CN201317704Y - Biological filter tower - Google Patents

Biological filter tower Download PDF

Info

Publication number
CN201317704Y
CN201317704Y CNU2008201858024U CN200820185802U CN201317704Y CN 201317704 Y CN201317704 Y CN 201317704Y CN U2008201858024 U CNU2008201858024 U CN U2008201858024U CN 200820185802 U CN200820185802 U CN 200820185802U CN 201317704 Y CN201317704 Y CN 201317704Y
Authority
CN
China
Prior art keywords
urceolus
biological filter
inner core
outer cylinder
combined working
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.)
Expired - Fee Related
Application number
CNU2008201858024U
Other languages
Chinese (zh)
Inventor
洪树虎
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.)
JIANGSU BAINA ENVIRONMENT ENGINEERING Co Ltd
Original Assignee
JIANGSU BAINA ENVIRONMENT ENGINEERING 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 JIANGSU BAINA ENVIRONMENT ENGINEERING Co Ltd filed Critical JIANGSU BAINA ENVIRONMENT ENGINEERING Co Ltd
Priority to CNU2008201858024U priority Critical patent/CN201317704Y/en
Application granted granted Critical
Publication of CN201317704Y publication Critical patent/CN201317704Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

The utility model discloses a biological filter tower, which comprises an outer cylinder of the biological filter tower, wherein, the lower part of the outer cylinder is provided with an inlet water distributing pipe, and the middle part of the outer cylinder is provided with an aerated conduit, and the interior of the outer cylinder is provided with a filter material blocking layer, biological filter material ceramic material, active granular filter material and a filter material filling layer from up to down; an inner cylinder is also arranged inside the outer cylinder, and the lower part of the inner cylinder is connected with an outlet pipe which extends out of the outer cylinder, and the middle part of the inner cylinder is filled with a quartz sand filter layer. Compared with the traditional AO bio-chemical process, the construction expense of the biological filter tower is 60 to 70 percent, and the energy consumption is 80 to 90 percent, and the biological filter tower has the function of synchronic denitrification and dephosphorization; the quality of the produced water is equal to or less than 15mg/1; BOD is equal to or less than 5 mg/1; COD is equal to or less than 35 mg/1; NH3 is equal to or less than 6 mg/1; the biological filter tower is obviously better than other biological filter towers.

Description

Biological filtering tower combined working
Technical field
The utility model relates to a kind of advanced treatment apparatus that is applied to sub-district, trade effluent, particularly a kind of biological filtering tower combined working.
Background technology
Biological filtering tower combined working is as the term suggests comprise bio-reactor and filtering system, it is the combination of a kind of embrane method biological treatment and high efficiency filter device, utilize the huge specific surface area absorption microorganism of filtering material particle, sewage is in the filtrate process of flowing through, with a large amount of microorganisms of adsorbing on the filtering material particle complicated biochemical reaction taking place, makes the organic substance in the sewage generate CO 2, H 2Innoxious substances such as O reach the purpose that purifies water; The aging microorganism that comes off, suspended substance etc. guarantee that with through biofiltration or precipitation final outflow water is qualified in the sewage.Biological filtering tower combined working technology is general divides aerobic and two sections of biofiltrations, and leading portion is based on bio-oxidation, and it is auxilliary that absorption is held back, it is main that back segment absorption is held back, and bio-oxidation is auxilliary, exists biochemical efficiency low, because have only the aerobic biochemical reaction, for difficult biochemical substances, the organic degradation effect will be had a greatly reduced quality; Filter or a precipitation effect difference, because as adopting biofiltration, back segment has biochemical function concurrently, after the long-time running, the aging microorganism that comes off can cause that SS in the final outflow water, BOD raise, aging microorganism is removed in backwash, and the destruction that can cause microbial film and filtering layer again causes biochemical reaction and filter effect deficiency, as adopt coprecipitation mode, the words of dosing have increased investment source and working cost greatly, and the words sedimentation effect of not dosing is never desirable, and suspended substance is difficult to up to standard in the water.
The utility model content
Goal of the invention: the purpose of this utility model is at the deficiencies in the prior art, provides a kind of sewage load to rise the low biological filtering tower combined working of Yang Cheng.
Technical scheme: the utility model discloses a kind of biological filtering tower combined working, the urceolus that comprises biological filtering tower combined working, be provided with into water water distributor in the urceolus bottom, be provided with aerated conduit at the urceolus middle part, urceolus inside is provided with filtrate blocking layer, biofilter material pottery material, active particle filtrate and filtrate packing course from top to bottom successively, also be provided with an inner core in urceolus, the inner core bottom connects the rising pipe that stretches out urceolus, and quartzy sand filter blanket is filled at the middle part.
The utility model utilizes the design of inner core, has realized the double filtration effect, under the situation that does not increase the biological filtering tower combined working height, has improved filtration efficiency greatly.
In the utility model, at the inner core top water distributor is arranged, making the urceolus water outlet enter inner core can be evenly, inner core middle part filling quartz sand.Former water enters from outer tube bottom, enters inner core through overflow behind anaerobism, the aerobic reaction, through inner core filtering separation suspended solid, finally from interior tube bottom water outlet.
In the utility model, preferably, inner core top is connected with the inner core water distributor, and making the urceolus water outlet enter inner core can be evenly.
In the utility model, preferably, described water inlet water distributor is " rich " font structure.
As further improvement of the utility model, the described biofilter material material of making pottery is porous ceramic grain, thereby provides carrier for microorganism.
Beneficial effect: biological filtering tower combined working described in the utility model is compared with traditional AO biochemical process, and construction cost is 60~70%, and energy consumption is 80~90%, has the synchronous denitrification dephosphorizing function, effluent quality SS≤15mg/l, BOD≤5mg/l, COD≤35mg/l, NH 3≤ 6mg/l obviously is better than other biological filtering tower combined working.
Description of drawings
Fig. 1 is the utility model structure biological filtering tower combined working synoptic diagram.
Fig. 2 is the utility model process flow sheet.
Embodiment
Below in conjunction with accompanying drawing the utility model is done further explanation.
As shown in Figure 1, the utility model discloses a kind of biological filtering tower combined working, the urceolus 6 that comprises biological filtering tower combined working, be provided with the water inlet water distributor 1 that is " rich " font structure in urceolus 6 bottoms, be provided with aerated conduit 3 at urceolus 6 middle parts, urceolus 6 inside are provided with filtrate blocking layer 5, biofilter material pottery material 4, active particle filtrate 2 and filtrate packing course 11 from top to bottom successively, in urceolus 6, also be provided with an inner core 7, inner core 7 tops are connected with inner core water distributor 9, the bottom connects the rising pipe 10 that stretches out urceolus, and quartzy sand filter blanket 8 is filled at inner core 7 middle parts.In the utility model, described biofilter material is made pottery and is expected that 4 is porous ceramic grain.
Biological filtering tower combined working described in the utility model adopts that anticorrosion or stainless steel is welded with carbon steel, and equipment is made up of the urceolus and the inner core of two reducings and different diameter, and small diameter cylinder is positioned at inside the large cylinder, independent separately one-tenth system.Former water enters from the large cylinder bottom, enters inner core through overflow behind anaerobism, the aerobic reaction, through inner core filtering separation suspended solid, finally from interior tube bottom water outlet.
Outer tube bottom filling active particle filtrate, plays former water is adsorbed and Decomposition owing to be anaerobic state to the stack shell middle part.
As shown in Figure 2, workflow of the present utility model is: be made up of sewage pump system, one section anaerobic reactor, one section aerobic reactor, two sections strainers, filter tank recoil and air systems, two concentric drums are formed two technique units, and inner core is positioned at the urceolus the inside.Urceolus divides anaerobic and aerobic two systems, is the upward flow device, and inner core is a filtering system, and to the stream device, one section system's water outlet enters two sections water distributors through compiling, after filtering water outlet for down.
The utility model has been given full play to the bio-reactor dirty removal capacities, and waste water is at first by one section anaerobic reactor, and the organic macromolecule of difficult degradation is decomposed into the organic molecule of easy degraded, improves the biodegradability and the solvability of waste water greatly; The anaerobism water outlet is removed organism through one section aerobic reactor again; Outputted aerobic water is the suspended substance in independent two sections filtration system filters outputted aerobic water again, reach the solid-liquid separation purpose, when independent filtering system water outlet is defective, carry out backwash, do not influence the prime bioreactor function, fully overcome the shortcoming that biological filtering tower combined working is in the past held back biochemical efficiency difference after aging microorganism deficiency and the backwash.And urceolus has utilized the upward flow filtering material particle to be difficult for stopping up, and cuts the strong advantage of dirt (not needing dosing for particulate matters such as suspended substances) to the stream filtrate under the inner core, thereby has formed the COMBINED PROCESS of bio-oxidation and mechanical filter.
The utility model provides a kind of thinking and method of biological filtering tower combined working; the method and the approach of this technical scheme of specific implementation are a lot; the above only is a preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model principle, can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.The all available prior art of each component part not clear and definite in the present embodiment is realized.

Claims (3)

1, a kind of biological filtering tower combined working, the urceolus (6) that comprises biological filtering tower combined working, be provided with into water water distributor (1) in urceolus (6) bottom, be provided with aerated conduit (3) at urceolus (6) middle part, urceolus (6) inside is provided with filtrate blocking layer (5) from top to bottom successively, biofilter material is made pottery and expected (4), active particle filtrate (2) and filtrate packing course (11), it is characterized in that, in urceolus (6), also be provided with an inner core (7), the bottom connects the rising pipe (10) that stretches out urceolus, and quartzy sand filter blanket (8) is filled at inner core (7) middle part.
2, biological filtering tower combined working according to claim 1 is characterized in that, inner core (7) top is connected with inner core water distributor (9).
3, biological filtering tower combined working according to claim 1 is characterized in that, described biofilter material is made pottery and expected that (4) are porous ceramic grain.
CNU2008201858024U 2008-09-11 2008-09-11 Biological filter tower Expired - Fee Related CN201317704Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201858024U CN201317704Y (en) 2008-09-11 2008-09-11 Biological filter tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201858024U CN201317704Y (en) 2008-09-11 2008-09-11 Biological filter tower

Publications (1)

Publication Number Publication Date
CN201317704Y true CN201317704Y (en) 2009-09-30

Family

ID=41196473

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201858024U Expired - Fee Related CN201317704Y (en) 2008-09-11 2008-09-11 Biological filter tower

Country Status (1)

Country Link
CN (1) CN201317704Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101928079A (en) * 2010-08-27 2010-12-29 绍兴永利环保科技有限公司 High-efficiency diatomaceous earth clarification tank
CN102267757A (en) * 2011-06-29 2011-12-07 无锡强工机械工业有限公司 Biomass three-phase separator device
CN103896430A (en) * 2014-03-14 2014-07-02 河海大学 Integrated water purifying water for removing fluoride in underground water
CN105523635A (en) * 2016-01-28 2016-04-27 西安建筑科技大学 Integrated biological contact device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101928079A (en) * 2010-08-27 2010-12-29 绍兴永利环保科技有限公司 High-efficiency diatomaceous earth clarification tank
CN101928079B (en) * 2010-08-27 2012-12-26 绍兴永利环保科技有限公司 High-efficiency diatomaceous earth clarification tank
CN102267757A (en) * 2011-06-29 2011-12-07 无锡强工机械工业有限公司 Biomass three-phase separator device
CN102267757B (en) * 2011-06-29 2013-02-13 无锡强工机械工业有限公司 Biomass three-phase separator device
CN103896430A (en) * 2014-03-14 2014-07-02 河海大学 Integrated water purifying water for removing fluoride in underground water
CN103896430B (en) * 2014-03-14 2015-12-30 河海大学 A kind of integral water purifying device removed for fluorochemical in underground water
CN105523635A (en) * 2016-01-28 2016-04-27 西安建筑科技大学 Integrated biological contact device
CN105523635B (en) * 2016-01-28 2017-12-26 西安建筑科技大学 A kind of integrated biological device

Similar Documents

Publication Publication Date Title
CN101560039B (en) Landfill leachate wastewater treatment system and process thereof
CN102417273B (en) Dynamic membrane purifying reactor and method for removing ammonia nitrogen and organic matters from reclaimed water
CN103880193B (en) Build the method for vertical current constructed wetland processing breeding wastewater based on waterworks sludge
CN104761107A (en) Irrigated area domestic wastewater activated iron-anaerobe coupling strengthening and nitrogen and phosphorus removal device
CN100348520C (en) Technique for treating garbage percolate based on diatomite and UASB
CN201317704Y (en) Biological filter tower
CN105271520A (en) Annular biological aerated filter and application thereof
CN105461166B (en) A kind of enhanced biological processing of high-concentration hardly-degradable organic industrial sewage and reclamation set and method
CN112939381A (en) Multi-efficiency combined biological filter
CN201116291Y (en) Advanced wastewater treatment device
CN102491500A (en) Layered oxygen-supply aeration bacteria filter
CN104098179A (en) Assembled type sewage treatment device for aerobic and anaerobic immobilized microorganisms
CN201648186U (en) Composite membrane bioreactor
CN203960015U (en) A kind of efficient ozone oxidation bonding membrane bioreactor system
CN201106004Y (en) Combined aerating biologic filtering pool
CN101786716B (en) High-concentration difficult-degradation organic sewage treating system
CN201485321U (en) High-efficiency composite biological aeration filter
CN201406361Y (en) Waste leachate waste water processing device
CN103193359B (en) Deposition and biological filter combined water purification system
CN213171946U (en) Circular biological aerated filter with precipitation function
CN104118941A (en) Efficient nitrogen and phosphorus removal artificial wetland device
CN2654598Y (en) Composite anaerobic biological waste water treatment reactor
CN203382619U (en) Sewage-land biological filtration and precipitation system for removing suspended solids and organic matters from sewage
CN2848842Y (en) Aeration biological filtering chamber
CN202519084U (en) Porous steel slag filter material sink filter reactor

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Solid waste washing-biological filtering tower combined working method for deodorization

Effective date of registration: 20120305

Granted publication date: 20090930

Pledgee: Pudong Development Bank of Shanghai, Limited by Share Ltd, Wuxi branch

Pledgor: Jiangsu Baina Environment Engineering Co., Ltd.

Registration number: 2012990000078

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090930

Termination date: 20150911

EXPY Termination of patent right or utility model