CN108751337A - A kind of photo catalysis reactor - Google Patents
A kind of photo catalysis reactor Download PDFInfo
- Publication number
- CN108751337A CN108751337A CN201810583619.8A CN201810583619A CN108751337A CN 108751337 A CN108751337 A CN 108751337A CN 201810583619 A CN201810583619 A CN 201810583619A CN 108751337 A CN108751337 A CN 108751337A
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- pond
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- plate
- photo catalysis
- catalysis reactor
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- 238000007146 photocatalysis Methods 0.000 title claims abstract description 15
- 230000001699 photocatalysis Effects 0.000 title claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 238000007664 blowing Methods 0.000 claims abstract description 19
- 238000006555 catalytic reaction Methods 0.000 claims description 12
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 2
- 239000002351 wastewater Substances 0.000 abstract description 23
- 238000000034 method Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 9
- 241000894006 Bacteria Species 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 6
- 239000010842 industrial wastewater Substances 0.000 abstract description 4
- 231100000567 intoxicating Toxicity 0.000 abstract description 4
- 230000002673 intoxicating effect Effects 0.000 abstract description 4
- 238000012797 qualification Methods 0.000 abstract description 4
- 239000010865 sewage Substances 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 3
- 239000001301 oxygen Substances 0.000 abstract description 3
- 229910052760 oxygen Inorganic materials 0.000 abstract description 3
- 229910000831 Steel Inorganic materials 0.000 abstract description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 2
- 230000004913 activation Effects 0.000 abstract description 2
- 238000013019 agitation Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000010959 steel Substances 0.000 abstract description 2
- 239000011701 zinc Substances 0.000 abstract description 2
- 229910052725 zinc Inorganic materials 0.000 abstract description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- -1 albumen Matter Substances 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000002772 monosaccharides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
Landscapes
- 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)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Water Treatments (AREA)
- Catalysts (AREA)
Abstract
The invention belongs to sewage treatment equipment fields, and in particular to a kind of photo catalysis reactor.After water is sent by intake pump by the present invention first,So that waste water is passed through staggeredly plate and carries out straggly flow down,Pass through dirty process straggly,It realizes and comes into full contact with waste water and air,And it realizes and primary activation is carried out to water quality,After entering electrical pond,Pass through the effect of electrolytic zinc-coated steel sheet,Water is decomposed,The present invention is provided with current detector,Blowing sprayer,By limiting the difference to plate,After making jet,Waste water can carry out adequately mixing agitation,And it is fully contacted with oxygen,Bacterium in waste water can effectively kill using the effect of ultraviolet light and removed,To solve current industrial wastewater since BOD/COD values are low,Biochemical treatment thus can not be carried out,Or biochemical waste water index is unstable,There is part can not biochemical composition,Bacterium intoxicating phenomenon frequent occurrence simultaneously,Keep the water qualification rate after biochemistry low,It is difficult to problem up to standard.
Description
Technical field
The invention belongs to sewage treatment equipment fields, and in particular to a kind of photo catalysis reactor.
Background technology
Wastewater biological method of chemical treatment is the metabolism using microorganism referred to as " wastewater biochemical method ", make be in waste water
The organic pollution of dissolving and colloidal state is converted into innocuous substance, the method to realize purification.Aerobe processing can be divided into
Method and Anaerobic biotreatment method, the former main active sludge, biofilm, oxidation pond process, sewage irrigation etc..Anaerobic waste water
Biological treatment is also known as " anaerobic digestion ", is to make purification of waste water using anaerobe with the organic pollution in degrading waste water
Method.Its mechanism is to decompose the organic matter in sludge under the action of anaerobic bacteria, finally generates methane and carbon dioxide
Equal gases.Complete anaerobic digestion process can divide three phases：1. the solid-state organic compound in sludge from anaerobic bacteria by means of dividing
It secretes the extracellular hydrolase to be dissolved, and cell is entered by cell wall, under the catalysis of hydrolase, by polysaccharide, albumen
Matter, fat are hydrolyzed to monosaccharide, amino acid, aliphatic acid etc. respectively；2. under the action of acid-producing bacteria, by the product of first stage into one
Step is degraded to better simply volatile organic acids, such as acetic acid, propionic acid, butyric acid；3. under the action of methane backeria, by second stage
The volatile acid of generation is converted to methane and carbon dioxide.Influence factor has temperature, pH value, nutriment, organic poison, anaerobic environment
Deng.The advantages of anaerobic bio-treated：The removal rate of the little energy of processing procedure consumption, organic matter is high, and the sludge of precipitation is few and easy
Dehydration, can kill pathogen, be not required to add the nutriments such as nitrogen, phosphorus.But anaerobic bacteria breeding is slower, and it is sensitive to poisonous substance, to ring
Border condition requires strictly, and it is still necessary to aerobe processing for final product.In recent years, it is commonly applied to the processing of high concentrated organic wastewater.
The target of wastewater treatment is to take into account treatment effect, treatment effeciency and operation processing cost, biochemical treatment process for wastewater
It is easy with management, the advantages of operating cost is cheap, non-secondary pollution, sewage disposal occasion is applied to by wide hair, it is still, many
Industrial wastewater can not carry out biochemical treatment since BOD/COD values are low, or biochemical waste water index is unstable, has part not
Biochemical ingredient, while bacterium intoxicating phenomenon frequent occurrence keep the water qualification rate after biochemistry low, it is difficult to up to standard.
Invention content
The technical problems to be solved by the invention：For current industrial wastewater since BOD/COD values are low, thus can not carry out
Biochemical treatment, or biochemical waste water index are unstable, have part can not biochemical composition, while bacterium intoxicating phenomenon frequent occurrence makes
Water qualification rate after biochemistry is low, it is difficult to which problem up to standard, the present invention provides a kind of photo catalysis reactors.
In order to solve the above technical problems, the present invention is using technical solution as described below：
A kind of photo catalysis reactor, including intake pump, water inlet pipe, the intake pump are connected with water inlet pipe, water inlet pipe
The other end is connected with running water pond, and the running water pond is internally provided with staggeredly plate, and basin bottom living is equipped with power supply, the running water bottom of pond
End is equipped with water outlet, blows the mouth of a river and is connected with electrical pond, and the electrical pond is internally provided with electrode plate, and electrical bottom of pond portion is equipped with electric current
The top of detector, blowing sprayer, the electrical pond is filter screen, and the electrical pond side farthest apart from running water pond connects purple
Outer fluorescent tube, the electrical pond top connection catalysis pond, is catalyzed inside pond and contains catalysing material, the catalysis bottom of pond portion connects gas transmission
Pipe, appendix are connected with air jet pipe, and appendix is supplied gas by air pump, and the catalysis pond side connects outlet pipe, water outlet
Pipe connects water outlet pump.
The staggeredly arrangement of the plate in running water pond is left and right staggered discharge or right left staggered discharge successively from top to bottom.Institute
To state staggeredly plate, in arrangement, the staggeredly plate of top is located at the 10~15cm of lower section on the minimum top in running water pond, and staggeredly plate
Length is 2/3rds of running water pond width.
Between electrode plate, blowing sprayer is connect with appendix 18 for the current detector, blowing sprayer.
The current detector is detected electrical pond, when detected value is less than the value for being set in current detector 10,
Blowing sprayer is opened, and jet is carried out, and blowing sprayer is closed when numerical value reaches.
It is uniformly provided with limit on the air jet pipe to piece, limits to being equipped with Yan Gai below piece, Yan Gai and limits to be equipped between piece and opens
Mouthful, so as to outlet.
The air jet pipe is uniformly arranged, and the direction of the limit on two neighboring air jet pipe to piece is opposite.
The catalysing material is TiO2。
Compared with other methods, advantageous effects are the present invention：
After water is sent by intake pump by the present invention first, so that waste water is passed through, staggeredly plate progress is straggly flows down, by straggly
Dirty process, realizes and comes into full contact with waste water and air, and realizes and carry out primary activation to water quality, is entering electrical pond
Afterwards, by the effect of electrolytic zinc-coated steel sheet, water is decomposed, forms the bubbles such as a large amount of oxygen, hydrogen, simultaneously because entering in waste water
The gas in partial air is dissolved in the process, the bubble of generation is allow preferably to be contacted with the impurity in waste water, is improved
Surface loading amount increases effect of mass transmitting in solution, and the present invention is provided with current detector, blowing sprayer, passes through electric current
The detection of detector reduces the problem of impurity such as suspended matter block pole plate, improves wastewater treatment using the purging of blowing sprayer
Efficiency, by being contacted with titanium dioxide, using the effect of ultraviolet light, improves titanium dioxide after waste water enters catalysis pond
The catalytic efficiency of titanium increases the decomposition to the pollutant in water, while being additionally provided with air jet pipe, by limiting the difference to plate, makes
After jet, waste water can carry out adequately mixing agitation, and fully be contacted with oxygen, and treatment effect is further increased,
Simultaneously bacterium in waste water can be carried out effectively to kill and remove using the effect of ultraviolet light, to solve current industrial wastewater due to
BOD/COD values are low, thus can not carry out biochemical treatment, or biochemical waste water index is unstable, have part can not biochemical composition, together
When bacterium intoxicating phenomenon frequent occurrence, keep the water qualification rate after biochemistry low, it is difficult to problem up to standard.
Description of the drawings
Fig. 1 is the structure chart of the present invention；
Fig. 2 is the structure chart of air jet pipe in the present invention；
Wherein, 1, intake pump；2, water inlet pipe；3, running water pond；4, interlock plate；5, power supply；6, water outlet；7, electrical pond；8,
Electrode plate；9, ultraviolet lamp tube；10, current detector；11, blowing sprayer；12, it is catalyzed pond；13, catalysing material；14, air jet pipe；15,
Outlet pipe；16, water outlet pump；17, air pump；18, appendix；19, Yan Gai；20, it limits to piece.
Specific implementation mode
Below in conjunction with the attached drawing in the present invention, technical solution in the embodiment of the present invention carry out it is clear, completely retouch
It states, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based on the present invention
In embodiment, all other reality that those skilled in the art is obtained without making creative work
Example is applied, protection scope of the present invention is belonged to.
A kind of photo catalysis reactor, including intake pump 1, water inlet pipe 2, the intake pump 1 are connected with water inlet pipe 2, water inlet
The other end of pipe is connected with running water pond 3, and the running water pond 3 is internally provided with staggeredly plate 4, and basin bottom living is equipped with power supply 5, described
3 bottom end of running water pond is equipped with water outlet 6, blows the mouth of a river and is connected with electrical pond 7, the electrical pond 7 is internally provided with electrode plate 8, electrically
Bottom of pond portion is equipped with current detector 10, blowing sprayer 11, and the top in the electrical pond 7 is filter screen, and most apart from running water pond 3
Remote electrical pond side connects ultraviolet lamp tube 9, and catalysis pond 12 is connected at the top of the electrical pond, is catalyzed inside pond and contains catalysing material
13, the 12 bottom connecting gas transmission pipe 18 of catalysis pond, appendix is connected with air jet pipe 14, and appendix is sent by air pump 17
Gas, 12 side of catalysis pond connect outlet pipe 15, and outlet pipe connects water outlet pump 16.The staggeredly arrangement of the plate 4 in running water pond 3
It is left and right staggered discharge or right left staggered discharge successively from top to bottom.The staggeredly plate 4 is in arrangement, the staggeredly plate of top
4 are located at the 10~15cm of lower section on 3 minimum top of running water pond, and staggeredly the length of plate is 2/3rds of 3 width of running water pond.Institute
Current detector 10, blowing sprayer 11 are stated between electrode plate 8, blowing sprayer is connect with appendix 18.The current detecting
Device 10 is detected electrical pond 7, and when detected value is less than the value for being set in current detector 10, blowing sprayer 11 is opened, into
Row jet, blowing sprayer is closed when numerical value reaches.It is uniformly provided with limit on the air jet pipe 14 to piece 20, limits and is equipped with to piece lower section
Prolong lid 19, Yan Gai and limit and be equipped with opening between piece, so as to outlet.The air jet pipe 14 is uniformly arranged, two neighboring air jet pipe
On direction from limit to piece 20 it is opposite.The catalysing material 13 is TiO2.The present invention has been done into one by specific embodiment above
Step description, it should be understood that, specific description, should not be construed as the restriction to the spirit and scope of the invention here,
The various modifications that one of ordinary skilled in the art after reading this specification makes above-described embodiment, belong to the present invention
The range protected.
Claims (8)
1. a kind of photo catalysis reactor, including intake pump (1), water inlet pipe (2), which is characterized in that the intake pump (1) and water inlet
Pipe (2) is connected, and the other end of water inlet pipe is connected with running water pond (3), and the running water pond (3) is internally provided with staggeredly plate (4), living
Basin bottom is equipped with power supply (5), and running water pond (3) bottom end is equipped with water outlet (6), blows the mouth of a river and be connected with electrical pond (7), institute
It states electrical pond (7) and is internally provided with electrode plate (8), electrical bottom of pond portion is equipped with current detector (10), blowing sprayer (11), the electricity
The top in gas pond (7) is filter screen, and the electrical pond side farthest apart from running water pond (3) connects ultraviolet lamp tube (9), the electricity
Connection catalysis pond (12) at the top of gas pond, catalysis contain catalysing material (13), catalysis pond (12) bottom connecting gas transmission pipe inside pond
(18), appendix is connected with air jet pipe (14), and appendix is supplied gas by air pump (17), and catalysis pond (12) side connects
Connected water outlet pipe (15), outlet pipe connect water outlet pump (16).
2. photo catalysis reactor according to claim 1, which is characterized in that the staggeredly arrangement of the plate (4) in running water pond (3)
It is left and right staggered discharge or right left staggered discharge successively from top to bottom.
3. photo catalysis reactor according to claim 1 or claim 2, which is characterized in that the staggeredly plate (4) is most pushed up in arrangement
The staggeredly plate (4) at end is located at the 10~15cm of lower section on running water pond (3) minimum top, and staggeredly the length of plate is running water pond (3)
2/3rds of width.
4. photo catalysis reactor according to claim 1, which is characterized in that the current detector (10), blowing sprayer
(11) between electrode plate (8), blowing sprayer is connect with appendix (18).
5. according to the photo catalysis reactor of claim 1 or 4, which is characterized in that the current detector (10) is to electrical pond
(7) it is detected, when detected value is less than the value for being set in current detector (10), blowing sprayer (11) is opened, and jet is carried out,
Blowing sprayer is closed when numerical value reaches.
6. photo catalysis reactor according to claim 1, which is characterized in that be uniformly provided with limit on the air jet pipe (14) to piece
(20), it limits to being equipped with Yan Gai (19) below piece, Yan Gai and limits and be equipped with opening between piece, so as to outlet.
7. photo catalysis reactor according to claim 1 or 6, which is characterized in that the air jet pipe (14) is uniformly arranged, adjacent
The direction of limit to piece (20) on two air jet pipes is opposite.
8. photo catalysis reactor according to claim 1, which is characterized in that the catalysing material (13) is TiO2。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810583619.8A CN108751337A (en) | 2018-06-08 | 2018-06-08 | A kind of photo catalysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810583619.8A CN108751337A (en) | 2018-06-08 | 2018-06-08 | A kind of photo catalysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108751337A true CN108751337A (en) | 2018-11-06 |
Family
ID=64000454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810583619.8A Pending CN108751337A (en) | 2018-06-08 | 2018-06-08 | A kind of photo catalysis reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108751337A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2639291Y (en) * | 2003-05-16 | 2004-09-08 | 詹伯君 | Electrolytical equipment for waste water treatment |
| US20090032460A1 (en) * | 2005-03-04 | 2009-02-05 | Kazuyuki Yamasaki | Wastewater treatment method and wastewater treatment equipment |
| CN105251759A (en) * | 2015-10-16 | 2016-01-20 | 北京德瑞科森环保科技有限公司 | Multi-section type soil in-situ aerating device |
| CN206156855U (en) * | 2016-11-01 | 2017-05-10 | 浙江水利水电学院 | Drop aeration and integrated anti -pollution device of anaerobic treatment |
| CN106946321A (en) * | 2017-03-30 | 2017-07-14 | 榆林学院 | A kind of utilization electrochemical reaction and light-catalyzed reaction handle the device of waste water |
| CN206395867U (en) * | 2017-01-19 | 2017-08-11 | 深圳市尤佳环境科技有限公司 | A kind of purifying device using photo-catalysis |
-
2018
- 2018-06-08 CN CN201810583619.8A patent/CN108751337A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2639291Y (en) * | 2003-05-16 | 2004-09-08 | 詹伯君 | Electrolytical equipment for waste water treatment |
| US20090032460A1 (en) * | 2005-03-04 | 2009-02-05 | Kazuyuki Yamasaki | Wastewater treatment method and wastewater treatment equipment |
| CN105251759A (en) * | 2015-10-16 | 2016-01-20 | 北京德瑞科森环保科技有限公司 | Multi-section type soil in-situ aerating device |
| CN206156855U (en) * | 2016-11-01 | 2017-05-10 | 浙江水利水电学院 | Drop aeration and integrated anti -pollution device of anaerobic treatment |
| CN206395867U (en) * | 2017-01-19 | 2017-08-11 | 深圳市尤佳环境科技有限公司 | A kind of purifying device using photo-catalysis |
| CN106946321A (en) * | 2017-03-30 | 2017-07-14 | 榆林学院 | A kind of utilization electrochemical reaction and light-catalyzed reaction handle the device of waste water |
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