CN101638285A - Sewage purification processing system - Google Patents
Sewage purification processing system Download PDFInfo
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- CN101638285A CN101638285A CN200910085287A CN200910085287A CN101638285A CN 101638285 A CN101638285 A CN 101638285A CN 200910085287 A CN200910085287 A CN 200910085287A CN 200910085287 A CN200910085287 A CN 200910085287A CN 101638285 A CN101638285 A CN 101638285A
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- pond
- processing system
- sewage purification
- purification processing
- ozone
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Abstract
The invention relates to a sewage purification processing system which sequentially comprises a grit chamber, an adjusting tank, an aerobic pond, an inclined plate sedimentation tank, a filtering tank, an ozone processing tank, wherein the bottom of the adjusting tank is provided with a preaerator, the aerobic pond is internally provided with a packing layer suspended in the middle part of the aerobic pond; an ozone oxidation pond is a plug-flow pool, and a water inlet pipeline of the ozone processing tank is provided with a pump and a venturi which are matched with each other; an outlet of the pump is connected with an inlet of the venturi, and a suction inlet of the venturi is connected with an ozone outlet of an ozonizer which adopts a plasma generator provided with an ozone air outlet;a plasma is provided with a high-voltage high frequency power supply circuit, and grille is arranged at the front par or in front of the grit chamber. The system has reasonable technique, good processing effect and lower cost, and the outlet water can be recycled in the life and industry.
Description
Technical field
The present invention relates to a kind of sewage purification processing system, mainly can be used for handling sanitary sewage and the production waste that pollution level is not really high and biodegradability is good, the water after the processing can be used as the undrinkable water reuse.
Background technology
For pollution level not really high sanitary sewage and part industrial sewage, aerobic biochemical is a kind of low-cost processes mode mode effectively, biochemical action by the aerobic microbiological flora, organism in the water is decomposed into inorganics or simple substance, separate solid particulate matters such as mud in the water outlet and colloidal sol etc. by modes such as precipitations then, the most of impurity of in the water other also can be along with mud separating treatment together, but when being back to life and production as non-quoted water, need the water after the aerobic treatment further be purified toward contact, various films are handled to separate and are used in practice, and obtained treatment effect preferably, but because the cost of film processing at present is higher relatively, influenced the development of reusing sewage, therefore the combination of various treatment technologies still is in the continuous discussion.
Summary of the invention
For overcoming the above-mentioned defective of prior art, the invention provides a kind of sewage purification processing system, the treatment effect of this treatment system is good, and cost is low.
The present invention realizes that the technical scheme of above-mentioned purpose is: comprise the settling pit that connects successively, equalizing tank, Aerobic Pond, inclined-plate clarifying basin, filtering basin and ozonize pond, be provided with the packing layer that is suspended from the middle part, pond in the described Aerobic Pond, the suction culvert in described ozonize pond is provided with pump and the Venturi meter that complements one another, described pump outlet connects the import of described Venturi meter, the suction port of described Venturi meter connects the ozone gas outlet of ozonizer, the front portion or the front of described settling pit are provided with grid, described equalizing tank bottom is provided with preaerator, described ozone oxidation pond is the plug-flow pond, described ozonizer adopts the plasma generator that is provided with the ozone-air outlet, and described plasma body is furnished with the high voltagehigh frequency power source circuit.
Because the present invention has adopted rational treatment process, sewage for good biodegradability, by catalytic oxidation mode efficiently organism wherein is converted to inorganics, and pollutents such as other particulate matter are adsorbed in the active sludge, remove most settleable matters in the water by inclined plate sedimentation mode efficiently then, to alleviate follow-up filtering load, further purify at filter type by high degree of purification, and then carry out ozonization and ozone oxidation, guaranteed the water quality of water outlet thus, made it to satisfy landscape water, water and pour water and multiple use such as industrial colling; Because technology of the present invention is reasonable, each step all provides condition for next step processing, reduce significantly through the impurity in the water after precipitation and the filtration, greatly reduced in ozonization and the oxidising process impurity to the absorption and the decomposition of ozone, improve the effective rate of utilization of ozone, thereby controlled required ozone amount and the processing cost of ozonize process effectively; Because the mode that has adopted jet to suck will contain in the inclusion of air water of ozone, effect by Venturi meter, make the mixing of ozone in water very fast, mixed effect is very good, greatly improved the actual meltage of ozone, strengthen the treatment effect that ozone concn in the sewage has improved ozone, strengthened the treatment effect of ozone; Owing to adopt the plug-flow pond as the ozonize pond, in the continuous propulsive process of water, form zone metastable and that gradually change, concentration at ingress's ozone is the highest, with ozone oxidation and sterilization is the principal reaction process, ozone consumes gradually and decomposes subsequently, when the plug-flow pond is enough big, ozone concn in the water part is just very low, can not cause erosion to water reuse apparatus, simultaneously, can play the effect of water collecting basin simultaneously because that the plug-flow pond can be provided with is long, from its afterbody (water part) directly water intaking can not produce material injury to the operation of system.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Embodiment
Referring to Fig. 1, sewage purification processing system of the present invention comprises Aerobic Pond 16, inclined-plate clarifying basin 18, filtering basin 20 and ozonize pond, be provided with the packing layer 15 that is suspended from the middle part, pond in the described Aerobic Pond, the suction culvert in described ozonize pond is provided with pump 11 and the Venturi meter 10 that complements one another, described pump outlet connects the import of described Venturi meter, and the suction port 21 of described Venturi meter connects the ozone gas outlet of ozonizer 22.
Described packing layer can be by the plastic filler ball of piling up, below the described plastic filler ball grid, orifice plate or the metal grill that is used to support these filling balls, the top of plastic filler ball does not have shelter, the water-in of described Aerobic Pond is positioned at the below of described packing layer, water outlet is positioned at the top of described packing layer, when water flowed from bottom to top, described plastic filler ball was in half suspended state.
The static piling height of described baton round filler is preferably the 40-60% of described Aerobic Pond projected depth.
Described Aerobic Pond bottom can be provided with some aerators or ventage 13, described aerator or ventage are connected with compressed air line or Fan pipeline, and described preaerator (can adopt aerator or ventage structure) also connects described compressed air line or Fan pipeline.
Be provided with sedimentation in the described inclined-plate clarifying basin and make up 17 with swash plate.
Can be provided with the filtering layer 19 that is suspended from the middle part, pond in the described filtering basin, by more meticulous physical filtering, the contaminant filter that does not precipitate in the inclined-plate clarifying basin is fallen, to reduce influence to follow-up ozonize, save the ozonize cost, the water-in of described filtering basin is positioned at the below of described filtering layer, and water outlet is positioned at the top of described filtering layer, and the bottom, pond is provided with scrapes mud structure and sewage draining exit.
Tank in the middle of the back of described filtering basin can be connected with, the import of described pump by pipe connection described in the middle of tank so that stable water source is provided and avoids pump that filtering layer is disturbed for pump.
Described ozonize pond can be plug-flow pond 24, is distributed with one or more advection traverse baffles 23 or one or more vertical stream traverse baffle in the described plug-flow pond.
Claims (10)
1. sewage purification processing system, it is characterized in that comprising the settling pit that connects successively, equalizing tank, Aerobic Pond, inclined-plate clarifying basin, filtering basin and ozonize pond, described equalizing tank bottom is provided with preaerator, be provided with the packing layer that is suspended from the middle part, pond in the described Aerobic Pond, described ozone oxidation pond is the plug-flow pond, the suction culvert in described ozonize pond is provided with pump and the Venturi meter that complements one another, described pump outlet connects the import of described Venturi meter, the suction port of described Venturi meter connects the ozone gas outlet of ozonizer, described ozonizer adopts the plasma generator that is provided with the ozone-air outlet, described plasma body is furnished with the high voltagehigh frequency power source circuit, and the front portion or the front of described settling pit are provided with grid.
2. sewage purification processing system as claimed in claim 1 is characterized in that being distributed with in the described ozonize pond one or more advection traverse baffles or is distributed with one or more vertical stream flaps, and the rear portion, pond is provided with out water pump.
3. sewage purification processing system as claimed in claim 1 or 2, it is characterized in that described packing layer is by the plastic filler ball of piling up, below the described plastic filler ball grid, orifice plate or the metal grill that is used to support these filling balls, the top of plastic filler ball does not have shelter, the water-in of described Aerobic Pond is positioned at the below of described packing layer, and water outlet is positioned at the top of described packing layer.
4. sewage purification processing system as claimed in claim 3, the static piling height that it is characterized in that described baton round filler is the 40-60% of described Aerobic Pond projected depth.
5. sewage purification processing system as claimed in claim 4 is characterized in that described Aerobic Pond bottom is provided with some aerators or ventage, and described aerator or ventage are connected with compressed air line or Fan pipeline.
6. sewage purification processing system as claimed in claim 5 is characterized in that described preaerator also connects described compressed air line or Fan pipeline.
7. sewage purification processing system as claimed in claim 1 or 2 is characterized in that being provided with sedimentation in the described inclined-plate clarifying basin makes up with swash plate.
8. sewage purification processing system as claimed in claim 7 is characterized in that described inclined-plate clarifying basin bottom is provided with mud-scraping mechanism and sewage draining exit.
9. sewage purification processing system as claimed in claim 1 or 2 is characterized in that being provided with in the described filtering basin filtering layer that is suspended from the middle part, pond, and the water-in of described filtering basin is positioned at the below of described filtering layer, and water outlet is positioned at the top of described filtering layer.
10. sewage purification processing system as claimed in claim 1 or 2 is characterized in that the back of described filtering basin is connected with middle tank, and the import of described pump is by the described middle tank of pipe connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910085287A CN101638285A (en) | 2009-05-27 | 2009-05-27 | Sewage purification processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910085287A CN101638285A (en) | 2009-05-27 | 2009-05-27 | Sewage purification processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101638285A true CN101638285A (en) | 2010-02-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910085287A Pending CN101638285A (en) | 2009-05-27 | 2009-05-27 | Sewage purification processing system |
Country Status (1)
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| CN (1) | CN101638285A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101863595A (en) * | 2010-06-24 | 2010-10-20 | 河南科技大学 | Landscape type combined domestic sewage purification system |
| LT6095B (en) | 2013-02-25 | 2014-11-25 | Uab "Ekovalitas" | Drinking water and wastewater treatment method and device |
| CN104891738A (en) * | 2015-05-27 | 2015-09-09 | 广东梅雁吉祥水电股份有限公司 | Ecological treatment method of municipal sewage |
| CN105107249A (en) * | 2015-09-07 | 2015-12-02 | 赵媛媛 | Sewage purification treatment system |
| CN112142258B (en) * | 2020-09-18 | 2023-02-10 | 中国科学院城市环境研究所 | Resource and standard treatment method for domestic sewage of villages and towns |
-
2009
- 2009-05-27 CN CN200910085287A patent/CN101638285A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101863595A (en) * | 2010-06-24 | 2010-10-20 | 河南科技大学 | Landscape type combined domestic sewage purification system |
| CN101863595B (en) * | 2010-06-24 | 2011-11-23 | 河南科技大学 | Landscape type combined domestic sewage purification system |
| LT6095B (en) | 2013-02-25 | 2014-11-25 | Uab "Ekovalitas" | Drinking water and wastewater treatment method and device |
| CN104891738A (en) * | 2015-05-27 | 2015-09-09 | 广东梅雁吉祥水电股份有限公司 | Ecological treatment method of municipal sewage |
| CN105107249A (en) * | 2015-09-07 | 2015-12-02 | 赵媛媛 | Sewage purification treatment system |
| CN105107249B (en) * | 2015-09-07 | 2017-01-18 | 盛世园林集团股份有限公司 | Sewage purification treatment system |
| CN112142258B (en) * | 2020-09-18 | 2023-02-10 | 中国科学院城市环境研究所 | Resource and standard treatment method for domestic sewage of villages and towns |
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Application publication date: 20100203 |