CN203360193U - Sewage treatment integration system - Google Patents
Sewage treatment integration system Download PDFInfo
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- CN203360193U CN203360193U CN 201320304381 CN201320304381U CN203360193U CN 203360193 U CN203360193 U CN 203360193U CN 201320304381 CN201320304381 CN 201320304381 CN 201320304381 U CN201320304381 U CN 201320304381U CN 203360193 U CN203360193 U CN 203360193U
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Abstract
The utility model provides a sewage treatment integration system which comprises a pretreatment device, an oxidant storage device, a micro electric catalytic processor, a first reactor, a flocculant storage device, a second reactor, a filter, a standing tank and an aerating apparatus, wherein the pretreatment device is used for receiving, intercepting and storing particulate matters in sewage; the oxidant storage device is used for storing and outputting an oxidant; the micro electric catalytic processor is provided with electrolysis units, and is used for performing electrolytic oxidation and reduction treatment on sewage; the first reactor is connected with an outlet of the pretreatment device and an outlet of the oxidant storage device; one electrolysis unit of the micro electric catalytic processor extends into the first reactor; the flocculant storage device is used for storing and outputting a flocculant; the second reactor is connected with an outlet of the first reactor and an outlet of the flocculant storage device; the other electrolysis unit of the micro electric catalytic processor extends into the second reactor; the filter is connected with an outlet of the second reactor; the standing tank is connected with an outlet of the filter; the aerating apparatus is positioned on the standing tank. The sewage treatment integration system has the advantages that the operation is relatively simple, the cost is relatively low, and the effect is relatively good.
Description
Technical field
The utility model relates to a kind of green technology device, relates in particular to a kind of sewage disposal integrated system that adopts micro-electrocatalysis to process.
Background technology
Traditional sewage treatmentmethod adopts grid interception big particle thing, remove showy oil stain through oil scraping plate again, then reduce COD, BOD, ammonia nitrogen, the SS numerical value in water by aeration desilting and biological degradation, practice shows, this type of sewage treatmentmethod effect is not fine, and complex process, processing cost is higher.
Summary of the invention
The purpose of this utility model is to provide a kind of sewage disposal integrated system, and to solve, the effect that prior art exists is bad, complex process, high in cost of production problem.
In order to address the above problem, the sewage disposal integrated system that the utility model provides comprises: pretreatment unit, for the particulate matter that receives sewage and tackle, take in sewage; The oxygenant storing device, for storage, output oxygenant; Micro-electrocatalysis treater, have electrolyzer, for sewage being carried out to electrolytic oxidation and reduction processing; The first reactor, be connected to receive the sewage that described pretreatment unit processed, the oxygenant of oxygenant storing device output with the outlet of the outlet of described pretreatment unit, oxygenant storing device, and a described electrolyzer of described micro-electrocatalysis treater stretches in described the first reactor; The flocculation agent storing device, for storage, output flocculation agent; The second reactor, be connected to receive the flocculation agent of described flocculation agent storing device output with the outlet of described the first reactor, the outlet of flocculation agent storing device, and another described electrolyzer of described micro-electrocatalysis treater stretches in described the second reactor; Strainer, be connected with the outlet of described the second reactor, for filtering coagulum; Standing pond, be connected the water of crossing for precipitating described filter process with the outlet of described strainer; Aerating apparatus, be positioned on described standing pond, for the water that makes described standing pond, is full of oxygen.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, described pretreatment unit is the cloth bag that can see through liquid.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, described oxygenant storing device is the hydrogen peroxide storing device.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, described flocculation agent storing device is the alum storing device.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, described strainer is activated charcoal filter.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, described aerating apparatus is the spraying aerating apparatus.
According to a kind of preferred implementation of above-mentioned sewage disposal integrated system, wherein, be respectively equipped with an oxygenating machine in described the first reactor and the second reactor.
By upper analysis, and test shows, the mode that the utility model adopts micro-electrocatalysis to process is carried out sewage disposal, is aided with other utility appliance simultaneously, has that operation is simpler, the advantages such as cost is lower, better effects if.
The accompanying drawing explanation
The functional block diagram that Fig. 1 is the utility model preferred embodiment.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further details.
Fig. 1 schematically shows the theory structure of the utility model preferred embodiment, as shown in the figure, this preferred embodiment comprise pretreatment unit 2, the first reactor 3, the second reactor 4, activated charcoal filter 5, standing pond 6, as the hydrogen peroxide storing device 7 of oxygenant storing device, alum storing device 8, aerating apparatus 9 and micro-electrocatalysis treater 10 as the flocculation agent storing device.
Wherein, the particulate matter that pretreatment unit 2 receives sewage and tackles, takes in sewage for the water inlet pipe 11 from input sewage.Pretreatment unit 2 can be cloth bag or other filamentary materials, and this preferred embodiment is selected cloth bag, for tackling and taking in particulate matter, has low cost and other advantages.
Hydrogen peroxide storing device 7 is the hydrogen peroxide as oxygenant for storage, via Teat pipette 71, hydrogen peroxide is delivered to the first reactor 3 simultaneously.
The outlet of the first reactor 3 and pretreatment unit 2, the outlet of hydrogen peroxide storing device 7 are connected to receive sewage that pretreatment unit 2 processed, hydrogen peroxide storing device 7 by the hydrogen peroxide of Teat pipette 71 outputs.
Import the electrolyzer 101 of micro-electrocatalysis treater 10 at the first reactor 3, sewage is carried out to electrolysis, by Teat pipette 71, the hydrogen peroxide in hydrogen peroxide storing device 7 is introduced to the first reactor 3 simultaneously.Hydrogen peroxide belongs to strong oxidizer, has the splendid effect of sterilization, deodorizing.Under the effect of micro-electrocatalysis treater 6, play good katalysis, can form more oxygen in water.
Alum storing device 8 is for storing, export the alum as flocculation agent.Be connected with Teat pipette 81 between alum storing device 8 and the second reactor 4.
In order to increase the oxygen level in water, the first reactor 3 and the second reactor 4 are interior can also arrange respectively an oxygenating machine, suppresses the growth of anerobe in water simultaneously.
The second reactor 4 is connected to receive alum storing device 8 by the alum of Teat pipette 81 outputs with the outlet of the first reactor 3, the outlet of alum storing device 8, and the electrolyzer 102 of micro-electrocatalysis treater 10 stretches in the second reactor 4.
After sewage enters the second reactor 4, import the electrolyzer 102 of micro-electrocatalysis treater 10 at the second reactor 4, sewage is carried out to electrolysis, by Teat pipette 81, the flocculation agent alum in alum storing device 8 is introduced to the second reactor 4 simultaneously.After alum is dissolved in sewage, after electrolyzer 102 electrolysis, ionization has produced positive trivalent aluminium ion, and positive trivalent aluminium ion is combined and has been generated aluminium hydroxide from the negative monovalence hydroxide ion produced with water power, and the alumine hydroxide colloid particle is with positive charge, with electronegative mud pellet micelle, meet, electric charge is neutralized each other, has lost the micelle of electric charge, will soon coalesce together, particle is tied larger and larger, finally sinks under water.Like this, water just becomes limpid clean.
Activated charcoal filter 5 is connected with the outlet of the second reactor 4, for filtering coagulum.
Standing pond 6 is connected with the outlet of activated charcoal filter 5, for precipitating activated charcoal filter 5 treated waters.Sewage enters the second reactor 4, and after completing flocculation sediment, it is limpid that sewage becomes, and then through rearmounted charcoal filter 5, enters standing pond 6.Standing pond 8 upper part arrange several spraying aerating apparatuss 9, make water be full of oxygen, thereby reduce in water after COD, BOD standing 20 to 30 hours of water, further precipitated impurities.
Through above-mentioned processing, can make water reach the standard that enters of urban life water, treated water can be discharged via rising pipe 12.
To sum up, the utility model, based on the electrochemical techniques principle, is aided with other utility appliance simultaneously, utilizes in the electrolytic catalysis reaction process the strong oxidic particle generated, and with organic pollutant in waste water, without chain reaction selectively occurs fast, carries out oxidative degradation.To sewage disposal have simple to operate, cost is low, the advantage such as effective.
As known by the technical knowledge, the utility model can be realized by other the embodiment that does not break away from its spirit or essential feature.Therefore, above-mentioned disclosed embodiment, with regard to each side, all just illustrate, and is not only.All in the utility model scope or the change be equal in scope of the present utility model all be included in the utility model.
Claims (7)
1. a sewage disposal integrated system, is characterized in that, comprising:
Pretreatment unit, for the particulate matter that receives sewage and tackle, take in sewage;
The oxygenant storing device, for storage, output oxygenant;
Micro-electrocatalysis treater, have electrolyzer, for sewage being carried out to electrolytic oxidation and reduction processing;
The first reactor, be connected to receive the sewage that described pretreatment unit processed, the oxygenant of oxygenant storing device output with the outlet of the outlet of described pretreatment unit, oxygenant storing device, and a described electrolyzer of described micro-electrocatalysis treater stretches in described the first reactor;
The flocculation agent storing device, for storage, output flocculation agent;
The second reactor, be connected to receive the flocculation agent of described flocculation agent storing device output with the outlet of described the first reactor, the outlet of flocculation agent storing device, and another described electrolyzer of described micro-electrocatalysis treater stretches in described the second reactor;
Strainer, be connected with the outlet of described the second reactor, for filtering coagulum;
Standing pond, be connected the water of crossing for precipitating described filter process with the outlet of described strainer;
Aerating apparatus, be positioned on described standing pond, for the water that makes described standing pond, is full of oxygen.
2. sewage disposal integrated system according to claim 1, is characterized in that, described pretreatment unit is the cloth bag that can see through liquid.
3. sewage disposal integrated system according to claim 1, is characterized in that, described oxygenant storing device is the hydrogen peroxide storing device.
4. sewage disposal integrated system according to claim 1, is characterized in that, described flocculation agent storing device is the alum storing device.
5. sewage disposal integrated system according to claim 1, is characterized in that, described strainer is activated charcoal filter.
6. sewage disposal integrated system according to claim 1, is characterized in that, described aerating apparatus is the spraying aerating apparatus.
7. sewage disposal integrated system according to claim 1, is characterized in that, is respectively equipped with an oxygenating machine in described the first reactor and the second reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320304381 CN203360193U (en) | 2013-05-30 | 2013-05-30 | Sewage treatment integration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320304381 CN203360193U (en) | 2013-05-30 | 2013-05-30 | Sewage treatment integration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203360193U true CN203360193U (en) | 2013-12-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320304381 Expired - Fee Related CN203360193U (en) | 2013-05-30 | 2013-05-30 | Sewage treatment integration system |
Country Status (1)
| Country | Link |
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| CN (1) | CN203360193U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150654A (en) * | 2013-05-30 | 2014-11-19 | 王海彬 | Integrated sewage treatment system |
| CN105621761A (en) * | 2016-03-11 | 2016-06-01 | 秦皇岛市桑格节能环保科技有限公司 | Oil field produced water treatment method and device |
-
2013
- 2013-05-30 CN CN 201320304381 patent/CN203360193U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150654A (en) * | 2013-05-30 | 2014-11-19 | 王海彬 | Integrated sewage treatment system |
| CN104150654B (en) * | 2013-05-30 | 2015-08-19 | 王海彬 | Sewage disposal integrated system |
| CN105621761A (en) * | 2016-03-11 | 2016-06-01 | 秦皇岛市桑格节能环保科技有限公司 | Oil field produced water treatment method and device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131225 Termination date: 20160530 |
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| CF01 | Termination of patent right due to non-payment of annual fee |