CN203498223U - Ozone wastewater treatment system - Google Patents
Ozone wastewater treatment system Download PDFInfo
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- CN203498223U CN203498223U CN201320531552.6U CN201320531552U CN203498223U CN 203498223 U CN203498223 U CN 203498223U CN 201320531552 U CN201320531552 U CN 201320531552U CN 203498223 U CN203498223 U CN 203498223U
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- ozone
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- ozonize
- treatment
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Abstract
The utility model discloses an ozone wastewater treatment system, comprising an upflow anaerobic sludge blanket (UASB) treatment module and an ozone treatment module, wherein the UASB treatment module comprises a UASB; one end of the UASB is connected with one end of a regulating reservoir; the other end of the regulating reservoir is connected with a sewage tank; the other end of the UASB is connected with one end of a secondary sedimentation tank; a sludge discharge hole of the UASB is connected with a sludge intake tank; the ozone treatment module comprises an ozone treatment pond; one end of the ozone treatment pond is connected with one end of the regulating reservoir; the other end of the regulating reservoir is connected with the sewage tank; an air inlet of the ozone treatment pond is connected with an ozone generator; the other end of the ozone treatment pond is connected with the secondary sedimentation tank; a tail gas discharge hole of the ozone treatment pond is connected with a tail gas treatment device. The ozone wastewater treatment system has the significant advantages that the ozone oxidation treatment wastewater is combined with the UASB treatment wastewater, various pollutants can be degraded into carbon dioxide and water, the purification effect is excellent, and the ozone oxidation wastewater is mixed with low-concentration wastewater subjected to UASB treatment, so that the target of recovering and utilizing the wastewater is achieved.
Description
Technical field
The utility model relates to a kind of Waste Water Treatment, particularly a kind of Waste Water Treatment that utilizes ozone.
Background technology
Now, the treatment process of industry, sanitary wastewater mainly contains biological clarification, physical filtering method etc., and object is in order to purify liquid waste, and can reuse, and reaches the target of environmental protection and energy saving.Ozone has strong oxidizing property, and be widely used in sterilizing, bleaching, catalysis etc., ozone also can apply to field of waste water treatment, because it has strong oxidizing property, ozone can be carbonic acid gas and water by the contaminant degradation in waste water, reach the object of water purification, and ozone high grade oxidation technology is the combination based on ozone oxidation and other water treatments.
Have patent to disclose ozone oxidation and be combined to process waste water with gac, but this technology is being applied to also there is certain defect aspect large-scale wastewater treatment, and decontamination effect improving also needs to be further improved.How will produce on a large scale ozone and by ozonize and the organic combination of other wastewater treatments, and reach the unusual effect of purification of waste water, be to have problem to be solved.
Utility model content
For solving the deficiencies in the prior art, the purpose of this utility model is to provide a kind of ozone Waste Water Treatment, and this system is combined ozone to carry out wastewater treatment with upflow anaerobic sludge blanket process UASB, good purification, and efficiency is high.
In order to realize above-mentioned target, the utility model adopts following technical scheme:
An ozone Waste Water Treatment, is characterized in that, comprises UASB processing module and ozonize module, and UASB processing module is connected by connecting tube with the terminal of ozonize module.
A kind of ozone Waste Water Treatment, it is characterized in that, described UASB processing module comprises UASB, UASB one end is connected with sewage pump one end by connecting tube, the sewage pump the other end is connected with equalizing tank one end by connecting tube, the equalizing tank the other end is connected with sewage lagoon by connecting tube, the UASB the other end is connected with second pond one end by connecting tube, the mud relief outlet of UASB enters pond by pipeline and mud and is connected, UASB is connected with water seal one end by pipe connecting, and the water seal the other end is connected with water inlet pipe.
A kind of ozone Waste Water Treatment, it is characterized in that, described ozonize module comprises ozonize pond, one end, ozonize pond is connected with sewage pump one end by connecting tube, the sewage pump the other end is connected with equalizing tank one end by connecting tube, the equalizing tank the other end is connected with sewage lagoon by connecting tube, ozonize pond ozone inlet mouth is connected with ozone generating-device by pipeline, the ozonize pond the other end is connected with second pond by pipeline, ozonize pond exhaust port is connected with exhaust gas processing device by pipeline, the ozonize pond discharge outlet of purifying waste water is connected with purification water pool by pipeline.
A kind of ozone Waste Water Treatment, it is characterized in that, between described UASB and second pond, be also provided with drip bed and pump well, UASB is connected with an one end of dripping by pipeline, a other end that drips is connected with pump well one end by pipeline, and the pump well the other end is connected with second pond by pipeline.
An ozone Waste Water Treatment, is characterized in that, described ozone generating-device shell is stainless steel.
An ozone Waste Water Treatment, is characterized in that, the discharge cell of described ozone generating-device is provided with independently safety interlock.
An ozone Waste Water Treatment, is characterized in that, described ozone tail gas concentration is below 0.015ppm.
Usefulness of the present utility model is: 1. waste water treatment by ozone oxidation is processed to waste water with UASB and combine, can form the extremely strong hydroxyl radical free radical of oxidizing power, making various contaminant degradations is carbonic acid gas and water, and purifying water effect is remarkable; 2. after the low concentration wastewater after the waste water after ozone oxidation being processed with UASB mixes, adopt again contact oxidation technology to process, effectively utilize physics, chemistry, biological method to carry out wastewater treatment, reduce and pollute, reach the object of waste water reclamation, utilization.
Accompanying drawing explanation
Fig. 1 is schematic flow sheet of the present utility model.
The implication of Reference numeral in figure: 1. sewage lagoon, 2. equalizing tank, 3. sewage pump, 4.UASB, 5. mud enters pond, 6. water seal, 7. water inlet pipe, 8. pump well, 9. second pond, 10. ozone generating-device, 11. ozonize ponds, 12. exhaust gas processing devices, 13. purification water pools.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is done to concrete introduction.
In conjunction with Fig. 1, a kind of ozone Waste Water Treatment, comprises UASB processing module and ozonize module, and UASB processing module is connected by connecting tube with the terminal of ozonize module.
Described UASB processing module comprises UASB4, UASB4 one end is connected with sewage pump 3 one end by connecting tube, sewage pump 3 the other ends are connected with equalizing tank 2 one end by connecting tube, equalizing tank 2 the other ends are connected with sewage lagoon 1 by connecting tube, sewage in sewage lagoon 1 flows into equalizing tank 2 by sewage pump 3, and after overregulating, sewage flows into UASB4; The UASB4 the other end is connected with pump well 8 one end by connecting tube, pump well 8 the other ends are connected with second pond 9 one end, the mud relief outlet of UASB4 enters pond 5 by pipeline and mud and is connected, UASB4 is connected with water seal 6 one end by pipe connecting, water seal 6 the other ends are connected with water inlet pipe 7, after flowing into the bed that drips after the deposition of sewage by UASB4, flow into pump well, finally flow into second pond.
Described ozonize module comprises ozonize pond 11,11 one end, ozonize pond are connected with sewage pump 3 one end by connecting tube, sewage pump 3 the other ends are connected with equalizing tank 2 one end by connecting tube, equalizing tank 2 the other ends are connected with sewage lagoon 1 by connecting tube, sewage in sewage lagoon 1 flows into equalizing tank 2 by sewage pump 3, and after overregulating, sewage flows into ozonize pond 11; Ozonize pond 11 ozone inlet mouths are connected with ozone generating-device 10 by pipeline, and ozonize pond 11 the other ends are connected with second pond 9 by pipeline, and sewage, through the oxygenolysis of ozone in ozonize pond 11, mixes with low concentration wastewater in second pond afterwards; Ozonize pond 11 exhaust ports are connected with exhaust gas processing device 12 by pipeline, and ozonize pond 11 discharge outlet of purifying waste water is connected with purification water pool 13 by pipeline, and ozonize pond 11 mud discharging mouths enter pond 5 with mud and are connected; Ozone generating-device 10 can produce required ozone, thus the organism in effective degradation of sewage; Exhaust gas processing device 12 can destroy unnecessary ozone gas, reaches environmental protection object; The sewage mixing in ozonize pond 11 is processed, is flowed into purification water pool 13 after blowdown mud through UASB and ozone double, obtains the water that can reuse through purifying.
Described ozone generating-device 10 shells are stainless steel; The discharge cell of described ozone generating-device 10 is provided with independently safety interlock; Described ozone tail gas concentration is 0.013ppm.
Product of the present utility model has been produced and has been come into operation, respond well.
More than show and described ultimate principle of the present utility model, principal character and advantage.The technician of the industry should understand, and above-described embodiment does not limit the utility model in any form, and all employings are equal to replaces or technical scheme that the mode of equivalent transformation obtains, all drops in protection domain of the present utility model.
Claims (1)
1. an ozone Waste Water Treatment, is characterized in that, comprises UASB processing module and ozonize module, and UASB processing module is connected by connecting tube with the terminal of ozonize module; Described UASB processing module comprises UASB, UASB one end is connected with sewage pump one end by connecting tube, the sewage pump the other end is connected with equalizing tank one end by connecting tube, the equalizing tank the other end is connected with sewage lagoon by connecting tube, the UASB the other end is connected with second pond one end by connecting tube, the mud relief outlet of UASB enters pond by pipeline and mud and is connected, and UASB is connected with water seal one end by pipe connecting, and the water seal the other end is connected with water inlet pipe; Described ozonize module comprises ozonize pond, one end, ozonize pond is connected with sewage pump one end by connecting tube, the sewage pump the other end is connected with equalizing tank one end by connecting tube, the equalizing tank the other end is connected with sewage lagoon by connecting tube, ozonize pond ozone inlet mouth is connected with ozone generating-device by pipeline, the ozonize pond the other end is connected with second pond by pipeline, ozonize pond exhaust port is connected with exhaust gas processing device by pipeline, and the ozonize pond discharge outlet of purifying waste water is connected with purification water pool by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320531552.6U CN203498223U (en) | 2013-08-28 | 2013-08-28 | Ozone wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320531552.6U CN203498223U (en) | 2013-08-28 | 2013-08-28 | Ozone wastewater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203498223U true CN203498223U (en) | 2014-03-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320531552.6U Expired - Fee Related CN203498223U (en) | 2013-08-28 | 2013-08-28 | Ozone wastewater treatment system |
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| Country | Link |
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| CN (1) | CN203498223U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110776231A (en) * | 2019-09-25 | 2020-02-11 | 减一污泥处理技术(江苏)有限公司 | Preparation method of sludge reduction coupling enhanced nitrogen and phosphorus removal material |
-
2013
- 2013-08-28 CN CN201320531552.6U patent/CN203498223U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110776231A (en) * | 2019-09-25 | 2020-02-11 | 减一污泥处理技术(江苏)有限公司 | Preparation method of sludge reduction coupling enhanced nitrogen and phosphorus removal material |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140326 Termination date: 20140828 |
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| EXPY | Termination of patent right or utility model |