CN205699822U - A kind of high-efficiency device for purifying waste gas - Google Patents

A kind of high-efficiency device for purifying waste gas Download PDF

Info

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
Application number
CN201620552278.4U
Other languages
Chinese (zh)
Inventor
黄艺超
黄朝山
王艮梅
周九程
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.)
Nanjing Panorama Environmental Protection Technology Co Ltd
Original Assignee
Nanjing Panorama Environmental Protection Technology Co Ltd
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 Nanjing Panorama Environmental Protection Technology Co Ltd filed Critical Nanjing Panorama Environmental Protection Technology Co Ltd
Priority to CN201620552278.4U priority Critical patent/CN205699822U/en
Application granted granted Critical
Publication of CN205699822U publication Critical patent/CN205699822U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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

A kind of high-efficiency device for purifying waste gas
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).
CN201620552278.4U 2016-06-08 2016-06-08 A kind of high-efficiency device for purifying waste gas Expired - Fee Related CN205699822U (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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
CN212334595U (en) Device that hydrogen sulfide was handled
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
CN215102210U (en) Catalytic wet oxidation reactor
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
WO2021128728A1 (en) System and method for treating ethylene desulfurization wastewater
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
CN204380493U (en) A kind of dusty gas cleaning system for power industry high reactivity
CN205569873U (en) Multistage siphon separator that hydrolysises of living beings
CN106110756B (en) Pollutant treatment system in impregnation drying production line
CN104892406A (en) Industrialized preparation method of 2-carboxyl-3-naphthalene formic acid
CN215387641U (en) Organic solvent separation and recovery system
CN215712299U (en) Multi-stage reaction device for catalyzing ozone according to pollutant types
CN215756943U (en) Industrial high-concentration wastewater treatment device

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