CN203904066U - Box-type biological aerated filter - Google Patents

Box-type biological aerated filter Download PDF

Info

Publication number
CN203904066U
CN203904066U CN201420244624.3U CN201420244624U CN203904066U CN 203904066 U CN203904066 U CN 203904066U CN 201420244624 U CN201420244624 U CN 201420244624U CN 203904066 U CN203904066 U CN 203904066U
Authority
CN
China
Prior art keywords
box
pipeline
support
brackets
box body
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
CN201420244624.3U
Other languages
Chinese (zh)
Inventor
蔡书强
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.)
BEIJING TAICHANG KERUI ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Original Assignee
BEIJING TAICHANG KERUI ENVIRONMENTAL PROTECTION TECHNOLOGY 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 BEIJING TAICHANG KERUI ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd filed Critical BEIJING TAICHANG KERUI ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Priority to CN201420244624.3U priority Critical patent/CN203904066U/en
Application granted granted Critical
Publication of CN203904066U publication Critical patent/CN203904066U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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

  • Activated Sludge Processes (AREA)

Abstract

The utility model relates to a box-type biological aerated filter, which includes a box body, wherein the top of the box body is opened; a first pipeline is arranged at the inner lower end of the box body; spiral mixing aerators are arrayed on the first pipeline; the first pipeline is communicated with an external aeration blower; first brackets are transversely arranged in the space above the spiral mixing aerators; second brackets are transversely arranged at the top of the box body; vertical brackets are arranged among the first brackets and the second brackets; hollow sphere paddings are mounted on the vertical brackets. The box-type biological aerated filter provided by utility model has the benefits that the structure is simple, the immobilization technology is utilized to fix enzymic preparations and variant bacteria on the surfaces of the hollow sphere paddings, loss of the enzymic preparations and variant bacteria is avoided, the contact area of the enzymic preparations and the variant bacteria with sewage in a filter is enlarged, and the cleaning ability reaches 95% above; the spiral mixing aerators greatly improve the oxygen use ratio, the use is simple, and the cost is low.

Description

A kind of box-type BAF
Technical field
The utility model belongs to field of environment engineering technology, relates to a kind of filter tank equipment, is specifically related to a kind of box-type BAF.
Background technology
At present, BAF (biological aerated filter), compared with conventional activated sludge process, has that organic loading is high, floor space is little, is 1/3 of conventional activated sludge process; Less investment, can not produce sludge bulking, oxygen transmission efficiency is high, effluent quality is good advantage, but that it requires water inlet SS is tighter, general requirement SS≤100mg/L, and preferably SS≤60mg/L, therefore need to carry out pre-treatment to water inlet.Meanwhile, its back flushing water yield, head loss are all larger.
The startup of BAF is identical with the Starting mode of general biomembrance process.Three kinds of modes of general employing abroad: 1. intermittently cultivate and also progressively increase flow velocity; 2. under design current velocity or increase gradually flow velocity and carry out cultured continuously; 3. with active sludge inoculation, steady-state operation.In three kinds of Starting mode, the Changing Pattern such as biomembranous growth velocity, distribution and the clearance to pollutent is different, but it is roughly the same to reach the required time of stable state.
Utility model content
In order to overcome defect of the prior art, the purpose of this utility model is to propose a kind of box-type BAF simple in structure.
The utility model is achieved by the following technical solution:
A kind of box-type BAF, comprises casing, described casing open top, and described box house lower end is provided with the first pipeline, arranges to be provided with and revolve mixed aerator on described the first pipeline, and described the first pipeline is connected with outside Aeration fan; In described space of revolving mixed aerator top, be laterally provided with the first support, described casing top cross is provided with the second support, between described the first support and the second support, is provided with vertical supports, and hollow ball filler is installed in described vertical supports.
Further, described the first support and the second support be arranged in parallel.
Further, described two adjacent width between centers of revolving between mixed aerator are 50cm.
Described hollow ball filler adopts acrylic plastering to make, and is spherical, is provided with reinforcing ring at spherical hollow ball filler middle part one along girth, and the above-below direction of reinforcing ring is respectively provided with 12 ball clacks, is radiation arranges along central shaft.
The utility model adopts immobilization technology, described zymin and variation bacterium are attached to the surface of described hollow ball filler, prevent the loss of zymin and variation bacterium, increased with filter tank in the contact area of sewage, described zymin and variation bacterium have been eliminated the stink that sewage produces, drive away pond fly, prevent secondary pollution; A large amount of lands used have been saved simultaneously.
Described variation bacterium and zymin belong to microorganism, after having sewage to enter in casing, in casing, add once make a variation bacterium and zymin, and these variation bacterium and zymin can be attached to the surface of hollow ball filler and breed metabolism, thereby play sewage purification effect.
Described form of revolving the cutting of mixed aerator employing multi-layer helical is carried out oxygenic aeration, in the time revolving mixed aerator described in air-flow enters, air-flow is first by entering lower floor's multilayer zig-zag aeration head after two road helical cut systems, carry out multilayer cutting, make bubble cut into microbubble, the utilization ratio that has so greatly improved oxygen, has aeration even, the feature that oxygen-transfer efficiency is high.
Further, described the first pipeline is UPVC pipe.Described UPVC pipe is existing installation, taking polyvinyl chloride (PVC) RESINS as carrier, in the time weakening the gravitation of molecular resin interchain, have temperature-sensitive accurately, timing melting, the good characteristic of the effective constituent of absorbing additives rapidly, simultaneously, adopt composite type heat stablizer, in being subject to catching in the process of high temperature and melting, suppressing, absorb at resin and the deviating from of hydrogenchloride, carry out two key addition reactions with polyene structure, active and unsettled chlorine atom in displacer molecule, thus catalyzed degradation and the oxygenolysis of resin under molten state effectively controlled.
Further, described bottom half is provided with sewage input tube; Described casing top is provided with output tube.
Compared with prior art, the superior effect of a kind of box-type BAF described in the utility model is: simple in structure, adopt immobilization technology, described zymin and variation bacterium are fixed on to the surface of described hollow ball filler, prevent the loss of zymin and variation bacterium, increased with filter tank in the contact area of sewage, soil removability is more than 95%; The utilization ratio of oxygen is revolved mixed aerator and has greatly been improved in employing, uses simple, with low cost.
Brief description of the drawings
Fig. 1 is a kind of box-type BAF structural representation described in the utility model.
Reference numeral is as follows:
1-casing, 2-the first pipeline, 3-revolve mixed aerator, 4-the first support, 5-the second support, 6-vertical supports, 7-hollow ball filler, 8-Aeration fan.
Embodiment
Below in conjunction with accompanying drawing, the utility model embodiment is described in further detail.
As shown in Figure 1, a kind of box-type BAF described in the utility model, comprises casing 1, described casing 1 open top, described casing 1 interior lower end is provided with the first pipeline 2, arranges to be provided with to revolve mixed aerator 3 on described the first pipeline 2, and described the first pipeline 2 is connected with outside Aeration fan 8; In described space of revolving mixed aerator 3 tops, be laterally provided with the first support 4, described casing 1 top cross is provided with the second support 5, between described the first support 4 and the second support 5, is provided with vertical supports 6, in described vertical supports 6, hollow ball filler 7 is installed.
Described casing 1 bottom is provided with sewage input tube (not shown); Described casing 1 top is provided with output tube (not shown).
Described casing 1 specification is 3 × 3 × 4m, and day output is 300m 3sanitary sewage.Further, install 36 and revolve mixed aerator 3 on the first pipeline 2 of described casing 1 bottom, two adjacent width between centers of revolving between mixed aerator 3 are 50cm, are 25cm near the mixed aerator 3 of revolving of casing 1 sidewall with the distance of casing 1 sidewall.The described oxygenation capacity that revolves mixed aerator 3 is: 0.077-0.147kg/h, and service area is 0.35-0.75 ㎡/individual, coefficient of oxygen utilization is 20.6%.Described Aeration fan 8 is selected according to the amount of disposing of sewage.
In use, the sewage in casing 1 drops into a small amount of microorganism, as variation bacterium and zymin; Adding less, flora propagation is fast, and water pollutant degradation speed is fast, compares with general biological process, and described microniological proudcts are much higher than traditional method to organic degradation speed, save cost.
All variation bacterium and zymin are the product from nature screening strengthening, and microorganism is broad-spectrum micro-organisms, under aerobic and anaerobic state, play a role, and the ability of tolerance inhibition is strong.
The mixed aerator 3, hollow ball filler 7, Aeration fan 8 of revolving described in the utility model is existing installation, and those skilled in the art can select according to the actual requirements.
The utility model is not limited to above-mentioned embodiment, and in the situation that not deviating from flesh and blood of the present utility model, any distortion, improvement, the replacement that it may occur to persons skilled in the art that all fall into scope of the present utility model.

Claims (5)

1. a box-type BAF, comprises casing, it is characterized in that, described casing open top, and described box house lower end is provided with the first pipeline, arranges to be provided with and revolve mixed aerator on described the first pipeline, and described the first pipeline is connected with outside Aeration fan; In described space of revolving mixed aerator top, be laterally provided with the first support, described casing top cross is provided with the second support, between described the first support and the second support, is provided with vertical supports, and hollow ball filler is installed in described vertical supports.
2. a kind of box-type BAF according to claim 1, is characterized in that, described the first support and the second support be arranged in parallel.
3. a kind of box-type BAF according to claim 1, is characterized in that, described two adjacent width between centers of revolving between mixed aerator are 50cm.
4. a kind of box-type BAF according to claim 1, is characterized in that, described the first pipeline is UPVC pipe.
5. a kind of box-type BAF according to claim 1, is characterized in that, described bottom half is provided with sewage input tube; Described casing top is provided with output tube.
CN201420244624.3U 2014-05-14 2014-05-14 Box-type biological aerated filter Expired - Fee Related CN203904066U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420244624.3U CN203904066U (en) 2014-05-14 2014-05-14 Box-type biological aerated filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420244624.3U CN203904066U (en) 2014-05-14 2014-05-14 Box-type biological aerated filter

Publications (1)

Publication Number Publication Date
CN203904066U true CN203904066U (en) 2014-10-29

Family

ID=51778356

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420244624.3U Expired - Fee Related CN203904066U (en) 2014-05-14 2014-05-14 Box-type biological aerated filter

Country Status (1)

Country Link
CN (1) CN203904066U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104478078A (en) * 2014-12-09 2015-04-01 符惠 Immobilized microbial tank for aeration
CN104743671A (en) * 2015-04-20 2015-07-01 江苏博凯环境科技有限公司 Vertical tube denitrification filler device
CN105819617A (en) * 2016-03-28 2016-08-03 煤科集团杭州环保研究院有限公司 Biological thickening treatment method and biological thickening device for high-salt organic chemical waste water
CN111943352A (en) * 2020-07-23 2020-11-17 浙江建投环保工程有限公司 Biological filter for wastewater treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104478078A (en) * 2014-12-09 2015-04-01 符惠 Immobilized microbial tank for aeration
CN104743671A (en) * 2015-04-20 2015-07-01 江苏博凯环境科技有限公司 Vertical tube denitrification filler device
CN105819617A (en) * 2016-03-28 2016-08-03 煤科集团杭州环保研究院有限公司 Biological thickening treatment method and biological thickening device for high-salt organic chemical waste water
CN111943352A (en) * 2020-07-23 2020-11-17 浙江建投环保工程有限公司 Biological filter for wastewater treatment

Similar Documents

Publication Publication Date Title
CN103693738B (en) Composite semi-nitration-anaerobic ammonia oxidation autotrophic denitrification device and operating method thereof
CN109368938B (en) Full-aerobic denitrification process for pretreatment of livestock and poultry breeding wastewater and integrated equipment
ES2441399T3 (en) System and method for processing organic waste material
CN203904066U (en) Box-type biological aerated filter
CN109650645B (en) Integrated rural domestic sewage treatment equipment and sewage treatment method
CN103253770A (en) Integrated biological reactor for treatment of industrial wastewater and domestic sewage
CN101817615A (en) Anaerobic-sequencing batch biofilm reactor-artificial wetland method for treating piggery wastewater
CN102583900A (en) Method for removing nitrogen and phosphorus by MBBRs (Moving Bed Biofilm Reactors) with sectionalized water inflow
US9421502B2 (en) Apparatus and method for enhanced wastewater treatment
CN101492202A (en) Micro-net dynamic membrane bioreactor for continuously updating dynamic membrane
CN105271520A (en) Annular biological aerated filter and application thereof
CN102363547A (en) Low concentration coal chemical industrial wastewater processing system
CN103641241B (en) Preposed denitrification aeration biofilter and method for treating sewage
CN105601025A (en) Culture wastewater efficient degrading and denitrifying treatment system and treatment method thereof
CN105819568A (en) Aerobic granular sludge sewage processing method having nitrogen removal effect and special-purpose equipment thereof
CN205170477U (en) A inner loop biological filter for treatment of domestic sewage
CN211338974U (en) Device for restoring black and odorous water body through local microorganism activation
CN105254010A (en) Reverse aeration sewage treatment pool and treatment method adopting treatment pool
CN201390676Y (en) Micro-grid dynamic membrane bioreactor for continuously updating dynamic membrane
CN206457319U (en) A kind of and oxygen MBR film domestic sewage treatment devices
CN104496016A (en) Biochemical oxygenation stirring process and device system
CN204958514U (en) Realize nitrifying device of high ammonia -nitrogen concentration waste water bological aerated filter short distance fast
CN201530751U (en) Biofilm-band jet-aeration circulating oxidation pond for sewage purification
CN102249399B (en) Nitrifying reactor suitable for low-temperature environment
CN201517062U (en) Sewage treatment system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141029

Termination date: 20190514