CN107244785A - A kind of microkinetic septic tank - Google Patents
A kind of microkinetic septic tank Download PDFInfo
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- CN107244785A CN107244785A CN201710616985.4A CN201710616985A CN107244785A CN 107244785 A CN107244785 A CN 107244785A CN 201710616985 A CN201710616985 A CN 201710616985A CN 107244785 A CN107244785 A CN 107244785A
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- lattice
- septic tank
- dividing plate
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- filler
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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
- C02F9/00—Multistage 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
- 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
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
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- 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)
Abstract
The present invention discloses a kind of septic tank for sanitary sewage disposal, and septic tank of the invention includes septic tank body, and the septic tank body is spaced one from into the first lattice, the second lattice and the 3rd lattice by the first dividing plate, second partition；The connector top rake for leading to the second lattice in the first lattice installs one piece of grid filter screen, the suspension of the overwhelming majority can be obstructed close to the connector of the one or two lattice, aeration type filter is there is also mounted on connector in addition, not only play filter suspended solids, the good environment depended on for existence is also provided to microorganism simultaneously, filler is full of aerobic microbiological and the suspension that is retained down during work, and suspension is just decomposed digestion as the nutrients of aerobic microbiological.Therefore, suspension did not resulted in the blocking of the mouth of a river and septic tank system.The septic tank of the present invention is obviously improved to the treatment effect of organic matter of sewage and improves treatment effeciency, significantly improves the phenomenons such as the slough that occurs current short circuit in pond, improves the dischargeable capacity in pond.
Description
Technical field
The present invention relates to a kind of processing pond for sewage disposal, especially a kind of septic tank for sewage disposal, category
In sewage treatment facility technical field.
Background technology
Septic tank is as important component in living drainage system, and it is mainly removed using precipitation and anaerobic digestion
Suspension in water etc., preliminary treatment is played a part of to sewage.So far the septic tank generally used, due to its internal structure not
A series of reasons such as enough reasonable and used processing modes are single, cause its treatment effect and efficiency poor.Traditional septic tank
Greatest problem present on internal structure is connected using pipeline or aperture between every lattice, and sewage fluidised form is to be in direct current flashing shape
State, easily causes short stream and slough phenomenon, reduces the dischargeable capacity in pond, influence overall treatment effect.In addition, current
Septic tank is single to use anaerobic ferment process, and is that can not meet having for directly discharge or follow-up Ecological Disposal only with anaerobic technique
Machine thing and ammonia nitrogen index request.Rural area and discrete areas for not yet building sewage collecting pipe network, septic tank now is
It is difficult to meet demand.
The content of the invention
There is provided it is an object of the invention to overcome in place of above-mentioned the deficiencies in the prior art one kind can effectively solve the problem that it is existing
Septic tank treatment effect and treatment effeciency are low, easily block, there are problems that the microkinetic septic tank of short stream in pond.
To achieve the above object, the technical scheme taken of the present invention is：A kind of microkinetic septic tank, including septic tank sheet
Body, the septic tank body is spaced one from into the first lattice, the second lattice and the 3rd lattice by the first dividing plate, second partition；Described first
Dividing plate is located between first lattice and the second lattice, and the second partition is located between second lattice and the 3rd lattice；Described
Connected, connected between second lattice and the 3rd lattice by bridge piece by connector between one lattice and second lattice
Logical, the bridge piece is located at the bottom of the outs opens of second lattice vertically the second lattice；
Provided with water inlet, grid and aeration type filter in first lattice, the water inlet is located at first lattice
Top；The grid is connected between the top and bottom of first lattice, and the aeration type filter is located at the connector
Towards the side of the first lattice；
Anaerobism filler and regulating weir are provided with second lattice, the regulating weir is located at connector one towards the second lattice
Side；
The 3rd lattice are separated into by anoxic zone, water by the 3rd dividing plate, the 4th dividing plate, the 5th dividing plate respectively in 3rd lattice
Flow area, aerobic zone, settling zone；The bottom of the anoxic zone is connected with the current area, the top in the current area with it is described good
Oxygen area is connected, and the bottom of the aerobic zone is connected with the settling zone；The anoxic zone includes anoxic filler and lacked located at described
The anoxic aeration head of oxygen area bottom, is provided with the sky for current between the bottom of the anoxic filler and the bottom of the anoxic zone
Between；The aerobic zone include aerobic filler and the aerobic aeration head located at the aerobic zone bottom, the aerobic filler with it is described
The space for current is provided between the bottom of aerobic zone；The top of the settling zone is provided with delivery port.
As the preferred embodiment of microkinetic septic tank of the present invention, the grid in first lattice is described first
Connection is tilted between at the top and bottom of lattice, and the angle between the grid and the first lattice bottom towards the second lattice direction is small
In 90 °.
As the preferred embodiment of microkinetic septic tank of the present invention, the aeration type filter includes shell, filled out
The filter packing and the aeration head located at the filler bottom filled in the shell, the shell is network structure.
As the preferred embodiment of microkinetic septic tank of the present invention, the aeration type filter is trapezium structure,
And the bottom of the aeration type filter of the trapezium structure is connected with the connector.
As the preferred embodiment of microkinetic septic tank of the present invention, the anaerobism filler bottom in second lattice is consolidated
The bottom of second lattice is scheduled on, the sky for current is provided between the periphery of the anaerobism filler and the side wall of second lattice
Between.
As the preferred embodiment of microkinetic septic tank of the present invention, in the 3rd lattice, the anoxic in anoxic zone
It is close to the second partition and the 3rd dividing plate in the periphery of filler；It is close to the described 4th in the periphery of aerobic filler in the aerobic zone
Dividing plate and the 5th dividing plate.
It is used as the preferred embodiment of microkinetic septic tank of the present invention, bottom and the anoxic of the 3rd dividing plate
The bottom of filler maintains an equal level, and the top of the 3rd dividing plate is higher than the height of the bridge piece.
As the preferred embodiment of microkinetic septic tank of the present invention, the bottom of the 4th dividing plate is fixed on described
The bottom of 3rd lattice, the top of the 4th dividing plate maintains an equal level with the top of the aerobic filler.
As the preferred embodiment of microkinetic septic tank of the present invention, the bottom of the 5th dividing plate with it is described aerobic
The bottom of filler maintains an equal level, and the top of the 5th dividing plate is higher than the height of the bridge piece.
As the preferred embodiment of microkinetic septic tank of the present invention, the bottom of the settling zone is oblique provided with water conservancy diversion
Plate, the lower end of the flow guiding inclined plate is fixed on the bottom of the settling zone, and the upper end of the flow guiding inclined plate is fixed on the described 3rd
On the side wall of lattice.
The microkinetic septic tank of the present invention has the advantages that：
1) water quality of water outlet is significantly improved.The present invention, which changes into the single anaerobic fermentation handling process of traditional septic tank, to be detested
The group technology of oxygen-and oxygen-Aerobic Process for Treatment, the technique of these three different characteristics complements each other, hence it is evident that improve organic to sewage
The treatment effect of thing and improve treatment effeciency.
2) incidence of septic tank blocking is significantly reduced.The present invention pacifies in the connector top rake that the first lattice lead to the second lattice
One piece of grid filter screen is filled, the suspension of the overwhelming majority can be obstructed close to the connector of the one or two lattice, gone back in addition on connector
It is mounted with to be aerated type filter, the filter is shaped as prismatoid, and shell is stamped to form by gross porosity grid, inside is full of filtering
Filler, and filler bottom is provided with aeration head, make filter interior be in aerobic state.It is outstanding that filter packing not only plays filtering
The effect of floating solid, while also provide the good environment depended on for existence to microorganism, during work filler full of aerobic microbiological and
The suspension being retained down, suspension is just decomposed digestion as the nutrients of aerobic microbiological.Therefore, suspension will not
Caused the blocking of the mouth of a river and septic tank system.
3) significantly improve and occur the phenomenons such as the short-circuit slough of current in pond, improve the dischargeable capacity in pond.One or two
Aeration type filter housing on lattice connector is the trapezoidal solids that grid is stamped to form, and current can enter from multiple directions
Inside filter, i.e. the current of the first lattice to the second lattice are the flowings of circulation flashing form, in the absence of short stream and slough.Two or three
Flow-guiding channel is provided with inside lattice, current, which rely on drop potential energy, to be promoted and moved from entrance toward outlet, thus be also not present backflow, it is short-circuit
With the phenomenon such as slough.
Brief description of the drawings
Fig. 1 is a kind of structural representation of embodiment of microkinetic septic tank of the present invention.
In figure, 1 it is the first lattice, 2 is the second lattice, 3 is the 3rd lattice, 10 is the first dividing plate, 20 is second partition, 30 is the 3rd
Dividing plate, 40 be the 4th dividing plate, 50 be the 5th dividing plate, 11 be water inlet, 12 be aeration type filter, 13 be connector, 14 be lattice
Grid, 21 be anaerobism filler, 22 be bridge piece, 23 be regulating weir, 31 be anoxic zone, 32 be current area, 33 be aerobic zone, 34 be
Settling zone, 310 be anoxic filler, 311 be anoxic aeration head, 330 be aerobic filler, 331 be aerobic aeration head, 340 be water conservancy diversion
Swash plate, 341 are delivery port.
Embodiment
To better illustrate the object, technical solutions and advantages of the present invention, below in conjunction with the drawings and specific embodiments pair
The present invention is described further.
A kind of embodiment of microkinetic septic tank of the present invention, as shown in Figure 1, the microkinetic septic tank of the present embodiment include
Septic tank body, the septic tank body is spaced one from into the first lattice 1, the second lattice 2 and by the first dividing plate 10, second partition 20
Three lattice 3；First dividing plate 10 is located between the lattice 2 of the first lattice 1 and second, and the second partition 20 is located at second lattice
2 and the 3rd between lattice 3；Connected between first lattice 1 and second lattice 2 by connector 13, second lattice 2 with it is described
Connected between 3rd lattice 3 by bridge piece 22, the bridge piece 22 is located at the outs open of second lattice 2 vertically
The bottom of second lattice 2；
Provided with water inlet 11, grid 14 and aeration type filter 12 in first lattice 1, the water inlet 11 is located at described
The top of first lattice 1；The grid 14 is connected between the top and bottom of first lattice 1, the aeration type filter 12
Located at the connector 13 towards the side of the first lattice 1；
It is provided with anaerobism filler 21 and regulating weir 23 in second lattice 2, the regulating weir 23 is located at connector 13 towards the
The side of two lattice 2；
The 3rd lattice 3 are separated into respectively by the 3rd dividing plate 30, the 4th dividing plate 40, the 5th dividing plate 50 in 3rd lattice 3
Anoxic zone 31, current area 32, aerobic zone 33, settling zone 34；The bottom of the anoxic zone 31 is connected with the current area 32, described
The top in current area 32 is connected with the aerobic zone 33, and the bottom of the aerobic zone 33 is connected with the settling zone 34；It is described to lack
Oxygen area 31 includes anoxic filler 310 and the anoxic aeration head 311 located at the bottom of anoxic zone 31, the anoxic filler 310
The space for current is provided between the bottom of bottom and the anoxic zone 31；The aerobic zone 33 includes the aerobic He of filler 330
Aerobic aeration first 331 located at the bottom of aerobic zone 33, is provided between the aerobic filler 330 and the bottom of the aerobic zone 33
Space for current；The top of the settling zone 34 is provided with delivery port 341.
It is preferred that as shown in Figure 1, the grid 14 in first lattice 1 inclines between the top and bottom of the first lattice 1
Tiltedly connection, and the angle in direction the second lattice 2 direction is less than 90 ° between the grid 14 and the bottom of the first lattice 1.
It is preferred that as shown in Figure 1, the aeration type filter 12 includes shell, the filtering being filled in the shell
Filler and the aeration head located at the filler bottom, the shell are network structure.
It is preferred that as shown in Figure 1, the type filter 12 that is aerated is trapezium structure, and the aeration of the trapezium structure
The bottom of type filter 12 is connected with the connector 13.
It is preferred that as shown in Figure 1, the bottom of anaerobism filler 21 in second lattice 2 is fixed on the bottom of second lattice 2
The space for current is provided between the side wall of portion, the periphery of the anaerobism filler 21 and second lattice 2.
It is preferred that as shown in Figure 1, in the 3rd lattice 3, institute is close on the periphery of the anoxic filler 310 in anoxic zone 31
State the dividing plate 30 of second partition 20 and the 3rd；It is close to the 4th dividing plate 40 in the periphery of aerobic filler 330 in the aerobic zone 33
With the 5th dividing plate 50.
It is preferred that as shown in Figure 1, the bottom of the 3rd dividing plate 30 maintains an equal level with the bottom of the anoxic filler 310, institute
The top for stating the 3rd dividing plate 30 is higher than the height of the bridge piece 22.
It is preferred that as shown in Figure 1, the bottom of the 4th dividing plate 40 is fixed on the bottom of the 3rd lattice 3, described
The top of four dividing plates 40 and the top of the aerobic filler 330 maintain an equal level.
It is preferred that as shown in Figure 1, the bottom of the 5th dividing plate 50 and the bottom of the aerobic filler 330 maintain an equal level, institute
The top for stating the 5th dividing plate 50 is higher than the height of the bridge piece 22.
It is preferred that as shown in Figure 1, the bottom of the settling zone 34 is provided with flow guiding inclined plate 340, the flow guiding inclined plate 340
Lower end be fixed on the bottom of the settling zone 34, the upper end of the flow guiding inclined plate 340 is fixed on the side wall of the 3rd lattice 3
On.
In the present embodiment, the top rake of connector 13 for leading to the second lattice 2 in the first lattice 1 installs one piece of grid 14；First
Lattice 1, which lead on the connector 13 of the second lattice 2, installs an aeration type filter 12, and being shaped as the aeration type filter 12 is trapezoidal
Body, shell is stamped to form by grid, and inside is full of filter packing, and filler bottom is provided with aeration head；The court of connector 13
Regulating weir 23 is installed on to the direction of the second lattice 2；Second lattice 2 are built-in with anaerobism filler 21, anaerobism filler 21 and the dividing plate of both sides first
10 and second partition 20 keep suitable distance, as water stream channel；Second lattice 2 are connected with the 3rd lattice 3 by bridge piece 22, even
Connect the bent tube section direction bottom of pond of the second lattice 2 of bend pipe 22；3rd lattice 3 are divided into four regions, and first area is anoxic from left to right
Anoxic filler 310 and anoxic aeration head 311 are installed in area 31, anoxic zone 31, anoxic filler 310 and bottom of pond retain appropriately distance with
As water stream channel, the right side of anoxic filler 310 is close to install under the 3rd dividing plate 30, the bottom of the 3rd dividing plate 30 and anoxic filler 310
Side maintains an equal level, and the top of the 3rd dividing plate 30 is more slightly higher than the tube top of bridge piece 22, and the 3rd dividing plate 30 makees fixed pivot by front and rear pool wall；
It is the second area of the 3rd lattice 3, i.e. current area 32 between 3rd dividing plate 30 and the 4th dividing plate 40, current area 32 is logical as current
Road；It is the 3rd region of the 3rd lattice 3, i.e. aerobic zone 33 between 4th dividing plate 40 and the 5th dividing plate 50, aerobic zone 33 installs aerobic
It is close to bottom of pond, the top of the 4th dividing plate 40 and the aerobic top of filler 330 in filler 330 and aerobic aeration first 331, the bottom of the 4th dividing plate 40
Maintain an equal level, aerobic filler 330 is close to the 4th dividing plate 40 and installed, the bottom of aerobic filler 330 and bottom of pond retain suitable distance for use as
Water stream channel；It is close to aerobic filler 330 and the 5th dividing plate 50 is installed, the bottom of the 5th dividing plate 50 is held with the aerobic lower sideline of filler 330
Flat, the top of the 5th dividing plate 50 is more slightly higher than the tube top of bridge piece 22, is the 4th region between the 5th dividing plate 50 and right pool wall, i.e.,
Settling zone 34, the precipitation that settling zone 34 is used as suspension is used；One piece is installed to the 3rd region aerobic zone 33 in the bottom of settling zone 34
Inclined deflector.
Microkinetic septic tank described in the present embodiment, in use, concrete processing procedure is as follows：
1st, sanitary sewage flows into the first lattice 1 by water inlet 11, and after precipitation and anaerobic fermentation, sewage is divided into three layers：Bottom
Layer sludge settling thing, middle level mixed liquor, upper strata excrement skin suspension.Grid 14 prevents bulky grain suspension from being connected close to two lattice are led to
Hole, thus the only middle level mixed liquor that can be flowed into after grid 14.These mixed liquors flow into aeration type filter 12, particle quilt again
Filter packing is retained, and filter packing is full of aerobic microbiological, and these particle suspensions of the positive good utilisation of these aerobic microbiologicals are made
It is able to decompose removing for the suspension of the nutrients of growth, thus retention.Mixed liquor is by being aerated type filter 12 and regulating weir
Enter the second lattice 2 after 23.In addition, the connector 13 of the first lattice 1 and the second lattice 2 is adjusted for one towards installation on the direction of the second lattice 2
Weir 23, the second lattice 2 are quantitatively delivered to by the mixed liquor of the first lattice 1, and the flowed fluctuation of sanitary sewage is made buffering by the first lattice 1 and adjusted
Section；
2nd, the mixed liquor into the second lattice 2 is from side infiltration anaerobism filler 21, and anaerobism filler 21 has been covered with the micro- life of anaerobism
Thing, these anaerobes carry out anaerobic reaction to the organic matter inside sewage, and mixed liquor after Anaerobic Treatment is from anaerobism
The opposite side outflow of filler 21, then enter the 3rd lattice 3 by bridge piece 22；
3rd, the mixed liquor into the 3rd lattice 3 first flows through anoxic filler 310, the abundant simultaneous oxygen of anoxic filler 310 from top to bottom
Microorganism carries out anoxic degraded to the organic matter of sewage, after hypoxia response, promotion of the mixed liquor in the drop potential energy that always comes in and goes out
Under, the water stream channel of bottom and side through anoxic filler 310 flow to the top of aerobic filler 330 from lower to upper.Mixed liquor is again
Aerobic filler 330 is flowed through from top to bottom, and the abundant aerobic microbiological of aerobic filler 330 carries out aerobic drop to the organic matter of mixed liquor
Solution.After the combination degradation technique of anaerobism-anoxic-aerobic, hence it is evident that improve the total removal rate and whole process of organic matter
Reaction efficiency.
4th, the mixed liquor for flowing to the aerobic bottom of filler 330 enters settling zone 34 by the inlet port of settling zone 34, through precipitation
Afterwards, supernatant is drained by delivery port 341, under guide functions of the sludge by flow guiding inclined plate 340, enters back into aerobic filler 330
Bottom, these sludge deliver to the inside of aerobic filler 330 again by the air-flow of aerobic aeration first 331, as strain and microorganism
Nutrients.
Finally, it should be noted that the above embodiments are merely illustrative of the technical solutions of the present invention rather than the present invention is protected
The limitation of scope is protected, although being explained in detail with reference to preferred embodiment to the present invention, one of ordinary skill in the art should
Understand, technical scheme can be modified or equivalent substitution, without departing from the essence of technical solution of the present invention
And scope.
Claims (10)
1. a kind of microkinetic septic tank, it is characterised in that including septic tank body, the septic tank body is by the first dividing plate,
Two dividing plates are spaced one from into the first lattice, the second lattice and the 3rd lattice；First dividing plate is located between first lattice and the second lattice,
The second partition is located between second lattice and the 3rd lattice；Connected between first lattice and second lattice by connector
It is logical, connected between second lattice and the 3rd lattice by bridge piece, the bridge piece is located at the portion of second lattice
Separate the bottom of mouth vertically the second lattice；
Provided with water inlet, grid and aeration type filter in first lattice, the water inlet is located at the top of first lattice；
The grid is connected between the top and bottom of first lattice, and the aeration type filter is located at the connector towards the
The side of one lattice；
Anaerobism filler and regulating weir are provided with second lattice, the regulating weir is located at the side of connector the second lattice of direction；
The 3rd lattice are separated into by anoxic zone, current by the 3rd dividing plate, the 4th dividing plate, the 5th dividing plate respectively in 3rd lattice
Area, aerobic zone, settling zone；The bottom of the anoxic zone is connected with the current area, the top in the current area with it is described aerobic
Area is connected, and the bottom of the aerobic zone is connected with the settling zone；The anoxic zone includes anoxic filler and located at the anoxic
The anoxic aeration head of area bottom, is provided with the sky for current between the bottom of the anoxic filler and the bottom of the anoxic zone
Between；The aerobic zone include aerobic filler and the aerobic aeration head located at the aerobic zone bottom, the aerobic filler with it is described
The space for current is provided between the bottom of aerobic zone；The top of the settling zone is provided with delivery port.
2. microkinetic septic tank as claimed in claim 1, it is characterised in that the grid in first lattice is in first lattice
Connection is tilted between top and bottom, and the angle in the second lattice direction of direction is less than between the grid and the first lattice bottom
90°。
3. microkinetic septic tank as claimed in claim 2, it is characterised in that the aeration type filter includes shell, filling
Filter packing in the shell and the aeration head located at the filler bottom, the shell are network structure.
4. microkinetic septic tank as claimed in claim 3, it is characterised in that the aeration type filter is trapezium structure, and
The bottom of the aeration type filter of the trapezium structure is connected with the connector.
5. microkinetic septic tank as claimed in claim 1, it is characterised in that the anaerobism filler bottom in second lattice is fixed
The sky for current is provided with the bottom of second lattice, between the periphery of the anaerobism filler and the side wall of second lattice
Between.
6. microkinetic septic tank as claimed in claim 1, it is characterised in that in the 3rd lattice, the anoxic in anoxic zone is filled out
It is close to the second partition and the 3rd dividing plate in the periphery of material；The periphery of aerobic filler in the aerobic zone be close to the described 4th every
Plate and the 5th dividing plate.
7. microkinetic septic tank as claimed in claim 1, it is characterised in that the bottom of the 3rd dividing plate is filled out with the anoxic
The bottom of material maintains an equal level, and the top of the 3rd dividing plate is higher than the height of the bridge piece.
8. microkinetic septic tank as claimed in claim 1, it is characterised in that the bottom of the 4th dividing plate is fixed on described
The bottom of three lattice, the top of the 4th dividing plate maintains an equal level with the top of the aerobic filler.
9. microkinetic septic tank as claimed in claim 1, it is characterised in that the bottom of the 5th dividing plate aerobic is filled out with described
The bottom of material maintains an equal level, and the top of the 5th dividing plate is higher than the height of the bridge piece.
10. microkinetic septic tank as claimed in claim 1, it is characterised in that the bottom of the settling zone is provided with flow guiding inclined plate,
The lower end of the flow guiding inclined plate is fixed on the bottom of the settling zone, and the upper end of the flow guiding inclined plate is fixed on the 3rd lattice
On the wall of side.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710616985.4A CN107244785B (en) | 2017-07-26 | 2017-07-26 | Micro-power septic tank |
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|---|---|---|---|
| CN201710616985.4A CN107244785B (en) | 2017-07-26 | 2017-07-26 | Micro-power septic tank |
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| CN107244785A true CN107244785A (en) | 2017-10-13 |
| CN107244785B CN107244785B (en) | 2023-04-18 |
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| CN201710616985.4A Active CN107244785B (en) | 2017-07-26 | 2017-07-26 | Micro-power septic tank |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046547A (en) * | 2018-01-29 | 2018-05-18 | 武汉都市环保工程技术股份有限公司 | Cultivate treatment for cow manure integrating device and system |
| CN109867403A (en) * | 2017-12-01 | 2019-06-11 | 中国水利水电科学研究院 | A kind of processing unit and sewage water treatment method of dispersing type sewage |
| CN110342748A (en) * | 2019-07-24 | 2019-10-18 | 杭州李春环境科技有限公司 | Toilet sewage purifier and method |
| CN117735721A (en) * | 2024-02-20 | 2024-03-22 | 中国市政工程华北设计研究总院有限公司 | Denitrification type low-carbon-emission five-grid septic tank and treatment process thereof |
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