CN203653369U - Washing circulating liquid electrocoagulation regeneration treatment system - Google Patents
Washing circulating liquid electrocoagulation regeneration treatment system Download PDFInfo
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- CN203653369U CN203653369U CN201320875225.2U CN201320875225U CN203653369U CN 203653369 U CN203653369 U CN 203653369U CN 201320875225 U CN201320875225 U CN 201320875225U CN 203653369 U CN203653369 U CN 203653369U
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- treatment system
- pond
- regeneration treatment
- strumbox
- coagulation
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Abstract
The utility model relates to the technical field of industrial waste liquid recyclable regeneration treatment, and particularly relates to a system for treating heavy metals and fine particles in circulating liquid. A washing circulating liquid electrocoagulation regeneration treatment system comprises a treatment box with an industrial waste liquid inlet, wherein the rear part of the treatment box is sequentially connected to a filtration box and a slag charge collecting box, the treatment box comprises a left acid-base balance tank and a right electrocoagulation tank, the industrial waste liquid inlet is formed in the top of the acid-base balance tank, a polar plate group is vertically arranged in the electrocoagulation tank and is connected to a rectifying power supply for power supply, and the polar plate group, the treatment box and the rectifying power supply form the electrocoagulation treatment system. Due to adoption of the technical scheme, the washing circulating liquid electrocoagulation regeneration treatment system is used for efficiently removing the heavy metals and organic and inorganic fine particle contaminants remained in the industrial waste liquid by using electrocoagulation principle and automatic acid-base balance, so that most liquid in the waste liquid is recycled, working environments are protected from being subjected to secondary pollution, and the health damage to workers is reduced to the maximum degree.
Description
Technical field
The utility model relates to industrial effluent recyclable regenerative processing technology field, is specifically related to the treatment system of heavy metal and fine particle in a kind of circulation fluid.
Background technology
In tradition offal treatment process, washing is with containing plurality of heavy metal and fine particle in circulating liquid, even if precipitation and the filter regeneration of process traditional technology also cannot effectively be removed these heavy metals and fine particle impurity continuously and automatically.Liquid is after treatment recycling in process, and heavy metal wherein and fine particle can use link infiltration to each, will affect production unit and Working environment, until operator's health.
In addition, in traditional technical matters, can not carry out the automatic adjusting of potential of hydrogen to the liquid in processing, liquid after treatment loses and recycles value because pH value is not up to standard, causes waste, and such liquid also can produce pollution to external world's discharge.
Utility model content
The purpose of this utility model is, a kind of cycles of washing liquid coagulation regeneration treatment system is provided, and solves above technical problem.
The technical problem that the utility model solves can realize by the following technical solutions:
Cycles of washing liquid coagulation regeneration treatment system, comprise an airtight processing casing, which is provided with industrial effluent entrance, described processing casing connects a strumbox, described strumbox connects slag charge collection box, it is characterized in that, described processing casing comprises the acid base equilibrium pond in left side and the coagulation pond on right side, and described industrial effluent entrance is arranged at the top in described acid base equilibrium pond;
Described coagulation is vertically provided with pole plate group in pond, described pole plate group comprises positive plate and negative plate, described pole plate group connects the rectifier power source of a power supply, described pole plate group, described processing casing, described rectifier power source form a coagulation treatment system, to trade effluent is carried out to coagulation processing, the fine particle in industrial effluent is separated from liquid with heavy metal and automatically remove continuously;
Described coagulation is provided with the docking port being connected with described strumbox in pond.
In described coagulation pond, be provided with a plurality of described pole plate groups, a plurality of described pole plate groups are uniformly distributed in described coagulation pond from left to right at certain intervals;
A plurality of described pole plate groups are connected in parallel on described rectifier power source;
A plurality of described pole plate groups form the multistage electrode cluster of a combined type, to increase the processing coverage rate in coagulation pond, improve Disposal quality.
The utility model is by arranging pole plate group, removes after utilizing coagulation principle that the heavy metal in industrial effluent and fine particle are isolated, so that clean liquid is convenient to recycle, saves industrial resources, also saved subsequent production input.The multistage electrode cluster of combined type can effectively carry out the overall situation to water treatment casing and cover, and has increased working efficiency, has improved Disposal quality.
Described rectifier power source adopts a variable direct current formula rectifier power source, can carry out current setting according to actual treatment quality and efficiency, to meet different treatment capacity needs.
The pole plate group that described pole plate group adopts soluble metal to make.The gas of separating out on the electrode that soluble metal is made is little, can eliminate the gas impact that processing brings to coagulation, improves Disposal quality.
In described acid base equilibrium pond, be provided with a motor-driven agitator, described agitator is arranged at described industrial effluent ingress, for by uniform liquid processing, makes the Impurity Distribution in liquid uniform and stable, is convenient to coordinate electrode work, improves coagulation Disposal quality;
The stirring rod of described agitator extends to bottom from the top in acid base equilibrium pond, described stirring rod keeps at a certain distance away from top to bottom and is distributed with plurality of vanes.
In described acid base equilibrium pond, be provided with pH value equilibrator, described pH value equilibrator comprises detection pH sensor and doser, described pH sensor connects described doser, be convenient to described doser and carry out administration timing of drug control and chemical feeding quantity adjustment according to the value of feedback of described pH sensor, described pH sensor setting is in described industrial effluent ingress, and described doser is arranged at the bottom in described acid base equilibrium pond.
Described processing casing carries out corrosion-resistance treatment, and described processing cabinet wall is provided with corrosion-resistant coating, to strengthen the corrosion resistance of equipment, and extension device work-ing life.
The bottom in described coagulation pond is provided with circulating water outlet, and after being convenient to coagulation to process, from industrial cycle liquid, isolated water body is collected rear recycling.
Also comprise a filtration paper web, described filtration paper web is provided with filtration paper tape, and described filter paper tep reel twists on described filtration paper web;
Described filtration paper tape tilts to penetrate the left and right sides of described strumbox, and the higher position point of described filtration paper tape is arranged at the right side of described strumbox, and the top, right side of described strumbox is located in the junction of described processing casing and described strumbox.
Described filtration paper tape is using transfer roller as carrying platform.
Described filtration paper tape is selected and is recycled the filtration paper tape that paper is made, and its thickness is 0.2mm-0.5mm, and it is 20 degree-30 degree that angle of inclination is set.
The lower position point of described filtration paper tape passes the left side wall of described strumbox, and its end below is provided with slag charge collection box, reclaims heavy metal and the fine particle after grain slag separates by slag charge collection box.
Described strumbox bottom is provided with circulation fluid outlet, and described circulation fluid outlet connects recycle pump and is convenient to regeneration liquid to suck circulating line recycling.
In the connecting tube of described strumbox and described processing casing, be provided with a sensor for detection of liquid resistance value, described sensor connects described rectifier power source.Situation by the resistance value to reprocessing cycle liquid is carried out Real-Time Monitoring, and output voltage or the electric current be convenient to rectifier power source are adjusted in time, controls washing liq quality after treatment.
Beneficial effect: owing to adopting technique scheme; the utility model utilizes coagulation principle efficiently to remove organic and mineral contaminants residual in industrial effluent; make partially liq in waste liquid obtain the value of cycling and reutilization; save resource; remove heavy metal and automatization acid base equilibrium has protected Working environment to avoid secondary pollution by automatization, reduced to greatest extent the Health cost that staff is subject to.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach object and effect is easy to understand, below in conjunction with further elaboration the utility model of concrete diagram.
With reference to Fig. 1, cycles of washing liquid coagulation regeneration treatment system, comprise that one is provided with the airtight processing casing 1 of industrial effluent entrance, process casing 1 and connect a strumbox 2, strumbox 2 connects slag charge collection box 3, process casing 1 and comprise the acid base equilibrium pond in left side and the coagulation pond on right side, industrial effluent entrance is arranged at the top in acid base equilibrium pond; In coagulation pond, be vertically provided with a plurality of equally distributed pole plate groups 101, the be connected in parallel rectifier power source 102 of a variable direct current formula of a plurality of pole plate groups 101, pole plate group 101, processing casing 1, rectifier power source 102 form a coagulation treatment system, to trade effluent is carried out to coagulation processing, the fine particle in industrial effluent is separated from liquid with heavy metal and remove; In coagulation pond, be provided with the docking port being connected with strumbox 2.The bottom in coagulation pond is provided with circulating water outlet 106, and after being convenient to coagulation to process, from industrial cycle liquid, isolated water body is collected rear recycling.The pole plate that the electrode of pole plate group adopts soluble metal to make.
The utility model can effectively carry out the overall situation to water treatment casing by the multistage electrode cluster of combined type and cover, and has increased working efficiency, has improved Disposal quality.
In acid base equilibrium pond, be provided with a motor-driven agitator 103, agitator 103 is arranged at industrial effluent ingress, for by uniform liquid processing, makes the Impurity Distribution in liquid uniform and stable, is convenient to coordinate electrode work, improves coagulation Disposal quality; The stirring rod of agitator 103 extends to bottom from the top in acid base equilibrium pond, stirring rod keeps at a certain distance away from top to bottom and is distributed with plurality of vanes.In acid base equilibrium pond, be provided with pH value equilibrator 104, pH value equilibrator comprises detection pH sensor and doser, pH sensor connects doser, be convenient to doser and carry out administration timing of drug control and chemical feeding quantity adjustment according to the value of feedback of pH sensor, pH sensor setting is in industrial effluent ingress, and doser is arranged at the bottom in acid base equilibrium pond.
Process casing 1 and carry out corrosion-resistance treatment, process the inwall of casing 1 and be provided with corrosion-resistant coating, to strengthen the corrosion resistance of equipment, extension device work-ing life.
Also comprise a filtration paper web 4, filter paper web 4 and be provided with filtration paper tape, filter paper tep reel twists in and filters on paper web 4; Filtration paper tape tilts to penetrate the left and right sides of strumbox 2, and the higher position point that filters paper tape is arranged at the right side of strumbox 2, and the top, right side of strumbox 2 is located in the junction of processing casing 1 and strumbox 2.Filter the filtration paper tape that paper tape selects recycling paper to make, its thickness is 0.2mm-0.5mm, and it is 20 degree-30 degree that angle of inclination is set.The lower position that filters paper tape is brought out the left side wall of strumbox 2 out into the open, and its end below is provided with slag charge collection box 3, reclaims heavy metal and the fine particle after grain slag separates by slag charge collection box 3.Strumbox 2 bottoms are provided with circulation fluid outlet 201, and circulation fluid outlet connects recycle pump and is convenient to regeneration liquid to suck circulating line recycling.
In the connecting tube of strumbox 2 and processing casing 1, be provided with a sensor 105 for detection of liquid resistance value, sensor 105 connects rectifier power source 102.By the resistance value of reprocessing cycle liquid is carried out to Real-Time Monitoring, output voltage or the electric current be convenient to rectifier power source 102 are adjusted in time, control liquid mass after treatment.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (10)
1. cycles of washing liquid coagulation regeneration treatment system, comprise an airtight processing casing, which is provided with industrial effluent entrance, described processing casing connects a strumbox, described strumbox connects slag charge collection box, it is characterized in that, described processing casing comprises the acid base equilibrium pond in left side and the coagulation pond on right side, and described industrial effluent entrance is arranged at the top in described acid base equilibrium pond;
Described coagulation is vertically provided with pole plate group in pond, and described pole plate group comprises positive plate and negative plate, and described pole plate group connects the rectifier power source of a power supply, and described pole plate group, described processing casing, described rectifier power source form a coagulation treatment system;
Described coagulation is provided with the docking port being connected with described strumbox in pond.
2. cycles of washing liquid coagulation regeneration treatment system according to claim 1, is characterized in that, is provided with a plurality of described pole plate groups in described coagulation pond, and a plurality of described pole plate groups are uniformly distributed in described coagulation pond from left to right at certain intervals;
A plurality of described pole plate groups are connected in parallel on and on described rectifier power source, form the multistage electrode cluster of a combined type.
3. cycles of washing liquid coagulation regeneration treatment system according to claim 2, is characterized in that, described rectifier power source adopts a variable direct current formula rectifier power source.
4. cycles of washing liquid coagulation regeneration treatment system according to claim 2, is characterized in that, the pole plate group that described pole plate group adopts soluble metal to make.
5. cycles of washing liquid coagulation regeneration treatment system according to claim 2, is characterized in that, is provided with a motor-driven agitator in described acid base equilibrium pond, and described agitator is arranged at described industrial effluent ingress;
The stirring rod of described agitator extends to bottom from the top in described acid base equilibrium pond, described stirring rod keeps at a certain distance away from top to bottom and is distributed with plurality of vanes.
6. cycles of washing liquid coagulation regeneration treatment system according to claim 2, it is characterized in that, in described acid base equilibrium pond, be provided with pH value equilibrator, described pH value equilibrator comprises detection pH sensor and doser, described pH sensor connects described doser, described pH sensor setting is in described industrial effluent ingress, and described doser is arranged at the bottom in described acid base equilibrium pond.
7. cycles of washing liquid coagulation regeneration treatment system according to claim 2, is characterized in that, described processing casing carries out corrosion-resistance treatment, and described processing cabinet wall is provided with corrosion-resistant coating.
8. according to the cycles of washing liquid coagulation regeneration treatment system described in any one in claim 2～7, it is characterized in that, also comprise a filtration paper web, described filtration paper web is provided with filtration paper tape, and described filter paper tep reel twists on described filtration paper web;
Described filtration paper tape tilts to penetrate the left and right sides of described strumbox, and the higher position point of described filtration paper tape is arranged at the right side of described strumbox, and the top, right side of described strumbox is located in the junction of described processing casing and described strumbox;
The lower position point of described filtration paper tape passes the left side wall of described strumbox, and its end below is provided with described slag charge collection box.
9. the cycles of washing liquid coagulation regeneration treatment system described according to Claim 8, is characterized in that, described filtration paper tape is selected and recycled the filtration paper tape that paper is made, and its thickness is 0.2mm-0.5mm, and it is 20 degree-30 degree that angle of inclination is set.
10. cycles of washing liquid coagulation regeneration treatment system according to claim 9, is characterized in that, is provided with a sensor for detection of liquid resistance value in the connecting tube of described strumbox and described processing casing, and described sensor connects described rectifier power source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320875225.2U CN203653369U (en) | 2013-12-27 | 2013-12-27 | Washing circulating liquid electrocoagulation regeneration treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320875225.2U CN203653369U (en) | 2013-12-27 | 2013-12-27 | Washing circulating liquid electrocoagulation regeneration treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN203653369U true CN203653369U (en) | 2014-06-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320875225.2U Expired - Fee Related CN203653369U (en) | 2013-12-27 | 2013-12-27 | Washing circulating liquid electrocoagulation regeneration treatment system |
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| CN (1) | CN203653369U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107639108A (en) * | 2017-07-21 | 2018-01-30 | 郑旭东 | A kind of Ex-situ washing remediation of heavy-metal contaminated soil |
| CN107855353A (en) * | 2017-07-21 | 2018-03-30 | 郑旭东 | A kind of plane leaching repairing method in situ of heavy-metal contaminated soil |
-
2013
- 2013-12-27 CN CN201320875225.2U patent/CN203653369U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107639108A (en) * | 2017-07-21 | 2018-01-30 | 郑旭东 | A kind of Ex-situ washing remediation of heavy-metal contaminated soil |
| CN107855353A (en) * | 2017-07-21 | 2018-03-30 | 郑旭东 | A kind of plane leaching repairing method in situ of heavy-metal contaminated soil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: GTS ENERGY TECHNOLOGY (SHANGHAI) CO., LTD. Effective date: 20150909 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150909 Address after: 201406 Shanghai city Fengxian District Nanqiao town Pu Xing Road No. 6978 Patentee after: GTS ENERGY TECHNOLOGY (SHANGHAI) CO.,LTD. Address before: 201406 Shanghai city Fengxian District Nanqiao town Pu Xing Road No. 6978 Patentee before: GTS ENERGY TECHNOLOGY (SHANGHAI) CO.,LTD. Patentee before: GTS POWER TECHNOLOGY (SHANGHAI) CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140618 Termination date: 20211227 |
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| CF01 | Termination of patent right due to non-payment of annual fee |