CN205699822U - A kind of high-efficiency device for purifying waste gas - Google Patents
A kind of high-efficiency device for purifying waste gas Download PDFInfo
- Publication number
- CN205699822U CN205699822U CN201620552278.4U CN201620552278U CN205699822U CN 205699822 U CN205699822 U CN 205699822U CN 201620552278 U CN201620552278 U CN 201620552278U CN 205699822 U CN205699822 U CN 205699822U
- Authority
- CN
- China
- Prior art keywords
- gas
- connects
- water scrubber
- compressor
- export
- 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
Links
Landscapes
- Cyclones (AREA)
Abstract
nullThis utility model relates to waste gas purification art field,Especially a kind of high-efficiency device for purifying waste gas includes water scrubber and sedimentation tank,It is divided into circular chamber and mud chamber by screen plate in described sedimentation tank,Described water scrubber is cylindric,And water scrubber inner chamber array from the bottom to top is provided with cyclone,The upper end of described water scrubber connects the first compressor,And the connection mud chamber, lower end of water scrubber,The port of export of described circular chamber connects the arrival end of water pump,This device can use cyclone to rapidly remove the solid particle in waste gas,Use electrical heating simultaneously and be passed through the mode removing part of reacting gas and be insoluble in the harmful gas of water,Finally gas is mixed with reactant liquor,React under conditions of High Temperature High Pressure catalyst,Remove harmful gas,Compare traditional approach and process more thorough,And it can be avoided that solid particle pollution subsequent reactions device,Extension fixture service life.
Description
Technical field
This utility model relates to waste gas purification technical field, is specially a kind of high-efficiency device for purifying waste gas.
Background technology
Industrial waste gas, especially contains sulfide and the more waste gas of nitride, and environment can be caused great by direct discharge
Polluting, it is therefore desirable to purify, existing purifier efficiency is the highest, when purifying in particular by upstream injection, by
In degree time of contact of gas Yu aqueous solution, response speed is slow, causes purifying the most thorough, if it is possible to invention one can be efficient
The purifier of purifying harmful gas just can solve the problem that problems, we provides a kind of high-efficiency device for purifying waste gas for this.
Utility model content
This utility model solves the technical problem that the defect being to overcome prior art, it is provided that a kind of efficiency of waste gas purifies dress
Put.It is high that described high-efficiency device for purifying waste gas has purification efficiency, purifies the features such as thorough.
For achieving the above object, this utility model provides following technical scheme: a kind of high-efficiency device for purifying waste gas includes water
Washing tower and sedimentation tank, be divided into circular chamber and mud chamber by screen plate in described sedimentation tank, described water scrubber is cylindric, and
Water scrubber inner chamber array from the bottom to top is provided with cyclone, and the upper end of described water scrubber connects the first compressor, and water scrubber
Connection mud chamber, lower end, the port of export of described circular chamber connects the arrival end of water pump, and the port of export of water pump connects water scrubber
Upper end, described first compressor coupled reaction tank, and be provided with heater in retort, the port of export of described retort is even
Connect the second compressor, and the port of export of the second compressor connects gas liquid reaction tower, is provided with catalysis anti-in described gas liquid reaction tower
Answering plate, and the inwall of gas liquid reaction tower is provided with atomization jetting device, the port of export of described gas liquid reaction tower connects gas-liquid separation
Device, and the escape pipe connection harmful gas analysis device of gas-liquid separation device, the drain pipe of described gas-liquid separation device connects
Solution conduit, and the port of export connection atomization jetting device of solution conduit, described harmful gas analysis device connects the second compressor, institute
State water pump, the first compressor, heater, the second compressor, atomization jetting device, gas-liquid separation device and harmful gas analysis
Device is all electrically connected with same controller.
Preferably, in described gas-liquid separation device, centrifugal gas-liquid separator is installed.
Preferably, described heater is array Resistant heating device.
Preferably, it is mounted on digital baroceptor in described retort and gas-liquid reaction tower.
Compared with prior art, the beneficial effects of the utility model are: this utility model can use cyclone to remove rapidly
Remove the solid particle in waste gas, use electrical heating simultaneously and be passed through the mode removing part of reacting gas and be insoluble in harmful gas of water
Body, finally mixes gas with reactant liquor, reacts under conditions of High Temperature High Pressure catalyst, removes harmful gas,
Compare traditional approach and process more thorough, and it can be avoided that solid particle pollution subsequent reactions device, extension fixture uses the longevity
Life.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
In figure: 1 water scrubber, 2 cyclones, 3 water pumps, 4 first compressors, 5 heaters, 6 retort, 7 second compressors,
8 catalytic reaction plates, 9 gas liquid reaction towers, 10 atomization jetting devices, 11 NaOH solution tank NaOHs, 12 gas-liquid separation devices, 13 harmful gas analysis
Device, 14 mud chambers, 15 screen plates, 16 circular chambers, 17 sedimentation tanks.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise
The every other embodiment obtained, broadly falls into the scope of this utility model protection.
Referring to Fig. 1, a kind of technical scheme of this utility model offer: a kind of high-efficiency device for purifying waste gas, including water scrubber 1
With sedimentation tank 17, being divided into circular chamber 16 and mud chamber 14 by screen plate 15 in sedimentation tank 17, water scrubber 1 is cylindric, and
Water scrubber 1 inner chamber array from the bottom to top is provided with cyclone 2, and the upper end of water scrubber 1 connects the first compressor 4, and water scrubber 1
Connection mud chamber, lower end 14, the port of export of circular chamber 16 connects the arrival end of water pump 3, and the port of export of water pump 3 connects washing
The upper end of tower 1, the first compressor 4 coupled reaction tank 6, and in retort 6, it is provided with heater 5, the port of export of retort 6 is even
Connect the second compressor 7, and the port of export of the second compressor 7 connects gas liquid reaction tower 9.
It is provided with catalytic reaction plate 8 in the gas liquid reaction tower 9 of this device, and the inwall of gas liquid reaction tower 9 is provided with atomization
Injection apparatus 10, the port of export of gas liquid reaction tower 9 connects gas-liquid separation device 12, and the escape pipe of gas-liquid separation device 12 connects
Harmful gas analysis device 13, the drain pipe of gas-liquid separation device 12 connects solution conduit 11, and the port of export of solution conduit 11 connects
Atomization jetting device 10, harmful gas analysis device 13 connects the second compressor 7.
Water pump 3, first compressor 4 of this device, heater the 5, second compressor 7, atomization jetting device 10, gas-liquid are divided
All it is electrically connected with same controller from device 12 and harmful gas analysis device 13, is provided with centrifugal in gas-liquid separation device 12
Gas-liquid separator, heater 5 is to be mounted on numeral in array Resistant heating device, retort 6 and gas-liquid reaction tower 9
Formula baroceptor.
The solid particle that the cyclone 2 within water scrubber 1 removes in waste gas, the solid being removed is utilized during the work of this device
Granule will enter mud chamber 14, and entrance circular chamber 16 is recirculated utilization by current, flow out the waste gas of water scrubber 1 by the first pressure
Contracting machine 4 is pressed into retort 6, reacts with the reacting gas in retort 6, and removing part is insoluble in harmful gas of aqueous solution
Body, waste gas continues flow through the second compressor 7 and is pressed into gas liquid reaction tower 9 and reacts, finally by gas-liquid separation device 12
Separating, aqueous solution re-starts circulation, and the gas after processing enters harmful gas separating device 13 and detects, and reaches
Directly discharging after standard, the not up to gas of standard reenters gas liquid reaction tower 9 and reacts, owing to this device entirety is permissible
Being placed in heat insulation loop domestic, whole processing procedure is all in hot environment, therefore, it is possible to reduce the loss of heat, increases reaction speed
Rate, and the gas after processing can also carry out waste heat recovery, improves heating efficiency, owing to this assembly first is gone out
Solid particle in waste gas, is polluted therefore, it is possible to be prevented effectively from follow up device by solid particle, increases the entirety of device
In service life, process more thorough, in hgher efficiency have the highest practical value.
Embodiment the most of the present utility model, for the ordinary skill in the art,
It is appreciated that in the case of without departing from principle of the present utility model and spirit and these embodiments can be carried out multiple change, repair
Changing, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (4)
1. a high-efficiency device for purifying waste gas, it is characterised in that: include water scrubber (1) and sedimentation tank (17), described sedimentation tank
(17) being divided into circular chamber (16) and mud chamber (14) by screen plate (15) in, described water scrubber (1) is cylindric, and washing
Tower (1) inner chamber array from the bottom to top is provided with cyclone (2), and the upper end of described water scrubber (1) connects the first compressor (4),
And the connection mud chamber, lower end (14) of water scrubber (1), the port of export of described circular chamber (16) connects the arrival end of water pump (3), and
The port of export of water pump (3) connects the upper end of water scrubber (1), described first compressor (4) coupled reaction tank (6), and retort (6)
Inside being provided with heater (5), the port of export of described retort (6) connects the second compressor (7), and the second compressor (7)
The port of export connects gas liquid reaction tower (9), is provided with catalytic reaction plate (8), and gas liquid reaction tower in described gas liquid reaction tower (9)
(9) inwall is provided with atomization jetting device (10), and the port of export of described gas liquid reaction tower (9) connects gas-liquid separation device
(12), and gas-liquid separation device (12) escape pipe connect harmful gas analysis device (13), described gas-liquid separation device (12)
Drain pipe connect solution conduit (11), and solution conduit (11) the port of export connect atomization jetting device (10), described harmful gas
Analytical equipment (13) connects the second compressor (7), described water pump (3), the first compressor (4), heater (5), the second compression
Machine (7), atomization jetting device (10), gas-liquid separation device (12) and harmful gas analysis device (13) are all electrically connected with same control
Device processed.
A kind of high-efficiency device for purifying waste gas the most according to claim 1, it is characterised in that: described gas-liquid separation device (12)
Centrifugal gas-liquid separator is inside installed.
A kind of high-efficiency device for purifying waste gas the most according to claim 1, it is characterised in that: described heater (5) is battle array
Column Resistant heating device.
A kind of high-efficiency device for purifying waste gas the most according to claim 1, it is characterised in that: described retort (6) and gas-liquid
Reaction tower is mounted on digital baroceptor in (9).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620552278.4U CN205699822U (en) | 2016-06-08 | 2016-06-08 | A kind of high-efficiency device for purifying waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620552278.4U CN205699822U (en) | 2016-06-08 | 2016-06-08 | A kind of high-efficiency device for purifying waste gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205699822U true CN205699822U (en) | 2016-11-23 |
Family
ID=57302399
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620552278.4U Expired - Fee Related CN205699822U (en) | 2016-06-08 | 2016-06-08 | A kind of high-efficiency device for purifying waste gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205699822U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107866146A (en) * | 2017-11-08 | 2018-04-03 | 湖州山海环保工程有限公司 | A kind of waste gas recovery processing unit |
CN107974393A (en) * | 2018-01-08 | 2018-05-01 | 深圳市朗司医疗科技有限公司 | A kind of heating unit being applied in nucleic acid extraction system |
-
2016
- 2016-06-08 CN CN201620552278.4U patent/CN205699822U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107866146A (en) * | 2017-11-08 | 2018-04-03 | 湖州山海环保工程有限公司 | A kind of waste gas recovery processing unit |
CN107974393A (en) * | 2018-01-08 | 2018-05-01 | 深圳市朗司医疗科技有限公司 | A kind of heating unit being applied in nucleic acid extraction system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103933826B (en) | A kind of processing method of cumyl peroxide process gas | |
CN101254392B (en) | Energy-saving type sodium sulphite circulation desulfurizing device and method | |
CN205699822U (en) | A kind of high-efficiency device for purifying waste gas | |
CN215916528U (en) | Three-phase separation system for tar, ammonia water and tar residues | |
CN105251231B (en) | The exhaust treatment system and method for organic silicon low-boiling-point substance conversion reaction | |
WO2021128728A1 (en) | System and method for treating ethylene desulfurization wastewater | |
CN210544314U (en) | Spraying evaporator | |
CN201775977U (en) | Treatment device for reaction tail gas in trimellitic acid production | |
CN205760487U (en) | A kind of yellow phosphoric tail gas absorption plant | |
CN201762264U (en) | Medium-pressure acetylene gas drying purification device | |
CN214233430U (en) | Energy-saving efficient type purifying column | |
CN203938621U (en) | A kind of by the refining isobutyric suite of equipment of isobutyric aldehyde | |
CN204911450U (en) | Fluoridize reaction kettle device organically | |
CN209885530U (en) | Acid mist absorption device of polyaluminium chloride production system | |
CN203316113U (en) | Continuous pressure-reducing backflow dehydration device of reaction still | |
CN207227161U (en) | A kind of coking wastewater strenuous primary treatment device | |
CN202052457U (en) | Novel low-pressure carbon dioxide regeneration tower | |
CN204380493U (en) | A kind of dusty gas cleaning system for power industry high reactivity | |
CN221267138U (en) | Mother liquor recovery tank for 2-chloropropionic acid production | |
CN106110756B (en) | Pollutant treatment system in impregnation drying production line | |
CN104892406A (en) | Industrialized preparation method of 2-carboxyl-3-naphthalene formic acid | |
CN104876397A (en) | Method for treating weak acid blue AS dye production wastewater | |
CN215712299U (en) | Multi-stage reaction device for catalyzing ozone according to pollutant types | |
CN215756943U (en) | Industrial high-concentration wastewater treatment device | |
CN219897617U (en) | Environment-friendly high-efficiency desulfurizing tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
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: 20161123 Termination date: 20180608 |