CN109607700A - A kind of conductive plastics electrode of electrolytic sewage slot - Google Patents
A kind of conductive plastics electrode of electrolytic sewage slot Download PDFInfo
- Publication number
- CN109607700A CN109607700A CN201910038613.7A CN201910038613A CN109607700A CN 109607700 A CN109607700 A CN 109607700A CN 201910038613 A CN201910038613 A CN 201910038613A CN 109607700 A CN109607700 A CN 109607700A
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- cover
- conductive plastics
- sewage
- electrode
- cathode
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- 239000010865 sewage Substances 0.000 title claims abstract description 29
- 239000004033 plastic Substances 0.000 title claims abstract description 24
- 229920003023 plastic Polymers 0.000 title claims abstract description 24
- 238000009413 insulation Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 29
- 238000000034 method Methods 0.000 abstract description 13
- 239000000126 substance Substances 0.000 abstract description 8
- 230000008569 process Effects 0.000 abstract description 7
- 239000005416 organic matter Substances 0.000 abstract description 3
- 238000006864 oxidative decomposition reaction Methods 0.000 abstract description 3
- 230000001590 oxidative effect Effects 0.000 abstract description 3
- 125000004430 oxygen atom Chemical group O* 0.000 abstract description 3
- 230000009471 action Effects 0.000 abstract description 2
- 230000000737 periodic effect Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 9
- 239000007788 liquid Substances 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 4
- 230000016615 flocculation Effects 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000004411 aluminium Substances 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 235000006708 antioxidants Nutrition 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000005518 electrochemistry Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 1
- YBGKQGSCGDNZIB-UHFFFAOYSA-N arsenic pentafluoride Chemical class F[As](F)(F)(F)F YBGKQGSCGDNZIB-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011538 cleaning material Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 238000012828 global research and development Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 1
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920001197 polyacetylene Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000001131 transforming effect Effects 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
A kind of conductive plastics electrode of electrolytic sewage slot, axial arranged in parallel with several truncated cone-shaped covers edges made of conductive plastics, centre is passed through to be fixed with shaft；Cover distinguishes positive pole, cathode；The active oxygen atom O that strong oxidizing property is generated after energization occurs oxidative decomposition with the organic matter in sewage, is decomposed into CO2And H2O.And periodic arrangement structure, so that carrying out electrochemical action process iterative cycles, organic substance is constantly removed in raw water, and purifying rate is high, achievees the purpose that purifying water body.Cover can be rotated with shaft.By quickly left-right rotation repeatedly, the shear flow of strong turbulence is formed, high speed souring can be caused to cover, it is very convenient to remove siltation.
Description
Technical field
The present invention relates to one kind to be aoxidized and be sterilized to sewage by electrochemistry, and water body is clarified, and improves sewage treatment effect
The conductive plastics electrode of the electrolytic sewage slot of fruit, belongs to electrolytic sewage process field.
Background technique
In recent years, China's rapid economic development, urban wastewater discharge continue to increase, and Urban Water Environment is by serious dirt
Dye, effluent problem has been China one severe environmental protection and economic problems.Due to cost of sewage disposal height, financial input is difficult
Think after so that wastewater treatment in China rate is very low, the cost and treatment effeciency of sewage treatment greatly restrict sewage treatment industry
Development.Therefore, research and development cost is low, and speed is fast, high-efficient sewage treatment technique, new equipment are sewage treatment industry
Developing direction.
Electrolytic treatment method of wastewater be exactly in electrolytic cell device pole plate be powered, make in waste water harmful substance in yin, yang two
Oxidation and reduction reaction, the method for transforming into innocuous substance to realize purification of waste water occurs on extremely respectively.
In a variety of metal materials that can be used as electrode, the price of aluminium and iron due to its good dissolubility and relative moderate
Most frequently it is chosen as electrolytic bath electrode plate.When industrial wastewater contains plurality of heavy metal pollutant, soda acid pollutant etc., iron is mostly used to make
Electrode；And for polluting relatively light sanitary sewage, then mostly use metallic aluminium to make electrode.This is because aluminium electrode water outlet is steady
Fixed, cleaning, is able to satisfy higher process demand.Electrolytic cell requires to take appropriate spacing between two-plate, to guarantee that power consumption is less
And it is easily installed, runs and repairs.
This water treating method includes that electrochemical action, indirect oxidation and the indirect reduction effect on electrode surface (utilize electricity
Substance chemically reacts in the chemical product and water that pole-liquid interface generates), electric flotation acts on (using producing in electrolytic process
Raw small O2、H2The floating of bubble), electric flocculation effect (since the ion that iron or aluminum metal anode dissolve further hydrolyzes,
The metal hydroxides activity coagulant not soluble in water as ferrous hydroxide or aluminium hydroxide etc..This substance is solidifying in porosity
Plastic structure has surface charge effect and stronger suction-operated, and it is solidifying to play obvolvent to the organic or inorganic pollutant in waste water
Poly- effect, makes pollutant agglomerate and separate from waste water) etc..
The advantages of electrolysis method processing, is: using low-voltage dc power supply, not expending a large amount of chemical agents, grasps at normal temperatures and pressures
Make, management is easy；If Pollutants in Wastewater concentration changes, it can guarantee water outlet by adjusting the method for voltage and current
Water stabilization；Processing unit occupied area is small.The disadvantage is that: power consumption when handling a large amount of waste water, its dissolubility anode consumption is larger,
The anode particle of dissolution forms flocculant as epipole, precipitates suspended solids in sewage, and a large amount of cotton-shaped suspended matters are attached to
On electrode plate, cause water flow low, and can be attached to it is more and more on electrode plate, cause flocculation plant between electrode plate therefore
Barrier, voltage of electric field is high, frequently alarms, and integral device is caused to deactivate.In order to solve this problem, people's some has been selected anti-oxidant
The strong titanium mesh of property, this increases equipment price and cost of sewage disposal again.
Black square professor carries out p-type doping to polyacetylene in the arsenic pentafluorides of discovery for the first time in 1977 and iodine and obtains 10 S/m's
After conductivity, conductive plastics has entered global research and development period, and various conductive plastics come into being.Conduction modeling
Material has the characteristics that lightweight, high intensity, anticorrosive, high temperature resistant, at low cost, easy processing, and application field is extensive, in electric conductivity
The advantage that energy, cost etc. have aluminum alloy materials irreplaceable.
Summary of the invention
It is consumed greatly to solve dissolubility anode, timing is needed to replace, and operating cost is high and largely cotton-shaped suspended matter adheres to
On electrode plate, cause water flow is low, between the electrode plate that takes place frequently the defects of flocculation plant failure, the present invention utilizes structural conductive
Plastics do electrolytic bath electrode plate.Conductive plastics is compared with conventional conducting materials, and more lightly, not similar shape can be made in easily molded processing
Shape, corrosion-resistant, not with acid and alkali reaction, oxidation resistance is strong, durable, waterproof, and resistance is easy to adjust, at low cost, and electrolytic process is only
There is CO2And H2O and without new derivative, belong to green cleaning material, so that the attachment of cotton-shaped suspended matter, product will not be generated on the electrode
It is poly-, clogging.
The technical solution adopted by the present invention to solve the technical problems:
A kind of conductive plastics electrode of electrolytic sewage slot, it is characterized in that: several shapes made of conductive plastics are identical, structure phase
The truncated cone-shaped cover edge same, cover is hollow is axial arranged in parallel, and centre, which is passed through, to be connected and fixed with hollow axle；Cover quantity is many
In 2, a cover connects positive pole, another cover connects power cathode；When cover quantity be greater than 4 when, cover or
Alternately connection positive pole, cathode；Or a cover connects power cathode, remaining cover connects positive pole；Between anode and cathode,
1~6 mutually indepedent, insulation cover can be pressed from both sides；Adjacent cover is at regular intervals.
The invention has the advantages that this conductive plastics electrode is easily molded, corrosion-resistant, anti-oxidant, at low cost, electrolytic process
Only CO2And H2O and without new derivative, no cotton-shaped suspended matter attachment accumulation, no blocking, removing product becomes silted up convenient, solves traditional electricity
It is big to solve the consumption of slot dissolubility anode, timing is needed to replace, operating cost is high and a large amount of cotton-shaped suspended matter adhesive electrodes, causes electrode
Flocculation plant failure between plate, the defect for causing integral device deactivated；Electrode connection is simple, and operational safety, power consumption is low, and energy conservation is high
Effect.
Detailed description of the invention
Present invention will be further explained below with reference to the attached drawings and examples.
Fig. 1 is the axial sectional view that the present invention applies in vertical-flow electrolytic cell.
Fig. 2 is the perspective view of the present invention of 6 layers of conductive plastics truncated cone-shaped cover structure.
Fig. 3 is the axial sectional view of the present invention of 6 layers of conductive plastics truncated cone-shaped cover structure.
Fig. 4 is the perspective view of the present invention of 1 layer of conductive plastics truncated cone-shaped cover structure.
Fig. 5 is independent conductive plastics truncated cone-shaped cover perspective view.
Fig. 6 is independent conductive plastics truncated cone-shaped cover axial sectional view.
Fig. 7 is the axial sectional view that the present invention applies in round Advection-type electric tank.
Fig. 8 is the F-F sectional view of Fig. 7.
In figure:
1. 4. reflecting plate of pond body 2. sewage, 3. center water inlet pipe, 5. apopore
6. 7. effluent trough 8. of effluent weir, which precipitates dirt 9., stores mud groove
10. 11. 12. shaft of conductive plastics truncated cone-shaped cover of sludge pipe, 13. grid
14. the fan-shaped cover of 15. wheel hub of conducting plastic substrate 16.
Specific embodiment
In the embodiment shown in fig. 1, of the invention (11) cover center sewage water inlet pipe (3) outside, supported by bracket.One pole
Plate connects positive pole, another pole plate connects power cathode, and circuit is powered by the collector ring of hollow axle (12).It is opened on cover
There are grid (13).Sewage (2) is entered in slot (1) from top to bottom by the water inlet pipe (3) for being located at electrolytic cell (1) center, manages lower umbrella shape
Baffle (4) spreads waste water horizontal homogeneous.It is limited by cover (11) space, raw water is assembled under cover, and grid on cover is passed through
(13) along the flowing axially upwards of shaft (12).Slot bottom has storage mud groove (9).
On electrode (11) solid-liquid boundary, electrolysis generates the active oxygen atom O of strong oxidizing property, or connects with the bacterium in sewage
Touching eliminates the bacterium in sewage, or oxidative decomposition occurs with the organic matter in sewage, is decomposed into CO2And H2O.To reach
The purpose of purifying water body.
Conductive plastics truncated cone-shaped cover (11) structure of multilayer periodic arrangement, makes the borderline electrochemistry of electrode (11) solid-liquid
Effect, redox reaction (substance chemically reacts in the chemical product and water generated using electrode-liquid interface) process
Iterative cycles carry out, and suspended material is constantly removed in raw water, and purifying rate is high.
In the embodiment shown in fig. 7, the present invention is placed on round electrolytic cell (1) center, conductive plastics truncated cone-shaped cover
(11) small angle inclination is presented.Cover (11) without grid, without through-hole.1 cover (11) connects power cathode, remaining connection power supply
Anode, circuit are powered by the collector ring of hollow axle (12).Water inlet (3) and water outlet (5) are diametrically.From radial water inlet
The sewage (2) that mouth (3) flows into, is limited by the round table-like arc cover (11) of overlapping arrangement, is further separated into the gap between arc cover (11)
Space, the gap between arc cover (11) constitute the very long shallow-layer electrolytic cell of length one by one.When the big suspended matter of upward component velocity,
Colloidal solid will move upwards, then limited by the lower surface of upper one layer of arc cover for tilting down extension, can only be along rotary table wall surface
(11) it moves.And the viscosity on solid-liquid boundary is maximum, will exhaust energy soon and sink.The suspension big to two sides component velocity
Object, colloidal solid are also bent downward two sides arc plate (11) and are limited, stopped before solid-liquid boundary.The speed that travels forward is big
Suspended matter, colloidal solid round table-like arc plate that extension is also tilted down by next layer upper surface limited.Solid-liquid frontier district
Domain is the main region of precipitating aggregation.On electrode (11) solid-liquid boundary, electrolysis generates the active oxygen atom O of strong oxidizing property, or
It is contacted with the bacterium in sewage, eliminates the bacterium in sewage, or oxidative decomposition occurs with the organic matter in sewage, be decomposed into
CO2And H2O, to achieve the purpose that purifying water body.Purified water body radial inflow water outlet (5) output.
The free of non-organic species such as sandstone, mud in sewage are sunk to the bottom quickly in long shallow layer precipitating pond, form mud, only
It needs rotating shaft (12), the mud (8) on cover (11) is got rid of down under the influence of centrifugal force.
By quick rotation shaft (12), the shear flow of strong turbulence is formed, high speed can be caused to wash away to cover (11)
Effect, remove it is possible siltation, block it is very convenient.Absorption, accumulation, clogging will not be generated on cover (11).
Claims (1)
1. a kind of conductive plastics electrode of electrolytic sewage slot, it is characterized in that: several shapes made of conductive plastics are identical, structure
The truncated cone-shaped cover edge identical, cover is hollow is axial arranged in parallel, and centre, which is passed through, to be connected and fixed with hollow axle；Cover quantity is not
Less than 2, a cover connects positive pole, another cover connects power cathode；When cover quantity be greater than 4 when, cover or
Person alternately connects positive pole, cathode；Or a cover connects power cathode, remaining cover connects positive pole；Anode and cathode it
Between, 1~6 mutually indepedent, insulation cover can be pressed from both sides；Adjacent cover is at regular intervals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910038613.7A CN109607700A (en) | 2019-01-16 | 2019-01-16 | A kind of conductive plastics electrode of electrolytic sewage slot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910038613.7A CN109607700A (en) | 2019-01-16 | 2019-01-16 | A kind of conductive plastics electrode of electrolytic sewage slot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109607700A true CN109607700A (en) | 2019-04-12 |
Family
ID=66019771
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910038613.7A Pending CN109607700A (en) | 2019-01-16 | 2019-01-16 | A kind of conductive plastics electrode of electrolytic sewage slot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109607700A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114195227A (en) * | 2021-11-12 | 2022-03-18 | 中国五环工程有限公司 | Plastic substrate three-dimensional particle electrode and preparation method thereof |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1161477A1 (en) * | 1983-03-11 | 1985-06-15 | Всесоюзный Проектно-Технологический Институт По Электробытовым Машинам И Приборам | Electrolyzer for processing waste water sediment |
| JPH06249999A (en) * | 1993-02-24 | 1994-09-09 | Nishiyama Stainless Chem Kk | Method and apparatus for removing radioactive contamination |
| JP2005334760A (en) * | 2004-05-26 | 2005-12-08 | Kobe Steel Ltd | Apparatus and method for treating water |
| JP2006213972A (en) * | 2005-02-04 | 2006-08-17 | Central Res Inst Of Electric Power Ind | Scraping blade in precipitate scraping type electrolyzer |
| CN2828014Y (en) * | 2005-09-07 | 2006-10-18 | 冯庆中 | Electrochemical reactor |
| CN105734616A (en) * | 2016-03-11 | 2016-07-06 | 国联汽车动力电池研究院有限责任公司 | Electrolysis device used for in-situ electricity reduction |
| US20170336350A1 (en) * | 2016-05-23 | 2017-11-23 | Hong Kong Applied Science and Technology Research Institute Company Limited | Static Disk Electrode for Electroplating Bath Analysis |
| CN108545810A (en) * | 2018-04-25 | 2018-09-18 | 武汉大学 | The electrolytic processing apparatus and method of big flow open type recirculated cooling water |
| CN209721666U (en) * | 2019-01-16 | 2019-12-03 | 韦志锋 | A kind of conductive plastics electrode of electrolytic sewage slot |
-
2019
- 2019-01-16 CN CN201910038613.7A patent/CN109607700A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1161477A1 (en) * | 1983-03-11 | 1985-06-15 | Всесоюзный Проектно-Технологический Институт По Электробытовым Машинам И Приборам | Electrolyzer for processing waste water sediment |
| JPH06249999A (en) * | 1993-02-24 | 1994-09-09 | Nishiyama Stainless Chem Kk | Method and apparatus for removing radioactive contamination |
| JP2005334760A (en) * | 2004-05-26 | 2005-12-08 | Kobe Steel Ltd | Apparatus and method for treating water |
| JP2006213972A (en) * | 2005-02-04 | 2006-08-17 | Central Res Inst Of Electric Power Ind | Scraping blade in precipitate scraping type electrolyzer |
| CN2828014Y (en) * | 2005-09-07 | 2006-10-18 | 冯庆中 | Electrochemical reactor |
| CN105734616A (en) * | 2016-03-11 | 2016-07-06 | 国联汽车动力电池研究院有限责任公司 | Electrolysis device used for in-situ electricity reduction |
| US20170336350A1 (en) * | 2016-05-23 | 2017-11-23 | Hong Kong Applied Science and Technology Research Institute Company Limited | Static Disk Electrode for Electroplating Bath Analysis |
| CN108545810A (en) * | 2018-04-25 | 2018-09-18 | 武汉大学 | The electrolytic processing apparatus and method of big flow open type recirculated cooling water |
| CN209721666U (en) * | 2019-01-16 | 2019-12-03 | 韦志锋 | A kind of conductive plastics electrode of electrolytic sewage slot |
Non-Patent Citations (1)
| Title |
|---|
| 周军等: "电解法处理废水的研究进展" * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114195227A (en) * | 2021-11-12 | 2022-03-18 | 中国五环工程有限公司 | Plastic substrate three-dimensional particle electrode and preparation method thereof |
| CN114195227B (en) * | 2021-11-12 | 2024-02-02 | 中国五环工程有限公司 | Plastic substrate three-dimensional particle electrode and preparation method thereof |
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Application publication date: 20190412 |