CN108689535A - A kind of emulsifying liquid waste water integrated treatment unit - Google Patents
A kind of emulsifying liquid waste water integrated treatment unit Download PDFInfo
- Publication number
- CN108689535A CN108689535A CN201810783512.8A CN201810783512A CN108689535A CN 108689535 A CN108689535 A CN 108689535A CN 201810783512 A CN201810783512 A CN 201810783512A CN 108689535 A CN108689535 A CN 108689535A
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- CN
- China
- Prior art keywords
- waste water
- liquid waste
- emulsifying liquid
- treatment unit
- integrated treatment
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 47
- 230000001804 emulsifying effect Effects 0.000 title claims abstract description 27
- 239000010808 liquid waste Substances 0.000 title claims abstract description 27
- 238000004062 sedimentation Methods 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 230000003647 oxidation Effects 0.000 claims abstract description 23
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 23
- 238000005273 aeration Methods 0.000 claims abstract description 21
- 239000002351 wastewater Substances 0.000 claims abstract description 21
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000003197 catalytic effect Effects 0.000 claims abstract description 12
- 239000004408 titanium dioxide Substances 0.000 claims abstract description 9
- 238000012856 packing Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 8
- 239000000919 ceramic Substances 0.000 claims description 7
- 239000003814 drug Substances 0.000 claims description 6
- 239000000701 coagulant Substances 0.000 claims description 5
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 238000004381 surface treatment Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims 1
- 239000005416 organic matter Substances 0.000 abstract description 5
- 238000005286 illumination Methods 0.000 abstract 1
- 230000001699 photocatalysis Effects 0.000 abstract 1
- 238000007146 photocatalysis Methods 0.000 abstract 1
- 230000005855 radiation Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 9
- 239000000839 emulsion Substances 0.000 description 9
- 239000010865 sewage Substances 0.000 description 9
- 239000003921 oil Substances 0.000 description 8
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 239000002173 cutting fluid Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
-
- 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
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- 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
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- 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
-
- 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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/32—Details relating to UV-irradiation devices
- C02F2201/322—Lamp arrangement
- C02F2201/3227—Units with two or more lamps
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/32—Details relating to UV-irradiation devices
- C02F2201/322—Lamp arrangement
- C02F2201/3228—Units having reflectors, e.g. coatings, baffles, plates, mirrors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/78—Details relating to ozone treatment devices
- C02F2201/784—Diffusers or nozzles for ozonation
-
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
-
- 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
- C02F2305/10—Photocatalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a kind of emulsifying liquid waste water integrated treatment units,Demulsification pond including being sequentially connected in series setting,Primary sedimentation basin,Reaction tank,Aeration tank,Secondary sedimentation tank,Advanced oxidation pond and clear water reserviors,Emulsifying liquid waste water passes through preliminary treatment twice first,The organic matter being easily processed in waste water is removed,Remaining waste water enters advanced oxidation pond and carries out advanced treating,Advanced oxidation pond includes shell of reactor,Aeration zone in shell of reactor is set from bottom to top,Packing area and reaction zone,Area of aeration system lower part includes water inlet and air inlet,Water outlet is arranged in reaction zone top,Titanium Dioxide plate is longitudinally disposed to be divided into multiple zoneofoxidations by reaction zone,Ultraviolet lamppost is vertically arranged in each oxidation district center respectively,Catalytic plate is completely in the radiation length of ultraviolet light,Reflective guide shell can reflect ultraviolet light,Reinforce illumination,Improve photocatalysis efficiency.
Description
Technical field
The present invention relates to technical field of waste water processing, more particularly to emulsifying liquid waste water integrated treatment unit.
Background technology
Emulsion is a kind of suspension got along swimmingly with each other, and is formulated by oil, water and various chemical addition agents.Emulsion
It is widely present among the production and life of all trades and professions.Food, oil such as Shi Lian, make steel, butcher, machining at all conglomeraties
It is directed to emulsion, emulsion is chiefly used in cooling, lubrication or transmits pressure etc., with certain lubricity, cooling, clear
Washing property and rust-preventing characteristic are most popular a kind of cutting fluids in current production.But its service life is short, uses a period of time
Afterwards because various factors cannot be continuing with, waste liquid is more.Emulsifying liquid waste water belongs to pollution sources important in industrial pollution source, directly
It connects emulsifying liquid waste water discharge is more serious to water pollution.
Therefore, it is necessary to be discharged again after emulsifying liquid waste water is handled.The characteristics of emulsifying liquid waste water is:High COD and BOD,
For domestic emulsion COD in 8000ppm or more, the COD's high of import can reach hundreds thousand of ppm, and oil mass also 3000~
5000ppm;High concentrtion, bio-refractory.And especially to machine emulsifying liquid waste water as most among all a variety of emulsifying liquid waste waters
One of difficult, its emulsification degree is high, and B/C values are low, high concentration, high concentrtion, high salinity, especially also containing there are many process
In mixed heavy metal, various chemical reagent etc..The process problem of emulsion waste liquid is always to annoying our problem.
The source of emulsifying liquid waste water is differed, and species concentrations, characteristic are also different, is given up at present to the oil emulsion that machinery industry generates
The processing of water is separated oil slick with hydrometer method using two-step method from emulsifying waste water or waste liquid, is then used again first
Chemistry, electricity or other physical methods destroy oil emulsion, and oil is made further to be detached with water, then by agglomerating electrofloatation, sand
Filter, activated carbon adsorption;If alkaline emulsion waste water, neutralization pretreatment is also carried out, wastewater purification can be just made.Such place
Reason method, equipment investment is more, and cumbersome, sewage disposal is not thorough.
Invention content
The technical problem to be solved in the present invention is to provide it is a kind of it is easy to operate, expense is low, high treating effect, effluent quality are steady
Fixed reliable emulsifying liquid waste water integrated treatment unit.
In order to solve the above technical problem, the present invention provides a kind of emulsifying liquid waste water integrated treatment units, including according to
The secondary demulsification pond being arranged in series, primary sedimentation basin, reaction tank, aeration tank, secondary sedimentation tank, advanced oxidation pond and clear water reserviors, breast
Change liquid waste water first by preliminary treatment twice, the organic matter being easily processed in waste water is removed, remaining waste water enters advanced
Oxidation pond carries out advanced treating, and the advanced oxidation pond includes shell of reactor, is arranged in shell of reactor from bottom to top
Aeration zone, packing area and reaction zone, it includes water inlet and air inlet that the aeration, which is area lower part, and the reaction zone top is provided
The mouth of a river, Titanium Dioxide plate is longitudinally disposed to be divided into multiple zoneofoxidations by the reaction zone, and ultraviolet lamppost is vertically arranged respectively
In each oxidation district center, the relative distance of ultraviolet lamppost and catalytic plate is more uniform at this time, and catalytic plate is completely in purple
In the best catalysis distance of outer lamppost, excellent catalytic effect, while the inner surface of the shell of reactor is mirror surface treatment, ultraviolet lamp
The light that column is sent out is specularly reflected, and greatly strengthens the light intensity of ultraviolet light, is conducive to the degradation effect for improving organic pollution.
Further, it adds component automatically by medicament and adds demulsifier and coagulant respectively into the demulsification pond, and
Waste water after addition medicament is stirred, the pollutants such as oils and the COD in waste water are handled.
Further, in whipping process, mixing speed is 40-60 revs/min, ensures the mobility of oily substance.
Further, the shell of reactor is tube structure, facilitates manufacture and ensures to obtain using identical material
Maximum volume.
Further, the catalytic plate right-angled intersection is arranged averagely is divided into 4 zoneofoxidations by the reaction zone, conveniently sets
It sets so that so that catalytic plate is respectively positioned in the best irradiation catalysis distance of ultraviolet lamppost, and each zoneofoxidation is sent out in addition to ultraviolet lamppost
The ultraviolet light of mirror-reflection, oxidation reinforced effect can be obtained outside the ultraviolet light gone out.
Further, the hollow ceramic ball that surface is coated with titanium dioxide-coated layer is provided in the packing area,
Hollow ceramic ball large specific surface area, sewage and ozone contact fully, tentatively with the titanium dioxide oxidizer of hollow ceramic ball surface
High treating effect.
Further, the primary sedimentation basin and secondary sedimentation tank are inclined-plate clarifying basin, and inclined-plate clarifying basin is with " shallow-layer is heavy
Form sediment " principle, shortens particle settling height, asks, and increase the desilting area of sedimentation basin, improve when so as to shorten precipitation
Treatment effeciency.
Further, sludge discharging machine is connected below the primary sedimentation basin and secondary sedimentation tank, ensures the lasting work of sedimentation basin
Make ability.
Further, it is provided with nano grade titanium alloy aeration plate in the aeration tank, makes to enter the ozone bubbles in sewage
It is finer and closely woven, it is more preferable with merging for sewage, improve oxidation effectiveness.
A kind of emulsifying liquid waste water integrated treatment unit of the present invention, advantageous effect compared with prior art are:Operation
Simply, expense is low, reliable by multistep treatment high treating effect, stable effluent quality.
Description of the drawings
Fig. 1 is overall structure of the present invention;
Fig. 2 is advanced oxidation pond of the present invention vertical view.
Specific implementation mode
The invention will be further described in the following with reference to the drawings and specific embodiments, so that those skilled in the art can be with
It more fully understands the present invention and can be practiced, but illustrated embodiment is not as a limitation of the invention.
As depicted in figs. 1 and 2, a kind of emulsifying liquid waste water integrated treatment unit of the invention, including it is sequentially connected in series setting
Demulsification pond 3, primary sedimentation basin 4, reaction tank 5, aeration tank 6, secondary sedimentation tank 7, advanced oxidation pond 1 and clear water reserviors 8, it is described broken
Mixing component 31 is equipped in newborn pond 3 and reaction tank 5, for mixing component 31 in whipping process, mixing speed is 40-60 revs/min,
Emulsifying liquid waste water enter demulsification pond 3 after, added automatically by medicament component 32 added respectively into the demulsification pond 3 demulsifier with
Coagulant, and the waste water after addition medicament is stirred, in the embodiment of the present invention, demulsifier and coagulant use inorganic matter,
Purpose is to make not generate new organic matter in waste water again, even if the COD value of waste water will not be due to being added demulsifier and coagulant
Increase, the waste water after coagulation enters primary sedimentation basin 4 and precipitated in primary sedimentation basin 4, and the partial organic substances in water are sunk
Shallow lake is got off, and the waste water after preliminary treatment is again introduced into reaction tank 5, PH adjustings is carried out in reaction tank 5, and then enter aeration tank 6,
The contact for reinforcing useless Organic substance in water and microorganism and dissolved ozone carries out oxygenolysis to useless Organic substance in water, and secondary
It is precipitated again in sedimentation basin 7, the sludge discharging machine 41 that primary sedimentation basin 4 is connected with the sediment in secondary sedimentation tank 7 through lower section
Discharge ensures that the continue working ability of sedimentation basin, the primary sedimentation basin 4 and secondary sedimentation tank 7 are inclined-plate clarifying basin, and inclined plate is heavy
Shallow lake pond uses " shallow layer precipitating " principle, shortens particle settling height, is asked when so as to shorten precipitation, and increase sedimentation basin
Desilting area improves treatment effeciency, and nano grade titanium alloy aeration plate 61 is provided in the aeration tank 6, makes to enter in sewage
Ozone bubbles it is finer and closely woven, it is more preferable with merging for sewage, improve oxidation effectiveness, by preliminary treatment twice, place be easy in waste water
The organic matter of reason is discharged, and remaining waste water enters advanced oxidation pond 1, and reluctant organic matter is in advanced oxidation pond 1 in waste water
Middle to be aoxidized, treated, and waste water is ultimately discharged into clear water reserviors 8 behind advanced oxidation pond 1.
The advanced oxidation pond 1 includes shell of reactor 11, the aeration zone being arranged from bottom to top in shell of reactor 11
12, packing area 13 and reaction zone 14, the aeration zone lower part include water inlet 15 and air inlet 16, and 14 top of the reaction zone is set
Water outlet 19 is set, water inlet 15 and air inlet 16 enter aeration to the waste water and ozone flowed out from secondary sedimentation tank 7 from below respectively
Area 12, and enter packing area 13 from aeration zone 12, it is hollow coated with titanium dioxide-coated layer that surface is provided in packing area 13
Ceramic Balls 2 carry out preliminary oxidation processing, 2 large specific surface area of hollow ceramic ball, sewage and ozone and hollow ceramic ball 2 to sewage
The titanium dioxide oxidizer contact on surface is abundant, effectively improves reaction efficiency, Titanium Dioxide plate 18 is longitudinally disposed will be described
Reaction zone 14 is divided into multiple zoneofoxidations 141, and ultraviolet lamppost 17 is vertically arranged in each 141 center of the zoneofoxidation respectively, because
This ultraviolet lamppost 17 and the relative distance of catalytic plate 18 are more uniform, and catalytic plate 18 is completely in the best catalysis of ultraviolet lamppost 17
In distance, achieve the effect that sufficiently catalytic oxidation and efficient, while the inner surface of the shell of reactor 11 is mirror surface treatment,
The light that ultraviolet lamppost 17 is sent out is specularly reflected, and greatly strengthens the light intensity of ultraviolet light, is conducive to the drop for improving organic pollution
Effect is solved, water outlet 19 of the sewage of completion above reaction zone 14 is handled and is discharged into clear water reserviors 8, manufacture for convenience and ensures to adopt
Maximum volume can be obtained with identical material, the shell of reactor 11 is tube structure, 18 right-angled intersection of the catalytic plate
It is arranged and the reaction zone 14 is averagely divided into 4 zoneofoxidations 141 so that catalytic plate 18 is made to be respectively positioned on the best of ultraviolet lamppost 17
In catalysis distance, and each zoneofoxidation 141 can obtain the ultraviolet of mirror-reflection other than the ultraviolet light that ultraviolet lamppost 17 is sent out
Light, oxidation reinforced effect.
Embodiment described above is only to absolutely prove preferred embodiment that is of the invention and being lifted, protection model of the invention
It encloses without being limited thereto.Those skilled in the art on the basis of the present invention made by equivalent substitute or transformation, in the present invention
Protection domain within.Protection scope of the present invention is subject to claims.
Claims (9)
1. a kind of emulsifying liquid waste water integrated treatment unit, which is characterized in that including being sequentially connected in series the demulsification pond of setting, once sinking
Shallow lake pond, reaction tank, aeration tank, secondary sedimentation tank, advanced oxidation pond and clear water reserviors, the advanced oxidation pond includes outside reactor
Shell, the aeration zone being arranged from bottom to top in shell of reactor, packing area and reaction zone, the aeration are that area lower part includes water inlet
Water outlet is arranged in mouth and air inlet, the reaction zone top, and Titanium Dioxide plate is longitudinally disposed to be divided into the reaction zone
Multiple zoneofoxidations, ultraviolet lamppost are vertically arranged in each oxidation district center respectively, and the shell of reactor inner surface is mirror
Surface treatment.
2. a kind of emulsifying liquid waste water integrated treatment unit as described in claim 1, which is characterized in that the demulsification pond passes through
Medicament adds component and adds demulsifier and coagulant respectively into pond automatically, and is stirred to the waste water after addition medicament.
3. a kind of emulsifying liquid waste water integrated treatment unit as claimed in claim 2, which is characterized in that in whipping process, stir
It is 40-60 revs/min to mix speed.
4. a kind of emulsifying liquid waste water integrated treatment unit as described in claim 1, which is characterized in that the shell of reactor
For tube structure.
5. a kind of emulsifying liquid waste water integrated treatment unit as claimed in claim 4, which is characterized in that the catalytic plate cross
It is arranged in a crossed manner that the reaction zone is averagely divided into 4 zoneofoxidations.
6. a kind of emulsifying liquid waste water integrated treatment unit as described in claim 1, which is characterized in that the packing area
Inside it is provided with the hollow ceramic ball that surface is coated with titanium dioxide-coated layer.
7. a kind of emulsifying liquid waste water integrated treatment unit as described in claim 1, which is characterized in that the primary sedimentation basin
It is inclined-plate clarifying basin with secondary sedimentation tank.
8. a kind of emulsifying liquid waste water integrated treatment unit as claimed in claim 7, which is characterized in that the primary sedimentation basin
With connection sludge discharging machine below secondary sedimentation tank.
9. a kind of emulsifying liquid waste water integrated treatment unit as described in claim 1, which is characterized in that set in the aeration tank
It is equipped with nano grade titanium alloy aeration plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810783512.8A CN108689535A (en) | 2018-07-17 | 2018-07-17 | A kind of emulsifying liquid waste water integrated treatment unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810783512.8A CN108689535A (en) | 2018-07-17 | 2018-07-17 | A kind of emulsifying liquid waste water integrated treatment unit |
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| CN108689535A true CN108689535A (en) | 2018-10-23 |
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| CN201810783512.8A Pending CN108689535A (en) | 2018-07-17 | 2018-07-17 | A kind of emulsifying liquid waste water integrated treatment unit |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109704524A (en) * | 2019-03-05 | 2019-05-03 | 苏州方舟环保科技有限公司 | A kind of micro-nano bubble emulsification liquid processing device |
| CN110372152A (en) * | 2019-07-29 | 2019-10-25 | 北京环球中科水务科技有限公司 | A kind of intellectual modularization Novel sewage integration apparatus |
| CN112960838A (en) * | 2021-04-06 | 2021-06-15 | 江苏科技大学 | Reduction treatment system and treatment method for machining emulsified waste liquid |
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