CN201292263Y - Vertical flow type aerobic gas float filter chamber - Google Patents

Vertical flow type aerobic gas float filter chamber Download PDF

Info

Publication number
CN201292263Y
CN201292263Y CNU2008201242578U CN200820124257U CN201292263Y CN 201292263 Y CN201292263 Y CN 201292263Y CN U2008201242578 U CNU2008201242578 U CN U2008201242578U CN 200820124257 U CN200820124257 U CN 200820124257U CN 201292263 Y CN201292263 Y CN 201292263Y
Authority
CN
China
Prior art keywords
water
pipe
filter chamber
aerophil
dissolved gas
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
CNU2008201242578U
Other languages
Chinese (zh)
Inventor
李冬
朱兆亮
曹相生
张�杰
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 University of Technology
Original Assignee
Beijing University of Technology
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 University of Technology filed Critical Beijing University of Technology
Priority to CNU2008201242578U priority Critical patent/CN201292263Y/en
Application granted granted Critical
Publication of CN201292263Y publication Critical patent/CN201292263Y/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

  • Physical Water Treatments (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

The utility model relate to a vertical flow type aerophil air-bearing filter chamber which belongs to a water treatment device. The vertical flow type aerophil air-bearing filter chamber is characterized in that a water inlet pipe and a dissolved gas backflow water pipe are fixed at the bottom of the filter chamber, and a dissolved gas releaser is mounted at the tail end of the dissolved gas backflow water pipe; slag-floating troughs are respectively arranged at the top of the filter chamber, a backwash waste water trough is arranged at the lower part of the dissolved gas separation region, and a piercing gas distribution pipe and a water collector pipe are embedded at the bottom of either material-filtering layer; the piercing gas distribution pipes are respectively connected with an aerated gas pipe and a backwash gas pipe, and the water collector pipes and water outlet pipes are respectively connected with backwash water inlet pipes. The vertical flow type aerophil air-bearing filter chamber combines physical treatment (dissolved gas) and biological treatment (aerophil filter chamber) to form an integrated device, the dissolved gas can further remove substances, such as sludge fragments, rubber particles, algae, and the like with densities approximate to water, and high-dissolved oxygen in the emergence of the dissolved gas supplies biological oxygen to the aerophil filter chamber which take the functions of physical retention, absorption and biodegradation for polluted substances so as to further purify water quality.

Description

Vertical-flow good Airfloat filtering pond
Technical field
The utility model belongs to a kind of water treatment device, relates to source water and handles and the advanced treatment of wastewater field.
Background technology
At present, coagulation+precipitation+filtration common process is generally adopted in the processing of advanced treatment of wastewater and source water, though this technology can effectively be removed suspended substance, pollution substances such as BOD, COD in the water, but indexs such as nutrition such as the nitrogen in the water outlet and algae can not satisfy corresponding water quality standard, and the technology floor space is big, complex management.
The utility model content
The purpose of this utility model is to overcome the shortcoming of common process, and a kind of novel water treatment device is provided.This device combines physical treatment (air supporting) and biological treatment (good air filter pond), forms integrated apparatus.Air supporting can approach density materials such as the mud fragment, colloidal solid, algae of water and further remove, high-solubility oxygen provides biological aerobic for good air filter pond in the water outlet of air supporting simultaneously, good air filter pond to pollution substance play that physics is held back, absorption and biodegradable function, thereby further purify water.
The technical solution of the utility model is as follows:
Vertical-flow good Airfloat filtering pond, it relates to a kind of improvement of floating filter structure, is to be modified into to increase aerating apparatus in vertical-flow on the basis of traditional flat flow floating filter, improves the biological treatment function.
The vertical-flow good Airfloat filtering pond of the utility model, it is characterized in that: water inlet pipe 1, molten gas backflow water pipe 2 are fixed on the bottom, filter tank, end at molten gas backflow water pipe 2 is installed dissolved air release 8, the top, filter tank is provided with scum silica frost groove 6,12 bottoms are provided with backwash waste groove 7 in the flotation separation zone, bury perforation gas distribution pipe 9 and header 10 underground in filter material layer 13 bottoms, its middle punch gas distribution pipe 9 is connected with aeration, backwash tracheae 5, and header 10 is connected with rising pipe 3 and backwash water inlet pipe 4.
This device with have water treatment device now and compared following advantage:
1, the air flotation pool of this device employing is compared with settling tank, is easy to remove the algae substances of suspended sludge fragment, colloidal solid and more difficult coagulating sedimentation in the secondary effluent, and also molten gas oxygenation in water outlet simultaneously is beneficial to the biochemical reaction in the follow-up good air filter pond.
2, this device has adopted the air filter pond to be similar to BAF, but filteration is more emphasized in good air filter pond, under the prerequisite that keeps the original filtration turbidity removal of conventional rapid filter function, increases aerating apparatus simultaneously, strengthen its biological action, strengthen the removal effect of filter tank indexs such as organism and ammonia nitrogens.
3, the employing of this device is vertical-flow compares with flat flow, the surface load height, and floor space is little, and it is little to the disengaging zone influence to scrape slag equipment, the effluent characteristics height.
4, the air flotation pool air filter pond of becoming reconciled is combined as a whole, and is reasonable in design, compact construction, convenient management and using.
Description of drawings
Fig. 1 is the utility model structure iron.
Embodiment
Concrete operations are as follows:
1, air-float filtration process: water inlet pipe 1 is from the water outlet of flocculation reaction, molten gas backflow water pipe 2 from the water outlet of floating filter by dissolved air water (the dissolved-air pressure 392kPa behind the molten gas of gas-liquid mixing pump, reflux ratio 40%), the two together enters air supporting zone of action 11 at the bottom of the pond, and upflow velocity is 11mm/S.Flco after the flocculation contacts with the bubble hit that dissolved air water disengages by reliever 8 and forms bubble-wadding burl zoarium, the two rises to flotation separation zone 12 and separates, decline flow velocity in disengaging zone is 1.4mm/S, scum silica frost overflows into scum silica frost groove 6 and discharges, the air supporting water outlet is by the filter material layer 13 in filter tank, filtering velocity is 4m/h, there is physics to hold back at filter material layer, adsorption, high-solubility oxygen in the water outlet of air supporting simultaneously provides aerobic environment for biological degradation, the insufficient oxygen of nitration reaction is replenished by aeration tube 5, be evenly distributed in the filtering layer through perforation gas distribution pipe 9, aeration rate is controlled at 100L/h, and last water outlet is collected through rising pipe 3 by header 10 and flowed out.
2, the backwash process of Airfloat filtering pond: when filter tank maximum head loss surpasses 1m, the filter end cycle need carry out the normal water outlet that backwash comes assurance device.Backwash process adopts air water associating backwash: backwash tracheae 5 is from aerating system, and backwash water pipe 4 provides from filter back water positive delivery or by elevated tank, and backwash waste is discharged through wastewater trough 7.The back flushing parameter is: gas is towards intensity 11.1L/m separately 2S, flushing 3min; Associating gas is towards intensity 11.1L/m 2S, water is towards intensity 4.5L/m 2S, flushing 6min; Water rinse intensity 8.9L/m 2S, rinsing time 5min.
As seen from Table 1, by vertical-flow good Airfloat filtering pond integrated apparatus, secondary effluent water quality is largely increased, except that the bacterium index need increase disinfect, all other indexs have reached the reuse water water-quality guideline.
The vertical-flow good Airfloat filtering pond of Sewage Plant secondary effluent and process is handled back effluent quality and clearance situation such as following table 1:
Index Turbidity/NTU Colourity/degree UV 254 /cm -1 COD /mg/L NH 3-N /mg/L TP /mg/L Total plate count/10 4Individual ml -1
Secondary effluent 4-15 100-150 0.12-0.27 50-80 15-70 1-5 13-22
Good Airfloat filtering pond water outlet 0.5-2.6 29.7-51. 7 0.03-0.17 22.5-35.2 0.4-15 0-0.8 3.9-6.1
Clearance (%) 78 65 46 47 80 83 63

Claims (1)

1. vertical-flow good Airfloat filtering pond, it is characterized in that: water inlet pipe, molten gas backflow water pipe are fixed on this bottom, filter tank, end at molten gas backflow water pipe is installed dissolved air release, this top, filter tank is provided with the scum silica frost groove, in the bottom, flotation separation zone the backwash waste groove is set, bury perforation gas distribution pipe and header underground in the filter material layer bottom, its middle punch gas distribution pipe is connected with aeration, backwash tracheae, and header is connected with rising pipe and backwash water inlet pipe.
CNU2008201242578U 2008-12-05 2008-12-05 Vertical flow type aerobic gas float filter chamber Expired - Fee Related CN201292263Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201242578U CN201292263Y (en) 2008-12-05 2008-12-05 Vertical flow type aerobic gas float filter chamber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201242578U CN201292263Y (en) 2008-12-05 2008-12-05 Vertical flow type aerobic gas float filter chamber

Publications (1)

Publication Number Publication Date
CN201292263Y true CN201292263Y (en) 2009-08-19

Family

ID=41005729

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201242578U Expired - Fee Related CN201292263Y (en) 2008-12-05 2008-12-05 Vertical flow type aerobic gas float filter chamber

Country Status (1)

Country Link
CN (1) CN201292263Y (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101928082A (en) * 2010-09-16 2010-12-29 江苏新龙鼎环保成套工程有限公司 Vertical-flow air flotation device with secondary filtering
CN101948156A (en) * 2010-09-16 2011-01-19 江苏新龙鼎环保成套工程有限公司 Electrocoagulation vertical air flotation device based on electrolytic reaction principle
CN101948196A (en) * 2010-09-16 2011-01-19 江苏新龙鼎环保成套工程有限公司 Cross flow air floating device with secondary filtration
CN103011509A (en) * 2012-12-15 2013-04-03 华北水利水电学院 Floatation/filtration-integrated polluted water advanced treatment device and method
CN103539318A (en) * 2013-10-31 2014-01-29 福州城建设计研究院有限公司 Air flotation biological filter tank integrated equipment and control method thereof
CN106745601A (en) * 2016-12-19 2017-05-31 芜湖万向新元环保科技有限公司 One kind flocculation aeration tank
CN107759035A (en) * 2017-12-06 2018-03-06 广州鹏凯环境科技股份有限公司 A kind of air supporting combination BAF integration apparatus and sewage treatment process
CN108218098A (en) * 2016-12-13 2018-06-29 黑龙江吉纳森生物工程股份有限公司 A kind of biological reinforced processing unit of oily wastewater

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101928082A (en) * 2010-09-16 2010-12-29 江苏新龙鼎环保成套工程有限公司 Vertical-flow air flotation device with secondary filtering
CN101948156A (en) * 2010-09-16 2011-01-19 江苏新龙鼎环保成套工程有限公司 Electrocoagulation vertical air flotation device based on electrolytic reaction principle
CN101948196A (en) * 2010-09-16 2011-01-19 江苏新龙鼎环保成套工程有限公司 Cross flow air floating device with secondary filtration
CN101948196B (en) * 2010-09-16 2013-04-10 江苏新龙鼎环保成套工程有限公司 Cross flow air floating device with secondary filtration
CN103011509A (en) * 2012-12-15 2013-04-03 华北水利水电学院 Floatation/filtration-integrated polluted water advanced treatment device and method
CN103539318A (en) * 2013-10-31 2014-01-29 福州城建设计研究院有限公司 Air flotation biological filter tank integrated equipment and control method thereof
CN108218098A (en) * 2016-12-13 2018-06-29 黑龙江吉纳森生物工程股份有限公司 A kind of biological reinforced processing unit of oily wastewater
CN106745601A (en) * 2016-12-19 2017-05-31 芜湖万向新元环保科技有限公司 One kind flocculation aeration tank
CN107759035A (en) * 2017-12-06 2018-03-06 广州鹏凯环境科技股份有限公司 A kind of air supporting combination BAF integration apparatus and sewage treatment process

Similar Documents

Publication Publication Date Title
CN201292263Y (en) Vertical flow type aerobic gas float filter chamber
CN106565017B (en) A kind of bicirculating denitrogenation dephosphorizing waste water treatment system and its method
CN106745749B (en) Aerobic-anoxic integrated AO membrane bioreactor
CN103214141A (en) Sewage advanced treatment and recycling method capable of substantially raising economy
CN109970289A (en) A kind of urban wastewater treatment mentions mark advanced treatment process and device
CN203613071U (en) Sewage treatment device
CN215480419U (en) Combined sewage treatment system combining oxidation ditch and deep bed denitrification filter
CN102107968A (en) Water purification system and water purification method of flotation filter tank
CN202924871U (en) Integrated air flotation-membrane bioreactor
CN101428943A (en) Full-flow process for upgrading and reconstructing urban sewage factory
CN105110556A (en) Integrated denitrification decarbonization biological aerated filter and processing system thereof
CN209906566U (en) IV-type water discharge standard domestic sewage treatment device
CN104773917B (en) A kind of middle-size and small-size integrated sewage treatment device
CN206396000U (en) Aquaculture wastewater processing system
CN210480920U (en) Air floatation system with sludge backflow function
CN212127901U (en) Sequencing batch type composite nitrogen and phosphorus removal sewage treatment device
CN209940749U (en) Optimized combined system for urban domestic sewage treatment
CN208776535U (en) A kind of domestic sewage in rural areas integrated equipment for wastewater treatment
CN209065678U (en) A kind of leachate in garbage transfer station processing Integration Equipment
CN208577593U (en) A kind of combination MBR sewage treatment unit
CN105884146A (en) Rural distributed wastewater treatment system
CN105541053A (en) Soy protein waste water treatment device
CN202576091U (en) Integral baffling biological filtering pond sewage treatment device
CN105439382A (en) Integral treatment apparatus of high-concentration organic matter wastewater
CN211847619U (en) Integrated sewage treatment system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090819

Termination date: 20121205