CN208361942U - A kind of industrial wastewater light-catalyzed reaction processing equipment - Google Patents
A kind of industrial wastewater light-catalyzed reaction processing equipment Download PDFInfo
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- CN208361942U CN208361942U CN201820803410.3U CN201820803410U CN208361942U CN 208361942 U CN208361942 U CN 208361942U CN 201820803410 U CN201820803410 U CN 201820803410U CN 208361942 U CN208361942 U CN 208361942U
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- back taper
- reaction
- tank body
- shunting
- industrial wastewater
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Abstract
The utility model discloses a kind of industrial wastewater light-catalyzed reaction processing equipments, using the structure that reaction tray is fixedly installed in tank body, tank body is divided into reaction zone and memory block by reaction tray, the side gap uniformly distributed by reaction tray edge again, reaction zone is connected to memory block, industrial wastewater is sprayed onto shunting back taper by water inlet pipe, it is mixed with the air that back taper sprays is shunted, photochemical catalyst hollow sphere on simultaneous reactions disk is under the agitating of the impeller driven by servo motor, constantly skimming over waste water mixes with air region, and the ultraviolet radiator in inner tank wall is also irradiated to waste water just and mixes with air region, complete light-catalyzed reaction, the impeller of rotation also acts as the effect of circulation stirring waste water simultaneously, after air rises to the reaction zone water surface or more from shunting back taper, so that the water surface for shunting the region around back taper in reaction tray also can Light-catalyzed reaction is carried out under the action of ultraviolet radiator, improves reflection efficiency.
Description
Technical field
The utility model belong to Industrial Wastewater Treatment instrument technical field more particularly to a kind of industrial wastewater photocatalysis it is anti-
Answer processing equipment.
Background technique
Industrial wastewater includes production waste water, production waste and cooling water, refer to the waste water generated in industrial processes and
Waste liquid, wherein containing the pollution generated in industrial production materials, intermediate product, byproduct and the production process outflowed with water
Object.Industrial wastewater is many kinds of, complicated component.Therefore it generally requires dedicated for the setting of industrial wastewater caused by specific plant area
Sewage treatment equipment.And due to light-catalyzed reaction it is easy to operate, low energy consumption, without secondary pollution, high-efficient the advantages that, generally exist
Light-catalyzed reaction processing equipment is paid the utmost attention to when handling industrial wastewater.But existing light-catalyzed reaction processing equipment is existing
Main problem is that photochemical catalyst generally uses reticular structure, by waste water by photochemical catalyst net, but due to water body flow, so that urging
Change reaction to be not thorough, efficiency is lower.
Utility model content
For the above existing problem, the utility model provides a kind of industrial wastewater light-catalyzed reaction processing equipment,
Using the structure that reaction tray is fixedly installed in tank body, tank body is divided by reaction zone and memory block by reaction tray, then by anti-
The uniformly distributed side gap in edge should be coiled, reaction zone is connected to memory block, industrial wastewater is sprayed onto shunting back taper by water inlet pipe,
It is mixed with the air that back taper sprays is shunted, the photochemical catalyst hollow sphere on simultaneous reactions disk is in the impeller driven by servo motor
It agitates down, constantly skims over waste water and mix with air region, and the ultraviolet radiator in inner tank wall is also irradiated to waste water and sky just
Light-catalyzed reaction is completed in gas Mixed Zone, while the impeller rotated also acts as the effect of circulation stirring waste water, in air from shunting
After back taper rises to the reaction zone water surface or more, so that the water surface for shunting the region around back taper in reaction tray also can be in ultraviolet light
Light-catalyzed reaction is carried out under the action of irradiation light, improves reflection efficiency, while light-catalyzed reaction carries out, keeps inflow
Do not had side gap to be not less than side gap lower end so that the liquid level in reaction tray is in always, so that treated water body and anti-yet
Air after answering area to react can drain down into memory block from side gap, and the air after reaction is arranged from the exhaust pipe of inner tank wall
Out, treated, and water body is discharged from discharge pipe, to complete entire industrial wastewater light-catalyzed reaction treatment process.
The technical solution of the utility model is:
The utility model provides a kind of industrial wastewater light-catalyzed reaction processing equipment, including cover, tank body, companion flange,
Water inlet pipe and drainpipe, the tank body is placed vertically and lower end center is fixedly installed the drainpipe, the upper end of the tank body
It is fixedly installed the companion flange, the upper end of the tank body is connected in a manner of bolted by the companion flange
Cover is stated, the water inlet pipe is provided on the cover, the water inlet pipe runs through the center of the cover vertically and lower end is protruded into
In the tank body, several motor racks are uniformly arranged around cover on the cover, the upper end of the motor rack is from top to bottom
It is embedded with servo motor, the main shaft of the servo motor downward and is connected with retarder, and the retarder is embedded in the motor
In frame and lower end is connected with shaft, and the shaft runs through the cover from the upper end of the cover and protrudes into the tank body vertically
Interior, the lower end of the shaft is fixedly installed impeller, and impeller is made and is nested in by pin connection using transparent tempered glass
The lower end of shaft；
Reaction tray is fixedly installed in the tank body, the tank interior is divided into reaction zone and storage by the reaction tray
Two parts above and below area；
The upper surface center of trying to get to the heart of a matter of the reaction tray is the shunting back taper to raise upward, and the shunting back taper is tapered and bores
Nose part protrudes into the lower end of the water inlet pipe, and the lower end of the water inlet pipe is not contacted with the shunting back taper；
The lower end for shunting back taper is fixedly installed gas supply funnel, the gas supply funnel be in back taper and with the shunting
Storage of higher pressures air cavity is formed between back taper, the upper surface for shunting back taper has been uniformly arranged several and has been connected to the storage of higher pressures
The lower end center of the fumarole of air cavity and the reaction zone, the gas supply funnel is fixedly installed high-pressure air feed pipe, the high pressure
Be provided with check valve on the part of the gas supply funnel on air supply pipe, the check valve make the gas supply funnel unidirectionally to
The storage of higher pressures air cavity gas supply, the high-pressure air feed pipe are pierced by the tank body far from the end of the gas supply funnel；
The upper surface of trying to get to the heart of a matter of the reaction tray, which is evenly distributed with laying around the shunting back taper, several photochemical catalyst hollow spheres；
The lower end of the impeller be in it is described shunting back taper and the reaction tray disk along between and not with the shunting
Back taper and the disk of the reaction tray are not also contacted along contact with the photochemical catalyst hollow sphere；
The disk of the reaction tray is provided through several around the reaction tray up and down along the junction with the tank body
The equally distributed side gap of axis, the fixed capping of the side gap have strainer, be arranged the side gap make the reaction zone and
Memory block connection, and the strainer is set then limits the photochemical catalyst reaction sphere and rolled in the reaction zone；
Exhaust pipe is fixedly installed on the tank wall, the external world is connected to by the exhaust pipe with the memory block；
Several ultraviolet radiator have been uniformly arranged in the inner tank wall in the reaction zone, the ultraviolet radiator
Axis is to the extended line for shunting back taper by the upper wall surface for shunting back taper.
Further, the diameter of the photochemical catalyst hollow sphere is 1mm-10mm, and the photochemical catalyst hollow sphere is straight
Diameter is all larger than the mesh diameter of the strainer and the diameter of the fumarole.
Further, the spacing between the lower end of the impeller and the photochemical catalyst hollow sphere is 20mm-60mm.
Further, the high-pressure air feed pipe is connected with high-pressure air feed device, institute far from the end outside the tank body
State the oxygen that high-pressure air feed device supplies photochemical catalytic oxidation by the high-pressure air feed pipe to the reaction zone.
Further, the axis of the water inlet pipe, the axis of the shaft and the side gap that is closed on the shaft
Side it is in the same vertical plane.
The utility model is allowed to specific positive beneficial effect compared with prior art due to using above-mentioned technology are as follows:
1, in the utility model, the impeller of rotation plays the role of circulation stirring waste water, rises in air from back taper is shunted
After more than to the reaction zone water surface, so that the water surface for shunting the region around back taper in reaction tray also can be in ultraviolet radiator
Effect is lower to carry out light-catalyzed reaction, improves reflection efficiency.
2, the utility model, the side of the axis of water inlet pipe, the axis of shaft and the side gap closed on shaft are in same
On one vertical plane so that the intracorporal impeller of tank rotates counterclockwise in the case where overlooking visual direction, the water body in reaction tray under impeller agitation,
The first drive in reaction tray is chivalrous to rotate a circle around impeller, then enters from the side gap closed on impeller from reaction zone downwards and deposits
Storage area increases light-catalyzed reaction duration, and industrial wastewater is enabled sufficiently to carry out light-catalyzed reaction.
3, in the utility model, several ultraviolet radiator, ultraviolet light have been uniformly arranged in the inner tank wall in reaction zone
The axis of lamp, by the upper wall surface of shunting back taper, enables ultraviolet radiator to guarantee to propose reaction tray to the extended line for shunting back taper
For sufficient energy.
4, in the utility model, the diameter of photochemical catalyst hollow sphere is 1mm-10mm, and the diameter of photochemical catalyst hollow sphere
It is all larger than the mesh diameter of strainer and the diameter of fumarole, photochemical catalyst hollow sphere is avoided to enter memory block from reaction zone, or
Entering high pressure from reaction zone.
5, in the utility model, the spacing between the lower end and photochemical catalyst hollow sphere of impeller is 20mm-60mm, avoids light
It is excessively fierce that catalyst hollow sphere moves under the agitating of impeller, causes turning for the hollow ball wear of photochemical catalyst, especially impeller
Speed should be controlled in 20RPM-60RPM.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the top view of the utility model；
Fig. 3 is the cross-sectional view in Fig. 2 at A-A；
Fig. 4 is the cross-sectional view in Fig. 3 at B-B.
In figure: 1- water inlet pipe, 2- servo motor, 3- motor rack, 4- retarder, 5- cover, 6- companion flange, 7- exhaust
Pipe, 8- tank body, 9- high-pressure air feed pipe, 10- drainpipe, 11- check valve, 12- supply funnel, 13- photochemical catalyst hollow sphere, 14-
Reaction tray, 15- strainer, the side 16- gap, 17- impeller, 18- shunt back taper, 19- shaft, 20- ultraviolet radiator.
Specific embodiment
In order to clarify the technical characteristics of the invention, below by specific embodiment, and its attached drawing is combined, to this reality
It is described in detail with novel.Following disclosure provides many different embodiments or example is used to realize the utility model
Different structure.In order to simplify the disclosure of the utility model, hereinafter the component of specific examples and setting are described.In addition,
The utility model can in different examples repeat reference numerals and/or letter.This repetition is for simplified and clear mesh
, the relationship between discussed various embodiments and/or setting itself is not indicated.It should be noted that illustrated in the accompanying drawings
Component is not drawn necessarily to scale.The description to known assemblies and treatment technology and process is omitted to avoid not in the utility model
Necessarily limit the utility model.
In addition, in the description of the present invention, it should be noted that term " center ", "center", "upper", "lower",
The orientation or positional relationship of the instructions such as "left", "right", "vertical", "horizontal", "inner", "outside" be orientation based on the figure or
Positional relationship is merely for convenience of describing the present invention and simplifying the description, rather than the device or member of indication or suggestion meaning
Part must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
In addition, term " first ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
Embodiment 1, as shown in attached drawing 1- attached drawing 4, the utility model provides a kind of industrial wastewater light-catalyzed reaction processing and sets
It is standby, including cover 5, tank body 8, companion flange 6, water inlet pipe 1 and drainpipe 10, tank body 8 is placed vertically and the fixation of lower end center is set
It is equipped with drainpipe 10, the upper end of tank body 8 is fixedly installed companion flange 6, and the upper end of tank body 8 is connected by companion flange 6 with bolt
The mode connect is connected with cover 5, water inlet pipe 1 is provided on cover 5, water inlet pipe 1 runs through the center of cover 5 vertically and lower end is protruded into
In tank body 8, several motor racks 3 are uniformly arranged around cover 5 on cover 5, the upper end of motor rack 3 is embedded with from top to bottom to be watched
Take motor 2, the main shaft of servo motor 2 downward and is connected with retarder 4, and retarder 4 is embedded in motor rack 3 and lower end is connected with
Shaft 19, shaft 19 through cover 5 and protrude into tank body 8 vertically from the upper end of cover 5, and the lower end of shaft 19 is fixedly installed fan
Wheel 17；
Reaction tray 14 is fixedly installed in tank body 8, reaction tray 14 will be divided into reaction zone and memory block or more inside tank body 8
Two parts；
The upper surface center of trying to get to the heart of a matter of reaction tray 14 is the shunting back taper 18 to raise upward, shunts that back taper 18 is tapered and cone
The lower end of water inlet pipe 1 is partially protruded into, the lower end of water inlet pipe 1 is not contacted with shunting back taper 18；
Shunt back taper 18 lower end be fixedly installed gas supply funnel 12, gas supply funnel 12 in back taper and with shunt back taper 18
Between form storage of higher pressures air cavity, the upper surface for shunting back taper 18 has been uniformly arranged several connection storage of higher pressures air cavitys and reaction
The fumarole in area, the lower end center of gas supply funnel 12 are fixedly installed high-pressure air feed pipe 9, leak on high-pressure air feed pipe 9 close to gas supply
Check valve 11 is provided on the part of bucket 12, check valve 11 to supply funnel 12 unidirectionally to storage of higher pressures air cavity gas supply, high pressure
Air supply pipe 9 is pierced by tank body 8 far from the end of gas supply funnel 12；
The upper surface of trying to get to the heart of a matter of reaction tray 14, which is evenly distributed with laying around shunting back taper 18, several photochemical catalyst hollow spheres 13；
The lower end of impeller 17 is in the disk for shunting back taper 18 and reaction tray 14 between and not with shunting back taper 18 and instead
The disk edge contact that 14 should be coiled, does not also contact with photochemical catalyst hollow sphere 13；
It is uniform around 14 axis of reaction tray that the disk of reaction tray 14 is provided through several above and below the junction with tank body 8
The side gap 16 of distribution；The fixed capping of side gap 16 has strainer 15, and setting side gap 16 is connected to reaction zone with memory block, and
Setting strainer 15 then limits photochemical catalyst reaction sphere and rolls in reaction zone；
Exhaust pipe 7 is fixedly installed on 8 side wall of tank body, the external world is connected to by exhaust pipe 7 with memory block；
Be uniformly arranged several ultraviolet radiator 20 on 8 inner wall of tank body in reaction zone, the axis of ultraviolet radiator 20 to
The extended line of back taper 18 is shunted by the upper wall surface of shunting back taper 18, ultraviolet radiator 20 is enabled to guarantee to provide reaction tray 14
Sufficient energy.
The diameter of photochemical catalyst hollow sphere 13 is 1mm-10mm, and the diameter of photochemical catalyst hollow sphere 13 is all larger than strainer 15
Mesh diameter and fumarole diameter, avoid photochemical catalyst hollow sphere 13 from entering memory block from reaction zone, or from reaction
Area enters high pressure.
Spacing between the lower end and photochemical catalyst hollow sphere 13 of impeller 17 is 20mm-60mm, avoids photochemical catalyst hollow
It is excessively fierce that ball 13 moves under the agitating of impeller 17, causes photochemical catalyst hollow sphere 13 to wear, especially the revolving speed of impeller 17
It should control in 20RPM-60RPM.
It will by reaction tray 14 using the structure that reaction tray 14 is fixedly installed in tank body 8 by using above-mentioned technical proposal
Tank body 8 is divided into reaction zone and memory block, then the side gap 16 uniformly distributed by 14 edge of reaction tray, by reaction zone and memory block
Connection, industrial wastewater are sprayed by water inlet pipe 1 and shunt back taper 18, are mixed with the air that back taper 18 sprays is shunted, simultaneous reactions
Photochemical catalyst hollow sphere 13 on disk 14 constantly skims over waste water and air under the agitating of the impeller 17 driven by servo motor 2
Mixed Zone, and the ultraviolet radiator 20 on 8 inner wall of tank body is also irradiated to waste water just and mixes with air region, and it is anti-to complete photocatalysis
The impeller 17 answered, while rotated also acts as the effect of circulation stirring waste water, rises to reaction zone water from back taper 18 is shunted in air
After more than face, so that the water surface for shunting the region around back taper 18 in reaction tray 14 also can be under the action of ultraviolet radiator
Light-catalyzed reaction is carried out, reflection efficiency is improved, while light-catalyzed reaction carries out, inflow is kept to make in reaction tray 14
Liquid level be in do not had side gap 16 also not less than 16 lower end of side gap always so that treated water body and reaction zone reaction
Air afterwards can drain down into memory block from side gap 16, and the air after reaction is discharged from the exhaust pipe 7 of 8 inner wall of tank body, place
Water body after reason is discharged from discharge pipe, to complete entire industrial wastewater light-catalyzed reaction treatment process.
Embodiment 2 axis of water inlet pipe 1, the axis of shaft 19 and is faced in the structure basis of embodiment 1 with shaft 19
The side of close side gap 16 is in the same vertical plane.
By using above-mentioned technical proposal, on the basis of embodiment 1, so that the impeller 17 in tank body 8 overlooks visual direction
Lower rotation counterclockwise, so that the water body in reaction tray 14 is under the agitation of impeller 17, it is first chivalrous around impeller in the drive of reaction tray 14
17 rotate a circle, and then enter memory block from reaction zone downwards from the side gap 16 closed on impeller 17, it is anti-to increase photocatalysis
Duration is answered, industrial wastewater is enabled sufficiently to carry out light-catalyzed reaction.
In the description of the present invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " company
Connect ", " fixation " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；It can be
Mechanical connection, is also possible to be electrically connected；It can be directly connected, two can also be can be indirectly connected through an intermediary
The interaction relationship of connection or two elements inside element.And the material side used by each components of the utility model
Face can be using spring steel material if the components with the description of " elasticity " term, can also be using rubber material
Matter；If the components with the description of " rigidity " term, can be using steel material, can also be using hard engineering plastic
Expect material.For the ordinary skill in the art, above-mentioned term can be understood in the utility model according to concrete condition
In concrete meaning.
One embodiment of the utility model is described in detail above, but the content is only the utility model
Preferred embodiment should not be considered as limiting the scope of the present invention.It is all to be made according to application scope of the utility model
All the changes and improvements etc., should still belong within the patent covering scope of the utility model.
Claims (5)
1. a kind of industrial wastewater light-catalyzed reaction processing equipment, including cover, tank body, companion flange, water inlet pipe and drainpipe, institute
State that tank body is placed vertically and lower end center is fixedly installed the drainpipe, the upper end of the tank body is fixedly installed the engagement
Flange, the upper end of the tank body are connected with the cover by the companion flange in a manner of bolted, on the cover
It is provided with the water inlet pipe, it is characterised in that: the water inlet pipe runs through the center of the cover vertically and the tank is protruded into lower end
In vivo, several motor racks have been uniformly arranged around cover on the cover, the upper end of the motor rack is embedded with from top to bottom
Servo motor, the main shaft of the servo motor downward and are connected with retarder, the retarder be embedded in the motor rack and
Lower end is connected with shaft, and the shaft through the cover and protrudes into the tank body vertically from the upper end of the cover, described
The lower end of shaft is fixedly installed impeller, and impeller is made and is nested under shaft by pin connection using transparent tempered glass
End；
Reaction tray is fixedly installed in the tank body, the tank interior is divided on reaction zone and memory block by the reaction tray
Lower two parts；
The upper surface center of trying to get to the heart of a matter of the reaction tray is the shunting back taper to raise upward, and the shunting back taper is tapered and cone tip part
Divide the lower end for protruding into the water inlet pipe, the lower end of the water inlet pipe is not contacted with the shunting back taper；
The lower end for shunting back taper is fixedly installed gas supply funnel, the gas supply funnel be in back taper and with the shunting back taper
Between form storage of higher pressures air cavity, the upper surface for shunting back taper has been uniformly arranged several and has been connected to the storage of higher pressures air cavity
High-pressure air feed pipe, the high-pressure air feed are fixedly installed with the lower end center of the fumarole of the reaction zone, the gas supply funnel
It is provided with check valve on the part of the gas supply funnel on pipe, the check valve makes the gas supply funnel unidirectionally to described
Storage of higher pressures air cavity gas supply, the high-pressure air feed pipe are pierced by the tank body far from the end of the gas supply funnel；
The upper surface of trying to get to the heart of a matter of the reaction tray, which is evenly distributed with laying around the shunting back taper, several photochemical catalyst hollow spheres；
The lower end of the impeller be in it is described shunting back taper and the reaction tray disk along between and not with the shunting back taper
Disk with the reaction tray is not also contacted along contact with the photochemical catalyst hollow sphere；
The disk of the reaction tray is along being provided through several reacts disk axis around described up and down with the junction of the tank body
Equally distributed side gap, the fixed capping of the side gap have strainer, and the side gap is arranged and makes the reaction zone and described
Memory block connection, and the strainer is set then limits the photochemical catalyst reaction sphere and rolled in the reaction zone；
Exhaust pipe is fixedly installed on the tank wall, the external world is connected to by the exhaust pipe with the memory block；
Several ultraviolet radiator, the axis of the ultraviolet radiator have been uniformly arranged in the inner tank wall in the reaction zone
To the extended line for shunting back taper by the upper wall surface for shunting back taper.
2. a kind of industrial wastewater light-catalyzed reaction processing equipment according to claim 1, it is characterised in that: the photocatalysis
The diameter of agent hollow sphere be 1mm-10mm, and the diameter of the photochemical catalyst hollow sphere be all larger than the strainer mesh diameter and
The diameter of the fumarole.
3. a kind of industrial wastewater light-catalyzed reaction processing equipment according to claim 1, it is characterised in that: the impeller
Spacing between lower end and the photochemical catalyst hollow sphere is 20mm-60mm.
4. a kind of industrial wastewater light-catalyzed reaction processing equipment according to claim 1, it is characterised in that: the high pressure supplies
Tracheae is connected with high-pressure air feed device far from the end outside the tank body, and the high-pressure air feed device is supplied by the high pressure
Oxygen of the tracheae to reaction zone supply photochemical catalytic oxidation.
5. a kind of industrial wastewater light-catalyzed reaction processing equipment according to claim 1, it is characterised in that: the water inlet pipe
Axis, the shaft axis and the side gap closed on the shaft side it is in the same vertical plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820803410.3U CN208361942U (en) | 2018-05-28 | 2018-05-28 | A kind of industrial wastewater light-catalyzed reaction processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820803410.3U CN208361942U (en) | 2018-05-28 | 2018-05-28 | A kind of industrial wastewater light-catalyzed reaction processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208361942U true CN208361942U (en) | 2019-01-11 |
Family
ID=64930436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820803410.3U Expired - Fee Related CN208361942U (en) | 2018-05-28 | 2018-05-28 | A kind of industrial wastewater light-catalyzed reaction processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208361942U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110605121A (en) * | 2019-09-25 | 2019-12-24 | 滨州学院 | Preparation method of bismuth oxide/ferroferric oxide/graphene three-component composite material |
-
2018
- 2018-05-28 CN CN201820803410.3U patent/CN208361942U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110605121A (en) * | 2019-09-25 | 2019-12-24 | 滨州学院 | Preparation method of bismuth oxide/ferroferric oxide/graphene three-component composite material |
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| CF01 | Termination of patent right due to non-payment of annual fee |
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| CF01 | Termination of patent right due to non-payment of annual fee |