CN205990323U - The micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device - Google Patents
The micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device Download PDFInfo
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- CN205990323U CN205990323U CN201620975009.9U CN201620975009U CN205990323U CN 205990323 U CN205990323 U CN 205990323U CN 201620975009 U CN201620975009 U CN 201620975009U CN 205990323 U CN205990323 U CN 205990323U
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Abstract
This utility model discloses a kind of micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device, including grid device, water collect tank, filter screen, ozone Oxidation Treatment device, settling tank, Biochemical pot, membrane permeation tank, sludge treatment equipment, clean water tank, air collector, air pump, ultraviolet catalytic oxidation tank and ozone filter, described ozone Oxidation Treatment device includes ozonator, micro-nano bubble generator, compressor pump, pumping chamber, barometric damper and ozone oxidation tank, described micro-nano bubble generator includes housing, dividing plate, gas-liquid mixed vacuum pump, vacuum water sprayer and aeration head.This utility model purpose is that provides a kind of Organic substance in water and can be to antibacterial in water and the micro-nano bubble of novel ozone that effectively be killed of virus and multi-medium filtering comprehensive water treatment device of can effectively removing, using the Organic substance in ozone micro-nano bubble rapid sewage treating, new pollution will not be brought, reduce water process difficulty.
Description
Technical field
This utility model is related to water treatment field, more particularly, to a kind of micro-nano bubble of novel ozone and multimedium
Filter comprehensive water treatment device.
Background technology
Water process includes sewage disposal and two kinds of drinking water treatment, in order to be applied to specific purposes, water is carried out
Sedimentation, filtration, coagulation, flocculation, and the process of the water quality such as inhibition, scale inhibition conditioning.Entered at sewage by urban sewage pipe network
The sewage of reason factory is derived from different sewage discharge sources, living area, shopping centre and industrial occupancy, the bulk contaminants in these sewage
It is not quite similar, but rely on existing water treatment facilities cannot meet the water process of the sewage being formed after these sewage mix, should
Reduce heavy metal ion, remove the Organic substance in decontaminated water again, also bacterial viruses in sewage will be killed.And existing equipment
In order to reduce the hazardness to environment for the sewage to greatest extent, by adding various medicaments in sewage, and these medicaments can bring
New pollution.
Utility model content
In view of this, this utility model purpose is that offer one kind can effectively remove Organic substance in water and can be to water
Middle antibacterial and the viral micro-nano bubble of novel ozone effectively killed and multi-medium filtering comprehensive water treatment device, using smelly
Organic substance in oxygen micro-nano bubble rapid sewage treating, will not bring new pollution, reduce water process difficulty.
For reaching above-mentioned purpose, this utility model adopts following technical proposals：The micro-nano bubble of novel ozone and multimedium
Filter comprehensive water treatment device, including grid device, water collect tank, filter screen, ozone Oxidation Treatment device, settling tank, Biochemical pot, film
Infiltration tank, sludge treatment equipment, clean water tank, air collector, air pump, ultraviolet catalytic oxidation tank and ozone filter, described ozone
Oxidation treatment device includes ozonator, micro-nano bubble generator, compressor pump, pumping chamber, barometric damper and ozone oxygen
Change tank, described micro-nano bubble generator includes housing, dividing plate, gas-liquid mixed vacuum pump, vacuum water sprayer and aeration head, described
Dividing plate is located in described housing and described housing internal cavity is divided into the molten air chamber that head and the tail connect successively, and described gas-liquid mixed is true
The liquid feeding end of empty pump is located in described housing, the liquid feeding end of the liquid outlet of described gas-liquid mixed vacuum pump and described vacuum water sprayer
Fluid communication connects, and the liquid outlet of described vacuum water sprayer is connected with the liquid feeding end fluid communication of described aeration head, described aeration
The liquid outlet of head is located in described ozone oxidation tank；The outlet side of described ozonator and the inlet end fluid of described compressor pump
Conducting connects, and the outlet side of described compressor pump is connected with the inlet end fluid communication of described pumping chamber, gives vent to anger in described pumping chamber
End is connected with the inlet end fluid communication of described housing, and the inlet end of described housing is located in described molten air chamber, and described air-flow is adjusted
Section valve is located on the outlet side of described pumping chamber；It is provided with composite filter, described composite filter bag in described ozone oxidation tank
Include installing frame, filtration activated carbon stripe board and filtration zeolite stripe board, described filtration activated carbon stripe board and described mistake
Across being located on described installing frame between filter zeolite stripe board, described filtration is used with the two ends of activated carbon stripe board and described filtration
The two ends of zeolite stripe board are fixedly connected with described installing frame respectively；The liquid outlet of described water collect tank and described ozone oxidation tank
Liquid feeding end fluid communication connects, and the liquid outlet of described ozone oxidation tank is connected with the liquid feeding end fluid communication of described settling tank, institute
The liquid feeding end fluid communication of the liquid outlet and described Biochemical pot of stating settling tank is connected, and the liquid outlet of described Biochemical pot is oozed with described film
The liquid feeding end fluid communication of tank connects thoroughly, and the liquid outlet of described membrane permeation tank is connected with the liquid feeding end fluid communication of described clean water tank
Connect, the liquid outlet of described clean water tank is connected with discharge of wastewater pipeline fluid communication up to standard；The mud outfan of described water collect tank, institute
The mud outfan of the mud outfan and described Biochemical pot of stating settling tank is inputted with the mud of described sludge treatment equipment respectively
End fluid communication connects；The outlet side of described water collect tank, the outlet side of described ozone oxidation tank, the outlet side of described settling tank,
The outlet side of the outlet side of described Biochemical pot and described membrane permeation tank is connected with the inlet end fluid communication of described air collector respectively,
The outlet side of described air collector is connected with the inlet end fluid communication of described air pump, the outlet side of described air pump and described purple
The inlet end fluid communication connection of outer catalysis oxidation tank, the outlet side of described ultraviolet catalytic oxidation tank and described ozone filter
Inlet end fluid communication connects；Described grid device is located at the water inlet end of described water collect tank, and described filter screen is located at described water collect tank
Water side.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, described pumping chamber and described housing
Between be provided with a safety can, the outlet side of described pumping chamber is connected with the inlet end fluid communication of described safety can, described peace
The full outlet side of tank is connected with the inlet end fluid communication of described housing.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, the inlet end of described air collector sets
There are surge tank, the outlet side of described water collect tank, the outlet side of described ozone oxidation tank, the outlet side of described settling tank, described life
The outlet side of the outlet side and described membrane permeation tank of changing tank is connected with the inlet end fluid communication of described surge tank respectively, described slow
The inlet end fluid communication of the inlet end and described air collector that rush tank is connected.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, the liquid feeding end of described aeration head sets
There is flow control valve.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, described dividing plate is provided with flow-disturbing
Plate.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, the inlet end of described housing is located at
The bottom of described housing.
The micro-nano bubble of above-mentioned novel ozone and multi-medium filtering comprehensive water treatment device, described composite filter will be described
Ozone oxidation tank inner space is separated into more than or equal to three end to end oxidation chamber successively.
The beneficial effects of the utility model are as follows：
1. this utility model made using the molten air chamber in micro-nano bubble generator smelly in the Ozone Water in molten air chamber
Oxygen concentration obtains the raising of maximum under equal pressure, so that the oxidation of the micro-nano bubble of ozone using ozone water generating
Dirt-removing power is improved, and ensures that the Organic substance in sewage can decompose, effectively exhaustive oxidation in ozone oxidation tank
Reduce the content of the Organic substance in sewage.
2. this utility model is removed to the Organic substance in water using the Strong oxdiative ability of the micro-nano bubble of ozone, and right
Bacterial viruses in water are killed, and do not result in water pollution, efficient and environment-friendly.
3. the ozone in the mixed gas that can discharge in ozone oxidation tank carries out further with not only can save
The material evaporating in sewage can also be carried out oxidation Decomposition by resource, and the antibacterial being carried is carried out effectively with virus
Kill.
4. in this utility model, the internal end to end oxidation chamber of ozone oxidation tank can increase sewage in ozone oxidation tank
Interior path, so that the Organic substance in sewage is removed further, and makes antibacterial in sewage and virus be entered
One step is killed.
Brief description
Fig. 1 is that the structure of the micro-nano bubble of novel ozone of the present utility model and multi-medium filtering comprehensive water treatment device is shown
It is intended to；
Fig. 2 is micro-nano in the micro-nano bubble of novel ozone of the present utility model and multi-medium filtering comprehensive water treatment device
The structural representation of bubble generator；
Fig. 3 is ozone oxygen in the micro-nano bubble of novel ozone of the present utility model and multi-medium filtering comprehensive water treatment device
Change the structural representation of tank；
Fig. 4 is to be combined in the micro-nano bubble of novel ozone of the present utility model and multi-medium filtering comprehensive water treatment device
The structural representation of filter plate.
In figure：1- water collect tank；2- ozone oxidation tank；3- settling tank；4- Biochemical pot；5- membrane permeation tank；6- clean water tank；7- is dirty
Mud processing meanss；8- air collector；9- air pump；10- ultraviolet catalytic oxidation tank；11- ozone filter；The micro-nano bubble of 12- is sent out
Raw device；13- safety can；14- barometric damper；15- pumping chamber；16- compressor pump；17- ozonator；18- grid device；
19- filter screen；20- housing；The inlet end of 21- housing；22- dividing plate；23- spoiler；24- gas-liquid mixed vacuum pump；25- vacuum water
Emitter；26- flow control valve；27- aeration head；The molten air chamber of 28-；29- composite filter；30- oxidation chamber；31- installing frame；32-
Filter and use activated carbon stripe board；33- filters and uses zeolite stripe board；34- surge tank.
Specific embodiment
In order to be illustrated more clearly that this utility model, with reference to preferred embodiments and drawings, this utility model is done into one
The explanation of step.In accompanying drawing, similar part is indicated with identical reference.It will be appreciated by those skilled in the art that below
Specifically described content is illustrative and be not restrictive, and should not limit protection domain of the present utility model with this.
As depicted in figs. 1 and 2, the micro-nano bubble of novel ozone of the present utility model and multi-medium filtering synthesis water process set
Standby, including grid device 18, water collect tank 1, filter screen 19, ozone Oxidation Treatment device, settling tank 3, Biochemical pot 4, membrane permeation tank 5,
Sludge treatment equipment 7, clean water tank 6, air collector 8, air pump 9, ultraviolet catalytic oxidation tank 10 and ozone filter 11, described ozone
Oxidation treatment device includes ozonator 17, micro-nano bubble generator 12, compressor pump 16, pumping chamber 15, barometric damper
14 and ozone oxidation tank 2, as shown in Fig. 2 described micro-nano bubble generator 12 to include housing 20, dividing plate 22, gas-liquid mixed true
Empty pump 24, vacuum water sprayer 25 and aeration head 27, described dividing plate 22 is located in described housing 20 and by described housing 20 internal cavity
It is divided into the molten air chamber 28 that head and the tail connect successively, the liquid feeding end of described gas-liquid mixed vacuum pump 24 is located in described housing 20, institute
The liquid outlet stating gas-liquid mixed vacuum pump 24 is connected with the liquid feeding end fluid communication of described vacuum water sprayer 25, described vacuum water-jet
The liquid outlet of device 25 is connected with the liquid feeding end fluid communication of described aeration head 27, and the liquid outlet of described aeration head 27 is located at described smelly
In oxygen oxidation tank 2；The outlet side of described ozonator 17 is connected with the inlet end fluid communication of described compressor pump 16, described pressure
The outlet side of contracting pump 16 is connected with the inlet end fluid communication of described pumping chamber 15, the outlet side of described pumping chamber 15 and described shell
The inlet end fluid communication of body 20 connects, and the inlet end of described housing 20 is located in described molten air chamber 28, described barometric damper
On 14 outlet sides being located at described pumping chamber 15；As shown in Figure 3 and Figure 4, it is provided with composite filter in described ozone oxidation tank 2
29, described composite filter 29 includes installing frame installing frame 31, filtration activated carbon stripe board 32 and filtration zeolite stripe board
33, across being located at described installing frame installing frame between described filtration activated carbon stripe board 32 and described filtration zeolite stripe board 33
On 31, described filtration with the two ends of the two ends of activated carbon stripe board 32 and described filtration zeolite stripe board 33 respectively with described peace
The installing frame 31 that frames up is fixedly connected；The liquid outlet of described water collect tank 1 is connected with the liquid feeding end fluid communication of described ozone oxidation tank 2
Connect, the liquid outlet of described ozone oxidation tank 2 is connected with the liquid feeding end fluid communication of described settling tank 3, described settling tank 3 go out liquid
End is connected with the liquid feeding end fluid communication of described Biochemical pot 4, the feed liquor of the liquid outlet of described Biochemical pot 4 and described membrane permeation tank 5
End fluid communication connects, and the liquid outlet of described membrane permeation tank 5 is connected with the liquid feeding end fluid communication of described clean water tank 6, described clear
The liquid outlet of water pot 6 is connected with discharge of wastewater pipeline fluid communication up to standard；The mud outfan of described water collect tank 1, described precipitation
The mud outfan of the mud outfan of the tank 3 and described Biochemical pot 4 mud input stream with described sludge treatment equipment 7 respectively
Body conducting connects；The outlet side of described water collect tank 1, the outlet side of described ozone oxidation tank 2, the outlet side of described settling tank 3, institute
The outlet side of the outlet side and described membrane permeation tank 5 of stating Biochemical pot 4 is connected with the inlet end fluid communication of described air collector 8 respectively
Connect, the outlet side of described air collector 8 is connected with the inlet end fluid communication of described air pump 9, the outlet side of described air pump 9 with
The inlet end fluid communication of described ultraviolet catalytic oxidation tank 10 connects, and the outlet side of described ultraviolet catalytic oxidation tank 10 is smelly with described
The inlet end fluid communication of oxygen filter 11 connects；Described grid device 18 is located at the water inlet end of described water collect tank 1, described filter screen
19 water sides being located at described water collect tank 1.
In order to avoid when equipment downtime overhauls or equipment occur catastrophic discontinuityfailure shut down when described micro-nano bubble generator
Water in 12 flows in described pumping chamber 15, in the present embodiment, is provided with one between described pumping chamber 15 and described housing 20
Safety can 13, the outlet side of described pumping chamber 15 is connected with the inlet end fluid communication of described safety can 13, described safety can 13
Outlet side be connected with the inlet end fluid communication of described housing 20.Simultaneously in order to avoid described water collect tank 1, described ozone oxidation
Water in tank 2, described settling tank 3, described Biochemical pot 4 and described membrane permeation tank 5 enters in described air collector 8, in the present embodiment,
It is provided with surge tank 34 in the inlet end of described air collector 8, the outlet side of described water collect tank 1, the giving vent to anger of described ozone oxidation tank 2
End, the outlet side of the outlet side of described settling tank 3, the outlet side of described Biochemical pot 4 and described membrane permeation tank 5 are delayed with described respectively
The inlet end fluid communication rushing tank 34 connects, the inlet end fluid communication of the inlet end of described surge tank 34 and described air collector 8
Connect.
And the ozone in order to avoid preparing is wasted, the premise of Organic substance and bacterial viruses detection in water body
Under, can be controlled to flowing into the micro-nano bubbles volume of ozone in described ozone oxidation tank 2, described smelly to flowing in order to realize
The purpose that the micro-nano bubbles volume of ozone in oxygen oxidation tank 2 is controlled, in the present embodiment, in the liquid feeding end of described aeration head 27
It is provided with flow control valve 26.And in view of because local temperature is different or other factors lead to water when material dissolves in water body
Internal concentration everywhere is different, and in order to allow ozone in described housing 20 be dissolved in the ozone Measuring Ozone Concentration in Water being formed after water more
Uniformly, in the present embodiment, described dividing plate 22 is provided with spoiler 23 so that Ozone Water is carried out constantly in described molten air chamber 28
Ground mixing, until extracted out described housing 20 by described gas-liquid mixed vacuum pump 24.Simultaneously for the ease of gas-liquid mixed so that ozone
Quickly dissolve in water, in this example, the inlet end of described housing 20 is located at the bottom of described housing 20.
In order that water body can the time of staying be longer in described ozone oxidation tank 2, and do not affect at the water of whole equipment
Described ozone oxidation tank 2 inner space, in the present embodiment, is separated into four head successively with described composite filter 29 by reason speed
The oxidation chamber 30 that tail is connected, arranges three described composite filters 29 in described ozone oxidation tank 2.
When staying water being processed using this utility model, staying water flow through described grid device 18 it
Afterwards, the larger object of the volume in water body is filtered out, and then water body flows in described water collect tank 1 and carries out preliminary sedimentation, with
When ensure stablizing of water volume flow rate in follow-up water treatment procedure, water body flows into described after the preliminary sedimentation of described water collect tank 1
In ozone oxidation tank 2, in described ozone oxidation tank 2, the activated carbon on described composite filter 29 and zeolite can be by water
Free Adsorption of Organic, and adsorb the micro-nano bubble of ozone that described micro-nano bubble generator 12 generates so that Organic substance
- the OH generating is reacted with ozone and water on described composite filter 29 react so that Organic substance is changed into carbon dioxide
With water etc., so that the Organic substance in water body is removed, and the micro-nano bubble of ozone can also kill to bacterial viruses
Go out, and after described ozone oxidation tank 2 disinfection and organics removal are processed, water body enters in described sedimentation tank and carries out
Precipitate again, after then water body sequentially passes through described Biochemical pot 4, described film reaction tank and described clean water tank 6 process again, pass through
Described discharge of wastewater pipeline up to standard enters public drainage.
Obviously, above-described embodiment of the present utility model is only intended to clearly illustrate this utility model example, and
It is not the restriction to embodiment of the present utility model, for those of ordinary skill in the field, in described above
On the basis of can also make other changes in different forms, all of embodiment cannot be exhaustive here,
Every belong to the obvious change that the technical solution of the utility model extended out or change still in of the present utility model
The row of protection domain.
Claims (7)
1. the micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device are it is characterised in that include grid device
(18), water collect tank (1), filter screen (19), ozone Oxidation Treatment device, settling tank (3), Biochemical pot (4), membrane permeation tank (5), mud
Processing meanss (7), clean water tank (6), air collector (8), air pump (9), ultraviolet catalytic oxidation tank (10) and ozone filter (11),
Described ozone Oxidation Treatment device includes ozonator (17), micro-nano bubble generator (12), compressor pump (16), pumping chamber
(15), barometric damper (14) and ozone oxidation tank (2), described micro-nano bubble generator (12) includes housing (20), dividing plate
(22), gas-liquid mixed vacuum pump (24), vacuum water sprayer (25) and aeration head (27), described dividing plate (22) is located at described housing
(20) it is divided into the molten air chamber (28) that head and the tail connect successively, described gas-liquid mixed vacuum pump in and by described housing (20) internal cavity
(24) liquid feeding end is located in described housing (20), the liquid outlet of described gas-liquid mixed vacuum pump (24) and described vacuum water sprayer
(25) liquid feeding end fluid communication connects, the liquid feeding end stream of the liquid outlet of described vacuum water sprayer (25) and described aeration head (27)
Body conducting connects, and the liquid outlet of described aeration head (27) is located in described ozone oxidation tank (2)；Described ozonator (17)
Outlet side is connected with the inlet end fluid communication of described compressor pump (16), the outlet side of described compressor pump (16) and described pumping chamber
(15) inlet end fluid communication connects, the inlet end fluid communication of the outlet side of described pumping chamber (15) and described housing (20)
Connect, the inlet end of described housing (20) is located in described molten air chamber (28), and described barometric damper (14) is located at described supercharging
On the outlet side of room (15)；It is provided with composite filter (29), described composite filter (29) includes in described ozone oxidation tank (2)
Installing frame (31), filtration activated carbon stripe board (32) and filtration zeolite stripe board (33), activated carbon bar shaped is used in described filtration
Across being located on described installing frame (31) between plate (32) and described filtration zeolite stripe board (33), described filtration uses active sketching charcoal
The two ends of shape plate (32) are fixedly connected with described installing frame (31) respectively with the two ends of described filtration zeolite stripe board (33)；Institute
The liquid outlet stating water collect tank (1) is connected with the liquid feeding end fluid communication of described ozone oxidation tank (2), described ozone oxidation tank (2)
Liquid outlet be connected with the liquid feeding end fluid communication of described settling tank (3), the liquid outlet of described settling tank (3) and described Biochemical pot
(4) liquid feeding end fluid communication connects, and the liquid feeding end fluid of the liquid outlet of described Biochemical pot (4) and described membrane permeation tank (5) is led
Lead to and connect, the liquid outlet of described membrane permeation tank (5) is connected with the liquid feeding end fluid communication of described clean water tank (6), described clean water tank
(6) liquid outlet is connected with discharge of wastewater pipeline fluid communication up to standard；The mud outfan of described water collect tank (1), described precipitation
The mud outfan of the mud outfan of tank (3) and described Biochemical pot (4) is defeated with the mud of described sludge treatment equipment (7) respectively
Enter to hold fluid communication to connect；The outlet side of described water collect tank (1), the outlet side of described ozone oxidation tank (2), described settling tank
(3) outlet side of outlet side, the outlet side of described Biochemical pot (4) and described membrane permeation tank (5) respectively with described air collector (8)
Inlet end fluid communication connect, the inlet end fluid communication of the outlet side of described air collector (8) and described air pump (9) is even
Connect, the outlet side of described air pump (9) is connected with the inlet end fluid communication of described ultraviolet catalytic oxidation tank (10), described ultraviolet
The outlet side of catalysis oxidation tank (10) is connected with the inlet end fluid communication of described ozone filter (11)；Described grid device
(18) it is located at the water inlet end of described water collect tank (1), described filter screen (19) is located at the water side of described water collect tank (1).
2. the micro-nano bubble of novel ozone according to claim 1 and multi-medium filtering comprehensive water treatment device, its feature
It is, between described pumping chamber (15) and described housing (20), be provided with a safety can (13), the giving vent to anger of described pumping chamber (15)
End is connected with the inlet end fluid communication of described safety can (13), the outlet side of described safety can (13) and described housing (20)
Inlet end fluid communication connects.
3. the micro-nano bubble of novel ozone according to claim 2 and multi-medium filtering comprehensive water treatment device, its feature
It is, the inlet end of described air collector (8) is provided with surge tank (34), the outlet side of described water collect tank (1), described ozone oxidation tank
(2) outlet side, the outlet side of described settling tank (3), the going out of the outlet side of described Biochemical pot (4) and described membrane permeation tank (5)
Gas end is connected with the inlet end fluid communication of described surge tank (34) respectively, the inlet end of described surge tank (34) and described gas collection
The inlet end fluid communication of tank (8) connects.
4. the micro-nano bubble of novel ozone according to claim 3 and multi-medium filtering comprehensive water treatment device, its feature
It is, the liquid feeding end of described aeration head (27) is provided with flow control valve (26).
5. according to the micro-nano bubble of the arbitrary described novel ozone of Claims 1 to 4 and multi-medium filtering comprehensive water treatment device,
It is characterized in that, described dividing plate (22) is provided with spoiler (23).
6. the micro-nano bubble of novel ozone according to claim 5 and multi-medium filtering comprehensive water treatment device, its feature
It is, the inlet end of described housing (20) is located at the bottom of described housing (20).
7. the micro-nano bubble of novel ozone according to claim 6 and multi-medium filtering comprehensive water treatment device, its feature
It is, described ozone oxidation tank (2) inner space is separated into first successively more than or equal to three by described composite filter (29)
The oxidation chamber (30) that tail is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620975009.9U CN205990323U (en) | 2016-08-29 | 2016-08-29 | The micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620975009.9U CN205990323U (en) | 2016-08-29 | 2016-08-29 | The micro-nano bubble of novel ozone and multi-medium filtering comprehensive water treatment device |
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| Publication Number | Publication Date |
|---|---|
| CN205990323U true CN205990323U (en) | 2017-03-01 |
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ID=58105201
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115536184A (en) * | 2022-11-02 | 2022-12-30 | 哈尔滨工业大学 | Integrated treatment device for town drinking water by combining micro-nano bubble ozone oxidation and electric flocculation and water treatment method thereof |
-
2016
- 2016-08-29 CN CN201620975009.9U patent/CN205990323U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115536184A (en) * | 2022-11-02 | 2022-12-30 | 哈尔滨工业大学 | Integrated treatment device for town drinking water by combining micro-nano bubble ozone oxidation and electric flocculation and water treatment method thereof |
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| 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: 20170301 Termination date: 20170829 |