CN105417644A - Improved ionized sewage treatment tank - Google Patents
Improved ionized sewage treatment tank Download PDFInfo
- Publication number
- CN105417644A CN105417644A CN201510953783.XA CN201510953783A CN105417644A CN 105417644 A CN105417644 A CN 105417644A CN 201510953783 A CN201510953783 A CN 201510953783A CN 105417644 A CN105417644 A CN 105417644A
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- China
- Prior art keywords
- chamber
- partition wall
- ionization type
- wall
- treatment tank
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Classifications
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- 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
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- 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)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention relates to an improved ionized sewage treatment tank which comprises a tank body, wherein the tank body is internally provided with a partition wall I (11) and a partition wall II (20), the partition wall I (11) and the partition wall II (20) divide the tank body into a trash chamber (1), a decontamination chamber (2) and a water storage chamber (3), the upper end position in the trash chamber (1) is provided with a screen (5), and the outer wall of the upper end of the trash chamber (1) is provided with a water inlet (4); the lower end position of the partition wall I (11) is provided with a communicating port I (12); the middle end position in the decontamination chamber (2) is provided with an ionized oxidation reactor (15), the lower end of the ionized oxidation reactor (15) is provided with a screen II (23), the lower end of the screen II (23) is a settling zone (24), and the inner wall of the top part of the decontamination chamber (2) is provided with a plurality of spinning nozzles (14); the upper end position of the partition wall II (20) is provided with a communicating port II (18); the upper end wall of the water storage chamber (3) is provided with a water outlet (21).
Description
Technical field
The present invention relates to technical field of waste water processing, especially a kind of modified version ionization type treatment tank.
Background technology
Along with the day of water resources is becoming tight, sewage disposal purifies, and recycling has become an important development direction indispensable in socio-economic development, and various sewage disposal device is constantly applied to field of waste water treatment.Industrial sewage is due to of a great variety, complicated component, intractability is larger, usually need large-scale treatment facility, and the existing sewage disposal device of midget plant or family exists, and area is huge, equipment is complicated, the treatment time is long or it is not good to there is treatment effect, the problems such as processing cost is high, effluent quality difference.
The present inventor is based on electrochemistry, take materialogy as a kind of multiduty advanced oxidation reactor technologies of point of penetration research and development, use this reactor technology device can carry out effective Strong oxdiative decomposition to the organic pollutant in the waste water of chemical industry, pharmaceutical industry, simultaneously can carry out effective oxygenolysis to the organic contamination in the percolate of high density, Sewage Plant residue water-containing sludge, use this device effectively can also to degrade to the residual organic pesticide in Algae toxins in water body and gourd, fruit and vegetable, grain, tealeaves.
Summary of the invention
The object of the invention is to: for the defect existed in prior art or deficiency; one is provided to be that medium ionizes with water under DC Electric Field; the oxidizing substance producing high density carries out Strong oxdiative decomposition to the organic pollutant in water body; reach protection of the environment, ensure that healthy object is applicable to the treatment tank of midget plant or family's use.
The technical solution used in the present invention is such: a kind of modified version ionization type treatment tank, Chi Ti, partition wall 1 and partition wall 2 20 is provided with in described pond body, pond body is divided into trash chamber 1, decontamination chamber 2 and reservoir chamber 3 by described partition wall 1 and partition wall 2 20, wherein, upper end position in described trash chamber 1 is provided with screen cloth 5, and described trash chamber 1 upper end outer wall is provided with water-in 4; The lower end position of described partition wall 1 is provided with connected entrance 1; Middle end position in described decontamination chamber 2 is provided with ionization type oxidation reactor 15, the lower end of described ionization type oxidation reactor 15 is provided with filtering net 2 23, the lower end of described filtering net 2 23 is settling region (24), and described decontamination chamber 2 top inner wall is provided with several rotary nozzles 14; The upper end position of described partition wall 2 20 is provided with connected entrance 2 18; The upper end wall of described reservoir chamber 3 is provided with water outlet 21; Described connected entrance 2 18 is in the position of the position of Chi Tizhong higher than ionization type oxidation reactor 15 upper surface; Described connected entrance 1 is in the position of the position of Chi Tizhong lower than ionization type oxidation reactor 15 lower surface; Also be provided with water pump 9 in the body of described pond, described water pump 9 is connected with connected entrance 1 by intermediate connector 10.
Further, described screen cloth 5 lower end is provided with filtering net 1, and described screen cloth 5 is 50 ~ 100 orders.
Further, the external wall in pond, lower end of described trash chamber 1, settling region 24 and reservoir chamber 3 is respectively equipped with sewage draining exit 1, sewage draining exit 2 13 and sewage draining exit 3 22.
Further, the lower end of described trash chamber 1 is provided with scarp 8, and the upper end, inclined-plane on described scarp 8 is connected with connected entrance 1, and the lower end, inclined-plane on described scarp 8 is connected with sewage draining exit 1.
Further, the lower surface of described settling region 24 is circular arc type structure.
In sum, owing to have employed technique scheme, the invention has the beneficial effects as follows:
1, structure of the present invention is simple, and use cost is cheap, and outlet effect is excellent, and suitable especially midget plant or family use.
2, ionization type advanced oxidation reactor of the present invention, be that medium excites the oxidizing substance of generation (OH) concentration to be 14 times of existing electrochemical techniques under equal voltage conditions with water, to the clearance of Organic Pollutants up to 99%, 99.95% is reached to the clearance of bacteriophage.
3, the present invention can be widely used in wastewater from chemical industry, paper waste, percolate, the process at drinking-water water source and disposal, effectively can remove remaining in food pest when using as oxidant generator, may be used for the degraded of melon and fruit, vegetables, tealeaves remains of pesticide simultaneously, also can be used for the exterminating bacterium of medical device.
Accompanying drawing explanation
Examples of the present invention will be described by way of reference to the accompanying drawings, wherein:
Fig. 1 is structural representation of the present invention.
Embodiment
All features disclosed in this specification sheets, or the step in disclosed all methods or process, except mutually exclusive feature and/or step, all can combine by any way.
Arbitrary feature disclosed in this specification sheets (comprising any accessory claim, summary and accompanying drawing), unless specifically stated otherwise, all can be replaced by other equivalences or the alternative features with similar object.That is, unless specifically stated otherwise, each feature is an example in a series of equivalence or similar characteristics.
A kind of modified version ionization type treatment tank as described in Figure 1, Chi Ti, partition wall 1 and partition wall 2 20 is provided with in described pond body, pond body is divided into trash chamber 1, decontamination chamber 2 and reservoir chamber 3 by described partition wall 1 and partition wall 2 20, wherein, upper end position in described trash chamber 1 is provided with screen cloth 5, and described trash chamber 1 upper end outer wall is provided with water-in 4; The lower end position of described partition wall 1 is provided with connected entrance 1; Middle end position in described decontamination chamber 2 is provided with ionization type oxidation reactor 15, the lower end of described ionization type oxidation reactor 15 is provided with filtering net 2 23, the lower end of described filtering net 2 23 is settling region (24), and described decontamination chamber 2 top inner wall is provided with several rotary nozzles 14; The upper end position of described partition wall 2 20 is provided with connected entrance 2 18; The upper end wall of described reservoir chamber 3 is provided with water outlet 21.
Concrete, described screen cloth 5 lower end is provided with filtering net 1, and described screen cloth 5 is 50 ~ 100 orders.
Concrete, the external wall in pond, lower end of described trash chamber 1, settling region 24 and reservoir chamber 3 is respectively equipped with sewage draining exit 1, sewage draining exit 2 13 and sewage draining exit 3 22.
Concrete, the lower end of described trash chamber 1 is provided with scarp 8, and the upper end, inclined-plane on described scarp 8 is connected with connected entrance 1, and the lower end, inclined-plane on described scarp 8 is connected with sewage draining exit 1.
Concrete, the lower surface of described settling region 24 is circular arc type structure.
Concrete, be provided with baffle plate 19 in described connected entrance 2 18.
Concrete, described ionization type oxidation reactor 15 is combined by some pieces of positive level electroplaxs 16 and some pieces of cathode electroplaxs 17, and described positive level electroplax 16 is identical with the quantity of cathode electroplax 17.
Concrete, described connected entrance 2 18 is in the position of the position of Chi Tizhong higher than ionization type oxidation reactor 15 upper surface.
Concrete, described connected entrance 1 is in the position of the position of Chi Tizhong lower than ionization type oxidation reactor 15 lower surface.
Concrete, be also provided with water pump 9 in the body of described pond, described water pump 9 is connected with connected entrance 1 by intermediate connector 10.
To the experiment of wastewater of chemical industry with high concentration
Experimental installation:
Sump pump, under meter, ionization type oxidation reactor, direct supply etc.
Experimental procedure:
Regulate flooding velocity, start direct supply, by pollutant concentration index in sewage, waste water body residence time in ionization type oxidation reactor is respectively 10 minutes, 20 minutes.
Detect data sheet: (chemical industry composite wastewater)
| Sample ID | Wastewater from chemical industry | Oxidation in 10 minutes | Clearance | Be oxidized 20 minutes | Clearance |
| CODcr | 1200mg/L | 180mg/L | 85％ | 60mg/L | 95％ |
| TN | 33.5mg/L | 8.4mg/L | 75％ | 5.0mg/l | 85％ |
Above-described specific embodiment, further describes object of the present invention, technical scheme and beneficial effect, and institute it should be understood that and the foregoing is only specific embodiments of the invention, is not limited to the present invention.The present invention expands to any new feature of disclosing in this manual or any combination newly, and the step of the arbitrary new method disclosed or process or any combination newly.
Claims (5)
1. a modified version ionization type treatment tank, comprise pond body, partition wall one (11) and partition wall two (20) is provided with in described pond body, pond body is divided into trash chamber (1), decontamination chamber (2) and reservoir chamber (3) by described partition wall one (11) and partition wall two (20), it is characterized in that, upper end position in described trash chamber (1) is provided with screen cloth (5), and described trash chamber (1) upper end outer wall is provided with water-in (4); The lower end position of described partition wall one (11) is provided with connected entrance one (12); Middle end position in described decontamination chamber (2) is provided with ionization type oxidation reactor (15), the lower end of described ionization type oxidation reactor (15) is provided with filtering net two (23), the lower end of described filtering net two (23) is settling region (24), and described decontamination chamber (2) top inner wall is provided with several rotary nozzles (14); The upper end position of described partition wall two (20) is provided with connected entrance two (18); The upper end wall of described reservoir chamber (3) is provided with water outlet (21); Wherein, described connected entrance two (18) in the position of Chi Tizhong higher than the position of ionization type oxidation reactor (15) upper surface; Described connected entrance one (12) in the position of Chi Tizhong lower than the position of ionization type oxidation reactor (15) lower surface; And be also provided with water pump (9) in the body of described pond, described water pump (9) is connected with connected entrance one (12) by intermediate connector (10).
2. modified version ionization type treatment tank according to claim 1, is characterized in that: described screen cloth (5) lower end is provided with filtering net one (6), and described screen cloth (5) is 50 ~ 100 orders.
3. modified version ionization type treatment tank according to claim 1, is characterized in that: the external wall in pond, lower end of described trash chamber (1), settling region (24) and reservoir chamber (3) is respectively equipped with sewage draining exit one (7), sewage draining exit two (13) and sewage draining exit three (22).
4. modified version ionization type treatment tank according to claim 3, it is characterized in that: the lower end of described trash chamber (1) is provided with scarp (8), the upper end, inclined-plane on described scarp (8) is connected with connected entrance one (12), and the lower end, inclined-plane of described scarp (8) is connected with sewage draining exit one (7).
5. modified version ionization type treatment tank according to claim 3, is characterized in that: the lower surface of described settling region (24) is circular arc type structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510953783.XA CN105417644A (en) | 2015-12-16 | 2015-12-16 | Improved ionized sewage treatment tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510953783.XA CN105417644A (en) | 2015-12-16 | 2015-12-16 | Improved ionized sewage treatment tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105417644A true CN105417644A (en) | 2016-03-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510953783.XA Pending CN105417644A (en) | 2015-12-16 | 2015-12-16 | Improved ionized sewage treatment tank |
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| Country | Link |
|---|---|
| CN (1) | CN105417644A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114702172A (en) * | 2022-05-07 | 2022-07-05 | 北京科瑞多环保科技有限公司 | A waste liquid treatment device for pesticide production |
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|---|---|---|---|---|
| CN102010038A (en) * | 2010-12-30 | 2011-04-13 | 波鹰(厦门)科技有限公司 | Nano catalytic electrolysis flocculation device |
| CN102139978A (en) * | 2010-12-31 | 2011-08-03 | 清华大学 | Movable type catering waste water treatment equipment |
| CN103466846A (en) * | 2013-10-11 | 2013-12-25 | 武汉水怡环保科技工程有限公司 | Sewage treatment device |
| CN203419777U (en) * | 2013-08-15 | 2014-02-05 | 中国石油天然气股份有限公司 | Electrochemical device for water treatment |
| WO2014172791A1 (en) * | 2013-04-24 | 2014-10-30 | Clear Pod Inc. | Fixed-film aeration apparatus and waste water treatment system |
| CN204022531U (en) * | 2014-08-25 | 2014-12-17 | 南京大学连云港高新技术研究院 | A kind of catalytic oxidation treatment facility |
| CN204417262U (en) * | 2015-01-21 | 2015-06-24 | 江苏锦明不锈钢新材料有限公司 | A kind of industrial wastewater treatment device |
| CN104743733A (en) * | 2013-12-30 | 2015-07-01 | 天津福润龙科技发展有限公司 | Sewage electrolytic flocculation device |
-
2015
- 2015-12-16 CN CN201510953783.XA patent/CN105417644A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010038A (en) * | 2010-12-30 | 2011-04-13 | 波鹰(厦门)科技有限公司 | Nano catalytic electrolysis flocculation device |
| CN102139978A (en) * | 2010-12-31 | 2011-08-03 | 清华大学 | Movable type catering waste water treatment equipment |
| WO2014172791A1 (en) * | 2013-04-24 | 2014-10-30 | Clear Pod Inc. | Fixed-film aeration apparatus and waste water treatment system |
| CN203419777U (en) * | 2013-08-15 | 2014-02-05 | 中国石油天然气股份有限公司 | Electrochemical device for water treatment |
| CN103466846A (en) * | 2013-10-11 | 2013-12-25 | 武汉水怡环保科技工程有限公司 | Sewage treatment device |
| CN104743733A (en) * | 2013-12-30 | 2015-07-01 | 天津福润龙科技发展有限公司 | Sewage electrolytic flocculation device |
| CN204022531U (en) * | 2014-08-25 | 2014-12-17 | 南京大学连云港高新技术研究院 | A kind of catalytic oxidation treatment facility |
| CN204417262U (en) * | 2015-01-21 | 2015-06-24 | 江苏锦明不锈钢新材料有限公司 | A kind of industrial wastewater treatment device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114702172A (en) * | 2022-05-07 | 2022-07-05 | 北京科瑞多环保科技有限公司 | A waste liquid treatment device for pesticide production |
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Application publication date: 20160323 |