CN209259874U - A kind of wastewater collection and processing system - Google Patents
A kind of wastewater collection and processing system Download PDFInfo
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- CN209259874U CN209259874U CN201821327904.5U CN201821327904U CN209259874U CN 209259874 U CN209259874 U CN 209259874U CN 201821327904 U CN201821327904 U CN 201821327904U CN 209259874 U CN209259874 U CN 209259874U
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- waste water
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Abstract
The utility model discloses a kind of wastewater collection and processing systems, including acidic and alkaline waste water Collecting and dealing unit, organic wastewater Collecting and dealing unit, removing wastewater collection and processing unit, TMAH wastewater collection and processing unit, CF wastewater collection and processing unit, copper-containing wastewater Collecting and dealing unit, phosphorus-containing wastewater Collecting and dealing unit and fluoride waste Collecting and dealing unit；A kind of wastewater collection provided by the utility model and processing system, by identifying to the ingredient in waste water, different former ponds is divided into this, carry out corresponding processing mode, improve the treatment effect to waste water, it reduces waste water and dysgenic probability is caused to environment, improve the rate of recovery of waste water, reduce production cost.
Description
Technical field
The utility model relates generally to technical field of waste water processing, in particular to a kind of wastewater collection and processing system.
Background technique
With the development of mankind's science and technology, the amount of generated industrial wastewater and sanitary wastewater is huge.Industrial wastewater refers to
Waste water, sewage and the waste liquid generated during industrial production, wherein containing the industrial production materials, the intermediate product that outflow with water
With the pollutant generated in product and production process.Due to containing a large amount of particulate matter not soluble in water in waste water and being dissolved in water
Chemical pollutant, if these direct discharging of waste water to the external world, environment certainly will be polluted, influence human health.
The prior art is generally relatively simple to the processing method of waste water, not only haves the defects that treatment effect is bad, moreover,
Generally treated at present, and waste water is just directly discharged to the external world after meeting environmental requirement, without to handled waste water progress
It recycles, therefore, causes the wasting of resources, while improving production cost.It is all used further for the waste water of different types
Agreement processing method, do not suit the remedy to the case, produce additional side effect.
Summary of the invention
For the deficiency overcome, the utility model provides a kind of wastewater collection and processing system.
In order to achieve the above object, the utility model uses following technical scheme: a kind of wastewater collection and processing system, packet
It is useless to include acidic and alkaline waste water Collecting and dealing unit, organic wastewater Collecting and dealing unit, removing wastewater collection and processing unit, TMAH
Water Collecting and dealing unit, CF wastewater collection and processing unit, copper-containing wastewater Collecting and dealing unit and phosphorus-containing wastewater collect and
Processing unit；
The acidic and alkaline waste water Collecting and dealing unit includes acidic and alkaline waste water former pond, pH conditioning tank I, releases pond, the acid
Alkali waste water former pond is connected with the pH conditioning tank I, and the pond that releases is connected with the pH conditioning tank I；
The organic wastewater Collecting and dealing unit includes organic wastewater former pond, and the organic wastewater former pond sequentially connects
Connect pH conditioning tank II and Anoxic/Aerobic reaction tank；
The removing wastewater collection and processing unit include removing waste water former pond, and the removing waste water former pond sequentially connects
Connect pH conditioning tank III, coagulation air-float reaction tank and Anoxic/Aerobic reaction tank；
The TMAH wastewater collection and processing unit include TMAH waste water former pond, and the TMAH waste water former pond sequentially connects
Connect pH conditioning tank IV, coagulation air-float reaction tank and Anoxic/Aerobic reaction tank；
The CF wastewater collection and processing unit include CF waste water former pond, and the CF waste water former pond is sequentially connected with pH tune
Save pond V, coagulation air-float reaction tank and Anoxic/Aerobic reaction tank；
The copper-containing wastewater Collecting and dealing unit includes copper-containing wastewater former pond, and the copper-containing wastewater former pond sequentially connects
Connect pH conditioning tank VI, heavy metal reaction tank, coagulative precipitation tank II and Anoxic/Aerobic reaction tank；
The phosphorus-containing wastewater Collecting and dealing unit includes phosphorus-containing wastewater former pond, and the phosphorus-containing wastewater former pond sequentially connects
Connect pH conditioning tank VII, coagulative precipitation tank III and Anoxic/Aerobic reaction tank；
The Anoxic/Aerobic reaction tank connects coagulative precipitation tank I, and the coagulative precipitation tank I connects biochemistry pool and releases pond,
The biochemistry pool is connected with cooling tower and scrubbing tower, described to release pond connection stain disease discharge manifold.
Preferably, the acidic and alkaline waste water former pond, organic wastewater former pond, removing waste water former pond, TMAH waste water are former
Filter screen is equipped in pond, CF waste water former pond, copper-containing wastewater former pond, phosphorus-containing wastewater former pond and fluoride waste former pond
Sieve.
Preferably, the pore size of the filtering mesh screen is 2mm ~ 5mm.
Preferably, the bottom of pond of the Anoxic/Aerobic reaction tank is equipped with power aerator.
The utility model has the advantages that compared with prior art, the utility model has the advantage that provided by the utility model a kind of useless
Water Collecting and dealing system is divided into different former ponds with this, carries out corresponding place by identifying to the ingredient in waste water
Reason mode improves the treatment effect to waste water, reduces waste water and causes dysgenic probability to environment, improves waste water
The rate of recovery reduces production cost.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Specific embodiment
In the following with reference to the drawings and specific embodiments, the utility model is furtherd elucidate, it should be understood that these embodiments are only used for
Illustrate the utility model rather than limitation the scope of the utility model, after having read the utility model, art technology
Personnel fall within the application range as defined in the appended claims to the modification of the various equivalent forms of the utility model.
As shown in Figure 1, wastewater collection and processing system, including acidic and alkaline waste water Collecting and dealing unit, organic wastewater are collected
And processing unit, removing wastewater collection and processing unit, TMAH wastewater collection and processing unit, CF wastewater collection and processing are single
Member, copper-containing wastewater Collecting and dealing unit, phosphorus-containing wastewater Collecting and dealing unit and fluoride waste Collecting and dealing unit；
Acidic and alkaline waste water Collecting and dealing unit includes acidic and alkaline waste water former pond, pH conditioning tank I and releases pond, is examined in waste water
It after measuring acidic and alkaline waste water, is isolated out and flows into acidic and alkaline waste water former pond, then flow into pH conditioning tank I, adjust its pH, pass through
It releases after pond examines its water quality qualified and flows into stain disease discharge manifold.
Organic wastewater Collecting and dealing unit includes organic wastewater former pond, and organic wastewater former pond is sequentially connected with pH adjusting
Pond II, coagulative precipitation tank I, releases pond or biochemistry pool at Anoxic/Aerobic reaction tank, after detecting organic wastewater in waste water, by it
It isolates and flows into organic wastewater former pond, then flow into pH conditioning tank II and neutralize its pH, carried out by Anoxic/Aerobic reaction tank
Biochemical treatment, then flow into coagulative precipitation tank I and be settled out waste material, the water for having separated waste material is flowed into and examines its water quality, after qualified
Stain disease discharge manifold is flowed by releasing pond, waste material flows into biochemistry pool and carries out MBR+RO reaction, then flows into cooling tower or washing
Moisturizing is recycled in tower；
It removes wastewater collection and processing unit includes removing waste water former pond, removing waste water former pond is sequentially connected with pH adjusting
Pond III, Anoxic/Aerobic reaction tank, coagulative precipitation tank I, releases pond or biochemistry pool at coagulation air-float reaction tank I, detects in waste water
After removing waste water, it is isolated out inflow removing waste water former pond, then flows into pH conditioning tank III and neutralizes its pH, flow into coagulation
Air bearing goes out waste material in air bearing reaction tank I, and remaining water is flowed into Anoxic/Aerobic reaction tank and carries out biochemical treatment, then flows into coagulation
It is settled out waste material in sedimentation basin I, the water for having separated waste material is flowed into and examines its water quality, flows into stain disease by releasing pond after qualification
Discharge manifold, waste material flow into biochemistry pool and carry out MBR+RO reaction, then flow into moisturizing in cooling tower or scrubbing tower and recycle；
TMAH wastewater collection and processing unit include TMAH waste water former pond, and TMAH waste water former pond is sequentially connected with pH adjusting
Pond IV, Anoxic/Aerobic reaction tank, coagulative precipitation tank I, releases pond or biochemistry pool at coagulation air-float reaction tank II, detects in waste water
It out after TMAH waste water, is isolated out and flows into TMAH waste water former pond, then flow into pH conditioning tank IV and neutralize its pH, flow into mixed
Air bearing goes out waste material in solidifying air bearing reaction tank II, and remaining water is flowed into Anoxic/Aerobic reaction tank and carries out biochemical treatment, then is flowed into
It is settled out waste material in coagulative precipitation tank I, the water for having separated waste material is flowed into and examines its water quality, it is dirty by releasing pond inflow after qualified
Discharge of wastewater general pipeline, waste material flow into biochemistry pool and carry out MBR+RO reaction, then flow into moisturizing in cooling tower or scrubbing tower and recycle；
CF wastewater collection and processing unit include CF waste water former pond, CF waste water former pond be sequentially connected with pH conditioning tank V,
Coagulation air-float reaction tank III, coagulative precipitation tank I, releases pond or biochemistry pool at Anoxic/Aerobic reaction tank, detects that CF is useless in waste water
It after water, is isolated out and flows into CF waste water former pond, then flow into pH conditioning tank V and neutralize its pH, flow into coagulation air-float reaction
Air bearing goes out waste material in pond III, and remaining water is flowed into Anoxic/Aerobic reaction tank and carries out biochemical treatment, then flows into coagulative precipitation tank I
In be settled out waste material, the water that will have separated waste material, which flows into, examines its water quality, it is qualified after by releasing pond, to flow into stain disease discharge total
Pipe, waste material flow into biochemistry pool and carry out MBR+RO reaction, then flow into moisturizing in cooling tower or scrubbing tower and recycle；
Copper-containing wastewater Collecting and dealing unit includes copper-containing wastewater former pond, and copper-containing wastewater former pond is sequentially connected with pH adjusting
Pond VI, coagulative precipitation tank II, Anoxic/Aerobic reaction tank, coagulative precipitation tank I, releases pond or biochemistry pool at heavy metal reaction tank, useless
It after detecting copper-containing wastewater in water, is isolated out and flows into copper-containing wastewater former pond, then flow into pH conditioning tank VI and neutralize it
PH first flows into heavy metal reaction tank, copper is precipitated, and flows into coagulative precipitation tank II and is settled out waste material for the first time, will be left
Water flow into Anoxic/Aerobic reaction tank and carry out biochemical treatment, then flow into coagulative precipitation tank I and be settled out waste material, will separate useless
The water of material, which flows into, examines its water quality, flows into stain disease discharge manifold by releasing pond after qualification, waste material flows into biochemistry pool and carries out MBR
+ RO reaction, then flow into moisturizing in cooling tower or scrubbing tower and recycle；
Phosphorus-containing wastewater Collecting and dealing unit includes phosphorus-containing wastewater former pond, and phosphorus-containing wastewater former pond is sequentially connected with pH adjusting
Pond VII, Anoxic/Aerobic reaction tank, coagulative precipitation tank I, releases pond or biochemistry pool at coagulative precipitation tank III；
Wherein the bottom of pond of Anoxic/Aerobic reaction tank is equipped with power aerator, dynamic for the process flow of anoxic+aerobic,
Guarantee that waste water energy sufficiently reflects.
Fluoride waste Collecting and dealing unit includes fluoride waste former pond, and fluoride waste former pond is sequentially connected with pH adjusting
Pond VIII, coagulative precipitation tank IV and fluoride waste discharge are managed, and after detecting fluoride waste in waste water, are isolated out inflow and are contained
Then fluorine waste water former pond flows into pH conditioning tank VIII and neutralizes its pH, then flows into coagulating sedimentation IV and be settled out waste material, will separate
The water of waste material, which flows into, examines its water quality, is emitted into during fluoride waste discharge manages after qualified.
In addition, acidic and alkaline waste water former pond, organic wastewater former pond, removing waste water former pond, TMAH waste water former pond, CF are useless
Filtering mesh screen, filter screen are equipped in water former pond, copper-containing wastewater former pond, phosphorus-containing wastewater former pond and fluoride waste former pond
The pore size of sieve is 2mm ~ 5mm, and setting filtering mesh screen can effectively stop waste material, prevents it from flowing into down by pipeline
In one reaction tank.
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 (4)
1. a kind of wastewater collection and processing system, it is characterised in that: received including acidic and alkaline waste water Collecting and dealing unit, organic wastewater
Collection and processing unit, removing wastewater collection and processing unit, TMAH wastewater collection and processing unit, CF wastewater collection and processing are single
Member, copper-containing wastewater Collecting and dealing unit, phosphorus-containing wastewater Collecting and dealing unit and fluoride waste Collecting and dealing unit；
The acidic and alkaline waste water Collecting and dealing unit includes acidic and alkaline waste water former pond, pH conditioning tank I, releases pond, and the soda acid is useless
Water former pond is connected with the pH conditioning tank I, and the pond that releases is connected with the pH conditioning tank I；
The organic wastewater Collecting and dealing unit includes organic wastewater former pond, and the organic wastewater former pond is sequentially connected with pH
Conditioning tank II and Anoxic/Aerobic reaction tank；
The removing wastewater collection and processing unit include removing waste water former pond, and the removing waste water former pond is sequentially connected with pH
Conditioning tank III, coagulation air-float reaction tank I and Anoxic/Aerobic reaction tank；
The TMAH wastewater collection and processing unit include TMAH waste water former pond, and the TMAH waste water former pond is sequentially connected with pH
Conditioning tank IV, coagulation air-float reaction tank II and Anoxic/Aerobic reaction tank；
The CF wastewater collection and processing unit include CF waste water former pond, and the CF waste water former pond is sequentially connected with pH conditioning tank
V, coagulation air-float reaction tank III and Anoxic/Aerobic reaction tank；
The copper-containing wastewater Collecting and dealing unit includes copper-containing wastewater former pond, and the copper-containing wastewater former pond is sequentially connected with pH
Conditioning tank VI, heavy metal reaction tank, coagulative precipitation tank II and Anoxic/Aerobic reaction tank；
The phosphorus-containing wastewater Collecting and dealing unit includes phosphorus-containing wastewater former pond, and the phosphorus-containing wastewater former pond is sequentially connected with pH
Conditioning tank VII, coagulative precipitation tank III and Anoxic/Aerobic reaction tank；
The Anoxic/Aerobic reaction tank connects coagulative precipitation tank I, and the coagulative precipitation tank I connects biochemistry pool and releases pond, described
Biochemistry pool is connected with cooling tower and scrubbing tower, described to release pond connection stain disease discharge manifold；
The fluoride waste Collecting and dealing unit includes fluoride waste former pond, and the fluoride waste former pond is sequentially connected with pH
Conditioning tank VIII, coagulative precipitation tank IV and fluoride waste discharge are managed.
2. wastewater collection according to claim 1 and processing system, it is characterised in that: the acidic and alkaline waste water former pond has
It is machine waste water former pond, removing waste water former pond, TMAH waste water former pond, CF waste water former pond, copper-containing wastewater former pond, phosphorous useless
Filtering mesh screen is equipped in water former pond and fluoride waste former pond.
3. wastewater collection according to claim 2 and processing system, it is characterised in that: the pore size of the filtering mesh screen
For 2mm ~ 5mm.
4. wastewater collection according to claim 1 and processing system, it is characterised in that: the pond of the Anoxic/Aerobic reaction tank
Bottom is equipped with power aerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821327904.5U CN209259874U (en) | 2018-08-17 | 2018-08-17 | A kind of wastewater collection and processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821327904.5U CN209259874U (en) | 2018-08-17 | 2018-08-17 | A kind of wastewater collection and processing system |
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| Publication Number | Publication Date |
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| CN209259874U true CN209259874U (en) | 2019-08-16 |
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| CN201821327904.5U Active CN209259874U (en) | 2018-08-17 | 2018-08-17 | A kind of wastewater collection and processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112174439A (en) * | 2020-10-14 | 2021-01-05 | 上海三邦水处理技术有限公司 | LED chip manufacturing industry wastewater treatment engineering process |
-
2018
- 2018-08-17 CN CN201821327904.5U patent/CN209259874U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112174439A (en) * | 2020-10-14 | 2021-01-05 | 上海三邦水处理技术有限公司 | LED chip manufacturing industry wastewater treatment engineering process |
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