CN108585381A - A kind of brush waste water treatment system processed - Google Patents
A kind of brush waste water treatment system processed Download PDFInfo
- Publication number
- CN108585381A CN108585381A CN201810578029.6A CN201810578029A CN108585381A CN 108585381 A CN108585381 A CN 108585381A CN 201810578029 A CN201810578029 A CN 201810578029A CN 108585381 A CN108585381 A CN 108585381A
- Authority
- CN
- China
- Prior art keywords
- waste water
- sludge
- pond
- treatment system
- air
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/70—Treatment of water, waste water, or sewage by reduction
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/722—Oxidation by peroxides
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/026—Fenton's reagent
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The present invention relates to a kind of brush waste water treatment systems processed, pH value and the flocculation of waste water are produced by adjusting, remove the most suspended substances in waste water, then MBR film methods are added using AO techniques, and by the operation change to AO techniques water intake mode and aeration mode, realize aerobic nitrification and anaerobic denitrifying denitrogenation；The present invention can effectively remove a large amount of suspended matters in waste water, and simultaneously for harmful substance in waste water such as benzene class, phenols and oils, colorant etc. can effectively be degraded, and reduce the security risk of waste water, while protecting environment.
Description
Technical field
The present invention relates to waste water treatment system more particularly to a kind of brush waste water treatment systems processed.
Background technology
With the improvement of people's living condition, requirement of the common people for environment is also higher and higher, how preferably to handle life
Living, industrial wastewater is also just at the most important thing.
Displacement water, wire drawing flushing water, centrifuge waste water and the ground cleaning waste water of the fermentation vat generated in existing production, wherein
Containing a large amount of benzene class, phenols and oils, colorant and suspended matter etc. belong to used water difficult to degradate, have seriously threatened our life
Dis environment.
Invention content
To solve the above-mentioned problems, the present invention provides a kind of brush waste water treatment systems processed.
Embodiment：
A kind of brush waste water treatment system processed, it is characterised in that：Including regulating reservoir, air-floating apparatus, acidification pool, Fenton tower, reaction tank,
Sedimentation basin, reduction pond, biochemical treatment integration apparatus, active carbon filter, clear water reserviors, sludge-tank and sludge drying pond, it is described
Regulating reservoir is internally provided with elevator pump, and the air-floating apparatus includes air floatation machine, dissolving and Slag Scraping Device, is prevented in the Fenton tower
There is oxidant, be placed with reducing agent in the reduction pond and be provided with self priming pump, the biochemical treatment integration apparatus includes
AO process equipments and MBR membrane cisternas are provided with self priming pump in the MBR membrane cisternas, and sludge pump is provided in the sludge-tank, and production is useless
Water is set by regulating reservoir, air-floating apparatus, acidification pool, Fenton tower, reaction tank, sedimentation basin, reduction pond, biochemical treatment integration successively
Standby, active carbon filter, clear water reserviors are finally discharged from total floss hole.
Further, the oxidant in the Fenton tower is Fenton reagent.
Further, the reducing agent in the reduction pond is sodium sulfite.
Advantageous effect：The present invention can effectively remove a large amount of suspended matters in waste water, such as simultaneously for harmful substance in waste water
Benzene class, phenols and oils, colorant etc. can effectively be degraded, and the security risk of waste water is reduced, while protect environment.
Description of the drawings
Fig. 1 is the process route chart of the present invention.
Specific implementation mode
The specific implementation mode of the present invention is described in detail below in conjunction with the accompanying drawings.
It is flowed into regulating reservoir as shown in Figure 1, the production waste water in processing plastic wire-drawing each stage flows automatically under gravity,
Sulfuric acid is added in regulating reservoir, the preliminary pH for adjusting waste water promotes the alkaline waste water regulated to 7-10, then by elevator pump
To air floatation machine, and flocculant poly aluminium chloride is added in air floatation machine（PAC）And polyacrylamide（PAM）, aluminium polychloride
（PAC）Molecule and polyacrylamide（PAM）Molecule, which builds bridge the suspended particles being suspended in waste water to adsorb, forms flocculate, then
Using pressure air-dissolving method, i.e., pending waste water is first pressurized to 3-4kg/cm2 with water pump, is then fed into the dissolving of special arrangement
In, so that air is substantially soluble in water in tank, then dissolving is put into air floatation machine, subtracts suddenly through release in air floatation machine
To normal pressure, the supersaturated air being at this moment dissolved in the water is escaped in the form of micro air bubble from pond, by suspended particle in water or
Elaioleucite takes the water surface to and forms dross, scrapes the dross of formation with Slag Scraping Device be discharged into sludge-tank later.Supernatant after air supporting
Gravity flow inflow acidification pool under the effect of gravity, in acidification pool plus sulfuric acid adjusts clear liquid to acidity, and then acid clear liquid gravity flow is flowed
Enter Fenton tower, in Fenton tower using Fenton reagent to acid clear liquid carry out advanced oxidation, remove waste water in 50% or more it is organic
Object, the waste water after peroxidating flow into reaction tank from Fenton tower, in reaction tank plus after the PH to neutrality of alkali neutralization waste water again
Flocculant poly aluminium chloride is added（PAC）Molecule and polyacrylamide（PAM）, the waste water inflow after abundant adsorption-flocculation
Sedimentation basin, in sedimentation basin after precipitation after a period of time, clear liquid floats, and flocculate sinks, work of the supernatant in gravity
After flowing into reduction pond with lower gravity flow, the flocculate residue in sedimentation basin is discharged into sludge-tank, then adds Asia in restoring pond
Then obtained waste water is pumped into biochemistry by sodium sulphate to remove remaining oxidant in waste water as reducing agent with self priming pump
Integration apparatus is handled, adds MBR film methods to handle waste water using AO techniques in a device, waste water is with certain speed stream first
Through biologic packing material, biomembrane is covered on filler, under the collective effect of biomembrane and activated sludge, by AO techniques into
The operation change of water mode and aeration mode is realized aerobic nitrification and anaerobic denitrifying denitrogenation, dephosphorization and is further removed
Organic matter in waste water, the water outlet being purified at this time is pumped into active carbon filter by self priming pump, and is inhaled by activated carbon
It is discharged into the total floss hole of plant area after flowing into clear water reserviors after attached effect progress advanced treating, later to MBR membrane cisternas, activated carbon filtering
Device, clear water reserviors are backwashed, and remove the impurity being trapped in filter material layer, filter tank is made to restore filter capacity in a short time.
Sludge gravity flow in air floatation machine and sedimentation basin flows into sludge-tank, and MBR membrane cisterna excess sludges are pumped into dirt by self priming pump
Mud sump, the sludge settled in sludge-tank are pumped into sludge drying pond by sludge pump and carry out nature desiccation, and residual moisture leads to respectively
It crosses natural evaporation bottom of pond naturally osmotic pipe to be back to sludge-tank overflow is to regulating reservoir again, after moisture content reduces, sludge obtains desiccation
Outward transport.
The basic principles, main features and advantages of the present invention have been shown and described above.The present invention is not by upper
The limitation of embodiment is stated, the above embodiments and description only illustrate the principle of the present invention, is not departing from the present invention
Various changes and improvements may be made to the invention under the premise of spirit and scope, these changes and improvements both fall within claimed sheet
In the range of invention.The claimed scope of the invention is defined by appended claims and its equivalent.
Claims (3)
1. a kind of brush waste water treatment system processed, it is characterised in that：Including regulating reservoir, air-floating apparatus, acidification pool, Fenton tower, reaction
Pond, sedimentation basin, reduction pond, biochemical treatment integration apparatus, active carbon filter, clear water reserviors, sludge-tank and sludge drying pond, institute
It states regulating reservoir and is internally provided with elevator pump, the air-floating apparatus includes air floatation machine, dissolving and Slag Scraping Device, is prevented in the Fenton tower
Only there is oxidant, is placed with reducing agent in the reduction pond and is provided with self priming pump, the biochemical treatment integration apparatus packet
AO process equipments and MBR membrane cisternas are included, self priming pump is provided in the MBR membrane cisternas, sludge pump is provided in the sludge-tank, is produced
Waste water passes through regulating reservoir, air-floating apparatus, acidification pool, Fenton tower, reaction tank, sedimentation basin, reduction pond, biochemical treatment integration successively
Equipment, active carbon filter, clear water reserviors are finally discharged from total floss hole.
2. a kind of brush waste water treatment system processed according to claim 1, it is characterised in that：Oxidant in the Fenton tower
For Fenton reagent.
3. a kind of brush waste water treatment system processed according to claim 1, it is characterised in that：Reducing agent in the reduction pond
For sodium sulfite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810578029.6A CN108585381A (en) | 2018-06-07 | 2018-06-07 | A kind of brush waste water treatment system processed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810578029.6A CN108585381A (en) | 2018-06-07 | 2018-06-07 | A kind of brush waste water treatment system processed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108585381A true CN108585381A (en) | 2018-09-28 |
Family
ID=63627536
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810578029.6A Pending CN108585381A (en) | 2018-06-07 | 2018-06-07 | A kind of brush waste water treatment system processed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108585381A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104845A (en) * | 2019-06-11 | 2019-08-09 | 武汉深能环保新沟垃圾发电有限公司 | A kind of percolation liquid membrane processing method reducing concentration output of fluid |
| CN114075012A (en) * | 2020-08-12 | 2022-02-22 | 大连大禹水处理技术有限公司 | Plastic regeneration cleaning wastewater treatment method and system |
-
2018
- 2018-06-07 CN CN201810578029.6A patent/CN108585381A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104845A (en) * | 2019-06-11 | 2019-08-09 | 武汉深能环保新沟垃圾发电有限公司 | A kind of percolation liquid membrane processing method reducing concentration output of fluid |
| CN114075012A (en) * | 2020-08-12 | 2022-02-22 | 大连大禹水处理技术有限公司 | Plastic regeneration cleaning wastewater treatment method and system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105948414B (en) | A kind of emulsifying liquid waste water processing system and its treatment process | |
| CN100551846C (en) | Stone oil well drilling sullage continuous processing technique | |
| KR101000742B1 (en) | Improvement of Phosphorus Removal Efficiency by Modification of Rectangular Sedimentation Basin | |
| CN108585380A (en) | A kind of process of brush wastewater treatment processed | |
| CN1962493A (en) | Drainage processing device and drainage processing method | |
| CN101857321A (en) | Method and equipment for treating and recycling reverse osmosis concentrated water and complex wastewater with high salt content | |
| CN108585381A (en) | A kind of brush waste water treatment system processed | |
| CN114940561A (en) | Oil sludge treatment waste liquid treatment system | |
| CN107585972A (en) | Grease processing waste water handling process and device | |
| CN207193070U (en) | A kind of efficient equipment for processing industrial sewage | |
| CN110156275A (en) | A kind of environmentally friendly recirculated water by-pass flow biological treatment system and method | |
| CN110482804A (en) | The method for handling oil removing degreasing waste water | |
| US4330407A (en) | Process for clarifying algae-laden waste water stream | |
| CN206538318U (en) | A kind of device for handling the high organic wastewater of industrial high salt | |
| CN107746154A (en) | One kind printing and dyeing（Containing antimony）Sewage disposal system | |
| CN208732846U (en) | A kind of brush waste water treatment system processed | |
| JP5105608B2 (en) | Waste water treatment system and operation method thereof | |
| CN206359396U (en) | A kind of MBR Treated sewage reusings processing unit | |
| JP3931279B2 (en) | Water purification equipment for suspended solids | |
| CN208814846U (en) | Oil-contained waste water treatment system | |
| CN205258241U (en) | Printing and dyeing wastewater treatment system | |
| CN209456217U (en) | Intermediate water reuse system | |
| CN207391162U (en) | A kind of pneumatically supported underground water treating device containing high-efficiency dissolued-air | |
| JP4549000B2 (en) | Water purification equipment for suspended solids | |
| CN206901987U (en) | A kind of sewage disposal system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180928 |