CN205687645U - A kind of Multilevel A/O Technology biological tank scum silica frost removal device - Google Patents

A kind of Multilevel A/O Technology biological tank scum silica frost removal device Download PDF

Info

Publication number
CN205687645U
CN205687645U CN201620548466.XU CN201620548466U CN205687645U CN 205687645 U CN205687645 U CN 205687645U CN 201620548466 U CN201620548466 U CN 201620548466U CN 205687645 U CN205687645 U CN 205687645U
Authority
CN
China
Prior art keywords
zone
weir plate
stationary partition
under water
biological tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201620548466.XU
Other languages
Chinese (zh)
Inventor
李震
杨海
李詹寅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TIANJIN HUASHUI WATER CONSTRUCTION Co Ltd
Original Assignee
TIANJIN HUASHUI WATER CONSTRUCTION Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TIANJIN HUASHUI WATER CONSTRUCTION Co Ltd filed Critical TIANJIN HUASHUI WATER CONSTRUCTION Co Ltd
Priority to CN201620548466.XU priority Critical patent/CN205687645U/en
Application granted granted Critical
Publication of CN205687645U publication Critical patent/CN205687645U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Removal Of Floating Material (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

This utility model relates to a kind of Multilevel A/O Technology biological tank scum silica frost removal device, biological tank includes the anaerobic zone separated by stationary partition, anoxic zone, aerobic zone, anaerobic zone, anoxic zone is respectively communicated with aerobic zone by the exhalant canal being located on described stationary partition, it is characterized in that stationary partition is that top is along the not stationary partition under water in water, arrange along the weir plate slide rail adjustable weir plate moving up and down that stationary partition two ends are fixedly mounted with under water in its anaerobic zone or side, anoxic zone, adjustable weir plate intercepts water plate in the vertical downward formation in the exhalant canal position of stationary partition under water described in correspondence, adjustable weir plate two ends are hinged with a vertical screw rod lower end by connecting shaft respectively, vertically screw rod upper end connects linear screw motor, two described linear screw motors are all connected to control its controller synchronizing start and stop;The adjustable weir plate of slagging-off state, upper along highly flushing with stationary partition under water;The adjustable weir plate of non-slagging-off state, upper edge exceeds anaerobic zone or anoxic zone liquid level.

Description

A kind of Multilevel A/O Technology biological tank scum silica frost removal device
Technical field
This utility model relates to sewage treatment process facility field, particularly relates to a kind of Multilevel A/O Technology biological tank scum silica frost and goes Except device.
Background technology
In recent years, Multilevel A/O Technology puies forward the emphasis technique of mark transformation as urban wastewater treatment firm denitrogenation dephosphorizing, exists Whole nation large amount of sewage treatment plant is applied, and much mutation technique occurs, such as multistage multi-stage process, improved cascade AO technique Deng, it is provided with the treatment effect of stabilizing energy-saving.Wherein, Multilevel A/O Technology is typically by anaerobic zone and 2 grades to 4 grades continuous print anoxic zones It is composed in series with aerobic zone respectively.Wherein, anaerobic zone and anoxic zone all carry out strict region disconnecting by partition wall, prevent aerobic zone The short stream of mixed liquor enter, bring dissolved oxygen into, destroy anaerobism and the state of anoxia.
Additionally, in most Multilevel A/O Technologies run, the problem that the most generally there is scum silica frost accumulation.This is due to multistage AO work The anaerobic zone of skill and anoxic zone quantity and area far surpass A2The technique such as O, oxidation ditch, internal waterpower hybrid mode typically use every Plate or agitator., generally there is hydraulic flow state dead angle in both modes, can produce scum silica frost, mud scum in anaerobic zone and anoxic zone Accumulation, not only account for pond and hold, and give an offensive smell, pollute environment, be repugnant to the eye, the most do not clear up a large amount of accumulation, water can be caused The shortening of the power time of staying, affects Nitrogen/Phosphorus Removal, and the artificial cost that wastes time and energy of dragging for clearly of scum silica frost, mud scum, improve fortune Battalion's cost.
Utility model content
Main purpose of the present utility model is for the problems referred to above, it is provided that one can adjust automatically according to hydraulics Except the Multilevel A/O Technology biological tank scum silica frost removal device of scum silica frost in Aeration tank, thus exempt the artificial clear of expense goods, materials and equipments of wasting time and energy Drag for, improve environment, improve Nitrogen/Phosphorus Removal, the process quality of lifting sewage, and promote Multilevel A/O Technology automatically control water Flat raising.
This utility model solves its technical problem and be the technical scheme is that
A kind of Multilevel A/O Technology biological tank scum silica frost removal device, described biological tank includes by detesting that multiple stationary partitions separate Oxygen district, anoxic zone and aerobic zone, described anaerobic zone, anoxic zone are respectively communicated with by the exhalant canal being located on respective stationary partition Aerobic zone, it is characterised in that described stationary partition is edge, the top not stationary partition under water in water, in anaerobic zone and side, anoxic zone Stationary partition under water on arrange along stationary partition two ends are fixedly mounted with under water weir plate slide rail adjustable weir plate moving up and down, described Adjustable weir plate intercepts water plate in the vertical downward formation in the exhalant canal position of stationary partition under water described in correspondence, and adjustable weir plate two ends are divided Not Tong Guo connecting shaft hinged with a vertical screw rod lower end, described vertical screw rod upper end connect linear screw motor, two described directly Line screw rod motor is all connected to control its controller synchronizing start and stop;Adjustable weir plate under slagging-off state, along height with under water on it Stationary partition flushes;Adjustable weir plate under non-slagging-off state, along anaerobic zone or the anoxic zone liquid level exceeding correspondence on it.
Described stationary partition top is along less than corresponding anaerobic zone or anoxic zone liquid level 30-40cm.
The intercepter plate area of described adjustable weir plate accounts for the 20%-30% of described exhalant canal cross-sectional area, non-slagging-off state Under the upper edge of adjustable weir plate exceed anaerobic zone or the anoxic zone liquid level 5-10cm of correspondence.
It is horizontal linear shape that waterside is crossed at the top of described adjustable weir plate.
The beneficial effects of the utility model are: compared with the prior art, utilize pulling flow type biological tank fluidised form principle to carry out dynamically Baffle design, can be along the weir that stationary partition two ends are fixedly mounted with under water by arranging on anaerobic zone and side, anoxic zone stationary partition under water The adjustable weir plate that plate slide rail moves up and down, makes the height of stationary partition under water become adjustable, makes scum silica frost mud scum get rid of in time, solves The problem that in Multilevel A/O Technology, biological tank accumulates scum silica frost, it is achieved automatically adjust removal anaerobic zone and anoxic zone according to hydraulics The effect of scum silica frost.Thus, exempt the artificial of expense goods, materials and equipments of wasting time and energy and drag for clearly, improve environment, improve Nitrogen/Phosphorus Removal, promote dirt The process quality of water.During work, the linear screw motor at adjustable weir plate two ends control its height promoting and declining, according to floating The accumulation time of slag, sets the interval time of linear screw motor, thus promotes the automatic control level of Multilevel A/O Technology Raising, full-automatic unmanned control on duty can be realized.This utility model can carry out non-stop production reformation on existing Process ba-sis, Simple for structure, be suitable to promote in multistage AO sewage treatment process field.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model and application thereof;
Fig. 2 is the A direction view of Fig. 1;
Fig. 3 is the structural representation at connecting shaft position.
In figure: 1 linear screw motor, 2 vertical screw rods, 3 connecting shafts, 4 adjustable weir plates, 41 intercept water plate, and 5 weir plate slide rails, 6 go out Aquaporin, 7 stationary partitions, 8 water inlets, 9 anaerobic zones or the liquid level of anoxic zone, 10 controllers, 11 mounting rings, I anaerobic zone, II lacks Oxygen district, III aerobic zone.
Below in conjunction with drawings and Examples, this utility model is described in detail.
Detailed description of the invention
Fig. 1-3 illustrates a kind of Multilevel A/O Technology biological tank scum silica frost removal device and application thereof, and described biological tank includes by solid Determining anaerobic zone I, anoxic zone II and aerobic zone III that partition wall 7 separates, described anaerobic zone I, anoxic zone II are by being located at each self-retaining Exhalant canal 6 on partition wall 7 is respectively communicated with aerobic zone III, and the Multilevel A/O Technology biological tank scum silica frost provided due to this utility model goes Except the device application in biological tank anaerobic zone I, anoxic zone II is identical, therefore, Fig. 1, Fig. 2 have employed simple schematic diagram.
Of the present utility model be characterised by described stationary partition 7 be top along the not stationary partition under water in water, in construction, This is less than corresponding anaerobic zone or anoxic zone liquid level 30-40cm in edge, stationary partition top under water.
The stationary partition under water of anaerobic zone I and side, anoxic zone II is arranged along the weir plate that stationary partition two ends are fixedly mounted with under water Slide rail 5 adjustable weir plate 4 moving up and down, it is horizontal linear shape that waterside is crossed at the top of described adjustable weir plate, and adjustable weir plate 4 exists The vertical downward formation in the position of the exhalant canal 6 of stationary partition 7 under water described in correspondence intercepts water plate 41, in practice of construction, adjustable The area of the intercepter plate 41 of weir plate 4 accounts for the 20%-30% of described exhalant canal cross-sectional area.
Adjustable weir plate 4 two ends are hinged with vertical screw rod 2 lower end by connecting shaft 3 respectively, and described vertical screw rod 2 upper end is even Connecing linear screw motor 1, two linear screw motors 1 are all connected to control its controller 10 synchronizing start and stop.See Fig. 3, this reality Execute in example, 4 liang of vertex angle parts of adjustable weir plate and vertically screw rod 2 bottom be all connected mounting ring 11, connecting shaft 3 have employed bolt and passes Two mounting ring 11 nut lockings, it is achieved adjustable weir plate 4 is hinged with vertical screw rod 2.It is articulated and connected and makes the upper of adjustable weir plate 4 Rise to decline and improve flexibility.Controller 10 can use PLC programmable controller, also can use based on the time relay Control circuit realizes the synchronization on off control to two linear screw motors 1.Thus control adjustable weir plate 4 and steadily lift.Slagging-off Adjustable weir plate 4 under state, it flushes along height with stationary partition under water;Adjustable weir plate under non-slagging-off state, edge on it Exceeding anaerobic zone or the anoxic zone liquid level of correspondence, in actual application, the upper edge of the adjustable weir plate under non-slagging-off state exceeds correspondence Anaerobic zone or anoxic zone liquid level 5-10cm.
Biological tank run time, treatment sewage enters biological tank anaerobic zone I, anoxic zone II from water inlet 8, due to scum silica frost, Mud scum is as what AO process operation was gradually piled up, under non-slagging-off state, controls linear screw motor 1 by controller 10 inverse Hour hands rotate, and the upper edge that vertical screw rod 2 is exercised adjustable weir plate 4 exceeds the liquid level 9 of anaerobic zone I or anoxic zone II, and being adjusted to can The upper edge of weir transfer plate exceeds anaerobic zone or the anoxic zone liquid level 5-10cm of correspondence.At this moment, the function of adjustable weir plate 4 is equivalent to increase The height of stationary partition under water, thus stop that the fluid of anaerobic zone I or anoxic zone II flows into aerobic zone III.Along with AO technique is transported OK, scum silica frost, mud scum are piled up, and now start slagging-off operation, under controller 10 controls, control linear screw motor 1 dextrorotation Turning, vertical screw rod is exercised for 2 times and is flushed with edge, the top of stationary partition 7 under water along height on adjustable weir plate 4, and now, liquid level is higher than under water The edge, top of stationary partition, simultaneously as the descending water outlet section making exhalant canal 6 of the plate 41 that intercepts water diminishes, surface flow rate of water flow carries Rising, scum silica frost progressively flows out to follow-up process section aerobic zone III, is ultimately discharged into sedimentation tank and carries out the separation removal of scum silica frost.
It can be seen that this utility model utilizes pulling flow type biological tank fluidised form principle to carry out dynamic baffle design, by detesting Arrange on the stationary partition under water of oxygen district and side, anoxic zone along the weir plate slide rail 41 that stationary partition two ends are fixedly mounted with under water can on move down Dynamic adjustable weir plate 4, makes the height of stationary partition under water become adjustable, thus solves biological tank in Multilevel A/O Technology and accumulate floating The problem of slag.During work, the linear screw motor 1 at adjustable weir plate two ends control its height promoting and declining;According to scum silica frost Accumulation time, set linear screw motor the interval time, thus can realize full-automatic unmanned control on duty.
This utility model, can carry out non-stop production reformation on existing Process ba-sis, simple for structure, is suitable to multistage AO sewage treatment process field is promoted.
Any pro forma restriction not made by structure of the present utility model, shape and material by above content.Every foundation Any simple modification, equivalent variations and the modification that above example is made by technical spirit of the present utility model, all still falls within this In the range of utility model technical scheme.

Claims (5)

1. a Multilevel A/O Technology biological tank scum silica frost removal device, described biological tank includes the anaerobism separated by multiple stationary partitions District, anoxic zone and aerobic zone, described anaerobic zone, anoxic zone are respectively communicated with by the exhalant canal being located on respective stationary partition Oxygen district, it is characterised in that described stationary partition is top along the not stationary partition under water in water, in anaerobic zone and side, anoxic zone Arrange along stationary partition two ends are fixedly mounted with under water weir plate slide rail adjustable weir plate moving up and down under water on stationary partition, described can Weir transfer plate intercepts water plate in the vertical downward formation in the exhalant canal position of stationary partition under water described in correspondence, and adjustable weir plate two ends are respectively Hinged with a vertical screw rod lower end by connecting shaft, described vertical screw rod upper end connects linear screw motor, two described straight lines Screw rod motor is all connected to control its controller synchronizing start and stop;Adjustable weir plate under slagging-off state, along height with solid under water on it Determine partition wall to flush;Adjustable weir plate under non-slagging-off state, along anaerobic zone or the anoxic zone liquid level exceeding correspondence on it.
A kind of Multilevel A/O Technology biological tank scum silica frost removal device the most according to claim 1, it is characterised in that described fixing Partition wall top is along less than corresponding anaerobic zone or anoxic zone liquid level 30-40cm.
A kind of Multilevel A/O Technology biological tank scum silica frost removal device the most according to claim 1 and 2, it is characterised in that described can The intercepter plate area of weir transfer plate accounts for the 20%-30% of described exhalant canal cross-sectional area, the adjustable weir plate under non-slagging-off state Upper edge exceeds anaerobic zone or the anoxic zone liquid level 5-10cm of correspondence.
A kind of Multilevel A/O Technology biological tank scum silica frost removal device the most according to claim 3, it is characterised in that described adjustable It is horizontal linear shape that waterside is crossed at the top of weir plate.
A kind of Multilevel A/O Technology biological tank scum silica frost removal device the most according to claim 1 and 2, it is characterised in that described can It is horizontal linear shape that waterside is crossed at the top of weir transfer plate.
CN201620548466.XU 2016-06-06 2016-06-06 A kind of Multilevel A/O Technology biological tank scum silica frost removal device Active CN205687645U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620548466.XU CN205687645U (en) 2016-06-06 2016-06-06 A kind of Multilevel A/O Technology biological tank scum silica frost removal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620548466.XU CN205687645U (en) 2016-06-06 2016-06-06 A kind of Multilevel A/O Technology biological tank scum silica frost removal device

Publications (1)

Publication Number Publication Date
CN205687645U true CN205687645U (en) 2016-11-16

Family

ID=57260933

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620548466.XU Active CN205687645U (en) 2016-06-06 2016-06-06 A kind of Multilevel A/O Technology biological tank scum silica frost removal device

Country Status (1)

Country Link
CN (1) CN205687645U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105858892A (en) * 2016-06-06 2016-08-17 天津市华水自来水建设有限公司 Multi-stage AO process biological pool dross removal device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105858892A (en) * 2016-06-06 2016-08-17 天津市华水自来水建设有限公司 Multi-stage AO process biological pool dross removal device

Similar Documents

Publication Publication Date Title
CN105417904B (en) Thorough cut sludge elutriating separates and waste water treating and reutilizing method
CN201777915U (en) Chemical degreasing sediment separator
CN110589922B (en) Flotation rectifying air floatation tank
CN202688032U (en) Efficient air floatation water-purification reaction device
CN201195707Y (en) Concentrating pool for turbid return water disposal process
CN110935213B (en) Large-diameter center transmission hydraulic sectional automatic rake-lifting thickener
CN101613164A (en) Inclined tube floating device for waste water treatment
CN201890788U (en) Double-layered pressure type oil remover
CN102794036B (en) Water-level-variable terminal catchment inclined tube or inclined plate sedimentation tank
CN101874943A (en) High-density clarifying tank
CN205687645U (en) A kind of Multilevel A/O Technology biological tank scum silica frost removal device
CN105858892A (en) Multi-stage AO process biological pool dross removal device
CN104671321A (en) Efficient dissolved air flotation machine
CN201890787U (en) Double-layered pressure type integrated deoiler
CN201626866U (en) Water distribution device of horizontal subsurface wetland sewage treatment system
CN204569607U (en) A kind of quick dewatering machine and the Sewage treatment systems based on quick dewatering machine
CN102432101A (en) Modified sequencing batch reactor (MSBR) process for sewage treatment
CN201737775U (en) Full-effect drop thrust aeration integrated oxidation ditch
CN105749592B (en) A kind of connectivity structure between treatment tank
CN105107240A (en) Treatment device for floating objects in sewage
CN201439031U (en) High-density clarification tank
CN201148371Y (en) Aluminum oxide industrial production wastewater treatment recycling apparatus
CN107698113B (en) Industrial wastewater centralized treatment system and method
CN207608441U (en) A kind of cyanobacteria water plant processing ship
CN113716724A (en) Wastewater treatment device and wastewater treatment method

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant