CN206126893U - Multistage air supporting tower of vertical flow type - Google Patents
Multistage air supporting tower of vertical flow type Download PDFInfo
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- CN206126893U CN206126893U CN201621004833.6U CN201621004833U CN206126893U CN 206126893 U CN206126893 U CN 206126893U CN 201621004833 U CN201621004833 U CN 201621004833U CN 206126893 U CN206126893 U CN 206126893U
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Abstract
The utility model belongs to multistage air supporting tower of vertical flow type, all be provided with the sewage water inlet on every grade of air supporting tower body, dissolve gas import, dross discharge port, gas vent, delivery port and drain, be provided with air supporting in every grade of air supporting tower and dissolve trachea, dissolved air releaser and honeycomb duct, be provided with the baffle between every grade, the gas vent sets up the top every grade of air supporting, the dross discharge port sets up the lower extreme at the gas vent, the sewage water inlet sets up the lower extreme at the dross discharge port, the drain setting in baffle upper end, dissolve gas import lower extreme, honeycomb duct one end is connected with the delivery port in the air supporting tower, and other end setting is dissolved below the trachea in air supporting, dissolve gas access connection dissolved air releaser, dissolved air releaser is last to be provided with air supporting and to dissolve the trachea, between upward one -level air supporting drain is connected with next stage air supporting gas vent. The utility model discloses throughput is big, efficient, the occupation of land is few. Internal structure is simple, maintains and overhauls easily. Elimination sludge bulking that can be better and reducing can float SS with SS can sink.
Description
Technical field
This utility model belongs to technical field of sewage, and in particular to one kind is used for oil-containing, wastewater efficient containing float
The vertical-flow multi stage flotation column for processing.
Background technology
In recent years, air supporting is widely used in sewage disposal, and especially the application in oil-polluted water field is more extensive.
Air supporting is that a kind of micro-bubble of utilization high degree of dispersion goes to stick the wadding grain in water for carrier, by the buoyance lift of bubble
Effect so as to which buoyancy, so as to realize the mandatory floating of grain of wadding a quilt with cotton, reaches a kind of detached skill of solid, liquid more than gravity and floating resistance
Art, can be divided into dispersion Bubble-floating Method, dissolved air flotation and electrolytic gas float glass process etc., at present in oil-containing, suspended matter-containing wastewater process often
For pressurized dissolved air flotation.
The principle of air-dissolving air-float is under an increased pressure, to make air soluble in water, forms air hypersaturated state, is then subtracted
To normal pressure, air is separated out, form a large amount of to close microbubble group, and make float and colloid micro- in slow uphill process
Grain, in bubble surface enrichment, and floats on the surface of the water with bubble, so as to reach the purpose for removing SS and CODcr, realizes air supporting.Pressurization
The main body of air-dissolving air-float can be divided into air-dissolving apparatus and gas floatation separation device, be usually used in having air supporting as gas floatation separation device at present
Pond and the class of air flotation tank two., due to structure and design problem, generally there is floor space big, molten in traditional flotation tank and air flotation tank
The problems such as gas release is easily blocked, daf efficiency is low, equipment is complicated.
The content of the invention
The purpose of this utility model is to provide a kind of new vertical-flow multi stage flotation column, overcomes the deficiencies in the prior art.
The technical solution of the utility model is as follows:
A kind of vertical-flow multi stage flotation column, is provided with sewage inlet, molten gas import, scum silica frost row on every grade of air supporting tower body
Outlet, air vent, outlet and sewage draining exit, in every grade of air supporting tower dissolved air floatation pipe, dissolved air release and mozzle are provided with;Often
Dividing plate is provided between level;Air vent is arranged on per grade of pneumatically supported the top;Scum silica frost outlet is arranged on the lower end of air vent;It is dirty
Water water inlet is arranged on the lower end of scum silica frost outlet;Sewage outfalls setting is in dividing plate upper end, molten gas import lower end;Air supporting tower Inner guide
Pipe one end is connected with outlet, and the other end is arranged on below dissolved air floatation pipe;Molten gas import connects dissolved air release, molten gas release
Dissolved air floatation pipe is provided with device;Between upper level air supporting sewage draining exit and the connection of next stage air supporting air vent.
The dividing plate is tilting, and angle of inclination is 5~10 °.It is arranged on upper level air supporting sewage draining exit and next stage air supporting
Between air vent, and less than upper level air supporting sewage draining exit, higher than next stage air vent.
The refluxing opening is arranged on afterbody air supporting sewage outlet lower end, 100~150mm of distance.
The air vent is arranged on per grade of pneumatically supported the top or is arranged on every grade of air supporting space bar 50~100mm of lower end
Place.
The scum silica frost outlet is arranged on the lower end of air vent, the 50~150mm of spacing with air vent.
The sewage mouth is arranged on the lower end of scum silica frost outlet, the 100~200mm of spacing with scum silica frost outlet.
The sewage outlet is arranged between wastewater inlet and scum silica frost outlet 1/2;Afterbody outlet of sewer
Tower body end is arranged at the 300mm of tower body bottom.
The sewage outfalls setting is per grade of pneumatically supported bottom or at 20~100mm of dividing plate.
The molten gas import is arranged at 200~500mm of dividing plate.
Wherein afterbody air supporting arranges refluxing opening and liquidometer, is not provided with mozzle.
During utility model works, floccule body float to the surface in the presence of lift of gas forms scum silica frost, subsequently into air supporting
Area.Floccule body float to the surface in the presence of lift of gas forms scum silica frost, and the clear water of lower floor passes through water outlet mozzle, into next stage
Air supporting, the scum silica frost on the flotation tank water surface is accumulated to after certain thickness, is discharged by scum silica frost mouth, and the SS that can sink is in tower body bottom
Precipitation, periodically excludes.
The utility model has the advantages that:Vertical-flow multi stage flotation column combines flotation tank and air flotation tank is multiple is used in series
Feature, disposal ability is big, efficiency high, take up an area it is few.Internal structure is simple, and it is easy to safeguard and overhaul.Sludge can preferably be eliminated swollen
It is swollen and reduce floating and SS and can sink SS.The air separated out during air supporting to going eliminating water in surfactant and stink have bright
Aobvious effect, while increased the dissolved oxygen in water, reduces part insolubility COD, and for subsequent treatment favourable bar is provided
Part.Dividing plate between every grade of air supporting adopts tilting dividing plate, is conducive to the discharge of precipitate.
Description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is embodiment of the present utility model intention;
Wherein:1. sewage running piping, 2. one-level air supporting water inlet, 3. one-level air supporting water outlet mozzle, 4. one-level air supporting
Outlet, 5. one-level air supporting outlet and two grades of water inlet connecting tubes, the 6. pneumatically supported molten gas import of one-level, 7. one-level air supporting are molten
Trachea, 8. one-level air suspension dissolved air releaser, 9. one-level air-flotation scum outlet, 10. one-level air supporting sewage draining exit, 11. one-level air supportings
Air vent, 12. secondary air-floatation water inlets, 13. secondary air-floatation water outlet mozzles, 14. secondary air-floatation outlets, 15. secondary air-floatations
Outlet and three-level water inlet connecting tube, the molten gas import of 16. secondary air-floatations, 17. secondary air-floatation Gas dissolving pipes, 18. secondary air-floatations
Dissolved air release, 19. secondary air-floatation scum silica frost outlets, 20. secondary air-floatation sewage draining exits, 21. secondary air-floatation air vents, 22. three-levels
Air supporting water inlet, 23. three-level air supporting outlets, 24. water drainage pipelines, 25. refluxing openings, the pneumatically supported molten gas import of 26. three-levels,
27. three-level dissolved air floatation pipes, 28. three-level air suspension dissolved air releasers, 29. three-level air-flotation scum outlets, 30. three-level air supporting blowdowns
Mouth, 31. three-level air supporting air vents, 32. liquidometers, 33/34. air supporting space bar, 34. air supporting tower tower bodies;N and n+1 represents air supporting
's.
Specific embodiment
This utility model is described in further details below in conjunction with accompanying drawing 2 and embodiment (is with three-level air supporting tower
Example).
As shown in Fig. 2 arranging one-level air supporting water inlet 2, one-level air supporting water outlet mozzle 3, one-level air supporting water outlet on tower body
Mouthfuls 4, one-level air supporting outlet and the pneumatically supported molten gas import 6 of two grades of water inlet connecting tubes 5, one-level, one-level dissolved air floatation pipe 7,
Level air suspension dissolved air releaser 8, one-level air-flotation scum outlet 9, one-level air supporting sewage draining exit 10,11, two grades of one-level air supporting air vent
Air supporting water inlet 12, secondary air-floatation water outlet mozzle 13, secondary air-floatation outlet 14, secondary air-floatation outlet and three-level water inlet
The molten gas import 16 of connecting tube 15, secondary air-floatation, secondary air-floatation Gas dissolving pipe 17, secondary air-floatation dissolved air release 18, secondary air-floatation
Scum silica frost outlet 19, secondary air-floatation sewage draining exit 20, secondary air-floatation air vent 21, three-level air supporting water inlet 22, three-level air supporting water outlet
Mouth 23, water drainage pipeline 24, the pneumatically supported molten gas import 26 of refluxing opening 25, three-level, three-level dissolved air floatation pipe 27, three-level dissolved air floatation
Release 28, three-level air-flotation scum outlet 29, three-level air supporting sewage draining exit 30, three-level air supporting air vent 31, liquidometer 32, air supporting
Space bar 33.
Dividing plate is provided between per grade, dividing plate is tilting, and angle of inclination is 5~10 °;Air vent is arranged on every grade of air supporting
The top or be arranged at every grade of air supporting space bar 50~100mm of lower end, wherein one-level air supporting air vent is arranged on tower body top
End;Scum silica frost outlet is arranged on the lower end of air vent, the 50~150mm of spacing with air vent;Sewage inlet is arranged on scum silica frost
The lower end of outlet, the 100~200mm of spacing with scum silica frost outlet;Sewage outlet is arranged on wastewater inlet and discharges with scum silica frost
At between mouthful 1/2;Afterbody outlet of sewer is arranged on tower body end at the 300mm of tower body bottom, sewage outfalls setting every
Plate upper end, at 20~100mm of dividing plate;Molten gas import is arranged at 200~500mm of dividing plate;Refluxing opening is arranged on last
Level air supporting sewage outlet lower end, 100~150mm of distance;Air supporting tower Inner guide pipe one end is connected with outlet, and the other end sets
Put below dissolved air floatation pipe;Molten gas import connects dissolved air release, and dissolved air floatation pipe is provided with dissolved air release;Upper level
Between air supporting sewage draining exit and the connection of next stage air supporting air vent;Wherein afterbody air supporting arranges refluxing opening and liquidometer, does not set
Put mozzle.
During utility model works, the initial stage first will fill sewage in air supporting tower, and using air supporting pressue device air supporting is circulated, and make
In tower after the abundant air supporting of sewage, quantitatively into sewage.
Sewage is entered the one-level air supporting section of air supporting top of tower, molten gas by sewage running piping 1 by one-level air supporting water inlet 2
Enter from the pneumatically supported molten gas import 6 of one-level, a large amount of bubbles of generation are discharged by dissolved air release 8 by one-level air supporting pipe 7, on bubble
Rise after sticking with bubble with the float or oils in sewage, liquid layer surface is risen under buoyancy, form scum layer, float
Gravity flow when slag blanket did not had one-level pneumatically supported scum silica frost mouth 9 is discharged.Pass through mozzle 3 by outlet through the sewage of one-level air supporting slagging-off
4 discharge, and one-level air supporting is completed.
The sewage discharged by outlet 4 enters secondary air-floatation water inlet 12 by connecting tube 5, and molten gas is from the molten of secondary air-floatation
Gas import 16 is entered, and a large amount of bubbles of generation is discharged by dissolved air release 18 by one-level air supporting pipe 17, in bubble rising and sewage
Float or after oils and bubble stick, liquid layer surface is risen under buoyancy, form scum layer, scum layer did not had two
Gravity flow during level pneumatically supported scum silica frost mouth 19 is discharged.Discharged by outlet 14 by mozzle 13 through the sewage of secondary air-floatation slagging-off,
Secondary air-floatation is completed.
The sewage discharged by outlet 14 enters three-level air supporting water inlet 22 by connecting tube 15, and molten gas is pneumatically supported from three-level
Molten gas import 26 is entered, and a large amount of bubbles of generation are discharged by dissolved air release 28 by three-level air supporting pipe 27, and bubble rises and sewage
In float or oils and bubble stick after, liquid layer surface is risen under buoyancy, form scum layer, scum layer did not had
Gravity flow during three-level pneumatically supported scum silica frost mouth 29 is discharged.Gradually clarify from top to bottom through the pneumatically supported sewage of three-level, three-level air supporting pipe with
Under water quality it is optimum, a part is supplied to molten gas pressue device by refluxing opening 25, for providing the dissolved air water of air supporting tower;One
Divide and next processing unit is drained into by sewage pipe 24 by discharge outlet 23.Three-level air supporting is completed.
The gas produced during air supporting is focused on by tank top air vent 11/21/31.Tower body each several part
Bottom sediment is discharged respectively by sewage draining exit 10/20/30.
The above, only for illustrating this utility model, not to limit this utility model, in this utility model
Spirit and principle within, any those familiar with the art in the technical scope that this utility model is disclosed, institute
Any modification, replacement and the improvement made, all should cover within protection domain of the present utility model.
Claims (10)
1. a kind of vertical-flow multi stage flotation column, is provided with sewage inlet, molten gas import, scum silica frost discharge on every grade of air supporting tower body
Mouth, air vent, outlet and sewage draining exit, in every grade of air supporting tower dissolved air floatation pipe, dissolved air release and mozzle are provided with;Per grade
Between be provided with dividing plate;Air vent is arranged on per grade of pneumatically supported the top;Scum silica frost outlet is arranged on the lower end of air vent;Sewage
Water inlet is arranged on the lower end of scum silica frost outlet;Sewage outfalls setting is in dividing plate upper end, molten gas import lower end;Air supporting tower Inner guide pipe
One end is connected with outlet, and the other end is arranged on below dissolved air floatation pipe;Molten gas import connects dissolved air release, dissolved air release
On be provided with dissolved air floatation pipe;Between upper level air supporting sewage draining exit and the connection of next stage air supporting air vent.
2. multi stage flotation column as claimed in claim 1, is characterized in that the dividing plate is tilting, and angle of inclination is 5~10 °;
It is arranged between upper level air supporting sewage draining exit and next stage air supporting air vent, and less than upper level air supporting sewage draining exit, under being higher than
One-level air vent.
3. multi stage flotation column as claimed in claim 1, is characterized in that being arranged back in afterbody air supporting sewage outlet lower end
Head piece, 100~150mm of distance.
4. multi stage flotation column as claimed in claim 1, it is characterized in that the air vent be arranged on per grade of pneumatically supported the top or
It is arranged at every grade of air supporting space bar 50~100mm of lower end.
5. multi stage flotation column as claimed in claim 1, is characterized in that the scum silica frost outlet is arranged on the lower end of air vent, with
50~the 150mm of spacing of air vent.
6. multi stage flotation column as claimed in claim 1, is characterized in that the sewage mouth is arranged on the lower end of scum silica frost outlet, with
100~the 200mm of spacing of scum silica frost outlet.
7. multi stage flotation column as claimed in claim 1, is characterized in that the sewage outlet is arranged on wastewater inlet and scum silica frost
At between outlet 1/2;Afterbody outlet of sewer is arranged on tower body end at the 300mm of tower body bottom.
8. multi stage flotation column as claimed in claim 1, it is characterized in that the sewage outfalls setting per grade of pneumatically supported bottom or
At 20~100mm of dividing plate.
9. multi stage flotation column as claimed in claim 1, is characterized in that the molten gas import is arranged on away from 200~500mm of dividing plate
Place.
10. multi stage flotation column as claimed in claim 1, is characterized in that wherein afterbody air supporting arranges refluxing opening and liquid level
Meter, is not provided with mozzle.
Priority Applications (1)
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CN201621004833.6U CN206126893U (en) | 2016-08-30 | 2016-08-30 | Multistage air supporting tower of vertical flow type |
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CN201621004833.6U CN206126893U (en) | 2016-08-30 | 2016-08-30 | Multistage air supporting tower of vertical flow type |
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ID=58568440
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106219653A (en) * | 2016-08-30 | 2016-12-14 | 天津市振津石油天然气工程有限公司 | Vertical-flow multi stage flotation column |
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2016
- 2016-08-30 CN CN201621004833.6U patent/CN206126893U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106219653A (en) * | 2016-08-30 | 2016-12-14 | 天津市振津石油天然气工程有限公司 | Vertical-flow multi stage flotation column |
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