CN203021377U - High-concentration liquid waste processing system - Google Patents
High-concentration liquid waste processing system Download PDFInfo
- Publication number
- CN203021377U CN203021377U CN 201320000728 CN201320000728U CN203021377U CN 203021377 U CN203021377 U CN 203021377U CN 201320000728 CN201320000728 CN 201320000728 CN 201320000728 U CN201320000728 U CN 201320000728U CN 203021377 U CN203021377 U CN 203021377U
- Authority
- CN
- China
- Prior art keywords
- pump
- waste liquid
- pond
- pool
- liquid
- 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
Images
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a high-concentration liquid waste processing system which comprises a lacquered wastewater pool, an electrophoresis liquid waste pool, a degreased liquid waste pool, a coagu-flocculation reaction tank, a bevel board precipitation tank and a pH reverse adjusting tank, wherein an air stirring device is arranged in each of the lacquered wastewater pool, the electrophoresis liquid waste pool and the degreased liquid waste pool, and the output ends of the lacquered wastewater pool, the electrophoresis liquid waste pool and the degreased liquid waste pool are respectively and correspondingly provided with a lacquered wastewater pump, an electrophoresis liquid waste pump and a degreased liquid waste pump. The high-concentration liquid waste processing system has a favorable fog processing effect; and energy sources can be saved.
Description
Technical field
The utility model relates to a kind of high-concentration waste liquid treating system, belongs to the technical field of Sewage treatment systems.
Background technology
The modern sewage disposal technology of existing sewage disposal is divided by degree for the treatment of and can be divided into one-level secondary and tertiary treatment.Coagulation is mainly removed requirement that the solid pollutant pledge reason facture major part that is suspended state in sewage can only complete coagulation and generally can be removed 30% left and right through the sewage BOD of coagulation and do not reach emission standard, and coagulation belongs to the pre-treatment second-stage treatment of second-stage treatment and mainly removes the organic pollution materials (BOD.COD material) that is colloid and dissolved state in sewage.Clearance can reach more than 90%. and make organic pollutant reach emission standard.Tertiary treatment. further process the organism of difficult degradation. nitrogen and phosphorus etc. can cause the solubility inorganics of body eutrophication etc.Main method has biological carbon and phosphorous removal method, coagulant sedimentation, sand coarse aggregate ratio method, active carbon adsorption, ion exchange method and electric osmose analytical method etc.Whole process is after promoting through sewage pump by the raw waste water that thick lattice are deleted, delete or sieve rate device through lattice, enter afterwards settling pit, through sand moisture from sewage enter and be coagulation (being physical treatment) more than first pond. the water outlet of preliminary sedimentation tank enters biological treating equipment, activated sludge process and biological process are arranged, and (wherein the reactor of activated sludge process has the biomembrance process such as aeration tank oxidation ditch to comprise the biological filter, blodisc, biological contact oxidation process and biological fluidized bed).The water outlet of biological treating equipment enters secondary sedimentation basins. and the water outlet of second pond is discharged or is entered the tertiary treatment coagulation and finishes to be second-stage treatment to this through sterilization.Tertiary treatment comprises biological carbon and phosphorous removal method, coagulant sedimentation, sand filtration method, active carbon adsorption, ion exchange method and electroosmose process.A mud part is back to primary sedimentation pond or biological treating equipment, and a part enters sludge thickener, enters afterwards sludge digestion tank, and after dehydration and drying plant, mud is utilized at last.But existing treatment technology treatment effect is not ideal, and needs a large amount of energy runnings.
The utility model content
The utility model purpose is to provide a kind of high-concentration waste liquid treating system for the defective that prior art exists.
The utility model adopts following technical scheme for achieving the above object:
the utility model high-concentration waste liquid treating system, comprise the painting wastewater pond, the electrophoresis waste liquid pool, the degreasing wasting liquid pond, the coagulating groove, the anti-groove of transferring of sloping plate deposition groove and pH, the painting wastewater pond, in electrophoresis waste liquid pool and degreasing wasting liquid pond, air stirrer is set all, the painting wastewater pond, the output terminal in electrophoresis waste liquid pool and degreasing wasting liquid pond correspondence respectively arranges the painting wastewater pump, electrophoresis waste drains pump and degreasing wasting liquid pump, described air stirrer is respectively to painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid stirs, painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid passes through respectively the painting wastewater pump, the electrophoresis waste drains pump, the degreasing wasting liquid pump is promoted to and regulates the pH value in the coagulating groove, enter the anti-groove of transferring of pH after waste liquid after adjusting pH value precipitates through the sloping plate deposition groove and further regulate pH value.
Described sloping plate deposition groove comprises outer settling bath body, resembles in the settling bath body between the mouth of a river and water outlet inclined plate packing is set.
A plurality of reinforcement channel-section steels also are set on described settling bath body.
The utility model is introduced into sanitary sewage (each compartmentation manure pit processed waste water of dining room waste water and factory) between the grid of the sanitary sewage equalizing tank front end in waste water station, after the rotary type grid is removed foreign material, be promoted to sanitary sewage equalizing tank (being provided with air stirrer) through pump after flowing into pump well, then be promoted to combined sewage pond (being provided with mechanical stirring device) through pump, materialization waste water also pumps into the combined sewage pond of waste water station;
Mechanical stirring device is established in the combined sewage pond, prevents the suspended substance precipitation, regulates simultaneously the waste water water yield and water quality.
In the combined sewage pond, sewage is promoted in hydrolysis acidification pool through pump, and through after acidication, the biodegradability of waste water is improved, and pollutent obtains the part removal simultaneously.Then waste water enters in contact-oxidation pool, biological contact oxidation process belongs to biomembrance process, by the microbial film that is attached in elastic filler, waste water flows in the elastic filler of up/down perforation, extensively contact with microbial film, under the condition of aerobic, through the effect of the bacteria metabolism function on microbial film, organic pollutant in waste water is removed, and waste water is purified.
Description of drawings
Fig. 1: the utility model one-piece construction figure;
Fig. 2: sloping plate deposition groove structure iron.
Embodiment
as shown in Figure 1, the utility model high-concentration waste liquid treating system, it is characterized in that comprising the painting wastewater pond, the electrophoresis waste liquid pool, the degreasing wasting liquid pond, the coagulating groove, the anti-groove of transferring of sloping plate deposition groove and pH, the painting wastewater pond, in electrophoresis waste liquid pool and degreasing wasting liquid pond, air stirrer is set all, the painting wastewater pond, the output terminal in electrophoresis waste liquid pool and degreasing wasting liquid pond correspondence respectively arranges the painting wastewater pump, electrophoresis waste drains pump and degreasing wasting liquid pump, described air stirrer is respectively to painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid stirs, painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid passes through respectively the painting wastewater pump, the electrophoresis waste drains pump, the degreasing wasting liquid pump is promoted to and regulates the pH value in the coagulating groove, enter the anti-groove of transferring of PH after waste liquid after adjusting pH value precipitates through the sloping plate deposition groove and further regulate the pH value.
As shown in Figure 2, described sloping plate deposition groove comprises outer settling bath body 3, interior elephant of settling bath body 3, inclined plate packing 2 is set between the mouth of a river and water outlet.
A plurality of reinforcement channel-section steels 1 also are set on described settling bath body 3.Wherein on settling bath body 3, d1-d2 is drain, the C1-C2 mud discharging mouth, and the b water outlet, a1-a2 resembles the mouth of a river.
The treatment process of high-concentration waste liquid treating system is as follows:
A) painting wastewater, electrophoresis waste liquid, degreasing wasting liquid are stored in separately waste liquid pool; Adopt air stirrer respectively painting wastewater, electrophoresis waste liquid, degreasing wasting liquid in painting wastewater pond, electrophoresis waste liquid pool and degreasing wasting liquid pond to be stirred;
B) enter after painting wastewater, electrophoresis waste liquid, the degreasing wasting liquid after stirring adopts the coagulating groove to carry out that coagulating, sloping plate deposition groove carry out sloping plate deposition and pH is counter to transfer groove to carry out that pH is anti-to transfer successively in the coating waste pond.
Painting wastewater, electrophoresis waste liquid, degreasing wasting liquid (with comprising assembly shop drench with rain waste water, press workshop mould Cleaning Wastewater) store in waste liquid pool separately.Air stirrer is set in the pond, respectively painting wastewater, electrophoresis waste liquid, degreasing wasting liquid is stirred, at the bottom of preventing that pollution substance from sinking to the pond.Painting wastewater, electrophoresis waste liquid, degreasing wasting liquid are promoted in coagulating groove 1 through painting wastewater pump, electrophoresis waste drains pump, degreasing wasting liquid pump respectively, add in the coagulating groove 1 calcium hydroxide and sulphur acid for adjusting pH value to suitable value (degreasing wasting liquid pH value: 2 ~ 3, degreasing wasting liquid adds the calcium chloride breakdown of emulsion simultaneously; Painting wastewater pH value: 3; Electrophoresis waste liquor PH value: 11 ~ 12), and then add Fe+, PAM, enter sloping plate deposition groove 4 through waste water after fully reacting, sedimentable matter sinks to the sloping plate deposition trench bottom, the waste water of clarification enters that pH is counter to be transferred in groove 2, add sulfuric acid or NaOH in transferring groove 2 pH is counter, regulate pH value to 6～9, water outlet enters in the coating waste pond.The mud that reaction produces drains in the mixing sludge pond.
The above is only preferred embodiment of the present utility model, be not limited to the utility model, although with reference to previous embodiment, the utility model is had been described in detail, for a person skilled in the art, it still can be modified to the technical scheme that aforementioned each embodiment puts down in writing, and perhaps part technical characterictic wherein is equal to replacement.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (3)
1. high-concentration waste liquid treating system, it is characterized in that comprising the painting wastewater pond, the electrophoresis waste liquid pool, the degreasing wasting liquid pond, the coagulating groove, the anti-groove of transferring of sloping plate deposition groove and pH, the painting wastewater pond, in electrophoresis waste liquid pool and degreasing wasting liquid pond, air stirrer is set all, the painting wastewater pond, the output terminal in electrophoresis waste liquid pool and degreasing wasting liquid pond correspondence respectively arranges the painting wastewater pump, electrophoresis waste drains pump and degreasing wasting liquid pump, described air stirrer is respectively to painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid stirs, painting wastewater, the electrophoresis waste liquid, degreasing wasting liquid passes through respectively the painting wastewater pump, the electrophoresis waste drains pump, the degreasing wasting liquid pump is promoted to and regulates the pH value in the coagulating groove, enter the anti-groove of transferring of pH after waste liquid after adjusting pH value precipitates through the sloping plate deposition groove and further regulate the pH value.
2. high-concentration waste liquid treating system according to claim 1, is characterized in that described sloping plate deposition groove comprises outer settling bath body (3), resembles in settling bath body (3) inclined plate packing (2) is set between the mouth of a river and water outlet.
3. high-concentration waste liquid treating system according to claim 2, is characterized in that also arranging on described settling bath body (3) a plurality of reinforcement channel-section steels (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320000728 CN203021377U (en) | 2013-01-03 | 2013-01-03 | High-concentration liquid waste processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320000728 CN203021377U (en) | 2013-01-03 | 2013-01-03 | High-concentration liquid waste processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203021377U true CN203021377U (en) | 2013-06-26 |
Family
ID=48645373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320000728 Expired - Fee Related CN203021377U (en) | 2013-01-03 | 2013-01-03 | High-concentration liquid waste processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203021377U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103043828A (en) * | 2013-01-03 | 2013-04-17 | 江苏新裕泰华环保有限公司 | System and method for treating high-concentration waste liquid |
| CN108128936A (en) * | 2018-02-01 | 2018-06-08 | 江苏华达环境工程有限公司 | Application degreasing wasting liquid processing unit |
| CN111943395A (en) * | 2020-08-13 | 2020-11-17 | 江苏华晖环保科技有限公司 | Electrophoresis wastewater treatment system and treatment method |
-
2013
- 2013-01-03 CN CN 201320000728 patent/CN203021377U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103043828A (en) * | 2013-01-03 | 2013-04-17 | 江苏新裕泰华环保有限公司 | System and method for treating high-concentration waste liquid |
| CN108128936A (en) * | 2018-02-01 | 2018-06-08 | 江苏华达环境工程有限公司 | Application degreasing wasting liquid processing unit |
| CN111943395A (en) * | 2020-08-13 | 2020-11-17 | 江苏华晖环保科技有限公司 | Electrophoresis wastewater treatment system and treatment method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102910788B (en) | A kind of waste water advanced denitrification process | |
| CN102557359B (en) | Device for treating wastewater during production of pentaerythritol | |
| CN101698550A (en) | Advanced treating method of landfill leachate | |
| CN103739107B (en) | A kind for the treatment of process of household appliances degreasing process waste water | |
| CN102795747A (en) | Waste water treatment process | |
| CN103435233B (en) | Equipment and method for recycling chemical fiber continuous-spinning wastewater | |
| CN104591487A (en) | Dimethylformamide and dimethylamine wastewater treatment process for synthetic leather production | |
| CN110104873A (en) | Municipal wastewater advanced treatment apparatus and its method | |
| CN204958667U (en) | Resident sewage treatment system | |
| CN104016550B (en) | Sewage water treatment method in Apparel Manufacturing | |
| CN203700070U (en) | Device for mixing and recycling steel waste water and municipal sewage | |
| CN203021377U (en) | High-concentration liquid waste processing system | |
| CN104926013A (en) | Bath water recycling MBR technology | |
| CN203922903U (en) | A kind of mine tailing wastewater treatment system | |
| CN106396245A (en) | A treating process for phosphorus-containing waste water | |
| CN203461924U (en) | Grain and oil production sewage treatment system | |
| CN203613075U (en) | Wastewater treatment system | |
| CN104944694A (en) | Equipment for sewage bio-treatment of coating factory by use of purified diatomite and treatment method for equipment | |
| RU124674U1 (en) | WASTE WATER TREATMENT SYSTEM FOR OIL AND GAS PRODUCING PLATFORMS AND TERMINALS | |
| CN205368049U (en) | Sizing agent effluent treatment plant | |
| CN104891738A (en) | Ecological treatment method of municipal sewage | |
| CN106865893B (en) | A kind of domestic sewage treatment process | |
| CN217103411U (en) | Mobile photoelectric complementary sewage deep purification system | |
| CN217103412U (en) | Movable integrated sewage treatment system | |
| CN205076943U (en) | Effluent disposal system who strains device is received in adoption |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130626 Termination date: 20160103 |