CN205676349U - Ozone microbubble floatation thickening device - Google Patents
Ozone microbubble floatation thickening device Download PDFInfo
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- CN205676349U CN205676349U CN201620580538.9U CN201620580538U CN205676349U CN 205676349 U CN205676349 U CN 205676349U CN 201620580538 U CN201620580538 U CN 201620580538U CN 205676349 U CN205676349 U CN 205676349U
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- eddy current
- phase blender
- phase
- ozone
- blender
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 76
- 230000008719 thickening Effects 0.000 title claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
- 239000003814 drug Substances 0.000 claims abstract description 35
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000002893 slag Substances 0.000 claims abstract description 16
- 238000000926 separation method Methods 0.000 claims description 16
- 230000001174 ascending effect Effects 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000000740 bleeding effect Effects 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 62
- 239000007789 gas Substances 0.000 abstract description 41
- 239000000377 silicon dioxide Substances 0.000 abstract description 31
- 238000005188 flotation Methods 0.000 abstract description 10
- 238000002156 mixing Methods 0.000 abstract description 9
- 230000018044 dehydration Effects 0.000 abstract description 7
- 238000006297 dehydration reaction Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 7
- 239000000356 contaminant Substances 0.000 abstract description 6
- 239000002245 particle Substances 0.000 abstract description 6
- 230000003647 oxidation Effects 0.000 abstract description 3
- 238000007254 oxidation reaction Methods 0.000 abstract description 3
- 239000010802 sludge Substances 0.000 description 29
- 238000000034 method Methods 0.000 description 26
- 229920002401 polyacrylamide Polymers 0.000 description 22
- 230000008569 process Effects 0.000 description 15
- 239000003344 environmental pollutant Substances 0.000 description 12
- 231100000719 pollutant Toxicity 0.000 description 12
- 239000010865 sewage Substances 0.000 description 10
- 239000007787 solid Substances 0.000 description 10
- 239000002351 wastewater Substances 0.000 description 10
- 239000010801 sewage sludge Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 238000007667 floating Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 239000007943 implant Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000003750 conditioning effect Effects 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000010842 industrial wastewater Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- -1 iron salt Chemical class 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000013043 chemical agent Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 239000003295 industrial effluent Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000008247 solid mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 241001672694 Citrus reticulata Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 235000015110 jellies Nutrition 0.000 description 1
- 239000008274 jelly Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000005036 potential barrier Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of ozone microbubble floatation thickening device.This device includes reactive tank, ozonator, slag remover, dreg collecting slot, is arranged side by side the eddy current three-phase blender of 46 groups of series connection above reactive tank.Mud is sent into by pressurization intake pump and is formed eddy current in multi-stage vortex three-phase blender；Ozone is sent in first order eddy current three-phase blender by gas boosting pump or air compressor machine；PAM medicament is pumped in the second level or third level eddy current three-phase blender by adding of agent；In multi-stage vortex three-phase blender, medicament contacts with contaminant particle, water, gas three mixing, and eddy current produces microbubble and forms flco；In flco, entrained air bubbles floats to be formed on liquid level scum silica frost.It is quenched that this utility model achieves mud by the oxidation effect of multi-stage vortex three-phase blender and ozone, is obtained in that moisture content 90～the air-flotation scum of 95%, follow-up supertension elasticity squeezer or the dehydration of sheet frame dewaterer simultaneously.
Description
Technical field
This utility model belongs to technical field of sludge treatment, relates to a kind of ozone microbubble floatation thickening device, it is adaptable to
Mud is quenched, concentration, and the scum silica frost after quenched concentration enters supertension elasticity squeezer and carries out press dewatering.
Background technology
Mud is the product after sewage disposal, is that one is made up of organic relic, microorganism, inorganic particle, colloid etc.
Extremely complex heterogeneous body.The key property of mud is that moisture content is high (may be up to more than 99%), and content of organics is high, holds
Easily corruption is smelly, and granule is relatively thin, and proportion is less, jelly liquid, and it is the concentrated thing between liquid and solid.Closely
Nian Lai, along with China's economy and the fast development of sewage disposal technology, the sludge quantity of generation the most quickly improves, and thus brings
Specific resistance to filtration problem day by day draw attention.Owing to sludge of sewage treatment plant moisture content is high, generation amount is big, and volume is big, easily
Producing stench, in Treatment of Sludge, most important link is just by sludge dewatering, is separated by the solid, liquid in mud, at present
The mud major part of sewage treatment plant uses the dehydration of mechanical dehydration, especially supertension elasticity squeezer or sheet frame dewaterer.One
As activated sludge (referring to the precipitate that activated sludge method processing technique second pond produces), its moisture content is up to about 99%.When
When moisture percentage in sewage sludge is down to 95% by 99%, the volume of mud can narrow down to original 1/5.To mud effectively, enter economically
One step processes, and reduces it and stores occupation of land, must first carry out sludge condensation.
In order to improve supertension elasticity squeezer or the efficiency of sheet frame dewaterer dehydration, also first mud is concentrated.
Domestic gravity concentration (precipitation) mode that uses the earliest, this kind of condensing mode concentrate after moisture percentage in sewage sludge be generally 95～
97%, exist floor space compared with big, concentrated effect is poor, concentrate after moisture percentage in sewage sludge high, easily fermentation produces the defects such as foul smell, limit
Make its development.The sludge condensation mode that at present sewage treatment plant is conventional is to use mechanical thickening, as dense in screw press formula, belt
Contracting machines etc., although this kind of condensing mode floor space is little, surrounding environment influence is little, but its cost is high, and power consumption is high, especially this kind
The mud extraction moisture content of condensing mode is high, and it is high that PAM adds rate, and equipment failure rate is high, there is also the problems such as washing water quantity is big, also limits
Its development.
In order to improve the dewatering of mud, before sludge pump excess of imports high-pressure elastomeric squeezer or sheet frame dewaterer are dehydrated,
It is also performed to mud modifier treatment.The conventional conditioning mode that conditioning mode is iron salt+Calx, but this conditioning mode introduces
Heavy metal iron ion, calcium ion, and add mud butt, it is unfavorable for follow-up Treatment of Sludge and disposal.
Along with China's urban development needs, land resource is in short supply, and highly desirable a kind of floor space is little, and treatment effect shows
Write, novel sludge concentration device that after process, moisture percentage in sewage sludge is low and the quenched method for concentration of mud.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of ozone microbubble floatation thickening dress
To put, to solve the problem that mud hardening and tempering method is unreasonable, sludge condensation mass dryness fraction is the highest of the prior art, it is achieved mud is quenched+
High mass dryness fraction concentrates synchronization and carries out, and is beneficial to the squeezing of supertension elasticity or the dehydration of sheet frame dewaterer of follow-up mud.
The technical solution of the utility model is as follows:
A kind of ozone microbubble floatation thickening device, it includes a reactive tank, is arranged side by side 4～6 groups above reactive tank
The eddy current three-phase blender that (4～6 grades) connect, is the first order by water outlet side, is afterbody by influent side, (i.e. from water outlet side
It is arranged in order as the first order, the second level to influent side ... N level), it is provided with A reactor in every grade of eddy current three-phase blender；
Reactive tank is separated into three rooms by weir plate from influent side to water outlet side: contact chamber, separation chamber and clear water collecting chamber；Above separation chamber
Slag remover is set, below the slag remover other end, dreg collecting slot is set；The outlet of water inlet manifold one end and intake pump is connected, the other end and the
The lateral inflow mouth of primary vortex three-phase blender connects；The bottom outlet of first order eddy current three-phase blender and whirlpool, the second level
The lateral inflow mouth of stream three-phase blender connects；... by that analogy, the bottom outlet of previous stage eddy current three-phase blender with
The lateral inflow mouth of rear stage eddy current three-phase blender connects；The bottom outlet of afterbody eddy current three-phase blender directly connects
Connect a release pipe；Release pipe outlet is positioned at reactive tank contact chamber bottom；The lateral inflow mouth of every primary vortex three-phase blender
The water inlet pipe at place is provided with bypass ascending pipe；The outlet of medicament preparation facilities is connected with adding of agent pump intake；Drug-feeding tube one end with
Adding of agent pump discharge connect, the drug-feeding tube other end respectively with the second level, the lateral inflow mouth of third level eddy current three-phase blender
The bypass ascending pipe at place connects；Ozone generator outlet is connected with gas boosting pump or air compressor machine entrance；Air inlet pipe one end and gas
Body booster pump or air compressor machine outlet connect, and the other end is connected with the top air inlet of first order eddy current three-phase blender；The third level
The gas outlet, top of eddy current three-phase blender connects an exhaustor；Exhaustor is provided with air bleeding valve.
Further, separation chamber is provided above slag remover, and the slag remover other end extends horizontally to above dreg collecting slot；Dreg collecting slot
Top less than the bottom of eddy current three-phase blender；Dreg collecting slot bottom is a greater part of is to tilt, and the inclination end is positioned at clear water collecting chamber
Top.
Further, the water inlet pipe at the lateral inflow mouth of every primary vortex three-phase blender is vertical with bypass ascending pipe.
Further, water inlet manifold is provided with effusion meter；Every primary vortex three-phase blender top is equipped with Pressure gauge.
Air inlet pipe is provided with intake valve, is additionally provided with check valve after intake valve.Check valve it also is provided with on drug-feeding tube.Dreg collecting slot is provided with liquid
Position meter.
A kind of quenched method for concentration of mud utilizing above-mentioned ozone microbubble floatation thickening device to carry out is as follows:
Mud (including domestic sewage sludge, industrial wastewater sludge, copper water-supply pipe) uses pressurization intake pump, by water inlet
Pipe, is conveyed in multi-stage vortex three-phase blender formation eddy current, i.e. after first order eddy current three-phase blender serially enters successively
In what eddy current three-phase blender of face；After ozone has been prepared by ozonator, compressed by gas boosting pump or air compressor machine,
After promoting the pressure of ozone gas, it is conveyed in first order eddy current three-phase blender by air inlet pipe；PAM medicament (polyacrylamide
Amine) after medicament preparation facilities prepares, use pressurized medicament to add pump, by drug-feeding tube, add the second level and the third level
On eddy current three-phase blender, the bypass ascending pipe at the lateral inflow mouth of eddy current three-phase blender injects and (is perpendicular to current side
To injecting or oblique injection)；In multi-stage vortex three-phase blender in the contact chamber of reactive tank, pressurized ozone is directly dissolved in
In incoming waste water, and then PAM medicament directly adds to molten gas-liquid, and medicament connects with contaminant particle (solid), water, gas three
Touching mixing, eddy current produces microbubble and implants in pollutant, and pollutant are captured, and forms flco；Separation chamber, flco press from both sides
Band bubble, floats to be formed on liquid level scum silica frost, completes solid-liquid separation；Utilizing slag remover to automatically remove scum silica frost, scum silica frost enters collection slag
Groove is collected or is processed；Collect clear water at clear water collecting chamber, reaction tank bottom discharge.
Moisture content is the mud (domestic sewage sludge, industrial wastewater sludge or copper water-supply pipe) of 98.5～99.5%, passes through
After this ozone microbubble floatation thickening device carries out quenched, concentration, it is thus achieved that the scum silica frost of higher mass dryness fraction, containing of this air-flotation scum
Water rate is 90～95%；Scum silica frost after this is quenched, without adding any medicament, can be fed directly to supertension elasticity squeezer and enter
Row squeezing, the moisture content of the cake after squeezing can reach 55～65%.
Intake pump is arranged on water inlet manifold road, and intake pump pressure is 0.6～0.9Mpa；First order eddy current three-phase blender
Pressure the highest (0.6～0.9Mpa), after pressure in what eddy current three-phase blender successively decrease the most one by one.
After PAM medicament (polyacrylamide) prepares, use pressurized medicament to add pump, add in the second level or third level whirlpool
On stream three-phase blender；The pressure that adds of PAM adding of agent pump is slightly larger than intake pump pressure (i.e. slightly larger than 0.6～0.9MPa).
The dosage of PAM medicament is 0.002～0.006gPAM/gDS (dewatered sludge).
This floatation thickening device is provided with ozone and prepares throwing device ozonator.Ozone (O3) it is the coordination of oxygen
Element, the oxidation-reduction potential in water is 2.07V, and oxidability is strong.By adding ozone in residual active sludge, by part
Bacterial oxidation is cell debris, and after cell breakage, protein, nucleic acid etc. are released, and makes mud reach quenched, strengthens follow-up
The performance of sludge dewatering.Due to ozone extremely unstable, it is impossible to load as other gas in bottle and use, can only be with producing with making
With.Therefore in this floatation thickening device and technique, it is provided with ozonator, after prepared by ozone, by gas boosting pump
Or air compressor machine compression, after promoting the pressure of ozone gas, it is conveyed in first order eddy current three-phase blender by air delivering pipeline.Smelly
The pressure of carrier of oxygen (i.e. gas boosting pump or the pressure of air compressor machine outlet) slightly larger than intake pump pressure (i.e. slightly larger than 0.6～
0.9MPa).Ozone dosage is 0.006～0.010gO3/ gDS (dewatered sludge).
The beneficial effects of the utility model:
Ozone microbubble floatation thickening device of the present utility model, for carrying out quenched concentration to mud.This utility model
Floatation thickening device and the quenched method for concentration of mud, by by a kind of special eddy current three-phase mixer application in the gas of mud
Floating concentration technology, and to propose the source of the gas used by air supporting be ozone, it is possible to the scum silica frost obtain high mass dryness fraction, being tempered, this scum silica frost can be straight
Connect in pumping into follow-up supertension elasticity squeezer or sheet frame squeezer and be dehydrated.
Ozone microbubble floatation thickening device of the present utility model and the quenched method for concentration of mud, it is possible to realize mud quenched
(PAM medicament and waste water, ozone are simultaneously introduced eddy current three-phase blender, by the physical action of multi-stage vortex three-phase blender
And ozone that the oxidation effect of mud is achieved mud is quenched), the alternative quenched mode of iron salt+Calx, improve mud
Dewatering；It is obtained in that the air-flotation scum (moisture content 90～95%) of higher mass dryness fraction simultaneously, is beneficial to follow-up supertension
Elastic squeezer or the dehydration of sheet frame dewaterer.
Ozone microbubble floatation thickening device of the present utility model, has a following characteristic:
Core component in A, ozone microbubble floatation thickening device is the water of a kind of special tectonic, gas, solid three-phase vortex
Mixing reactor (i.e. eddy current three-phase blender), collect molten gas, differential stirring, granule attachment, flco aerating, molten gas nucleus generate and
Bubble release function is in one；By eddy current three-phase blender, flco is formed and is formed in the same time with bubble nucleus, causes wadding
Body is huge and porous, rises rapidly；All incoming waste waters are by 100% aerating, it is not necessary to water circulating pump and clear water reserviors；Reactive tank is by weir
Plate is separated into three rooms: contact chamber, separation chamber and clear water collecting chamber；In eddy current three-phase blender in contact chamber, medicament with
Contaminant particle (solid), water, gas three contact mixing, and eddy current produces microbubble and also implants in pollutant, and pollutant are captured,
Form flco；Entrained air bubbles in separation chamber, flco, floats on liquid level, completes solid-liquid separation, and rear portion only needs to scrape slag i.e.
Can；Clear water water outlet is collected at clear water collecting chamber.This device PAM dosing is few, and the moisture content of scum silica frost is more dry；
B, the source of the gas of ozone microbubble floatation thickening device are slightly larger than 0.6～the ozone of 0.9MPa pressure, utilize ozone
Strong oxidizing property to make air-flotation scum obtain quenched；
C, the high mass dryness fraction of mud concentrate and mud dosing is quenched is carried out simultaneously, and air-flotation scum is follow-up quenched without dosing again,
It is directly entered supertension elasticity squeezer or the dehydration of sheet frame dewaterer.
The technical characteristic of ozone microbubble floatation thickening device of the present utility model is, it is achieved that equipment is integrated, dirty
Mud is quenched, the innovation of Mud up-floating, eliminate dissolved air water prepare, circulation and the bubble attaching process of slow poor efficiency, real
Show unprecedented scum silica frost removal efficiency (scum silica frost clearance reaches more than 99%), save the floor space of more than 90% and big
Amount capital expenditure expense.Owing to removal efficiency is high, rear class can be substantially reduced and process the load of technique and increase its stability.By
Aqueous less and closely knit in produced scum silica frost, scum silica frost can be greatly reduced and house the volume in pond.Whole technique more may be used
Lean on, floor space and operating cost are all substantially reduced.
The principle of ozone microbubble floatation thickening device of the present utility model is contrary with gravity concentration, and bubble adhesion is suspending
As carrier on thing, form the gas-solid mixture that density is lighter than water, float to the water surface, so that suspended contamination is separated from water,
Then scraping into mud drainage slot with scraper plate by thickened sludge, sludge water is then discharged from the bottom of pond.Of the present utility model have the quenched work of mud
Ozone microbubble floatation thickening device, compare gravity concentration, there is concentration speed fast, the time of staying is short, scum silica frost moisture content
The feature such as low, effluent quality is high, floor space is little.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model a kind of ozone microbubble floatation thickening device；
Fig. 2 is the workflow schematic diagram of ozone microbubble floatation thickening device of the present utility model；
Fig. 3 is the structural representation of the eddy current three-phase blender of six grades of series connection in this utility model.
In figure: 1. intake pump 2. effusion meter 3. air compressor machine 4. intake valve 5. reactive tank A, contact chamber B, separation chamber
C, clear water collecting chamber 6. dreg collecting slot 7. liquidometer 8. slag remover 9. air bleeding valve 10. Pressure gauge 11. eddy current three-phase blender
Water inlet pipe 15. at the lateral inflow mouth of 12. drug-feeding tube 13. water inlet manifold 14. eddy current three-phase blenders bypasses ascending pipe
16, ozonator 17, adding of agent pump 18, medicament preparation facilities
Detailed description of the invention
Below in conjunction with drawings and Examples, this utility model is further described.
Embodiment 1
As shown in Figure 1, Figure 3, this utility model one ozone microbubble floatation thickening device, it includes a reactive tank 5,
Be arranged side by side above reactive tank eddy current three-phase blender that six groups (six grades) connect 11 (be arranged in order from water outlet side to influent side into
The first order, the second level ... the 6th grade), it is provided with A reactor in every grade of eddy current three-phase blender；Reactive tank from influent side to
Water outlet side is separated into three rooms by weir plate, it may be assumed that contact chamber A, separation chamber B and clear water collecting chamber C；Separation chamber B is provided above slagging-off
Machine 8, slag remover 8 other end extends horizontally to above dreg collecting slot 6；The top of dreg collecting slot 6 is less than the end of eddy current three-phase blender 11
Portion；Dreg collecting slot 6 bottom is a greater part of is to tilt, and the inclination end is positioned at above clear water collecting chamber C；Water inlet manifold 13 one end and intake pump
1 outlet connects；Water inlet manifold 13 other end is connected with the lateral inflow mouth of first order eddy current three-phase blender；On water inlet manifold 13
It is provided with effusion meter 2；The bottom outlet of first order eddy current three-phase blender and the lateral inflow of second level eddy current three-phase blender
Mouth connects；... by that analogy, the bottom outlet of previous stage eddy current three-phase blender and rear stage eddy current three-phase blender
Lateral inflow mouth connects；The bottom outlet of afterbody (the 6th grade) eddy current three-phase blender is directly connected to a release pipe；
Release pipe outlet is positioned at reactive tank contact chamber A bottom；Water inlet pipe 14 at the lateral inflow mouth of every primary vortex three-phase blender
It is provided with vertical bypass ascending pipe 15；Medicament preparation facilities 18 outlet is connected with adding of agent pump 17 entrance；Drug-feeding tube 12 1
End with adding of agent pump 17 export be connected, drug-feeding tube 12 other end respectively with the second level, the side of third level eddy current three-phase blender
The bypass ascending pipe 15 of water inlet, face connects；Ozonator 16 outlet is connected with air compressor machine 3 entrance；Air inlet pipe one end is with empty
Press 3 outlet connects, and the other end is connected with the top air inlet of first order eddy current three-phase blender；Third level eddy current three-phase mixes
The gas outlet, top of device connects an exhaustor；Exhaustor is provided with air bleeding valve 9.Every primary vortex three-phase blender top is all provided with
There is Pressure gauge 10.Air inlet pipe is provided with intake valve 4, is additionally provided with check valve after intake valve 4.It also is provided with unidirectional on drug-feeding tube 12
Valve.Dreg collecting slot 6 is provided with liquidometer 7, for controlling the start and stop of follow-up deslagging pump.
Ozone microbubble floatation thickening device of the present utility model is the one of pressure air-dissolving air-float, this by microbubble with
Micro-floccule concurrently forms and combines, and then the process jointly growing into band gas flco is referred to as " copolymerization ".Bubble is the least, more
It is easily accessible flco, or quilt wadding catches, thus form stable copolymerization flco.It discharges the micro-of highly dense in time delay
Bubble, when being sufficiently mixed with mixed reaction water of offeing medicine, both grow up simultaneously, and the band gas flco so formed was floating
The advantages such as Cheng Zhong, has floating fast, and scum silica frost is stable, and the tolerance of consumption is few.
The design principle of ozone microbubble floatation thickening device of the present utility model is: utilize eddy current three-phase blender,
Waste water is directly added into gas and medicament, completes molten gas and stirring simultaneously, finally realize self-skimming.Eddy current three-phase blender collection is molten
The stirring of gas, differential, flco aerating, granule attachment, the generation of molten gas nucleus and bubble release function are in one.Its workflow bag
Include: 2. the highest pressure solution gas stretch medicament and be 3. sufficiently stirred for 4. nucleus and form 5. bubble and condense 6. flco and merge that 8. 7. scum silica frost is quenched follows
Ring flocculates.Eddy current three-phase blender and the difference of tradition air-dissolving air-float: maximally utilise chemical agent；Form ultralight hollow
Flco, makes flco moisture content and proportion reduce, and flco is solid and has and the strongest goes up i, beneficially self-skimming voluntarily.
As in figure 2 it is shown, the work process of ozone microbubble floatation thickening device of the present utility model is: (1) intakes: use
Waste water is formed eddy current from regulating reservoir input multi-stage vortex three-phase blender by pressurization intake pump；(2) aerating/dosing mixing is stirred
Mix: in multi-stage vortex three-phase blender, pressurized ozone being directly dissolved in incoming waste water, and then chemical agent is directly thrown
Add in molten gas-liquid, complete medicament and mix with contaminant particle (solid), water, gas three-phase；Agent molecule is initially coil-shape, whirlpool
Flow and agent molecule stretching is put forward effect, be sufficiently stirred for；(3) eddy current produces microbubble and implants in float: medicament and pollutant
After grain, water, gas mixture are discharged in the contact chamber A of reactive tank, then weir flow enters separation chamber B, and eddy current produces microbubble and plants
Entering in pollutant, pollutant are captured, and flco is formed and floats；(4) release float；(5) slag remover is utilized to automatically remove floating
Slag；Scum silica frost (mud) enters dreg collecting slot 6 and collects or process；Collect clear water at clear water collecting chamber C, reaction tank bottom discharge.
Ozone microbubble floatation thickening device of the present utility model, produces microbubble by eddy current three-phase blender, adheres to
As carrier in float, form the gas-solid mixture that density is lighter than water, float to the water surface, so that suspended contamination and water
Separate；Can effectively remove solid suspended particles, oils, turbidity and the Organic substance etc. in complex wastewater；Effectively facilitate pollutant
Efficient process, reach outstanding effects of energy saving and emission reduction.
Ozone microbubble floatation thickening device of the present utility model quotes external eddy current three-phase hybrid technology, at eddy current three-phase
In blender, current produce fierce eddy current, thus reach medicament, water, the differential stirring of gas and mixing.Use bypass ascending pipe
Flocculant is injected the raw water tubes (i.e. water inlet pipe) import department's (i.e. lateral inflow mouth of eddy current three-phase blender close to reaction zone
Place), the caliber of bypass ascending pipe is more small than the caliber of raw water tubes, and the aperture of bypass ascending pipe is perpendicular to former with the biggest speed
The direction injection of water pipe current, flocculant is injected former water flow turbulence intensity maximum when (in breach and near nodal position
Put), the most easily quickly mix with former water.Flocculant mixing can be divided into three sections, and first paragraph is potential barrier section, jet in this section
Flow velocity is constant, and jet starts water former with surrounding and mixes；Second segment is deviation section, in raw water tubes under the effect of current jet to water
Flow path direction deviation, and mix with former water further；3rd section is whirlpool section, if there is carried interest whirlpool above the water flow section of jet
Whirlpool, makes jet spread rapidly, is thoroughly mixed with former water.In a word, through breach and node, there is violent convergence, disperse, turn
To, tear, therefore forming countless little whirlpool, make medium turbulent fluctuation and Surface Renewal speed greatly speed up, liquid-film resistance is greatly lowered, institute
The highest with mass transfer rate.
The feature of ozone microbubble floatation thickening device of the present utility model is as follows:
1, high pressure solution gas: pressurized ozone 100% is dissolved in and becomes a mandarin in sewage, the most pneumatically supported bubble attachment reason
Opinion, this step realizes contaminant molecule and contacts gas attachment under dissolved state with the least limit of bubble；
2, medicament is stretched: generally polymer is in strand when adding and kinks agglomerating state, and this product is distinctive efficiently
Blender can will kink the stretching of agglomerating strand and become strip strand, makes agent molecule chain institute electrically charged can fully be exposed profit
With, reduce waste；
3, be sufficiently stirred for: multi-stage, efficient blender by various effective speeds realize medicament and pollutant be fully contacted with
Mixing.Enable pollutant by entrained by agent molecule chain and the electric charge that exposes adsorbs securely；
4, scum silica frost is formed: along with the reduction of pressure, the gas of the dissolved gradually forms countless pole by pollutant flco
Thin bubble, is grown directly upon among mud flco；
5, bubble cohesion: bubble constantly merges expansion, produces the granule of spongy flco；
6, flco merges: during flocs float, the rapid coalescence of tiny flco, and bubble the most drastically expands simultaneously,
Tie up the space of flco internal clearance water, make flco moisture content and proportion reduce further, flco solid and have the strongest voluntarily
Upper i；
7, quenched scum silica frost: scum silica frost floats up to Chi Mianshang, mutually piles up, is bonded to scum silica frost blanket, forms entirety and floats, moisture content
Reduce further；
8, effluent collection: the water outlet of floatation thickening is discharged by reaction tank bottom, enters collector pipe and collects clear water zone；
9, scum layer controls: controls water outlet liquid level by regulation weir plate, thus controls the thickness of scum layer.
Embodiment 2-5
A kind of ozone microbubble floatation thickening device utilized described in embodiment 1 of this utility model carries out the quenched concentration of mud
Method as follows: (embodiment 2-5 processes the most in this way)
Mud (domestic sewage sludge, industrial wastewater sludge, copper water-supply pipe) uses pressurization intake pump, by water inlet pipe, defeated
Send into and multi-stage vortex three-phase blender formed eddy current, i.e. from first order eddy current three-phase blender serially enter successively below what
In eddy current three-phase blender；After ozone has been prepared by ozonator, compressed by gas boosting pump or air compressor machine, promote smelly
After the pressure of carrier of oxygen, it is conveyed in first order eddy current three-phase blender by air inlet pipe；PAM medicament is through medicament preparation facilities system
After getting ready, use pressurized medicament to add pump, by drug-feeding tube, add on the second level and third level eddy current three-phase blender, from
Bypass ascending pipe at the lateral inflow mouth of eddy current three-phase blender injects (being perpendicular to water (flow) direction inject)；Connecing at reactive tank
Touching in indoor multi-stage vortex three-phase blender, pressurized ozone is directly dissolved in incoming waste water, and and then PAM medicament is directly thrown
Adding in molten gas-liquid, medicament contacts with contaminant particle (solid), water, gas three mixing, and eddy current produces microbubble and also implants dirt
In dye thing, pollutant are captured, and form flco；Entrained air bubbles in separation chamber, flco, floats to be formed on liquid level scum silica frost,
Complete solid-liquid separation；Utilizing slag remover to automatically remove scum silica frost, scum silica frost enters dreg collecting slot and collects or process；Collect at clear water collecting chamber
Clear water, is discharged by reaction tank bottom.
Moisture content is the mud of 98.5～99.5%, carries out quenched, concentration through this ozone microbubble floatation thickening device
After process, it is thus achieved that the scum silica frost of higher mass dryness fraction, the moisture content of this air-flotation scum is 90～95%；Scum silica frost after this is quenched is without adding
Any medicament, can be fed directly to supertension elasticity squeezer and squeeze, the moisture content of the cake after squeezing can reach 55～
65%.
PAM added amount of chemical is 0.002～0.006gPAM/gDS (dewatered sludge), ozone dosage be 0.006～
0.010gO3/ gDS (dewatered sludge).Intake pump pressure is 0.6～0.9Mpa；Pressure (i.e. gas boosting pump or the sky of ozone gas
The pressure of press outlet) slightly larger than intake pump pressure (i.e. slightly larger than 0.6～0.9MPa)；PAM adding of agent pump add pressure
Slightly larger than intake pump pressure (i.e. slightly larger than 0.6～0.9MPa).The pressure of first order eddy current three-phase blender the highest (0.6～
0.9Mpa), after, the pressure in what eddy current three-phase blender successively decreases the most one by one.
Embodiment 2: process object be certain sanitary sewage water source be the residue that the second pond of main sewage treatment plant is discharged
Mud (moisture content 99%), uses the ozone microbubble floatation thickening device of embodiment 1 to carry out quenched, concentration: PAM adds
Amount is 0.003gPAM/gDS (dewatered sludge), and ozone dosage is 0.00625gO3/ gDS (dewatered sludge)；Intake pump pressure is
About 0.8Mpa；The pressure (i.e. gas boosting pump or the pressure of air compressor machine outlet) of ozone gas is slightly larger than intake pump pressure (slightly
More than 0.8MPa)；The pressure that adds of PAM adding of agent pump is slightly larger than intake pump pressure (slightly larger than 0.8 MPa).First order eddy current
The pressure of three-phase blender is the highest (about 0.8Mpa), the pressure in follow-up eddy current three-phase blender successively decrease one by one (as 0.7Mpa,
0.6Mpa, 0.5Mpa, 0.4Mpa, 0.3Mpa or 0.2Mpa, measured value may have deviation with above-mentioned data).
After, concentration quenched through ozone microbubble floatation thickening device of the present utility model, it is thus achieved that air-flotation scum
Moisture content is 93%.Scum silica frost after this is quenched no longer adds any medicament, is fed directly to the squeezing of supertension elasticity squeezer, pressure
Moisture content of the cake after squeezing reaches 59%.
Embodiment 3: process object be certain grocery trade waste water be the second pond of main industrial effluent treatment plant discharge surplus
Remaining mud (moisture content 98.7%), uses the ozone microbubble floatation thickening device of embodiment 1 to carry out quenched, concentration: PAM
Dosage is 0.0035gPAM/gDS, and ozone dosage is 0.008gO3/ gDS (dewatered sludge)；Intake pump pressure is that 0.6Mpa is left
Right；The pressure of ozone gas is slightly larger than intake pump pressure (slightly larger than 0.6MPa)；The pressure that adds of PAM adding of agent pump is slightly larger than
Intake pump pressure (slightly larger than 0.6 MPa).The pressure of first order eddy current three-phase blender is the highest (about 0.6Mpa), follow-up eddy current three
Pressure in phase blender successively decreases one by one.
After, concentration quenched through ozone microbubble floatation thickening device of the present utility model, it is thus achieved that air-flotation scum
Moisture content is 94%.Scum silica frost after this is quenched no longer adds any medicament, is fed directly to the squeezing of supertension elasticity squeezer, pressure
Moisture content of the cake after squeezing reaches 62%.
Embodiment 4: process object be certain sanitary sewage water source be the residue that the second pond of main sewage treatment plant is discharged
Mud (moisture content 98.5%), uses the ozone microbubble floatation thickening device of embodiment 1 to carry out quenched, concentration: PAM and throws
Dosage is 0.006gPAM/gDS, and ozone dosage is 0.010gO3/ gDS (dewatered sludge)；Intake pump pressure is about 0.7Mpa；
The pressure of ozone gas is slightly larger than intake pump pressure (slightly larger than 0.7MPa)；PAM adding of agent pump add pressure be slightly larger than into
Water-aspirator pressure (slightly larger than 0.7 MPa).The pressure of first order eddy current three-phase blender is the highest (about 0.7Mpa), follow-up eddy current three-phase
Pressure in blender successively decreases one by one.
After the ozone microbubble quenched concentration of floatation thickening device of the present utility model, it is thus achieved that air-flotation scum contain
Water rate is 90%.Scum silica frost after this is quenched no longer adds any medicament, is fed directly to the squeezing of supertension elasticity squeezer, squeezing
After moisture content of the cake reach 55%.
Embodiment 5: process object be certain grocery trade waste water be the second pond of main industrial effluent treatment plant discharge surplus
Remaining mud (moisture content 99.5%), uses the ozone microbubble floatation thickening device of embodiment 1 to carry out quenched, concentration: PAM
Dosage is 0.002gPAM/gDS, and ozone dosage is 0.006gO3/ gDS (dewatered sludge)；Intake pump pressure is that 0.9Mpa is left
Right；The pressure of ozone gas is slightly larger than intake pump pressure (slightly larger than 0.9MPa)；The pressure that adds of PAM adding of agent pump is slightly larger than
Intake pump pressure (slightly larger than 0.9 MPa).The pressure of first order eddy current three-phase blender is the highest (about 0.9Mpa), follow-up eddy current three
Pressure in phase blender successively decreases one by one.
After the ozone microbubble quenched concentration of floatation thickening device of the present utility model, it is thus achieved that air-flotation scum contain
Water rate is 95%.Scum silica frost after this is quenched no longer adds any medicament, is fed directly to the squeezing of supertension elasticity squeezer, squeezing
After moisture content of the cake reach 65%.
Claims (8)
1. an ozone microbubble floatation thickening device, it is characterised in that it includes a reactive tank, sets side by side above reactive tank
Put the eddy current three-phase blender of 4～6 grades of series connection, be the first order by water outlet side, be afterbody by influent side；Reactive tank is from water inlet
Side is separated into three rooms to water outlet side by weir plate: contact chamber, separation chamber and clear water collecting chamber；Separation chamber is provided above slag remover,
Below the slag remover other end, dreg collecting slot is set；Water inlet manifold one end is connected with intake pump outlet, the other end and first order eddy current three
The lateral inflow mouth of phase blender connects；The bottom outlet of first order eddy current three-phase blender mixes with second level eddy current three-phase
The lateral inflow mouth of device connects；By that analogy, the bottom outlet of previous stage eddy current three-phase blender and rear stage eddy current three-phase
The lateral inflow mouth of blender connects；The bottom outlet of afterbody eddy current three-phase blender is directly connected to a release pipe；
Release pipe outlet is positioned at reactive tank contact chamber bottom；Set on water inlet pipe at the lateral inflow mouth of every primary vortex three-phase blender
There is bypass ascending pipe；The outlet of medicament preparation facilities is connected with adding of agent pump intake；Drug-feeding tube one end and adding of agent pump discharge
Connect, the drug-feeding tube other end respectively with the second level, third level eddy current three-phase blender lateral inflow mouth at bypass ascending pipe
Connect；Ozone generator outlet is connected with gas boosting pump or air compressor machine entrance；Air inlet pipe one end and gas boosting pump or pneumatics
Machine outlet connects, and the other end is connected with the top air inlet of first order eddy current three-phase blender；Third level eddy current three-phase blender
Gas outlet, top connect an exhaustor；Exhaustor is provided with air bleeding valve.
2. ozone microbubble floatation thickening device as claimed in claim 1, it is characterised in that the slag remover other end is horizontal-extending
Above dreg collecting slot；The top of dreg collecting slot is less than the bottom of eddy current three-phase blender；Dreg collecting slot bottom is a greater part of is to tilt, and inclines
Wedged bottom is positioned at above clear water collecting chamber.
3. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that every primary vortex three-phase mixes
Water inlet pipe at the lateral inflow mouth of clutch is vertical with bypass ascending pipe.
4. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that water inlet manifold is provided with stream
Gauge.
5. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that every primary vortex three-phase mixes
Clutch top is equipped with Pressure gauge.
6. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that air inlet pipe is provided with air inlet
Valve, is provided with check valve after intake valve.
7. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that drug-feeding tube is provided with unidirectional
Valve.
8. ozone microbubble floatation thickening device as claimed in claim 1 or 2, it is characterised in that dreg collecting slot is provided with liquid level
Meter.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620580538.9U CN205676349U (en) | 2016-06-14 | 2016-06-14 | Ozone microbubble floatation thickening device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620580538.9U CN205676349U (en) | 2016-06-14 | 2016-06-14 | Ozone microbubble floatation thickening device |
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| CN205676349U true CN205676349U (en) | 2016-11-09 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105859076A (en) * | 2016-06-14 | 2016-08-17 | 上海同臣环保有限公司 | Ozone microbubble air floating concentration device and sludge conditioning and concentration method |
| CN109851091A (en) * | 2019-01-18 | 2019-06-07 | 中国石油工程建设有限公司 | The efficient microbubble oil removal by air bubbling oil removal system of oil gas field brine waste and technique |
-
2016
- 2016-06-14 CN CN201620580538.9U patent/CN205676349U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105859076A (en) * | 2016-06-14 | 2016-08-17 | 上海同臣环保有限公司 | Ozone microbubble air floating concentration device and sludge conditioning and concentration method |
| CN109851091A (en) * | 2019-01-18 | 2019-06-07 | 中国石油工程建设有限公司 | The efficient microbubble oil removal by air bubbling oil removal system of oil gas field brine waste and technique |
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| C14 | Grant of patent or utility model | ||
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161109 |