CN206570120U - A kind of high concentrated organic wastewater processing unit - Google Patents
A kind of high concentrated organic wastewater processing unit Download PDFInfo
- Publication number
- CN206570120U CN206570120U CN201720128661.1U CN201720128661U CN206570120U CN 206570120 U CN206570120 U CN 206570120U CN 201720128661 U CN201720128661 U CN 201720128661U CN 206570120 U CN206570120 U CN 206570120U
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- China
- Prior art keywords
- storehouse
- welded
- coal dust
- dilution
- dust absorption
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Abstract
The utility model discloses a kind of high concentrated organic wastewater processing unit, including filtering cabin, final coal dust absorption storehouse, delivery port, and water inlet, the filtering cabin side is welded with water inlet at top, by-pass filtration film is connected with respectively from the side close to water inlet inside the filtering cabin, secondary filtration film and three-stage filtration film, another side bottom of filtering cabin is welded by water pipe with the dilution side-lower of storehouse one, the dilution silo roof portion is welded with filler, dilution storehouse inner upper is welded with water tank, and it is threaded with several flush ports below water tank, the dilution storehouse other end is welded by welding water pipe with the primary coal dust absorption side-lower of storehouse one, by being welded below water pipe and oxidation catalysis storehouse below the primary coal dust absorption storehouse opposite side, the primary coal dust absorption storehouse welded by filtering cabin rear greatly reduces cost instead of activated carbon, and it can recycle as fuel.
Description
Technical field
The utility model is related to technical field of sewage, specially a kind of high concentrated organic wastewater processing unit.
Background technology
With industrial boom, the type and quantity of waste water rapidly increase, and the pollution to water body is also increasingly extensively and tight
Weight, threatens the health and safety of the mankind, because the composition of industrial wastewater is more complicated, some are also toxic, Industrial Wastewater Treatment ratio
Municipal sewage treatment is more difficult also more important, and high concentrated organic wastewater mainly has the characteristics that：One is that organic concentration is high,
COD is general in 2 000 more than mg/L, the even as high as tens of thousands of or even hundreds of thousands mg/L having, and comparatively, BOD is relatively low, a lot
Waste water BOD and COD ratio are less than 0.3, and two be complicated component, and Organic substance in water is given up with aromatic compound containing toxicant
Thing and heterocyclic compound are in the majority, more than contain sulfide, nitride, heavy metal and toxic organic compound, three be that colourity is high, there is different
Taste, some waste water give out pungent stench, are had undesirable effect to surrounding environment, and four be with strong acid and strong base.
Therefore the processing of high concentrated organic wastewater will be the medical ethics problem of wastewater treatment, and existing wastewater treatment is mostly
Directly using dilution oxidation, either just with charcoal absorption after dilution or using method as distillation burning method, for this
The method of purification of waste water plays in a little method medical courses in general institutes, and its cost is high or clean-up effect is not good, is extremely difficult to target, so
Needed for can not realizing existing production.
Utility model content
The purpose of this utility model is to provide a kind of high concentrated organic wastewater processing unit, to solve above-mentioned background technology
The problem of middle proposition.
To achieve the above object, the utility model provides following technical scheme：A kind of high concentrated organic wastewater processing unit,
Including adsorbing storehouse, delivery port including filtering cabin, dilution storehouse, primary coal dust absorption storehouse, oxidation catalysis storehouse, final coal dust and entering water
Mouthful, the filtering cabin side is welded with top inside water inlet, the filtering cabin to be distinguished from the side close to water inlet
By-pass filtration film, secondary filtration film and three-stage filtration film are connected with, another side bottom of filtering cabin passes through water pipe and dilution storehouse
One side-lower is welded, and the dilution silo roof portion is welded with filler, and dilution storehouse inner upper is welded with water tank, and water tank
Square thread is connected with several flush ports, and the dilution storehouse other end is by welding water pipe and the primary coal dust absorption side-lower of storehouse one
By being welded below water pipe and oxidation catalysis storehouse below welding, the primary coal dust absorption storehouse opposite side, the oxidation catalysis storehouse
Adsorbed and welded below storehouse by water pipe and final coal dust below opposite side, is welded with below the final coal dust absorption storehouse opposite side
Screen pack is all connected with inside delivery port, the primary coal dust absorption storehouse, oxidation catalysis storehouse and final coal dust absorption storehouse.
It is preferred that, the primary coal dust absorption storehouse, oxidation catalysis storehouse and final coal dust absorption storehouse lower inside are all welded with
Aerator.
It is preferred that, the flush port is injecting type flush port.
It is preferred that, all it is threaded with suction pump on the water pipe.
It is preferred that, it is threaded with outlet water control valve on the delivery port.
Compared with prior art, the beneficial effects of the utility model are：By filtering cabin by high concentrated organic wastewater
Floating object or the filtering of solid particle waste residue, while filtering cabin rear is welded with dilution storehouse so that high concentrated organic wastewater dilution side
Just subsequent treatment, the primary coal dust absorption storehouse welded by filtering cabin rear greatly reduces cost instead of activated carbon, and can
To recycle as fuel, the oxidation catalysis storehouse that storehouse rear is welded is adsorbed by primary coal dust so that organic matter passes through oxidation
Catalyzed conversion eliminates the organic matter in waste water so that high concentrated organic wastewater is preferably pre-processed.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Fig. 2 is schematic appearance of the present utility model.
In figure：1- filtering cabins；2- by-pass filtration films；3- secondary filtration films；4- three-levels cross film；5- dilutes storehouse；6- water tanks；7-
Flush port；8- filler；9- screen packs；10- primary coal dust absorption storehouse；11- oxidation catalysis storehouse；The final coal dust absorption storehouses of 12-；
13- outlet water control valves；14- delivery ports；15- aerators；16- suction pumps；17- water pipes；18- water inlets.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Fig. 1-2 is referred to, the utility model provides a kind of technical scheme：A kind of high concentrated organic wastewater processing unit, bag
Include filtering cabin 1, dilution storehouse 5, primary coal dust absorption storehouse 10, oxidation catalysis storehouse 11, final coal dust absorption storehouse 12, the and of delivery port 14
Water inlet 18, the side of filtering cabin 1 is welded with water inlet 18 at top, and the inside of filtering cabin 1 is from close to water inlet
18 side is connected with by-pass filtration film 2, secondary filtration film 3 and three-stage filtration film 4, another side bottom of the filtering cabin 1 respectively
Welded by water pipe 17 with the dilution side-lower of storehouse 5 one, the top of dilution storehouse 5 is welded with inside filler 8, the dilution storehouse 5
Top is welded with water tank 6, and the lower section of water tank 6 is threaded with several flush ports 7, and the other end of dilution storehouse 5 passes through welding
Pass through water pipe 17 below water pipe 17 and the primary coal dust absorption side-lower of storehouse 10 1 welding, the primary coal dust absorption opposite side of storehouse 10
Welded with the lower section of oxidation catalysis storehouse 11, storehouse 12 is adsorbed by water pipe 17 and final coal dust below the opposite side of oxidation catalysis storehouse 11
Lower section is welded, and delivery port 14, the primary coal dust absorption storehouse 10, oxygen are welded with below the final coal dust absorption opposite side of storehouse 12
Change and screen pack 9 is all connected with inside catalysis storehouse 11 and final coal dust absorption storehouse 12, the primary coal dust absorption storehouse 10, oxidation catalysis
Storehouse 11 and the final coal dust absorption lower inside of storehouse 12 are all welded with aerator 15, and the flush port 7 is injecting type flush port, institute
State and suction pump 16 is all threaded with water pipe 17, outlet water control valve 13 is threaded with the delivery port 14.
Operation principle：High concentrated organic wastewater is injected into filtering cabin 1 by water inlet 18 when using, filtered by second class
Film 2, secondary filtration film 3 and the filtration treatment of three-stage filtration film 4 by water pipe 17 imported into dilution storehouse 5 by flush port 7 wash by water it is dilute
After releasing, primary coal dust is imported into by water pipe 17 and adsorbed after the absorption of storehouse 10, oxidation catalysis storehouse is imported into through peroxide by water pipe 17
Change after catalytic treatment, imported into final coal dust absorption storehouse 12 and finally adsorbed by water pipe 17, obtain pretreated waste water.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of high concentrated organic wastewater processing unit, including filtering cabin（1）, dilution storehouse（5）, primary coal dust absorption storehouse（10）、
Oxidation catalysis storehouse（11）, final coal dust absorption storehouse（12）, delivery port（14）And water inlet（18）, it is characterised in that：The filtering
Storehouse（1）Side is welded with water inlet at top（18）, the filtering cabin（1）Internal certainly close water inlet（18）Side point
By-pass filtration film is not connected with（2）, secondary filtration film（3）With three-stage filtration film（4）, the filtering cabin（1）Another side bottom leads to
Cross water pipe（17）With dilution storehouse（5）One side-lower is welded, the dilution storehouse（5）Top is welded with filler（8）, the dilution storehouse
（5）Inner upper is welded with water tank（6）, and water tank（6）Lower section is threaded with several flush ports（7）, the dilution storehouse（5）
The other end is by welding water pipe（17）Storehouse is adsorbed with primary coal dust（10）One side-lower is welded, the primary coal dust absorption storehouse（10）
Pass through water pipe below opposite side（17）With oxidation catalysis storehouse（11）Lower section is welded, the oxidation catalysis storehouse（11）It is logical below opposite side
Cross water pipe（17）Storehouse is adsorbed with final coal dust（12）Lower section is welded, the final coal dust absorption storehouse（12）It is welded with below opposite side
Delivery port（14）, the primary coal dust absorption storehouse（10）, oxidation catalysis storehouse（11）Storehouse is adsorbed with final coal dust（12）All block inside
It is connected to screen pack（9）.
2. a kind of high concentrated organic wastewater processing unit according to claim 1, it is characterised in that：The primary coal dust is inhaled
Attached storehouse（10）, oxidation catalysis storehouse（11）Storehouse is adsorbed with final coal dust（12）Lower inside is all welded with aerator（15）.
3. a kind of high concentrated organic wastewater processing unit according to claim 1, it is characterised in that：The flush port（7）
For injecting type flush port.
4. a kind of high concentrated organic wastewater processing unit according to claim 1, it is characterised in that：The water pipe（17）On
All it is threaded with suction pump（16）.
5. a kind of high concentrated organic wastewater processing unit according to claim 1, it is characterised in that：The delivery port（14）
On be threaded with outlet water control valve（13）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720128661.1U CN206570120U (en) | 2017-02-13 | 2017-02-13 | A kind of high concentrated organic wastewater processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720128661.1U CN206570120U (en) | 2017-02-13 | 2017-02-13 | A kind of high concentrated organic wastewater processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206570120U true CN206570120U (en) | 2017-10-20 |
Family
ID=60059292
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720128661.1U Expired - Fee Related CN206570120U (en) | 2017-02-13 | 2017-02-13 | A kind of high concentrated organic wastewater processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206570120U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467205A (en) * | 2018-12-19 | 2019-03-15 | 武汉格林环保设施运营有限责任公司 | High-concentration organic wastewater treatment system |
| CN112028295A (en) * | 2020-07-20 | 2020-12-04 | 南京传业环保科技有限公司 | High-concentration organic wastewater treatment device |
-
2017
- 2017-02-13 CN CN201720128661.1U patent/CN206570120U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467205A (en) * | 2018-12-19 | 2019-03-15 | 武汉格林环保设施运营有限责任公司 | High-concentration organic wastewater treatment system |
| CN109467205B (en) * | 2018-12-19 | 2021-10-08 | 武汉格林环保设施运营有限责任公司 | High-concentration organic wastewater treatment system |
| CN112028295A (en) * | 2020-07-20 | 2020-12-04 | 南京传业环保科技有限公司 | High-concentration organic wastewater treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171020 Termination date: 20180213 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |