CN108975635A - Purifying domestic sewage processing equipment - Google Patents
Purifying domestic sewage processing equipment Download PDFInfo
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- CN108975635A CN108975635A CN201811023825.XA CN201811023825A CN108975635A CN 108975635 A CN108975635 A CN 108975635A CN 201811023825 A CN201811023825 A CN 201811023825A CN 108975635 A CN108975635 A CN 108975635A
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- 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
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- 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
- C02F3/02—Aerobic processes
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Abstract
The invention discloses purifying domestic sewage processing equipments, including sequentially connected water inlet pipe, conditioning tank, biochemistry pool, membrane biological reaction pond, collection processing pond and outlet pipe;Membrane biological reaction pond is equipped with film biofilter and several sliding bars, and film biofilter, which slides up and down, to be connected on sliding bar.Realize effective purification of sanitary sewage;The cleaning to itself is achieved that by up and down motion of the film biofilter in membrane biological reaction pond, without interrupting the process flow of sewage, can be carried out cleaning treatment at any time, be improved sewage treating efficiency, increase service life of equipment.
Description
Technical field
The present invention relates to technical field of sewage more particularly to purifying domestic sewage processing equipments.
Background technique
With the economic fast development in China city, the sewage quantity for producing and living in city and generate is also gradually
Increase, sanitary sewage discharge amount is continuously increased, it has also become one of primary pollution source of water body.Existing sanitary sewage disposal side
Method mostly uses greatly traditional AO Process processing mode, takes up a large area, and energy consumption is high, and installation is complicated, and its treatment effect
Generally, treated, and water outlet can not reach the best standard level-one A standard of existing country.And emerging membrane biological reaction technique
Method processing mode constantly improve in experimental study and engineering practice, net to become more mature at present and more common water quality
Change technology.
Technical solution CN204224400U provides a kind of sanitary sewage integrated equipment for wastewater treatment, including integrated pond, one
Changing pond includes the moving bed biofilm reactor pond (MBBR) and the pond membrane bioreactor (MBR), and is set between the pond MBBR and the pond MBR
There are the partition in carry potential overflow hole, sewage Unidirectional relief between the pond MBBR and the pond MBR;Sludge is additionally provided between the pond MBBR and the pond MBR
Return pipe;The pond MBBR is connect with air blower respectively with the pond MBR.The technical solution keeps the pond MBBR integrated with the pond MBR, reduces land occupation
Area, good sewage processing effect.But at work, on the filter membrane of MBBR and MBR can continuous adsorbing contaminant, with using the time
Increase the filter efficiency that can reduce MBBR and MBR, influences sewage treating efficiency.
Technical solution CN205821114U discloses domestic sewage processing system, the machinery being successively discharged into including sanitary sewage
Grid, conditioning tank, anaerobic pond, bio-contact oxidation reaction tank, secondary settling tank, the pond MBR, more medium filter, active carbon filter,
Sterilization pool is set on sterilization pool there are two discharge outlet, a discharge outlet connection discharge pond, another discharge outlet connects reuse pool,
Reuse pool supplies water to using water spot;The top of sterilization pool be equipped with chlorine dioxide feed bin, chlorine dioxide feed bin be equipped with display screen, two
The discharge port of chlorine monoxid feed bin is equipped with the baffle for closing the discharge port, and display screen shows the time when baffle is opened, also
Including backwashing pump, one end of backwashing pump connects sterilization pool, and the other end connects more medium filter, active carbon filter, further includes
The blower being connected with the life contact oxidation pond.The technical solution is provided with backwash structure, can be to filter just
Row backwash is to achieve the effect that clean filter.But normal filtration step need to be suspended when backwashing, sewage purification is will affect and set
Standby day-to-day operation is more suitable as the deep purifying of long periodicity.
Sewage disposal system mentioned by above scheme, has following defects that
One, only setting or not set back purge system, MBR can not effectively be rinsed, easily reduction MBR service life;
Two, by back purge system, reach the cleaning of MBR, greatly reduce the treatment effeciency of sewage-treatment plant, need to open repeatedly
It opens and closes water plug and back purge system, easily reduce the service life of water plug and back purge system.
Therefore, necessary that domestic sewage processing system in the prior art dress is improved.
Summary of the invention
It is an object of the invention to overcome defect existing in the prior art, purifying domestic sewage processing equipment is provided, it is real
Interim membrane biological reaction pond can be rinsed in present membrane biological reaction pond, not influence the normal operation of sewage treatment.
In order to realize the above technical effect, the technical solution of the present invention is as follows: purifying domestic sewage processing equipment, including successively connect
Water inlet pipe, conditioning tank, biochemistry pool, membrane biological reaction pond, collection processing pond and the outlet pipe connect;Membrane biological reaction pond is raw equipped with film
Object filter and several sliding bars, film biofilter, which slides up and down, to be connected on sliding bar.
Through the above technical solutions, realizing being effectively treated for sanitary sewage, sewage flows into conditioning tank and completes water storage and make
After partial impurities obtain precipitating, just heavy sewage flows into biochemistry pool;After completing biochemical treatment, membrane biological reaction pond is flowed into;By film
After the filtration treatment of biofilter, into processing pond is collected, last collection and reprocessing is completed, water flow qualified discharge is made.
At work, biofilter can move up and down in pending water, using inertia and relative motion to cotton-shaped floating material into
Row cleaning, improves preliminary cleaning effect.
Specifically, film biofilter includes water-collecting tray, it is the cavity that catchments inside water-collecting tray, water-collecting tray lower surface is connected with
Several collection water columns, collection water column is hollow to collect water passage, and collection water passage is connected with cavity bottom of catchmenting, and catchment cavity top company
Logical to be equipped with drinking-water pipe, drinking-water pipe open end direction collects processing pond;Collect the connection of water column side wall and be equipped with several water inlets, collects water column
Outer surface is fixed with filter membrane;In membrane biological reaction pond sewage by filter membrane filter after, followed by water inlet, catchment it is logical
Road, the cavity that catchments enter drinking-water pipe;Drinking-water pipe is equipped with suction pump;Several are provided in water-collecting tray outer rim to cooperate with sliding bar
The cunning mouth slided up and down;Water-collecting tray upper surface is fixedly connected with floating air ring, floating air ring and floating balloon inflation pump and floating gas
Enclose aspiration pump connection;Dismountable mass is additionally provided in floating air ring;Water-collecting tray is in floating balloon inflation and deflation course
It is slided up and down along sliding bar.Mass can also be fixed at water-collecting tray upper surface.
Such structure handles the sewage water filtration of film biofilter and is effectively carried out, and negative pressure equipment increases
The power of suction filtration, multiple collection water columns and water inlet increase suction filtration area, improve filter efficiency.Meanwhile realizing film biology
Filter moving up and down in membrane biological reaction pond.Film biofilter is arranged in sliding bar by the cunning mouth on water-collecting tray
On, by give floating balloon inflation, upward buoyancy is generated to film biofilter, make film biofilter along sliding bar not
It is disconnected to rise.It when needing to clean film biofilter, deflates to floating air ring, due to the reduction and mass and film biology mistake of buoyancy
The gravity of filter itself moves downward film biofilter along sliding bar direction, realizes the side by inflation/deflation
Formula controls film biofilter, easy to control, and structure is simple.
Preferred technical solution is the film aeration being fixed with below film biofilter for flushing membrane biofilter
Flusher, film aeration flusher include gas collection disk, are gas collection cavity inside gas collection disk, gas collection disk upper surface is connected with several
Root collection air column, integrates that air column is hollow as gas collection access, and gas collection access is connected to gas collection cavity top;Collection air column side wall offers several
A solarization air cap, the connection of gas collection cavity lower part are equipped with gas collection gas tube;Gas collection gas tube is connect with air pump is rinsed;Adjacent two collection air column
Between be equipped with flowing water gap, collect water column in sliding process with flowing water interstitial site cooperate.Such mode, by being aerated sum aggregate
Water column cooperates in sliding process with flowing water interstitial site, carries out aeration punching to the impurity screening being adsorbed on filter membrane outer wall
It washes, accelerates falling off for impurity screening, further catchment surface is cleaned, improve cleaning effect.
Preferred technical solution is that cavity top of catchmenting is connect by water collecting joint, hose, the connector that draws water with drinking-water pipe.
Such design can realize film biofilter upper and lower displacement by the flexibility of hose, while be connected to drinking-water pipe holding.
Specifically, drinking-water pipe is successively arranged water pumping valve and suction pump, the water inlet of water pumping valve and drinking-water pipe along water (flow) direction
Between be equipped with backwash water pipe;The water outlet of backwash water pipe is connected to drinking-water pipe, and the water inlet of backwash water pipe is towards processing pond is collected, instead
Wash water pipe is equipped with backwash water valve and backwash water pump.Such structure need to only close water pumping valve and suction pump, open backwash water valve
With backwash water pump, makes to collect the water reflux in processing pond, realize the backwash to film biofilter.Thoroughly remove filter membrane
The impurity screening adsorbed on outer wall is suitable as the clean and maintenance of long periodicity.
Specifically, collect processing pond in be equipped with partition, partition will collect processing pond be divided into from left to right sludge reclaiming chamber with
Disinfected-decolorized chamber;The water outlet of the water outlet of drinking-water pipe and backwash water pipe is towards disinfected-decolorized chamber;Disinfected-decolorized chamber connection water outlet
Pipe, and it is equipped with disinfectant adding set and decolorization device;It further include the first sewage pipe and the second sewage pipe;First sewage pipe
Set on conditioning tank lower part, it is connected to conditioning tank and sludge reclaiming chamber;Second sewage pipe is set to membrane biological reaction pond lower part, and connection film is raw
Object reaction tank and sludge reclaiming chamber;It is respectively equipped with the first pumping dirt pump and second on first sewage pipe and the second sewage pipe and takes out dirty pump;
Decolorization device is ozone generator.Such structure realizes the decoloration disinfection treatment to drainage is crossed, guarantees processing gained
The qualified discharge of water.Disinfectant adding set also can be replaced artificial dispensing.In conditioning tank and membrane biological reaction pond, make big portion
Divide sludge to be precipitated, is discharged into sludge reclaiming chamber from the first sewage pipe and the second sewage pipe, accelerates the place of later period sewage treatment
Efficiency is managed, the reprocessing or recycling to sludge are also convenient for.
Specifically, biochemistry pool is equipped with biochemistry pool aerator and biological bacteria adding set.Biological bacteria adding set can also replace
It is changed to artificial dispensing.Such structure makes sewage in biochemistry pool by after being aerated and being sufficiently mixed and react with the biological bacteria of addition
Flow into membrane biological reaction pond.
Specifically, being additionally provided with filtering grid in conditioning tank, sewage enters after conditioning tank flows into biochemistry by filtering grid again
Pond.Such structure realizes the pretreatment to sewage, the biggish impurity of volume in filter sewage, these impurity is avoided to enter
In post-processing process, equipment operation is influenced.
The advantages and beneficial effects of the present invention are: realizing effective purification of sanitary sewage;Pass through film biofilter
Up and down motion in membrane biological reaction pond achieves that the cleaning to itself can be at any time without interrupting the process flow of sewage
Cleaning treatment is carried out, sewage treating efficiency is improved, increases service life of equipment.
Detailed description of the invention
Fig. 1 is the schematic cross-sectional view of integrated domestic sewage treatment system embodiment 1 of the present invention;
Fig. 2 is the partial cross-sectional structural diagram of film biofilter in embodiment 1;
Fig. 3 is that partial cross-sectional structural diagram of the air ring without gas sinking state to full gas floating state is floated in embodiment 1;
Fig. 4 is the schematic cross-sectional view of embodiment 2;
Fig. 5 is the partial cross-sectional structural diagram of film aeration flusher in embodiment 2;
Fig. 6 is the partial cross-sectional structural diagram of film biofilter in embodiment 2;
Fig. 7 is partial cross-sectional structural diagram of the floating air ring without gas sinking state to full gas floating state in embodiment 2;
Fig. 8 is the schematic cross-sectional view of embodiment 3;
Fig. 9 is the partial cross-sectional structural diagram of 3 mesophytization pond aerator of embodiment;
Figure 10 is the schematic cross-sectional view of embodiment 4.
In figure: 1, water inlet pipe;2, conditioning tank;3, biochemistry pool;4, membrane biological reaction pond;5, processing pond is collected;5-1, sludge
Reclaiming chamber;5-2, disinfected-decolorized chamber;6, outlet pipe;7, film biofilter;7-1, water-collecting tray;7-11, catchment cavity;7-2, collection
Water column;7-21, collection water passage;7-22, water inlet;7-3, drinking-water pipe;7-4, filter membrane;7-5, suction pump;7-6, water pumping valve;7-
7, backwash water pipe;7-8, backwash water valve;7-9, backwash water pump;8, film is aerated flusher;8-1, gas collection disk;8-11, gas collection are empty
Chamber;8-2, collection air column;8-21, gas collection access;8-22, solarization air cap;8-3, gas collection gas tube;8-4, air pump is rinsed;9, it slides
Bar;10, sliding mouth;11, partition;12, ozone generator;13, biochemistry pool aerator;13-1, biochemistry pool are aerated case;13-11, life
Change pond and is aerated cavity;13-12, biochemistry pool are aerated port;13-2, biochemistry pool aeration tube;13-3, biochemistry pool aeration pump;14, first
Sewage pipe;15, the second sewage pipe;16, first dirty pump is taken out;17, first dirty pump is taken out;18, filtering grid;19, floating air ring;20,
Mass;21, water collecting joint;22, hose;23, draw water connector;24, limit film.
Specific embodiment
With reference to the accompanying drawings and examples, further description of the specific embodiments of the present invention.Following embodiment is only
For clearly illustrating technical solution of the present invention, and not intended to limit the protection scope of the present invention.
Embodiment 1
As shown in Figures 1 to 3, the integrated domestic sewage treatment system of embodiment 1, including sequentially connected water inlet pipe 1, conditioning tank
2, biochemistry pool 3, membrane biological reaction pond 4, collection processing pond 5 and outlet pipe 6;Membrane biological reaction pond 4 is fixed with film biofiltration
Device 7 and several sliding bars 9, film biofilter 7, which slides up and down, to be connected on sliding bar 9.It is raw that sliding bar 9 is vertically installed in film
4 inner bottom surface of object reaction tank.Film biofilter 7 includes water-collecting tray 7-1, is the cavity 7-11 that catchments, water-collecting tray inside water-collecting tray 7-1
The connection of the lower surface 7-1 is equipped with several collection water column 7-2, and collection water column 7-2 is hollow for collection water passage 7-21, collection water passage 7-21 and collection
The bottom water cavity 7-11 is connected, and the top cavity 7-11 connection of catchmenting is equipped with drinking-water pipe 7-3, and the open end drinking-water pipe 7-3 direction is received
Collect processing pond 5;Collect the connection of water column 7-2 side wall and be equipped with several water inlets 7-22, the collection outer surface water column 7-2 is fixed with filter membrane 7-
4;After sewage is filtered by filter membrane 7-4 in membrane biological reaction pond 4, followed by water inlet 7-22, collection water passage 7-21, catchment
Cavity 7-11 enters drinking-water pipe 7-3;Drinking-water pipe 7-3 is equipped with suction pump 7-5.Sliding mouth 10 is provided in water-collecting tray 7-1 outer rim, it is sliding
Mouth 10 cooperates with 9 phase position of sliding bar, and sliding bar 9 is arranged in sliding mouth 10;The upper surface water-collecting tray 7-1 is fixedly connected with floating gas
Circle 19, floating air ring 19 is pumped with floating balloon inflation and floating air ring aspiration pump is connected;Mass 20 is fixed at water-collecting tray
The upper surface 7-1;Water-collecting tray 7-1 is slided up and down during floating air ring 19 is inflatable and deflatable along sliding bar 9;Floating air ring 19 is
Annular shape, drinking-water pipe 7-3 are located in the hollow circular ring of floating air ring 19, and sliding bar 9 protrudes from membrane biological reaction pond 4.
After starting sewage treatment, floating balloon inflation pump is first opened, makes floating air ring 19 full of gas.Sewage pass sequentially through into
After water pipe 1, conditioning tank 2 and biochemistry pool 3 enter membrane biological reaction pond 4, and liquid level touches film biofilter 7, unlatching is drawn water
Pump 7-5.Film biofilter 7 starts to filter work, after sewage is filtered out of membrane biological reaction pond 4 by filter membrane 7-4, successively
Water inlet 7-22, collection water passage 7-21, the cavity 7-11 that catchments, drinking-water pipe 7-3 are flowed through, into processing pond 5 is collected, finally by out
Water pipe 6 is discharged, and completes sewage treatment works.Meanwhile in membrane biological reaction pond 4 liquid level constantly rise, when liquid level touches
After film biofilter 7, since floating air ring 19 is to the Float upward function power of film biofilter 7, make film biofilter 7 with
Liquid level also constantly rises.
Along with the progress that film biofilter 7 filters, impurity screening (cotton-shaped floating material) is made constantly to be gathered in water inlet
On filter membrane 7-4 near 7-22.After having accumulated more impurity screening on filter membrane 7-4, closes floating balloon inflation and pump, in unlatching
Floating air ring aspiration pump, reduces the buoyancy of floating air ring 19, simultaneously because the gravity of mass 20 and film biofilter 7 itself
Effect, moves downward film biofilter 7 along 9 direction of sliding bar.It repeats the above steps, film biofilter 7 can be made to exist
It moves up and down repeatedly in membrane biological reaction pond 4, makes the impurity for being attached to 7 surface of film biofilter by movement drive and water flow
It acts on and falls off, realize the cleaning of film biofilter 7.
Embodiment 2
To advanced optimizing for embodiment 1, as shown in Fig. 4 to 7, embodiment 2 the difference from embodiment 1 is that, film biofiltration
It is fixed with below device 7 and is aerated flusher 8 for the film of flushing membrane biofilter 7.It includes gas collection that film, which is aerated flusher 8,
It is gas collection cavity 8-11 inside disk 8-1, gas collection disk 8-1, the upper surface gas collection disk 8-1 is connected with several collection air column 8-2, collects air column
8-2 hollow is gas collection access 8-21, and gas collection access 8-21 is connected to the top gas collection cavity 8-11;Collection air column 8-2 side wall offers
Several solarization air caps 8-22, the connection of the gas collection lower part cavity 8-11 are equipped with gas collection gas tube 8-3;Gas collection gas tube 8-3 and flushing gas
Pump 8-4 connection;It is adjacent two collection air column 8-2 between be equipped with flowing water gap, collect water column 7-2 in sliding process with flowing water interstitial site
Cooperation.Catchmenting, the top cavity 7-11 passes through water collecting joint 21, hose 22, the connector 23 that draws water is connect with drinking-water pipe 7-3.Drinking-water pipe 7-
3 are successively arranged water pumping valve 7-6 and suction pump 7-5 along water (flow) direction, are equipped between water pumping valve 7-6 and the water inlet of drinking-water pipe 7-3
Backwash water pipe 7-7;The water outlet of backwash water pipe 7-7 is connected to drinking-water pipe 7-3, and the water inlet of backwash water pipe 7-7 is located at collection processing
In pond 5, backwash water pipe 7-7 is equipped with backwash water valve 7-8 and backwash water pump 7-9.Hose 22 is preferably corrugated flexible hose.
In work, when needing to clean film biofilter 7, opening flushing air pump 8-4 makes, and extraneous gas passes through collection
Gas gas tube 8-3 successively passes through gas collection cavity 8-11 and gas collection access 8-21, and by the solarization air cap 8-22 on collection air column 8-2 into
Enter membrane biological reaction pond 4.The bubble of generation has certain impact force to the impurity screening on filter membrane 7-4 outer wall, makes to filter
Impurity falls off.When cleaning, floating balloon inflation pump can also be in off state, floating air ring aspiration pump is open state, makes film
Biofilter 7 is gradually reduced.Collection water column 7-2 is gradually arranged in the flowing water gap between collection air column 8-2, with collection water column 7-
Area increase is worn in the 2 flowing water gaps being arranged between collection air column 8-2, the gas of solarization air cap 8-22 discharge is on filter membrane 7-4
The impact force that the impurity screening of attachment has increases, and can accelerate falling off for impurity screening, improves cleaning rate.After the completion of cleaning, open
Floating balloon inflation pump is opened, floating air ring aspiration pump is closed, film biofilter 7 is gradually increasing and rinses dress far from film aeration
8 region is set, the filter contact surface of film biofilter 7 caused by collection air column 8-2 enters is reduced and filters circulating rate
It reduces and reduces.In the process of cleaning, also collection water column 7-2 can be driven to exist along with the repeatedly inflated and deflated of floating air ring 19
It is moved up and down in flowing water gap between collection air column 8-2, washes away bubble more fully to filter membrane 7-4.Filtered
Cheng Zhong, interval are once washed away filter membrane 7-4 in 2-5 minutes, and filter effect is further increased.
In the up and down motion of film biofilter 7, the hose 22 that drinking-water pipe 7-3 is connect with the cavity 7-11 that catchments, meeting
It is shunk with the rising of film biofilter 7, is drawn high with the decline of film biofilter 7, cut down drinking-water pipe 7-3's
Upper and lower displacement.Due to filtering for a long time, need that the micro- of filter membrane surface will be attached to 7 reverse cleaning of film biofilter
Wisp cleaning.Ensure to rinse air pump 8-4 to be in off state, and interlocking lever 10 slides into 9 top of sliding groove, makes film biofiltration
Device 7 is fully located at 8 top of film aeration flusher, closes water pumping valve 7-6 and suction pump 7-5, opens backwash water valve 7-8 and backwash
Water pump 7-9 will collect the processing water back suction in processing pond 5 into film biofilter 7, processing water is made to pass through backwash water pipe 7-7,
Followed by drinking-water pipe 7-3, the cavity 7-11 that catchments, collection water passage 7-21 and water inlet 7-22, enter finally by filter membrane 7-4
Membrane biological reaction pond 4.Using the back flush of processing water, deep clean is carried out to filter membrane 7-4.After completing cleaning, close anti-
Wash water valve 7-8 and backwash water pump 7-9.Such thorough cleaning carries out primary daily.
In this way, the aeration surface flushed filter membrane 7-4 by interval combines daily back flush, it can be maximum
Improve the filter efficiency of filter membrane 7-4.
Embodiment 3
To advanced optimizing for embodiment 2, as shown in Figure 8-9, embodiment 3 the difference from example 2 is that, biochemistry pool 3 is equipped with
Biochemistry pool aerator 13 and the artificial dispensing port of biological bacteria, biochemistry pool aerator 13 includes that biochemistry pool is aerated case 13-1, biochemical
It is that biochemistry pool is aerated cavity 13-11 that pond, which is aerated inside case 13-1, and biochemistry pool is aerated the top case 13-1 and exposes equipped with several biochemistry pools
Gas port 13-12, biochemistry pool are aerated the lower part case 13-1 connection biochemistry pool aeration cavity 13-11 and are equipped with biochemistry pool aeration tube 13-2,
Biochemistry pool aeration tube 13-2 is connected with biochemistry pool aeration pump 13-3.It collects and is equipped with partition 11 in processing pond 5, partition 11 will be collected
Processing pond 5 is divided into sludge reclaiming chamber 5-1 and disinfected-decolorized chamber 5-2 from left to right;The water outlet and backwash water pipe 7- of drinking-water pipe 7-3
7 water outlet is towards disinfected-decolorized chamber 5-2;Disinfected-decolorized chamber 5-2 connection outlet pipe 6, and be equipped with the artificial dispensing port of disinfectant with
Ozone generator 12;It further include the first sewage pipe 14 and the second sewage pipe 15;First sewage pipe 14 is set to 2 lower part of conditioning tank, even
Logical conditioning tank 2 and sludge reclaiming chamber 5-1;Second sewage pipe 15 is set to 4 lower part of membrane biological reaction pond, is connected to membrane biological reaction pond 4
With sludge reclaiming chamber 5-1;It is respectively equipped with the first pumping dirt pump 16 and second on first sewage pipe 14 and the second sewage pipe 15 and takes out dirty pump
17;Filtering grid 18 is additionally provided in conditioning tank 2, sewage enters after conditioning tank 2 flows into biochemistry pool 3 by filtering grid 18 again.It is smelly
The model of Oxygen Generator 12 is preferably MTS-CFG-50A.
At work, sewage flows into conditioning tank 2 by water inlet pipe 1, by filtering grid 18, by the biggish impurity mistake of volume
Filter is gradually gathered in the other side of filtering grid 18 in 2 side initial filter sewage of conditioning tank.When initial filter sewage level reaches certain height
Biochemistry pool 3 is flowed into after degree.Meanwhile sewage is constantly assembled in conditioning tank 2, the partial sludge in sewage can gradually be deposited in adjusting
2 bottom of pond.When sludge settling for a period of time after, open first and take out dirty pump 16, sludge and partial impurities is made to pass through the first sewage pipe
14 are discharged into sludge reclaiming chamber 5-1.
After initial filter sewage enters biochemistry pool 3, opens biochemistry pool aeration pump 13-3 and biological bacteria is added, lead to gas successively
Cross biochemistry pool aeration tube 13-2, aeration cavity 13-11 and biochemistry pool be aerated port 13-12 enter biochemistry pool 3, to initial filter sewage into
Row aeration, and biological bacteria is sufficiently mixed with initial filter sewage, oxygen needed for enough reactions are provided to biological bacteria obtains biochemical mixing
Sewage.Biological bacteria by after the substance biochemical reaction in sewage to COD, BOD5, SS, TP, NH in sewage3The realizations such as-N, TN are effective
Removal.After its liquid level reach a certain height, membrane biological reaction pond 4 is flowed into, is filtered, resulting drainage of crossing is evacuated to disinfection
Decolourize chamber 5-2.It has served as that disinfectant is added after drainage enters disinfected-decolorized chamber 5-2, has opened ozone generator 12, carried out to drainage is crossed
Disinfection and fade treatment.Resulting water of handling well is discharged finally by outlet pipe 6 after disinfected-decolorized processing.Meanwhile in film
Sludgd deposition can be also generated in biological reaction pool 4, can open the second pumping dirt pump 17, sludge is made to be discharged into dirt by the second sewage pipe 15
Mud reclaiming chamber 5-1.
Embodiment 4
To advanced optimizing for embodiment 3, as shown in Figure 10, embodiment 3 the difference from example 2 is that, 9 lower part of sliding bar is solid
Surely it is equipped with limit film 24.The setting of limit film 24 limits the down position of film biofilter 7, prevents excessive descent
Cause film biofilter 7 and film to be aerated flusher 8 and generate mutual collision, to damage equipment.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, without departing from the technical principles of the invention, several improvements and modifications can also be made, these improvements and modifications
Also it should be regarded as protection scope of the present invention.
Claims (9)
1. purifying domestic sewage processing equipment, including sequentially connected water inlet pipe, conditioning tank, biochemistry pool, membrane biological reaction pond, receipts
Collect processing pond and outlet pipe;It is characterized in that, the membrane biological reaction pond is equipped with film biofilter and several sliding bars, institute
It states film biofilter and slides up and down and be connected on sliding bar.
2. purifying domestic sewage processing equipment according to claim 1, which is characterized in that the film biofilter includes
Water-collecting tray, the water-collecting tray inside is the cavity that catchments, and the water-collecting tray lower surface is connected with several collection water columns, the collection water column
Hollow to collect water passage, the collection water passage is connected with cavity bottom of catchmenting, and the cavity top connection of catchmenting, which is equipped with, draws water
Pipe, drinking-water pipe open end direction collect processing pond;The collection water column side wall, which is connected to, is equipped with several water inlets, outside the collection water column
Surface is fixed with filter membrane;In the membrane biological reaction pond sewage by filter membrane filter after, followed by water inlet, catchment it is logical
Road, the cavity that catchments enter drinking-water pipe;The drinking-water pipe is equipped with suction pump;Several and cunning are provided in the water-collecting tray outer rim
Lever cooperates the cunning mouth slided up and down;The water-collecting tray upper surface is fixedly connected with floating air ring, the floating air ring and floating gas
Circle inflator pump is connected with floating air ring aspiration pump;Dismountable mass is additionally provided in the floating air ring;The water-collecting tray exists
It is slided up and down in floating balloon inflation and deflation course along sliding bar.
3. purifying domestic sewage processing equipment according to claim 2, which is characterized in that below the film biofilter
It is fixed with and is aerated flusher for the film of flushing membrane biofilter, the film aeration flusher includes gas collection disk, institute
Stating is gas collection cavity inside gas collection disk, and gas collection disk upper surface is connected with several collection air columns, and the collection air column is hollow for collection
Gas access, the gas collection access are connected to gas collection cavity top;The collection air column side wall offers several solarization air caps, the collection
The connection of gas cavity lower part is equipped with gas collection gas tube;The gas collection gas tube is connect with air pump is rinsed;It is described it is adjacent two collection air column it
Between be equipped with flowing water gap, the collection water column in sliding process with flowing water interstitial site cooperation.
4. purifying domestic sewage processing equipment according to claim 2, which is characterized in that the cavity top of catchmenting passes through
Water collecting joint, hose, the connector that draws water are connect with drinking-water pipe.
5. purifying domestic sewage processing equipment according to claim 2, which is characterized in that the drinking-water pipe is along water (flow) direction
It is successively arranged water pumping valve and suction pump, backwash water pipe is equipped between water pumping valve and the water inlet of drinking-water pipe;The backwash water pipe
Water outlet is connected to drinking-water pipe, and the water inlet of backwash water pipe is equipped with backwash water valve and backwash towards processing pond, backwash water pipe is collected
Water pump.
6. purifying domestic sewage processing equipment according to claim 6, which is characterized in that be equipped in the collection processing pond
Partition, partition are divided into sludge reclaiming chamber and disinfected-decolorized chamber for processing pond is collected from left to right;The water outlet of the drinking-water pipe with
The water outlet of backwash water pipe is towards disinfected-decolorized chamber;The disinfected-decolorized chamber connects outlet pipe, and is equipped with disinfectant adding set
With decolorization device.
7. purifying domestic sewage processing equipment according to claim 7, which is characterized in that further include the first sewage pipe and
Two sewage pipes;First sewage pipe is set to conditioning tank lower part, connection conditioning tank and sludge reclaiming chamber;Second sewage pipe is set
In membrane biological reaction pond lower part, it is connected to membrane biological reaction pond and sludge reclaiming chamber;On first sewage pipe and the second sewage pipe
It is respectively equipped with the first pumping dirt pump and second and takes out dirty pump.
8. purifying domestic sewage processing equipment according to claim 1, which is characterized in that the biochemistry pool is equipped with biochemistry pool
Aerator and biological bacteria adding set.
9. according to purifying domestic sewage processing equipment described in claim 1, which is characterized in that the conditioning tank is equipped with filter grid
Grid, sewage enters after conditioning tank flows into biochemistry pool by filtering grid again.
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CN201811023825.XA CN108975635A (en) | 2018-09-04 | 2018-09-04 | Purifying domestic sewage processing equipment |
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CN201811023825.XA CN108975635A (en) | 2018-09-04 | 2018-09-04 | Purifying domestic sewage processing equipment |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111206403A (en) * | 2019-12-26 | 2020-05-29 | 陈国卫 | Dry cleaning machine with filtering device |
CN114684977A (en) * | 2020-12-31 | 2022-07-01 | 江苏启德水务有限公司 | Rural sewage treatment system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN205275305U (en) * | 2015-12-30 | 2016-06-01 | 山东水发环境科技有限公司 | Membrane bioreactor |
CN206502669U (en) * | 2016-08-31 | 2017-09-19 | 云南滇清环境科技有限公司 | One kind exempts from drawing-in type integration MBR sewage disposal devices |
CN107226530A (en) * | 2017-06-13 | 2017-10-03 | 汤波 | A kind of efficient denitrification integrated apparatus |
DE202017106678U1 (en) * | 2017-11-06 | 2018-03-22 | Chengdu Huarilvlan Engineering Technology Co., Ltd. | Municipal wastewater disposal system with MBR composite membrane |
CN208869462U (en) * | 2018-09-04 | 2019-05-17 | 江苏云天路公共卫生服务管理有限公司 | Purifying domestic sewage processing equipment |
-
2018
- 2018-09-04 CN CN201811023825.XA patent/CN108975635A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN205275305U (en) * | 2015-12-30 | 2016-06-01 | 山东水发环境科技有限公司 | Membrane bioreactor |
CN206502669U (en) * | 2016-08-31 | 2017-09-19 | 云南滇清环境科技有限公司 | One kind exempts from drawing-in type integration MBR sewage disposal devices |
CN107226530A (en) * | 2017-06-13 | 2017-10-03 | 汤波 | A kind of efficient denitrification integrated apparatus |
DE202017106678U1 (en) * | 2017-11-06 | 2018-03-22 | Chengdu Huarilvlan Engineering Technology Co., Ltd. | Municipal wastewater disposal system with MBR composite membrane |
CN208869462U (en) * | 2018-09-04 | 2019-05-17 | 江苏云天路公共卫生服务管理有限公司 | Purifying domestic sewage processing equipment |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111206403A (en) * | 2019-12-26 | 2020-05-29 | 陈国卫 | Dry cleaning machine with filtering device |
CN114684977A (en) * | 2020-12-31 | 2022-07-01 | 江苏启德水务有限公司 | Rural sewage treatment system |
CN114684977B (en) * | 2020-12-31 | 2023-12-19 | 江苏启德水务有限公司 | Rural sewage treatment system |
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