CN106082541A - A kind of quality purifying device for water of polluted-water - Google Patents
A kind of quality purifying device for water of polluted-water Download PDFInfo
- Publication number
- CN106082541A CN106082541A CN201610574941.5A CN201610574941A CN106082541A CN 106082541 A CN106082541 A CN 106082541A CN 201610574941 A CN201610574941 A CN 201610574941A CN 106082541 A CN106082541 A CN 106082541A
- Authority
- CN
- China
- Prior art keywords
- water
- oxygen
- hypoxia response
- enriched
- filtering ponds
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
nullA kind of quality purifying device for water of polluted-water，Including framework，The floating frame being connected with framework，Framework has N number of and interconnects successively，Framework is made up of hypoxia response pond and oxygen-enriched filtering ponds，Hypoxia response pond is provided with current turn round flow cavity，Bottom, hypoxia response pond arranges wastewater inlet，Hypoxia response pond arranges connected entrance，Hypoxia response arranges filler in pond，Bottom oxygen-enriched filtering ponds, aerator is set，Oxygen-enriched filtering ponds inner chamber arranges Dynamic membrane filter，Water in oxygen-enriched filtering ponds enters into through Dynamic membrane filter in Dynamic membrane filter inner chamber，Or，Dynamic membrane filter inner chamber is connected with urban river water through delivery pump by pipeline，The intracavity bottom of oxygen-enriched filtering ponds passes through sludge pipe through sludge reflux pump and the sludge pipe opening in communication extending into inner chamber bottom, hypoxia response pond，The sludge pipe being positioned at framework top position is provided with excessive mud mud valve.Having an advantage in that: easy to make, effectively utilizing the carbon source in water, effects of purification quality is good.
Description
Technical field
The present invention relates to environmental protection technical field, especially relate to the quality purifying device for water of a kind of purifying contaminated water body.
Background technology
Due to factors such as production, life style, dietary structure changes, China city, domestic sewage in rural areas all present carbon
The feature that source is not enough, forms low ratio of carbon to ammonium, low carbon-phosphorus ratio trend, adds the difficulty of traditional biological denitrogenation dephosphorizing.So, fully
Utilizing carbon source in water is the essential condition that river carries out denitrogenation dephosphorizing.
Existing a kind of application number CN2010068237.3 entitled " being placed in the rice terrace water-break quality purifying device for water of ridge "
Chinese invention patent disclose a kind of rice terrace water-break quality purifying device for water being placed in ridge, it is characterized in that the reinforcing bar with φ 10
Building monomer quality purifying device for water framework, both sides are set to plastic plate, and other 4 faces are set to steel wire, and front end arranges plastics
Gate, is divided into A, part B with the steel wire of fine and closely woven degree inside device, and the volume ratio of two parts of A, B is 2: 1, part A steel wire
Net is big density steel wire, and fills biologic packing material ball, and part B steel wire is fine and closely woven degree steel wire, and fills activity, monomer water
Matter purifier front-back is designed as openable, monomer quality purifying device for water or two monomer quality purifying device for water and is placed in water
In paddy field drainage end ridge, and fix with timber.Advantage: improve tradition rice field and directly open the in line rice field water-break of gate,
Water quality can not get the conventional discharge mode of any purification, can be with nitrogen, phosphorus, Organic substance in the water-break of effectively catching farmland be difficult to biology
The harmful substances such as the pesticide residue of degraded.But, this invention can not utilize the carbon source in water very well, therefore, it is necessary to this
Method is improved further.
Summary of the invention
The technical problem to be solved is to provide a kind of easy to make, effectively for above-mentioned prior art present situation
Utilize the carbon source in water, the quality purifying device for water of the polluted-water that effects of purification quality is good.
The present invention solves the technical scheme that above-mentioned technical problem used: the quality purifying device for water of this polluted-water, bag
Include the framework being placed in river course, the floating frame in being connected with framework and framework being bubbled through the water column, it is characterised in that: described frame
Body has N number of and interconnects successively, and each framework is made up of hypoxia response pond and oxygen-enriched filtering ponds, described hypoxia response
Being provided with current in pond to turn round flow cavity, bottom, one, described hypoxia response pond is provided with the wastewater inlet of river sewage, described lacks
The other end of oxygen reaction tank is provided with the connected entrance that intracavity sewage is connected with oxygen-enriched filtering ponds through the flow cavity that turns round, and lacks described
Oxygen reaction tank is arranged microorganism and/or contaminants filler thereon, described oxygen-enriched filtering ponds intracavity bottom can be promoted to set
Being equipped with aerator, described aerator is connected with gasing pump by appendix, the oxygen-enriched filtering ponds above aerator
Being provided with Dynamic membrane filter in inner chamber, the water in oxygen-enriched filtering ponds enters in Dynamic membrane filter through Dynamic membrane filter
In chamber, and Dynamic membrane filter inner chamber by pipeline through delivery pump and adjacent hypoxia response pond intracavity inter-connection, or, described
Dynamic membrane filter inner chamber is connected with urban river water through delivery pump by pipeline, and the intracavity bottom of described oxygen-enriched filtering ponds is by dirt
Mud pipeline, through sludge reflux pump and the sludge pipe opening in communication extending into inner chamber bottom, hypoxia response pond, is being positioned in framework
Be provided with excessive mud mud valve on the sludge pipe that orientation is put, described N be not zero natural number.
As improvement, the other end in described hypoxia response pond is preferably provided with intracavity sewage through the flow cavity that turns round with oxygen-enriched
The connected entrance that filtering ponds are connected, its structure is: hypoxia response pond inner chamber is separated into H+ by described hypoxia response pond H block dividing plate
Vertical between separate space, the wastewater inlet of described river sewage be arranged at first vertical between the bottom of separate space, between first is vertical
The water of separate space be flowed into second vertical between separate space passage be positioned at the top of dividing plate, second vertical between the water of separate space be flowed into the
Three vertical between separate space passage be positioned at the bottom of dividing plate, and top-bottom cross is arranged successively, and in hypoxia response pond, last is vertical
Between the separate space connection stomatodeum that is flowed in oxygen-enriched filtering ponds inner chamber be positioned at the bottom in hypoxia response pond.
As improvement, the other end in described hypoxia response pond is preferably provided with intracavity sewage through the flow cavity that turns round with oxygen-enriched
The connected entrance that filtering ponds are connected, its structure is: described oxygen-enriched filtering ponds are positioned at the middle part of framework, described hypoxia response pond cincture
Ground is by oxygen-enriched filtering ponds Wei Yu center, and the wastewater inlet in described framework is positioned at the bottom that framework is peripheral, and described connected entrance is positioned at
The bottom position enclosed in framework.
As improvement, described filler is preferably hung in the inner chamber of hypoxia response pond with striped stride distribution.
Improving further, centrage and PP elastic yarn that the filler of every strip is preferably rolled into by PE form, described PP
Elastic yarn forms the filler of a strip with the ligation being spaced up and down on axial cord.
As improvement, described oxygen-enriched filtering ponds inner chamber is preferably placed with and promotes the formation of Dynamic Membrane and delay Dynamic Membrane to decline
Old powdery active carbon filler and PP floating stuffing.
As improvement, described Dynamic membrane filter preferably connects and has for backwash Dynamic membrane filter to recover dynamic
The breather of state film filter film body flux, described breather is connected with gasing pump.
Improving further, described breather is preferably connected with gasing pump by three-way magnetic valve with appendix, and
Air gauge automatic programme control adjusting means, described air gauge automatic programme control adjusting means it is provided with on appendix above described framework
It is connected with three-way magnetic valve by circuit.
As improvement, described Dynamic membrane filter inner chamber preferably passes through pipeline through delivery pump and adjacent hypoxia response pond
In inner chamber, the interval of river sewage import is connected.
As improvement, described sludge pipe being preferably provided with threeway solenoid electric valve, described mud mud valve is positioned at
In threeway solenoid electric valve, described threeway solenoid electric valve is connected with program controller.
Compared with prior art, it is an advantage of the current invention that: combine anaerobism oxygen enriching process former with bioreactor of dynamic membrane
Reason design, is replaced the mud-water separation effect of second pond by bioreactor of dynamic membrane, it is not necessary to consider the settling property of mud, separates
Effect is more preferable；Making sludge concentration maintain in higher level, faster, and nitrifier is trapped and can be the most numerous in reaction
Grow, promote nitrification and the carrying out of anti-nitration reaction；Some dissolved oxygen contents is sufficient but polluted-water that content of microorganisms is relatively low
In, high sludge content in reaction tank of the present invention, can effectively assemble microorganism, promote the denitrogenation dephosphorizing of water body；Use segmental influent,
Thered is provided carbon source by sewage for anti-nitration reaction, save the input of carbon source.And improve the pH value in hypoxia response pond, promote nitrification
The carrying out of reaction；Dynamic Membrane is made up of layer of non-woven fabric material, and non-woven fabrics is cheap, wide material sources, and Dynamic Membrane makes simple,
It is easy to industrialized production；Framework is supported by floating frame, can be placed on the river course central authorities water surface, and the denitrogenation dephosphorizing carrying out river processes；
Easy maintenance, as there is fouling membrane, device automatic backwash, recovers membrane flux；Consume energy little, can reach with circular treatment river
Corresponding water quality requirement.
Accompanying drawing explanation
Fig. 1 is the vertical cross section structural representation in the single framework of the embodiment of the present invention；
Fig. 2 is the vertical cross section structural representation after framework is sequentially connected with in Fig. 1；
Fig. 3 is Fig. 2 structural representation when being in vertical view state；
Fig. 4 is the vertical cross section structural representation in the single framework of another kind embodiment of the present invention；
Fig. 5 is the vertical cross section structural representation after framework is sequentially connected with in Fig. 4；
Fig. 6 is Fig. 5 structural representation when being in vertical view state.
Detailed description of the invention
Below in conjunction with accompanying drawing embodiment, the present invention is described in further detail.
As shown in Figure 1 to Figure 3, the quality purifying device for water of the polluted-water of the present embodiment, include the frame being placed in river course
Body 3, the floating frame 4 in being connected with framework 3 and framework 3 being bubbled through the water column, described framework 3 has N number of and is interconnected on successively
Together, each framework 3 is made up of hypoxia response pond 1 and oxygen-enriched filtering ponds 2, is provided with current and turns round stream in described hypoxia response pond 1
Dynamic chamber 11, bottom, 1 one, described hypoxia response pond is provided with the wastewater inlet 12 of river sewage, described hypoxia response pond 1 another
One is provided with the connected entrance 13 that intracavity sewage is connected with oxygen-enriched filtering ponds 2 through the flow cavity 11 that turns round, at described hypoxia response
Arranging in pond 1 and can promote microorganism and/or contaminants filler thereon 14, described oxygen-enriched filtering ponds 2 intracavity bottom is arranged
Aerator 21, described aerator 21 is had to be connected with gasing pump 23 by appendix 22, the richness above aerator 21
Being provided with Dynamic membrane filter 24 in oxygen filtering ponds 2 inner chamber, the water in oxygen-enriched filtering ponds 2 enters into through Dynamic membrane filter 24
In Dynamic membrane filter 24 inner chamber, and Dynamic membrane filter 24 inner chamber passes through pipeline through delivery pump 25 and adjacent hypoxia response pond
1 intracavity inter-connection, or, described Dynamic membrane filter 24 inner chamber is connected with urban river water through delivery pump 25 by pipeline, described
The intracavity bottom of oxygen-enriched filtering ponds 2 by sludge pipe 26 through sludge reflux pump 27 with extend into inner chamber bottom, hypoxia response pond 1
Sludge pipe opening in communication, the sludge pipe being positioned at framework 3 top position is provided with excessive mud mud valve, described
N be not zero natural number.The other end in hypoxia response pond 1 is provided with intracavity sewage through flow cavity 11 and the oxygen-enriched filtering ponds of turning round
The connected entrance 13 that 2 are connected, its structure is: hypoxia response pond 1 inner chamber is separated into H+1 by described hypoxia response pond 1H block dividing plate 15
Individual vertical between separate space, the wastewater inlet 12 of described river sewage be arranged at first vertical between the bottom of separate space, first is erected
To the water of a separate space be flowed into second vertical between separate space passage be positioned at the top of dividing plate 15, second vertical between the current of separate space
Enter the bottom being positioned at dividing plate 15 to the 3rd separate space passage between vertical, and top-bottom cross is arranged successively, last in hypoxia response pond 1
One vertical between separate space connected entrance 13 road that is flowed in oxygen-enriched filtering ponds 2 inner chamber be positioned at the bottom in hypoxia response pond 1.
As shown in Figures 4 to 6, the other end in hypoxia response pond 1 is provided with intracavity sewage through the flow cavity 11 that turns round with oxygen-enriched
The connected entrance 13 that filtering ponds 2 are connected, its structure is: described oxygen-enriched filtering ponds 2 are positioned at the middle part of framework 3, described hypoxia response
Pond 1 is circumferentially by oxygen-enriched filtering ponds 2 Wei Yu center, and the wastewater inlet 12 in described framework 3 is positioned at the bottom that framework is peripheral, described
Connected entrance 13 is positioned at the bottom position that framework 3 is enclosed.
Filler 14 is hung in the inner chamber of hypoxia response pond 1 with striped stride distribution.The filler 14 of every strip is by PE volume
The centrage become and PP elastic yarn composition, described PP elastic yarn forms a strip with the ligation being spaced up and down on axial cord
Filler 14.Oxygen-enriched filtering ponds 2 inner chamber is placed with and promotes the formation of Dynamic Membrane and delay the powdered active carbon that Dynamic Membrane is old and feeble
Filler 20 and PP floating stuffing 28.Connect in Dynamic membrane filter 24 and have for backwash Dynamic membrane filter with Restoration dynamics film
The breather 29 of filter film body flux, described breather 29 is connected with gasing pump 23.Breather 29 passes through with appendix 22
Three-way magnetic valve 5 is connected with gasing pump 23, and is provided with air gauge automatic programme control on the appendix 22 above described framework 3
Adjusting means 6, described air gauge automatic programme control adjusting means 6 is connected with three-way magnetic valve 5 by circuit.Dynamic membrane filter
24 inner chambers are connected by pipeline interval of river sewage import in delivery pump 25 and adjacent hypoxia response pond 1 inner chamber.Dirty
Being provided with threeway solenoid electric valve 31 on mud pipeline, described mud mud valve is positioned in threeway solenoid electric valve 31, described threeway
Solenoid electric valve 31 is connected with program controller.
Described aerator refers to: outside air can spray into aerophore to oxygen-enriched reaction tank, and this is the art
In known technology.
The operation principle of the present invention is: sewage inlet designs bottom hypoxia response pond, can be to deeper in river
Water carries out processing, circulating.Hypoxia response pond adds suspension type filler in advance, promotes germs collect on filler, increases
Microorganism and the contact area of water.Sewage enters the motion of tailing edge dividing plate baffling, extends water sport track thus extends the response time,
It is possible to prevent again bottom into water along hypoxia response pond to flow directly into oxygen-enriched filtering ponds, increases contacting of activated sludge and water inlet simultaneously
Area, increases reaction rate.Add PP floating stuffing and Powdered Activated Carbon in oxygen-enriched reaction tank in advance, promote the shape of Dynamic Membrane
Become, delay film old and feeble.Dynamic Membrane is made by nonwoven cloth material, and its Main Function is to retain mud and algae.Taking out at delivery pump
Deliver to, bottom the hypoxia response pond of next monomer, mix, under carrying out with the sewage entered in this pond by processing water under suction effect
One step processes.Aerator is set and has both sides effect: can be that oxygen-enriched filtering ponds provide dissolved oxygen；Strengthen Dynamic Membrane surface
Cross-flow velocity, the hardly degraded organic substance making to be blocked in Dynamic Membrane surface departs from film surface, lessening membrane fouling.Aerator aeration
During work, on three-way magnetic valve, valve is always maintained at opening, and right valve cuts out, and lower valve and electromagnetic valve are opened.Pass through air gauge
The aeration intensity of determinator, vacuum meter detection membrane inside pressure.Surely when null representation is to certain numerical value, under three-way magnetic valve
Valve and electromagnetic valve simultaneously close off, and the right valve of electric T-shaped valve is opened, and carries out backwash to Dynamic Membrane, recovers its membrane flux, it is possible to
By stopping delivery pump, to allow aerator wash away membrane module and to make it recover membrane flux；Three-way magnetic valve and electromagnetic valve are by automatically
Controlling device to control, base sludge reflux keeps the activated sludge concentration in hypoxia response pond at a higher water further
Flat.During mud normal reflow, under threeway solenoid electric valve, valve and upper valve are opened, when oxygen-enriched filtering ponds sludge concentration is too high, and threeway
Under solenoid electric valve, valve cuts out, and right valve is opened, and mud is discharged.If hypoxia response pond also needs spoil disposal, threeway Electromagnetic Control can be closed
The upper valve of valve, opens right valve and lower valve, by discharging mud at the external sludge pump of right valve.
The operation principle of another kind of deformation device is: hypoxia response pond adds filler and assembles microorganism, promotes activated sludge
With waste water.Oxygen-enriched filtering ponds add Powdered Activated Carbon, filler, promote the formation of Dynamic Membrane, and can be with lessening membrane fouling.
Oxygen-enriched filtering ponds are placed on one circular passage of hypoxia response pond intermediate formation, process sewage and the last period after water enters constantly to
Front mixed flow, forms plug-flow state forward, and promotion water is fully contacted with activated sludge, improves anti-nitration reaction speed.
After entering oxygen-enriched filtering ponds identical with said apparatus control principle.Water purification flow path: in first box body, hypoxia response pond needs pre-
First add filler, utilize the biomembrane generated on floating stuffing can eliminate a part of Organic substance, it is also possible to as microorganism
Carrier, makes activated sludge be suspended in water.Sewage enters from bottom water inlet, contacts with returned sludge mixing, due to backflow dirt
Containing substantial amounts of NO in mud liquid3-and NO2-, utilizing the organic carbon in sewage is carbon source, occurs denitrification anti-under anaerobic environment
Should, discharge N2.In this post processing water, nitrogen substance is ammonia nitrogen and organic nitrogen.Meanwhile, the polyP bacteria generated under anaerobic environment fills
Subrelease puts phosphorus.Then into oxygen-enriched filtering ponds.Oxygen-enriched filtering ponds throw in PP floating stuffing and Powdered Activated Carbon in advance, at delivery pump
Swabbing action under form Dynamic Membrane, sewage enters inside Dynamic Membrane, the activity under the filtration of Dynamic Membrane and non-woven fabrics, in water
Mud and algae can be retained down completely, and in making oxygen-enriched filtering ponds, activated sludge content maintains a higher level all the time.
PolyP bacteria in activated sludge also fully absorbs phosphorus, reaches the purpose of dephosphorization.Further, nitrifier is also by effectively catching and in reaction
Amount reproduction in pond, and its time-to-live is longer, can substantially increase the quantity of nitrifier, the ammonia nitrogen in sewage and organic nitrogen
Being substantially oxidized, ammonia nitrogen and organic nitrogen content reduce rapidly, NO3-and NO2-content rises rapidly.Therefore, the place of oxygen-enriched filtering ponds
Reason Shuifu County is containing NO3-and NO2-, process water and enter in the hypoxia response pond that next section of framework is interval, newly enter sewage and backflow with this section
Mud mixes, under anaerobic environment, with the Organic substance in sewage as carbon source, in the environment containing high-concentration activated sludge fully
Carry out anti-nitration reaction, discharge N2, the phosphorus of polyP bacteria release simultaneously, this post processing water enters oxygen-enriched filtering ponds to be carried out at next step
Reason.
Claims (10)
1. a quality purifying device for water for polluted-water, includes the framework (3) being placed in river course, be connected with framework (3) and
Floating frame (4) in framework (3) being bubbled through the water column, it is characterised in that: described framework (3) has N number of and is interconnected on one successively
Rising, each framework (3) is made up of hypoxia response pond (1) and oxygen-enriched filtering ponds (2), is provided with current in described hypoxia response pond (1)
Turn round flow cavity (11), and bottom, (1) one, described hypoxia response pond is provided with the wastewater inlet (12) of river sewage, described anoxia
The other end of reaction tank (1) is provided with the connected entrance that intracavity sewage is connected with oxygen-enriched filtering ponds (2) through the flow cavity that turns round (11)
(13), arrange in described hypoxia response pond (1) and microorganism and/or contaminants filler thereon (14) can be promoted, described
Oxygen-enriched filtering ponds (2) intracavity bottom is provided with aerator (21), and described aerator (21) passes through appendix (22) and gas transmission
Pump (23) is connected, and is provided with Dynamic membrane filter (24) in oxygen-enriched filtering ponds (2) inner chamber of aerator (21) top, rich
Water in oxygen filtering ponds (2) enters in Dynamic membrane filter (24) inner chamber through Dynamic membrane filter (24), and Dynamic Membrane mistake
Filter (24) inner chamber by pipeline through delivery pump (25) and adjacent hypoxia response pond (1) intracavity inter-connection, or, described dynamically
Film filter (24) inner chamber is connected with urban river water through delivery pump (25) by pipeline, at the bottom of the inner chamber of described oxygen-enriched filtering ponds (2)
Portion passes through sludge pipe (26) through sludge reflux pump (27) and the sludge pipe opening extending into hypoxia response pond (1) inner chamber bottom
Being connected, be provided with excessive mud mud valve on the sludge pipe being positioned at framework (3) top position, described N is not to be zero
Natural number.
Quality purifying device for water the most according to claim 1, it is characterised in that: the other end of described hypoxia response pond (1) sets
Being equipped with the connected entrance (13) that intracavity sewage is connected with oxygen-enriched filtering ponds (2) through the flow cavity that turns round (11), its structure is: described scarce
Oxygen reaction tank (1) H block dividing plate (15) hypoxia response pond (1) inner chamber is separated into H+1 vertical between separate space, described river sewage
Wastewater inlet (12) be arranged at first vertical between the bottom of separate space, first vertical between the water of separate space be flowed into second and erect
Be positioned at the top of dividing plate (15) to a separate space passage, second vertical between the water of separate space be flowed into the 3rd vertical between separate space passage
Being positioned at the bottom of dividing plate (15), and top-bottom cross is arranged successively, between in hypoxia response pond (1), last is vertical, separate space is flowed into
Connected entrance (13) road in oxygen-enriched filtering ponds (2) inner chamber is positioned at the bottom of hypoxia response pond (1).
Quality purifying device for water the most according to claim 1, it is characterised in that: the other end of described hypoxia response pond (1) sets
Being equipped with the connected entrance (13) that intracavity sewage is connected with oxygen-enriched filtering ponds (2) through the flow cavity that turns round (11), its structure is: described richness
Oxygen filtering ponds (2) are positioned at the middle part of framework (3), described hypoxia response pond (1) circumferentially by oxygen-enriched filtering ponds (2) Wei Yu center,
Wastewater inlet (12) in described framework (3) is positioned at the bottom that framework is peripheral, and described connected entrance (13) is positioned at what framework (3) was enclosed
Bottom position.
Quality purifying device for water the most according to claim 1 and 2, it is characterised in that: described filler (14) divides with striped stride
It is hung in hypoxia response pond (1) inner chamber cloth.
Quality purifying device for water the most according to claim 4, it is characterised in that: the filler (14) of every strip is rolled into by PE
Centrage and PP elastic yarn composition, described PP elastic yarn forms filling out of a strip with the ligation being spaced up and down on axial cord
Material (14).
6. according to described quality purifying device for water arbitrary in claims 1 to 3, it is characterised in that: in described oxygen-enriched filtering ponds (2)
Chamber is placed with and promotes the formation of Dynamic Membrane and delay powder activated carbon filling material (20) and the PP floating stuffing that Dynamic Membrane is old and feeble
(28)。
7. according to described quality purifying device for water arbitrary in claims 1 to 3, it is characterised in that: described Dynamic membrane filter
(24) upper connection has for backwash Dynamic membrane filter with the breather (29) of Restoration dynamics film filter film body flux, described
Breather (29) is connected with gasing pump (23).
Quality purifying device for water the most according to claim 7, it is characterised in that: described breather (29) leads to appendix (22)
Cross three-way magnetic valve (5) to be connected with gasing pump (23), and be provided with air pressure on the appendix (22) of described framework (3) top
Table automatic programme control adjusting means (6), described air gauge automatic programme control adjusting means (6) passes through circuit and three-way magnetic valve (5) phase
Connect.
9. according to described quality purifying device for water arbitrary in claims 1 to 3, it is characterised in that: described Dynamic membrane filter
(24) inner chamber is connected by pipeline interval of river sewage import in delivery pump (25) and adjacent hypoxia response pond (1) inner chamber
Logical.
10. according to described quality purifying device for water arbitrary in claims 1 to 3, it is characterised in that: arrange on described sludge pipe
Threeway solenoid electric valve (31), described mud mud valve is had to be positioned in threeway solenoid electric valve (31), described threeway Electromagnetic Control
Valve (31) is connected with program controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610574941.5A CN106082541A (en) | 2016-07-11 | 2016-07-11 | A kind of quality purifying device for water of polluted-water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610574941.5A CN106082541A (en) | 2016-07-11 | 2016-07-11 | A kind of quality purifying device for water of polluted-water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106082541A true CN106082541A (en) | 2016-11-09 |
Family
ID=57221143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610574941.5A Withdrawn CN106082541A (en) | 2016-07-11 | 2016-07-11 | A kind of quality purifying device for water of polluted-water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106082541A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107381792A (en) * | 2017-07-21 | 2017-11-24 | 博天环境集团股份有限公司 | A kind of double self-loopa integration MBR reactors |
| CN108178458A (en) * | 2018-02-02 | 2018-06-19 | 宁波大学 | A kind of polluted water purification processing unit |
| CN111302550A (en) * | 2019-12-11 | 2020-06-19 | 莫玲 | Sewage treatment device with microorganism gathering function |
-
2016
- 2016-07-11 CN CN201610574941.5A patent/CN106082541A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107381792A (en) * | 2017-07-21 | 2017-11-24 | 博天环境集团股份有限公司 | A kind of double self-loopa integration MBR reactors |
| CN107381792B (en) * | 2017-07-21 | 2020-06-19 | 博天环境集团股份有限公司 | Double-self-circulation integrated MBR (membrane bioreactor) |
| CN108178458A (en) * | 2018-02-02 | 2018-06-19 | 宁波大学 | A kind of polluted water purification processing unit |
| CN111302550A (en) * | 2019-12-11 | 2020-06-19 | 莫玲 | Sewage treatment device with microorganism gathering function |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104528932B (en) | A kind of advanced treatment of wastewater denitrification bio-filter apparatus system and process technique | |
| CN109970289A (en) | A kind of urban wastewater treatment mentions mark advanced treatment process and device | |
| CN108271730A (en) | A kind of low-carbon zero-emission industrial circulating water cultivating system based on anaerobic denitrifying | |
| CN206127067U (en) | Container formula sludge -biofilm intergrowth integrative sewage treatment device | |
| CN105000722B (en) | A kind of active filter preparation system removing ammonia nitrogen in eliminating water for catalysis oxidation | |
| CN106082541A (en) | A kind of quality purifying device for water of polluted-water | |
| CN108383337A (en) | A kind of sewage diafiltration clean processing method | |
| CN205473179U (en) | Integrate sewage treatment system | |
| CN106348441A (en) | Carbon-nitrogen separation type bottom incoming water artificial rapid infiltration system and sewage treatment method thereof | |
| CN106673257A (en) | Micropolluted raw water treatment integrated plant | |
| CN107777773A (en) | A kind of batch-type exchange cycles method for activated sludge wastewater treatment | |
| CN108178458A (en) | A kind of polluted water purification processing unit | |
| RU2554575C2 (en) | Deep purification and decontamination of natural waters and waters containing anthropogenic and man-caused pollutants | |
| CN205893002U (en) | Pollute water purification device of water | |
| CN209039279U (en) | A kind of organic pollution aquifer dystopy Ecosystem restoration system | |
| CN208029987U (en) | A kind of low-carbon zero-emission industrial circulating water cultivating system based on anaerobic denitrifying | |
| CN103449665B (en) | A kind of polluted water land biogenic sediment filtering system for mud-water separation | |
| CN106277593A (en) | A kind of integrated domestic sewage treatment system | |
| CN207031192U (en) | A kind of system for handling waste erythromycin producing water | |
| CN205442762U (en) | Light biological filter | |
| CN206570169U (en) | Water body in lake in-situ purification system | |
| CN215250251U (en) | Multistage water body remediation system | |
| CN210620520U (en) | Urban river sewage ecological restoration system | |
| CN205820982U (en) | A kind of integration combined biological filter tank | |
| CN109111054A (en) | A kind of organic pollution aquifer dystopy Ecosystem restoration system and ecological restoring method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20161109 |
|
| WW01 | Invention patent application withdrawn after publication |