CN109422412A - A kind of Integrated Processing Unit of coating waste-water and sanitary sewage - Google Patents
A kind of Integrated Processing Unit of coating waste-water and sanitary sewage Download PDFInfo
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- CN109422412A CN109422412A CN201710704177.3A CN201710704177A CN109422412A CN 109422412 A CN109422412 A CN 109422412A CN 201710704177 A CN201710704177 A CN 201710704177A CN 109422412 A CN109422412 A CN 109422412A
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- sewage
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- 239000002351 wastewater Substances 0.000 title claims abstract description 46
- 239000010865 sewage Substances 0.000 title claims abstract description 44
- 238000000576 coating method Methods 0.000 title claims abstract description 34
- 239000011248 coating agent Substances 0.000 title claims abstract description 33
- 238000012545 processing Methods 0.000 title claims description 14
- 239000010802 sludge Substances 0.000 claims abstract description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims abstract description 11
- 238000005188 flotation Methods 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 7
- 238000004062 sedimentation Methods 0.000 claims abstract description 6
- 230000003750 conditioning effect Effects 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 12
- 230000001112 coagulating effect Effects 0.000 claims description 11
- 238000001556 precipitation Methods 0.000 claims description 8
- 238000005273 aeration Methods 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 7
- 238000009298 carbon filtering Methods 0.000 claims description 4
- 230000000593 degrading effect Effects 0.000 claims description 3
- 238000000855 fermentation Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 230000015271 coagulation Effects 0.000 abstract description 2
- 238000005345 coagulation Methods 0.000 abstract description 2
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 239000003973 paint Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 5
- 230000001965 increasing effect Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- -1 treated Substances 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000004065 wastewater treatment 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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/14—Paint wastes
-
- 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
- C02F3/1263—Sequencing batch reactors [SBR]
-
- 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
- C02F3/28—Anaerobic digestion processes
- C02F3/2846—Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Physical Water Treatments (AREA)
Abstract
本发明公开一种涂料废水和生活污水的综合处理装置，包括预处理阶段、生物处理阶段、过滤阶段、污泥处理阶段。预处理阶段包括集水池、混凝沉淀池、气浮池、调节池；生物处理阶段包括UASB、SBR池；过滤阶段为活性炭过滤池；污泥处理阶段包括污泥浓缩池、污泥泵、板框压滤机。采用上述技术方案，本发明所述的涂料废水和生活污水的综合处理装置，将涂料废水经过预处理阶段后，与生活污水一同进入生物处理阶段进行处理，处理后的废水可排放或回用，减少了环境污染，并且有效节约了水资源。
The invention discloses a comprehensive treatment device for paint wastewater and domestic sewage, which includes a pretreatment stage, a biological treatment stage, a filtration stage and a sludge treatment stage. The pretreatment stage includes water collection tank, coagulation sedimentation tank, air flotation tank and adjustment tank; the biological treatment stage includes UASB and SBR tank; the filtration stage is activated carbon filter tank; the sludge treatment stage includes sludge concentration tank, sludge pump, plate and frame filter press. By adopting the above technical scheme, the comprehensive treatment device for coating wastewater and domestic sewage according to the present invention, after the coating wastewater is passed through the pretreatment stage, enters the biological treatment stage together with the domestic sewage for treatment, and the treated wastewater can be discharged or reused, It reduces environmental pollution and effectively saves water resources.
Description
Technical field
The present invention relates to the Integrated Processing Units of a kind of coating waste-water and sanitary sewage, in particular to be using more
The integrated technology of grade pretreatment and biosystem invents the Integrated Processing Unit of a kind of coating waste-water and sanitary sewage.
Background technique
Since the production and use of coating have obtained quick development, a large amount of coating waste-waters are produced thereupon.Coating
Waste water is one of high organic matter, high concentrtion, high-colour intensity wastewater, is mainly derived from the flushing of reaction kettle and material-compound tank, ground
The waste water that cleaning and research and development department generate.Contain a variety of industrial chemicals and the increasings such as resin, organic solvent, auxiliary agent in coating waste-water
Thick dose, the macromolecular organic compounds such as dispersing agent, organic matter severely exceed, and biodegradability is very poor, if direct without processing
Discharge will generate serious pollution to environment.Currently, coating waste-water processing method has physico-chemical process and biochemical method, physico-chemical process mainly has
Coagulating sedimentation, absorption, micro-filtration, ultrafiltration etc., biochemical treatment mainly include anaerobic bio-treated, Aerobic biological process, activated sludge
Method etc..Most widely used at present is materializing strategy, although this method can reduce cost for wastewater treatment, and is applied in short-term
Pollution caused by material enterprise wastewater will not influence too much, but as waste water is continuously increased and the increasing of coating products kind
It is more, waste water quality becomes increasingly complex, organic concentration is high, pollution also can be increasingly severe, cause coating waste-water processing difficult.And
The sanitary sewage feature small because of its water, some coatings enterprises can select direct emission, to cause environmental pollution.
Summary of the invention
It is an object of the invention in place of overcome the deficiencies in the prior art, provide a kind of high treating effect, structurally reasonable
The Integrated Processing Unit of coating waste-water and sanitary sewage.
The present invention solves its technical problem and adopts the following technical solutions to achieve:
A kind of Integrated Processing Unit of coating waste-water and sanitary sewage, including pretreatment stage, biological treatment stage, filtering
Stage, Treatment of Sludge stage.Pretreatment stage includes that the sequentially connected collecting-tank of pipeline, coagulative precipitation tank, air pressure pump, pressure are molten
Gas tank, flotation tank, conditioning tank；Biological treatment stage includes the pond UASB, SBR；Filtration stage is active carbon filtering ponds；Treatment of Sludge
Stage includes sludge concentration tank, sludge pump, plate and frame filter press.Coating waste-water into cross pretreatment stage, i.e., into cross coagulating sedimentation with
And enter conditioning tank after flotation tank, and sanitary sewage enters conditioning tank by intake pump and mixes with coating waste-water, enters together
Biological treatment stage.
The process coating waste-water and sanitary sewage that the biological treatment stage uses UASB to combine with SBR, waste water
Enter Sludge Bed from the bottom UASB, sufficiently reacted with sludge, Organic substance in water matter by anaerobic fermentation generate biogas, sludge, water,
Biogas enters three phase separator, export at the top of biogas autoreactor, the Sludge Bed of sludge automatic sedimentation to reactor bottom, processing
Sewage afterwards is discharged from upper right side, and boosted pump enters SBR, after sewage level reaches setting height in pond, carries out intermittent
Aeration, is sufficiently mixed sewage with sludge, and the organic substance in sewage of further degrading, treated, and sewage enters intermediate water
Pond, sludge are discharged into sludge concentration tank.
The advantages and positive effects of the present invention are:
1. the present invention uses coagulation and the dual preconditioning technique of air bearing, major part SS in waste water is eliminated, raw water is reduced
Turbidity and coloration, while also reducing COD, BOD, TN and TP, greatly reduce the load of subsequent biosystem.
2. process coating waste-water and sanitary sewage that the present invention uses UASB to combine with SBR, degradable major part
Organic matter improves the biodegradability of waste water；SBR process operation mode is flexible, and become reconciled feeding process of anaerobism alternately occurs, sludge age is short,
It is active high, substantially increase the removal efficiency of TN and TP in waste water.
3. the present invention uses active carbon filter plant, it is further processed, goes remaining in water removal to relatively clear
The substances such as particle, bacterium, microorganism make to be discharged qualified discharge or reuse.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of a kind of coating waste-water and sewage treatment unit of the invention
Specific embodiment
The invention will be further described with reference to the accompanying drawing and by specific embodiment, and following embodiment is descriptive
, it is not restrictive, this does not limit the scope of protection of the present invention.
As shown in Figure 1, a kind of coating waste-water and sanitary sewage Integrated Processing Unit, including by pipeline it is sequentially connected into
Water pump 1 (11), collecting-tank 3, coagulative precipitation tank 4, air pressure pump 5, pressure volume pot 6, flotation tank 10, conditioning tank 12, UASB15,
SBR18, micro porous aeration head 19, compressed air 20, intermediate pool 21, active carbon filtering ponds 22, sludge concentration tank 23 (26), sheet frame
Filter press 25 (28).Coating waste-water enters collecting-tank 3 under the action of intake pump 1, then precipitates through coagulative precipitation tank 4 laggard
Enter flotation tank 10, removes a large amount of solid suspension and colloidal substance；Enter conditioning tank 12 later, sanitary sewage is through intake pump 11
Into conditioning tank, mixed with by pretreated coating waste-water；The water outlet of conditioning tank 12 enters the progress anaerobism of the pond UASB 15 and disappears
Change, the organic matter in sewage of degrading；UASB15 water outlet enters SBR18, and the bottom SBR18 is equipped with micro porous aeration head 19, provides oxygen
It is sufficiently mixed waste water with sludge, degradation of organic substances, water outlet enters intermediate pool；Intermediate pool water outlet enters active carbon filtering ponds
22, it further purifies, produces water qualified discharge or reuse.
The precipitating generated after 4 dosing of the coagulative precipitation tank flocculation is discharged into sludge concentration tank 26, enters plate through sludge pump 27
Frame filter press 28, effluent recycling to collecting-tank 3, mud cake outward transport；The sludge that other each units generate is discharged by spoil disposal pipeline
Sludge concentration tank 23 enters plate and frame filter press 25, effluent recycling to conditioning tank 12, mud cake outward transport through sludge pump 24；
10 working method of air-floating apparatus is that the water outlet of coagulative precipitation tank 4 enters pressure air-dissolving tank 6 through air pressure pump 5,
It is passed through air into dissolving 6 simultaneously, opening pressure reducing valve 7 makes gas and water enter flotation tank, a large amount of fine gas bubbles is generated, in waste water
Substance similar in density and water attaches to bubble, is floated to wastewater surface, enters scum trough 8 through Slag Scraping Device 9, and in scum trough 8
Sludge be discharged into sludge concentration tank 23；
The characteristics of conditioning tank 12 has regulating pondage, uniformly walks water, flotation tank water outlet enters conditioning tank, lives simultaneously
Sewage enters conditioning tank by intake pump 11 and mixes with by pretreated coating waste-water.
The UASB15 is made of sludge reaction area, gas-liquid-solid three-phase separator 13 and gas chamber three parts.Have one in bottom
A high concentration, the Sludge Bed of high activity, sewage enter UASB15 from bottom to top, come into full contact in base sludge bed with sludge,
Organic substance in water matter becomes biogas by anaerobic fermentation.Biogas constantly merges in uphill process forms biggish bubble, sludge,
Water, biogas enter three phase separator 13 together, when biogas encounters the reflecting plate of separator lower part, are folded to the surrounding of reflecting plate, so
Water layer is passed through afterwards and enters gas chamber, concentrates on the export of gas chamber conduit 14, solid-liquid mixed liquor is by being reflected into three phase separator 13
Settling zone, the sludge in sewage flocculates, and particle is gradually increased, and is settled under the effect of gravity, and Sludge Bed is slid back to.Processing
Sewage afterwards is discharged from upper right side, and the sludge overflowed from sludge settling area top is discharged into sludge concentration tank 23.
The SBR18 working method is that UASB15 water outlet enters SBR18 by elevator pump 16, and sewage level reaches in pond
After setting height, compressed air 20 and 19 equipment of micro porous aeration head provide intermittent oxygen, are sufficiently mixed sewage with sludge,
Organic substance in degradation sewage, treated, and sewage enters intermediate pool 21, and sludge is discharged into sludge concentration tank 23.
The treatment process of a kind of coating waste-water and sanitary sewage includes such as the next stage:
1. pretreatment stage: coating waste-water flows into collecting-tank under the action of intake pump, later by the waste water in collecting-tank
Be introduced into coagulative precipitation tank, be added flocculant, by gravitational settling removal waste water in pollutant, finally by flotation tank into
One step removes SS, TP.
2. biological treatment stage: water outlet on last stage enters in UASB, carries out anaerobic reaction, and it is useless can to remove coating
Most of organic matter in water；Sewage is discharged from the upper port of UASB, and boosted pump enters in the pond SBR, and micropore is equipped in this device
Aeration head, can intermittent offer oxygen, be sufficiently mixed sewage with sludge, degradation of organic substances matter, while aerobic in the pond SBR
Replace generation, further denitrogenation dephosphorizing with anaerobic processes.
3. active carbon filtration stage: the water pumping in above-mentioned intermediate pool being gone out, is filtered by active carbon, will be given up
Some SS, colloidal substance, macromolecule organic, microorganism in water etc. further remove, and finally water outlet reaches sewage discharge mark
It is quasi-.
4. the Treatment of Sludge stage: flocculation medicament will be added in coagulative precipitation tank, flocculates, generate a large amount of sediment,
Sediment is discharged into sludge concentration tank by mud discharging mouth, is dehydrated under the action of plate and frame filter press, and the filtrate of generation flows back into
Collecting-tank, mud cake outward transport；The sludge that other each units generate is discharged into sludge concentration tank by spoil disposal pipeline, in the work of sludge pump
It enters plate and frame filter press under to be dehydrated, the filtrate of generation is back to conditioning tank, mud cake outward transport.
The above is the embodiment of the present invention, and it's not limited to that, all in spirit of the invention and appended claims
Same replacement, change and modification for being done within the scope of etc., should all be included in the protection scope of the present invention.
Claims (3)
1. the Integrated Processing Unit of a kind of coating waste-water and sanitary sewage, it is characterised in that: including pretreatment stage, biological treatment
Stage, filtration stage, Treatment of Sludge stage.Pretreatment stage include collecting-tank, coagulative precipitation tank, air pressure pump, pressure air-dissolving tank,
Flotation tank, conditioning tank；Biological treatment stage includes the pond UASB, SBR；Filtration stage is active carbon filtering ponds；The Treatment of Sludge stage
Including sludge concentration tank, sludge pump, plate and frame filter press.The equipment in each stage is sequentially connected in series by pipeline.
2. the Integrated Processing Unit of a kind of coating waste-water and sanitary sewage according to claim 1, it is characterised in that: coating
Waste water enters conditioning tank later into coagulating sedimentation and flotation tank excessively into pretreatment stage excessively, and sanitary sewage passes through water inlet
Pump enters conditioning tank and mixes with coating waste-water, enters biological treatment stage together.
3. the Integrated Processing Unit of a kind of coating waste-water and sanitary sewage according to claim 1, it is characterised in that: described
The process coating waste-water and sanitary sewage that biological treatment stage uses UASB to combine with SBR, waste water enter the bottom UASB
Sludge Bed is sufficiently reacted with sludge, and Organic substance in water matter generates biogas by anaerobic fermentation, and sludge, water, biogas enter three-phase separate
From device, export, the Sludge Bed of sludge automatic sedimentation to reactor bottom at the top of biogas autoreactor, treated sewage is from upper right
End discharge, boosted pump enter SBR, micro porous aeration head are equipped in the pond SBR, after sewage level reaches setting height in pond, carry out
Intermittent aeration, is sufficiently mixed sewage with sludge, and the organic substance in sewage of further degrading, treated, and sewage enters
Intermediate pool, sludge are discharged into sludge concentration tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710704177.3A CN109422412A (en) | 2017-08-16 | 2017-08-16 | A kind of Integrated Processing Unit of coating waste-water and sanitary sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710704177.3A CN109422412A (en) | 2017-08-16 | 2017-08-16 | A kind of Integrated Processing Unit of coating waste-water and sanitary sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109422412A true CN109422412A (en) | 2019-03-05 |
Family
ID=65497659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710704177.3A Withdrawn CN109422412A (en) | 2017-08-16 | 2017-08-16 | A kind of Integrated Processing Unit of coating waste-water and sanitary sewage |
Country Status (1)
| Country | Link |
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| CN (1) | CN109422412A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109824221A (en) * | 2019-04-04 | 2019-05-31 | 上海电气集团股份有限公司 | A kind of water paint waste water treatment system and application method |
| CN110818144A (en) * | 2019-12-21 | 2020-02-21 | 陈博文 | Waste water treatment device for cosmetic production |
| CN111908740A (en) * | 2020-09-06 | 2020-11-10 | 山东蓝城分析测试有限公司 | Method for treating wall imitation stone coating wastewater |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN205222944U (en) * | 2015-11-20 | 2016-05-11 | 浙江弗莱德环境科技有限公司 | Sewage treatment system |
-
2017
- 2017-08-16 CN CN201710704177.3A patent/CN109422412A/en not_active Withdrawn
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN205222944U (en) * | 2015-11-20 | 2016-05-11 | 浙江弗莱德环境科技有限公司 | Sewage treatment system |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109824221A (en) * | 2019-04-04 | 2019-05-31 | 上海电气集团股份有限公司 | A kind of water paint waste water treatment system and application method |
| CN110818144A (en) * | 2019-12-21 | 2020-02-21 | 陈博文 | Waste water treatment device for cosmetic production |
| CN110818144B (en) * | 2019-12-21 | 2022-05-24 | 康伦智美科技产业(青岛)有限公司 | Waste water treatment device for cosmetic production |
| CN111908740A (en) * | 2020-09-06 | 2020-11-10 | 山东蓝城分析测试有限公司 | Method for treating wall imitation stone coating wastewater |
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Application publication date: 20190305 |