CN204897653U - Rubber effluent disposal system - Google Patents
Rubber effluent disposal system Download PDFInfo
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- CN204897653U CN204897653U CN201520602605.8U CN201520602605U CN204897653U CN 204897653 U CN204897653 U CN 204897653U CN 201520602605 U CN201520602605 U CN 201520602605U CN 204897653 U CN204897653 U CN 204897653U
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- sewage
- tank
- pond
- settling tank
- ammonia nitrogen
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Abstract
The utility model discloses a rubber effluent disposal system, include: sewage import, the grid, the equalizing basin, the reaction tank, sedimentation tank no. 1, the anaerobism pond, the biology pond of hydrolysising, the oxidation pond, sedimentation tank no. 2, middle pond, deamination nitrogen ware, carbon filter, clean water basin, sludge tihckener, each component parts pass through the conduit flow waterline connect as an organic whole, the utility model discloses a biochemical treatment and materialization are handled and are combined together, and the treatment effect is good, and the working costs is low, and the mud volume is few, has the better effect of getting rid of to the ammonia nitrogen pollutant.
Description
Technical field
The utility model relates to water treatment field, particularly relates to a kind of Rubber Industrial Wastewater treatment system.
Background technology
Along with the development of social productive forces, water resources more and more lacks, water saving, effluent cycle utilization is an important topic of current social development, also be the effective ways of social sustainable development, the waste water discharged in rubber production contains the organic wastewater such as ammonia, nitrogen, CODcr, BOD5, the waste water discharged in the sewage source water production process that mainly rubber production is used, containing organism and mineral compound in waste water, and poisonous and hazardous material, directly enter rivers if not treated, serious water pollutions and problem of environmental pollution certainly will be caused.For this reason, the utility model provides a kind of Rubber Industrial Wastewater treatment system, and system architecture is simple, is applicable to the sewage purification recycling of each enterprise in rubber industry.
Utility model content
The technical problem that the utility model mainly solves is to provide a kind of Rubber Industrial Wastewater treatment system, the recycle of sewage can be realized, environmental protect simultaneously, solve the problem in short supply of water resources, meanwhile, the wastewater treatment of a kind of Rubber Industrial Wastewater of the utility model treatment system can reach national associated emission standard.
Described a kind of Rubber Industrial Wastewater treatment system, comprise: wastewater inlet, grid, equalizing tank, reaction tank, settling tank one, anaerobic pond, biological hydrolysis pond, oxidation pond, settling tank two, intermediate pool, ammonia nitrogen removal device, carbon filter, clean water basin, sludge thickener, each integral part is connected as one by Pipeline, wherein on described reaction tank, be connected with medicine machine, described oxidation pond connects and is provided with blower fan, sewage enters from wastewater inlet, discharged or recovery by light-water pond relief outlet through process, in sewage treatment process, the mud that ammonia nitrogen removal device and carbon filter produce enters into sludge thickener, in sludge thickener after pressure filter press filtration, carry out dewatered sludge outward transport process.
Wherein, described grid is pretreatment pool equipment, adopts brick mix structure, removes oarse-grained silt, impurity and domestic refuse, the fine particle of flocculation agent is removed simultaneously.
Described grid is connected to equalizing tank, and sewage, after grid process, enters equalizing tank, described equalizing tank adopts underground type skeleton construction, and useful volume 600 cubic metres, passes through equalizing tank, sewage energy fully Balance Water Quality, the water yield, makes sewage more evenly can enter subsequent processing units.
A kind of optimization technique side ammonia, is provided with submersible stirring pump or aeration tube, prevents deposited phenomenon in described equalizing tank.
Described equalizing tank is connected to reaction tank, and sewage, after equalizing tank, enters into reaction tank, described reaction tank is the most important integral part of the utility model, and the useful volume of reaction tank 140 cubic metres, in described reaction tank, add flocculation agent or alkali lye, make sewage react coacervation.
Described reaction tank is connected to settling tank one, and sewage enters into settling tank one after reaction tank, and described settling tank one is materializing strategy pond, adopts intermediate processing, sewage is separated.
Described settling tank one is connected to anaerobic pond, sewage enters anaerobic pond and carries out anaerobic treatment, sewage decomposes organic phosphorus content in the ammonia nitrogen removed in sewage, CODcr, BOD and degradation of sewage under effect anerobe of the process of anaerobism, sewage is made to obtain rough purification, sewage through anaerobic pond enters biological hydrolysis pond, sewage enters acidication in biological hydrolysis pond, and reduce the harmful organic substances such as ammonia nitrogen in sewage, phosphorus, sulphur, the sewage after acidication enters oxidation pond.
Described oxidation pond, adopt aerobic activated sludge biological method process organic sewage, in aeration oxygen supply, ensure certain pH value and temperature and nutritive salt is provided state under, the diversified microorganism composition such as the bacterium in water, Mycophyta, protozoa and small metazoan zoogloea, in water, dissolved organic matter is absorbed by bacterium (or Mycophyta) cell walls and infiltrates in cell paste, and under endoenzyme effect, biochemical reaction generates CO
2, H
2o, P
4o
3-, SO
4 2-, NO
3-deng inorganics.Sewage decomposes and organism composition in degradation of sewage under the effect of aerobic bacteria, and sewage is purified further.
Sewage after oxidation pond, enter into settling tank two, described settling tank two adopts underground type skeleton construction, useful volume 300 cubic metres, PAM medicament is added, the oxide film coacervation precipitation that the subparticle in sewage, impurity foreign material and oxidation pond are come off in settling tank.
Sewage after settling tank two enters into intermediate pool.
A kind of optimal technical scheme, described intermediate pool adopts underground type skeleton construction, useful volume 180 cubic metres.
Described intermediate pool is connected to ammonia nitrogen removal device, by being connected to carbon filter after ammonia nitrogen removal device, to ensure that in waste water, ammonia-nitrogen content is lower than emission standard.
Through the water of carbon filter, be connected to clean water basin, the water of clean water basin, through detecting, can realize sewage and reclaim or discharge.
Meanwhile, at described ammonia nitrogen removal device, carbon filter is connected to sludge thickener, and sludge thickener is concentrated sludge press filtration by pressure filter, then carries out dewatered sludge outward transport process.
The beneficial effects of the utility model are: a kind of Rubber Industrial Wastewater treatment system of the utility model, waste water adopts biochemical treatment and materializing strategy to combine, treatment effect is good, working cost is low, sludge quantity is few, effectively remove the organic pollutant in waste water, to ammonia nitrogen pollutant, there is good removal effect.
Accompanying drawing explanation
Fig. 1 is a kind of Rubber Industrial Wastewater treatment system of the utility model one-piece construction schematic diagram.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail, to make advantage of the present utility model and feature can be easier to be readily appreciated by one skilled in the art, thus more explicit defining is made to protection domain of the present utility model.
Refer to Fig. 1,
Described a kind of Rubber Industrial Wastewater treatment system, comprise: wastewater inlet, grid, equalizing tank, reaction tank, settling tank one, anaerobic pond, biological hydrolysis pond, oxidation pond, settling tank two, intermediate pool, ammonia nitrogen removal device, carbon filter, clean water basin, sludge thickener, each integral part is connected as one by Pipeline, wherein on described reaction tank, be connected with medicine machine, described oxidation pond connects and is provided with blower fan, sewage enters from wastewater inlet, discharged or recovery by light-water pond relief outlet through process, in sewage treatment process, the mud that ammonia nitrogen removal device and carbon filter produce enters into sludge thickener, in sludge thickener after pressure filter press filtration, carry out dewatered sludge outward transport process.
Wherein, described grid is pretreatment pool equipment, adopts brick mix structure, removes oarse-grained silt, impurity and domestic refuse, the fine particle of flocculation agent is removed simultaneously.
Described grid is connected to equalizing tank, and sewage, after grid process, enters equalizing tank, described equalizing tank adopts underground type skeleton construction, and useful volume 600 cubic metres, passes through equalizing tank, sewage energy fully Balance Water Quality, the water yield, makes sewage more evenly can enter subsequent processing units.
A kind of optimization technique side ammonia, is provided with submersible stirring pump or aeration tube, prevents deposited phenomenon in described equalizing tank.
Described equalizing tank is connected to reaction tank, and sewage, after equalizing tank, enters into reaction tank, described reaction tank is the most important integral part of the utility model, and the useful volume of reaction tank 140 cubic metres, in described reaction tank, add flocculation agent or alkali lye, make sewage react coacervation.
Described reaction tank is connected to settling tank one, and sewage enters into settling tank one after reaction tank, and described settling tank one is materializing strategy pond, adopts intermediate processing, sewage is separated.
Described settling tank one is connected to anaerobic pond, sewage enters anaerobic pond and carries out anaerobic treatment, sewage decomposes organic phosphorus content in the ammonia nitrogen removed in sewage, CODcr, BOD and degradation of sewage under effect anerobe of the process of anaerobism, sewage is made to obtain rough purification, sewage through anaerobic pond enters biological hydrolysis pond, sewage enters acidication in biological hydrolysis pond, and reduce the harmful organic substances such as ammonia nitrogen in sewage, phosphorus, sulphur, the sewage after acidication enters oxidation pond.
Described oxidation pond, adopt aerobic activated sludge biological method process organic sewage, in aeration oxygen supply, ensure certain pH value and temperature and nutritive salt is provided state under, the diversified microorganism composition such as the bacterium in water, Mycophyta, protozoa and small metazoan zoogloea, in water, dissolved organic matter is absorbed by bacterium (or Mycophyta) cell walls and infiltrates in cell paste, and under endoenzyme effect, biochemical reaction generates CO
2, H
2o, P
4o
3-, SO
4 2-, NO
3-deng inorganics.Sewage decomposes and organism composition in degradation of sewage under the effect of aerobic bacteria, and sewage is purified further.
Sewage after oxidation pond, enter into settling tank two, described settling tank two adopts underground type skeleton construction, useful volume 300 cubic metres, PAM medicament is added, the oxide film coacervation precipitation that the subparticle in sewage, impurity foreign material and oxidation pond are come off in settling tank.
Sewage after settling tank two enters into intermediate pool.
A kind of optimal technical scheme, described intermediate pool adopts underground type skeleton construction, useful volume 180 cubic metres.
Described intermediate pool is connected to ammonia nitrogen removal device, by being connected to carbon filter after ammonia nitrogen removal device, to ensure that in waste water, ammonia-nitrogen content is lower than emission standard.
Through the water of carbon filter, be connected to clean water basin, the water of clean water basin, through detecting, can realize sewage and reclaim or discharge.
Meanwhile, at described ammonia nitrogen removal device, carbon filter is connected to sludge thickener, and sludge thickener is concentrated sludge press filtration by pressure filter, then carries out dewatered sludge outward transport process.
The foregoing is only embodiment of the present utility model; not thereby the scope of the claims of the present utility model is limited; every utilize the utility model specification sheets and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present utility model.
Claims (3)
1. a Rubber Industrial Wastewater treatment system, it is characterized in that, comprise: wastewater inlet, grid, equalizing tank, reaction tank, settling tank one, anaerobic pond, biological hydrolysis pond, oxidation pond, settling tank two, intermediate pool, ammonia nitrogen removal device, carbon filter, clean water basin, sludge thickener, each integral part is connected as one by Pipeline, wherein on described reaction tank, be connected with medicine machine, described oxidation pond connects and is provided with blower fan, sewage enters from wastewater inlet, discharge through process by clean water basin relief outlet or reclaim, wherein, described grid is pretreatment pool equipment, adopt brick mix structure, remove oarse-grained silt, impurity and domestic refuse, described grid is connected to equalizing tank, described equalizing tank adopts underground type skeleton construction, described equalizing tank is connected to reaction tank, sewage is after equalizing tank, enter into reaction tank, reaction tank is connected to settling tank one, described settling tank one is materializing strategy pond, described settling tank one is connected to anaerobic pond, sewage enters anaerobic pond and carries out anaerobic treatment, sewage after acidication enters oxidation pond, described oxidation pond, adopt aerobic activated sludge biological method process organic sewage, sewage after oxidation pond, enter into settling tank two, described settling tank two adopts underground type skeleton construction, sewage after settling tank two enters into intermediate pool, described intermediate pool is connected to ammonia nitrogen removal device, by being connected to carbon filter after ammonia nitrogen removal device, through the water of carbon filter, be connected to clean water basin, simultaneously, at described ammonia nitrogen removal device, carbon filter is connected to sludge thickener.
2. Rubber Industrial Wastewater treatment system according to claim 1, is characterized in that, is provided with submersible stirring pump or aeration tube in described equalizing tank.
3. Rubber Industrial Wastewater treatment system according to claim 1, is characterized in that, described intermediate pool adopts underground type skeleton construction, useful volume 180 cubic metres.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520602605.8U CN204897653U (en) | 2015-08-12 | 2015-08-12 | Rubber effluent disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520602605.8U CN204897653U (en) | 2015-08-12 | 2015-08-12 | Rubber effluent disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204897653U true CN204897653U (en) | 2015-12-23 |
Family
ID=54919845
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520602605.8U Expired - Fee Related CN204897653U (en) | 2015-08-12 | 2015-08-12 | Rubber effluent disposal system |
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| CN (1) | CN204897653U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108706816A (en) * | 2018-05-07 | 2018-10-26 | 苏州亚得宝消防设备有限公司 | A kind of house refuse sewage treatment process |
-
2015
- 2015-08-12 CN CN201520602605.8U patent/CN204897653U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108706816A (en) * | 2018-05-07 | 2018-10-26 | 苏州亚得宝消防设备有限公司 | A kind of house refuse sewage treatment process |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151223 Termination date: 20170812 |