CN206935083U - Industrial waste gas purifying processing system - Google Patents
Industrial waste gas purifying processing system Download PDFInfo
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- CN206935083U CN206935083U CN201720595779.5U CN201720595779U CN206935083U CN 206935083 U CN206935083 U CN 206935083U CN 201720595779 U CN201720595779 U CN 201720595779U CN 206935083 U CN206935083 U CN 206935083U
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- Treating Waste Gases (AREA)
Abstract
A kind of industrial waste gas purifying processing system, including catalyst chamber, magnetization chamber, clear up absorption plant；The catalyst chamber, magnetization chamber are hollow columnar, and catalyst chamber connects with magnetization chamber, and catalyst chamber one end is exhaust gas inlet, and the magnetization chamber other end is inserted in the resolution absorption plant by exhaust piping, and resolution absorption plant is built with resolution absorbing liquid.Waste gas is passed through into catalyst chamber, magnetization chamber, resolution absorption plant step by step, first the nitrogen oxides in waste gas, sulfide are removed while reduce the content of PM10, PM2.5 in flue dust, neutralized again by clearing up absorption plant and the acid mist generated in magnetization chamber and filter out big particle, the concentration and formula of the liquid proportion of digestion pool are determined by the composition of waste gas, flexible modulation, the various harmful components that can be effectively gone in removing exhaust gas by the utility model, while apparatus structure is simple, input is low.
Description
Technical field
It the utility model is related to technical field of waste gas treatment, and in particular to a kind of industrial waste gas purifying processing system.
Background technology
Industrial waste gas is caused in plant area of enterprise fuel combustion and production process various to be discharged into containing for air
The general name of contaminant gases.These waste gas have：Carbon dioxide, carbon disulfide, hydrogen sulfide, fluoride, nitrogen oxides, chlorine, chlorination
Hydrogen, carbon monoxide, sulfuric acid (mist) lead mercury, beryllide, flue dust and industrial dust, are discharged into air, can pollute air.These materials
Entered by different approach respiratory tracts inside people, the direct generation harm having, some also has cumulative effect, can be more serious
The health for endangering people.
Industrial waste gas processing the active carbon adsorption of principle, Production by Catalytic Combustion Process, catalytic oxidation, acid-base neutralization method, etc.
A variety of principles such as ion method, due to industrial waste gas complicated component, various processing methods are difficult to effectively go harmful in removing exhaust gas
Material.
Utility model content
The utility model is in order to solve the above technical problems, provide a kind of industrial waste gas purifying processing system.
Technical problem to be solved in the utility model is realized using following technical scheme.
A kind of industrial waste gas purifying processing system, including catalyst chamber, magnetization chamber, clear up absorption plant；The catalyst chamber, magnetic
Change room is hollow columnar, and catalyst chamber connects with magnetization chamber, and catalyst chamber one end is exhaust gas inlet, and the magnetization chamber other end passes through flue gas leading
In the road insertion resolution absorption plant, resolution absorption plant is built with resolution absorbing liquid.
The catalyst chamber both ends are provided with the front shroud of manhole, back shroud respectively, and annular catalyst reaction hood is placed in
In catalyst chamber, the annular catalyst reaction hood central axis overlaps with catalyst chamber central axis, the end seal of annular catalyst reaction hood one
Close, another end opening, openend is fixed on back shroud, and annular catalyst reaction hood blind end sets aperture, ring towards front shroud
Vortex generator is set on shape catalytic reaction cover blind end inwall.
Manhole diameter on the catalyst chamber front shroud is more than the manhole diameter on back shroud.
The catalysis chamber interior walls set atomizer close to front shroud.
Secondary response cover is set in the annular catalyst reaction hood, and the secondary response cover opening end is fixed on back shroud
On, quadric catalysis is carried out to gas by secondary response cover.
Backflow preventer is set on the catalyst chamber back shroud outer wall, avoids waste gas from flowing backwards into catalyst chamber.
The atomizer includes high-pressure pump, and water inlet is set in the high-pressure pump side wall, and high-pressure pump delivery port one end is set
Cover plate, high-pressure pump delivery port are connected with core body, and mist cover is set on the outside of the core body, and described mist cover one end is fixed on the cover board.
The magnetization chamber interior walls are close to set ozone generator with catalyst chamber junction, and magnet is close to magnetization chamber interior walls
On, magnetization chamber interior walls set apparatus for eliminating sludge between ozone generator and magnet.
The magnetization chamber interior walls, which are located on different cross section to be respectively separated, sets 2-4 ozone generator, magnet, scale removal dress
Put.
The resolution absorption plant includes resolution absorption cell, and digestion solution is placed in the resolution absorption cell, the flue gas leading
It is connected in road end insertion digestion solution and with blast pipe, clears up and PH meters, thermometer, pressure gauge are set respectively on absorption cell inwall,
The PH meters, thermometer, pressure gauge are connected with data acquisition controller respectively, and the data acquisition controller connects with controller
Connect, the controller is connected with dosing pump, and dosing pump discharge pipe is stretched into resolution absorption cell, and medicament enters from dosing pump inlet tube
Enter.
The beneficial effects of the utility model are：By waste gas step by step by catalyst chamber, magnetization chamber, resolution absorption plant, first will
Nitrogen oxides, sulfide in waste gas remove while reduce the content of PM10, PM2.5 in flue dust, then by clearing up absorption plant
Neutralize the acid mist generated in magnetization chamber and filter out big particle, the concentration and formula of the liquid proportion of digestion pool are by waste gas
Composition determines that flexible modulation, by the various harmful components of the invention that can effectively go in removing exhaust gas, while apparatus structure is simple
Single, input is low.
Brief description of the drawings
Fig. 1 is the utility model simplified schematic diagram；
Fig. 2 is the utility model catalyst chamber schematic cross-section；
Fig. 3 is the utility model atomizer schematic diagram；
Fig. 4 is the utility model magnetization chamber schematic diagram；
Fig. 5 is that the utility model clears up absorption cell schematic diagram.
Embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
As shown in figure 1, a kind of industrial waste gas purifying processing system, including catalyst chamber 1, magnetization chamber 2, clear up absorption plant 3；
Catalyst chamber 1, magnetization chamber 2 are hollow columnar, and catalyst chamber 1 connects with magnetization chamber 2, and the one end of catalyst chamber 1 is exhaust gas inlet, magnetization chamber 2
The other end is inserted in resolution absorption plant 3 by exhaust piping 4, and resolution absorption plant 3 is built with resolution absorbing liquid.
Catalyst chamber 1, the section of magnetization chamber 2 are circular or square.
As shown in Fig. 2 the both ends of catalyst chamber 1 are provided with the front shroud 18 of manhole, back shroud 19, front shroud 18 respectively
On manhole diameter be more than manhole diameter on back shroud 19, annular catalyst reaction hood 13 is placed in catalyst chamber 1, ring
The central axis of shape catalytic reaction cover 13 is overlapped with the central axis of catalyst chamber 1, and the one end of annular catalyst reaction hood 13 closing, the other end is opened
Mouthful, openend is fixed on back shroud 19, and the blind end of annular catalyst reaction hood 13 sets aperture 16 towards front shroud 18, and annular is urged
Change and vortex generator 12 is set on the blind end inwall of reaction hood 13, waste gas enters in annular catalyst reaction hood 13 from aperture 16 to be driven
Vortex generator 12 is rotated so as to produce vortex in annular catalyst reaction hood 13, and the inwall of catalyst chamber 1 is set close to the interval of front shroud 18
Atomizer 11 is put, is atomized the waste gas entered in catalyst chamber 1 by atomizer 11, further in annular catalyst reaction hood 13
Interior setting secondary response cover 14, the openend of secondary response cover 14 is fixed on back shroud 19, by secondary response cover 14 to gas
Quadric catalysis is carried out, backflow preventer 15 is set on the outer wall of 1 back shroud of catalyst chamber 19, avoids waste gas from flowing backwards into catalyst chamber 1.
Fig. 3 show the atomizer 11 in the present invention, and atomizer 11 includes high-pressure pump 112, set in the side wall of high-pressure pump 112
Water inlet 111, the delivery port one end of high-pressure pump 112 set cover plate 115, and the delivery port of high-pressure pump 112 is connected with core body 113, passes through core
The water that body 113 sprays high-pressure pump 112 from delivery port is atomized, and the outside of core body 113 sets mist cover 114, and the one end of mist cover 114 is consolidated
It is scheduled on cover plate 115.
Magnetization chamber 2 sets ozone generator 21, magnet as shown in figure 4, the inwall of magnetization chamber 2 is close with the junction of catalyst chamber 1
22 are close on the inwall of magnetization chamber 2, and 22 preferred annular magnet of magnet, the inwall of magnetization chamber 2 is located at ozone generator 21 and magnet 22
Between set apparatus for eliminating sludge 23, can the inwall of magnetization chamber 2 be located on different cross section be respectively separated setting 2-4 ozone generator
21st, magnet 22, apparatus for eliminating sludge 23.
Fig. 4 show the resolution absorption plant 3 in the present invention, including resolution absorption cell 311, digestion solution 301 are placed in resolution
In absorption cell 311, it is connected in the end of exhaust piping 4 insertion digestion solution 301 and with blast pipe 304, blast pipe 304 is preferably rectangular
Shape tabular to increase waste gas and the contact area of digestion solution 301, clear up set on the inwall of absorption cell 311 PH count 306, thermometer 307,
Pressure gauge 308, PH meters 306, thermometer 307, pressure gauge 308 are connected with data acquisition controller 310 respectively, by PH meters 306,
Thermometer 307, the detection of pressure gauge 308 clear up the indices of digestion solution 301 in absorption cell 311 and feed data back to data acquisition
Controller 310, data acquisition controller 310 are connected with controller 305, and controller 305 is connected with dosing pump 303, dosing pump 303
Outlet is stretched into resolution absorption cell 311, and the outlet pipe end connection guard 309, medicament is from the inlet tube 302 of dosing pump 303
Into when PH counts 306, thermometer 307, pressure gauge 308 detects that the indices of digestion solution 301 deviate setting value, by data
Data acquisition controller 310 is fed back to, data acquisition controller 310 sends signal to controller 305, and controller 305, which is sent, to be opened
Dynamic dosing pump 303 is ordered, so as to add medicament into resolution absorption cell 311.
Operation principle of the present invention：Industrial waste gas main component is nitrogen oxides (NOx), sulfide (SO2) etc., and gas endangers
For maximum, at the same in flue dust PM10, PM2.5 content it is also higher.
High-temperature gas enters catalyst chamber 1, and the water smoke that atomizer 11 generates makes high-temperature gas cool to suitable catalyst
The temperature of reaction, nitrogen oxides, sulfide in waste gas enter catalyst chamber 1 by annular catalyst reaction hood 13 ((rhodium (Rh), palladium
(Pd), platinum (Pt)) catalytic decomposition.As decomposition reaction NO → 1/2N2+1/2O2, wherein Pt, Pd have to CO, HC oxidation removal
High activity, and Rh has the catalysis reduction excellent to NO, N0 selectively can be reduced to N2 and suppress NH3 generation by it.
Gas blade rotation, is produced vortex, waste gas is repeated by catalytic reaction by the aperture high speed impact swirl vane of reaction hood
Reduction.
The effect of atomizer of the present invention：Make particulate matter in flue gas and by the nitrogen oxides of catalysis reduction and sulfide with
Vapor forms larger particle, similar to the formation of acid rain, NO->HNO3, HNO2, acid mist enter in reaction tank and digestion pool
Bases liquid neutralize into harmless salts substances.The effect of high intensity magnet has, adsorbing metal particle, adsorbs charged ion
Grain, further purify the particulate matter in waste gas
Ozone generator in magnetization chamber, substantial amounts of ozone is produced, reacting generation nitrogen reaction equation with nitrogen oxide is：
N2O+O--->N2+O2, N2+O2--->2NO
NO+O3--->NO2+O2, NO2+O--->NO+O2
O3+0--->202
The effect of digestion pool of the present invention：Neutralize remaining acid in magnetization chamber and filter out big particle, the liquid of digestion pool
The concentration and formula of body proportioning are determined by the composition of waste gas.Basis is ammoniacal liquor, sodium chloride etc..
The advantages of general principle and principal character of the present utility model and the utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the spirit and scope of the utility model is not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within claimed the scope of the utility model.The utility model
Claimed scope is by appended claims and its equivalent thereof.
Claims (10)
- A kind of 1. industrial waste gas purifying processing system, it is characterised in that：Including catalyst chamber, magnetization chamber, absorption plant is cleared up；It is described Catalyst chamber, magnetization chamber are hollow columnar, and catalyst chamber connects with magnetization chamber, and catalyst chamber one end is exhaust gas inlet, the magnetization chamber other end Inserted by exhaust piping in the resolution absorption plant, resolution absorption plant is built with resolution absorbing liquid.
- 2. industrial waste gas purifying processing system as claimed in claim 1, it is characterised in that：The catalyst chamber both ends are set respectively Front shroud, back shroud with manhole, annular catalyst reaction hood are placed in catalyst chamber, the annular catalyst reaction hood center Axis overlaps with catalyst chamber central axis, and the closing of annular catalyst reaction hood one end, another end opening, openend is fixed on back shroud On, annular catalyst reaction hood blind end sets aperture towards front shroud, and vortex is set on annular catalyst reaction hood blind end inwall Generator.
- 3. industrial waste gas purifying processing system as claimed in claim 2, it is characterised in that：Circle on the catalyst chamber front shroud Shape through-hole diameter is more than the manhole diameter on back shroud.
- 4. industrial waste gas purifying processing system as claimed in claim 2, it is characterised in that：The catalysis chamber interior walls are close to protecgulum Plate sets atomizer.
- 5. industrial waste gas purifying processing system as claimed in claim 2, it is characterised in that：Set in the annular catalyst reaction hood Secondary response cover is put, the secondary response cover opening end is fixed on back shroud.
- 6. industrial waste gas purifying processing system as claimed in claim 2, it is characterised in that：On the catalyst chamber back shroud outer wall Backflow preventer is set.
- 7. industrial waste gas purifying processing system as claimed in claim 4, it is characterised in that：The atomizer includes high-pressure pump, Water inlet is set in the high-pressure pump side wall, and high-pressure pump delivery port one end sets cover plate, and high-pressure pump delivery port is connected with core body, institute State and mist cover is set on the outside of core body, described mist cover one end is fixed on the cover board.
- 8. industrial waste gas purifying processing system as claimed in claim 1, it is characterised in that：The magnetization chamber interior walls are close with urging Change room junction and ozone generator is set, magnet is close in magnetization chamber interior walls, and magnetization chamber interior walls are located at ozone generator and magnetic Apparatus for eliminating sludge is set between iron.
- 9. industrial waste gas purifying processing system as claimed in claim 8, it is characterised in that：The magnetization chamber interior walls are positioned at difference It is respectively separated on section and 2-4 ozone generator, magnet, apparatus for eliminating sludge is set.
- 10. industrial waste gas purifying processing system as claimed in claim 1, it is characterised in that：The resolution absorption plant includes Absorption cell is cleared up, digestion solution is placed in the resolution absorption cell, and the exhaust piping end is inserted in digestion solution and and blast pipe Connection, clear up and PH meters, thermometer, pressure gauge be set respectively on absorption cell inwall, the PH meters, thermometer, pressure gauge respectively with Data acquisition controller is connected, and the data acquisition controller is connected with controller, and the controller is connected with dosing pump, dosing Pump discharge pipe is stretched into resolution absorption cell, and medicament enters from dosing pump inlet tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720595779.5U CN206935083U (en) | 2017-05-25 | 2017-05-25 | Industrial waste gas purifying processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720595779.5U CN206935083U (en) | 2017-05-25 | 2017-05-25 | Industrial waste gas purifying processing system |
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| CN206935083U true CN206935083U (en) | 2018-01-30 |
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ID=61362285
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107088353A (en) * | 2017-05-25 | 2017-08-25 | 合肥德秦人居环境科技有限公司 | Industrial waste gas purifying processing system |
| CN108246040A (en) * | 2018-03-29 | 2018-07-06 | 蒙城县弘文信息科技有限公司 | A kind of atmosphere pollution preventing mean |
| CN108261903A (en) * | 2018-03-29 | 2018-07-10 | 蒙城县弘文信息科技有限公司 | A kind of Air Pollution Control preventing mean |
| CN108434909A (en) * | 2018-03-29 | 2018-08-24 | 蒙城县弘文信息科技有限公司 | A kind of Air Pollution Control device |
| CN109011983A (en) * | 2018-08-24 | 2018-12-18 | 郑州釜鼎热能技术有限公司 | A kind of dedusting decontamination device of magnetic liquid purifying contaminated gas |
-
2017
- 2017-05-25 CN CN201720595779.5U patent/CN206935083U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107088353A (en) * | 2017-05-25 | 2017-08-25 | 合肥德秦人居环境科技有限公司 | Industrial waste gas purifying processing system |
| CN107088353B (en) * | 2017-05-25 | 2023-11-17 | 合肥德秦人居环境科技有限公司 | Industrial waste gas purifying treatment system |
| CN108246040A (en) * | 2018-03-29 | 2018-07-06 | 蒙城县弘文信息科技有限公司 | A kind of atmosphere pollution preventing mean |
| CN108261903A (en) * | 2018-03-29 | 2018-07-10 | 蒙城县弘文信息科技有限公司 | A kind of Air Pollution Control preventing mean |
| CN108434909A (en) * | 2018-03-29 | 2018-08-24 | 蒙城县弘文信息科技有限公司 | A kind of Air Pollution Control device |
| CN108434909B (en) * | 2018-03-29 | 2020-01-17 | 蒙城县弘文信息科技有限公司 | Atmospheric pollution control device |
| CN109011983A (en) * | 2018-08-24 | 2018-12-18 | 郑州釜鼎热能技术有限公司 | A kind of dedusting decontamination device of magnetic liquid purifying contaminated gas |
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