CN206295817U - Stench catalyzing, oxidizing and purifying tower - Google Patents
Stench catalyzing, oxidizing and purifying tower Download PDFInfo
- Publication number
- CN206295817U CN206295817U CN201621414020.4U CN201621414020U CN206295817U CN 206295817 U CN206295817 U CN 206295817U CN 201621414020 U CN201621414020 U CN 201621414020U CN 206295817 U CN206295817 U CN 206295817U
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- CN
- China
- Prior art keywords
- catalyst
- stench
- tower body
- nozzle barrel
- barrel
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- 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 stench catalyzing, oxidizing and purifying tower, including nozzle barrel, catalyst liberation port, catalyst transfer tube, reative cell, waste gas inlet, tower body, catalyst liquid locker room and catalyst power set, tower body is cylindrical, inside is cavity, and waste gas inlet is arranged on the side wall top of tower body；Nozzle barrel is cylindrical, and circular opening is provided with its barrel, and nozzle barrel is vertically placed at tower body internal axis；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 stench after catalyst atomization, improve the mixability of catalyst and stench, make catalyst more uniform with the reaction of stench, 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 stench catalyzing, oxidizing and purifying tower.
Background technology
Malodor 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 odor prevention technology, 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 stench 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 stench undercompounding
Be that stench catalyzing, oxidizing and purifying tower is provided, improve the mixability of catalyst and stench, make the reaction of catalyst and stench
It is more uniform, the utilization rate of catalyst is improved, effectively reduce catalyst and go use cost.
The utility model is achieved through the following technical solutions：
Stench catalyzing, oxidizing and purifying tower, including nozzle barrel, catalyst liberation port, catalyst transfer tube, reative cell, waste gas enter
Gas port, tower body, catalyst liquid locker room and catalyst power set, the tower body are cylindrical, and inside is cavity, described useless
Gas air inlet is arranged on the side wall top of tower body；The nozzle barrel is cylindrical, and circular opening, nozzle barrel are provided with its barrel
It is vertically placed at tower body internal axis；The catalyst liberation port is arranged on catalyst transmission tube wall, catalyst transfer tube
It is placed on nozzle barrel inwall, catalyst liberation port is corresponding with the position of the circular opening of nozzle barrel；The catalyst liquid
Locker room is cuboid, and it is cavity that it is internal, and tower body lower end is arranged on catalyst liquid locker room upper surface, and the catalyst is moved
Power apparatus are arranged on catalyst liquid locker room upper surface, and the reative cell is shape between nozzle tube outer surface and tower body inner surface
Into cavity.Waste gas inlet makes stench enter reative cell, and catalyst power set make the catalyst of catalyst liquid locker room
Nozzle barrel is entered by catalyst transfer tube, catalyst is atomized by the hole on nozzle barrel barrel and enters anti-under pressure
Should be indoor, stench mixes with catalyst in reative cell, plays the effect that catalyst clears up stench.
Further, waste gas inlet at least 4, and it is evenly distributed on the circle of tower body one.Waste gas inlet is arranged on tower
Body one week, can improve the processing speed of stench.
Further, catalyst transfer tube at least one, its lower ending opening and is placed directly within catalyst liquid locker room
Middle and lower part, thereon end closure be placed in nozzle barrel upper end medial surface.The length of catalyst transfer tube is differed not with the length of nozzle barrel
It is many, the space in reative cell can be more made full use of, improve the efficiency of catalyst treatment stench.
Further, stench catalyzing, oxidizing and purifying tower, also including light source, the light source is arranged on nozzle barrel outer surface,
Number of light sources at least four.Using light source, the reaction to catalyst and stench plays the effect of catalysis, imitates the treatment of stench
Rate 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 be more fully mixed with stench after catalyst atomization, improve the mixability of catalyst and stench, make to urge
Agent is more uniform with the reaction of stench, improves the utilization rate of catalyst, effectively reduces catalyst and 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- waste gas inlets, 6- tower bodies,
7- light sources, 8- catalyst liquids locker room, 9- catalyst power set.
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, stench catalyzing, oxidizing and purifying tower, including nozzle barrel 1, catalyst liberation port 2, catalyst transfer tube 3,
Reative cell 4, waste gas inlet 5, tower body 6, catalyst liquid locker room 8 and catalyst power set 9, the tower body 6 are in cylinder
Shape, inside is cavity, and the waste gas inlet 5 is arranged on the side wall top of tower body 6；The nozzle barrel 1 is cylindrical, its barrel
On be provided with 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
On the tube wall of transfer tube 3, catalyst transfer tube 3 is placed on the inwall of nozzle barrel 1, the circular port of catalyst liberation port 2 and nozzle barrel 1
The position in hole is 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 catalysis
The upper surface of agent liquid locker room 8, the catalyst power set 9 are arranged on the upper surface of catalyst liquid locker room 8, the reaction
Room 4 is the cavity formed between the outer surface of nozzle barrel 1 and the inner surface of tower body 6.Waste gas inlet 5 at least 4, and be uniformly distributed
Enclosed in tower body 6 one.Catalyst transfer tube 3 at least one, its lower ending opening and under being placed directly within catalyst liquid locker room 8
Portion, thereon end closure be placed in the upper end medial surface of nozzle barrel 1.Stench catalyzing, oxidizing and purifying tower, also including light source 7, the light source 7 sets
Put in the outer surface of nozzle barrel 1, the number of light source 7 at least four.
In the present embodiment, waste gas inlet 5 is provided with 22, and waste gas inlet is circle, and its circle is in same level
On face, and it is evenly distributed on the upper end side surface of tower body 6；Less than the diameter of tower body 6, the inner side of nozzle barrel 1 is provided with the diameter of nozzle barrel 1
6 catalyst transfer tubes 3, homogeneous vertical is distributed in the inner surface of nozzle barrel 1, catalyst liberation port 2 and the spray of catalyst transfer tube 3
Circular opening on mouth 1 barrel of cylinder matches, and each catalyst transfer tube 3 is provided with 14 catalyst liberation ports 2, and catalysis
Agent liberation port 2 uses atomizer by catalyst feeding reative cell 4, and light source 7 is provided with 5 row, and each column is evenly distributed on
On the outer wall of nozzle barrel 1, each row are vertical 5, and its spacing is equal；Catalyst power set 9 use drip pump and
The combination unit of booster, liquid catalyst is sent catalyst from catalyst liquid locker room 8 using drip pump first
Enter catalyst transfer tube 3, reuse booster by liquid catalyst under the effect of the pressure by the atomization of catalyst liberation port 2
Nozzle enters reative cell 4, makes stench that reaction is sufficiently mixed under illumination condition with catalyst, improves the service efficiency of catalyst,
Reduces cost.
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. stench catalyzing, oxidizing and purifying tower, it is characterised in that including nozzle barrel (1), catalyst liberation port (2), catalyst transmission
Pipe (3), reative cell (4), waste gas inlet (5), tower body (6), catalyst liquid locker room (8) and catalyst power set (9),
The tower body (6) is cylindrical, and inside is cavity, and the waste gas inlet (5) is arranged on the side wall top of tower body (6)；It is described
Nozzle barrel (1) is cylindrical, and circular opening is provided with its barrel, and nozzle barrel (1) is vertically placed at tower body (6) internal axis；
The catalyst liberation port (2) is arranged on catalyst transfer tube (3) tube wall, and catalyst transfer tube (3) is placed in nozzle barrel (1)
On inwall, catalyst liberation port (2) is corresponding with the position of the circular opening of nozzle barrel (1)；The catalyst liquid locker room
(8) it 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 catalysis
Agent power set (9) are arranged on catalyst liquid locker room (8) upper surface, the reative cell (4) be nozzle barrel (1) outer surface with
The cavity formed between tower body (6) inner surface.
2. stench catalyzing, oxidizing and purifying tower according to claim 1, it is characterised in that the waste gas inlet (5) is at least
There are 4, and be evenly distributed on the circle of tower body (6).
3. stench catalyzing, oxidizing and purifying tower according to claim 1, it is characterised in that the catalyst transfer tube (3) is extremely
Rare one, its lower ending opening and catalyst liquid locker room (8) middle and lower part is placed directly within, end closure is placed in nozzle barrel thereon
(1) upper end medial surface.
4. stench catalyzing, oxidizing and purifying tower according to claim 1, it is characterised in that also including light source (7), the light source
(7) nozzle barrel (1) outer surface, light source (7) number at least four are arranged on.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621414020.4U CN206295817U (en) | 2016-12-21 | 2016-12-21 | Stench catalyzing, oxidizing and purifying tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621414020.4U CN206295817U (en) | 2016-12-21 | 2016-12-21 | Stench catalyzing, oxidizing and purifying tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206295817U true CN206295817U (en) | 2017-07-04 |
Family
ID=59213866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621414020.4U Expired - Fee Related CN206295817U (en) | 2016-12-21 | 2016-12-21 | Stench catalyzing, oxidizing and purifying tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206295817U (en) |
-
2016
- 2016-12-21 CN CN201621414020.4U patent/CN206295817U/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 |
Granted publication date: 20170704 Termination date: 20201221 |
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| CF01 | Termination of patent right due to non-payment of annual fee |