CN204981495U - High -concentration organic wastewater treatment device - Google Patents
High -concentration organic wastewater treatment device Download PDFInfo
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- CN204981495U CN204981495U CN201520527229.0U CN201520527229U CN204981495U CN 204981495 U CN204981495 U CN 204981495U CN 201520527229 U CN201520527229 U CN 201520527229U CN 204981495 U CN204981495 U CN 204981495U
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- treating pond
- cylindrical shell
- treatment device
- wastewater treatment
- organic wastewater
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a high -concentration organic wastewater treatment device, handle the pond including first processing pond and second, first processing pond water inlet is equipped with the ozone oxidation subassembly, the ozone oxidation subassembly includes the barrel, the position that the barrel lateral wall is close to the top is equipped with the inlet tube, the barrel bottom is equipped with ozone generator, the top surface middle part is equipped with the (mixing) shaft by motor drive in the barrel, be equipped with stirring vane on the (mixing) shaft, stirring vane is two sets of, wherein a set of stirring vane is straight paddle, the stirring vane of another group is the arc paddle, barrel top both sides are equipped with ultraviolet tube respectively and the pipe is added to the catalyst. The utility model discloses an effectual processing is carried out to organic waste water to electrode treatment, ozone treatment and microorganism tertiary treatment's mode.
Description
Technical field
The utility model belongs to field of environment protection equipment, is specifically related to a kind of high-concentration organic wastewater treatment device.
Background technology
Organic wastewater with difficult degradation thereby COD is higher, and generally all at more than 2000mg/L, and its biodegradability is lower, and BOD/COD value is generally all even lower below 0.3, so be difficult to directly utilize biological process to be reduced by its COD.At present, conventional administering method has coagulant sedimentation, absorption method and Fenton reagent method etc.These methods can improve the biodegradability of used water difficult to degradate to a certain extent, and can reduce its COD concentration.But also there is following shortcoming: running cost is high, effluent quality is unstable, needing combines to apply with other further treatment technique just can reach emission standard, cannot meet reuse water requirement, and level of automation is low.Therefore, need now a kind of can effectively to the equipment that organic waste water processes, to reach better treatment effect.
Utility model content
Technical problem to be solved in the utility model is for above-mentioned the deficiencies in the prior art, provides a kind of high-concentration organic wastewater treatment device, by the mode of Electrode treatment, ozonize and microorganism tertiary treatment, effectively processes organic waste water.
The technical scheme that the utility model adopts is: a kind of high-concentration organic wastewater treatment device, comprise the first treating pond and the second treating pond, described first treating pond water-in is provided with ozone oxidation assembly, described ozone oxidation assembly comprises cylindrical shell, described cylindrical shell outer side wall is provided with water inlet pipe near the position at top, described cylinder body bottom is provided with ozonizer, be provided with in the middle part of described cylindrical shell inner top surface by motor-driven stir shaft, described stir shaft is provided with agitating vane, described agitating vane is two groups, described wherein one group of agitating vane is straight blade, another group agitating vane described is arc blade, both sides, described cylindrical shell top are respectively equipped with quartz burner and catalyzer adds pipe, described first treating pond bottom surface is provided with aerator, be respectively equipped with by the plate electrode of supply lead ground connection and the pin electrode that is connected with the high-voltage pulse power source being arranged at the first treating pond outer side wall in described cylindrical shell, described first treating pond top is provided with quartz burner, described first treating pond outer side wall is connected with the second biochemistry pool by pipe connecting near the position of bottom, described pipe connecting is respectively equipped with sewage sampling mouth and under meter, described second biochemistry pool inner top is provided with several pasture and water plantation bar, the side that described second biochemistry pool is relative with pipe connecting is provided with return line and rising pipe successively near the position of bottom, the described return line the other end is communicated with the first treating pond, described rising pipe is provided with activated carbon filter component and membrane filtration module successively.
As preferably, described two groups of agitating vanes are stretching structure.
As preferably, described catalyzer enters pipe and is provided with lid.
As preferably, described activated carbon filter component is the three layers of activated charcoal strainer be sealedly attached in housing, and described three layers of activated charcoal strainer thickness are 2cm.
As preferably, described membrane filtration module is the trilamellar membrane filtering net be sealedly attached in housing, and described trilamellar membrane filtering net thickness is 2cm.
The beneficial effects of the utility model are: by the plate electrode in ozone oxidation assembly, the first treating pond and pin electrode and the second treating pond pasture and water plantation bar with the use of, the process of three grades can be carried out to organic waste water, ensure process effect.Activated carbon filter component and membrane filtration module carry out filtration again to the water after process, increase the effect of filtering.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1, the first treating pond; 2, the second treating pond; 3, cylindrical shell; 4, water inlet pipe; 5, ozonizer; 6, motor; 7, stir shaft; 8, agitating vane; 9, quartz burner; 10, catalyzer adds pipe; 11, aerator; 12, plate electrode; 13, high-voltage pulse power source; 14, pin electrode; 15, pipe connecting; 16, sewage sampling mouth; 17, under meter; 18, pasture and water plantation bar; 19, return line; 20, rising pipe; 21, activated carbon filter component; 22, membrane filtration module; 23, lid.
Embodiment
Below in conjunction with the accompanying drawings and the specific embodiments the utility model is described in further detail.
As shown in Figure 1, a kind of high-concentration organic wastewater treatment device, comprise the first treating pond 1 and the second treating pond 2, described first treating pond 1 water-in is provided with ozone oxidation assembly, described ozone oxidation assembly comprises cylindrical shell 3, described cylindrical shell 3 outer side wall is provided with water inlet pipe 4 near the position at top, ozonizer 5 is provided with bottom described cylindrical shell 3, the stir shaft 7 driven by motor 6 is provided with in the middle part of described cylindrical shell 3 inner top surface, described stir shaft 7 is provided with agitating vane 8, described agitating vane 8 is two groups, described wherein one group of agitating vane 8 is straight blade, another group agitating vane 8 described is arc blade, both sides, described cylindrical shell 3 top are respectively equipped with quartz burner 9 and catalyzer adds pipe 10, described first treating pond 1 bottom surface is provided with aerator 11, be respectively equipped with by the plate electrode 12 of supply lead ground connection and the pin electrode 14 that is connected with the high-voltage pulse power source 13 being arranged at the first treating pond 1 outer side wall in described cylindrical shell 3, described first treating pond 1 top is provided with quartz burner 9, described first treating pond 1 outer side wall is connected with the second biochemistry pool by pipe connecting 15 near the position of bottom, described pipe connecting 15 is respectively equipped with sewage sampling mouth 16 and under meter 17, described second biochemistry pool inner top is provided with several pasture and water plantation bar 18, the side that described second biochemistry pool is relative with pipe connecting 15 is provided with return line 19 and rising pipe 20 successively near the position of bottom, described return line 19 the other end is communicated with the first treating pond 1, described rising pipe 20 is provided with successively activated carbon filter component 21 and membrane filtration module 22.
In the present embodiment, described two groups of agitating vanes 8 are stretching structure.
In the present embodiment, described catalyzer adds pipe 10 and is provided with lid 23.
In the present embodiment, described activated carbon filter component 21 is for being sealedly attached to three layers of activated charcoal strainer in housing, and described three layers of activated charcoal strainer thickness are 2cm.
In the present embodiment, described membrane filtration module 22 is for being sealedly attached to the trilamellar membrane filtering net in housing, and described trilamellar membrane filtering net thickness is 2cm.
During present treatment equipment work, organic sewage enters in the cylindrical shell 3 of ozone oxidation assembly by water inlet pipe 4, and ozonizer 5 works, and adding pipe 10 from catalyzer adds the catalyzer such as titanium dioxide simultaneously.Motor 6 works, and drive stir shaft 7 to rotate, stir shaft 7 drives agitating vane 8 to rotate, and stirs the water in cylindrical shell 3.In addition, be used as the energy derive of chemical reaction with the energy of quartz burner 9 in the process of reaction, accelerated oxidation reduction reaction, make to be adsorbed on the ozone on surface and water molecules to be excited into and to have active OH-free radical, all organic substances to human body or bad environmental of the extremely strong almost separable solution of free radical of these oxidizing powers and part inorganic substance.
After coagulation completes, organic sewage enters the first treating pond 1, pin electrode 14 is in addition after high pressure, multiple plasma channel is propagated from pin electrode 14 to flat board, electronics obtains energy from electric field simultaneously, excites other molecules, impels organism to excite cracking or ionization, high-voltage pulse power source 13 in the present embodiment adopts repetition rate to be 0-800Hz, and amplitude is ± high-voltage pulse power source 13 of 20Hz.
After second-stage treatment completes, organic sewage enters the second treating pond 2.On pasture and water plantation bar 18 in second treating pond 2, the pasture and water of plantation energy separate absorbent objectionable impurities, carry out tertiary treatment to organic sewage.By activated carbon filter component 21 and membrane filtration module 22, the water after process is further filtered again after tertiary treatment, increase the effect of filtering.
Claims (5)
1. a high-concentration organic wastewater treatment device, it is characterized in that: comprise the first treating pond (1) and the second treating pond (2), described first treating pond (1) water-in is provided with ozone oxidation assembly, described ozone oxidation assembly comprises cylindrical shell (3), described cylindrical shell (3) outer side wall is provided with water inlet pipe (4) near the position at top, described cylindrical shell (3) bottom is provided with ozonizer (5), the stir shaft (7) driven by motor (6) is provided with in the middle part of described cylindrical shell (3) inner top surface, described stir shaft (7) is provided with agitating vane (8), described agitating vane (8) is two groups, described wherein one group of agitating vane (8) is straight blade, another group agitating vane (8) described is arc blade, described cylindrical shell (3) both sides, top are respectively equipped with quartz burner (9) and catalyzer adds pipe (10), described first treating pond (1) bottom surface is provided with aerator (11), be respectively equipped with by the plate electrode (12) of supply lead ground connection and the pin electrode (14) that is connected with the high-voltage pulse power source (13) being arranged at the first treating pond (1) outer side wall in described cylindrical shell (3), described first treating pond (1) top is provided with quartz burner (9), described first treating pond (1) outer side wall is connected with the second biochemistry pool by pipe connecting (15) near the position of bottom, described pipe connecting (15) is respectively equipped with sewage sampling mouth (16) and under meter (17), described second biochemistry pool inner top is provided with several pasture and water plantation bar (18), the side that described second biochemistry pool is relative with pipe connecting (15) is provided with return line (19) and rising pipe (20) successively near the position of bottom, described return line (19) the other end is communicated with the first treating pond (1), described rising pipe (20) is provided with successively activated carbon filter component (21) and membrane filtration module (22).
2. high-concentration organic wastewater treatment device according to claim 1, is characterized in that: described two groups of agitating vanes (8) are stretching structure.
3. high-concentration organic wastewater treatment device according to claim 1 and 2, is characterized in that: described catalyzer adds pipe (10) and is provided with lid (23).
4. high-concentration organic wastewater treatment device according to claim 1 and 2, it is characterized in that: described activated carbon filter component (21) is for being sealedly attached to three layers of activated charcoal strainer in housing, and described three layers of activated charcoal strainer thickness are 2cm.
5. high-concentration organic wastewater treatment device according to claim 1 and 2, is characterized in that: described membrane filtration module (22) is for being sealedly attached to the trilamellar membrane filtering net in housing, and described trilamellar membrane filtering net thickness is 2cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520527229.0U CN204981495U (en) | 2015-07-20 | 2015-07-20 | High -concentration organic wastewater treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520527229.0U CN204981495U (en) | 2015-07-20 | 2015-07-20 | High -concentration organic wastewater treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204981495U true CN204981495U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520527229.0U Expired - Fee Related CN204981495U (en) | 2015-07-20 | 2015-07-20 | High -concentration organic wastewater treatment device |
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| CN (1) | CN204981495U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630278A (en) * | 2016-12-14 | 2017-05-10 | 郑州游爱网络技术有限公司 | Reverse osmosis disinfection plant for water supply equipment |
| CN108955796A (en) * | 2018-07-11 | 2018-12-07 | 西安交通大学 | One seed channel Flow Sampling Device and method |
-
2015
- 2015-07-20 CN CN201520527229.0U patent/CN204981495U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630278A (en) * | 2016-12-14 | 2017-05-10 | 郑州游爱网络技术有限公司 | Reverse osmosis disinfection plant for water supply equipment |
| CN106630278B (en) * | 2016-12-14 | 2019-08-16 | 济南一杯水环保科技有限公司 | A kind of reverse osmosis sterilizer of supply equipment |
| CN108955796A (en) * | 2018-07-11 | 2018-12-07 | 西安交通大学 | One seed channel Flow Sampling Device and method |
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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: 20160120 Termination date: 20160720 |