CN113149294A - Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology - Google Patents
Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology Download PDFInfo
- Publication number
- CN113149294A CN113149294A CN202110335039.9A CN202110335039A CN113149294A CN 113149294 A CN113149294 A CN 113149294A CN 202110335039 A CN202110335039 A CN 202110335039A CN 113149294 A CN113149294 A CN 113149294A
- Authority
- CN
- China
- Prior art keywords
- aluminum
- plate
- electrocoagulation
- electric flocculation
- aeration
- 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.)
- Pending
Links
Images
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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
-
- 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
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
Abstract
The invention discloses a method and a device for treating phosphorus-containing sewage by using a double-aluminum-plate anode electric flocculation technology. Mainly comprises a direct current power supply, a water inlet adjusting tank, a periodic programming direction changer, a water inlet pump, an aeration fan, an aluminum electrode plate, an aeration device, an electrocoagulation groove body and a water outlet groove. The water inlet adjusting tank is connected with a water inlet pump through a pipeline to feed water into the electric flocculation tank, and the outlet water is discharged through the water outlet tank; the aluminum electrode plate and the aeration device are both arranged in the groove; the adjacent electrode plates are respectively connected with the positive electrode and the negative electrode of the direct-current power supply, and a periodic programming direction changer is arranged in the connecting circuit to control the switching of the positive electrode and the negative electrode. The aeration device aerates the electric flocculation tank through a pipeline by an aeration fan. The invention adopts the measures of a double-aluminum anode electric flocculation system, an introduced aeration system, a periodic programming commutator and the like, improves the treatment efficiency of pollutants, reduces the treatment cost, avoids electrolytic short circuit and has low phosphorus concentration of effluent. The double-aluminum anode electroflocculation dephosphorization method and the device are suitable for treating inorganic phosphorus wastewater with various concentrations.
Description
Technical Field
The invention relates to the technical field of environmental engineering sewage treatment, in particular to a method and a device for treating phosphorus-containing sewage by using a double-aluminum-plate anode electric flocculation technology.
Background
A great deal of research shows that the key to solving the eutrophication problem of the water body lies in how to effectively control the concentration of the phosphorus nutritive salt in the water body. According to the discharge standard of urban sewage treatment plants (GB18918-2002) in China, the primary standard A of total phosphorus discharge of urban sewage treatment plants constructed from 1 month and 1 day in 2006 is 0.5mg/L (counted by P). With the stricter requirements of our country on the discharge standard of the phosphorus-containing wastewater, governments and enterprises have to pay attention to the treatment of the phosphorus-containing wastewater.
At present, the method for removing phosphate in water mainly comprises a biological phosphorus removal method, a chemical precipitation method, an adsorption method and the like. The electric flocculation technology is applied to the treatment of phosphorus-containing wastewater, and the research is less, mainly due to the following reasons: firstly, after electrification and electrolysis, the anode generates high-concentration metal cations, an ion concentration gradient is formed between the ion concentration of the solution near the electrode and the bulk solution, and concentration polarization can influence the electrolysis efficiency of a polar plate; secondly, the commonly adopted iron electrode is electrolyzed to generate ferrous ions, and the ferrous ions and the color substances in the water lead the raw water to change color; meanwhile, the flocculation sediment quickly sinks into the bottom of the tank, and the flocculation effect is poor; in addition, the electrolysis short circuit phenomenon is easy to occur in the multi-polar plate parallel electrolysis.
Therefore, it is required to provide a method for efficiently treating phosphorus-containing wastewater, which can slow down the passivation of the electrode plate, avoid the short circuit of electrolysis, prevent the raw water from discoloring, prevent the secondary pollution from being introduced.
Disclosure of Invention
The invention aims to solve the technical problems and provides a method for treating phosphorus-containing sewage by using a double-aluminum plate anode electric flocculation technology.
The technical scheme adopted by the invention for solving the technical problems is as follows:
a method for treating phosphorus-containing sewage by double-aluminum plate anode electrocoagulation technology,
firstly, adjusting the pH value of the sewage to 6.0-8.0;
pumping the sewage to an electric flocculation reaction tank by a pump, feeding water into the electric flocculation reaction tank from the bottom,
an aeration device is arranged at the bottom of the electric flocculation reaction tank, aeration is carried out in the electric flocculation reaction tank through the aeration device,
the electrocoagulation time is 5-120 min.
In one embodiment, a water outlet groove is arranged on one side of the top of the electrocoagulation reaction tank, and when water is discharged, water in the electrocoagulation reaction tank flows into the water outlet groove from one side of the water outlet groove and then is discharged from the other side of the water outlet groove.
In one embodiment, the electrocoagulation reaction tank comprises a tank body and a plurality of aluminum electrode plates arranged in the tank body, wherein the aluminum electrode plates are sequentially arranged at intervals, one of two adjacent aluminum electrode plates is used as an anode electrode plate, the other one of the two adjacent aluminum electrode plates is used as a cathode electrode plate, each aluminum electrode plate is respectively connected with a periodic programming deviator, and the periodic programming deviator is connected with a power supply.
In one embodiment, the periodical programming direction changer sets the cathode and anode direction changing time to be 100-1000 s, preferably 200-300 s; the distance between two adjacent aluminum electrode plates is 1-4 cm, preferably 2-3 cm.
In one embodiment, the aeration rate in the electrocoagulation reaction tank is 1.0-3.0L/(L.min), preferably 1.5-2.0L/(L.min). The power supply of the electric flocculation reaction tank is a direct current power supply, and the current density is 5.00-15.00A/m2(ii) a The phosphorus concentration of the sewage is 0.5-200 mg/L.
A device special for the sewage treatment method is characterized in that:
comprises a direct current power supply, a water inlet adjusting tank, a periodic programming direction changer, a water inlet pump, an aeration fan, a plurality of aluminum electrode plates, a plurality of aeration devices, an electrocoagulation groove body and a water outlet groove,
the water inlet adjusting tank is connected with a water inlet pump through a pipeline, the water inlet pump is connected with a water inlet arranged at the bottom of the electrocoagulation cell body through a pipeline, the water outlet groove is arranged at one side of the top of the electrocoagulation cell body,
each aluminum electrode plate and each aeration device are arranged in the electric flocculation tank body, each aluminum electrode plate is sequentially arranged at intervals, one aluminum electrode plate in two adjacent aluminum electrode plates is used as an anode electrode plate, the other aluminum electrode plate is used as a cathode electrode plate, each aluminum electrode plate is respectively connected with a periodic programming deviator, the periodic programming deviator is connected with a direct current power supply,
each aeration device is arranged at the bottom of the electric flocculation tank body, the aeration fan supplies air to the aeration device through a pipeline, and the aeration device aerates in the electric flocculation tank body.
The invention has the beneficial effects that: the invention is based on the electric flocculation dephosphorization technology, has simple and efficient process and easy operation, and simultaneously avoids the problems of secondary pollution caused by a chemical method, low dephosphorization efficiency of a biological method, long running period and the like. The electric flocculation technology has high efficiency and low cost, does not introduce secondary pollution, and is an environment-friendly sewage treatment technology. Meanwhile, compared with the existing electrocoagulation sewage treatment technology, the electrocoagulation phosphorus removal technology adopts the measures of a double-aluminum anode electrocoagulation system, an introduced aeration system, a periodic programming reverser and the like, so that the treatment efficiency of pollutants is improved, the treatment cost is reduced, the aeration system effectively avoids electrolytic short circuit, and the effluent reaches the domestic sewage discharge standard. The double-aluminum anode electroflocculation dephosphorization method and the device are suitable for treating inorganic phosphorus wastewater with various concentrations. Compared with other phosphorus removal technologies, the electric flocculation phosphorus removal technology has the advantages of high efficiency, low cost, stable operation and the like. The high efficiency of the double-aluminum plate anode electrocoagulation dephosphorization technology lies in the flowing mode of sewage, the introduction of an aeration system and a double-aluminum plate electrode. The introduction of the aeration system greatly reduces the ion concentration of the solution near the polar plate and the concentration gradient of the bulk solution, and avoids the reduction of the electrolysis efficiency caused by concentration polarization. The adoption of the double aluminum electrode plate effectively avoids the problem that the iron electrode discolors raw water. The introduction of the periodical programming direction changer enables the cathode and the anode to be exchanged according to the time rule, and the problem of polar plate passivation is relieved to a great extent. The adoption of the aluminum electrode avoids the problem of water outlet color of the traditional iron electrode. The electric flocculation dephosphorization technique is suitable for treating inorganic phosphorus wastewater with various concentrations, has simple required equipment, easy operation, low cost and stable operation, and is a dephosphorization technique with great market application prospect.
Drawings
FIG. 1 is a schematic diagram of an apparatus for a method for treating phosphorus-containing sewage by using a double-aluminum plate anode electrocoagulation technology, which is disclosed by the embodiment of the invention.
Labeled as: 1. a direct current power supply; 2. a water inlet adjusting tank; 3. periodically programming a direction changer; 4. a water inlet pump; 5. an aeration fan; 6. aluminum electrode plates 7, 8, 9, 10, 11, 12, 13 and 10; 14. aeration device, 15, 16, aeration device; 17. an electrocoagulation tank body; 18. a water outlet groove.
Detailed Description
The present invention will be described in detail with reference to examples. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. The experimental procedures, in which specific conditions are not noted in the following examples, are generally carried out according to conventional conditions or according to conditions recommended by the manufacturers.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art. In addition, any methods and materials similar or equivalent to those described herein can be used in the methods of the present invention. The preferred embodiments and materials described herein are intended to be exemplary only.
As shown in fig. 1, an embodiment of the present invention provides a method for treating phosphorus-containing sewage by double-aluminum plate anodic electrocoagulation, which comprises:
firstly, adjusting the pH value of the sewage to 6.0-8.0; pumping sewage to an electric flocculation reaction tank through a pump, wherein water is fed into the electric flocculation reaction tank from the bottom; an aeration device is arranged at the bottom of the electrocoagulation reaction tank, and aeration is carried out in the electrocoagulation reaction tank through the aeration device; the electrocoagulation time is 5-120 min, for example, 5min, 100min, 120min, etc. The aeration device can be provided in a plurality of numbers, for example, in fig. 1, comprising an aeration device 14, an aeration device 15 and an aeration device 16.
In this embodiment, the water outlet groove 18 is disposed on one side of the top of the tank body of the electrocoagulation reaction tank, and when water is discharged, water in the tank body of the electrocoagulation reaction tank flows into the water outlet groove 18 from one side of the water outlet groove 18, and then is discharged from the other side of the water outlet groove 18.
In this embodiment, the electrocoagulation reaction tank includes a tank body and a plurality of aluminium electrode plates arranged in the tank body, each aluminium electrode plate is arranged at intervals in sequence, and one aluminium electrode plate of two adjacent aluminium electrode plates is used as an anode plate, and the other aluminium electrode plate is used as a cathode plate, each aluminium electrode plate is connected with the periodic programming deviator 3 respectively, the periodic programming deviator 3 is connected with a power supply.
The polarity of each aluminum electrode plate can be exchanged after a certain time interval by the periodical programming deviator 3, namely, the aluminum electrode plate which is originally used as the anode is exchanged to be used as the cathode electrode plate, and the aluminum electrode plate which is originally used as the cathode electrode plate is exchanged to be used as the anode electrode plate.
For example, the aluminum electrode plate 6 is a cathode plate, the aluminum electrode plate 7 is an anode plate, the aluminum electrode plate 8 is a cathode plate, the aluminum electrode plate 9 is an anode plate, the aluminum electrode plate 10 is a cathode plate, the aluminum electrode plate 11 is an anode plate, the aluminum electrode plate 12 is a cathode plate, and the aluminum electrode plate 13 is an anode plate.
After the replacement, the aluminum electrode plate 6 is an anode plate, the aluminum electrode plate 7 is a cathode plate, the aluminum electrode plate 8 is an anode plate, the aluminum electrode plate 9 is a cathode plate, the aluminum electrode plate 10 is an anode plate, the aluminum electrode plate 11 is a cathode plate, the aluminum electrode plate 12 is an anode plate, and the aluminum electrode plate 13 is a cathode plate.
In the embodiment, the periodical programming direction changer 3 sets the cathode and anode direction changing time to be 100-1000 s, and the distance between two adjacent polar plates is 1-4 cm.
For example, the periodic programming redirector 3 sets the cathode and anode redirection period to 100s, 500s, 800s, or 1000s, etc. The distance between two adjacent polar plates is 1cm, 3cm or 4cm and the like.
In the embodiment, the aeration rate in the electrocoagulation reaction tank is 1.0-3.0L/(L.min); the power supply of the electric flocculation reaction tank is a direct current power supply 1, and the current density is 5.00-15.00A/m2(ii) a The phosphorus concentration of the sewage is 0.5-200 mg/L.
For example, the aeration rate in the electrocoagulation reaction tank may be 1L/(L · min), 2L/(L · min), 3.0L/(L · min), or the like.
For example, the power supply of the electric flocculation reaction tank is a direct current power supply 1, and the current density is 5.00A/m2、10A/m2Or 15.00A/m2And the like.
For example, the sewage contains phosphorus at a concentration of 0.5mg/L, 100mg/L, or 200mg/L, etc.
The effectiveness of the above-described method of the present invention is verified by specific tests below.
Example 1:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 1 cm. Adjusting pH to 7.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 10.00A/m2The electrode turning period is 100s, the electrocoagulation time is 20min, and the aeration intensity is 1.0L/(L.min). And (4) standing the discharged water for 10min after the reaction is finished, and testing that the total phosphorus concentration of the discharged water is 0.45mg/L, namely the removal rate reaches 95.5%.
Example 2:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 2 cm. Adjusting pH to 7.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 10.00A/m2The electrode turning period is 100s, and the electrocoagulation time is 20 min. And (4) standing the discharged water for 10min after the reaction is finished, and testing that the total phosphorus concentration of the discharged water is 0.35mg/L, namely the removal rate reaches 96.5%.
Example 3:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 1 cm. Adjusting pH to 7.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 10.00A/m2The electrode turning period is 100s, the electrocoagulation time is 20min, and the aeration intensity is 1.5L/(L.min). Standing the discharged water for 10min after the reaction is finished, and testing the total phosphorus concentration of the discharged waterThe degree is 0.25mg/L, namely the removal rate reaches 97.5 percent.
Example 4:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 2 cm. Adjusting pH to 6.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 10.00A/m2The electrode turning period is 100s, and the electrocoagulation time is 20 min. And (4) standing the discharged water for 10min after the reaction is finished, and testing that the total phosphorus concentration of the discharged water is 0.20mg/L, namely the removal rate reaches 98.0%.
Example 5:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 2 cm. Adjusting pH to 7.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 10.00A/m2The electrode turning period is 200s, and the electrocoagulation time is 20 min. And (4) standing the discharged water for 10min after the reaction is finished, and testing that the total phosphorus concentration of the discharged water is 0.22mg/L, namely the removal rate reaches 97.8%.
Example 6:
the double-aluminum plate anode electrocoagulation dephosphorization process reaction tank for simulating the phosphorus-containing sewage adopts an organic glass plate, the specification of which is 500mm multiplied by 500mm, and the effective volume of the reaction tank is 100L. An aluminum plate is used as an electrode plate, and the specification of the electrode plate is 250mm multiplied by 100mm multiplied by 3 mm. 8 electrode plates are arranged, and the plate distance is 2 cm. Adjusting pH to 7.0, the initial total phosphorus concentration to 10.0mg/L, and using DC power supply generator with current density of 15.00A/m2The electrode turning period is 200s, and the electrocoagulation time is 20 min. And (4) standing the discharged water for 10min after the reaction is finished, and testing that the total phosphorus concentration of the discharged water is 0.12mg/L, namely the removal rate reaches 98.8%.
As shown in figure 1, the embodiment of the invention also provides a device special for the sewage treatment method, which comprises a direct current power supply 1, a water inlet adjusting tank 2, a periodic programming diverter 3, a water inlet pump 4, an aeration fan 5, a plurality of aluminum electrode plates, a plurality of aeration devices, an electric flocculation tank body 17 and a water outlet tank 18.
For example, the plurality of aluminum electrode plates include an aluminum electrode plate 6, an aluminum electrode plate 7, an aluminum electrode plate 8, an aluminum electrode plate 9, an aluminum electrode plate 10, an aluminum electrode plate 11, an aluminum electrode plate 12, an aluminum electrode plate 13, and the like.
For example, the plurality of aeration apparatuses include an aeration apparatus 14, an aeration apparatus 15, and an aeration apparatus 16.
The water inlet adjusting tank 2 is connected with a water inlet pump 4 through a pipeline, the water inlet pump 4 is connected with a water inlet arranged at the bottom of the electrocoagulation groove body 17 through a pipeline, and a water outlet groove 18 is arranged at one side of the top of the electrocoagulation groove body 17. The water inlet adjusting tank 2 is used for adjusting the pH value of the sewage.
Each aluminum electrode plate and each aeration device are arranged in the electrocoagulation cell body 17, each aluminum electrode plate is arranged at intervals in sequence, one of two adjacent aluminum electrode plates is used as an anode plate, the other one is used as a cathode plate, each aluminum electrode plate is respectively connected with the periodic programming deviator 3, and the periodic programming deviator 3 is connected with the direct-current power supply 1.
Each aeration device is arranged at the bottom of the electric flocculation tank body 17, the aeration fan 5 supplies air to the aeration device through a pipeline, and the aeration device aerates the electric flocculation tank body 17.
The above-mentioned embodiments are intended to illustrate the objects, technical solutions and advantages of the present invention in further detail, and it should be understood that the above-mentioned embodiments are only exemplary embodiments of the present invention, and are not intended to limit the present invention, and any modifications, equivalents, improvements and the like made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (6)
1. A method for treating phosphorus-containing sewage by double-aluminum plate anode electrocoagulation technology is characterized by comprising the following steps:
firstly, adjusting the pH value of the sewage to 6.0-8.0;
pumping the sewage to an electric flocculation reaction tank by a pump, feeding water into the electric flocculation reaction tank from the bottom,
an aeration device is arranged at the bottom of the electric flocculation reaction tank, aeration is carried out in the electric flocculation reaction tank through the aeration device,
the electrocoagulation time is 5-120 min.
2. The method for treating phosphorus-containing sewage by double-aluminum-plate anode electrocoagulation technology according to claim 1, wherein a water outlet groove is arranged on one side of the top of the electrocoagulation reaction tank, and when water is discharged, water in the electrocoagulation reaction tank flows into the water outlet groove from one side of the water outlet groove and then is discharged from the other side of the water outlet groove.
3. The method for treating phosphorus-containing sewage by the double-aluminum-plate anodic electrocoagulation technology as claimed in claim 1, wherein the electrocoagulation reaction tank comprises a tank body and a plurality of aluminum electrode plates arranged in the tank body, each aluminum electrode plate is arranged at intervals in sequence, one of two adjacent aluminum electrode plates is used as an anode plate, the other one is used as a cathode plate, each aluminum electrode plate is respectively connected with a periodic programming deviator, and the periodic programming deviator is connected with a power supply.
4. The method for treating phosphorus-containing sewage by the double-aluminum-plate anodic electrocoagulation technology as recited in claim 3, wherein: the periodic programming deviator is provided with a cathode and an anode with the deviator time of 100-1000 s and the distance between two adjacent aluminum electrode plates is 1-4 cm.
5. The method for treating phosphorus-containing sewage by the double-aluminum-plate anodic electrocoagulation technology as recited in claim 1, wherein: the aeration rate in the electrocoagulation reaction tank is 1.0-3.0L/(L.min); the power supply of the electric flocculation reaction tank is a direct current power supply, and the current density is 5.00-15.00A/m2(ii) a The phosphorus concentration of the sewage is 0.5-200 mg/L.
6. An apparatus dedicated to the method of any one of claims 1 to 5, characterized in that:
comprises a direct current power supply, a water inlet adjusting tank, a periodic programming direction changer, a water inlet pump, an aeration fan, a plurality of aluminum electrode plates, a plurality of aeration devices, an electrocoagulation groove body and a water outlet groove,
the water inlet adjusting tank is connected with a water inlet pump through a pipeline, the water inlet pump is connected with a water inlet arranged at the bottom of the electrocoagulation cell body through a pipeline, the water outlet groove is arranged at one side of the top of the electrocoagulation cell body,
each aluminum electrode plate and each aeration device are arranged in the electric flocculation tank body, each aluminum electrode plate is sequentially arranged at intervals, one aluminum electrode plate in two adjacent aluminum electrode plates is used as an anode electrode plate, the other aluminum electrode plate is used as a cathode electrode plate, each aluminum electrode plate is respectively connected with a periodic programming deviator, the periodic programming deviator is connected with a direct current power supply,
each aeration device is arranged at the bottom of the electric flocculation tank body, the aeration fan supplies air to the aeration device through a pipeline, and the aeration device aerates in the electric flocculation tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110335039.9A CN113149294A (en) | 2021-03-29 | 2021-03-29 | Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110335039.9A CN113149294A (en) | 2021-03-29 | 2021-03-29 | Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113149294A true CN113149294A (en) | 2021-07-23 |
Family
ID=76885580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110335039.9A Pending CN113149294A (en) | 2021-03-29 | 2021-03-29 | Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113149294A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115140807A (en) * | 2022-06-15 | 2022-10-04 | 徐凯波 | Overflow type electrochemical water treatment equipment |
| CN115259299A (en) * | 2022-07-12 | 2022-11-01 | 同研智慧(苏州)环境科技有限公司 | Electric flocculation coupling ultrasonic cavitation river lake in-situ phosphorus removal and algae inhibition system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203319806U (en) * | 2013-06-24 | 2013-12-04 | 长江大学 | Electrolysis dephosphorization device for treating domestic sewage |
| CN103613170A (en) * | 2013-11-22 | 2014-03-05 | 苏州优德通力电气有限公司 | Double-aluminum-electrode electrolytic phosphorous removing device and using method thereof |
| CN104787859A (en) * | 2015-04-22 | 2015-07-22 | 中国中化股份有限公司 | Method and device for treating phosphorus wastewater by adopting multi-electrode baffling electric flocculation process |
-
2021
- 2021-03-29 CN CN202110335039.9A patent/CN113149294A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203319806U (en) * | 2013-06-24 | 2013-12-04 | 长江大学 | Electrolysis dephosphorization device for treating domestic sewage |
| CN103613170A (en) * | 2013-11-22 | 2014-03-05 | 苏州优德通力电气有限公司 | Double-aluminum-electrode electrolytic phosphorous removing device and using method thereof |
| CN104787859A (en) * | 2015-04-22 | 2015-07-22 | 中国中化股份有限公司 | Method and device for treating phosphorus wastewater by adopting multi-electrode baffling electric flocculation process |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115140807A (en) * | 2022-06-15 | 2022-10-04 | 徐凯波 | Overflow type electrochemical water treatment equipment |
| CN115259299A (en) * | 2022-07-12 | 2022-11-01 | 同研智慧(苏州)环境科技有限公司 | Electric flocculation coupling ultrasonic cavitation river lake in-situ phosphorus removal and algae inhibition system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100560517C (en) | A kind of method of preprocessing coking wastewater by electrochemical oxidation flocculating composite technique | |
| CN102603119B (en) | Garbage leachate treatment device and treatment method thereof | |
| CN104787859B (en) | A kind of method and device of use multi-electrode baffling electric flocculation technique Removal of Phosphorus in Wastewater | |
| CN101302073B (en) | Electroplating sewerage advanced treatment process | |
| CN103936106B (en) | Electrochemical synchronous nitrogen and phosphorus removal apparatus and municipal sewage treatment method | |
| CN113149294A (en) | Method and device for treating phosphorus-containing sewage by double-aluminum-plate anode electric flocculation technology | |
| CN101723490A (en) | Pulse electro-flocculation treatment process and device of berberine waste water | |
| CN107098441A (en) | The method that electrochemistry removes Determination of Total Nitrogen in Waste Water | |
| CN103539296A (en) | Method and device for treating high-concentration nonbiodegradable organic wastewater | |
| CN105152422A (en) | System for treating heavy metal wastewater by electrochemical-microflocculation-floatation process | |
| CN105384222A (en) | Waste water electric flocculation treatment device | |
| CN106241971B (en) | Pulse electrolytic flocculation device and treatment method for simultaneously treating electroplating wastewater and organic wastewater | |
| CN110980891B (en) | Tower type electric flocculation water treatment device | |
| CN111333235A (en) | Landfill leachate treatment system and process | |
| CN203781882U (en) | Oxidation-flocculation complex bed device for landfill leachate | |
| CN205088058U (en) | Little electrolysis processing system of high concentration organic waste water | |
| CN210140521U (en) | Printing industry effluent disposal system | |
| CN209778578U (en) | electrolytic phosphorus removal equipment and sewage treatment system applying same | |
| CN211111206U (en) | Electric flocculation purifies little surface water device that pollutes | |
| CN206843153U (en) | Electrochemistry removes Determination of Total Nitrogen in Waste Water plug flow diaphragm electrolysis apparatus | |
| CN212076515U (en) | Iron-carbon micro-electrolysis principle sewage treatment device | |
| CN106630029A (en) | Pulse electrolysis system and method for electrolyzing wastewater by means of pulse electrolysis system | |
| CN214495999U (en) | High salinity organic matter effluent disposal system | |
| CN102992484B (en) | Micro-charge sewage treatment method | |
| CN214141926U (en) | Heavy metal sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210723 |
|
| RJ01 | Rejection of invention patent application after publication |