CN107537249A - A kind of soot processing device - Google Patents

A kind of soot processing device Download PDF

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Publication number
CN107537249A
CN107537249A CN201711052610.6A CN201711052610A CN107537249A CN 107537249 A CN107537249 A CN 107537249A CN 201711052610 A CN201711052610 A CN 201711052610A CN 107537249 A CN107537249 A CN 107537249A
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CN
China
Prior art keywords
process tank
dispersion plate
tank
processing device
air inlet
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Pending
Application number
CN201711052610.6A
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Chinese (zh)
Inventor
杨胜亿
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Individual
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Individual
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Priority to CN201711052610.6A priority Critical patent/CN107537249A/en
Publication of CN107537249A publication Critical patent/CN107537249A/en
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Abstract

The invention discloses a kind of soot processing device, it is made up of blower fan and the process tank installed in the air inlet side of blower fan, process tank is closed tank body, and processing pot sidewall is respectively equipped with air inlet pipe, gas outlet, water level controller, hydro-peening blast pipe, blowdown water valve, gas outlet is located at the top of the tank body of process tank, air inlet pipe is located at the tank base of process tank, and at least one dispersion plate is also equipped with inside process tank, and dispersion plate is located above air inlet pipe.Using the soot processing device of above technical scheme, gas is again washed the dust and other impurities in gas by treatment fluid, treatment fluid after fully refinement, at the same time it can also which some in gas are absorbed with gas frowzy.In addition, air pressure that both can be when process tank had added water or discharged water inside and outside Balance Treatment tank by hydro-peening blast pipe, while can also be connected with external water source, have the function that to clean dispersion plate.

Description

A kind of soot processing device
Technical field
The present invention relates to exhaust gas processing device, more particularly to a kind of soot processing device.
Background technology
As the enhancing of rapid development of economy and people to environmental consciousness, the dust removal requirement of those industrial coals are also continuous Improve, be faced with for the enterprise of some dusty gases discharge, cement plant, Metallurgical Factory, waste incineration industry etc. huge Challenge.
There are the diversified forms such as electric precipitation, cloth dedusting for current deduster, dust removal combined electricity with fabric device is by electric cleaner It is separately positioned on cloth deduster behind electric cleaner in sack cleaner, the connection between electric cleaner is connected using associated mode Or flue connection.The structure of such electric cloth deduster causes the circulation track of waste gas to become single, when electric cleaner needs to examine , it is necessary to which stopping whole dust removal combined electricity with fabric device completely could be overhauled when repairing or clearing up, such maintenance without it is solidifying have impact on it is whole Individual production, reduce the production efficiency of enterprise.
The content of the invention
It is an object of the invention to provide a kind of dust treatment dress.
According to an aspect of the invention, there is provided a kind of soot processing device, by blower fan and the air intake installed in blower fan The process tank of mouth side is formed, and process tank is closed tank body, and is handled pot sidewall and be respectively equipped with air inlet pipe, gas outlet, water level Controller, hydro-peening blast pipe, blowdown water valve, gas outlet are located at the top of the tank body of process tank, and air inlet pipe is located at the tank body of process tank Bottom, at least one dispersion plate is also equipped with inside process tank, dispersion plate is located at the entrance top of air inlet pipe, and dispersion plate has aperture For below 0.3mm dispersion hole, water level controller is located at below the dispersion plate of top layer, is equipped with and sprays below every layer of dispersion plate The hydro-peening head that blast pipe is connected is washed, blowdown water valve is positioned at the bottom of every layer of dispersion plate and draws outside process tank, the tank of process tank Another blowdown water valve is also drawn in body bottom simultaneously, and the air inlet of gas outlet and blower fan is built-in by pipeline communication, process tank There is treatment fluid, and filled it up with by water level controller and maintain water level, when blower fan is started working, the outside gas containing flue dust passes through Air inlet pipe enters inside process tank, then disperses gas by the dispersion hole of dispersion plate and be refined into tiny bubble, tiny Bubble flows in treatment fluid to gas outlet, is more conducive to fully contact with treatment fluid in flow process, in physics, chemical reaction In the presence of, the species precipitate of solid-state, condensed state and liquid is formed, suspends or swims in treatment fluid, it is net so as to obtain Change, purified gas enters blower fan by the air inlet of gas outlet and blower fan, and is discharged by the exhaust outlet of blower fan, hydro-peening blast pipe With double action, in process tank plus water or open as steam vent with the air pressure inside and outside Balance Treatment tank when discharging water;Spray simultaneously Washing blast pipe can also be connected with external water source, and current wash dispersion plate below by hydro-peening primary drying, so as to reach cleaning The effect of dispersion plate.
Using the soot processing device of above technical scheme, gas passes through treatment fluid, treatment fluid again after fully refinement Dust and other impurities in gas are washed, at the same time it can also which some in gas are absorbed with gas frowzy.Gas passes through Cross after the washing and absorption for the treatment of fluid, be substantially free of dust, and stink also disappears substantially.In process tank, flue dust can be with Fully contacted with treatment fluid, the effect of processing is more preferable.In addition, both can be when process tank have added water or discharged water by hydro-peening blast pipe Air pressure inside and outside Balance Treatment tank, while can also be connected with external water source, have the function that to clean dispersion plate.
In some embodiments, be provided with multiple dispersion plates inside process tank, multiple dispersion plates vertically successively between Every stacking, spacing distance is 200mm or so.It is possible thereby to further strengthen the scattered and thinning effect of gas.
In some embodiments, dispersion plate is made up of stainless steel microwell plate and sheet frame, and stainless steel microwell plate is arranged on plate The middle part of frame, stainless steel micropore panel aperture are below 0.3mm.
In some embodiments, water level controller is ball float liquid feed valve.
In some embodiments, dispersion plate edge has groove, and blowdown water valve is located at groove, is deposited on for discharging Waste liquid and slag mud above dispersion plate.
In some embodiments, the air inlet side of blower fan is provided with multiple process tanks, and multiple process tanks pass through pipeline phase Mutually series connection.
In some embodiments, the exhaust outlet side of blower fan is also provided with process tank, and process tank passes through pipe with exhaust outlet Road is connected.
In some embodiments, the treatment fluid inside process tank is water or the aqueous solution.
In some embodiments, the treatment fluid held in multiple process tanks is identical or different.
In some embodiments, the floating body of the greasy dirt for adsorption treatment liquid surface is additionally provided with above the dispersion plate of top layer Thing.It is possible thereby to remove the oily matter being difficult to by water or aqueous solution absorption.
Brief description of the drawings
Fig. 1 is the structural representation of the soot processing device of one embodiment of the present invention.
Fig. 2 is the structural representation of dispersion plate shown in Fig. 1.
Fig. 3 is the installation diagram of dispersion plate shown in Fig. 2.
Fig. 4 is the structural representation of the soot processing device of another embodiment of the present invention.
Embodiment
The invention will now be described in further detail with reference to the accompanying drawings.
Embodiment 1
Fig. 1 to Fig. 3 schematically shows a kind of soot processing device according to one embodiment of the present invention.Such as figure Shown, process tank 4 of the device by blower fan 2 and installed in the air inlet side of blower fan 2 is formed.
Wherein, blower fan 2 is connected with power supply 1.
Process tank 4 is closed tank body, and the side wall of process tank 4 be respectively equipped with air inlet pipe 5, gas outlet, water level controller 17, Hydro-peening blast pipe 12 and blowdown water valve 13.
Gas outlet is located at the top of the tank body of process tank 4, and air inlet pipe 5 is located at the tank base of process tank 5.
At least one dispersion plate 9 is also equipped with inside process tank 4.
Dispersion plate 9 is located at the entrance top of air inlet pipe 5.
Dispersion plate 9 has the dispersion hole that aperture is below 0.3mm.
Water level controller 17 is located at the lower section of dispersion plate 9 of top layer.
The lower section of every layer of dispersion plate 9 is equipped with the hydro-peening being connected with hydro-peening blast pipe 12 first 8.
Blowdown water valve 13 is positioned at the bottom of every layer of dispersion plate 9 and draws outside process tank 4.
The tank base of process tank 4 also draws another blowdown water valve 13 simultaneously.
Gas outlet is connected with the air inlet of blower fan 2 by pipeline 3.
Process tank 4 is filled it up with by water level controller 17 built with treatment fluid 7 and maintains water level.
In the present embodiment, the inside of process tank 4 is provided with multiple dispersion plates 9.
Vertically interval stacks multiple dispersion plates 9 successively, and spacing distance is 200mm or so.
The edge of dispersion plate 9 has groove 11, and blowdown water valve 13 is deposited on dispersion plate 9 at groove 11, for discharging The waste liquid and slag mud of side.
As shown in Figures 2 and 3, dispersion plate 9 is made up of stainless steel microwell plate 92 and sheet frame 91.
Stainless steel microwell plate 92 is arranged on the middle part of sheet frame 91, and the aperture of stainless steel microwell plate 92 is below 0.3mm.
In the present embodiment, water level controller 17 is ball float liquid feed valve.
Treatment fluid 7 inside process tank 4 is water or sodium hydrate aqueous solution.
In the present embodiment, the top of dispersion plate 9 of top layer is additionally provided with the floating body thing of the greasy dirt for the surface of adsorption treatment liquid 7 16。
When blower fan 2 is started working, the outside gas 6 containing flue dust is entered inside process tank 4 by air inlet pipe 5, then is passed through Gas is disperseed and is refined into tiny bubble 10 by the dispersion hole of dispersion plate 9, and tiny bubble 10 is in treatment fluid 7 to gas outlet Flowing, it is more conducive to fully contact with treatment fluid 7 in flow process, in the presence of physics, chemical reaction, forms solid-state, coagulates The species precipitate of poly- state and liquid, suspend or swim in treatment fluid 7, so as to be purified, purified gas is by going out The air inlet of gas port and blower fan 2 enters blower fan 2, and is discharged by the exhaust outlet of blower fan 2, and hydro-peening blast pipe 12 has double action, Valve 14 is opened when process tank 4 adds water or discharges water as steam vent with the air pressure inside and outside Balance Treatment tank 4;Hydro-peening exhaust simultaneously Pipe 12 can also be connected with external water source, and current rinse dispersion plate 9 below by hydro-peening first 8, so as to reach cleaning point Fall apart 9 effect.
Using the soot processing device of above technical scheme, gas passes through treatment fluid, treatment fluid again after fully refinement Dust and other impurities in gas are washed, at the same time it can also which some in gas are absorbed with gas frowzy.Gas passes through Cross after the washing and absorption for the treatment of fluid, be substantially free of dust, and stink also disappears substantially, and also sodium hydroxide solution may be used also To absorb the sour gas such as the carbon dioxide in gas, sulfur dioxide or other oxynitrides, it is possible thereby to enter to gas The further purification of row.In process tank, flue dust can fully contact with treatment fluid, and the effect of processing is more preferable.In addition, pass through spray The air pressure that blast pipe both can be when process tank have added water or discharged water inside and outside Balance Treatment tank is washed, while can also be with external water source phase Connection, have the function that to clean dispersion plate.
Embodiment 2
Fig. 4 schematically shows a kind of soot processing device according to another embodiment of the invention.As schemed Show, the device is made up of two Fans and three process tanks (A, B, C), and each process tank 4 puts one layer of dispersion plate 9 and a water Level controller 17.
Two Fans and three process tanks 4 (A, B, C) are arranged at intervals, and are connected by pipeline 3.
The side wall of process tank 4 is also respectively equipped with air inlet pipe 5 and hydro-peening blast pipe 12.
The outside gas 6 containing flue dust enters process tank 4 by air inlet pipe 5, and by dispersion plate 9 in treatment fluid 7 shape Into tiny bubble 10.
The top of process tank 4 is additionally provided with the floating body thing 16 of the greasy dirt for the surface of adsorption treatment liquid 7.
The tank base of process tank 4 draws a blowdown water valve 13 respectively.
The treatment fluid 7 held in three process tanks 4 is identical or different.
Blower fan 2 is connected with power supply 1.
Above-described is only some embodiments of the present invention.For the person of ordinary skill of the art, not On the premise of departing from the invention design, various modifications and improvements can be made, these belong to the protection model of the present invention Enclose.

Claims (10)

1. a kind of soot processing device, it is characterised in that by blower fan and the process tank installed in the air inlet side of the blower fan Form, the process tank be closed tank body, and it is described handle pot sidewall be respectively equipped with air inlet pipe, gas outlet, water level controller, Hydro-peening blast pipe and blowdown water valve, the gas outlet are located at the top of the tank body of the process tank, and the air inlet pipe is located at the place The tank base of tank is managed, is also equipped with least one dispersion plate inside the process tank, the dispersion plate is located at the entrance of air inlet pipe Top, the dispersion plate have the dispersion hole that aperture is below 0.3mm, and the water level controller is located under the dispersion plate of top layer It is square, the hydro-peening head being connected with the hydro-peening blast pipe is equipped with below every layer of dispersion plate, the blowdown water valve is located at every layer The bottom of dispersion plate is simultaneously drawn outside the process tank, and the tank base of the process tank also draws another sewer simultaneously Valve, the air inlet of the gas outlet and the blower fan is by pipeline communication, and the process tank is built with treatment fluid, and by described Water level controller is filled it up with and maintains water level, and when the blower fan is started working, the fume gases that outside is contained pass through the air inlet pipe Gas is disperseed and is refined into tiny bubble into inside the process tank, then by the dispersion hole of the dispersion plate, it is tiny Bubble in the treatment fluid to the gas outlet flow, in flow process be more conducive to fully contacted with the treatment fluid, In the presence of physics, chemical reaction, the species precipitate of solid-state, condensed state and liquid is formed, suspends or swims in described In treatment fluid, so as to be purified, purified gas enters blower fan by the air inlet of gas outlet and blower fan, and by the row of blower fan Air port is discharged, and the hydro-peening blast pipe has double action, opened when the process tank adds water or discharged water as steam vent with Balance the air pressure inside and outside the process tank;The hydro-peening blast pipe can also be connected with external water source simultaneously, and current pass through institute State hydro-peening primary drying and wash the dispersion plate below, so as to have the function that the cleaning dispersion plate.
2. soot processing device according to claim 1, it is characterised in that multiple described points are provided with inside the process tank Fall apart, vertically interval stacks multiple dispersion plates successively, and spacing distance is 200mm or so.
3. soot processing device according to claim 1, it is characterised in that the dispersion plate is by stainless steel microwell plate and plate Frame is formed, and the stainless steel microwell plate is arranged on the middle part of the sheet frame, and the stainless steel micropore panel aperture is below 0.3mm.
4. soot processing device according to claim 1, it is characterised in that the water level controller is ball float liquid feed valve.
5. soot processing device according to claim 1, it is characterised in that the dispersion plate edge has groove, described Blowdown water valve is located at the groove, for discharging the waste liquid and slag mud that are deposited on above the dispersion plate.
6. soot processing device according to claim 1, it is characterised in that the air inlet side of the blower fan is provided with multiple The process tank, multiple process tanks are serially connected by the pipeline.
7. soot processing device according to claim 1, it is characterised in that the exhaust outlet side of the blower fan is also provided with The process tank, the process tank are connected with the exhaust outlet by the pipeline.
8. soot processing device according to claim 1, it is characterised in that treatment fluid inside the process tank for water or Person's aqueous solution.
9. the soot processing device according to claim 5 or 6, it is characterised in that the institute held in multiple process tanks It is identical or different to state treatment fluid.
10. soot processing device according to claim 1, it is characterised in that be additionally provided with above the dispersion plate of top layer For the floating body thing for the greasy dirt for adsorbing the treatment fluid surface.
CN201711052610.6A 2017-10-30 2017-10-30 A kind of soot processing device Pending CN107537249A (en)

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Application Number Priority Date Filing Date Title
CN201711052610.6A CN107537249A (en) 2017-10-30 2017-10-30 A kind of soot processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711052610.6A CN107537249A (en) 2017-10-30 2017-10-30 A kind of soot processing device

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Publication Number Publication Date
CN107537249A true CN107537249A (en) 2018-01-05

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113559649A (en) * 2021-05-12 2021-10-29 杨胜亿 Smoke dust purification device

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2855520Y (en) * 2005-04-01 2007-01-10 蔡昌品 Equipment for purifying waste air
CN201124075Y (en) * 2007-07-16 2008-10-01 娄爱娟 Tower for absorbing and purifying exhaust air sulfur dioxide
KR20100016986A (en) * 2008-08-05 2010-02-16 주식회사 젠트로 Apparatus for treating pollution gas
CN102784533A (en) * 2011-05-20 2012-11-21 徐自升 Multipurpose pumping-exhaust flue dust processor of serially-connected gas-washing pools
CN202823635U (en) * 2012-09-25 2013-03-27 福建龙净环保股份有限公司 Washing device for wet electric precipitator
CN203139839U (en) * 2013-03-16 2013-08-21 郑敏 Waste gas treatment system
CN203244879U (en) * 2013-04-20 2013-10-23 宁波海曙信满贸易有限公司 Waste gas absorption tower
CN204601901U (en) * 2014-12-19 2015-09-02 惠生工程(中国)有限公司 A kind of spray washing gas wash tower
CN105396410A (en) * 2015-12-11 2016-03-16 天紫工程管理(天津)有限公司 Waste gas purification processing system
CN105605690A (en) * 2016-01-21 2016-05-25 西北大学 Indoor air purifying system and method based on wet filtering
CN208426799U (en) * 2017-10-30 2019-01-25 杨胜亿 A kind of soot processing device

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2855520Y (en) * 2005-04-01 2007-01-10 蔡昌品 Equipment for purifying waste air
CN201124075Y (en) * 2007-07-16 2008-10-01 娄爱娟 Tower for absorbing and purifying exhaust air sulfur dioxide
KR20100016986A (en) * 2008-08-05 2010-02-16 주식회사 젠트로 Apparatus for treating pollution gas
CN102784533A (en) * 2011-05-20 2012-11-21 徐自升 Multipurpose pumping-exhaust flue dust processor of serially-connected gas-washing pools
CN202823635U (en) * 2012-09-25 2013-03-27 福建龙净环保股份有限公司 Washing device for wet electric precipitator
CN203139839U (en) * 2013-03-16 2013-08-21 郑敏 Waste gas treatment system
CN203244879U (en) * 2013-04-20 2013-10-23 宁波海曙信满贸易有限公司 Waste gas absorption tower
CN204601901U (en) * 2014-12-19 2015-09-02 惠生工程(中国)有限公司 A kind of spray washing gas wash tower
CN105396410A (en) * 2015-12-11 2016-03-16 天紫工程管理(天津)有限公司 Waste gas purification processing system
CN105605690A (en) * 2016-01-21 2016-05-25 西北大学 Indoor air purifying system and method based on wet filtering
CN208426799U (en) * 2017-10-30 2019-01-25 杨胜亿 A kind of soot processing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113559649A (en) * 2021-05-12 2021-10-29 杨胜亿 Smoke dust purification device

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