CN201634490U - Sewage purification device using solar electro-flotation - Google Patents
Sewage purification device using solar electro-flotation Download PDFInfo
- Publication number
- CN201634490U CN201634490U CN2009202538988U CN200920253898U CN201634490U CN 201634490 U CN201634490 U CN 201634490U CN 2009202538988 U CN2009202538988 U CN 2009202538988U CN 200920253898 U CN200920253898 U CN 200920253898U CN 201634490 U CN201634490 U CN 201634490U
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- 239000010865 sewage Substances 0.000 title claims abstract description 38
- 238000000746 purification Methods 0.000 title claims abstract description 13
- 238000005188 flotation Methods 0.000 title abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000007599 discharging Methods 0.000 claims description 20
- 238000005868 electrolysis reaction Methods 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 4
- 239000004571 lime Substances 0.000 claims description 4
- 238000012546 transfer Methods 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 2
- 238000010168 coupling process Methods 0.000 claims description 2
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004134 energy conservation Methods 0.000 abstract description 4
- 238000003756 stirring Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 230000007774 longterm Effects 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 description 14
- 238000012545 processing Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 229910021421 monocrystalline silicon Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000013082 photovoltaic technology Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910021417 amorphous silicon Inorganic materials 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008396 flotation agent Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000012549 training Methods 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/20—Climate change mitigation technologies for sector-wide applications using renewable energy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model provides a sewage purification device using solar electro-flotation. The device comprises a solar power supply appliance, a sewage stirring pool and an electrolytic processor, wherein the solar power supply appliance comprises a solar photovoltaic battery pack, a charge-discharge controller, an inverter, a manostat and a battery; a stirrer is arranged in the sewage stirring pool; a cathode plate and an anode plate are arranged in the electrolytic processor, and an inlet and an outlet are formed on the electrolytic processor; and the sewage stirring pool is connected with the electrolytic processor through a delivery pipe and a water pump on the delivery pipe. The device is characterized in that the stirrer, the water pump, the cathode plate and the anode plate are electrically connected with the solar power supply appliance through conducting wires. The device provided by the utility model fundamentally solves the problems that the electro-floatation method for sewage treatment causes large electrical consumption, so that the treatment cost is high, enterprises are difficult to keep running normally, sewage water is still discharged after repeated prohibition, and the pollution is serious; besides, the device saves energy, reduces running cost, is particularly suitable for sewage treatment in occasions with inconvenient electric energy supply, and has the characteristics of safety, environmental protection, energy conservation, good purification effect, low cost, long service life, long-term profit with one investment and the like.
Description
Technical field
The utility model relates to a kind of device of purifying waste water, and especially a kind of device that utilizes sun power electrolysis floatation purification sewage belongs to the technical field of disposing of sewage with electro-flotation method.
Background technology
Along with the order benefit of wastewater discharge standard is strict, the expense of municipal effluent and trade effluent biological treatment improves constantly.For this reason, people try hard to seek that processing costs is low, processing efficiency is high, the obvious results novel method.Electro-flotation method is handled the comparatively energy-conservation approach that provides for sewage purification, it sticks to sewage and pollutants in waste water on the small hydrogen and oxygen bubble that electrolysis produces, and with bubble float on the water surface and and water sepn, therefore, electro-flotation method has been used to handle the makers' sewage of plam oil, oily(waste)water and oil-containing oil emulsion, laughable factory effluent, mining wastewater, underground sewage, laundry effluents, fatty waste water, hotel waste water, foodstuffs industry sewage, dairy factory waste water, municipal effluent, pit water, the waste water that contains colloidal particle and heavy metal, and can from cyanide wastewater, reclaim Jin Heyin.But in the electro-flotation method process for the treatment of waste water, but want the mass consumption energy, especially to from public electric wire net, obtain electric energy, be unfavorable for saving energy and reduce the cost, and too high because of processing costs, make many enterprises be difficult to bear, therefore, blowdown just can occur and remain incessant after repeated prohibition, rivers and lakes pollute more and more serious situation.Particularly along with worldwide energy dilemma, electro-flotation method also will face problems such as energy shortage, cost rising.And in the development of contemporary science and technology, energy-conservation and environmental protection is global progressive two principal themes.
The training Crelle had found " photovoltaic effect " in 1839, and since then, especially closely during the last ten years, photovoltaic technology has had development rapidly.Through research for many years, developed monocrystalline silicon battery, polycrystal silicon cell, amorphous silicon battery, hull cell and multiple compound battery, and the efficiency of conversion of battery is significantly improved.The efficient of commercialization battery has reached 15%~17% (monocrystalline silicon battery) and 14%~15% (polycrystal silicon cell) respectively at present, and the highest laboratory efficient surpasses 25%.And along with the progress of photovoltaic technology and the expansion of industry size, the manufacturing cost of solar cell and price also will constantly descend.These all are that road has been paved in the large scale application of sun power.
Summary of the invention
The purpose of this utility model is to provide a kind of waste disposal plant of middle and small scale, and the electric energy that promptly utilizes the solar-energy photo-voltaic cell array to produce drives the electrolytic floatage system, and then handles, purifies waste water, and makes it to reach emission request, and is simultaneously energy-conservation.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of device that utilizes sun power electrolysis floatation purification sewage, comprise by the solar-energy photo-voltaic cell group, charging-discharging controller, invertor, potentiostat, the solar energy electric supplier that battery constitutes, establish the sewage agitated pool of agitator in it, establish negative electrode and positive plate in it, establish the electrolytic treater of import and outlet on it, and the sewage agitated pool by transfer lime and on water pump link to each other with electrolytic treater, it is characterized in that agitator, water pump, negative electrode and positive plate are all by lead and solar energy electric supplier electrical coupling.With the electric energy that utilizes sun power to be converted to waste disposal plant is powered, to save conventional electrical network electric energy.
The drive-motor of described agitator and water pump links to each other with invertor by lead, invertor links to each other with charging-discharging controller by lead, charging-discharging controller links to each other with the solar-energy photo-voltaic cell group by lead, so that the electric energy that the solar-energy photo-voltaic cell group is produced is through charging-discharging controller, again after the invertor conversion, for drive-motor provides working power.
Described negative electrode all links to each other with potentiostat by lead with positive plate, potentiostat links to each other with charging-discharging controller by lead, charging-discharging controller links to each other with the solar-energy photo-voltaic cell group by lead, so that the electric energy that the solar-energy photo-voltaic cell group is produced is through charging-discharging controller, again after the potentiostat voltage stabilizing, for negative electrode and positive plate provide the electrolysis electric energy.
The utility model compared with prior art has following advantage and effect: adopt such scheme, the electric energy that promptly utilizes sun power to produce is powered to the consumer of electrolytic floatage technology, not only can fundamentally solve the processing costs height that electro-flotation method is disposed of sewage and brought greatly because of current consumption, enterprise is difficult to normally keep, blowdown remains incessant after repeated prohibition, problem such as seriously polluted, and saved the energy, reduced running cost, be applicable to mining wastewater, laundry effluents, hotel waste water, the processing of municipal effluent and colloidal particle waste water and purification are specially adapted to the sewage disposal that electric energy is supplied inconvenient occasion.This system has that safety and environmental protection, save energy, good purification, running cost are low, long service life, less investment, instant effect, long-term characteristics such as be benefited of investment once.Index after table 1, table 2 have provided and disposed of sewage with the utility model.
Table 1. sewage parameter
Table 2. sewage disposal result
Description of drawings
Fig. 1 is the structural representation of the utility model.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further.
As Fig. 1, the device that utilizes sun power electrolysis floatation purification sewage that the utility model provides, comprise solar energy electric supplier, sewage agitated pool and electrolytic treater, wherein, solar energy electric supplier is by solar-energy photo-voltaic cell group 5, charging-discharging controller 7, invertor 4, potentiostat 9, battery 8 constitutes, establish agitator 3 in the sewage agitated pool 2, agitator 3 supports by support 1, so that after in sewage lagoon 2, throwing in flotation reagent, stir by agitator 3, thereby for electrolytic floatage is prepared, negative plate 16 and positive plate 17 are installed by bench insulator 15 respectively in first treatment chamber 11 in the electrolytic treater 22 and 12 bottoms, precision processing chamber, establish import 19 on the electrolytic treater 22, this import 19 links to each other with sewage agitated pool 2 by transfer lime and water pump 20, place the pipe end of the transfer lime in the sewage agitated pool 2 to be provided with filtering net 21, electrolytic treater 22 is provided with clear water output 14 and emissions mouth 18, the drive-motor of agitator 3 and water pump 20 links to each other with invertor 4 by lead 6, invertor 4 links to each other with charging-discharging controller 7 by lead 6, charging-discharging controller 7 links to each other with solar-energy photo-voltaic cell group 5 by lead 6, so that the electric energy that the solar-energy photo-voltaic cell group is produced is through charging-discharging controller 7, again after invertor 4 conversions, for drive-motor provides working power; Negative plate 16 all links to each other with potentiostat 9 by lead 6 with positive plate 17, potentiostat 9 links to each other with charging-discharging controller 7 by lead 6, charging-discharging controller 7 links to each other with solar-energy photo-voltaic cell group 5 by lead 6, so that the electric energy that solar-energy photo-voltaic cell group 5 is produced is through charging-discharging controller 7, again after potentiostat 9 voltage stabilizings, for negative plate 16 and positive plate 17 provide the electrolysis electric energy, also can charge to battery 8 by charging-discharging controller 7.When to agitator 3, water pump 20 and negative plate 16, positive plate 17 power supplies, by agitator 3 flotation reagent and the sewage that drops into is mixed, under water pump 20 effects, the sewage that is mixed with flotation agent is entered in it through the import 19 that filter screen 20 is pumped into electrolytic treater 22, behind first treatment chamber 11 electrolytic floatages, dirt enters ash pit 10 with foam after slag-drip opening 18 is discharged, and remaining water enters precision processing chamber 12 continuation electrolytic floatages again, clear water flows out from exporting 14, thereby finishes sewage disposal.
Claims (3)
1. device that utilizes sun power electrolysis floatation purification sewage, comprise the solar energy electric supplier that constitutes by solar-energy photo-voltaic cell group, charging-discharging controller, invertor, potentiostat, battery, establish the sewage agitated pool of agitator in it, establish negative electrode and positive plate in it, establish the electrolytic treater of import and outlet on it, and the sewage agitated pool by transfer lime and on water pump link to each other with electrolytic treater, it is characterized in that agitator, water pump, negative electrode and positive plate are all by lead and solar energy electric supplier electrical coupling.
2. the device that utilizes sun power electrolysis floatation purification sewage according to claim 1, the drive-motor that it is characterized in that described agitator and water pump links to each other with invertor by lead, invertor links to each other with charging-discharging controller by lead, and charging-discharging controller links to each other with the solar-energy photo-voltaic cell group by lead.
3. the device that utilizes sun power electrolysis floatation purification sewage according to claim 1, it is characterized in that described negative electrode all links to each other with potentiostat by lead with positive plate, potentiostat links to each other with charging-discharging controller by lead, and charging-discharging controller links to each other with the solar-energy photo-voltaic cell group by lead.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2009202538988U CN201634490U (en) | 2009-12-14 | 2009-12-14 | Sewage purification device using solar electro-flotation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2009202538988U CN201634490U (en) | 2009-12-14 | 2009-12-14 | Sewage purification device using solar electro-flotation |
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CN201634490U true CN201634490U (en) | 2010-11-17 |
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CN2009202538988U Expired - Fee Related CN201634490U (en) | 2009-12-14 | 2009-12-14 | Sewage purification device using solar electro-flotation |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102583660A (en) * | 2012-01-19 | 2012-07-18 | 华东理工大学 | Electrolytic process for wastewater treatment by solar photovoltaic generation energy |
CN105858825A (en) * | 2016-04-12 | 2016-08-17 | 武汉大学 | Photovoltaic array direct coupling technology-based air floatation apparatus |
CN106698605A (en) * | 2017-02-16 | 2017-05-24 | 云南中绿文德生态环保科技股份有限公司 | Process and equipment for electrochemical treatment of chloramphenicol in sewage |
-
2009
- 2009-12-14 CN CN2009202538988U patent/CN201634490U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102583660A (en) * | 2012-01-19 | 2012-07-18 | 华东理工大学 | Electrolytic process for wastewater treatment by solar photovoltaic generation energy |
CN105858825A (en) * | 2016-04-12 | 2016-08-17 | 武汉大学 | Photovoltaic array direct coupling technology-based air floatation apparatus |
CN106698605A (en) * | 2017-02-16 | 2017-05-24 | 云南中绿文德生态环保科技股份有限公司 | Process and equipment for electrochemical treatment of chloramphenicol in sewage |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101117 Termination date: 20131214 |