CN207210213U - A kind of deep-well aeration sewage disposal system - Google Patents
A kind of deep-well aeration sewage disposal system Download PDFInfo
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- CN207210213U CN207210213U CN201721154165.XU CN201721154165U CN207210213U CN 207210213 U CN207210213 U CN 207210213U CN 201721154165 U CN201721154165 U CN 201721154165U CN 207210213 U CN207210213 U CN 207210213U
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Abstract
The utility model discloses a kind of deep-well aeration sewage disposal system, including regulating reservoir, microfilter, neutralize adsorption tank, hydrolysis acidification pool, deep-well, deaerate pond, two sedimentation basins, coagulative precipitation tank, sandfiltration pot, outer row pond and sludge concentration tank, the regulating reservoir is connected with microfilter by pipeline, the microfilter is connected with neutralizing adsorption tank by pipeline, the neutralization adsorption tank is connected with hydrolysis acidification pool by pipeline, the hydrolysis acidification pool is connected with deep-well by pipeline, the deep-well is connected with degassing pond by pipeline, the degassing pond is connected with two sedimentation basins by pipeline, the upper end of two sedimentation basin is connected with coagulative precipitation tank by pipeline, the coagulative precipitation tank is connected with sandfiltration pot by pipeline, the sandfiltration pot is connected with outer row pond by pipeline.The utility model beneficial effect：The advantages of with good waste water treatment effect, and the wasting of resources is avoided that, the characteristics of reducing production cost, and extensive processing can be applied to.
Description
Technical field
It the utility model is related to technical field of waste water processing, and in particular to a kind of deep-well aeration sewage disposal system.
Background technology
At present, the processing method of waste water includes physical method and chemical method, such as physical method, absorption method；Chemical method,
Such as oxidizing process, electrolysis, photocatalytic method.With industrial expansion, caused amount of industrial wastewater is huge.Industrial wastewater refers to
Caused waste water, sewage and waste liquid during industrial production, wherein containing the industrial production materials outflowed with water, middle production
Caused pollutant in thing and product and production process.Due to contain in industrial wastewater substantial amounts of particulate matter not soluble in water and
The chemical pollutant of water is dissolved in, if these industrial wastewaters are directly discharged to the external world, environment certainly will be polluted, influence human health.
Prior art is typically relatively simple to the processing method of waste water, the defects for the treatment of effect is bad not only be present, moreover, general at present
Waste water after processing is just directly discharged to the external world after environmental requirement is met, without carrying out recovery profit to handled waste water
With therefore, causing the wasting of resources, while improve production cost.
Utility model content
The utility model provides a kind of deep-well aeration sewage disposal system, solves showing of being run into above-mentioned background technology
There is technology typically relatively simple to the processing method of waste water, the defects for the treatment of effect is bad not only be present, moreover, general place at present
Waste water after reason is just directly discharged to the external world after environmental requirement is met, without being recycled to handled waste water,
Therefore, the problem of causing the wasting of resources, while improving production cost.
In order to solve the above-mentioned technical problem, the utility model provides following technical scheme：
A kind of deep-well aeration sewage disposal system of the utility model, including regulating reservoir, microfilter, neutralization absorption
Pond, hydrolysis acidification pool, deep-well, degassing pond, two sedimentation basins, coagulative precipitation tank, sandfiltration pot, outer row pond and sludge concentration tank, it is described
Regulating reservoir is connected with microfilter by pipeline, and the microfilter is connected with neutralizing adsorption tank by pipeline, in described
Be connected with adsorption tank with hydrolysis acidification pool by pipeline, the hydrolysis acidification pool is connected with deep-well by pipeline, the deep-well with
Degassing pond is connected by pipeline, and the degassing pond is connected with two sedimentation basins by pipeline, the upper end of two sedimentation basin and coagulation
Sedimentation basin is connected by pipeline, and the coagulative precipitation tank is connected with sandfiltration pot by pipeline, and the sandfiltration pot passes through with outer row pond
Pipeline connects.
As a kind of optimal technical scheme of the present utility model, the lower end of two sedimentation basin is with neutralizing adsorption tank, hydrolysis
Acidification pool, deep-well are connected by pipeline.
As a kind of optimal technical scheme of the present utility model, the neutralization adsorption tank, hydrolysis acidification pool, deep-well, two sink
Shallow lake pond, coagulative precipitation tank, sandfiltration pot and sludge concentration tank are connected by pipeline.
As a kind of optimal technical scheme of the present utility model, the pipeline between the regulating reservoir and microfilter is set
There is water pump.
As a kind of optimal technical scheme of the present utility model, pH adjusting agent is added in the neutralization adsorption tank.
The beneficial effect that the utility model is reached is：This kind of deep-well aeration sewage disposal system, there is wastewater treatment
The advantages of effect is good, and the wasting of resources is avoided that, the characteristics of reducing production cost, and extensive processing can be applied to.
Brief description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and a part for constitution instruction, with this practicality
New embodiment is used to explain the utility model together, does not form to limitation of the present utility model.
In the accompanying drawings：
Fig. 1 is a kind of overall structure figure of deep-well aeration sewage disposal system of the utility model；
In figure：1st, regulating reservoir；2nd, water pump；3rd, microfilter；4th, pH adjusting agent；5th, adsorption tank is neutralized；6th, hydrolysis acidification
Pond；7th, deep-well；8th, deaerate pond；9th, two sedimentation basin；10th, coagulative precipitation tank；11st, sandfiltration pot；12nd, outer row pond；13rd, sludge condensation
Pond.
Embodiment
Preferred embodiment of the present utility model is illustrated below in conjunction with accompanying drawing, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain the utility model, be not used to limit the utility model.
Embodiment：As shown in figure 1, a kind of deep-well aeration sewage disposal system of the utility model, including it is regulating reservoir 1, super
Micro-filter 3, neutralize adsorption tank 5, hydrolysis acidification pool 6, deep-well 7, degassing pond 8, two sedimentation basins 9, coagulative precipitation tank 10, sandfiltration pot
11st, outer row pond 12 and sludge concentration tank 13, regulating reservoir 1 are connected with microfilter 3 by pipeline, and microfilter 3 is with neutralizing
Adsorption tank 5 is connected by pipeline, is neutralized adsorption tank 5 and is connected with hydrolysis acidification pool 6 by pipeline, hydrolysis acidification pool 6 is logical with deep-well 7
Piping is connected, and deep-well 7 is connected with degassing pond 8 by pipeline, and degassing pond 8 is connected with two sedimentation basins 9 by pipeline, two sedimentation basins
9 upper end is connected with coagulative precipitation tank 10 by pipeline, and coagulative precipitation tank 10 is connected with sandfiltration pot 11 by pipeline, sandfiltration pot 11
It is connected with outer row pond 12 by pipeline.
The lower end of two sedimentation basins 9 is connected with neutralizing adsorption tank 5, hydrolysis acidification pool 6, deep-well 7 by pipeline, is easy to two precipitations
The activated sludge of precipitation is partly refluxed to deep-well 7 in pond 9, and redundance incorporation neutralizes adsorption tank 5 and hydrolysis acidification pool 6 etc., just
In neutralization precipitation pond 5 SS in waste water and partial organic substances and poisonous and harmful are removed using the adsorptivity of activated sludge, coherency
Material.
It is dense to neutralize adsorption tank 5, hydrolysis acidification pool 6, deep-well 7, two sedimentation basins 9, coagulative precipitation tank 10, sandfiltration pot 11 and sludge
Contracting pond 13 is connected by pipeline, is easy to neutralize adsorption tank 5, hydrolysis acidification pool 6, deep-well 7, second pond 9, coagulative precipitation tank 10, sand
Sludge caused by the grade of filter tank 11 is discharged into sludge concentration tank 13, and after concentrated dehydration, press filtration is carried out to sludge, is at utmost reduced dirty
Influence of the mud to environment.
Pipeline between regulating reservoir 1 and microfilter 3 is provided with water pump 2, is easy to the waste water in regulating reservoir 1 being transported to
In super prestige filter 3.
Neutralize adsorption tank 5 in add pH adjusting agent 4, be easy to waste water in and adsorption tank 5 in and and adsorption precipitation.
Specifically, comprehensive wastewater enters in regulating reservoir 1, water quality and quantity regulation, the waste water after regulation are carried out in regulating reservoir 1
Lifted, flowed through in microfilter 3 through the pump of water 2, in microfilter 3 is removed and entered in waste water after bulky grain solid content and inhaled
Attached pond 5, pH adjusting agent 4 is added in and in adsorption tank 5, waste water is neutralized, while will be amount of activated in two sedimentation basins 9
Sludge is mixed by pipeline and neutralized in adsorption tank 5, and SS and part in waste water are removed using the adsorptivity of activated sludge, coherency
Organic matter and poisonous and harmful substance, in neutralization precipitation pond 5 supernatant gravity flow enter in hydrolysis acidification pool 6, be passed through a certain amount of sky
Gas, using the hydrolysis acidification section of anaerobic fermentation process, makes insoluble organic matter in water be converted into solubility to hydrolysis acidification pool 6
Organic matter, the macromolecular substances of difficult degradation are converted into the small-molecule substance of easily biological-degradable and improve the biochemical of waste water
Property, supernatant gravity flow enters deep-well 7 and pushes up pond and carry out the processing of the aeration biochemical of deep-well 7, because the hydrostatic pressure of deep-well 7 is high, dissolved oxygen is dense
Degree is big, oxidability is strong, the oxidation operation in waste water quickly and efficiently can be decomposed into CO2、H2O, change are harmful to be harmless；It is deep
Well 7 enters two sedimentation basins 9 progress separation of solid and liquid, the activity of two sedimentation basins, 9 interior precipitation after handling the degassed pond removing microbubble of water
Sludge part is back to deep-well 7, and redundance, which mixes, neutralizes adsorption tank 5 and hydrolysis acidification pool 6 etc., the supernatant in two sedimentation basins 9
Liquid gravity flow enters coagulative precipitation tank 10, and a small amount of coagulated agent, reacted removal part COD, supernatant are added in coagulative precipitation tank 10
Liquid gravity flow enters sandfiltration pot 11, and filtering clarification, the water outlet of sandfiltration pot 11 gravity flow enters reuse and outer row pond 12, to treat reuse, neutralizes
Sludge caused by adsorption tank 5, two sedimentation basins 9, coagulative precipitation tank 10, sandfiltration pot 11 etc. is discharged into sludge concentration tank 13, concentrated de-
After water, press filtration is carried out to sludge, at utmost reduces influence of the sludge to environment, supernatant flows into regulating reservoir 1.
This kind of deep-well aeration sewage disposal system, there is the advantages of good waste water treatment effect, and be avoided that resource wave
Take, the characteristics of reducing production cost, and extensive processing can be applied to.
Finally it should be noted that：Preferred embodiment of the present utility model is the foregoing is only, is not limited to this
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Carry out equivalent substitution.All any modification, equivalent substitution and improvements within the spirit and principles of the utility model, made etc.,
It should be included within the scope of protection of the utility model.
Claims (5)
1. a kind of deep-well aeration sewage disposal system, including regulating reservoir (1), microfilter (3), neutralization adsorption tank (5), water
Solve acidification pool (6), deep-well (7), degassing pond (8), two sedimentation basins (9), coagulative precipitation tank (10), sandfiltration pot (11), outer row pond
(12) and sludge concentration tank (13), it is characterised in that the regulating reservoir (1) is connected with microfilter (3) by pipeline, described
Microfilter (3) is connected with neutralizing adsorption tank (5) by pipeline, and the neutralization adsorption tank (5) passes through with hydrolysis acidification pool (6)
Pipeline is connected, and the hydrolysis acidification pool (6) is connected with deep-well (7) by pipeline, and the deep-well (7) passes through pipe with degassing pond (8)
Road is connected, and degassing pond (8) is connected with two sedimentation basins (9) by pipeline, the upper end of two sedimentation basin (9) and coagulating sedimentation
Pond (10) is connected by pipeline, and the coagulative precipitation tank (10) is connected with sandfiltration pot (11) by pipeline, the sandfiltration pot (11)
It is connected with outer row pond (12) by pipeline.
A kind of 2. deep-well aeration sewage disposal system according to claim 1, it is characterised in that two sedimentation basin
(9) lower end is connected with neutralizing adsorption tank (5), hydrolysis acidification pool (6), deep-well (7) by pipeline.
A kind of 3. deep-well aeration sewage disposal system according to claim 1, it is characterised in that the neutralization adsorption tank
(5), hydrolysis acidification pool (6), deep-well (7), two sedimentation basins (9), coagulative precipitation tank (10), sandfiltration pot (11) and sludge concentration tank
(13) connected by pipeline.
A kind of 4. deep-well aeration sewage disposal system according to claim 1, it is characterised in that the regulating reservoir (1)
Pipeline between microfilter (3) is provided with water pump (2).
A kind of 5. deep-well aeration sewage disposal system according to claim 1, it is characterised in that the neutralization adsorption tank
(5) addition pH adjusting agent (4) in.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721154165.XU CN207210213U (en) | 2017-09-11 | 2017-09-11 | A kind of deep-well aeration sewage disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721154165.XU CN207210213U (en) | 2017-09-11 | 2017-09-11 | A kind of deep-well aeration sewage disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207210213U true CN207210213U (en) | 2018-04-10 |
Family
ID=61823812
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721154165.XU Expired - Fee Related CN207210213U (en) | 2017-09-11 | 2017-09-11 | A kind of deep-well aeration sewage disposal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207210213U (en) |
-
2017
- 2017-09-11 CN CN201721154165.XU patent/CN207210213U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180410 Termination date: 20210911 |