CN207856650U - A kind of spray scattering tower - Google Patents

A kind of spray scattering tower Download PDF

Info

Publication number
CN207856650U
CN207856650U CN201820005614.2U CN201820005614U CN207856650U CN 207856650 U CN207856650 U CN 207856650U CN 201820005614 U CN201820005614 U CN 201820005614U CN 207856650 U CN207856650 U CN 207856650U
Authority
CN
China
Prior art keywords
storehouse
tower
tower body
liquid pool
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.)
Active
Application number
CN201820005614.2U
Other languages
Chinese (zh)
Inventor
董新良
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ding Tai Energy-Conserving And Environment-Protective Science And Technology Ltd Of Shaoxin City
Original Assignee
Ding Tai Energy-Conserving And Environment-Protective Science And Technology Ltd Of Shaoxin City
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ding Tai Energy-Conserving And Environment-Protective Science And Technology Ltd Of Shaoxin City filed Critical Ding Tai Energy-Conserving And Environment-Protective Science And Technology Ltd Of Shaoxin City
Priority to CN201820005614.2U priority Critical patent/CN207856650U/en
Application granted granted Critical
Publication of CN207856650U publication Critical patent/CN207856650U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses the chimney at the top of a kind of spray scattering tower, including tower body, tower body, the tower body includes upper storehouse, Zhong Cang and lower storehouse, and upper storehouse includes from top to bottom flue outlet, demister and particulate matter blocking apparatus;Middle storehouse is the stage casing inner cylinder being arranged along tower body inner wall, and middle storehouse is equipped with flue entrance on tower body wall surface, and spray equipment is equipped in middle storehouse, diffuser is connected below middle storehouse, and diffuser extends in lower storehouse, is the uptake flue of connection upper storehouse and lower storehouse in the middle part of middle storehouse;Lower orlop portion is to absorb liquid pool, absorbs interior be equipped with of liquid pool and connects oxidation fan oxygen-supplying tube;The low dedusting of compact-sized, reasonable design, operating cost and deep desulfuration and the spray of denitration scatter tower.

Description

A kind of spray scattering tower
Technical field
The utility model is related to field of environment protection equipment, specially a kind of spray scatters tower.
Background technology
With the fast development of China's economy, the NOx of bituminous coal fired boiler discharge and SO2 pages of also constantly growth, by coal burning 85%, the NOx that the SO2 discharged accounts for total amount accounts for the 60% of total release, and the acid rain caused by the two accounts for the 82% of total acid rainfall, It is pointed out according to related research, the about several hundred million members of economic loss caused by NOx and SO2 that China is discharged every year.
By our understandings to flue gas, waste gas purification apparatus, each list such as dedusting, denitration, desulfurization in flue gas, exhaust gas The more complete equipments of basic need in only purification system, such as:Conversion equipment, redox arrangement, filtering adsorpting device etc. are absorbed, In each individual smoke eliminator, often there is a phenomenon where the cross reactions between each pollutant, cause secondary dirt Dye.
Utility model content
The purpose of this utility model is to provide for a kind of spray scattering tower, and compact-sized, reasonable design, operating cost are low Dedusting and deep desulfuration and the spray of denitration scatter tower.
In order to achieve the above-mentioned object of the invention, the utility model uses following technical scheme:A kind of spray scattering tower, including Chimney at the top of tower body, tower body, the tower body include upper storehouse, Zhong Cang and lower storehouse, and upper storehouse includes from top to bottom flue outlet, demisting Device and particulate matter blocking apparatus;Middle storehouse is the stage casing inner cylinder being arranged along tower body inner wall, and middle storehouse is equipped with flue on tower body wall surface Entrance is equipped with spray equipment in middle storehouse, diffuser is connected below middle storehouse, and diffuser extends in lower storehouse, is connection in the middle part of middle storehouse The uptake flue of upper storehouse and lower storehouse;Lower orlop portion is to absorb liquid pool, absorbs interior be equipped with of liquid pool and connects oxidation fan oxygen-supplying tube.
Preferably, being connected with multiple diffusers below the middle storehouse, the diffuser extends to the middle level for absorbing liquid pool Or lower layer position;Increase the circulation passage of flue gas cool-down by multiple diffusers, improve the efficiency of gas cleaning processing, and dissipates Tracheae, which extends to the middle level for absorbing liquid pool or lower layer position, can ensure that trapping absorption of the flue gas in absorbing liquid pool is more increased Effect, gas-liquid contact is more abundant, and mass transferring in gas phase effect is more preferable.
Preferably, the particulate matter blocking apparatus is aerosol and ease ammonia blocking apparatus;Can trap salt fog and PM2.5 pollutants below.
Preferably, connecing oxidation fan oxygen-supplying tube at least provided with two sections in the absorption liquid pool, and connect oxidation fan Oxygen-supplying tube is equipped with several bubble oxygen mouths;The amount of oxygen of oxygen-supplying tube discharge is equal to or more than the influx of flue gas, ensures logical The oxygen of oxygen pipe discharge aoxidizes the The sub-salt in flue gas enough, prevents the not oxidised loss of flue gas, in order to increase the oxidation effect of flue gas Rate.
Preferably, being equipped with overflow port at the absorption liquid pool upper liquid position;The liquid for absorbing liquid pool can be monitored and controlled Face height, limitation liquid level are more than to prevent liquid from releasing.
Compared with prior art, a kind of spray scattering tower for using above-mentioned technical proposal, has the advantages that:
One, by cleaning dust, water bath dust-removing, foam dust-removing, water film filtering dedusting, flue gas can finely be removed The effect of dirt, deep desulfuration and denitration.
Two, the technical process such as trapping, absorption, oxidation, dissolving can be merged into an individual gas, liquid, solid phase reaction In device.
In order to realize low operating cost, the absorbent quality requirements absorbed in liquid pool are relatively low, and amino, calcium base, magnesium can be used Base, sodium base, various alkaline waste liquors etc. can be replaced at any time in spray scatters tower operational process.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram of spray scattering tower embodiment of the utility model;
Fig. 2 is the structural schematic diagram inside tower body in the present embodiment;
Fig. 3 is the structural schematic diagram of stage casing inner cylinder in the present embodiment.
Reference numeral:1, tower body;2, chimney;3, flue outlet;4, demister;5, particulate matter blocking apparatus;6, in stage casing Cylinder;60, uptake flue;7, flue entrance;8, spray equipment;9, diffuser;10, liquid pool is absorbed;11, it connects oxidation fan and leads to oxygen Pipe;12, overflow port.
Specific implementation mode
The utility model is described further below in conjunction with the accompanying drawings.
A kind of spray as shown in Figures 1 to 3 scatters tower, including tower body 1, chimney 2, flue outlet 3, demister 4, particulate matter Blocking apparatus 5, the stage casing inner cylinder 6 along the setting of 1 inner wall of tower body, the flue entrance 7 on 1 wall surface of tower body, the spray equipment in middle storehouse 8, the diffuser 9 under middle storehouse, the uptake flue 60 of connection upper storehouse and lower storehouse, the absorption liquid pool 10 in lower orlop portion, absorption liquid pool 10 The interior overflow port 12 connect on oxidation fan oxygen-supplying tube 11 and absorption liquid pool 10 at liquid level.
As shown in Fig. 2, in needing the flue gas purified to enter first by flue entrance 7 in storehouse, and sprayed by spray equipment 8 The spray liquid spilt increases humidity to flue gas, flue-gas temperature is dropped to chemical reaction required temperature, while flue gas uniformly being distributed Into multiple diffusers 9, the preliminary trapping to the fine grained pollutant in flue gas and preliminary desulfurization and denitration to flue gas are completed, Diffuser 9 is mounted below middle storehouse and is connected to lower storehouse, and is inserted into the absorption liquid pool 10 in lower storehouse, and therefrom storehouse passes through air-dispersing to flue gas Pipe 9 enters directly into the absorbing liquid in lower storehouse, and is gushed to floating by absorbing liquid in the form of tiny bubble, and absorbing liquid is to flue gas In SO2 and NOx carry out mass transferring in gas phase, while absorbing the oxidation fan oxygen-supplying tube 11 that connects in liquid pool 10 can be by the Asia in flue gas Salt etc. is oxidized into normal salt, flue gas is floating gush during complete deep purifying to flue gas, i.e.,:Fine dedusting to flue gas It falls off with depth and denitration, flue gas enters upper storehouse by uptake flue 60 again, removed through particulate matter blocking apparatus 5 and demister 4 After the moisture carried secretly in salt fog, PM2.5 atmosphere pollution below and flue gas, clean flue gas is by 7 qualified discharge of flue outlet Into air.
Multiple diffusers 9 are connected below middle storehouse, flue gas enters absorption liquid pool in a manner of multi-passage circulating along diffuser 9 In 10, flue gas influx increases, and explosive flue gas can be handled with fast purification, and diffuser 9 is extended to and absorbed in liquid pool 10 Layer or lower layer position, the time of flue gas residence in a liquid is longer when flue gas is gushed to liquid level is floating, and the contact of gas-liquid is more abundant, So that smoke gas fine dedusting and depth is fallen off and reaches best with denitration.
Particulate matter blocking apparatus 5 is that aerosol and ease ammonia blocking apparatus, such as PM2.5 that can be handled in flue gas are below Atmosphere pollution, it is more preferable to the purified treatment effect of particulate matter in flue gas.
Oxidation fan oxygen-supplying tube 11 is connect at least provided with two sections absorbing in liquid pool 10, is to ensure the oxygen of oxygen-supplying tube discharge Change gas and be more than or equal to exhaust gas volumn, keeps the reaction of oxidizing gas and flue gas sufficient, avoid oxidizing gas content deficiency flue gas It cannot be purified completely, occur omitting flue gas.
Overflow port 12 is equipped at liquid level on absorbing liquid pool 10, the liquid level for absorbing liquid pool 10 can be monitored and controlled, Limitation liquid level is more than to prevent liquid from releasing.
The above makes preferred embodiments of the present invention, does not depart from for those of ordinary skill in the art Under the premise of the utility model principle, several variations and modifications can also be made, these also should be regarded as the protection of the utility model Range.

Claims (5)

1. the chimney (2) at the top of a kind of spray scattering tower, including tower body (1), tower body (1), it is characterised in that:The tower body includes Upper storehouse, Zhong Cang and lower storehouse, upper storehouse include from top to bottom flue outlet (3), demister (4) and particulate matter blocking apparatus (5);Middle storehouse For the stage casing inner cylinder (6) being arranged along tower body (1) inner wall, middle storehouse is equipped with flue entrance (7) on tower body (1) wall surface, in middle storehouse Equipped with spray equipment (8), connection diffuser (9), diffuser (9) extend in lower storehouse below middle storehouse, in connection in the middle part of middle storehouse The uptake flue (60) in storehouse and lower storehouse;Lower orlop portion is to absorb liquid pool (10), is absorbed logical equipped with oxidation fan is connect in liquid pool (10) Oxygen pipe (11).
2. a kind of spray according to claim 1 scatters tower, it is characterised in that:It is connected with multiple air-dispersings below the middle storehouse It manages (9), the diffuser (9) extends to the middle level for absorbing liquid pool (10) or lower layer position.
3. a kind of spray according to claim 1 scatters tower, it is characterised in that:The particulate matter blocking apparatus (5) is Aerosol and ease ammonia blocking apparatus.
4. a kind of spray according to claim 1 scatters tower, it is characterised in that:It is at least set in the absorption liquid pool (10) There are two sections to connect oxidation fan oxygen-supplying tube (11), and connects oxidation fan oxygen-supplying tube (11) and be equipped with several bubble oxygen mouths.
5. a kind of spray according to claim 1 scatters tower, it is characterised in that:On the absorption liquid pool (10) at liquid level Equipped with overflow port (12).
CN201820005614.2U 2018-01-03 2018-01-03 A kind of spray scattering tower Active CN207856650U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820005614.2U CN207856650U (en) 2018-01-03 2018-01-03 A kind of spray scattering tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820005614.2U CN207856650U (en) 2018-01-03 2018-01-03 A kind of spray scattering tower

Publications (1)

Publication Number Publication Date
CN207856650U true CN207856650U (en) 2018-09-14

Family

ID=63464494

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820005614.2U Active CN207856650U (en) 2018-01-03 2018-01-03 A kind of spray scattering tower

Country Status (1)

Country Link
CN (1) CN207856650U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112023569A (en) * 2020-08-26 2020-12-04 哈尔滨理工大学 Novel welding flue gas purification device
CN114849465A (en) * 2022-04-15 2022-08-05 佛山市蓝宇环保科技有限公司 Energy-recovery type energy-saving environment-friendly waste gas treatment spray tower

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112023569A (en) * 2020-08-26 2020-12-04 哈尔滨理工大学 Novel welding flue gas purification device
CN114849465A (en) * 2022-04-15 2022-08-05 佛山市蓝宇环保科技有限公司 Energy-recovery type energy-saving environment-friendly waste gas treatment spray tower
CN114849465B (en) * 2022-04-15 2023-09-08 佛山市蓝宇环保科技有限公司 Energy recovery type energy-saving environment-friendly waste gas treatment spray tower

Similar Documents

Publication Publication Date Title
CN206500008U (en) A kind of umbrella waterfall type sprays flue gas cleaner
CN102049167B (en) High-SO2 concentration pressure smoke desulfuration method and device
CN207856650U (en) A kind of spray scattering tower
CN105642104A (en) Deep purification method and device of flue gas after wet-process desulfurization
CN105056678B (en) The dust removal integrated flue gas cleaner of desulphurization denitration, demercuration
CN102580509A (en) Two-level absorption desulfuration denitration demercuration particulate matter 2.5 (PM2.5) removal washing tower
CN101530738B (en) Flue gas desulphurization device by circulating ash humidifying and semi-drying method provided with hot air fluidized air machine
CN203494388U (en) Flue gas desulfurization and dedusting device of coal-fired boiler
CN109289475A (en) A kind of high effective flue gas fair current dust-removal and desulfurizing disappears white processing method and its device
CN201445885U (en) Desulfuration and dedusting device
JPH08108042A (en) Desulfurization and denitrification of flue gas,method and device for removal of carbon dioxide and catalyst and absorbent used therein
CN208711402U (en) A kind of high-efficiency multi-stage spraying foam dust-removing desulfurating apparatus
CN209138324U (en) A kind of high effective flue gas fair current dust-removal and desulfurizing disappears white device
CN201088905Y (en) Dedusting desulfurization unit
CN112675698B (en) Desulfurization, denitrification and dust removal device of turbulent bed in separate bin and process thereof
CN207822781U (en) Double loop smoke eliminator
JPH0788325A (en) Treatment of waste gas and device therefor
CN107441907A (en) A kind of material boiler smoke multi-pollutant handling process and equipment
CN208074996U (en) A kind of exhaust gas purification system of dangerous waste incineration
CN106064016A (en) The ultra-clean dust removal integrated plant of exhuast gas desulfurization denitration
CN110237681A (en) The coal-fired flue-gas of collaboration deep purifying takes off white system
CN101301572B (en) Dry-wet mixed type dust-removing and desulfurizing integrated device
CN105056683B (en) A kind of flue-gas dust-removing and desulfurization denitrification integral system and method
CN205288076U (en) Flue gas deep purification device behind wet flue gas desulfurization
CN205055798U (en) Modular wet -type flue gas desulfurization dust collector

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant