig. 2, desulfurization spraying layer 18 is level Four, respectively：First desulfurization spraying layer 1800, the second desulfurization spraying layer
1801, third desulfurization spraying layer 1802, the 4th desulfurization spraying layer 1803.
Baffle type mist eliminator 19 is two-stage, respectively：First baffle type mist eliminator 1900, the second baffle plate type demisting
Device 1901.
Mesh mist eliminator 20 is two-stage, respectively：First mesh mist eliminator 2000, the second mesh mist eliminator 2001.
A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen of the utility model, processing and fabricating
It is simple and convenient, processing and fabricating shown in by specification attached drawing.
It is the known technology of those skilled in the art in addition to the technical characteristic described in specification.
Claims (3)
1. a kind of desulfurized dust collection column with silk screen, which is characterized in that including：Tower body, lower central position is provided in tower body
Center rotary island is disposed with desulfurization spraying layer, baffle type mist eliminator, baffling from bottom to top above the rotary island of center, in tower body
Board-like demisting rinses layer, mesh mist eliminator, silk screen demisting and rinses layer,
The external desulfuration recycle pump of desulfurization spraying layer, alkali kiln gas sprays through desulfurization spraying layer and carries out desulfurization, through baffle plate type
Demister removes most of water droplet, then through mesh mist eliminator, by flue gas sicker and tiny water droplet remove.
2. a kind of desulfurized dust collection column with silk screen according to claim 1, which is characterized in that the desulfurization spraying layer is
Level Four, baffle type mist eliminator are two-stage, and mesh mist eliminator is two-stage.
3. a kind of alkali kiln gas desulfurization dust-removal system, which is characterized in that including：Zheng Fa Nong liquid bath, Ru Lu liquid bath, liquid add
Hot device, dissolving tank, filtrate filter, send caustic room, electrostatic precipitator, steam-operating air inducing pull-over gear, such as right at alkali recovery boiler
It is required that desulfurized dust collection column, chimney, sode ash dissolving tank, primary air fan described in 1 or 2, two wind turbine, air preheater three times；
Zheng Fa Nong liquid bath, Ru Lu liquid bath, liquid heater, alkali recovery boiler, dissolving tank, filtrate filter, send causticization work
Section is sequentially connected by pipeline；
Alkali recovery boiler, electrostatic precipitator, steam-operating air inducing pull-over gear, desulfurized dust collection column, chimney are sequentially connected by flue, are formed
Flue gas dust collecting system；
Primary air fan, two are connected after wind turbine is connected with air preheater three times, then by process pipelines with alkali recovery boiler, are formed
The air feed system of alkali recovery boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820001211.0U CN207822768U (en) | 2018-01-02 | 2018-01-02 | A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820001211.0U CN207822768U (en) | 2018-01-02 | 2018-01-02 | A kind of desulfurized dust collection column and alkali kiln gas desulfurization dust-removal system with silk screen |
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| CN207822768U true CN207822768U (en) | 2018-09-07 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109821380A (en) * | 2018-12-26 | 2019-05-31 | 广西粤桂广业控股股份有限公司 | A kind of alkali recovery boiler circulation of tail gas processing method and equipment |
| CN110975525A (en) * | 2019-11-06 | 2020-04-10 | 福建省青山纸业股份有限公司 | Production method for effectively reducing emission of dust and sulfur dioxide in flue gas of alkali recovery furnace |
-
2018
- 2018-01-02 CN CN201820001211.0U patent/CN207822768U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109821380A (en) * | 2018-12-26 | 2019-05-31 | 广西粤桂广业控股股份有限公司 | A kind of alkali recovery boiler circulation of tail gas processing method and equipment |
| CN110975525A (en) * | 2019-11-06 | 2020-04-10 | 福建省青山纸业股份有限公司 | Production method for effectively reducing emission of dust and sulfur dioxide in flue gas of alkali recovery furnace |
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