CN208345992U - A kind of processing system of cosmetics waste water - Google Patents
A kind of processing system of cosmetics waste water Download PDFInfo
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- CN208345992U CN208345992U CN201820682957.2U CN201820682957U CN208345992U CN 208345992 U CN208345992 U CN 208345992U CN 201820682957 U CN201820682957 U CN 201820682957U CN 208345992 U CN208345992 U CN 208345992U
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- communicating pipe
- pond
- aerobic
- sedimentation basin
- waste water
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of processing systems of cosmetics waste water, including grid pond, grid pond is connected with conditioning tank by communicating pipe, conditioning tank is connected with coagulation reaction tank by communicating pipe, coagulation reaction tank is connected with sedimentation basin by communicating pipe, sedimentation basin is connected with air-floating apparatus by communicating pipe, air-floating apparatus is connected with hydrolysis acidification pool by communicating pipe, hydrolysis acidification pool is by being connected with UASB reactor communicating pipe, UASB reactor is by being connected with aerobic bio-contact oxidation pond communicating pipe, aerobic bio-contact oxidation pond is by being connected with the first aerobic sludge sedimentation basin communicating pipe, first aerobic sludge sedimentation basin is by being connected with reinforced anaerobic pond communicating pipe, reinforced anaerobic pond is by being connected with reinforcing contact-oxidation pool communicating pipe, strengthen contact-oxidation pool by being connected with the second aerobic mudpan communicating pipe.The utility model can effectively be handled cosmetics waste water, be conducive to the processing and discharge of cosmetics waste water.
Description
Technical field
The utility model relates to environmental technology field more particularly to a kind of processing systems of cosmetics waste water.
Background technique
Cosmetic-producing wastewater is mainly derived from cleaning flushing waste water and product processing process drain.Waste water is mainly special
Point has: 1, water and variation water quality are larger；2, the pollutant concentrations such as COD, LAS are higher, when wherein LAS is excessively high, have to microorganism
Toxicity processed and foam can be generated in aerobe reactor；3, waste component is complicated, such as cocounut oil propyl betaine, to chlor-alkali two
Cresols, essence, glycerol etc.；4, bio-refractory substance is more, such as glycerol octadecyl alcolol, half glycidic acid ester grease type and some
Cosmetic additive agent, emulsification degree are higher.
At present for cosmetics organic wastewater, existing sewage disposal system is difficult to reach when to cosmetics wastewater treatment
Discharge standard is unfavorable for the processing and discharge of cosmetics waste water.For this purpose, we have proposed a kind of processing systems of cosmetics waste water
System.
Utility model content
Purpose of the utility model is to solve disadvantages present in background technique, and a kind of cosmetics waste water proposed
Processing system.
To achieve the goals above, the utility model adopts the technical scheme that
A kind of processing system of cosmetics waste water, including grid pond, the grid pond are connected with conditioning tank by communicating pipe,
The conditioning tank is by being connected with coagulation reaction tank communicating pipe, and the coagulation reaction tank is by being connected with sedimentation basin, institute communicating pipe
Sedimentation basin is stated by being connected with air-floating apparatus communicating pipe, the air-floating apparatus is described by being connected with hydrolysis acidification pool communicating pipe
Hydrolysis acidification pool is connect by being connected with UASB reactor, the UASB reactor communicating pipe by being connected with aerobe communicating pipe
Oxidation pond is touched, by being connected with the first aerobic sludge sedimentation basin communicating pipe, described first is good in the aerobic bio-contact oxidation pond
Oxygen mudpan strengthens contact by being connected with communicating pipe by being connected with reinforced anaerobic pond, the reinforced anaerobic pond communicating pipe
Oxidation pond, the reinforcing contact-oxidation pool is by being connected with the second aerobic mudpan, second aerobic sludge communicating pipe
Sedimentation basin is connected with clear water reserviors by communicating pipe by being connected with MBR film reaction pond, the MBR film reaction pond communicating pipe.
Preferably, by connecting jointly communicating pipe between the aerobic bio-contact oxidation pond and the first aerobic sludge sedimentation basin
It is connected to the first sludge refluxing apparatus.
Preferably, by being connected with jointly communicating pipe between the reinforcing contact-oxidation pool and the second aerobic mudpan
Second sludge refluxing apparatus.
Preferably, by communicating pipe being connected with back purge system jointly between MBR film reaction pond and clear water reserviors.
The utility model proposes a kind of cosmetics waste water processing system, beneficial effect is: being entirely in this programme
System can effectively be handled cosmetics waste water during utilization, so that treated, water outlet reaches the mark of discharge
Standard, and then whole system is conducive to the processing and discharge of cosmetics waste water.
Detailed description of the invention
Fig. 1 be the utility model proposes a kind of cosmetics waste water processing system structural schematic diagram.
In figure: grid pond 1, conditioning tank 2, coagulation reaction tank 3, sedimentation basin 4, air-floating apparatus 5, hydrolysis acidification pool 6, UASB
Reactor 7, the first aerobic sludge sedimentation basin 9, reinforced anaerobic pond 10, strengthens contact-oxidation pool at aerobic bio-contact oxidation pond 8
11, the second aerobic mudpan 12, MBR film reaction pond 13, clear water reserviors 14, the first sludge refluxing apparatus 15, the second sludge return
Flow device 16, back purge system 17.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.
In the description of the present invention, it should be understood that term " on ", "lower", "front", "rear", "left", "right",
The orientation or positional relationship of the instructions such as "top", "bottom", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
Referring to Fig.1, a kind of processing system of cosmetics waste water, including grid pond 1, grid pond 1 are connected with by communicating pipe
Conditioning tank 2, conditioning tank 2 are connected with sedimentation basin by communicating pipe by being connected with coagulation reaction tank 3, coagulation reaction tank 3 communicating pipe
4, sedimentation basin 4 is hydrolyzed by being connected with air-floating apparatus 5, air-floating apparatus 5 communicating pipe by being connected with hydrolysis acidification pool 6 communicating pipe
Acidification pool 6 contacts oxygen by being connected with aerobe communicating pipe by being connected with UASB reactor 7, UASB reactor 7 communicating pipe
Change pond 8, aerobic bio-contact oxidation pond 8 is by being connected with the first aerobic sludge sedimentation basin 9, aerobic bio-contact oxidation communicating pipe
By being connected with the first sludge refluxing apparatus 15 communicating pipe jointly between pond 8 and the first aerobic sludge sedimentation basin 9, the first sludge is returned
Stream device 15 can be such that the first aerobic sludge sedimentation basin 9 obtains in sludge reflux to aerobic biological contact oxidation pond 8, be maintained with this
The stabilization of sludge concentration in oxygen biological contact oxidation pond 8.
First aerobic sludge sedimentation basin 9 passes through connection by being connected with reinforced anaerobic pond 10, reinforced anaerobic pond 10 communicating pipe
Pipe, which is connected with, strengthens contact-oxidation pool 11, strengthens contact-oxidation pool 11 by being connected with the second aerobic mudpan communicating pipe
12, strengthen between contact-oxidation pool 11 and the second aerobic mudpan 12 by communicating pipe being connected with the second sludge reflux jointly
Device 16, the second sludge refluxing apparatus 16 can make the sludge reflux in the second aerobic mudpan 12 to reinforcing contact oxygen
Change in pond 11, the stabilization for strengthening 11 inside sludge concentration of contact-oxidation pool is maintained with this.
Second aerobic mudpan 12 is passed through by being connected with MBR film reaction pond 13, MBR film reaction pond 13 communicating pipe
Clear water reserviors 14 are connected with communicating pipe, by being connected with backwash dress communicating pipe jointly between MBR film reaction pond 13 and clear water reserviors 14
17 are set, clear water remaining in clear water reserviors 14 can further be passed through MBR film reaction pond 13 and handled by back purge system 17, therefore
Ensure that the water outlet of clear water reserviors 14 meets standard of drainage.
Working principle and effect: the existing grid pond 1 that enters of waste water carries out grid interception in this programme, subsequently into conditioning tank
2, the aerating system being equipped in conditioning tank can play the role of uniform water and water quality to waste water, the waste water of conditioning tank 2 even into
Coagulation reaction tank 3, the waste water of coagulation reaction tank 3 flocculation sedimentation under the action of coagulant, and eliminate most suspended substances and
Organic pollutant；The water outlet gravity flow of coagulation reaction tank 3 enters air-floating apparatus 5, and the overwhelming majority can be removed under the action of air-floating apparatus 5
LAS, grease type difficult to degrade and partial suspended thing, the water outlet of air-floating apparatus 5 enters hydrolysis acidification pool 6, big in hydrolysis acidification pool 6
Measuring hydrolytic bacteria, being acidified insoluble hydrolysis of organic matter under bacterium effect is dissolved organic matter, by the macromolecular of difficult for biological degradation
Substance is converted into the process of the small-molecule substance of easily biological-degradable, so as to improve the biodegradability of waste water, establishes for subsequent processing
Basis, after the water outlet of hydrolysis acidification pool 6 enters UASB reactor 7, organic matter participates in substrate in anaerobic bacteria and other microorganisms
Conversion process and convert a substrate into final product --- the inorganic matters such as natural pond gas and water, waste water subsequently into aerobe contact oxygen
Change pond 8, and remove most organic in aerobic bio-contact oxidation pond 8, aerobic tank mixed liquor is through the first aerobic sludge
Enter the first aerobic sludge sedimentation basin 9 after 9 mud-water separation of sedimentation basin, COD in water removal is further removed, finally by reinforcing catalytic oxidation
Pond 11 and the second aerobic mudpan 12 enter back into MBR film reaction pond 13, the COD that further degrades, remove oil removal, out water flow
Enter clear water reserviors 14, the water outlet of clear water reserviors 14 can stably reach the effluent quality of " integrated wastewater discharge standard " (GB8978-1996)
It is required that therefore whole system effectively cosmetics waste water can be handled during utilization so that treated go out
Water reaches the standard of discharge, and then whole system is conducive to the processing and discharge of cosmetics waste water.
The preferable specific embodiment of the above, only the utility model, but the protection scope of the utility model is not
It is confined to this, anyone skilled in the art is within the technical scope disclosed by the utility model, practical according to this
Novel technical solution and its utility model design are subject to equivalent substitution or change, should all cover the protection model in the utility model
Within enclosing.
Claims (4)
1. a kind of processing system of cosmetics waste water, including grid pond (1), which is characterized in that the grid pond (1) passes through connection
Pipe is connected with conditioning tank (2), and the conditioning tank (2) is by being connected with coagulation reaction tank (3), the coagulation reaction tank communicating pipe
(3) by being connected with communicating pipe sedimentation basin (4), the sedimentation basin (4) is by being connected with air-floating apparatus (5), the gas communicating pipe
Device (5) are floated by being connected with communicating pipe hydrolysis acidification pool (6), the hydrolysis acidification pool (6) is connected with UASB by communicating pipe
Reactor (7), the UASB reactor (7) is by being connected with aerobic bio-contact oxidation pond (8), the aerobe communicating pipe
Contact-oxidation pool (8) is by being connected with the first aerobic sludge sedimentation basin (9), the first aerobic sludge sedimentation basin (9) communicating pipe
By being connected with communicating pipe reinforced anaerobic pond (10), the reinforced anaerobic pond (10) is by being connected with reinforcing catalytic oxidation communicating pipe
Pond (11), the reinforcing contact-oxidation pool (11) is by being connected with the second aerobic mudpan (12) communicating pipe, and described second
Aerobic sludge sedimentation basin (12) passes through connection by being connected with MBR film reaction pond (13), MBR film reaction pond (13) communicating pipe
Pipe is connected with clear water reserviors (14).
2. a kind of processing system of cosmetics waste water according to claim 1, which is characterized in that the aerobe contact
By being connected with the first sludge refluxing apparatus (15) communicating pipe jointly between oxidation pond (8) and the first aerobic sludge sedimentation basin (9).
3. a kind of processing system of cosmetics waste water according to claim 1, which is characterized in that the reinforcing catalytic oxidation
By being connected with the second sludge refluxing apparatus (16) communicating pipe jointly between pond (11) and the second aerobic mudpan (12).
4. a kind of processing system of cosmetics waste water according to claim 1, which is characterized in that MBR film reaction pond
(13) by being connected with back purge system (17) communicating pipe jointly between clear water reserviors (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820682957.2U CN208345992U (en) | 2018-05-09 | 2018-05-09 | A kind of processing system of cosmetics waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820682957.2U CN208345992U (en) | 2018-05-09 | 2018-05-09 | A kind of processing system of cosmetics waste water |
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| Publication Number | Publication Date |
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| CN208345992U true CN208345992U (en) | 2019-01-08 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820682957.2U Active CN208345992U (en) | 2018-05-09 | 2018-05-09 | A kind of processing system of cosmetics waste water |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113072247A (en) * | 2021-03-23 | 2021-07-06 | 昆山水清华环保科技有限公司 | Cosmetics sewage treatment system |
-
2018
- 2018-05-09 CN CN201820682957.2U patent/CN208345992U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113072247A (en) * | 2021-03-23 | 2021-07-06 | 昆山水清华环保科技有限公司 | Cosmetics sewage treatment system |
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