CN104817229B - A kind of bamboo product Waste Water Treatment - Google Patents
A kind of bamboo product Waste Water Treatment Download PDFInfo
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- CN104817229B CN104817229B CN201510179103.3A CN201510179103A CN104817229B CN 104817229 B CN104817229 B CN 104817229B CN 201510179103 A CN201510179103 A CN 201510179103A CN 104817229 B CN104817229 B CN 104817229B
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Abstract
The present invention relates to a kind of bamboo product Waste Water Treatment, including wastewater equalization pond, strengthening flotation tank, ozone oxidation sedimentation tank, deflector type anoxia anaerobic reation pool, aerobic contact oxidation pond, second pond and sand filter；Strengthening flotation tank sequentially consists of silt particle district, mixed zone and Disengagement zone；Ozone oxidation sedimentation tank includes that aeration mixed zone and settling zone, deflector type anoxia anaerobic reation pool include double oxygen section, anoxia section and the anaerobism section being separated into by deflection plate；Aerobic contact oxidation pond is provided with water inlet pipe, water distribution pyrometric cone and aeration regulator control system；Waste water is adjusted pond and enters strengthening flotation tank removal scum silica frost, then waste water enters ozone oxidation sedimentation tank, the oxidized decomposition of pollutant, enter back into deflector type anoxia anaerobic reation pool, aerobic contact oxidation pond carries out anoxia, anaerobic and aerobic reaction, through precipitation and filter after qualified discharge.
Description
Technical field
The present invention relates to technical field of waste water processing, be specifically related to a kind of bamboo product Waste Water Treatment.
Background technology
In recent years, bamboo industry develops rapidly, and during bamboo product drawing process, bamboo silk needs through dioxygen
The steaming and decocting of water processes, to reach the effect such as anticorrosion, mothproof, bleaching, and the bamboo product waste water tool that this stage produces
There are organic concentration high (20000-50000mg/L), pH value low (2.5-5), with features such as certain colourities.
In bamboo product waste water, pollutant component is complicated, and such waste water mainly contains cell serosity class material, saccharide, organic
Acid, aminoacid, Folium Bambosae flavone class, tannins, plant pigment class, long chain alkane class, benzene class and esters etc.
Pollutant.It is directly discharged into water body after bamboo product waste water is unprocessed, the severe contamination of surface water can be caused, and
In the area that some bamboo product processing enterprise density is bigger, even subsoil water has been contaminated.Therefore, as
What handles bamboo product waste water well effectively to keeping ecological environment, guaranteeing that the sustainable development of bamboo product industry has
Significant.
Due to the impact of the many factors such as cost, operability and treatment effect, bamboo product waste water is the most uncomfortable
Close and use single physico-chemical process or bioanalysis to process, and it is also contemplated that the group technology of multiple method.
Probe into effective and feasible bamboo product waste water treatment process, to solve the ecology that Bamboo Industry Development is caused
Environmental problem, thus the sustainable development for this industry provides technical support.
Summary of the invention
The technical problem to be solved in the present invention is: in order to solve the difficult problem during above-mentioned bamboo product waste water processes, this
Invention provides a kind of bamboo product Waste Water Treatment.
The technical solution adopted for the present invention to solve the technical problems is: a kind of bamboo product Waste Water Treatment,
Including wastewater equalization pond, strengthening flotation tank, ozone oxidation sedimentation tank, deflector type anoxia anaerobic reation pool, good
Oxygen contact-oxidation pool, second pond and sand filter；Described wastewater equalization pond, strengthening flotation tank, ozone oxidation are sunk
Pond, shallow lake, deflector type anoxia anaerobic reation pool, aerobic contact oxidation pond, second pond and sand filter are sequentially communicated.
Described wastewater equalization pond includes water inlet pipe and outlet pipe, for regulating water quality and the water of bamboo product waste water
Amount.
Described strengthening flotation tank includes water inlet pipe and the outlet pipe of water, described strengthening after discharging process
Flotation tank sequentially consists of silt particle district, mixed zone and Disengagement zone；Described Disengagement zone include gathering ground and
It is positioned at Nei Jizha district, gathering ground；It is provided with aeration plate between silt particle district and the mixed zone of described strengthening flotation tank,
Described aeration plate be arranged over water distribution branch pipe, described water distribution branch pipe connects water inlet pipe, described aeration
Dish connects the blower fan having outside strengthening flotation tank by aeration tube；It is provided with three phase separator in described Disengagement zone,
Described three phase separator include deflector and be positioned at below deflector with deflector with the use of triangle water conservancy diversion
Ring, described triangle guide ring be arranged on strengthening flotation tank inwall on, the top of described deflector with point
Shape from district is identical, and the bottom of described deflector is horn-like, the internal diameter of the bottom of described deflector
Internal diameter more than triangle guide ring；The top of described Disengagement zone outer wall is provided with overfalling weir, described overfalling weir
It is connected with outlet pipe；Described Ji Zhaqu is laid with scum board and scum trough；When waste water overflows from the bottom up, water
Entered the bottom of deflector together with scum silica frost by triangle guide ring, scum silica frost continues up to enter Ji Zhaqu, water
By the entrance gathering ground, gap between deflector and triangle guide ring；The effect processed for waste water is more preferable,
Described water distribution branch pipe is arranged to concentric circles or cross shape, and water distribution branch pipe has horizontal radiation water outlet
Mouthful；Further, described aeration plate is the pore type aeration plate being evenly arranged with micropore；Due to water, precipitation
The density of thing is different, realizes separating under three phase separator effect；In order to discharge the precipitate after process, institute
It is provided with sediment discharge valve bottom the strengthening flotation tank stated.
The outlet pipe of described strengthening flotation tank connects with the water inlet pipe of ozone oxidation sedimentation tank.
Described ozone oxidation sedimentation tank includes that aeration mixed zone and settling zone, aeration are provided with bottom mixed zone
Ozonation aerated dish, described ozonation aerated dish be arranged over water distribution branch pipe, described water distribution branch pipe connect into
Water pipe, described ozonation aerated dish is connected by aeration tube the blower fan outside ozone oxidation sedimentation tank, and blower fan leads to
Piping connection ozonator；Being provided with baffle plate in described settling zone, this baffle plate is formed with the inwall of sedimentation tank
Enter the waste water runner of settling zone as waste water, the exit of settling zone is provided with three phase separator, settling zone
Outlet top is provided with overfalling weir, the tapered structure of settling zone bottom design, is provided with spoil disposal bottom settling zone
Valve.
Described deflector type anoxia anaerobic reation pool is included the double oxygen section, the anoxia section that are separated into by deflection plate and detests
Oxygen section, described double oxygen section head end is provided with the water inlet pipe for feeding waste water, hold concurrently oxygen section end and anoxia section head end
Connection, anoxia section end connects with anaerobism section head end, and described anoxia section and anaerobism section are intake side deflection plate
Bottom is provided with the corner of 45 degree, the percussion produced during to avoid current to enter, thus plays buffered water
Stream and the effect of water distribution uniformity；Anaerobism section end is provided with three phase separator and overfalling weir, and overfalling weir connects water outlet
Pipe；Described double oxygen section, anoxia section and the tapered structure of anaerobism section bottom design, pyramidal structure connects mud row
Put valve；The double oxygen section of described deflector type anoxia anaerobic reation pool, anoxia section become circular cone with anaerobism section upper cover design
Shape structure, conical structure top is designed with independent methane waste product discharge.Described double oxygen section, anoxia section
It is designed with filler with in anaerobism section.
In described aerobic contact oxidation pond, middle and lower part is provided with water inlet pipe, and described water inlet pipe bottom is provided with water distribution three
Pyramid；Described aerobic contact oxidation pond is provided with aeration regulator control system, described aeration regulator control system include aeration plate,
Aerator and dissolved oxygen sensing regulation device；Further, described aeration plate is be evenly arranged with micropore micro-
Cellular type aeration plate, described aeration plate connects aerator by aeration tube, and aerator is arranged on aerobic contact oxidation
Outside pond, the top in aerobic contact oxidation pond, waste water underwater arrange dissolved oxygen sensing regulation device, described molten
Solve oxygenation measurement regulation device according to oxygen content regulation and control aerator work；Described aerobic contact oxidation pond is built-in with to be filled out
Material；The water outlet in described aerobic contact oxidation pond is laid with downflow weir.
The outlet pipe in described aerobic contact oxidation pond connects second pond, is provided with sludge recirculation system bottom second pond,
A part of sludge reflux is to deflector type anoxia anaerobic reation pool.
Water after sedimentation in secondary sedimentation tank processes enters sand filter through downflow weir, qualified discharge after filtration.
A kind of method using above-mentioned bamboo product Waste Water Treatment to carry out waste water process, has following steps:
1. bamboo product waste water enters wastewater equalization pond regulating water quality and the water yield by water inlet pipe.
The most then waste water enters the middle and lower part of strengthening flotation tank Disengagement zone by water inlet pipe；It is positioned at strengthening flotation tank
Aeration plate below water inlet pipe produces a large amount of tiny bubbles makes the solids in waste water produce friction, removes solid
Other pollutant on thing；The tiny bubble that aeration plate produces and supernatant adhere to form mixture and make at buoyancy
Using lower rising, under the effect of strengthening flotation tank Disengagement zone three phase separator, mixture rises to Ji Zhaqu,
Under the effect of scum board, scum silica frost enters scum trough cleaned outward transport；Precipitate under gravity under
Sink to strengthen the silt particle district of flotation tank bottom, discharged by the sediment discharge valve bottom strengthening flotation tank；Point
Water after processing enters strengthening flotation tank gathering ground under strengthening flotation tank three-phase separation area deflector effect,
The water inlet pipe of ozone oxidation sedimentation tank is connected by overfalling weir, outlet pipe and connecting tube.
3. waste water enters ozone oxidation sedimentation tank by water inlet pipe and the water distribution branch pipe of ozone oxidation sedimentation tank
Middle and lower part；It is positioned at a large amount of tiny bubbles of generation of the ozonation aerated dish below ozone oxidation sedimentation tank water distribution branch pipe to make
Solids in waste water rubs further, the macromolecular substances in waste water is oxidized to be prone to absorb and inhale simultaneously
Attached small-molecule substance, the waste water after oxidation Decomposition enters settling zone, and the three phase separator of settling zone realizes mud
Water separates；Mud sinks to the bottom of ozone oxidation sedimentation tank settling zone under gravity, by bottom
Mud valve discharge；Waste water connects deflector type anoxia anaerobic reation pool by overfalling weir, outlet pipe with connecting tube
Water inlet pipe.
4. waste water by deflector type anoxia anaerobic reation pool hold concurrently oxygen section water inlet pipe enter deflector type anoxia anaerobism anti-
The bottom of Ying Chi；Waste water enters deflector type anoxia anaerobic reation pool tailing edge deflection plate and advances up and down, passes sequentially through
The Sludge Bed of each reative cell of oxygen section, anoxia section and the anaerobism section held concurrently, the mud in reaction tank is along with waste water
Up and down flowing and biogas rise effect and move, the barrier effect of deflection plate and the settlement action of mud self
The flow velocity making again mud reduces, and the most substantial amounts of mud is all trapped within reaction tank, the micro-life in reaction tank
Thing is fully contacted with the Organic substance in waste water.The heterotrophic bacteria of the amphimicrobe of oxygen section, anoxia section and the anaerobism section held concurrently will
Hydrolysis of organic matter in waste water is organic acid, makes larger molecular organics be decomposed into small organic molecule, insoluble
Organic substance change into dissolved organic matter.
5. the three phase separator that the waste water after anaerobic reaction is provided with at anaerobism section end realizes mud, water, methane gas
Separation, mud sinks to the bottom of deflector type anoxia anaerobic reation pool, unnecessary dirt under gravity
Mud is discharged by the mud discharging valve of bottom；The methane waste product that deflector type anoxia anaerobic reation pool produces is by anti-
Ying Chi top discharge collects discharge；Waste water after process is connected with connecting tube by overfalling weir, outlet pipe
The water inlet pipe of oxygen contact-oxidation pool.
6. waste water enters the middle and lower part in aerobic contact oxidation pond by water inlet pipe, under the effect of water distribution pyrometric cone
Water distribution uniformity, described aeration plate is the pore type aeration plate being evenly arranged with micropore, produces substantial amounts of micro-gas
Bubble, described dissolved oxygen sensing regulation device is according to oxygen content regulation and control aerator work, it is ensured that aerobic contact oxidation
Dissolved oxygen in water is more than 2mg/L, and the waste water after process is flowed out by downflow weir and outlet pipe.
7. the outlet pipe in aerobic contact oxidation pond connects the water distributor of second pond, the precipitating sludge of second pond one
Dividing sludge reflux to deflector type anoxia anaerobic reation pool, a part is as excess sludge.
8. the water after sedimentation in secondary sedimentation tank processes enters sand filter through downflow weir, qualified discharge after filtration.
9. strengthen flotation tank, ozone oxidation sedimentation tank, deflector type anoxia anaerobic reation pool, second pond discharge
Transport outward after excess sludge dehydration.
The invention has the beneficial effects as follows: present configuration is simple, and cost is relatively low, bamboo product waste water is processed tool
There are reasonable depth effect, convenient management.
Accompanying drawing explanation
The present invention is further described with embodiment below in conjunction with the accompanying drawings.
Fig. 1 is the structural representation of embodiment of the present invention strengthening flotation tank.
In Fig. 1: 1. strengthening flotation tank, 1-1. strengthens flotation tank water inlet pipe, 1-2. silt particle district, and 1-3. mixes
Closing district, 1-4. gathering ground, 1-5. Ji Zhaqu, 1-6. strengthen flotation tank aeration plate, and 1-7. strengthens flotation tank
Water distribution branch pipe, 1-8. aerator and gas flowmeter, 1-9. strengthens flotation tank three phase separator, and 1-10. overflows
Mill weir, 1-11. scum board, 1-12. scum trough, 1-13. sediment discharge valve.
Fig. 2 is the structural representation of embodiment of the present invention ozone oxidation sedimentation tank.
In Fig. 2: 2. ozone oxidation sedimentation tank, 2-1. aeration mixed zone, 2-2. settling zone, 2-3. ozone
Aeration plate, 2-4. water distribution branch pipe, 2-5. water inlet pipe, 2-6. ozone aerator and gas flowmeter, 2-7. is smelly
Oxygen Generator, 2-8. baffle plate, 2-9. ozone oxidation sedimentation tank three phase separator, 2-10. ozone oxidation sedimentation tank
Overfalling weir, 2-11. mud valve.
Fig. 3 is the structural representation of embodiment of the present invention deflector type anoxia anaerobic reation pool.
In Fig. 3: 3. deflector type anoxia anaerobic reation pool, 3-1. deflection plate, 3-2. holds concurrently oxygen section, 3-3. anoxia
Section, 3-4. anaerobism section, 3-5. deflector type anoxia anaerobic reation pool water inlet pipe, 3-6. deflector type anoxia anaerobism
Reaction tank three phase separator, 3-7. deflector type anoxia anaerobic reation pool overfalling weir, 3-8. mud discharging valve, 3-9.
Upper cover, 3-10. discharge, 3-11. filler.
Fig. 4 is the structural representation in embodiment of the present invention aerobic contact oxidation pond.
In Fig. 4: 4. aerobic contact oxidation pond, 4-1. aerobic contact oxidation pond water inlet pipe, 4-2. water distribution three
Pyramid, 4-3. aeration regulator control system, 4-4. filler, 4-5. aerobic contact oxidation pond downflow weir.
Fig. 5 is the process chart of the embodiment of the present invention.
Detailed description of the invention
In conjunction with the accompanying drawings, the present invention is further detailed explanation.These accompanying drawings are the signal of simplification
Figure, illustrates the basic structure of the present invention the most in a schematic way, and therefore it only shows the structure relevant with the present invention
Become.
Embodiment
As shown in Fig. 1～Fig. 5, one bamboo product Waste Water Treatment of the present invention, including wastewater equalization pond, by force
Change flotation tank 1, ozone oxidation sedimentation tank 2, deflector type anoxia anaerobic reation pool 3, aerobic contact oxidation pond 4,
Second pond and sand filter；Described wastewater equalization pond, strengthening flotation tank 1, ozone oxidation sedimentation tank 2, deflector type
Anoxia anaerobic reation pool 3, aerobic contact oxidation pond 4, second pond and sand filter are sequentially communicated.
Described wastewater equalization pond includes water inlet pipe and outlet pipe, for regulating water quality and the water of bamboo product waste water
Amount.
Described strengthening flotation tank 1 include water inlet pipe 1-1 and after discharging process the outlet pipe of water, described
Strengthening flotation tank sequentially consist of silt particle district 1-2, mixed zone 1-3 and Disengagement zone；Described Disengagement zone
Including gathering ground 1-4 and be positioned at Nei Jizha district, gathering ground 1-5；The silt particle district 1-2 of described strengthening flotation tank and
Be provided with aeration plate 1-6 between the 1-3 of mixed zone, described aeration plate be arranged over water distribution branch pipe 1-7, institute
The water distribution branch pipe stated connects water inlet pipe 1-1, described aeration plate 1-6 has strengthening flotation tank by aeration tube connection
Outer blower fan 1-8.Three phase separator 1-9, described three phase separator 1-9 bag it is provided with in described Disengagement zone
Include deflector and be positioned at below deflector with deflector with the use of triangle guide ring, described triangle water conservancy diversion
Ring is arranged on the inwall of strengthening flotation tank, and the top of described deflector is identical with the shape of Disengagement zone, institute
The bottom of the deflector stated is horn-like, and the internal diameter of the bottom of described deflector is interior more than triangle guide ring
Footpath；The top of described Disengagement zone outer wall is provided with overfalling weir 1-10, described overfalling weir 1-10 and outlet pipe phase
Even；Described Ji Zha district 1-5 is laid with scum board 1-11 and scum trough 1-12；When waste water overflows from the bottom up,
Water enters the bottom of deflector together with scum silica frost by triangle guide ring, and scum silica frost continues up to enter Ji Zhaqu
1-5, water is by entrance gathering ground, the gap 1-4 between deflector and triangle guide ring；For waste water process
Effect is more preferable, and described water distribution branch pipe 1-7 is arranged to concentric circles or cross shape, and water distribution branch pipe has
There is horizontal radiation outlet；Further, described aeration plate is the pore type aeration plate being evenly arranged with micropore；
Due to water, sedimentary density difference, realize separating under three phase separator effect；After discharging process
Precipitate, be provided with sediment discharge valve 1-13 bottom described strengthening flotation tank.
The outlet pipe of described strengthening flotation tank 1 connects with the water inlet pipe 2-5 of ozone oxidation sedimentation tank 2.
Described ozone oxidation sedimentation tank 2 includes aeration mixed zone 2-1 and settling zone 2-2, at the bottom of aeration mixed zone
Portion is provided with ozonation aerated dish 2-3, described ozonation aerated dish be arranged over water distribution branch pipe 2-4, described
Water distribution branch pipe 2-4 connects water inlet pipe 2-5, described ozonation aerated dish 2-3 has ozone oxygen by aeration tube connection
Change the blower fan outside sedimentation tank, blower and pipeline connection ozonator 2-7；It is provided with baffle plate in described settling zone
2-8, this baffle plate forms the waste water runner as waste water entrance settling zone, going out of settling zone with the inwall of sedimentation tank
Being provided with three phase separator 2-9 at Kou, the outlet top of settling zone is provided with overfalling weir 2-10, sets bottom settling zone
Count tapered structure, bottom settling zone, be provided with mud valve 2-11.
Described deflector type anoxia anaerobic reation pool 3 includes double oxygen section 3-2, the anoxia being separated into by deflection plate 3-1
Section 3-3 and anaerobism section 3-4, described double oxygen section 3-2 head end is provided with the water inlet pipe 3-5 for feeding waste water, oxygen of holding concurrently
Section 3-2 end connects with anoxia section 3-3 head end, and anoxia section 3-3 end connects with anaerobism section 3-4 head end, described
The bottom of anoxia section 3-3 and anaerobism section 3-4 water inlet side deflection plate is provided with the corner of 45 degree, to avoid current
The percussion produced during entrance, thus play buffering current and the effect of water distribution uniformity；Anaerobism section 3-4 end
Being provided with three phase separator 3-6 and overfalling weir 3-7, overfalling weir 3-7 connects outlet pipe；Described double oxygen section 3-2, lack
Oxygen section 3-3 and the tapered structure of anaerobism section 3-4 bottom design, pyramidal structure connects mud discharging valve 3-8；Described
The upper cover 3-9 of double oxygen section, anoxia section and the anaerobism section of deflector type anoxia anaerobic reation pool is designed to cone knot
Structure, conical structure top is designed with independent methane waste product discharge 3-10；Described double oxygen section, anoxia section
Be designed with filler 3-11 in anaerobism section.
In described aerobic contact oxidation pond 4, middle and lower part is provided with water inlet pipe 4-1, and described water inlet pipe 4-1 bottom sets
There is water distribution pyrometric cone 4-2；Described aerobic contact oxidation pond 4 is provided with aeration regulator control system 4-3, and described aeration is adjusted
Ore-controlling Role 4-3 includes aeration plate, aerator and dissolved oxygen sensing regulation device；Further, described aeration
Dish is the pore type aeration plate being evenly arranged with micropore.Described aeration plate connects aerator, drum by aeration tube
Blower fan is arranged on outside aerobic contact oxidation pond, and the top in aerobic contact oxidation pond, waste water underwater arrange dissolving
Oxygenation measurement regulation device, described dissolved oxygen sensing regulation device is according to oxygen content regulation and control aerator work；Described
Aerobic contact oxidation pond is built-in with filler 4-4；The exit in described aerobic contact oxidation pond is laid with downflow weir
4-5。
The outlet pipe in described aerobic contact oxidation pond 4 connects second pond, is provided with sludge reflux system bottom second pond
System, in a part of sludge reflux to deflector type anoxia anaerobic reation pool 3, a part is excess sludge.
Water after sedimentation in secondary sedimentation tank processes enters sand filter through downflow weir, qualified discharge after filtration.
A kind of method using above-mentioned bamboo product Waste Water Treatment to carry out waste water process, has following steps:
1. bamboo product waste water enters wastewater equalization pond regulating water quality and the water yield by water inlet pipe.
The most then waste water enters the middle and lower part of strengthening flotation tank Disengagement zone by water inlet pipe 1-1；It is positioned at strengthening gas
Aeration plate 1-6 below the water inlet pipe of floating pond produces a large amount of tiny bubbles makes the solids in waste water produce friction,
Remove other pollutant on solids；The tiny bubble that aeration plate 1-6 produces and supernatant adhere to be formed and mix
Fit rising under buoyancy, under the effect of strengthening flotation tank three phase separator 1-9, mixture rises
To Ji Zha district 1-5, under the effect of scum board 1-11, scum silica frost enters scum trough 1-12 cleaned outward transport；
Precipitate sinks to strengthen the silt particle district 1-2 of flotation tank bottom under gravity, at the bottom of strengthening flotation tank
The sediment discharge valve 1-13 in portion discharges；Water after separating treatment is at strengthening flotation tank three-phase separation area deflector
Effect is lower enters strengthening flotation tank gathering ground 1-4, connects smelly by overfalling weir 1-10, outlet pipe and connecting tube
The water inlet pipe 2-5 of oxygen oxidization and sedimentation basin.
3. waste water is sunk by ozone oxidation sedimentation tank water inlet pipe 2-5 and water distribution branch pipe 2-4 entrance ozone oxidation
The middle and lower part in pond, shallow lake 2；It is positioned at the ozonation aerated dish 2-3 below ozone oxidation sedimentation tank water distribution branch pipe and produces big
Amount tiny bubble makes the solids in waste water rub further, the macromolecular substances in waste water is oxidized to simultaneously
Being prone to absorb and the small-molecule substance of absorption, the waste water after oxidation Decomposition enters the waste water runner of settling zone, heavy
The three phase separator 2-9 in shallow lake district realizes mud-water separation；Mud sinks to ozone oxidation under gravity and sinks
The bottom of pond, shallow lake settling zone 2-2, is discharged by the mud valve 2-11 of bottom；Waste water by overfalling weir 2-10,
Outlet pipe connects the water inlet pipe 3-5 of deflector type anoxia anaerobic reation pool with connecting tube.
4. waste water by deflector type anoxia anaerobic reation pool hold concurrently oxygen section water inlet pipe 3-5 enter deflector type anoxia detest
The bottom of oxygen reaction tank 3；Waste water enters deflector type anoxia anaerobic reation pool tailing edge deflection plate and advances up and down, depends on
The Sludge Bed of secondary each reative cell by double oxygen section 3-2, anoxia section 3-3 and anaerobism section 3-4, in reaction tank
Mud along with waste water up and down flowing and biogas rise effect and move, the barrier effect of deflection plate and dirt
The settlement action of mud self makes again the flow velocity of mud reduce, and the most substantial amounts of mud is all trapped within reaction tank,
Microorganism in reaction tank is fully contacted with the Organic substance in waste water.The double amphimicrobe of oxygen section 3-2, anoxia section
Hydrolysis of organic matter in waste water is organic acid by the heterotrophic bacteria of 3-3 and anaerobism section 3-4, makes larger molecular organics divide
Solving is small organic molecule, and insoluble Organic substance changes into dissolved organic matter.
5. the waste water after anaerobic reaction the three phase separator 3-6 that anaerobism section 3-4 end is provided with realize mud, water,
The separation of methane gas, mud sinks to the bottom of deflector type anoxia anaerobic reation pool under gravity, many
Remaining mud is discharged by the mud discharging valve 3-8 of bottom；The methane that deflector type anoxia anaerobic reation pool produces
Waste gas collects discharge by reaction tank top discharge 3-10；Waste water is by overfalling weir, outlet pipe and connecting tube
The water inlet pipe 4-1 in connection aerobic contact oxidation pond.
6. waste water enters the middle and lower part in aerobic contact oxidation pond 4 by water inlet pipe 4-1, at water distribution pyrometric cone 4-2
Effect under water distribution uniformity, described aeration plate produces substantial amounts of microbubble, described dissolved oxygen sensing regulation and control dress
Put according to oxygen content regulation and control aerator work, it is ensured that the dissolved oxygen in aerobic contact oxidation water is more than 2mg/L,
Waste water after process is flowed out by downflow weir 4-5 and outlet pipe.
7. the outlet pipe in aerobic contact oxidation pond connects the water distributor of second pond, the precipitating sludge of second pond one
Point sludge reflux is in deflector type anoxia anaerobic reation pool 3, and a part is as excess sludge.
8. the water after sedimentation in secondary sedimentation tank processes enters sand filter through downflow weir, qualified discharge after filtration.
9. strengthening flotation tank 1, ozone oxidation sedimentation tank 2, deflector type anoxia anaerobic reation pool 3, second pond row
Transport outward after the excess sludge dehydration gone out.
With the above-mentioned desirable embodiment according to the present invention for enlightenment, by above-mentioned description, relevant staff
Completely can be without departing from carrying out various change and amendment in the range of this invention technological thought.This
The content that the technical scope of invention is not limited in description, it is necessary to come really according to right
Its technical scope fixed.
Claims (2)
1. a bamboo product Waste Water Treatment, it is characterised in that: include wastewater equalization pond, strengthening flotation tank
(1), ozone oxidation sedimentation tank (2), deflector type anoxia anaerobic reation pool (3), aerobic contact oxidation pond (4),
Second pond and sand filter；
Described regulating reservoir includes water inlet pipe and outlet pipe, for regulating water quality and the water yield of bamboo product waste water；
Described strengthening flotation tank (1) includes water inlet pipe (1-1) and for discharging the outlet pipe of water after process,
Described strengthening flotation tank sequentially consists of silt particle district (1-2), mixed zone (1-3) and Disengagement zone；Described
Disengagement zone include gathering ground (1-4) and be positioned at Nei Jizha district, gathering ground (1-5)；Described strengthening flotation tank
Aeration plate (1-6), being arranged over of described aeration plate it is provided with between silt particle district (1-2) and mixed zone (1-3)
Water distribution branch pipe (1-7), described water distribution branch pipe connects water inlet pipe (1-1), and described aeration plate (1-6) is by exposing
Trachea connects the blower fan having outside strengthening flotation tank；Three phase separator (1-9) it is provided with in described Disengagement zone, described
Three phase separator (1-9) include deflector and be positioned at below deflector with deflector with the use of triangle lead
Stream ring, described triangle guide ring be arranged on strengthening flotation tank inwall on, the top of described deflector with
The shape of Disengagement zone is identical, and the bottom of described deflector is horn-like, the bottom of described deflector interior
Footpath is more than the internal diameter of triangle guide ring；The top of described Disengagement zone outer wall is provided with overfalling weir (1-10), described
Overfalling weir (1-10) be connected with outlet pipe；Described Ji Zhaqu (1-5) is laid with scum board (1-11) and scum silica frost
Groove (1-12)；When waste water overflows from the bottom up, water is entered under deflector by triangle guide ring together with scum silica frost
Portion, scum silica frost continues up to enter Ji Zhaqu (1-5), and water is entered by the gap between deflector and triangle guide ring
Enter gathering ground (1-4)；The effect processed for waste water is more preferable, and described water distribution branch pipe (1-7) is arranged to one heart
Toroidal or cross shape, water distribution branch pipe has horizontal radiation outlet；Further, described aeration plate
It it is the pore type aeration plate being evenly arranged with micropore；Due to water, sedimentary density difference, in three phase separation
Realize under device effect separating；In order to discharge the precipitate after process, it is heavy to be provided with bottom described strengthening flotation tank
Shallow lake thing drain valve (1-13)；
Described ozone oxidation sedimentation tank (2) includes aeration mixed zone (2-1) and settling zone (2-2), and aeration mixes
Be provided with ozonation aerated dish (2-3) bottom district, described ozonation aerated dish be arranged over water distribution branch pipe (2-4),
Described water distribution branch pipe (2-4) connects water inlet pipe (2-5), and described ozonation aerated dish (2-3) is by aeration tube even
It is connected to the blower fan outside ozone oxidation sedimentation tank, blower and pipeline connection ozonator (2-7)；Described precipitation
Being provided with baffle plate (2-8) in district, this baffle plate forms the waste water stream as waste water entrance settling zone with the inwall of sedimentation tank
Road, the exit of settling zone is provided with three phase separator (2-9), and the outlet top of settling zone is provided with overfalling weir
(2-10), the tapered structure of settling zone bottom design, bottom settling zone, it is provided with mud valve (2-11)；
Described deflector type anoxia anaerobic reation pool (3) includes the double oxygen section being separated into by deflection plate (3-1)
(3-2), anoxia section (3-3) and anaerobism section (3-4), described double oxygen section (3-2) head end is provided with for supplying
Entering the water inlet pipe (3-5) of waste water, oxygen section (3-2) end of holding concurrently connects with anoxia section (3-3) head end, anoxia
Section (3-3) end connects with anaerobism section (3-4) head end；Described anoxia section (3-3) and anaerobism section (3-4)
The bottom of water inlet side deflection plate be provided with the corner of 45 degree, the impact produced during to avoid current to enter work
With, thus play buffering current and the effect of water distribution uniformity；Anaerobism section (3-4) end is provided with three phase separator
(3-6) with overfalling weir (3-7), overfalling weir (3-7) connects outlet pipe；Described double oxygen section (3-2), lack
Oxygen section (3-3) and the tapered structure of anaerobism section (3-4) bottom design, pyramidal structure connects mud discharging valve
(3-8)；The upper cover (3-9) of double oxygen section, anoxia section and the anaerobism section of described deflector type anoxia anaerobic reation pool
Being designed to conical structure, conical structure top is designed with methane waste product discharge (3-10), described double oxygen
It is designed with filler (3-11) in section, anoxia section and anaerobism section；
The interior middle and lower part of described aerobic contact oxidation pond (4) is provided with water inlet pipe (4-1), described water inlet pipe (4-1)
Bottom is provided with water distribution pyrometric cone (4-2)；Described aerobic contact oxidation pond (4) is provided with aeration regulator control system (4-3),
Described aeration regulator control system (4-3) includes aeration plate, aerator and dissolved oxygen sensing regulation device；Further,
Described aeration plate is the pore type aeration plate being evenly arranged with micropore；Described aeration plate is connected by aeration tube
Aerator, aerator is arranged on outside aerobic contact oxidation pond, the top in aerobic contact oxidation pond, the waste water water surface
Under dissolved oxygen sensing regulation device is set, described dissolved oxygen sensing regulation device regulates and controls aerator according to oxygen content
Work；Described aerobic contact oxidation pond is built-in with filler (4-4)；The exit in described aerobic contact oxidation pond
It is laid with downflow weir (4-5)；
The outlet pipe of described aerobic contact oxidation pond (4) connects second pond, is provided with sludge reflux bottom second pond
System, a part of sludge reflux is to deflector type anoxia anaerobic reation pool (3)；
Water after sedimentation in secondary sedimentation tank processes enters sand filter through downflow weir, qualified discharge after filtration.
2. use the method that bamboo product Waste Water Treatment as claimed in claim 1 carries out waste water process,
There are following steps:
1. bamboo product waste water enters wastewater equalization pond regulating water quality and the water yield by water inlet pipe；
The most then waste water enters the middle and lower part of strengthening flotation tank Disengagement zone by water inlet pipe (1-1)；It is positioned at strengthening
Aeration plate (1-6) below flotation tank water inlet pipe produces a large amount of tiny bubble makes the solids generation in waste water rub
Wipe, remove other pollutant on solids；The tiny bubble that aeration plate (1-6) produces adheres to supernatant
Form mixture to rise under buoyancy, under the effect of strengthening flotation tank three phase separator (1-9), mixed
Zoarium rises to Ji Zhaqu (1-5), and under the effect of scum board (1-11), scum silica frost enters scum trough (1-12)
And cleaned outward transport；Precipitate sinks to strengthen the silt particle district (1-2) of flotation tank bottom under gravity,
Discharged by the sediment discharge valve (1-13) bottom strengthening flotation tank；Water after separating treatment is at strengthening gas
Enter strengthening flotation tank gathering ground (1-4) under the deflector effect of Fu Chi three-phase separation area, pass through overfalling weir
(1-10), outlet pipe connects the water inlet pipe (2-5) of ozone oxidation sedimentation tank with connecting tube；
3. waste water enters ozone by ozone oxidation sedimentation tank water inlet pipe (2-5) and water distribution branch pipe (2-4)
The middle and lower part of oxidization and sedimentation basin (2)；It is positioned at the ozonation aerated dish below ozone oxidation sedimentation tank water distribution branch pipe
(2-3) producing a large amount of tiny bubble makes the solids in waste water rub further, simultaneously big point in waste water
Sub-material is oxidized to be prone to absorb and the small-molecule substance of absorption, and the waste water after oxidation Decomposition enters settling zone
Waste water runner, the three phase separator (2-9) of settling zone realizes mud-water separation；Mud under gravity under
Sink to the bottom of ozone oxidation sedimentation tank settling zone (2-2), discharged by the mud valve (2-11) of bottom；
Waste water enters the water inlet pipe of deflector type anoxia anaerobic reation pool by overfalling weir (2-10), outlet pipe and connecting tube
(3-5)；
4. waste water by deflector type anoxia anaerobic reation pool hold concurrently oxygen section water inlet pipe (3-5) enter deflector type anoxia
The bottom of anaerobic reation pool (3)；Waste water enters deflector type anoxia anaerobic reation pool tailing edge deflection plate (3-1)
Advance up and down, pass sequentially through double oxygen section (3-2), anoxia section (3-3) and anaerobism section (3-4) each instead
Answering the Sludge Bed of room, the mud in reaction tank moves along with flowing up and down and the effect of biogas rising of waste water,
The barrier effect of deflection plate (3-1) and the settlement action of mud self make again the flow velocity of mud reduce, the most greatly
The mud of amount is all trapped within reaction tank, and the microorganism in reaction tank is fully contacted with the Organic substance in waste water；
The heterotrophic bacteria of the amphimicrobe of oxygen section (3-2), anoxia section (3-3) and the anaerobism section (3-4) held concurrently is by waste water
Hydrolysis of organic matter is organic acid, makes larger molecular organics be decomposed into small organic molecule, insoluble Organic substance
Change into dissolved organic matter；
5. the three phase separator (3-6) that the waste water after anaerobic reaction is provided with at anaerobism section (3-4) end realizes
Mud, water, the separation of methane gas, mud sinks to deflector type anoxia anaerobic reation pool under gravity
Bottom, unnecessary mud is discharged by the mud discharging valve (3-8) of bottom；Deflector type anoxia anaerobic reation pool
The methane waste product produced collects discharge by reaction tank top discharge (3-10)；Waste water by overfalling weir,
Outlet pipe and connecting tube enter the water inlet pipe in aerobic contact oxidation pond (4)；
6. waste water enters the middle and lower part in aerobic contact oxidation pond (4) by water inlet pipe (4-1), at water distribution three
Water distribution uniformity under the effect of pyramid (4-2), described aeration plate is the pore type aeration being evenly arranged with micropore
Dish, produces substantial amounts of microbubble, and described dissolved oxygen sensing regulation device works according to oxygen content regulation and control aerator,
Guarantee that the dissolved oxygen in aerobic contact oxidation water passes through downflow weir (4-5) more than 2mg/L, the waste water after process
Flow out with outlet pipe；
7. the outlet pipe of aerobic contact oxidation pond (4) connects the water distributor of second pond, the precipitating sludge of second pond
A part of sludge reflux is in deflector type anoxia anaerobic reation pool (3), and a part is as excess sludge；
8. the water after sedimentation in secondary sedimentation tank processes enters sand filter, qualified discharge after filtration through second pond downflow weir；
9. strengthen flotation tank (1), ozone oxidation sedimentation tank (2), deflector type anoxia anaerobic reation pool (3),
Transport outward with after the excess sludge dehydration of second pond discharge.
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| CN201510179103.3A CN104817229B (en) | 2015-04-15 | 2015-04-15 | A kind of bamboo product Waste Water Treatment |
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| CN105152477A (en) * | 2015-09-08 | 2015-12-16 | 常州大学 | Rice winery wastewater treatment system |
| CN106495394A (en) * | 2016-10-20 | 2017-03-15 | 安吉逢春污水处理有限公司 | A kind of bamboo product processing waste water processing system and its processing method |
| CN111056722B (en) * | 2018-10-17 | 2024-03-19 | 中电建生态环境集团有限公司 | Sludge treatment equipment |
| CN112960847A (en) * | 2021-01-28 | 2021-06-15 | 常州大学 | Integrated wood cooking wastewater treatment device and method |
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| CN202297310U (en) * | 2011-10-21 | 2012-07-04 | 波鹰(厦门)科技有限公司 | Treatment device of hair product waste water |
| CN102795747A (en) * | 2012-08-29 | 2012-11-28 | 重庆钢铁(集团)有限责任公司 | Waste water treatment process |
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Effective date of registration: 20201109 Address after: 221300 Chahe Town New District, Pizhou City, Xuzhou City, Jiangsu Province Patentee after: Pizhou Borui Investment Management Co.,Ltd. Address before: Gehu Lake Road Wujin District 213164 Jiangsu city of Changzhou province No. 1 Patentee before: CHANGZHOU University |