CN106731599A - A kind of flue spray dust remover - Google Patents
A kind of flue spray dust remover Download PDFInfo
- Publication number
- CN106731599A CN106731599A CN201611151929.XA CN201611151929A CN106731599A CN 106731599 A CN106731599 A CN 106731599A CN 201611151929 A CN201611151929 A CN 201611151929A CN 106731599 A CN106731599 A CN 106731599A
- Authority
- CN
- China
- Prior art keywords
- level
- alkali lye
- flue
- aerosolater
- spray
- 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.)
- Pending
Links
- 239000007921 spray Substances 0.000 title claims abstract description 36
- 239000000428 dust Substances 0.000 title claims abstract description 34
- 239000003513 alkali Substances 0.000 claims abstract description 43
- 230000001629 suppression Effects 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 230000003009 desulfurizing effect Effects 0.000 claims description 12
- 238000000889 atomisation Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 18
- 239000003546 flue gas Substances 0.000 abstract description 18
- 230000000694 effects Effects 0.000 abstract description 4
- 239000007789 gas Substances 0.000 abstract description 4
- 238000005457 optimization Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 5
- 239000002253 acid Substances 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/08—Means for controlling the separation process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention provides a kind of flue spray dust remover, increase deduster previous stage spray for dust suppression equipment, by lye tank for one-level spray for dust suppression provides alkali lye, multiple spray heads are provided with inside one-level aerosolater, using the operation principle of spray dust, a large amount of dusts in raw flue gas are collected, the purpose of dust content in flue gas is reduced so as to reach, flue-gas temperature can be simultaneously reduced in addition, so as to reduce exhaust gas volumn after demister, the load of deduster and air-introduced machine can be reduced, reach optimization deduster dust removing effects and reduce the purpose of station-service electric load, it is significant to energy-conserving and environment-protective.
Description
Technical field
The invention belongs to smoke treated field, and in particular to a kind of flue spray dust remover.
Background technology
With industrial expansion, energy input gradually rises, and the discharge capacity of atmosphere pollution increases.Air quality is environment matter
How one important indicator of amount, remove the important goal that the dust floated in air is environmental improvement.The flue gas of boiler discharge
In contain substantial amounts of dirt, traditional dust collection method carries out dedusting for high-temperature flue gas are directly entered deduster, although high temperature fume dust removal
Method also have many, including bag-type dusting, electrostatic precipitation and method etc. electric precipitation.But these methods are due to deduster dedusting
Limited in one's ability, the flue gas ash removal effect after dedusting is unsatisfactory, and dust collection method is complicated, cleaner high cost.
The content of the invention
The present invention provides a kind of flue spray dust remover to solve Problems Existing, increases the spraying of deduster previous stage and removes
Dirt equipment, by lye tank for one-level spray for dust suppression provides alkali lye, is provided with multiple spray heads inside one-level aerosolater, utilize
The operation principle of spray dust, a large amount of dusts in raw flue gas are collected, and the purpose of dust content in flue gas is reduced so as to reach,
Flue-gas temperature can be simultaneously reduced in addition, so as to reduce exhaust gas volumn after demister, can reduce the load of deduster and air-introduced machine, reach
The purpose of optimization deduster dust removing effects and reduction station-service electric load is significant to energy-conserving and environment-protective.
What the present invention was achieved through the following technical solutions:
A kind of flue spray dust remover, including:It is boiler, lye tank, one-level aerosolater, deduster, air-introduced machine, de-
Sulphur tower and chimney, wherein:The boiler connects one-level aerosolater by flue, and one-level aerosolater top is provided with point
With main pipe, the multiple atomizers of distribution main pipe connection, the atomizer connects spray head, the one-level aerosolater
Bottom is provided with delivery port, and the one-level aerosolater connects deduster by flue, and the deduster connects air-introduced machine, described to draw
Blower fan connects desulfurizing tower, and the desulfurizing tower connects chimney, MOD, the lye tank are provided between the desulfurizing tower and chimney
Alkali lye water inlet pipe is connected by alkali lye outlet pipe I, the alkali lye water inlet pipe connects the distribution main pipe of one-level aerosolater,
Parallel connection is provided with alkali lye outlet pipe II and alkali lye outlet pipe III on the alkali lye outlet pipe I.
Multiple spray head erects in the one-level aerosolater are arranged in parallel.
Thermometer is installed at the outlet flue of the one-level aerosolater, the flue gas after temperature control spray for dust suppression
Temperature is more than 130 DEG C, it is ensured that the temperature that flue gas enters deduster below is higher than acid dew point.
On the alkali lye water inlet pipe control valve group II and control valve group I, institute are sequentially provided with along alkali lye flow direction
State control valve group I and be parallel with control valve.
Check-valves and force (forcing) pump are equipped with the alkali lye outlet pipe II and alkali lye outlet pipe III, the check-valves is along alkali lye
Flow direction is arranged on before force (forcing) pump.
Alkali lye is operationally delivered to one-level aerosolater water inlet and enters one by the present invention by the adjusted valve of force (forcing) pump
Level aerosolater, high pressure alkali lye sprays through the atomization that one-level aerosolater distribution main pipe is distributed to one-level aerosolater
Mouth, the water mists of atomization enter flue and are mixed with heat smoke by spray head ejection, to flue gas cool-down, while with the dirt in flue gas
Grain is the nuclei of condensation, condenses into the thin dirt in big water droplet aggregation flue gas, ultimately forms the sludge pellet of bulky grain, and the flue dust of bulky grain is with cigarette
The deduster that gas enters below carries out dedusting collection, and the smog after final dedusting is discharged by chimney.
Beneficial effects of the present invention are:
(1) it is of the invention in original deduster previous stage aerosolater, by lye tank for one-level spray for dust suppression is provided
Alkali lye, is provided with multiple spray heads inside one-level aerosolater, using the operation principle of spray dust, will be big in raw flue gas
Amount dust is collected, and the purpose of dust content in flue gas is reduced so as to reach.
(2) because the spray of alkali lye reduces the temperature of flue gas, so as to reduce exhaust gas volumn after demister, deduster can be reduced
And the load of air-introduced machine, reach optimization deduster dust removing effects and reduce the purpose of station-service electric load, to energy-conserving and environment-protective meaning weight
Greatly.
Brief description of the drawings
Fig. 1 is structural representation of the invention;
Fig. 2 is the schematic diagram of one-level aerosolater;
Fig. 3 is the sectional view of one-level aerosolater A-A;
Wherein:1 is chimney;2 is MOD;3 is desulfurizing tower;4 is air-introduced machine;5 is deduster;6 is that one-level spraying is removed
Dirt device;7 is alkali lye water inlet pipe;8 is industrial outlet pipe;9 is boiler;10 is control valve group I;11 is control valve;12 is tune
Section valve group II;13 is check-valves;14 is alkali lye outlet pipe I;15 is force (forcing) pump;16 is lye tank;17 is alkali lye outlet pipe II;
18 is alkali lye outlet pipe III;19 is distribution main pipe;20 is atomizer;21 is spray head;22 is delivery port.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and detailed description.
Embodiment 1
A kind of flue spray dust remover, including:Boiler 9, lye tank 16, one-level aerosolater 6, deduster 5, air inducing
Machine 4, desulfurizing tower 3 and chimney 1, wherein:The boiler 9 is by flue connection one-level aerosolater 6, the one-level aerosolater
6 tops are provided with distribution main pipe 19, and the distribution main pipe 19 connects multiple atomizers 20, the connection spray head of the atomizer 20
21, the bottom of one-level aerosolater 6 is provided with delivery port 22, and the one-level aerosolater 6 connects deduster 5 by flue,
The deduster 5 connects air-introduced machine 4, the connection desulfurizing tower 3 of the air-introduced machine 4, the connection chimney 1 of the desulfurizing tower 3, the desulfurizing tower
MOD 2 is provided between 3 and chimney 1, the lye tank 16 connects alkali lye water inlet pipe 7 by alkali lye outlet pipe I 14, described
The distribution main pipe 19 of the connection one-level of alkali lye water inlet pipe 7 aerosolater 6, parallel connection is provided with alkali lye on the alkali lye outlet pipe I 14
Outlet pipe II 17 and alkali lye outlet pipe III 18.
Multiple spray heads 21 in the one-level aerosolater 6 are arranged in parallel vertically.
Thermometer is installed at the outlet flue of the one-level aerosolater 6, the cigarette after temperature control spray for dust suppression
Temperature degree is more than 130 DEG C, it is ensured that the temperature that flue gas enters deduster below is higher than acid dew point.
On the alkali lye water inlet pipe 7 control valve group II 12 and control valve group I are sequentially provided with along alkali lye flow direction
10, the control valve group I 10 is parallel with control valve 11.
Check-valves 13 and force (forcing) pump 15, the non-return are equipped with the alkali lye outlet pipe II 17 and alkali lye outlet pipe III 18
Valve 13 is arranged on before force (forcing) pump 15 along alkali lye flow direction.
The above is only not the limitation to technical scheme described in the invention for understanding that the present invention is used.One's own profession
The technical staff of industry can also make various changes or deformation on the basis of the technical scheme described in claim, all etc.
Same change or deformation should all be covered within claims of the invention.
Claims (6)
1. a kind of flue spray dust remover, including:Boiler (9), lye tank 16), one-level aerosolater (6), deduster
(5), air-introduced machine (4), desulfurizing tower (3) and chimney (1), it is characterised in that:The boiler (9) connects one-level spray for dust suppression by flue
Device (6), one-level aerosolater (6) top is provided with distribution main pipe (19), the multiple atomizations of distribution main pipe (19) connection
Nozzle (20), the atomizer (20) connects spray head (21), and one-level aerosolater (6) bottom is provided with delivery port
(22), the one-level aerosolater (6) connects deduster (5) by flue, and the deduster (5) connects air-introduced machine (4), described
Air-introduced machine (4) connects desulfurizing tower (3), and the desulfurizing tower (3) connects chimney (1), set between the desulfurizing tower (3) and chimney (1)
There is MOD (2), the lye tank (16) connects alkali lye water inlet pipe (7) by alkali lye outlet pipe I (14), and the alkali lye enters
The distribution main pipe (19) of water branch pipe (7) connection one-level aerosolater (6), parallel connection is provided with alkali on the alkali lye outlet pipe I (14)
Liquid outlet pipe II (17) and alkali lye outlet pipe III (18).
2. a kind of flue spray dust remover according to claim 1, it is characterised in that:The one-level aerosolater
(6) the multiple spray heads (21) in are arranged in parallel vertically.
3. a kind of flue spray dust remover according to claim 1, it is characterised in that:The one-level aerosolater
(6) thermometer is installed at outlet flue.
4. a kind of flue spray dust remover according to claim 1, it is characterised in that:The alkali lye water inlet pipe (7)
On be sequentially provided with control valve group II (12) and control valve group I (10), the control valve group I (10) along alkali lye flow direction
It is parallel with control valve (11).
5. a kind of flue spray dust remover according to claim 1, it is characterised in that:The alkali lye outlet pipe II (17)
With check-valves (13) and force (forcing) pump (15) are equipped with alkali lye outlet pipe III (18).
6. a kind of flue spray dust remover according to claim 5, it is characterised in that:Check-valves (13) flows along alkali lye
Direction is arranged on before force (forcing) pump (15).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611151929.XA CN106731599A (en) | 2016-12-14 | 2016-12-14 | A kind of flue spray dust remover |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611151929.XA CN106731599A (en) | 2016-12-14 | 2016-12-14 | A kind of flue spray dust remover |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106731599A true CN106731599A (en) | 2017-05-31 |
Family
ID=58888489
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611151929.XA Pending CN106731599A (en) | 2016-12-14 | 2016-12-14 | A kind of flue spray dust remover |
Country Status (1)
Country | Link |
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CN (1) | CN106731599A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110772958A (en) * | 2019-10-29 | 2020-02-11 | 黄山中科新佳生物科技有限公司 | Plant deodorant for treating odor of garbage collection station and preparation method and application thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201454409U (en) * | 2009-07-14 | 2010-05-12 | 中电投远达环保工程有限公司 | Flue gas mist cooling scrubbing system |
CN101732938A (en) * | 2008-11-26 | 2010-06-16 | 威海市正大环保设备有限公司 | Method and device for electric catching and dry-process purification of carbon baking flue gas |
CN104406184A (en) * | 2014-12-16 | 2015-03-11 | 威海鲁源科技环保设备有限公司 | Tail gas purification treatment device of cremation machine |
CN106076095A (en) * | 2016-08-02 | 2016-11-09 | 福建龙净环保股份有限公司 | Mercury in flue gas and the control method of sulfur trioxide and device is removed based on electrostatic fabric filter |
CN206463763U (en) * | 2016-12-14 | 2017-09-05 | 国源设计院有限公司 | A kind of flue spray dust remover |
-
2016
- 2016-12-14 CN CN201611151929.XA patent/CN106731599A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101732938A (en) * | 2008-11-26 | 2010-06-16 | 威海市正大环保设备有限公司 | Method and device for electric catching and dry-process purification of carbon baking flue gas |
CN201454409U (en) * | 2009-07-14 | 2010-05-12 | 中电投远达环保工程有限公司 | Flue gas mist cooling scrubbing system |
CN104406184A (en) * | 2014-12-16 | 2015-03-11 | 威海鲁源科技环保设备有限公司 | Tail gas purification treatment device of cremation machine |
CN106076095A (en) * | 2016-08-02 | 2016-11-09 | 福建龙净环保股份有限公司 | Mercury in flue gas and the control method of sulfur trioxide and device is removed based on electrostatic fabric filter |
CN206463763U (en) * | 2016-12-14 | 2017-09-05 | 国源设计院有限公司 | A kind of flue spray dust remover |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110772958A (en) * | 2019-10-29 | 2020-02-11 | 黄山中科新佳生物科技有限公司 | Plant deodorant for treating odor of garbage collection station and preparation method and application thereof |
CN110772958B (en) * | 2019-10-29 | 2021-12-07 | 黄山中科新佳生物科技有限公司 | Plant deodorant for treating odor of garbage collection station and preparation method and application thereof |
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PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
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WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170531 |
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