CN208471840U - Decentralized integrated sewage treatment device - Google Patents
Decentralized integrated sewage treatment device Download PDFInfo
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- CN208471840U CN208471840U CN201820969151.1U CN201820969151U CN208471840U CN 208471840 U CN208471840 U CN 208471840U CN 201820969151 U CN201820969151 U CN 201820969151U CN 208471840 U CN208471840 U CN 208471840U
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Abstract
The utility model announces a kind of decentralized integrated sewage treatment device, belongs to technical field of sewage treatment equipment.Including anaerobic pond, anoxic pond, aerobic membrane cisterna and the equipment room set gradually；Anaerobic pond is provided with water inlet, is equipped with agitating device in anaerobic pond；Anoxic pond upper end is connected to anaerobic pond, and anoxic pond lower end is connected to aerobic membrane cisterna；Reflux water pump and membrane module are equipped in aerobic membrane cisterna, aerobic membrane cisterna upper end is equipped with overflow port, and aerobic membrane cisterna lower end is equipped with interior discharge outlet；The water outlet of reflux water pump is connected to anaerobic pond；Membrane module water outlet is connected with water producing pipe；Overflow port is connected with outer discharge outlet, and interior discharge outlet connects outer discharge outlet by the first valve；Blower, dissolved oxygen instrument are equipped in equipment room；Blower connects membrane module by air hose.The utility model structure is simple, easy to use, environmental protection and energy saving, effectively realizes the processing discharge of sewage, discharge water quality is good, suitable for the fluctuating change to adapt to water, water quality, the Urban Areas of land used anxiety.
Description
Technical field
The utility model relates to technical field of sewage treatment equipment, specifically a kind of distributing integrated sewage disposal dress
It sets.
Background technique
Currently, the traditional handicraft principle for sewage treatment includes filler biological embrane method and artificial swamp method:
Wherein the former Type of equipment is based on FBBR or MBBR, passes through filling out for design structure unlike material and space structure
Material improves biochemical degradation efficiency, and indirect labor's oxygenic aeration maintains anaerobic/anoxic/aerobic office necessary to biological carbon and phosphorous removal
Portion's microenvironment meets the requirement of standard water discharge discharge.Substantially, filler biological embrane method belongs to typical underload biological treatment model
Farmland, it is difficult to for cities and towns/villages and small towns sewage quality water change in time and space, big, TN/TP impact load frequently takes measures quickly to cope with,
Therefore the water outlet long-term stably reaching standard of TN/TP is practically impossible to the target completed.In addition, loosely adhere on filler biomembrane when
It often falls off, it is exceeded to will also result in water outlet SS；
The Type of equipment of the latter with vertical subsurface flow, horizontal drowned flow or vertical/horizontal undercurrent it is compound based on, it is less use surface
Flow pattern formula, the fresh combatants of pollutant fluxes are still the microorganism in root system habitat, and operational effect has apparent seasonal variety special
Sign, effluent quality seldom being capable of long-term stably reaching standard.Matrix easily blocks, is artificial swamp vulnerable to pest and disease damage, starting period length
Three big latent defects, exist take up a large area, " offline cleaning operation too complex " can not be long-term running etc. in villages and small towns area
Problem.
Summary of the invention
In order to solve the above technical problems, the utility model provides a kind of decentralized integrated sewage treatment device.
The utility model is achieved through the following technical solutions: a kind of decentralized integrated sewage treatment device, including successively
Anaerobic pond, anoxic pond, aerobic membrane cisterna and the equipment room of setting；
The anaerobic pond is provided with water inlet, is equipped with agitating device in anaerobic pond；
The anoxic pond upper end is connected to anaerobic pond, and anoxic pond lower end is connected to aerobic membrane cisterna；
It is equipped with reflux water pump and membrane module in the aerobic membrane cisterna, aerobic membrane cisterna upper end is equipped with overflow port, under aerobic membrane cisterna
End is equipped with interior discharge outlet；The water outlet of the reflux water pump is connected to anaerobic pond；The membrane module water outlet is connected with water producing pipe,
The water producing pipe other end is to produce the mouth of a river；The overflow port is connected with outer discharge outlet, and interior discharge outlet is connected described outer by the first valve
Discharge outlet；
Blower, and the dissolved oxygen instrument for detecting aerobic membrane cisterna are equipped in the equipment room；The blower passes through air
Pipe connects the membrane module；There is dissolved oxygen instrument display on the dissolved oxygen instrument.
It is further: the decentralized integrated sewage treatment device includes a rectangular cabinet, in the cabinet
It is inside successively arranged first partition, second partition, third plate from left to right；Anaerobic pond on the left of the first partition, first every
There is gap between plate upper end and cabinet；It is anoxic pond, second partition lower end and cabinet between the first partition and second partition
Between have gap；The second partition and third plate are aerobic membrane cisternas；It is equipment room, third plate on the right side of the third plate
Surrounding is fixedly connected with box sealing.
The agitating device is mixing pump.
The production mouth of a river is arranged outside equipment room, and production water pump is equipped in water producing pipe；In the forward and backward side for producing water pump
Water producing pipe in be separately installed with the second valve, third valve；It is equipped in the production mouth of a river between the second valve and production water pump
Pressure sensor；The production water pump, the second valve, pressure sensor, third valve are located in equipment room.
Be equipped with power distribution cabinet in the equipment room, power distribution cabinet connect mixing pump, reflux water pump, produce water pump, blower, membrane module,
Dissolved oxygen instrument.
The aerobic membrane cisterna upper end is equipped with the dosing mouth being connected to membrane module.
The membrane module is connected with the solenoid valve for controlling membrane module start and stop.
Compared with prior art, the utility model has the beneficial effects that decentralized integrated sewage treatment device structure letter
Single, the processing discharge of sewage is effectively realized in easy to use, environmental protection and energy saving, and discharge water quality is good, suitable for adapt to water, water quality
Fluctuating change, the Urban Areas of land used anxiety.
Detailed description of the invention
Fig. 1 is the utility model structure diagram (main view)；
Fig. 2 is the utility model structure diagram (top view)；
In figure: 1, mixing pump；2, flow back water pump；3, the second valve；4, water pump is produced；5, blower；6, membrane module；7, distribution
Cabinet；8, the first valve；9, the second valve；10, dissolved oxygen instrument；11, dissolved oxygen instrument display；12, pressure sensor；13, electromagnetism
Valve；14, third valve；15, first partition；16, second partition；17, third plate；A, outer discharge outlet；B, the mouth of a river is produced；C, it intakes
Mouthful；D, overflow port；E, interior discharge outlet；F, dosing mouth；G, water producing pipe；H, air hose.
Specific embodiment
Below with reference to the attached drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out clear
Chu is fully described by, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole realities
Example is applied, the embodiments of the present invention are based on, those having ordinary skill in the art is obtained under the premise of not making creative work
Every other example, belong to the protection scope of the utility model.
As depicted in figs. 1 and 2, decentralized integrated sewage treatment device includes a rectangular cabinet, in cabinet from
Left-to-right is successively arranged first partition 15, second partition 16, third plate 17.Anaerobic pond on the left of first partition 15, first every
There is gap between 15 upper end of plate and cabinet.Anoxic pond between first partition 15 and second partition 16,16 lower end of second partition with
There is gap between cabinet.Second partition 16 and third plate 17 are aerobic membrane cisternas.It is equipment room, third on the right side of third plate 17
17 surrounding of plate is fixedly connected with box sealing.
Anaerobic pond is provided with water inlet C, is equipped with agitating device in anaerobic pond, agitating device is selected specifically to mixing pump 1.
Anoxic pond upper end is connected to by the gap between 15 upper end of first partition and cabinet with anaerobic pond, and anoxic pond lower end is logical
The gap crossed between 16 lower end of second partition and cabinet is connected to aerobic membrane cisterna.
Reflux water pump 2 and membrane module 6 are equipped in aerobic membrane cisterna, aerobic membrane cisterna upper end is equipped with overflow port D, aerobic membrane cisterna lower end
Equipped with interior discharge outlet E.The water outlet of reflux water pump 2 is connected to anaerobic pond, passes through back when aerobic membrane cisterna sewage reaches a certain amount of
Flowing water pump 2 is back to anaerobic pond to carry out circular treatment.Aerobic membrane cisterna upper end is equipped with the dosing mouth F being connected to membrane module 6, adds
Medicine mouth F is used to that medicament to be added to membrane module 6.Membrane module 6 is connected with solenoid valve 13, and membrane module 6 is controlled by solenoid valve 13
Start and stop.
It is arranged outside equipment room and produces mouth of a river B, produces mouth of a river B and pass through 6 water outlet of water producing pipe G connection membrane module, 6 output of membrane module
Water is flowed out by water producing pipe G.Water pump 4 is produced in addition, being equipped in water producing pipe G；In the water producing pipe G of forward and backward side for producing water pump 4
It is separately installed with the second valve 3, third valve 14, the second valve 3, third valve 14 are manual ball valves；In the second valve 3 and production
Pressure sensor 12 is installed in production mouth of a river B between water pump 4.Outer discharge outlet A is additionally provided with outside equipment room, aerobic membrane cisterna overflows
The interior discharge outlet E of the outer discharge outlet A of head piece D connection, aerobic membrane cisterna also connect outer discharge outlet A by the first valve 8；First valve 8
For Hand-operated butterfly valve.Blower 5 is equipped in equipment room, blower 5 is logical for providing to membrane module 6 by air hose H connection membrane module 6
Gas.It is equipped with the dissolved oxygen instrument 10 for detecting aerobic membrane cisterna in equipment room, has dissolved oxygen instrument display 11 on dissolved oxygen instrument 10.If
Standby interior equipped with power distribution cabinet 7, power distribution cabinet 7 is used to power to equipment.
The course of work:
Sewage, even into anaerobic pond, is stirred to react carry out dephosphorization by mixing pump 1 by water inlet C；
After sewage reaches certain water level, anoxic pond is overflowed to by the first partition 15 of setting and is carried out at denitrification reaction
Reason；
Then enter aerobic membrane cisterna by the reserved opening of the low second partition in pond；
Blower 5 is that membrane module 6 provides air quantity progress sewage treatment by air hose H；Treated, and clear water is logical through water producing pipe G
It crosses after production water pump 4 aspirates to reach and produces mouth of a river B.
Anaerobic pond is back to carry out circular treatment by the water pump 2 that flows back when aerobic tank sewage reaches a certain amount of；Add
The effect of medicine mouth F is when equipment is run after a certain period of time, and membrane module 6 will carry out adding medicament when online dosing cleaning；Aerobic film
Pool water level reaches a timing, is discharged by overflow port D, interior discharge outlet E, outer discharge outlet A；Dissolved oxygen instrument 10 and thereon molten
Solve Data Detection and display that oxygen instrument display 11 is used for dissolved oxygen；Pressure sensor 12 is for supervising the pressure of water producing pipe
It surveys；For the adjusting between equipment, all devices component is controlled by power distribution cabinet 7 for first valve 8, the second valve 9, third valve 14
System operation realization movement.
In the present embodiment,
Anaerobic pond: reflux rich phosphorous sludge is thoroughly mixed with sanitary sewage, under strictly anaerobic environmental condition, by certain time
Anaerobic digestion, remove some organic pollutants, a small amount of nitrogenous compound of water phase is converted to N2 (denitrification) and discharges,
The poly- phosphorus microorganism (PAOs) of mud phase releases phosphorus, meets the needs of bacterial multiplication is to phosphorus.
Anoxic pond: reflux nitrification liquid flows into anoxic pond and mixes with the mixed liquor from anaerobic pond, under the conditions of anaerobic environment
(DO≤0.5mg/L), the denitrifying bacteria of anoxic pond is using carbonaceous organic material undecomposed in sewage as carbon source, by the nitrification liquid that flows back
The a large amount of NO3- carried are reduced to N2, head space release.The denitrification phosphorus-collecting microorganism (DPAOs) of mud phase is absorbed using anaerobism section
COD and formed PHB a part supply it is denitrifying simultaneously, another part be configured to anoxic inhale phosphorus.In addition, there is part in anoxic pond
Micro- oxygen, part TP is under the effect of facultative microbe H3P reducing bacteria, gasification finish.
Aerobic membrane cisterna: under complete aerobic condition (DO=2 ~ 4mg/L), the COD in water phase is decomposed under heterotrophic bacteria group effect
For CO2 and H2O.NH3-N in water phase generates NO3- under nitrifier effect, while the oxidation operation in water phase decomposes supply
Phosphorus microorganism energy is inhaled, phosphorus formation ATP or ADP is excessively inhaled from water and enters cell tissue, is enriched in microbial body；Again through film
Component solid-liquor separation is discharged from system in the form of rich phosphorous sludge, reaches biological phosphate-eliminating purpose.It is driven in the gravity for producing water pump auxiliary
Under dynamic, water outlet imports discharge bay.As needed, qualified discharge or safe reuse.
The sewage-treatment plant, it is easy to operate, convenient for management, take up little area, be with low investment, operating cost it is low；It avoids and reduces
Secondary pollution；There are biggish flexibility, adjustability, to adapt to the fluctuating change of water, water quality.Membrane module is flat using A2O-MBR
Plate membrane process cracked traditional A2O technology process using hollow membrane MBR and other plate membrane MBR as core integration apparatus " from
Line cleaning operation too complex " can not be in the long-term running problem in villages and small towns area.It is acted on by the mechanical grading of membrane module, A2O-
The decoupling regulation of hydraulic detention time (HRT) and sludge retention time (SRT) may be implemented in MBR technique, fundamentally solves tradition
A2O technique biological denitrificaion and " releasing phosphorus-suction phosphorus " recycle the inner contradictions relied on SRT, really realize TN, TP stably reaching standard.Separately
Outside, high performance membrane group almost 100% prevents generation cycle long nitrifier and heterotroph bolus flow and loses, and is obviously improved TCA, EMP, N-
The biochemical degradations such as dN, dP process, rate and efficiency, effluent index not only meet the minimum pressure demand of qualified discharge comprehensively, and
Its main indicator can reach " water environment quality standard " (GB3838-2002) IV class require can direct reuse, simply
Change intensive structure design, the more traditional A of occupied area2O technique reduces 50% or more, is particularly suitable for the Urban Areas of land used anxiety.
Above-described embodiment can be seen that the utility model with following obvious advantage:
(1) the long-term stably reaching standard of TN, TP uses A2O-MBR technique fundamentally releases and solves tradition A2O technique biology is de-
Nitrogen and " releasing phosphorus-suction phosphorus " recycle the inner contradictions relied on SRT, independent regulation denitrogenation and dephosphorization process, really realize that TN, TP are normal
Year stably reaching standard is better than the level-one A of GB18918；
(2) the high tradition A of contamination index's removal efficiency2O technique biological tank operates in the area 3000 ~ 5000mgMLSS/L mostly
Between, decentralized integrated sewage treatment device biological tank then operates in the section 10000 ~ 20000mgMLSS/L, that is, A2O work
2 ~ 4 times of skill！Higher sludge concentration is obviously improved the efficiency of pollutant bioconversion degradation, the removal rate of each contamination index
It greatly improves, main indicator all the period of time is better than the ground Table IV class of GB3838；
(3) occupied area is small, and when saving space biological treatment high-concentration waste water, concentration for the treatment of is higher, needs treatment trough
Size is bigger.Using A2O-MBR technique can be operated, it is possible to significantly under high loads due to sludge concentration height
It saves floor occupying area；
(4) the high plate membrane of stable effluent quality, transparency can retain almost all of microorganism, especially be difficult to precipitate
, the microorganism that growth rate is slow, therefore the biology in system is by extreme enrichment, activated sludge acclimatization, increment process significantly
Shorten, the shock proof ability of depth and system of processing is enhanced, and effluent quality is highly stable；
(5) operational management is convenient, safeguards simple tradition A2The high sludge loading operating condition operation of O technique, inevitably occurs
Sludge bulking phenomenon, cause to operate normally for a long time, be discharged it is not up to standard.And A2O-MBR technique is carried out by the suction of film
Mud-water separation, therefore, influence of the sludge bulking to water outlet are much smaller than tradition A2O technique has operational management very convenient, automatically
Change degree is high, safeguards outstanding advantages of simple；
(6) SRT long A2The UF membrane of O-MBR technique makes the ingredient difficult to degrade of the macromolecular in sewage, in the life of finite volume
Possess enough residence times in object pond, substantially increases the degradation efficiency of hardly degraded organic substance.Biological tank high volumetric loading,
It is run under the conditions of low sludge loading, long sludge age, excess sludge emission reduction may be implemented.Due to SRT long, it is more suitable time long micro-
Biological growth is conducive to remove organic substance difficult to degrade in sewage；
(7) capacity of resisting impact load is by force when having large change in the amount of inlet water short time, it may be considered that the short time increases
Film is impacted by flow with achieving the purpose that alleviate.When influent quality variation, since biological tank has higher sludge concentration,
It also can achieve the purpose for alleviating impact in a certain range.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting
Related claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (7)
1. a kind of decentralized integrated sewage treatment device, it is characterised in that: including the anaerobic pond, anoxic pond, good set gradually
Oxygen membrane cisterna and equipment room；
The anaerobic pond is provided with water inlet (C), and agitating device is equipped in anaerobic pond；
The anoxic pond upper end is connected to anaerobic pond, and anoxic pond lower end is connected to aerobic membrane cisterna；
Reflux water pump (2) and membrane module (6) are equipped in the aerobic membrane cisterna, aerobic membrane cisterna upper end is equipped with overflow port (D), aerobic film
Pond lower end is equipped with interior discharge outlet (E)；The water outlet of reflux water pump (2) is connected to anaerobic pond；Membrane module (6) water outlet
It is connected with water producing pipe (G), water producing pipe (G) other end is to produce the mouth of a river (B)；The overflow port (D) is connected with outer discharge outlet (A), interior
Discharge outlet (E) connects the outer discharge outlet (A) by the first valve (8)；
Blower (5) are equipped in the equipment room, and the dissolved oxygen instrument (10) for detecting aerobic membrane cisterna；The blower (5) is logical
It crosses air hose (H) and connects the membrane module (6)；There are dissolved oxygen instrument display (11) on the dissolved oxygen instrument (10).
2. decentralized integrated sewage treatment device according to claim 1, it is characterised in that: the distributing integration
Sewage-treatment plant includes a rectangular cabinet, is successively arranged first partition (15), second from left to right in the cabinet
Partition (16), third plate (17)；It is anaerobic pond on the left of the first partition (15), first partition (15) is between upper end and cabinet
There is gap；It is anoxic pond between the first partition (15) and second partition (16), second partition (16) is between lower end and cabinet
There is gap；The second partition (16) and third plate (17) are aerobic membrane cisternas；It is equipment room on the right side of the third plate (17),
Third plate (17) surrounding is fixedly connected with box sealing.
3. decentralized integrated sewage treatment device according to claim 1, it is characterised in that: the agitating device is mixed
Close pump (1).
4. decentralized integrated sewage treatment device according to claim 1, it is characterised in that: the production mouth of a river (B) sets
It sets outside equipment room, is equipped in water producing pipe (G) and produces water pump (4)；Water producing pipe (G) in the forward and backward side for producing water pump (4)
In be separately installed with the second valve (3), third valve (14)；In the second valve (3) and produce the production mouth of a river (B) between water pump (4)
In pressure sensor (12) are installed；The production water pump (4), the second valve (3), pressure sensor (12), third valve (14)
In equipment room.
5. decentralized integrated sewage treatment device according to claim 4, it is characterised in that: be equipped in the equipment room
Power distribution cabinet (7), power distribution cabinet (7) connect mixing pump (1), reflux water pump (2), produce water pump (4), blower (5), membrane module (6), dissolution
Oxygen instrument (10).
6. decentralized integrated sewage treatment device according to claim 1, it is characterised in that: the aerobic membrane cisterna upper end
Equipped with the dosing mouth (F) being connected to membrane module (6).
7. decentralized integrated sewage treatment device according to claim 1, it is characterised in that: the membrane module (6) is even
It is connected to the solenoid valve (13) for controlling membrane module (6) start and stop.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820969151.1U CN208471840U (en) | 2018-06-22 | 2018-06-22 | Decentralized integrated sewage treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820969151.1U CN208471840U (en) | 2018-06-22 | 2018-06-22 | Decentralized integrated sewage treatment device |
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| CN208471840U true CN208471840U (en) | 2019-02-05 |
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ID=65214761
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| CN201820969151.1U Active CN208471840U (en) | 2018-06-22 | 2018-06-22 | Decentralized integrated sewage treatment device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110282740A (en) * | 2019-06-24 | 2019-09-27 | 西安科技大学 | A kind of processing unit suitable for sewage quantity fluctuation |
| CN112520852A (en) * | 2020-04-08 | 2021-03-19 | 同济大学 | Method for removing and recovering phosphorus in sewage |
| CN114527254A (en) * | 2022-03-04 | 2022-05-24 | 江西中烟工业有限责任公司 | Visual sewage treatment COD and BOD detection device and method |
-
2018
- 2018-06-22 CN CN201820969151.1U patent/CN208471840U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110282740A (en) * | 2019-06-24 | 2019-09-27 | 西安科技大学 | A kind of processing unit suitable for sewage quantity fluctuation |
| CN112520852A (en) * | 2020-04-08 | 2021-03-19 | 同济大学 | Method for removing and recovering phosphorus in sewage |
| CN112520852B (en) * | 2020-04-08 | 2022-06-14 | 同济大学 | Method for removing and recovering phosphorus in sewage |
| CN114527254A (en) * | 2022-03-04 | 2022-05-24 | 江西中烟工业有限责任公司 | Visual sewage treatment COD and BOD detection device and method |
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