CN206295807U - Soil waste gas is in situ to administer cleaning equipment - Google Patents
Soil waste gas is in situ to administer cleaning equipment Download PDFInfo
- Publication number
- CN206295807U CN206295807U CN201621412477.1U CN201621412477U CN206295807U CN 206295807 U CN206295807 U CN 206295807U CN 201621412477 U CN201621412477 U CN 201621412477U CN 206295807 U CN206295807 U CN 206295807U
- Authority
- CN
- China
- Prior art keywords
- waste gas
- catalyst
- transfer tube
- tower body
- soil
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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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- Processing Of Solid Wastes (AREA)
- Fire-Extinguishing Compositions (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses soil waste gas improvement cleaning equipment in situ, including nozzle barrel, catalyst liberation port, catalyst transfer tube, reative cell, waste gas inlet, tower body, catalyst liquid locker room, catalyst power set, waste gas transfer tube and exhaust gas pressure nozzle, the tower body is cylindrical, inside is cavity, the waste gas inlet is arranged on the side wall top of tower body, waste gas transfer tube is connected with waste gas inlet port, waste gas transfer tube is arranged on tower body inner surface, and exhaust gas pressure nozzle is arranged at waste gas transmission tube wall；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 improves the mixability of catalyst and soil waste gas, makes catalyst more uniform with the reaction of soil waste gas, improves the utilization rate of catalyst, effectively reduces catalyst and goes use cost.
Description
Technical field
The utility model is related to cleaning equipment, and in particular to soil waste gas is in situ to administer cleaning equipment.
Background technology
Soil exhaust gas source is divided into natural origin and artificial source.Natural origin is included in immobilising Hu Gou marshes, various
Methyl sulphur, methyl mercaptan that pasture and water, algae catabolism are produced etc.；Spoil and the corrupt sulphur for decomposing to give off such as plant debris
Change the corruptibility foul smell such as hydrogen, ammonia.One process of the development experience of soil waste gas Prevention Technique, progressively sends out from initial WATER-WASHING METHOD
Open up microbial method, active carbon adsorption, the photocatalytic degradation method to today.Industrialized production pursues mechanization production, automation
Control, but be there is also some problems using the purifying column of catalyst in the prior art, including catalyst mixes with soil waste gas
Insufficient to cause reaction 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 reaction uneven with soil waste gas undercompounding
It is even, it is therefore intended that to provide soil waste gas the mixability administered cleaning equipment, improve catalyst and soil waste gas in situ, make catalysis
Agent is more uniform with the reaction of soil 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：
Soil waste gas is in situ to administer cleaning equipment, including nozzle barrel, catalyst liberation port, catalyst transfer tube, reative cell,
Waste gas inlet, tower body, catalyst liquid locker room, catalyst power set, waste gas transfer tube and exhaust gas pressure nozzle, it is described
Tower body is cylindrical, and inside is cavity, and the waste gas inlet is arranged on the side wall top of tower body, and waste gas transfer tube enters with waste gas
Entrance is connected, and waste gas transfer tube is arranged on tower body inner surface, and exhaust gas pressure nozzle is arranged at waste gas transmission tube wall；It is described
Nozzle barrel is cylindrical, and circular opening is provided with its barrel, and nozzle barrel is vertically placed at tower body internal axis；The catalyst
Liberation port be arranged on catalyst transmission tube wall on, catalyst transfer tube is placed on nozzle barrel inwall, catalyst liberation port with
The position of the circular opening of nozzle barrel is corresponding；The catalyst liquid locker room is cuboid, and it is cavity that it is internal, under tower body
End is arranged on catalyst liquid locker room upper surface, and the catalyst power set are arranged on catalyst liquid locker room upper table
Face, the reative cell is the cavity formed between nozzle tube outer surface and tower body inner surface.Waste gas inlet enters soil waste gas
Enter waste gas transfer tube, the exhaust gas pressure nozzle that waste gas transmission tube wall is set makes soil waste gas enter reative cell under high pressure, has
Effect promotes the mixed uniformly degree of soil waste gas and catalyst, and catalyst power set make urging for catalyst liquid locker room
Agent enters nozzle barrel by catalyst transfer tube, under pressure catalyst by the hole on nozzle barrel barrel be atomized into
Enter in reative cell, soil waste gas mixes with catalyst in reative cell, play the effect that catalyst clears up soil waste gas.
Further, waste gas inlet at least 4, and it is evenly distributed on tower body surrounding.Waste gas inlet is arranged on tower
Body one week, can improve the processing speed of soil waste gas.
Further, the radical of waste gas transfer tube and the number of waste gas inlet are identical, and waste gas transfer tube is vertically arranged in
Tower body inner surface.
Further, the number of exhaust gas pressure nozzle is at least 4, and equidistantly distributed transmits tube wall in waste gas.
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 soil waste gas.
Further, soil waste gas is in situ administers cleaning equipment, and also including light source, the light source is arranged on nozzle barrel outside
Surface, number of light sources at least four.Using light source, the reaction to catalyst and soil waste gas plays the effect of catalysis, makes soil
The treatment effeciency of earth 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, and soil waste gas sprays also by waste gas transfer tube and exhaust gas pressure
Mouth rapidly enters reative cell, and further mixing is abundant to make catalyst and soil waste gas, improves the mixing of catalyst and soil waste gas
Degree, makes catalyst more uniform with the reaction of soil waste gas, improves the utilization rate of catalyst, effectively reduces catalyst and goes to 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, 10- waste gas transfer tubes, 11- exhaust gas pressure nozzles.
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, soil waste gas is in situ to administer cleaning equipment, including nozzle barrel 1, catalyst liberation port 2, catalyst are passed
Defeated pipe 3, reative cell 4, waste gas inlet 5, tower body 6, catalyst liquid locker room 8, catalyst power set 9, waste gas transfer tube
10 and exhaust gas pressure nozzle 11, the tower body 6 is cylindrical, and inside is cavity, and the waste gas inlet 5 is arranged on tower body 6
Side wall top, waste gas transfer tube 10 is connected with waste gas inlet port 5, and waste gas transfer tube 10 is arranged on the inner surface of tower body 6, waste gas pressure
Power nozzle 11 is arranged at the tube wall of waste gas transfer tube 10；The nozzle barrel 1 is cylindrical, and circular opening is provided with its barrel,
Nozzle barrel 1 is vertically placed at the internal axis of tower body 6；The catalyst liberation port 2 is arranged on the tube wall of catalyst transfer tube 3, is urged
Agent transfer tube 3 is placed on the inwall of nozzle barrel 1, and 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, and it is cavity that it is internal, and the lower end of tower body 6 is arranged in catalyst liquid locker room 8
Surface, the catalyst power set 9 are arranged on the upper surface of catalyst liquid locker room 8, and the reative cell 4 is outside nozzle barrel 1
The cavity formed between surface and the inner surface of tower body 6.Waste gas inlet 5 at least 4, and it is evenly distributed on the surrounding of tower body 6.It is useless
The radical of gas transfer tube 10 is identical with the number of waste gas inlet 10, and waste gas transfer tube 10 is vertically arranged in the inner surface of tower body 6.It is useless
The number of atmospheric pressure nozzle 11 is at least 4, and equidistantly distributed is in the tube wall of waste gas transfer tube 10.Catalyst transfer tube 3 is at least
There is one, its lower ending opening and be placed directly within the middle and lower part of catalyst liquid locker room 8, end closure is placed in the upper end of nozzle barrel 1 thereon
Medial surface.Soil waste gas is in situ to administer cleaning equipment, and also including light source 7, the light source 7 is arranged on the outer surface of nozzle barrel 1, light
The number of 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 the upper end side surface of tower body 6 is evenly distributed on, waste gas transfer tube 10 is consistent with the number of waste gas inlet 5, waste gas transmission
Pipe 10 is provided with 22, and exhaust gas pressure nozzle 11 is evenly arranged with its each tube wall of waste gas transfer tube 10, makes soil waste gas
Reative cell 4 is rapidly entered under the effect of the pressure；Less than the diameter of tower body 6, the inner side of nozzle barrel 1 is provided with 6 to the diameter of nozzle barrel 1
Catalyst transfer tube 3, homogeneous vertical is distributed in the inner surface of nozzle barrel 1, the catalyst liberation port 2 and nozzle of catalyst transfer tube 3
Circular opening on 1 barrel of cylinder matches, and each catalyst transfer tube 3 is provided with 14 catalyst liberation ports 2, and catalyst
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 spray
On mouth 1 outer wall of cylinder, each row are vertical 5, and its spacing is equal；Catalyst power set 9 use drip pump and increasing
The combination unit of depressor, liquid catalyst is sent into catalyst from catalyst liquid locker room 8 using drip pump first
Catalyst transfer tube 3, is reused booster and is sprayed liquid catalyst by the atomization of catalyst liberation port 2 under the effect of the pressure
Mouth enters reative cell 4, makes soil waste gas that reaction is sufficiently mixed under illumination condition with catalyst, and that improves catalyst uses effect
Rate, 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 (6)
1. soil waste gas is in situ administers cleaning equipment, it is characterised in that including nozzle barrel (1), catalyst liberation port (2), catalysis
Agent transfer tube (3), reative cell (4), waste gas inlet (5), tower body (6), catalyst liquid locker room (8), catalyst power dress
(9), waste gas transfer tube (10) and exhaust gas pressure nozzle (11) are put, the tower body (6) is cylindrical, inside is cavity, it is described useless
Gas air inlet (5) is arranged on the side wall top of tower body (6), and waste gas transfer tube (10) is connected with waste gas inlet port (5), waste gas transmission
Pipe (10) is arranged on tower body (6) inner surface, and exhaust gas pressure nozzle (11) is arranged at waste gas transfer tube (10) tube wall；The spray
Mouth 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；Institute
State catalyst liberation port (2) to be arranged on catalyst transfer tube (3) tube wall, catalyst transfer tube (3) is placed in nozzle barrel (1)
On wall, 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, and the catalyst is moved
Power apparatus (9) are 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. soil waste gas according to claim 1 is in situ administers cleaning equipment, it is characterised in that the waste gas inlet
(5) at least 4, and it is evenly distributed on tower body (6) surrounding.
3. soil waste gas according to claim 2 is in situ administers cleaning equipment, it is characterised in that the waste gas transfer tube
(10) radical is identical with the number of waste gas inlet (10), and waste gas transfer tube (10) is vertically arranged in tower body (6) inner surface.
4. soil waste gas according to claim 1 is in situ administers cleaning equipment, it is characterised in that the exhaust gas pressure nozzle
(11) number is at least 4, and equidistantly distributed is on waste gas transfer tube (10) tube wall.
5. soil waste gas according to claim 1 is in situ administers cleaning equipment, it is characterised in that the catalyst transfer tube
(3) at least one, its lower ending opening and catalyst liquid locker room (8) middle and lower part is placed directly within, end closure is placed in spray thereon
Mouth cylinder (1) upper end medial surface.
6. soil waste gas according to claim 1 is in situ administers cleaning equipment, it is characterised in that also including light source (7), institute
State light source (7) and be arranged on nozzle barrel (1) outer surface, light source (7) number at least four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621412477.1U CN206295807U (en) | 2016-12-21 | 2016-12-21 | Soil waste gas is in situ to administer cleaning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621412477.1U CN206295807U (en) | 2016-12-21 | 2016-12-21 | Soil waste gas is in situ to administer cleaning equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206295807U true CN206295807U (en) | 2017-07-04 |
Family
ID=59214852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621412477.1U Expired - Fee Related CN206295807U (en) | 2016-12-21 | 2016-12-21 | Soil waste gas is in situ to administer cleaning equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206295807U (en) |
-
2016
- 2016-12-21 CN CN201621412477.1U patent/CN206295807U/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 |