CN206295812U - Sewage treatment plants exhaust-gas treatment integration apparatus - Google Patents
Sewage treatment plants exhaust-gas treatment integration apparatus Download PDFInfo
- Publication number
- CN206295812U CN206295812U CN201621419622.9U CN201621419622U CN206295812U CN 206295812 U CN206295812 U CN 206295812U CN 201621419622 U CN201621419622 U CN 201621419622U CN 206295812 U CN206295812 U CN 206295812U
- Authority
- CN
- China
- Prior art keywords
- catalyst
- tower body
- nozzle barrel
- blower fan
- integration apparatus
- 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
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- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model discloses sewage treatment plants exhaust-gas treatment integration apparatus, including nozzle barrel, catalyst liberation port, catalyst transfer tube, reative cell, gas inlet pipeline, tower body, catalyst liquid locker room and catalyst power set, blower fan, the tower body is cylindrical, tower body inside is cavity, and its top is the type of falling bucket pipeline；Described gas inlet pipeline one end is connected with the type of falling bucket pipeline, and its other end is connected with blower fan；The catalyst liberation port is arranged on catalyst transmission tube wall, and catalyst transfer tube is placed on nozzle barrel inwall, and catalyst liberation port is corresponding with the position of the circular opening of nozzle barrel.The utility model uses catalyst power set, make to be more fully mixed with waste gas after catalyst atomization, improve the mixability of catalyst and waste gas, make catalyst more uniform with the reaction of waste gas, the utilization rate of catalyst is improved, catalyst is effectively reduced and is gone use cost.
Description
Technical field
The utility model is related to purifying column, and in particular to sewage treatment plants exhaust-gas treatment integration apparatus.
Background technology
Exhaust gas source is divided into natural origin and artificial source.Natural origin include immobilising Hu Gou marshes in, various pasture and water,
Methyl sulphur, methyl mercaptan that algae catabolism is produced etc.；The corrupt hydrogen sulfide for decomposing to give off such as spoil and plant debris,
The corruptibility foul smell such as ammonia.One process of the development experience of waste gas Prevention Technique, today is progressively developed into from initial WATER-WASHING METHOD
Microbial method, active carbon adsorption, photocatalytic degradation method.Industrialized production pursues mechanization production, Automated condtrol, but
Be there is also some problems using the purifying column of catalyst in the prior art, including catalyst causes reaction with waste gas undercompounding
Uneven, catalyst utilization rate is low, increased the use cost of catalyst.
Utility model content
Technical problem to be solved in the utility model is that catalyst causes to react uneven, mesh with waste gas undercompounding
Be that sewage treatment plants exhaust-gas treatment integration apparatus are provided, improve the mixability of catalyst and waste gas, make catalysis
Agent is more uniform with the reaction of waste gas, improves the utilization rate of catalyst, effectively reduces catalyst and goes use cost.
The utility model is achieved through the following technical solutions：
Sewage treatment plants exhaust-gas treatment integration apparatus, including the transmission of nozzle barrel, catalyst liberation port, catalyst
Pipe, reative cell, gas inlet pipeline, tower body, catalyst liquid locker room and catalyst power set, blower fan, the tower body is in
Cylindric, tower body inside is cavity, and its top is the type of falling bucket pipeline；Described gas inlet pipeline one end connects with the type of falling bucket pipeline
Connect, its other end is connected with blower fan；The nozzle barrel is cylindrical, and circular opening is provided with its barrel, and nozzle barrel is put vertically
At tower body internal axis；The catalyst liberation port is arranged on catalyst transmission tube wall, and catalyst transfer tube is placed in
On nozzle barrel inwall, catalyst liberation port is corresponding with the position of the circular opening of nozzle barrel；The catalyst liquid locker room
It is cuboid, it is cavity that it is internal, and tower body lower end is arranged on catalyst liquid locker room upper surface, the catalyst power set
Catalyst liquid locker room upper surface is arranged on, the reative cell is the sky formed between nozzle tube outer surface and tower body inner surface
Chamber.Waste gas is sent into reative cell by blower fan from gas inlet pipeline, and catalyst power set make the catalysis of catalyst liquid locker room
Agent enters nozzle barrel by catalyst transfer tube, and catalyst is atomized by the hole on nozzle barrel barrel and entered under pressure
In reative cell, waste gas mixes with catalyst in reative cell, plays the effect that catalyst clears up waste gas.
Further, nozzle barrel top sealing.The sealing of nozzle barrel top is in order to avoid waste gas is directly entered catalyst liquid
Untapped catalyst is polluted in body locker room.
Further, sewage treatment plants exhaust-gas treatment integration apparatus, also including electrical control cubicles, the electrical control cubicles are set
Near blower fan, electrical control cubicles are used to control the switch and rotating speed of blower fan.Electrical control cubicles control the switch and rotating speed of blower fan, control waste gas
Into in the reative cell of tower body reaction is sufficiently mixed with catalyst.
Further, sewage treatment plants exhaust-gas treatment integration apparatus, also including light source, the light source is arranged on spray
Mouth cylinder outer surface, number of light sources at least four.Using light source, the effect of catalysis is played in the reaction to catalyst and waste gas,
Making the treatment effeciency of waste gas further increases.
The utility model compared with prior art, has the following advantages and advantages：The utility model uses catalysis
Agent power set, make to enter reative cell after catalyst atomization, while in waste gas is rapidly entered reative cell using blower fan, improving
Waste gas and the mixability of catalyst, make catalyst more uniform with the reaction of waste gas, improve the utilization rate of catalyst, effectively subtract
Few catalyst goes use cost.
Brief description of the drawings
Accompanying drawing described herein is used for providing further understanding the utility model embodiment, constitutes the one of the application
Part, does not constitute the restriction to the utility model embodiment.In the accompanying drawings：
Fig. 1 is the utility model structural representation.
Mark and corresponding parts title in accompanying drawing：
1- nozzle barrels, 2- catalyst liberation ports, 3- catalyst transfer tubes, 4- reative cells, 5- gas inlet pipelines, 6- towers
Body, 7- light sources, 8- catalyst liquids locker room, 9- catalyst power set, 10- blower fans, 11- electrical control cubicles.
Specific embodiment
To make the purpose of this utility model, technical scheme and advantage become more apparent, with reference to embodiment and accompanying drawing,
The utility model is described in further detail, and exemplary embodiment of the present utility model and its explanation are only used for explaining this
Utility model, is not intended as to restriction of the present utility model.
Embodiment
As shown in figure 1, sewage treatment plants exhaust-gas treatment integration apparatus, including nozzle barrel 1, catalyst liberation port 2,
Catalyst transfer tube 3, reative cell 4, gas inlet pipeline 5, tower body 6, catalyst liquid locker room 8 and catalyst power set 9,
Blower fan 10, the tower body 6 is cylindrical, and the inside of tower body 6 is cavity, and its top is the type of falling bucket pipeline；The gas inlet pipeline 5
One end is connected with the type of falling bucket pipeline, and its other end is connected with blower fan 10；The nozzle barrel 1 is cylindrical, is provided with its barrel
Circular opening, nozzle barrel 1 is vertically placed at the internal axis of tower body 6；The catalyst liberation port 2 is arranged on catalyst transfer tube 3
On tube wall, catalyst transfer tube 3 is placed on the inwall of nozzle barrel 1, the position of the circular opening of catalyst liberation port 2 and nozzle barrel 1
Put corresponding；The catalyst liquid locker room 8 is cuboid, and it is cavity that it is internal, and the lower end of tower body 6 is arranged on catalyst liquid
The upper surface of locker room 8, the catalyst power set 9 are arranged on the upper surface of catalyst liquid locker room 8, and the reative cell 4 is
The cavity formed between the outer surface of nozzle barrel 1 and the inner surface of tower body 6.The sealing of the top of the nozzle barrel 1.Sewage treatment plants give up
Gas disposal integration apparatus, also including electrical control cubicles 11, the electrical control cubicles are arranged near blower fan 10, and electrical control cubicles 11 are used to control wind
The switch and rotating speed of machine 10.Sewage treatment plants exhaust-gas treatment integration apparatus, also including light source 7, the light source 7 is arranged on
The outer surface of nozzle barrel 1, the number of light source 7 at least four.
In the present embodiment, gas inlet pipeline 5 is made up of multistage hollow cylinder, and blower fan 10 is arranged on gas inlet pipeline 5
Inside, its control circuit is arranged in the middle of electrical control cubicles 11, and electrical control cubicles 11 can control the switch and rotating speed of blower fan 10；Nozzle barrel 1 is straight
Footpath is provided with 6 catalyst transfer tubes 3 less than the diameter of tower body 6 on the inside of nozzle barrel 1, and homogeneous vertical is distributed in table in nozzle barrel 1
Face, catalyst liberation port 2 and the circular opening on the barrel of nozzle barrel 1 of catalyst transfer tube 3 match, and each catalyst is passed
Defeated pipe 3 is provided with 14 catalyst liberation ports 2, and catalyst liberation port 2 uses atomizer that catalyst is sent into reaction
In room 4, light source 7 is provided with 5 row, and each column is evenly distributed on the outer wall of nozzle barrel 1, and each row are vertical 5, and its spacing is equal；Urge
Agent power set 9 use the combination unit of drip pump and booster, first using drip pump by catalyst
By liquid catalyst feeding catalyst transfer tube 3 from catalyst liquid locker room 8, reuse booster and liquid catalyst exists
Atomizer in the presence of pressure by catalyst liberation port 2 enters reative cell 4, makes waste gas with catalyst under illumination condition
Reaction is sufficiently mixed, the service efficiency of catalyst, reduces cost is improved.
Above-described specific embodiment, is entered to the purpose of this utility model, technical scheme and beneficial effect
One step is described in detail, be should be understood that and be the foregoing is only specific embodiment of the present utility model, is not used to limit
Fixed protection domain of the present utility model, all any modifications within spirit of the present utility model and principle, made, equally replaces
Change, improve, should be included within protection domain of the present utility model.
Claims (4)
1. sewage treatment plants exhaust-gas treatment integration apparatus, it is characterised in that including nozzle barrel (1), catalyst liberation port
(2), catalyst transfer tube (3), reative cell (4), gas inlet pipeline (5), tower body (6), catalyst liquid locker room (8) and urge
Agent power set (9), blower fan (10), the tower body (6) are cylindrical, are cavity inside tower body (6), and its top is the type of falling bucket
Pipeline；Described gas inlet pipeline (5) one end is connected with the type of falling bucket pipeline, and its other end is connected with blower fan (10)；The nozzle
Cylinder (1) is cylindrical, and circular opening is provided with its barrel, and nozzle barrel (1) is vertically placed at tower body (6) internal axis；It is described
Catalyst liberation port (2) is arranged on catalyst transfer tube (3) tube wall, and catalyst transfer tube (3) is placed in nozzle barrel (1) inwall
On, catalyst liberation port (2) is corresponding with the position of the circular opening of nozzle barrel (1)；The catalyst liquid locker room (8) is
Cuboid, it is cavity that it is internal, and tower body (6) lower end is arranged on catalyst liquid locker room (8) upper surface, the catalyst power
Device (9) is arranged on catalyst liquid locker room (8) upper surface, and the reative cell (4) is nozzle barrel (1) outer surface and tower body
(6) cavity formed between inner surface.
2. sewage treatment plants exhaust-gas treatment integration apparatus according to claim 1, it is characterised in that the nozzle
The sealing of cylinder (1) top.
3. sewage treatment plants exhaust-gas treatment integration apparatus according to claim 1, it is characterised in that also including electricity
Control cabinet (11), the electrical control cubicles are arranged near blower fan (10), and electrical control cubicles (11) are for controlling the switch and rotating speed of blower fan (10).
4. sewage treatment plants exhaust-gas treatment integration apparatus according to claim 1, it is characterised in that also including light
Source (7), the light source (7) is arranged on nozzle barrel (1) outer surface, light source (7) number at least four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621419622.9U CN206295812U (en) | 2016-12-21 | 2016-12-21 | Sewage treatment plants exhaust-gas treatment integration apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621419622.9U CN206295812U (en) | 2016-12-21 | 2016-12-21 | Sewage treatment plants exhaust-gas treatment integration apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206295812U true CN206295812U (en) | 2017-07-04 |
Family
ID=59204262
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621419622.9U Expired - Fee Related CN206295812U (en) | 2016-12-21 | 2016-12-21 | Sewage treatment plants exhaust-gas treatment integration apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206295812U (en) |
-
2016
- 2016-12-21 CN CN201621419622.9U patent/CN206295812U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170704 Termination date: 20201221 |