CN206692495U - A kind of sewage and waste water treatment device - Google Patents
A kind of sewage and waste water treatment device Download PDFInfo
- Publication number
- CN206692495U CN206692495U CN201720458715.0U CN201720458715U CN206692495U CN 206692495 U CN206692495 U CN 206692495U CN 201720458715 U CN201720458715 U CN 201720458715U CN 206692495 U CN206692495 U CN 206692495U
- Authority
- CN
- China
- Prior art keywords
- processing unit
- unit according
- waste water
- mixer
- tank
- 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
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 8
- 239000010865 sewage Substances 0.000 title claims abstract description 7
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- 230000000694 effects Effects 0.000 claims abstract description 15
- 238000005660 chlorination reaction Methods 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 239000010802 sludge Substances 0.000 claims description 8
- 239000008187 granular material Substances 0.000 claims description 7
- 238000005868 electrolysis reaction Methods 0.000 claims description 6
- 238000006555 catalytic reaction Methods 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910002804 graphite Inorganic materials 0.000 claims description 3
- 239000010439 graphite Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- 239000010936 titanium Substances 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- 241000276438 Gadus morhua Species 0.000 abstract description 8
- 235000019516 cod Nutrition 0.000 abstract description 8
- 240000007842 Glycine max Species 0.000 abstract description 7
- 235000010469 Glycine max Nutrition 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 6
- 201000010099 disease Diseases 0.000 abstract description 4
- 230000037250 Clearance Effects 0.000 abstract description 3
- 230000035512 clearance Effects 0.000 abstract description 3
- 238000007654 immersion Methods 0.000 abstract description 2
- 238000010297 mechanical methods and process Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 description 27
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000000126 substance Substances 0.000 description 5
- 239000003814 drug Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- MHAJPDPJQMAIIY-UHFFFAOYSA-N hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- BAUYGSIQEAFULO-UHFFFAOYSA-L Iron(II) sulfate Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000000249 desinfective Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
Abstract
The utility model belongs to stain disease processing technology field, and in particular to a kind of sewage and waste water treatment device, including comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sedimentation basin, more medium filter, chlorination equipment；The comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sedimentation basin, more medium filter, chlorination equipment pass sequentially through pipeline connection.The beneficial effects of the utility model are that apparatus structure provided by the utility model is simple, the stain disease that can effectively administer after immersion soya bean, COD clearances are made to reach more than 80%, easy to operate simple and treatment effect is excellent, stable, there is very strong feasibility in actual mechanical process.
Description
Technical field
The utility model belongs to stain disease processing technology field, and in particular to a kind of sewage and waste water treatment device.
Background technology
Soybean processing waste water meeting dissolution many amino acid, protein and organic matters, therefore, the COD of soybean processing waste water
Generally all, because amino acid and phosphatic content are high, cause body eutrophication tight in 10000-26000mg/L or so
Weight, makes the dissolved oxygen in water decline rapidly, waste water is easily putrid and deteriorated to make water quality deterioration, and discharges the effluviums such as hydrogen sulfide
Taste.
In the prior art, flotation tank and biochemical process, these methods pair are typically used to soybean processing waste water processing method
COD reduction has certain effect, but reduces unobvious, or unsatisfactory.In recent years, electrochemical method is as a kind of environment
Friendly technology, the bio-refractory organic matter particularly in waste water is increasingly valued by people in terms of environmental pollution improvement
In terms of removal, heavy metal wastewater thereby etc. is related to, electrochemistry has played immeasurable effect.Thus, electrochemical water treatment technology is near
Nian Laiyi turns into the quite active research field of world's water technology, by extensive concern both domestic and external.
Utility model content
To solve above-mentioned the deficiencies in the prior art, the utility model provides a kind of dirt of double section ionization integrations and given up
Water treatment facilities, the device make COD clearances reach more than 80%, and phosphor-removing effect is very good, and technique is advanced, easy to operate and place
Manage excellent effect.
To achieve the above object, technical solution adopted in the utility model is as follows：
A kind of sewage and waste water treatment device, including comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sedimentation basin be situated between more
Mass filter, chlorination equipment；The comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sedimentation basin, more medium filter,
Chlorination equipment passes sequentially through pipeline connection.
Full-automatic agent-feeding device is provided between the comprehensive collecting-tank and Hi-mixer, is mainly used in adjusting pH in waste water
Value, prepared to enter ionization device reaction, wherein chemical feeding quantity will determine according to pH value of waste water.
The medicament is technical-grade hydrochloric acid or technical-grade hydrochloric acid, the mixture of hydrogen peroxide and ferrous sulfate.
Double section ionization devices are divided into a stage and two-stage, wherein the single order section is excessively electric including at least a three-dimensional
Position electrolysis unit, two-stage comprise at least a catalyst reaction device；One stage was mainly used in reducing COD value, as long as the two-stage
For improving pH value, the waste water after being handled through double sections of ionization devices is set to reach the pH value for discharging water in neutrality.
The sedimentation basin is provided with mud-removing bucket, sets spoil disposal pipeline at mud-removing bucket, is connected with sludge storage pool.
The medial launder of cushioning effect has been provided between the sedimentation basin and more medium filter.
The positive plate material is steel plate or titanium pole plate, and the negative electrode is graphite or red copper.
The granule electrode is activated carbon or conductivity ceramics.
The three-dimensional overpotential electrolysis unit includes fast reaction groove, electric negative electrode, anode, granule electrode, inlet channel, gone out
Mill weir, steam line, gas distributing pipeline.
The catalyst reaction device include catalytic reaction groove, high effective and modified elctro-catalyst, backwash pump, inlet channel,
Effluent weir, steam line, gas distributing pipeline.
The high effective and modified elctro-catalyst is iron C catalyst.
Multimedium is activated carbon and quartz sand in the more medium filter.
During plant running, soybean processing waste water is excluded in comprehensive collecting-tank, chemical feeding quantity is determined according to pH value of waste water, will
Waste water and medicament are discharged into double section ionization devices after Hi-mixer is well mixed and handled, main to reduce COD and dephosphorization,
Wherein three-dimensional overpotential electrolysis unit includes two sections, and when finishing draining to epimere operation, waste water is pumped into hypomere operation,
When hypomere operation finishes draining, then waste water is pumped into epimere operation, such alternate run, after double sections of ionization device processing
Waste water is pumped into sedimentation basin, enters sludge storage pool through mud-removing bucket after sludge settling in waste water, and waste water further flows into medial launder, is risen
Cushioning effect, more medium filter is then pumped into again and carries out filtration treatment, is most flowed back afterwards through disinfection by ultraviolet light rear portion, one
Divide discharge.
Relative to prior art, the beneficial effects of the utility model are that apparatus structure provided by the utility model is simple,
The stain disease that can effectively administer after immersion soya bean, makes COD clearances reach more than 80%, phosphor-removing effect is very good, easy to operate
Simple and treatment effect is excellent, stable, there is very strong feasibility in actual mechanical process.In addition, using double section electricity
From equipment, take wastewater treatment packet to carry out, electric current can be reduced, reduce actual motion cost.
Brief description of the drawings
Fig. 1 is the utility model schematic flow sheet；
Fig. 2 is the utility model structure diagram；
Fig. 3 is double section ionization device structural representations；
Wherein, 1 is comprehensive collecting-tank, and 2 be Hi-mixer, and 3 be double section ionization devices, and 4 be sedimentation basin, and 5 be multimedium
Filter, 6 be sterilization pool, and 7 be reuse pool, and 8 be sludge storage pool, and 9 be medial launder, and 10 be backwash pump, and 11 full-automatic
Chemicals dosing plant；31 be inlet channel, and 32 be fast reaction groove, and 33 be electric negative electrode, and 34 be anode, and 35 be granule electrode, and 36 be confession
Feed channel, 37 be effluent weir, and 38 be catalytic reaction groove, and 39 be high effective and modified elctro-catalyst, and 310 be water distribution pipe, and 311 be gas distribution
Pipeline, 312 be backwash pump.
Specific embodiment
The utility model is further explained below in conjunction with the accompanying drawings, but embodiment does not do any shape to the utility model
The restriction of formula.Unless stated otherwise, the utility model uses reagent, method and apparatus is the art conventional reagent, sides
Method and equipment.
A kind of sewage and waste water treatment device, including comprehensive collecting-tank 1, Hi-mixer 2, double sections of ionization devices 3, sedimentation basin 4,
More medium filter 5, chlorination equipment 6；It is the comprehensive collecting-tank 1, Hi-mixer 2, double sections of ionization devices 3, sedimentation basin 4, more
Medium filter 5, chlorination equipment 6 pass sequentially through pipeline connection.
Full-automatic agent-feeding device 11 is provided between the comprehensive collecting-tank 1 and Hi-mixer 2, is mainly used in adjusting waste water
Middle pH value, prepared to enter ionization device reaction, wherein chemical feeding quantity will determine according to pH value of waste water.
The medicament is technical-grade hydrochloric acid or technical-grade hydrochloric acid, the mixture of hydrogen peroxide and ferrous sulfate.
Double section ionization devices 3 include fast reaction groove 32, electric negative electrode 33, anode 34, granule electrode 35, inlet channel
31st, effluent weir 37, steam line 36, gas distributing pipeline 311, catalytic reaction groove 38, high effective and modified elctro-catalyst 39, backwash pump
312。
The sedimentation basin 4 is provided with mud-removing bucket, sets spoil disposal pipeline at mud-removing bucket, is connected with sludge storage pool 8.
The medial launder 9 of cushioning effect has been provided between the sedimentation basin 4 and more medium filter 5.
The plate material of anode 34 is steel plate or titanium pole plate, and the electric negative electrode 33 is graphite or red copper.
The granule electrode 35 is activated carbon or conductivity ceramics.
The high effective and modified elctro-catalyst 39 is iron C catalyst.
During plant running, soybean processing waste water is excluded in comprehensive collecting-tank 1, chemical feeding quantity is determined according to pH value of waste water,
Waste water and medicament are discharged into double section ionization devices 3 after Hi-mixer 2 is well mixed to be handled, it is main reduce COD and
Dephosphorization, wherein three-dimensional overpotential electrolysis unit includes two sections, when finishing draining to epimere operation, waste water is pumped into hypomere
Operation, when hypomere operation finishes draining, then waste water is pumped into epimere operation, such alternate run, at double sections of ionization devices 3
Waste water after reason is pumped into sedimentation basin 4, enters sludge storage pool 8 through mud-removing bucket after sludge settling in waste water, waste water further flows
Enter medial launder 9, play cushioning effect, be then pumped into more medium filter 5 again and carry out filtration treatment, last sterilized rear portion is returned
Stream, part discharge.
Embodiments above describes general principle and preparation method of the present utility model, and the technical staff of the industry should
The understanding, the utility model are not restricted to the described embodiments, and simply illustrate this reality described in above-described embodiment and specification
With new principle and structure, the utility model also has various changes on the premise of the spirit and scope of the utility model is not departed from
Change and improve, these changes and improvements are both fallen within claimed scope.
Claims (9)
1. a kind of sewage and waste water treatment device, it is characterised in that including comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sink
Shallow lake pond, more medium filter, chlorination equipment；The comprehensive collecting-tank, Hi-mixer, double sections of ionization devices, sedimentation basin, more Jie
Mass filter, chlorination equipment pass sequentially through pipeline connection.
2. processing unit according to claim 1, it is characterised in that be provided between the comprehensive collecting-tank and Hi-mixer
Full-automatic agent-feeding device.
3. processing unit according to claim 1, it is characterised in that double section ionization devices are divided into a stage and second order
Section, wherein the single order section comprises at least a three-dimensional overpotential electrolysis unit, the two-stage comprises at least a catalytic reaction and filled
Put.
4. processing unit according to claim 3, it is characterised in that the three-dimensional overpotential electrolysis unit includes fast reaction
Groove, electric negative electrode, anode, granule electrode, inlet channel, effluent weir, steam line, gas distributing pipeline.
5. processing unit according to claim 1, it is characterised in that the sedimentation basin is provided with mud-removing bucket, is set at mud-removing bucket
Spoil disposal pipeline is put, is connected with sludge storage pool.
6. processing unit according to claim 1, it is characterised in that be provided between the sedimentation basin and more medium filter
The medial launder of cushioning effect.
7. processing unit according to claim 4, it is characterised in that the positive plate material is steel plate or titanium pole plate, described
Negative electrode is graphite or red copper.
8. processing unit according to claim 4, it is characterised in that the granule electrode is activated carbon or conductivity ceramics.
9. processing unit according to claim 3, it is characterised in that the catalyst reaction device includes catalytic reaction groove, height
The modified elctro-catalyst of effect, backwash pump, inlet channel, effluent weir, steam line, gas distributing pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720458715.0U CN206692495U (en) | 2017-04-27 | 2017-04-27 | A kind of sewage and waste water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720458715.0U CN206692495U (en) | 2017-04-27 | 2017-04-27 | A kind of sewage and waste water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206692495U true CN206692495U (en) | 2017-12-01 |
Family
ID=60447821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720458715.0U Expired - Fee Related CN206692495U (en) | 2017-04-27 | 2017-04-27 | A kind of sewage and waste water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206692495U (en) |
-
2017
- 2017-04-27 CN CN201720458715.0U patent/CN206692495U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2010115319A1 (en) | Sewage treatment process and system | |
| CN107337301B (en) | A kind of method of the electric Fenton processing waste water of additional hydrogen peroxide | |
| CN106800356A (en) | A kind of advanced treatment of wastewater regeneration device based on biochemical and electrolysis tech | |
| CN205313291U (en) | Refrigeration cycle water integrated processing system | |
| CN104402172A (en) | Industrial wastewater treatment method | |
| CN102153221A (en) | Process for treating oil field produced water | |
| CN107055937A (en) | A kind of advanced treatment of wastewater regeneration method based on biochemical and electrolysis tech | |
| CN109368746A (en) | A kind of high COD, difficult biochemical waste water pretreatment unit pretreatment system and method | |
| CN210176671U (en) | High-salt high-concentration degradation-resistant organic wastewater treatment equipment | |
| WO2020238021A1 (en) | Intensive modular combined aquaculture tail water treatment system | |
| CN203319806U (en) | Electrolysis dephosphorization device for treating domestic sewage | |
| CN105417839B (en) | A kind of processing system and method for pre-electroplating treatment waste water | |
| CN105036261B (en) | A kind of internal-circulation type iron-carbon micro-electrolysis reactor | |
| CN110066054A (en) | Electric Fenton system and landfill leachate thick liquid processing method for the processing of landfill leachate dope | |
| CN207062081U (en) | A kind of pharmaceutical wastewater processing system | |
| CN105314772B (en) | The final waste discharge processing system of cold rolling and processing method | |
| CN101973659A (en) | Device and method for refining waste water by treating vitamin B12 by means of co-use of micro-electrolysis and physicochemical method | |
| CN105217846B (en) | Cold rolling alkalescence waste discharge advanced treatment system and processing method | |
| CN206692495U (en) | A kind of sewage and waste water treatment device | |
| CN206255960U (en) | A kind of city domestic sewage processing system | |
| CN109336328A (en) | A kind of bioelectrochemistry synchronous denitrification dephosphorizing devices and methods therefor | |
| CN205313294U (en) | But continuous operation's cooling circulating water treatment system | |
| CN105060656B (en) | Biochemical system auxiliary device and application thereof | |
| CN106882900A (en) | A kind of later stage depth processing unit of organic wastewater and its technological process | |
| CN207659238U (en) | A kind of film electricity combination water treatment facilities |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171201 Termination date: 20190427 |