CN103508597A - EWTS electrochemical sewage treatment method and system - Google Patents
EWTS electrochemical sewage treatment method and system Download PDFInfo
- Publication number
- CN103508597A CN103508597A CN201310412368.4A CN201310412368A CN103508597A CN 103508597 A CN103508597 A CN 103508597A CN 201310412368 A CN201310412368 A CN 201310412368A CN 103508597 A CN103508597 A CN 103508597A
- Authority
- CN
- China
- Prior art keywords
- liquid
- ewts
- alloy electrode
- treatment
- sewage
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 46
- 239000010865 sewage Substances 0.000 title claims abstract description 44
- 239000007788 liquid Substances 0.000 claims abstract description 81
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000000956 alloy Substances 0.000 claims abstract description 38
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 37
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 17
- 230000003647 oxidation Effects 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 14
- 239000011229 interlayer Substances 0.000 claims abstract description 7
- 239000007787 solid Substances 0.000 claims abstract description 7
- 230000005518 electrochemistry Effects 0.000 claims description 26
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 12
- 150000001875 compounds Chemical class 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 9
- 239000002351 wastewater Substances 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 7
- 238000004458 analytical method Methods 0.000 claims description 6
- 150000001491 aromatic compounds Chemical class 0.000 claims description 6
- 229910021419 crystalline silicon Inorganic materials 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 6
- 229910001385 heavy metal Inorganic materials 0.000 claims description 6
- 150000003016 phosphoric acids Chemical class 0.000 claims description 6
- 150000003254 radicals Chemical class 0.000 claims description 6
- 238000006479 redox reaction Methods 0.000 claims description 6
- 229910052717 sulfur Inorganic materials 0.000 claims description 6
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 239000002002 slurry Substances 0.000 abstract 2
- 238000005868 electrolysis reaction Methods 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 230000029219 regulation of pH Effects 0.000 abstract 1
- 239000010802 sludge Substances 0.000 description 6
- 238000010291 electrical method Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000031018 biological processes and functions Effects 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 150000004831 organic oxygen compounds Chemical class 0.000 description 1
- 238000002161 passivation Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Images
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses an EWTS electrochemical sewage treatment method and system. The method comprises the following steps of: (1) storing a liquid to be treated in a raw water tank, and then allowing the liquid to flow from the raw water tank into a pH regulation tank; (2) allowing the liquid to enter an EWTS electrical process device for treatment, wherein the treatment process includes the steps of allowing the liquid to go through an interlayer between a positive alloy electrode plate and a negative alloy electrode plate, and charging the positive/negative alloy electrode plates with a high-frequency current, so that the alloy material molecules of the positive/negative alloy electrode plates are released at the same time into the liquid under the action of the high-frequency current, ionized and non-ionized pollutants in the liquid are adsorbed under the combined action of charges, electrolysis products and metal plate materials and discharged in the form of solid slurry; and (3) introducing the liquid resulting from the treatment with the EWTS electrical process device into an oxidation tank where inorganic and organic matters in the liquid are oxidized. The method provided by the invention has the advantages of low treatment cost, low slurry output, small floor area, high degree of automation and simplicity in management, and the capability of removing different types of pollutants at the same time.
Description
Technical field
The present invention relates to sewage treatment area, relate in particular to a kind of EWTS electrochemistry sewage water treatment method and system.
Background technology
Prior art probably has several method to sewage water treatment method:
The first is biological process, by biological adsorption and the new cellular material of microorganism, synthesize and consume degraded, the method can be gone out COD 60% left and right, and running cost is lower, shortcoming is that floor space is large, invests high, be subject to waste water composition and concentration limit, the residence time is long, manageability not, and processing water can not reuse.
The second is chemical method, adds coagulating agent, reduces the operating range of electric charge and electrostatic double layer, by adsorption bridging, forms large floc sedimentation, COD can be gone out to 70% left and right, and shortcoming is that processing costs is high, and sludge quantity is large, and narrow application range is difficult up to standard.
The third is general chemical oxidization method, by conventional oxygenant decomposing organic matter, can make some organic oxygen compounds decompose, and the residence time is few, and oxygenant consumption is large, and only effective to some hardly degraded organic substance, the scope of application is narrow.
The various defects such as the 4th kind of method is common electrochemical appliance treatment process, and the method electrode easily corrodes, and work-ing life is short, easily produce bubble, reduced electrical method efficiency, the easy fouling of electrode, passivation, clean inconvenient, electrode need to adopt pickling, causes the pollution again to environment, and treatment capacity is little.
In several sewage water treatment methods, all there is weak point separately above.
Therefore, need that a kind of processing cost is low, sludge quantity is few, floor space is little, level of automation is high badly, manageability, can remove EWTS electrochemistry sewage water treatment method and the system of multiple pollutant simultaneously.
Summary of the invention
First object of the present invention is to provide that a kind of processing cost is low, sludge quantity is few, floor space is little, level of automation is high, manageability, can remove the EWTS electrochemistry sewage water treatment method of multiple pollutant simultaneously.
Second object of the present invention is to provide that a kind of processing cost is low, sludge quantity is few, floor space is little, level of automation is high, manageability, can remove the EWTS electrochemistry Sewage treatment systems of multiple pollutant simultaneously.
In order to realize above-mentioned first object, technical scheme provided by the invention is: a kind of EWTS electrochemistry sewage water treatment method is provided, and it comprises, following steps:
(1) pending liquid storage Zhi Yuan pond, then flow into PH equalizing tank by described former pond;
(2) allowing liquid enter EWTS device processes, treating processes is to allow liquid pass through the interlayer between positive and negative alloy electrode plate, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
(3) liquid after processing by EWTS device is imported to oxidation pond, the inorganics in liquid, organism are carried out to oxide treatment.
Liquid through oxide treatment in step (3) is passed through to centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter successively, obtain clear water and import clean water basin.
In described pH value equalizing tank, the pH value of sewage is detected, the PH data that then root detects are carried out PID analysis, then carry out PH proportioning by automatic liquid feeder.
In step (2), the data that described EWTS device can feed back by detection, the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
In step (2), the sewage after processing by EWTS device, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove the Cr6 in waste water
+, Zn2
+, Ni2
+, Cu2
+, Cd2
+heavy metal and CN, oil, phosphoric acid salt and COD, SS.
In step (3), described oxide treatment is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
In order to realize above-mentioned second object, technical scheme provided by the invention is: provide a kind of EWTS electrochemistry Sewage treatment systems it comprise:
Former pond and pH value equalizing tank, pending liquid is stored in described former pond, and liquid flows into described pH value equalizing tank by described former pond and carries out pH value adjusting;
EWTS device, described EWTS device comprises positive and negative alloy electrode, allow liquid pass through the interlayer between described positive and negative alloy electrode, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
Oxidation pond, imports oxidation pond by the liquid after processing by EWTS device, and described oxidation pond carries out oxide treatment by the inorganics in liquid, organism.
Also comprise centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter, the liquid through oxide treatment is passed through to described centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter successively, obtain clear water and import clean water basin.
In described pH value equalizing tank, be provided with the analytical equipment that PH data that proofing unit that the pH value of sewage is detected, root detect are carried out PID analysis, carry out the automatic liquid feeder of PH proportioning.
The data that described EWTS device can feed back by detection, the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
Sewage after processing by EWTS device, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove the Cr6 in waste water
+, Zn2
+, Ni2
+, Cu2
+, Cd2
+heavy metal and CN, oil, phosphoric acid salt and COD, SS.
Oxide treatment in described oxidation pond is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
Compared with prior art, EWTS electrochemistry sewage water treatment method of the present invention and system are that a kind of processing cost is low, sludge quantity is few, floor space is little, level of automation is high, manageability, can remove EWTS electrochemistry sewage water treatment method and the system of multiple pollutant simultaneously.
By following description also by reference to the accompanying drawings, it is more clear that the present invention will become, and these accompanying drawings are used for explaining embodiments of the invention.
Accompanying drawing explanation
Fig. 1 is the system chart of EWTS electrochemistry Sewage treatment systems of the present invention.
Embodiment
With reference now to accompanying drawing, describe embodiments of the invention, in accompanying drawing, similarly element numbers represents similar element.As mentioned above, as shown in Figure 1, provided by the inventionly provide a kind of EWTS electrochemistry sewage water treatment method, it comprises, following steps:
(1) pending liquid storage Zhi Yuan pond 10, then flow into PH equalizing tank 20 by described former pond 10, wherein by liquid Cong Yuan pond 10, entering PH equalizing tank is to inject by water pump 30;
(2) allowing liquid enter EWTS device 40 processes, treating processes is to allow liquid pass through the interlayer between positive and negative alloy electrode plate, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
(3) liquid after processing by EWTS device 40 is imported to oxidation pond 50, the inorganics in liquid, organism are carried out to oxide treatment.
Liquid through oxide treatment in step (3) is passed through to centrifugal settler 60, vertical baffling plate region (not showing on figure), pressure filter 70, medium filter 80, ultra-fine filter 90 successively, obtain clear water and import clean water basin 100.
In described pH value equalizing tank 20, the pH value of sewage is detected, the PH data that then root detects are carried out PID analysis, then carry out PH proportioning by automatic liquid feeder.
In step (2), the data that described EWTS device 40 can feed back by detection, the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
In step (2), sewage after processing by EWTS device 40, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove Cr6+, Zn2+, Ni2+, Cu2+, Cd2+ heavy metal and CN, oil, phosphoric acid salt and COD, SS in waste water.
In step (3), described oxide treatment is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
In order to realize above-mentioned second object, as shown in Figure 1, technical scheme provided by the invention is: provide a kind of EWTS electrochemistry Sewage treatment systems 200 it comprise:
EWTS device 20, described EWTS device 40 comprises positive and negative alloy electrode, allow liquid pass through the interlayer between described positive and negative alloy electrode, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
Also comprise centrifugal settler 60, vertical baffling plate region, pressure filter 70, medium filter 80, ultra-fine filter 90, liquid through oxide treatment is passed through to described centrifugal settler 60, vertical baffling plate region, pressure filter 70, ultra-fine filter 90 successively, obtain clear water and import clean water basin 100.
In described pH value equalizing tank 20, be provided with the analytical equipment that PH data that proofing unit that the pH value of sewage is detected, root detect are carried out PID analysis, carry out the automatic liquid feeder of PH proportioning.
The data that described EWTS device 40 can feed back by detection, the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
Sewage after processing by EWTS device 40, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove Cr6+, Zn2+, Ni2+, Cu2+, Cd2+ heavy metal and CN, oil, phosphoric acid salt and COD, SS in waste water.
Oxide treatment in described oxidation pond 50 is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
The key technical indexes reference when EWTS electrical method sewage water treatment method of the present invention and system treating part industry waste water:
By lower list 1 and table 2, can find out, EWTS method has good effect when processing these industry waste water.
Table 1
Remarks: all test results are all to take mg/l as unit.
Table 2
In conjunction with Fig. 1, table 1 and table 2, EWTS electrochemistry sewage water treatment method of the present invention and system are that a kind of processing cost is low, sludge quantity is few, floor space is little, level of automation is high, manageability, can remove EWTS electrochemistry sewage water treatment method and the system of multiple pollutant simultaneously.Above disclosed is only the preferred embodiments of the present invention, certainly can not limit with this interest field of the present invention, and the equivalent variations of therefore doing according to the present patent application the scope of the claims, still belongs to the scope that the present invention is contained.
Claims (12)
1. an EWTS electrochemistry sewage water treatment method, is characterized in that, comprises following steps:
(1) pending liquid storage Zhi Yuan pond, then flow into PH equalizing tank by described former pond;
(2) allowing liquid enter EWTS device processes, treating processes is to allow liquid pass through the interlayer between positive and negative alloy electrode plate, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
(3) liquid after processing by EWTS device is imported to oxidation pond, the inorganics in liquid, organism are carried out to oxide treatment.
2. EWTS electrochemistry sewage water treatment method as claimed in claim 1, it is characterized in that: the liquid through oxide treatment in step (3) is passed through to centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter successively, obtain clear water and import clean water basin.
3. EWTS electrochemistry sewage water treatment method as claimed in claim 1, is characterized in that: in described pH value equalizing tank, the pH value of sewage is detected, the PH data that then root detects are carried out PID analysis, then carry out PH proportioning by automatic liquid feeder.
4. EWTS electrochemistry sewage water treatment method as claimed in claim 1, it is characterized in that: in step (2), the data that described EWTS device can feed back by detection, the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
5. EWTS electrochemistry sewage water treatment method as claimed in claim 1, it is characterized in that: in step (2), sewage after processing by EWTS device, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove the Cr6 in waste water
+, Zn2
+, Ni2
+, Cu2
+, Cd2
+heavy metal and CN, oil, phosphoric acid salt and COD, SS.
6. EWTS electrochemistry sewage water treatment method as claimed in claim 1, it is characterized in that: in step (3), described oxide treatment is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
7. an EWTS electrochemistry Sewage treatment systems, is characterized in that, comprising:
Former pond and pH value equalizing tank, pending liquid is stored in described former pond, and liquid flows into described pH value equalizing tank by described former pond and carries out pH value adjusting;
EWTS device, described EWTS device comprises positive and negative alloy electrode, allow liquid pass through the interlayer between described positive and negative alloy electrode, and by the logical upper high-frequency current of described positive and negative alloy electrode plate, allow the material molecule of alloy of described positive and negative alloy electrode plate be discharged in liquid under the effect of described high-frequency current simultaneously, ionization in liquid and unionized pollutent are adsorbed the acting in conjunction that is subject to electric charge, electrolysate and metallic sheet material, and discharge with the form of solid mud;
Oxidation pond, imports oxidation pond by the liquid after processing by EWTS device, and described oxidation pond carries out oxide treatment by the inorganics in liquid, organism.
8. EWTS electrochemistry Sewage treatment systems as claimed in claim 7, it is characterized in that, also comprise centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter, liquid through oxide treatment is passed through to described centrifugal settler, vertical baffling plate region, pressure filter, ultra-fine filter successively, obtain clear water and import clean water basin.
9. EWTS electrochemistry Sewage treatment systems as claimed in claim 7, it is characterized in that, in described pH value equalizing tank, be provided with the analytical equipment that PH data that proofing unit that the pH value of sewage is detected, root detect are carried out PID analysis, carry out the automatic liquid feeder of PH proportioning.
10. EWTS electrochemistry Sewage treatment systems as claimed in claim 7, is characterized in that, the data that described EWTS device can feed back by detection, and the alloy electrode of automatic switchover different qualities, to coordinate liquid of different nature to process.
11. EWTS electrochemistry Sewage treatment systemss as claimed in claim 7, it is characterized in that, sewage after processing by EWTS device, the organic and inorganic pollution substance in liquid is carried out to redox reaction, and then cohesion, floating except pollutent is separated from water body, remove the Cr6 in waste water
+, Zn2
+, Ni2
+, Cu2
+, Cd2
+heavy metal and CN, oil, phosphoric acid salt and COD, SS.
12. EWTS electrochemistry Sewage treatment systemss as claimed in claim 7, it is characterized in that, oxide treatment in described oxidation pond is for to carry out oxide treatment by ozone, by the free radical of ozone and pollutent in liquid: C==C, C ≡ C, aromatic compound, heterogeneous ring compound, isocyclic compound ,==N-N ,==S, C ≡ N, C-N, C-Si ,-OH ,-SH ,-NH2, ,-CHO ,-N==N-react.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310412368.4A CN103508597B (en) | 2013-09-09 | 2013-09-09 | electrochemical sewage treatment method and system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310412368.4A CN103508597B (en) | 2013-09-09 | 2013-09-09 | electrochemical sewage treatment method and system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103508597A true CN103508597A (en) | 2014-01-15 |
| CN103508597B CN103508597B (en) | 2017-01-25 |
Family
ID=49892091
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310412368.4A Active CN103508597B (en) | 2013-09-09 | 2013-09-09 | electrochemical sewage treatment method and system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103508597B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104140173A (en) * | 2014-07-18 | 2014-11-12 | 中国海洋石油总公司 | Method for deep processing oil and gas field fracture flowback liquid |
Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1269328A (en) * | 1999-04-06 | 2000-10-11 | 陈弓 | Low-voltage and high-frequency electric field waste water treating technology |
| CN2401539Y (en) * | 1999-11-29 | 2000-10-18 | 韩庆生 | Electronic water processing device |
| US20050000905A1 (en) * | 2002-08-12 | 2005-01-06 | Universal Water Technologies, Llc | Multi-stage photo-catalytic oxidation fluid treatment system |
| CN1586375A (en) * | 2004-09-07 | 2005-03-02 | 顾宗义 | Electrolytic function drinking water machine |
| CN201074201Y (en) * | 2007-06-06 | 2008-06-18 | 张华� | Constant-pressure self-cleaning electrolyzation water making machine |
| CN101302073A (en) * | 2008-06-13 | 2008-11-12 | 吴江市运东邱舍污水处理有限公司 | Advanced treatment process for electroplating sewage |
| CN101376548A (en) * | 2008-09-19 | 2009-03-04 | 袁伟光 | Waste water advanced purifying process and equipment thereof |
| CN101544434A (en) * | 2009-05-04 | 2009-09-30 | 杨高利 | Sewage treatment method and device thereof |
| CN101560040A (en) * | 2009-05-08 | 2009-10-21 | 北京清大国华环保科技有限公司 | Method and device for processing pharmaceutical wastewater by pulse electrocoagulation-MBR |
| CN201777924U (en) * | 2010-06-12 | 2011-03-30 | 骆志尚 | Electrolysis bath for treating garbage filter-pressing liquid via electric flocculation |
| CN102249465A (en) * | 2010-05-20 | 2011-11-23 | 昆山明宽环保节能科技有限公司 | System and process for treating waste water with electrochemical method |
| CN102718351A (en) * | 2012-07-12 | 2012-10-10 | 中国环境科学研究院 | Device and method for sewage desalting |
| US20130118994A1 (en) * | 2011-03-21 | 2013-05-16 | R360 Environmental Solutions | System and Methods for Wastewater and Produced Water Cleaning and Reclamation |
| CN203668156U (en) * | 2013-09-09 | 2014-06-25 | 胡军 | EWTS (electrochemical wastewater treatment system) |
-
2013
- 2013-09-09 CN CN201310412368.4A patent/CN103508597B/en active Active
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1269328A (en) * | 1999-04-06 | 2000-10-11 | 陈弓 | Low-voltage and high-frequency electric field waste water treating technology |
| CN2401539Y (en) * | 1999-11-29 | 2000-10-18 | 韩庆生 | Electronic water processing device |
| US20050000905A1 (en) * | 2002-08-12 | 2005-01-06 | Universal Water Technologies, Llc | Multi-stage photo-catalytic oxidation fluid treatment system |
| CN1586375A (en) * | 2004-09-07 | 2005-03-02 | 顾宗义 | Electrolytic function drinking water machine |
| CN201074201Y (en) * | 2007-06-06 | 2008-06-18 | 张华� | Constant-pressure self-cleaning electrolyzation water making machine |
| CN101302073A (en) * | 2008-06-13 | 2008-11-12 | 吴江市运东邱舍污水处理有限公司 | Advanced treatment process for electroplating sewage |
| CN101376548A (en) * | 2008-09-19 | 2009-03-04 | 袁伟光 | Waste water advanced purifying process and equipment thereof |
| CN101544434A (en) * | 2009-05-04 | 2009-09-30 | 杨高利 | Sewage treatment method and device thereof |
| CN101560040A (en) * | 2009-05-08 | 2009-10-21 | 北京清大国华环保科技有限公司 | Method and device for processing pharmaceutical wastewater by pulse electrocoagulation-MBR |
| CN102249465A (en) * | 2010-05-20 | 2011-11-23 | 昆山明宽环保节能科技有限公司 | System and process for treating waste water with electrochemical method |
| CN201777924U (en) * | 2010-06-12 | 2011-03-30 | 骆志尚 | Electrolysis bath for treating garbage filter-pressing liquid via electric flocculation |
| US20130118994A1 (en) * | 2011-03-21 | 2013-05-16 | R360 Environmental Solutions | System and Methods for Wastewater and Produced Water Cleaning and Reclamation |
| CN102718351A (en) * | 2012-07-12 | 2012-10-10 | 中国环境科学研究院 | Device and method for sewage desalting |
| CN203668156U (en) * | 2013-09-09 | 2014-06-25 | 胡军 | EWTS (electrochemical wastewater treatment system) |
Non-Patent Citations (3)
| Title |
|---|
| 德格雷蒙(E.DEGREMONT)编著，韦荫辉等译: "《水处理手册》", 31 December 1959 * |
| 杨永军等: "用化学组合工艺处理油田含油污水", 《石油化工腐蚀与防护》 * |
| 毕鹏禹等: "电絮凝－O3氧化法处理石化工业污水的研究", 《北京化工大学学报》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104140173A (en) * | 2014-07-18 | 2014-11-12 | 中国海洋石油总公司 | Method for deep processing oil and gas field fracture flowback liquid |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103508597B (en) | 2017-01-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102786182B (en) | Device for processing landfill leachate | |
| CN102276117A (en) | Treatment device and method for garbage percolate | |
| CN1141263C (en) | Method for controlling oil-bearing waste water | |
| CN106219892A (en) | A kind of Powdered Activated Carbon magnetic-coagulation depositing reservoir processes indegradable industrial effluent method and device | |
| CN101781001A (en) | Method for processing effluent by two-stage electrolysis and device thereof | |
| CN105693044A (en) | Treatment system for removing zinc in electroplating wastewater | |
| CN102001776B (en) | Method and device for recycling organic wastewater with high salinity | |
| CN108178423B (en) | Cylindrical spiral electrode biomembrane organic sewage and wastewater reaction device | |
| Radeef et al. | Bioelectrochemical treatment of actual carwash wastewater associated with sustainable energy generation in three-dimensional microbial fuel cell | |
| CN111170587A (en) | Spraying wastewater treatment process | |
| CN105836879B (en) | A kind of the anaerobism conductivity ceramics membrane biological reaction apparatus and method of effective control fouling membrane | |
| CN203668156U (en) | EWTS (electrochemical wastewater treatment system) | |
| CN105152421A (en) | Treatment method of distillation extraction waste liquid in fine chemical engineering production | |
| CN205222941U (en) | Processing system of automobile industry oiliness emulsion waste water | |
| CN204474504U (en) | The treatment unit of brown coal low-temperature pyrolysis waste water | |
| CN103508597A (en) | EWTS electrochemical sewage treatment method and system | |
| CN204550297U (en) | Electrochemistry associating photocatalytic method process organic waste water system | |
| CN103755099B (en) | Multidimensional poleless electro-oxidation wastewater treatment method | |
| CN112374666B (en) | Three-dimensional electrolytic sewage treatment method | |
| CN211946682U (en) | Zero-discharge treatment system for spraying wastewater | |
| CN108751573B (en) | BAME treatment and recycling method for printing and dyeing wastewater | |
| CN113479976A (en) | Integrated wastewater treatment device and application thereof | |
| CN107311360A (en) | The method that catalytic ozonation coupling three-diemsnional electrode handles product oil storage field oil-polluted water | |
| CN112830553A (en) | Synchronous electrocatalytic oxidation-reduction degradation reactor and method for treating membrane filtration concentrate | |
| CN104609673A (en) | Non-antibiotic pharmaceutical wastewater treatment process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190830 Address after: 518000 Building 101, No. 1, No. 2, No. 3, No. 4, Shajingjie Street, Baoan District, Shenzhen City, Guangdong Province Patentee after: Shenzhen Sansheng Environmental Protection Technology Co., Ltd. Address before: 518000 Guangdong city of Shenzhen province Baoan District Xixiang Jin Hua Lu Tianjiao family 1 Building 3 Patentee before: Hu Jun |