CN206736017U - Antibiotic waste water processing unit - Google Patents
Antibiotic waste water processing unit Download PDFInfo
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- CN206736017U CN206736017U CN201720272616.3U CN201720272616U CN206736017U CN 206736017 U CN206736017 U CN 206736017U CN 201720272616 U CN201720272616 U CN 201720272616U CN 206736017 U CN206736017 U CN 206736017U
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Abstract
The utility model discloses a kind of antibiotic waste water processing unit, it includes reservoir, reactor, anaerobic pond, Aerobic Pond, sedimentation basin, ozone generator and high-concentration waste water pot, the reservoir connects with reactor, the reactor connects with anaerobic pond, the anaerobic pond connects with Aerobic Pond, the Aerobic Pond connects with sedimentation basin, the ozone generator connects with reactor, the high-concentration waste water pot connects with anaerobic pond, the utility model is completed to the pretreatment containing antibiotic waste water, device toxicity is reduced by carrying out the mode such as aoxidizing to antibiotic, it is easy to the biological treatment of follow-up Sewage Disposal.
Description
Technical field
It the utility model is related to medical sewage processing technology field, and in particular to a kind of antibiotic waste water processing unit.
Background technology
Our company needs to exclude the waste water containing antibiotic on a small quantity in process of production daily and that scraps on a small quantity contain high concentration
Substandard products medicament, the waste water containing antibiotic are the organic wastewater containing hard-degraded substance, bio-toxicity material and high S and N, are resisted
The antibiotic remained in raw plain pharmacy waste water is Biostatic material, if being directly entered plant area's Sewage Disposal, can seriously be endangered
The biological treatment of evil sewage disposal, causes Sewage Disposal to be not normally functioning.
Utility model content
The utility model is in order to eliminate harm of the antibiotic waste water to sewage disposal, there is provided a kind of antibiotic waste water processing dress
Put.
To achieve the above object, the utility model uses following technical scheme：
A kind of antibiotic waste water processing unit, it includes reservoir, reactor, anaerobic pond, Aerobic Pond, sedimentation basin, ozone
Generator and high-concentration waste water pot, the reservoir connect with reactor, and the reactor connects with anaerobic pond, the anaerobic pond
Connected with Aerobic Pond, the Aerobic Pond connects with sedimentation basin, and the ozone generator connects with reactor, the high-concentration waste water
Tank is connected with anaerobic pond, and liquid level sensor is provided with the inwall of the reservoir, and agitator, institute are provided with the reactor
The stirring motor that agitator includes being arranged on reactor upper end is stated, stirring rod, the stirring rod are provided with the stirring motor
In reactor, anaerobism filler support is provided with the anaerobic pond, anaerobism filler is provided with the anaerobism filler support,
Be provided with aerobic filler support in the Aerobic Pond, between the aerobic filler on be provided with aerobic filler, in the Aerobic Pond
Bottom be provided with micro-hole aerator, the micro-hole aerator is connected by steel pipe with High-Pressure Compressor, the sedimentation basin
Inside it is provided with Inlet and outlet water baffle plate.
Further technical scheme is to offer reservoir inlet respectively on the reservoir and reservoir goes out liquid
Mouthful, reactor inlet and reactor liquid outlet are offered respectively on the reactor, are offered and are detested respectively on the anaerobic pond
Oxygen pond inlet and anaerobic pond liquid outlet, Aerobic Pond inlet and Aerobic Pond liquid outlet, institute are offered respectively on the Aerobic Pond
State and offer sedimentation basin inlet and sedimentation basin liquid outlet on sedimentation basin respectively, the reservoir liquid outlet passes through pipeline and reaction
Device inlet is connected, and the reactor liquid outlet is connected by pipeline with anaerobic pond inlet, and the anaerobic pond liquid outlet passes through
Pipeline connects with Aerobic Pond inlet, and the Aerobic Pond liquid outlet connects with sedimentation basin inlet, and the ozone generator passes through
Pipeline is connected with reactor inlet, and the high-concentration waste water pot is connected by pipeline with anaerobic pond inlet.
Further technical scheme is that it also includes active carbon adsorber and blower fan, and the active carbon adsorber is with sinking
Shallow lake pond connects, and the blower fan connects with active carbon adsorber.
Further technical scheme is that the quantity of the micro-hole aerator is ten, and ten micro-hole aerators uniformly divide
Cloth is on the bottom in Aerobic Pond.
Further technical scheme is that the quantity of the Inlet and outlet water baffle plate is two, one in two Inlet and outlet water baffle plates
Individual to be arranged on sedimentation basin inlet, therein another is arranged on sedimentation basin liquid outlet.
The processing method of antibiotic waste water mainly has Physical, chemical method and bioanalysis etc..Physical mainly have Bubble-floating Method,
Absorption method and membrane technology；Chemical method mainly has Ozonation, Fenton oxidation method and electrochemical techniques；Bioanalysis mainly has
SBR methods (sequencing batch active sludge), MBR methods (membrane bioreactor) and up-flow anaerobic sludge blanket method.High concentration is organic
Sewage is suitably handled using the method for " anaerobism+aerobic ".The features such as waste water water is small, antibiotic is complicated is discharged according to our company,
Applicable processing method mainly has the Ozonation in Bubble-floating Method and chemical method in Physical.But there is floating for Bubble-floating Method
Slag is added, and must be also not suitable for the project by danger Waste disposal.Pretreatment of the ozone oxidation as antibiotic waste water, will portion big absolutely
Divide after having a strong impact on the antibiotic oxidation of biological treatment, then follow-up " anaerobism+aerobic " life is blended in high concentrated organic wastewater
Plant area's Sewage Disposal is discharged into after thing processing to be further processed.So in the technical program by using including reservoir,
The antibiotic waste water processing unit that reactor, anaerobic pond, Aerobic Pond, sedimentation basin, ozone generator and high-concentration waste water pot form
To realize the handling process of " ozone oxidation+anaerobism+aerobic ".
Plant area enters reservoir after being collected containing antibiotic waste water in the technical program, after reaching setting liquid level, level sensing
Device starts to alarm, and then starts ozone generator, by caused ozone input reactor.The oxidisability of ozone is very strong, can be straight
Connecing or strong oxidation reaction occurs with organic matter indirectly, antibiotic in waste water etc. suppresses the biological substance overwhelming majority and is oxidized,
BOD/COD ratios in waste water substantially increase, i.e. wastewater biodegradability increase, are created favorable conditions for follow-up biological treatment.
In order to strengthen the reaction of ozone and waste water, agitator is set in reactor.Sewage is reacted after reacting terminate after a period of time, is given up
Water enters follow-up anaerobic pond, and is mixed with the high concentrated organic wastewater in high-concentration waste water pot, in the presence of anaerobic bacteria, goes
Except Aerobic Pond is entered after most pollutant, under the biodegradation of aerobic bacteria, pollutant is further removed, water outlet enters precipitation
Pond, settle the activated sludge in waste water and the biomembrane to come off.Finally enter in plant area's pipe network, be delivered to plant area's Sewage Disposal
Continue biological treatment.
Active carbon adsorption can remove many odorants, mainly by the suction-operated of activated carbon, will produce evil
Smelly material is adsorbed in activated carbon capillary.Wherein, the odor pollutant such as acetaldehyde, indoles, 3- methyl indols is gone by physical absorption
Remove；Some other smelly composition (such as H2S and mercaptan and chlorine etc.) of cause is then to carry out oxidation reaction in activated carbon surface and enter one
Walk Adsorption.After activated carbon reaches saturation, it need to be submerged by hot-air, steam or caustic alkali and be regenerated or replaced.Should
Method has higher efficiency compared with chemical absorption method, and active carbon adsorption is generally used together with wet scrubber method.It is wet
Formula washer can remove most of H2S and NH3 etc. in stench, the activated carbon then nytron in primary attachment stench
Thing.
In summary, passed through in the technical program by setting active carbon adsorber and blower fan to realize active carbon adsorption
Active carbon adsorber is by the material that smell is produced in waste water in sedimentation basin (for example, producing odoring substance mainly by carbon, nitrogen and sulphur member
Element composition) absorption.
Compared with prior art, the beneficial effects of the utility model are：
The utility model is completed to the pretreatment containing antibiotic waste water, and device is reduced by carrying out the mode such as aoxidizing to antibiotic
Toxicity, it is easy to the biological treatment of follow-up Sewage Disposal.
Brief description of the drawings
Fig. 1 is a kind of structural representation of the antibiotic waste water processing unit of embodiment of the present utility model.
As shown in figure 1, wherein corresponding reference is entitled：
1 reservoir, 2 reactors, 3 anaerobic ponds, 4 Aerobic Ponds, 5 sedimentation basins, 6 active carbon adsorbers, 7 blower fans, 8 ozone hair
Raw device, 9 high-concentration waste water pots.
Embodiment
The utility model is further elaborated below in conjunction with the accompanying drawings.
Antibiotic waste water processing unit as shown in Figure 1, it include reservoir 1, reactor 2, anaerobic pond 3, Aerobic Pond 4,
Sedimentation basin 5, ozone generator 8 and high-concentration waste water pot 9, reservoir inlet is offered respectively on reservoir 1 and reservoir goes out
Liquid mouth, reactor inlet and reactor liquid outlet are offered respectively on reactor 2, anaerobic pond is offered respectively on anaerobic pond 3
Inlet and anaerobic pond liquid outlet, offer Aerobic Pond inlet and Aerobic Pond liquid outlet on Aerobic Pond 4 respectively, on sedimentation basin 5
Sedimentation basin inlet and sedimentation basin liquid outlet are offered respectively, reservoir liquid outlet is connected by pipeline with reactor inlet,
Reactor liquid outlet is connected by pipeline with anaerobic pond inlet, and anaerobic pond liquid outlet is connected by pipeline and Aerobic Pond inlet
Logical, Aerobic Pond liquid outlet connects ozone generator 8 with sedimentation basin inlet and connected by pipeline with reactor inlet, high concentration
Waste water tank 9 is connected with anaerobic pond inlet by pipeline and liquid level sensor is provided with the inwall of reservoir 1, is set in reactor 2
Agitator is equipped with, agitator includes the stirring motor installed in the upper end of reactor 2, stirring rod is provided with stirring motor, stirs
Rod is located in reactor 2, and anaerobism filler support is provided with anaerobic pond 3, and anaerobism filler is provided with anaerobism filler support, good
Aerobic filler support is provided with oxygen pond 4,Aerobic filler supportOn be provided with aerobic filler, the bottom in Aerobic Pond 4 is provided with
Micro-hole aerator, the quantity of micro-hole aerator is ten, and ten micro-hole aerators are evenly distributed on Aerobic Pond4On interior bottom,
Micro-hole aerator is connected by steel pipe with High-Pressure Compressor, and Inlet and outlet water baffle plate, Inlet and outlet water baffle plate are provided with sedimentation basin 5
Quantity be two, one in two Inlet and outlet water baffle plates is arranged on sedimentation basin inlet, and it is heavy that therein another is arranged on
On the liquid outlet of shallow lake pond.
Ozone generator 8 carries out strong oxidation reaction by ozone to antibiotic, lowers its toxicity, high-concentration sewage is being detested
In oxygen pond 3, by anaerobe to its anaerobic biodegradation, lower its pollutional load, be easy to follow-up Aerobic biological process,
The sewage that anaerobic pond 3 pre-processes existsAerobic Pond 4It is interior, by the biodegradation of aerobic microbiological, mitigate its pollutional load significantly, sink
Activated sludge in shallow lake pond 5 in gravitational settling sewage and the biomembrane to come off；Meanwhile the activated sludge for the loss that flows back.
In order to which the material that smell is produced in middle waste water is removed, the preferable technical scheme of the present embodiment is, in addition to activity
Charcoal absorber 6 and blower fan 7, active carbon adsorber 6 connect with sedimentation basin 5, and blower fan 7 connects with active carbon adsorber 6.
Essence of the present utility model is described in detail above embodiment, but can not be to of the present utility model
Protection domain is limited, it should be apparent that, under enlightenment of the present utility model, those of ordinary skill in the art can be with
Carry out many improvement and modification, it should be noted that these are improved and modification all falls in claim of the present utility model protection
Within the scope of.
Claims (5)
- A kind of 1. antibiotic waste water processing unit, it is characterised in that it include reservoir (1), reactor (2), anaerobic pond (3), Aerobic Pond (4), sedimentation basin (5), ozone generator (8) and high-concentration waste water pot (9), the reservoir (1) connect with reactor (2) Logical, the reactor (2) connects with anaerobic pond (3), and the anaerobic pond (3) connects with Aerobic Pond (4), the Aerobic Pond (4) and Sedimentation basin (5) connects, and the ozone generator (8) connects with reactor (2), the high-concentration waste water pot (9) and anaerobic pond (3) Connect, liquid level sensor is provided with the inwall of the reservoir (1), agitator is provided with the reactor (2), it is described to stir The stirring motor that device includes being arranged on reactor (2) upper end is mixed, stirring rod, the stirring rod position are provided with the stirring motor In reactor (2), anaerobism filler support is provided with the anaerobic pond (3), anaerobism is provided with the anaerobism filler support Filler, the Aerobic Pond (4) is interior to be provided with aerobic filler support, and aerobic filler is provided with the aerobic filler support, described Bottom in Aerobic Pond (4) is provided with micro-hole aerator, and the micro-hole aerator is connected by steel pipe with High-Pressure Compressor, Inlet and outlet water baffle plate is provided with the sedimentation basin (5).
- 2. antibiotic waste water processing unit according to claim 1, it is characterised in that opened respectively on the reservoir (1) Provided with reservoir inlet and reservoir liquid outlet, reactor inlet and reactor are offered respectively on the reactor (2) Liquid outlet, offers anaerobic pond inlet and anaerobic pond liquid outlet on the anaerobic pond (3) respectively, on the Aerobic Pond (4) point Aerobic Pond inlet and Aerobic Pond liquid outlet are not offered, are offered sedimentation basin inlet on the sedimentation basin (5) respectively and are sunk Shallow lake pond liquid outlet, the reservoir liquid outlet are connected by pipeline with reactor inlet, and the reactor liquid outlet passes through pipe Road is connected with anaerobic pond inlet, and the anaerobic pond liquid outlet is connected by pipeline with Aerobic Pond inlet, and the Aerobic Pond goes out Liquid mouth is connected with sedimentation basin inlet, and the ozone generator (8) is connected by pipeline with reactor inlet, the high concentration Waste water tank (9) is connected by pipeline with anaerobic pond inlet.
- 3. antibiotic waste water processing unit according to claim 1, it is characterised in that it also includes active carbon adsorber (6) connected with blower fan (7), the active carbon adsorber (6) with sedimentation basin (5), the blower fan (7) and active carbon adsorber (6) Connection.
- 4. antibiotic waste water processing unit according to claim 2, it is characterised in that the quantity of the micro-hole aerator is Ten, ten micro-hole aerators are evenly distributed on the bottom in Aerobic Pond.
- 5. antibiotic waste water processing unit according to claim 1, it is characterised in that the quantity of the Inlet and outlet water baffle plate is Two, one in two Inlet and outlet water baffle plates is arranged on sedimentation basin inlet, and therein another goes out liquid installed in sedimentation basin On mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720272616.3U CN206736017U (en) | 2017-03-20 | 2017-03-20 | Antibiotic waste water processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720272616.3U CN206736017U (en) | 2017-03-20 | 2017-03-20 | Antibiotic waste water processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206736017U true CN206736017U (en) | 2017-12-12 |
Family
ID=60557972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720272616.3U Active CN206736017U (en) | 2017-03-20 | 2017-03-20 | Antibiotic waste water processing unit |
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| Country | Link |
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| CN (1) | CN206736017U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862936A (en) * | 2018-08-13 | 2018-11-23 | 云南林强建设工程有限公司 | A kind of technique and device for disinfecting pharmacy waste water |
| CN109231704A (en) * | 2018-10-30 | 2019-01-18 | 黄心 | A kind of method of the microbial bacteria flora of efficient degradation antibiotic and antibiotic of degrading |
| CN110981116A (en) * | 2019-12-27 | 2020-04-10 | 扬州大学 | Treatment process of lincomycin antibiotic production wastewater |
-
2017
- 2017-03-20 CN CN201720272616.3U patent/CN206736017U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862936A (en) * | 2018-08-13 | 2018-11-23 | 云南林强建设工程有限公司 | A kind of technique and device for disinfecting pharmacy waste water |
| CN109231704A (en) * | 2018-10-30 | 2019-01-18 | 黄心 | A kind of method of the microbial bacteria flora of efficient degradation antibiotic and antibiotic of degrading |
| CN110981116A (en) * | 2019-12-27 | 2020-04-10 | 扬州大学 | Treatment process of lincomycin antibiotic production wastewater |
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