CN209602309U - A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system - Google Patents
A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system Download PDFInfo
- Publication number
- CN209602309U CN209602309U CN201822023506.0U CN201822023506U CN209602309U CN 209602309 U CN209602309 U CN 209602309U CN 201822023506 U CN201822023506 U CN 201822023506U CN 209602309 U CN209602309 U CN 209602309U
- Authority
- CN
- China
- Prior art keywords
- pond
- reaction
- tank
- phosphorus
- fenton
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing systems, including wastewater treatment component and Treatment of Sludge component, wastewater treatment component includes the first intermediate pool, the second intermediate pool, front end Fenton's reaction, biochemical reaction treatment process, rear end Fenton's reaction, end filtration process and the discharge pond that waste water successively passes through, evaporator is equipped between first intermediate pool and the second intermediate pool, processing of the Treatment of Sludge component as settled sludge in wastewater treatment component, and the waste water in sludge can be returned and be handled again through wastewater treatment component.The utility model is compact to design, rationally distributed, unified management, with strong points and high treating effect, can persistently handle sewage, and has rear end guarantee processing, it is ensured that wastewater treatment qualified discharge.
Description
Technical field
The utility model relates to field of waste water treatment, in particular to a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system.
Background technique
Nowadays with the continuous development of Urbanization in China, sewage quantity is also being continuously increased.These sewage are seriously dirty
Contaminate environment, it is necessary to can just discharge after sewage disposal device processing is up to standard.
And pass of the construction and operation of sewage treatment project as industrial important component and water pollution control
Key link, meaning are very great.
Since the construction and operation of sewage treatment project be not single, cost is larger, and is restricted and influenced by many factors,
Wherein the optimum choice for the treatment of process scheme is the most key to the operational effect and reduction expense that ensure treatment plant, it is therefore necessary to
According to determining standard and rule, from the idea of global optimization, in conjunction with design scale, sewage quality characteristic and enterprise
The physical condition of industry production and requirement, select practical, economical rationality treatment process scheme, through overall technique Economic contrast
Preferably go out optimal general process scheme and embodiment afterwards.
Utility model content
The utility model is to solve the above problems, provide a kind of compact to design, rationally distributed, unified management, with strong points
And the not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system of high treating effect, persistently sewage can be handled, and have rear end guarantor
Barrier processing, it is ensured that wastewater treatment qualified discharge.
In order to achieve the above objectives, the technical solution adopted in the utility model is: one kind is not at Nitrogen-and Phosphorus-containing comprehensive wastewater rear end
Reason system, including wastewater treatment component and Treatment of Sludge component, the wastewater treatment component include first that waste water successively passes through
Intermediate pool, the second intermediate pool, front end Fenton's reaction, biochemical reaction treatment process, rear end Fenton's reaction, end filtration process
With discharge pond, evaporator, the front end Fenton's reaction and institute are equipped between first intermediate pool and the second intermediate pool
It states and is equipped with level-one coagulating basin, two-stage coagulation pond and third intermediate pool between biochemical reaction treatment process, at the biochemical reaction
Secondary settling tank is equipped between science and engineering sequence and the rear end Fenton's reaction, between the rear end Fenton's reaction and the end filtration process
It is successively arranged three-level coagulating sedimentation and the 4th intermediate pool；
The Treatment of Sludge component includes sludge concentration tank and filter press, and the sludge concentration tank collects the wastewater treatment
Sludge in component, and return line is equipped between the sludge concentration tank, the filter press and second intermediate pool；
Return line also is provided between the end filtration process, the discharge pond and second intermediate pool.
Further, the front end Fenton's reaction includes the first conditioning tank set gradually, front end Fenton's reaction pond and
Two conditioning tanks, the rear end Fenton's reaction include the third conditioning tank set gradually, rear end Fenton's reaction pond and the 4th conditioning tank.
Further, first conditioning tank and the third conditioning tank are acid conditioning tank, second conditioning tank and
4th conditioning tank is alkaline conditioning tank.
Further, the biochemical reaction treatment process includes the hydrolysis acidification pool, anaerobic pond and aerobic tank successively carried out.
Further, the level-one coagulating basin, the two-stage coagulation pond, the hydrolysis acidification pool, the anaerobic pond, described
Aerobic tank, the secondary settling tank and the three-level coagulating basin with the sludge concentration tank sludge pipeline connection.
Further, the end filtration process includes sand coarse aggregate ratio system and carbon filtration system, and the discharge pond is equipped with recoil
Wash pipeline and the sand coarse aggregate ratio system, the carbon filtration system connectivity.
Further, be added in the level-one coagulating basin, the two-stage coagulation pond and the three-level coagulating basin PAC and
PAM。
Further, the third intermediate pool is equipped with acid/base chemicals dosing plant.
In conclusion the utility model has following advantages:
The utility model is compact to design, rationally distributed, unified management, Nitrogen-and Phosphorus-containing is not comprehensive for strong points and high treating effect
Waste water back-end processing system can persistently be handled sewage, and have rear end guarantee processing, it is ensured that wastewater treatment row up to standard
It puts.
In general, the utility model integrated artistic more coordinate, effect it is more preferable, substantially increase sewage treatment management water
It is flat.
Detailed description of the invention
Fig. 1 is the structure flow chart of the utility model；
Fig. 2 is biochemical reaction processing front end process schematic diagram；
Fig. 3 is biochemical reaction treatment process schematic diagram；
Fig. 4 is biochemical reaction processing rear end process schematic diagram.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and embodiments:
Embodiment 1:
A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system, as shown in Figure 1, including wastewater treatment component and Treatment of Sludge
Component.
Wherein, wastewater treatment component includes the first intermediate pool, the second intermediate pool, front end Fenton that waste water successively passes through
Reaction, biochemical reaction treatment process, rear end Fenton's reaction, end filtration process and discharge pond, first intermediate pool and
Between second intermediate pool be equipped with evaporator, between front end Fenton's reaction and biochemical reaction treatment process be equipped with level-one coagulating basin,
Two-stage coagulation pond and third intermediate pool, are equipped with secondary settling tank between biochemical reaction treatment process and rear end Fenton's reaction, rear end is fragrant
Pause and is successively arranged three-level coagulating sedimentation and the 4th intermediate pool between reaction and end filtration process；
Front end Fenton's reaction includes the first conditioning tank set gradually, front end Fenton's reaction pond and the second conditioning tank, rear end
Fenton's reaction includes the third conditioning tank set gradually, rear end Fenton's reaction pond and the 4th conditioning tank, specifically, the first conditioning tank
It is acid conditioning tank with the third conditioning tank, the second conditioning tank and the 4th conditioning tank are alkaline conditioning tank.
In wastewater treatment component, biochemical reaction treatment process includes the hydrolysis acidification pool successively carried out, anaerobic pond and aerobic
Pond
And Treatment of Sludge component includes sludge concentration tank and filter press, sludge concentration tank is collected in the wastewater treatment component
Sludge, and return line is equipped between sludge concentration tank, filter press and the second intermediate pool, so the supernatant of sludge concentration tank
Liquid, the moisture in filter press can be back to the beginning step in wastewater treatment stage, and realization is traced back back processing.
Specifically, level-one coagulating basin, two-stage coagulation pond, hydrolysis acidification pool, anaerobic pond, aerobic tank, secondary settling tank and three-level are mixed
The sludge party that solidifying Chi Junyu sludge concentration tank sludge pipeline connection, i.e. these stages generate by the filters pressing of Treatment of Sludge component at
Mud cake discharge.
End filtration process is as the further safeguard before wastewater treatment discharge, including sand coarse aggregate ratio system and carbon filtration system
System, also, discharge pond and be equipped with counter-flushing pipeline and sand coarse aggregate ratio system, carbon filtration system connectivity, meanwhile, end filtration process, discharge
Return line also is provided between pond and the second intermediate pool.
It is further illustrated in conjunction with its treatment mechanism:
The comprehensive wastewater of Nitrogen-and Phosphorus-containing does not judge its TDS and COD, TDS≤9000mg/L after pretreatment,
COD≤10000mg/L enters the second intermediate pool, if TDS >=9000mg/L, COD >=10000mg/L after pretreatment
Into the first intermediate pool.
Liquid passes through evaporator evaporation process in first intermediate pool, and evaporation condensate enters the second intermediate pool, evaporation
The outer processing of crystallized product committee.
Subsequent second intermediate pool to the first conditioning tank, adjusts pH between 2.5-3.0, with laggard by water pump lifting
Enter front end Fenton's reaction pond, is added after Fenton reagent through the organic matter and coloration in Fenton oxidation decomposing wasting liquid.
After after the second conditioning tank adjusts pH to 8-8.5, into level-one coagulative precipitation tank, after PAC, PAM is added, precipitating
Sludge enters sludge concentration tank, and supernatant enters two-stage coagulation sedimentation basin, and after PAC, PAM is added, it is dense that precipitating sludge enters sludge
Contracting pond, supernatant enter third intermediate pool, and third intermediate pool is equipped with acid/base chemicals dosing plant, adjust pH and are used as into biochemical
The front-end processing of reaction treatment process.
It is worth noting that, heating device is set in third intermediate pool with guarantee aftertreatment systems coolant-temperature gage 35 ±
2 degree or so, biochemical treatment section uses hydrolysis acidification pool+anaerobic pond+aerobic tank.
Hydrolysis acidification pond water temperature is at 35 ± 2 degree or so, and to guarantee effectively hydrolyzing acidification reactor, temperature is lower in winter
In the case where can also be run with good state.
Hydrolysis acidification technique has been widely used in organic industry liquid waste processing and effect is very good, in order to guarantee hydrolysis acid
Change pond treatment effeciency, spy controls waste liquid temperature before waste liquid is entered hydrolysis acidification.
Anaerobic waste water biological treatment refers under conditions of free-dioxygen through anaerobe (including facultative microbe)
Effect, by waste water it is various complexity organic matter decomposition and inversions at the substances such as methane and carbon dioxide process.
During anaerobic bio-treated, complicated organic compound is decomposed, and is converted into simple, stable chemical combination
Object releases energy simultaneously.
Wherein, most energy occurs in the form of methane, this is a kind of fuel gas, recoverable.
Only a small amount of organic matter is converted and synthesizes new part of the cell simultaneously, therefore for opposite aerobic method, anaerobism
Method sludge growth rate is much smaller.
Aerobic biological treatment be using aerobic microbiological (including aerobic-anaerobic microbe) under the conditions of having existing for oxygen into
Row biological metabolism stablizes it, innoxious processing method with degradation of organic substances.
Microorganism is that substrate carries out aerobic metabolism using organic pollutant present in water, by a series of biochemical anti-
It answers, releases energy step by step, finally settled out with the inorganic matter of low energy position, reach innoxious requirement, so as to return to the nature ring
Border is further processed.
Subsequent aerobic tank water outlet enters secondary settling tank, and sedimentation in secondary sedimentation tank sludge enters sludge concentration tank, second pond supernatant into
Enter third conditioning tank and adjust pH between 2.5-3.0, then passes through Fenton oxygen after Fenton reagent is added in rear end Fenton's reaction pond
Change the organic matter and coloration in decomposing wasting liquid, later again after the 4th conditioning tank adjusts pH to 8-8.5, into three-level coagulating sedimentation
PAC, PAM are added in pond, further waste water is handled, guarantees that it meets discharge mark.
Precipitating sludge enters sludge concentration tank, and supernatant enters the 4th intermediate pool.
Waste liquid in 4th intermediate pool can pass through end filtration process before discharge, as last one before its discharge
It ensures, specifically, Sand Filtration System removes various suspended matters, microorganism and other subparticles in water removal using filter medium, most
Achieve the purpose that reduction water turbidity, purify water effect eventually.
Carbon filters the surface concentration that system forms a layer equilibration with activated carbon granule surface, then organic substance impurity absorption is arrived
In active carbon particle, SS and organic matter tiny in waste liquid are removed.
Carbon filtration system water outlet enter discharge pond, discharge water quality of pond detect it is up to standard, then be discharged into waste water pipe network entrance
Subsequent municipal sewage plant is discharged into environment after continuing, if discharge pond is detected not up to standard, is then discharged into the second intermediate water
Pond continues with rear discharge up to standard.
Above embodiment is only to illustrate the technical ideas and features of the present invention, and its object is to allow be familiar with this skill
The people of art can understand the content of the utility model and implement accordingly, not limit the protection scope of the present invention.
It is all according to the spirit of the present invention substantially equivalent transformation that is done or modification, should all cover the protection scope of the utility model it
It is interior.
Claims (8)
1. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system, it is characterised in that: including wastewater treatment component and Treatment of Sludge
Component, the wastewater treatment component include that the first intermediate pool for successively passing through of waste water, the second intermediate pool, front end Fenton are anti-
It answers, biochemical reaction treatment process, rear end Fenton's reaction, end filtration process and discharge pond, first intermediate pool and the
Evaporator is equipped between two intermediate pools, it is mixed equipped with level-one between the front end Fenton's reaction and the biochemical reaction treatment process
Solidifying pond, two-stage coagulation pond and third intermediate pool, are equipped between the biochemical reaction treatment process and the rear end Fenton's reaction
Secondary settling tank is successively arranged three-level coagulating sedimentation and the 4th intermediate water between the rear end Fenton's reaction and the end filtration process
Pond；
The Treatment of Sludge component includes sludge concentration tank and filter press, and the sludge concentration tank collects the wastewater treatment component
In sludge, and between the sludge concentration tank, the filter press and second intermediate pool be equipped with return line；
Return line also is provided between the end filtration process, the discharge pond and second intermediate pool.
2. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 1, it is characterised in that: the front end is fragrant
Reaction of pausing includes the first conditioning tank, front end Fenton's reaction pond and the second conditioning tank set gradually, the rear end Fenton's reaction packet
Include the third conditioning tank set gradually, rear end Fenton's reaction pond and the 4th conditioning tank.
3. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 2, it is characterised in that: described first adjusts
It saves pond and the third conditioning tank is acid conditioning tank, second conditioning tank and the 4th conditioning tank are alkaline conditioning tank.
4. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 1, it is characterised in that: described biochemical anti-
Answering treatment process includes the hydrolysis acidification pool, anaerobic pond and aerobic tank successively carried out.
5. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 4, it is characterised in that: the level-one is mixed
Solidifying pond, the two-stage coagulation pond, the hydrolysis acidification pool, the anaerobic pond, the aerobic tank, the secondary settling tank and the three-level
Coagulating basin with the sludge concentration tank sludge pipeline connection.
6. a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 1, it is characterised in that: the end mistake
Filter process includes sand coarse aggregate ratio system and carbon filtration system, and the discharge pond is equipped with counter-flushing pipeline and the sand coarse aggregate ratio system, the charcoal
Filter system connectivity.
7. any one of -6 a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 1, it is characterised in that: institute
It states in level-one coagulating basin, the two-stage coagulation pond and the three-level coagulating basin and PAC and PAM is added.
8. any one of -6 a kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system according to claim 1, it is characterised in that: institute
Third intermediate pool is stated equipped with acid/base chemicals dosing plant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822023506.0U CN209602309U (en) | 2018-12-04 | 2018-12-04 | A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822023506.0U CN209602309U (en) | 2018-12-04 | 2018-12-04 | A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209602309U true CN209602309U (en) | 2019-11-08 |
Family
ID=68395269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822023506.0U Expired - Fee Related CN209602309U (en) | 2018-12-04 | 2018-12-04 | A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209602309U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115367952A (en) * | 2022-07-19 | 2022-11-22 | 江苏绿境生态环境科技股份有限公司 | High-salinity sewage accident sewage and low-salinity high-concentration sewage comprehensive treatment system and method |
-
2018
- 2018-12-04 CN CN201822023506.0U patent/CN209602309U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115367952A (en) * | 2022-07-19 | 2022-11-22 | 江苏绿境生态环境科技股份有限公司 | High-salinity sewage accident sewage and low-salinity high-concentration sewage comprehensive treatment system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105585220B (en) | A kind of urban sewage treatment system and purification method | |
| JP5658306B2 (en) | Advanced treatment method and apparatus for sewage that does not discharge sludge | |
| CN102107988B (en) | Phenol-amine wastewater treatment and recycling method and device | |
| CN101353196A (en) | Fur nitro dyeing wastewater treatment and cyclic utilization method | |
| CN102107958A (en) | Method for performing advanced treatment and reuse on oil-refining sewage and matched device | |
| CN106277655A (en) | Method for treating garbage percolation liquid and system | |
| CN208684701U (en) | A kind of indegradable industrial effluent biochemical treatment system | |
| CN205740644U (en) | A kind of garbage burning factory percolate qualified discharge processing system | |
| CN208869459U (en) | A kind of processing system of landfill leachate | |
| CN207726919U (en) | A kind of Multistage Membranes composite processing system of landfill leachate | |
| CN107324511A (en) | A kind of cooling recirculation system by the use of ammoniacal liquor as moisturizing | |
| CN209602309U (en) | A kind of not Nitrogen-and Phosphorus-containing comprehensive wastewater back-end processing system | |
| CN207512019U (en) | A kind of sanitary sewage, technique waste water, stripper Wastewater Concentrated device | |
| CN211712893U (en) | Difficult degradation industrial waste water treatment system | |
| CN105621805A (en) | Refuse incineration plant leachate up-to-standard discharge treatment system and method | |
| CN104787960A (en) | Treatment technology and treatment system of leather waste water | |
| CN205035215U (en) | Landfill leachate treatment device | |
| CN208250110U (en) | A kind of plastic industry waste water processing station | |
| CN116495930A (en) | Application of STRO membrane system in coal wastewater | |
| CN107010796A (en) | A kind of system by the use of remained ammonia as cooling circular water replenishing | |
| CN211999015U (en) | Improved UCT coupling biological rotating disc sewage treatment system for black and odorous water body | |
| CN109607945B (en) | Method for improving biochemical efficiency of wastewater in photovoltaic and electronic industries | |
| CN208218511U (en) | The processing unit of high-concentration sewage | |
| CN209685508U (en) | A kind of nitrogenous phosphorus waste liquid back-end processing system | |
| CN101070218A (en) | Neutralization-free furfural wastewater biochemical treatment process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191108 Termination date: 20211204 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |