CN205635243U - Vitamin C waste water advanced treatment unit - Google Patents
Vitamin C waste water advanced treatment unit Download PDFInfo
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- CN205635243U CN205635243U CN201520394022.0U CN201520394022U CN205635243U CN 205635243 U CN205635243 U CN 205635243U CN 201520394022 U CN201520394022 U CN 201520394022U CN 205635243 U CN205635243 U CN 205635243U
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Abstract
The utility model relates to a sewage treatment technical field, special design is to the vitamin C waste water's through the processing of traditional sewage treatment method sewage advanced treatment unit. Does the device include that the one -level is by the oxygen deficiency the anaerobism the biological membrane bioreactor that good oxygen is constituteed, is the one -level by the oxygen deficiency biological membrane bioreactor and two -stage ozone that good oxygen is constituteed the unsteady biological pond of bed to make the oxygen deficiency through methods such as backward flows the anaerobism good oxygen obtains the coupling effect. The beneficial effects are that oxygen deficiency through the coupling the anaerobism good oxygen fluctuation freight elevator degrades the difficult degradation pollutant through reinforceing biochemical method, carry out the oxidation modification to the pollutant that still can not degrade and passing through biochemical degradation, thereby obtain innoxious advanced wastewater treatment result with the most economic biochemical reactions, it reaches the national municipal one -level A emission standard of china with the processing of vitamin C waste water to strengthen biochemical (OEB) process through multistage compound space biofilm reactor (MCM) and multistage oxidation.
Description
Technical field
This utility model relates to technical field of sewage, specifically, relates to processing for through traditional wastewater device
After still can not the deep treatment method of sewage of qualified discharge, particular for the vitamin C processed through traditional wastewater device
Produce waste water and process to reach the advanced treatment method for sewage water of discharge standard further.
Technical background
Traditional sewage-treatment plant is typically based on activated sludge process.The kind of microorganism and work in activated sludge process
Property is restricted, thus some Organic substances are difficult to be degraded, and affect treatment effect.Traditional wastewater treatment technology is generally being difficult to
The Organic substance degraded by activated sludge is referred to as " hardly degraded organic substance " or can not biochemical Organic substance.For the city containing industrial wastewater
Political affairs sewage, or for industrial wastewater, larger amount of " hardly degraded organic substance " can be remained by traditional sewage disposal, it is difficult to reach
Discharge standard or follow-up reuse technology requirement.The waste water that production of vitamin C produces has that wastewater flow rate is big, pollution concentration is high, saliferous
Amount high, is difficult to reach cities and towns discharge standard with traditional sewage treatment.
Last century, owing to wastewater from vitamin C production is difficult to process the problems such as up to standard, it is the most all of that the U.S. does not closes it
Factory.China becomes global production of vitamin C center at present.Common wastewater from vitamin C production chemical oxygen consumption (COC)
(COD) at more than 10000mg/L.COD, through strong process, can be reduced to below 500mg/L, reach by manufacturing enterprise
Industrial undertaking is discharged into the standard of municipal sewage plant.But, these remaining COD almost all are " hardly degraded organic substances ",
The highest nitrogen pollutant, high rigidity and the salinity more than 1%, feels simply helpless in traditional municipal sewage plant.
There is expert it is thought that mankind's sewage treatment area " world-famous puzzle " that face.By up to standard for this kind of commercial production sewage disposal will be
The big problem of the numerous similar enterprises final and decisive juncture of China, needs to develop advanced treatment of wastewater technology on the basis of traditional wastewater processes
With method (Acute Waste Water Treatment, AWWT).
Advanced treatment of wastewater (AWWT) technology refers to the " difficulty in the sewage after traditional wastewater processes containing higher concentration
Degradation of organic substances ", need the sewage disposal technology used when processing further.The application that advanced treatment of wastewater technology is main
Including: after (1) conventional process, sewage can not reach discharge standard, needs advanced treating (including proposing mark transformation)；(2) tradition
After method process, sewage can not meet the inflow requirement of reuse technology, needs advanced treating；(3) in order to make the tail water of reuse technology
Emission request can be reached, sewage or reuse technology tail water are implemented advanced treating.
Common advanced treatment of wastewater technology includes multiple method.The most common Fenton reagent method is a kind of chemistry side
Method, consumes substantial amounts of chemicals, produces substantial amounts of chemical sludge, and operating cost is high.Due to Fenton reagent method mainly with flocculation
The mode of precipitation removes pollutant, therefore preferable to the Pollutant Treatment effect of relatively macromole, and the pollutant to less molecule,
Treatment effect is limited.Membrane bioreactor (MBR) can also as a kind of advanced treatment of wastewater method, but due to MBR method still
So with activated sludge as core, reduce the limited space of " hardly degraded organic substance " further.Biomembrane biochemistry advanced treatment of wastewater
Biochemical method (Oxidation Enhanced Bio-is strengthened in method (Bio-Film Bio-reaction, BFB) and oxidation
Reaction, OEB) substantial amounts of chemical sludge will not be produced, run power consumption low, be the method for relatively environmental protection.
It is true that whether organic pollutant can be relevant with microbe species and population composition by biochemical degradation, if energy
Enough cultivate more horn of plenty and microbial population targetedly, the Organic substance of some conventional method " difficult degradation " is possible to become
For " degradable " Organic substance.Therefore for cultivate more horn of plenty microorganism and create conditions be eliminate " hardly degraded organic substance " direction it
One.
Chinese patent " composite biological packing and bioreactor thereof " (201020204406.9) discloses a kind of composite gap
Biologic packing material (Multi-Cavity MEdia, MCM), including a netted shell of hard and be filled in this shell two kinds with
On medium block.Owing to having bigger space between shell, between medium block, there is less space, in medium block, have micro-interstices；
Mixing wastewater with air give-and-take conditions marked difference in big space, little space and microvoid causes the marked difference of dissolved oxygen, permissible
Realize aerobic, the coupling on the spot of anoxia, anaerobism.Typical media block combination simultaneously is to have the coke briquette of micropore or charcoal lump and fire
The combination of mountain rock, the feature of this combination is coke briquette or charcoal lump has a relatively low redox potential, and the oxidation in volcanic rock
Ferrous components has higher redox potential, and different microorganisms can select different dielectric surfaces to perch.
Chinese patent (200710195135.8) discloses a kind of biofilm reactor, wherein uses MCM first to realize
Oxygen, anoxia, the coupling on the spot of anaerobism.Under air stripping recycle stream effect, in this reactor, realize multistage aerobic, anoxia again, detest
Coupling in oxygen reactor.Above biofilm reactor technology to cultivate more horn of plenty and targetedly microbial population with fall
Solve " hardly degraded organic substance " and provide technical foundation.Simultaneously because the existence of multiple-microorganism so that synchronize digestion/denitrification with
Synchronous degradation residue biological sludge is achieved.
But when similar techniques is used for the pollutant of more difficult degradation, the process especially for vitamin C tail water is, single
One method is also not enough so that sewage disposal is up to standard, needs many secondary coupling of multiple bioprocesses.
Through the biomembrane biochemistry advanced treatment of wastewater of many secondary coupling, part " hardly degraded organic substance " is still had to be difficult to be given birth to
Change degraded.Strong oxidizer can be used to aoxidize these " hardly degraded organic substances ", change its chemical property, improving it can be biochemical
Property, carry out biochemical treatment the most again.This process can be referred to as the biochemical reaction (OEB) that oxidation is strengthened.
Utility model content
Can not reach after this utility model traditional wastewater to be solved disposal methods difficult degradation sewage to process the skill required
Art problem, is difficult to the processed skill reaching mark discharge especially for wastewater from vitamin C production such as similar wastewater from vitamin C production
Art problem, discloses a kind of advanced treatment of wastewater technology.
In order to solve above-mentioned technical problem, this wastewater from vitamin C production advanced treatment apparatus includes that the first water inlet connects successively
Mouth, a coagulative precipitation tank, the first biomembrane hypoxia response pond, the first biological membrane anaerobic reaction tank, the first biomembrane aerobic reaction
Pond, one-level elevator pump, the second biomembrane hypoxia response pond, the second biomembrane aerobic reaction pond, two-stage hoisting pump, the second coagulation sink
Pond, shallow lake, the first oxidation reaction pond, the first flotation bed biological tank, the second oxidation reaction pond, the second flotation bed biological tank, product water connect
Mouthful；Also include that oxygen/anoxia backwash blower fan, aerobic operation blower fan, flotation bed biological tank backwash blower fan, flotation bed biological tank run wind
Machine, ozonator, necessary valve, instrument and automatic control system；Wherein the first coagulative precipitation tank and the second coagulating sedimentation
Discharge pipeline, wherein the first biomembrane hypoxia response pond, the first biological membrane anaerobic reaction tank and two biomembrane anoxias it are provided with bottom pond
Air purge aerator it is provided with, wherein bottom the first biomembrane aerobic reaction pond and the second biomembrane aerobic reaction pond bottom reaction tank
It is provided with aerobic aeration device, is wherein provided with multiple ozonation aerated device bottom the first oxidation reaction pond and the second oxidation reaction pond,
Wherein the first flotation bed biological tank and the second flotation bed biological tank, bottom is provided with water-gas distribution device；Wherein the first biomembrane is good
Oxygen reaction tank part is produced water and is back to the first biomembrane hypoxia response pond through one-level elevator pump and the first reflux pipe, and second is raw
Thing film aerobic reaction pond part is produced water and is back to the second biomembrane hypoxia response pond through two-stage hoisting pump and the second reflux pipe,
Second biomembrane aerobic reaction pond part is produced water and is back to the with biomembrane anoxia through two-stage hoisting pump and the 3rd reflux pipe
Reaction tank.
This wastewater from vitamin C production deep treatment method provides the benefit that the microorganism owing to parasitizing on biologic packing material
Being fixed in particular pool, in the first biomembrane aerobic reaction pond and the second biomembrane aerobic reaction pond, dominant bacteria is according to pollution
Thing composition change and the difference (can be controlled) of dissolved oxygen and different.In like manner, the first biomembrane hypoxia response pond, the first life
Change that in thing film anaerobic reation pool and the second biomembrane hypoxia response pond, dominant bacteria forms with pollutant and dissolved oxygen difference
And different, just because of the difference of these microorganisms, various " persistent organic pollutants " under the effect of extraordinary microorganism by
Step is degraded.Another of this wastewater from vitamin C production advanced treatment apparatus provide the benefit that utilize biologic packing material realize anoxia and
Coupling the most on the spot of aerobic reaction, then realize anoxia between biological reaction pool and aerobic by Aerobic Pond to the backflow of prime anoxic pond
Coupling.One of these anoxias and aerobic coupling effect are that hypoxia response product can be by aerobic degradation, and aerobic reaction product can
To be degraded by hypoxia response；Rear class product may be degraded by prime again；The residue biological sludge that rear class produces is refluxed,
And be progressively degraded so that biological sludge amount substantially reduces.Another of this wastewater from vitamin C production advanced treatment apparatus is useful
Effect is the filler selecting to have features.Another of this wastewater from vitamin C production advanced treatment apparatus provides the benefit that can
To select when necessary to add the nutrient that degraded Recalcitrant chemicals needs.This wastewater from vitamin C production advanced treatment apparatus
Another provide the benefit that by adding oxidant the most on a small quantity real to biomembrane reaction rear section " persistent organic pollutants "
Existing " limited oxidation " is modified, then the pollutant of these degeneration of degrading with follow-up flotation bed biological tank, the therefore efficiency of oxidant
Higher.Biochemical (OEB) process is strengthened vitamin C is raw by multistage composite gap biological membrane reactor (MCM) and multi-stage oxidizing
Produce waste water process and reach China national municipal administration one-level emission standard A.The experiment proved that these apparatus and method are for numerous difficult falls
The advanced treating solving sewage has extensive effect.
Accompanying drawing explanation
Fig. 1 is this wastewater from vitamin C production advanced treatment apparatus schematic flow sheet.
10. first water inlet interface in figure, 11. second water inlet interfaces, 20. produce water interface, 30. discharge pipelines, and 50. charcoal sources are added
Device, 110. first coagulative precipitation tanks, 120. first biomembrane hypoxia response ponds, 130. first biological membrane anaerobic reaction tanks,
140. first biomembrane aerobic reaction ponds, 150. one-level elevator pumps, 151. first reflux pipes, 160. second biomembrane anoxias are anti-
Ying Chi, 170. second biomembrane aerobic reaction ponds, 180. two-stage hoisting pumps, 181. second reflux pipes, 182. the 3rd return ducts
Road, 200. 2 coagulative precipitation tanks, 310. first oxidation reaction ponds, 320. first flotation bed biological tanks, 330. second oxidation reactions
Pond, 340. second flotation bed biological tanks, 510. anaerobism and anoxia backwash blower fan, 511. air purge aerators, 520. aerobic operations
Blower fan, 521. aerobic aeration devices, 530. BAF backwash blower fans, 531. water-gas distribution devices, 540. flotation beds are raw
Blower fan is run in thing pond, and 541. flotation bed biological tanks run aerator, 600. ozone generating-devices, 601. ozonation aerated devices.
For simplicity, necessary valve, instrument and automatic control system are omitted in the drawings.
Detailed description of the invention
As it is shown in figure 1, this wastewater from vitamin C production advanced treatment apparatus, it is characterised in that include that the first water inlet connects successively
Mouth (10), the first coagulative precipitation tank (110), the first biomembrane hypoxia response pond (120), the first biological membrane anaerobic reaction tank
(130), the first biomembrane aerobic reaction pond (140), one-level elevator pump (150), the second biomembrane hypoxia response pond (160),
Two biomembrane aerobic reaction ponds (170), two-stage hoisting pump (180), the second coagulative precipitation tank (200), the first oxidation reaction pond
(310), the first flotation bed biological tank (320), the second oxidation reaction pond (330), the second flotation bed biological tank (340), product water connect
Mouth (20)；Also include oxygen/anoxia backwash blower fan (510), aerobic operation blower fan (520), flotation bed biological tank backwash blower fan
(530), flotation bed biological tank runs blower fan (540), ozonator (600), necessary valve, instrument and automatically controls and be
System；Wherein the first coagulative precipitation tank (110) and the second coagulation sink a biomembrane anaerobic reation pool (130) and two biomembrane anoxias
Reaction tank (160) bottom is provided with air purge aerator (511), wherein the first biomembrane aerobic reaction pond (140) and the second biology
Bottom, film aerobic reaction pond (170) is provided with aerobic aeration device (521), wherein the first oxidation reaction pond (310) and the second oxidation
Reaction tank (330) bottom is provided with multiple ozonation aerated device (601), and wherein the first flotation bed biological tank (320) and second floats
Bed biological tank (340) bottom is provided with water-gas distribution device (531)；Wherein the first biomembrane aerobic reaction pond (140) part produces water
Being back to the first biomembrane hypoxia response pond (120) through one-level elevator pump (150) and the first reflux pipe (151), second is raw
Thing film aerobic reaction pond (170) part is produced water and is back to the second life through two-stage hoisting pump (180) and the second reflux pipe (181)
Thing film hypoxia response pond (160), the second biomembrane aerobic reaction pond (170) part produces water through two-stage hoisting pump (180) and the 3rd
Reflux pipe (182) is back to biomembrane hypoxia response pond (120).
This wastewater from vitamin C production advanced treatment apparatus also includes to the second biomembrane hypoxia response pond (160) for former water
Second water inlet interface (11), this interface can utilize former water for denitrification provide charcoal source.
This wastewater from vitamin C production advanced treatment apparatus also includes to the second biomembrane hypoxia response pond (160) for charcoal source
Charcoal source adding set (50), this device when former water charcoal source deficiency for degree of depth denitrification provide charcoal source.
This wastewater from vitamin C production advanced treatment apparatus the first biomembrane hypoxia response pond (120), the first biological membrane anaerobic
Reaction tank (130), the first biomembrane aerobic reaction pond (140), one-level elevator pump (150), the second biomembrane hypoxia response pond
(160), the second biomembrane aerobic reaction pond (170) is added composite gap biological filler.
This wastewater from vitamin C production advanced treatment apparatus the first flotation bed biological tank (320) and the second flotation bed biological tank
(340) active carbon filler is comprised.
Embodiment
Utilize this wastewater from vitamin C production advanced treatment apparatus, the wastewater from vitamin C production through biochemical treatment is carried out
Advanced treating, through exceeding debugging half a year and stable operation, continuous 10 days detection numbers of third party during final formal demarcation examination
According to as follows:
Unit: mg/L
The result of appraisal stably reach China national first discharge standard.
Claims (5)
1. a wastewater from vitamin C production advanced treatment apparatus, it is characterised in that include successively the first water inlet interface (10), first
Coagulative precipitation tank (110), the first biomembrane hypoxia response pond (120), the first biological membrane anaerobic reaction tank (130), the first biology
Film aerobic reaction pond (140), one-level elevator pump (150), the second biomembrane hypoxia response pond (160), the second biomembrane are aerobic instead
Ying Chi (170), two-stage hoisting pump (180), the second coagulative precipitation tank (200), the first oxidation reaction pond (310), the first flotation bed
Biological tank (320), the second oxidation reaction pond (330), the second flotation bed biological tank (340), product water interface (20)；Also include oxygen/
Anoxia backwash blower fan (510), aerobic operation blower fan (520), flotation bed biological tank backwash blower fan (530), flotation bed biological tank are transported
Sector-style machine (540), ozonator (600), necessary valve, instrument and automatic control system；Wherein the first coagulative precipitation tank
(110) and the second coagulative precipitation tank (200) bottom is provided with discharge pipeline (30), wherein the first biomembrane hypoxia response pond (120), the
One biomembrane anaerobic reation pool (130) and bottom, two biomembrane hypoxia response ponds (160) are provided with air purge aerator (511), its
In the first biomembrane aerobic reaction pond (140) and the second biomembrane aerobic reaction pond (170) bottom be provided with aerobic aeration device
(521), wherein the first oxidation reaction pond (310) and bottom, the second oxidation reaction pond (330) are provided with multiple ozonation aerated device
(601), wherein the first flotation bed biological tank (320) and the second flotation bed biological tank (340) bottom are provided with water-gas distribution device
(531)；Wherein the first biomembrane aerobic reaction pond (140) part produces water through one-level elevator pump (150) and the first reflux pipe
(151) being back to the first biomembrane hypoxia response pond (120), the second biomembrane aerobic reaction pond (170) part produces water through two
Level elevator pump (180) and the second reflux pipe (181) are back to the second biomembrane hypoxia response pond (160), the second biomembrane
Aerobic reaction pond (170) part is produced water and is back to the with biomembrane through two-stage hoisting pump (180) and the 3rd reflux pipe (182)
Hypoxia response pond (120).
Wastewater from vitamin C production advanced treatment apparatus the most according to claim 1, it is characterised in that also include to second raw
Thing film hypoxia response pond (160) is for the second water inlet interface (11) of former water.
Wastewater from vitamin C production advanced treatment apparatus the most according to claim 1, it is characterised in that also to the second biomembrane
Hypoxia response pond (160) is for charcoal source adding set (50) in charcoal source.
Wastewater from vitamin C production advanced treatment apparatus the most according to claim 1, it is characterised in that the first biomembrane anoxia
Reaction tank (120), the first biological membrane anaerobic reaction tank (130), the first biomembrane aerobic reaction pond (140), one-level elevator pump
(150), the second biomembrane hypoxia response pond (160), the second biomembrane aerobic reaction pond (170) comprise composite gap biological to fill out
Material.
Wastewater from vitamin C production advanced treatment apparatus the most according to claim 1, it is characterised in that the first flotation bed is biological
Pond (320) and the second flotation bed biological tank (340) comprise active carbon filler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520394022.0U CN205635243U (en) | 2015-06-10 | 2015-06-10 | Vitamin C waste water advanced treatment unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520394022.0U CN205635243U (en) | 2015-06-10 | 2015-06-10 | Vitamin C waste water advanced treatment unit |
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| Publication Number | Publication Date |
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| CN205635243U true CN205635243U (en) | 2016-10-12 |
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ID=57077619
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201520394022.0U Active CN205635243U (en) | 2015-06-10 | 2015-06-10 | Vitamin C waste water advanced treatment unit |
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| CN (1) | CN205635243U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104909517A (en) * | 2015-06-10 | 2015-09-16 | 北京格兰特膜分离设备有限公司 | Industrial production wastewater advanced treatment device |
| CN108033629A (en) * | 2017-11-23 | 2018-05-15 | 南京大学 | Coagulation-ozone-MBBR group technologies processing VB12The device and method of waste water |
-
2015
- 2015-06-10 CN CN201520394022.0U patent/CN205635243U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104909517A (en) * | 2015-06-10 | 2015-09-16 | 北京格兰特膜分离设备有限公司 | Industrial production wastewater advanced treatment device |
| CN108033629A (en) * | 2017-11-23 | 2018-05-15 | 南京大学 | Coagulation-ozone-MBBR group technologies processing VB12The device and method of waste water |
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| DD01 | Delivery of document by public notice |
Addressee: BEIJING GRANT MEMBRANE SEPARATION EQUIPMENT Co.,Ltd. Document name: Notification to Make Rectification |
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| DD01 | Delivery of document by public notice |
Addressee: BEIJING GRANT MEMBRANE SEPARATION EQUIPMENT Co.,Ltd. Document name: Notification of Decision on Request for Restoration of Right |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 2nd Floor, Building 2, Yard 12 Tianzhu West Road, Airport Industrial Zone A, Shunyi District, Beijing, 101312 Patentee after: Huazi Grant Environmental Protection Technology (Beijing) Co.,Ltd. Address before: 2nd Floor, Building 2, Yard 12 Tianzhu West Road, Airport Industrial Zone A, Shunyi District, Beijing, 101312 Patentee before: BEIJING GRANT MEMBRANE SEPARATION EQUIPMENT Co.,Ltd. |
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