CN205873993U - Counter -current biological filter under leading aeration - Google Patents
Counter -current biological filter under leading aeration Download PDFInfo
- Publication number
- CN205873993U CN205873993U CN201620728225.3U CN201620728225U CN205873993U CN 205873993 U CN205873993 U CN 205873993U CN 201620728225 U CN201620728225 U CN 201620728225U CN 205873993 U CN205873993 U CN 205873993U
- Authority
- CN
- China
- Prior art keywords
- water
- aeration
- filtering area
- pipe
- backwash
- 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
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Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a counter -current biological filter under leading aeration. Counter -current biological filter under leading aeration includes mutual independence and adjacent leading aeration district and lower counter -current filtering area, and aeration equipment is only installed in distinguishing to leading aeration, and lower counter -current filtering area is provided with water distribution drainage channel, filter layer, supporting layer, the water distribution distribution layer of catchmenting. Intake through leading aeration district back, enter into down the counter -current filtering area through adjustable inlet valve from upper portion in, rivers are from last to down through the filter layer, from the outlet pipe outflow. The utility model discloses li baoqiqu separates with the filtering area for aeration equipment is installation and maintenance easily, and the filtration mode of counter -current under the filtering area adopts goes out the aquatic in the time of can solving air water upward flow filtering pond operation simultaneously and carries biomembrane and foam, dissolved oxygen and the high problem of suspended solid concentration that comes off secretly, gets rid of pollutants such as organics in water, ammonia nitrogen, total nitrogen and suspended solid better, and it is better that the messenger draws water quality of water.
Description
Technical field
This utility model relates to a kind of BAF removing the pollutant such as Organic substance in water, ammonia nitrogen, total nitrogen, specifically
For a kind of preposition aeration Downward-flow biofilter.
Background technology
The aerating system of existing BAF, in filter material layer, need to clean out the filtrate in pond during maintenance, time-consuming
Arduously, operation inconvenience;In aerating system makes filter tank simultaneously, aqueous vapor flows up so that be entrained with the biomembrane come off in water outlet
And dissolved oxygen in foam, and water outlet and concentration of suspension high, water quality inferiority.
Summary of the invention
For solving problem above, this utility model provides the biofilter that a kind of aeration zone separates with filtering area so that
The construction of biofilter and easy to maintenanceization, effluent quality is high.
This utility model is by the following technical solutions: a kind of preposition aeration Downward-flow biofilter, it is characterised in that: described
Biofilter by preposition aeration zone and lower to stream filtering area form, described preposition aeration zone with lower to flow filtering area be two adjacent
Compartment;In described preposition aeration zone, aerator is installed;Described lower to stream filtering area be internally provided with defecator.
Described preposition aeration zone exterior bottom is provided with water inlet pipe;Described lower to stream filtering area exterior bottom, water outlet is installed
Pipe;Described preposition aeration zone and lower interlayer top between stream filtering area are provided with scalable inlet valve;Described lower to stream
Filtering area upper inside wall is provided with water distribution drainage ditch.
It is provided with water intaking valve on described water inlet pipe, described outlet pipe is provided with scalable outlet valve.
Described lower to stream side, filtering area gas and water back purge system is installed.
Described gas and water back purge system includes backwash trachea, drain pipe, backwash water pipe, blow-down pipe;Described backwash
Trachea is provided with backwash air valve, drain pipe is provided with drain valve, backwash water pipe is provided with backwash water valve, blow-down pipe is provided with
Atmospheric valve.
Described lower to stream filtering area within defecator be followed successively by filter material layer, supporting layer, filter from top to bottom.
For the water and air distributing layer that catchments below described filter.
The beneficial effects of the utility model are: preposition aeration Downward-flow biofilter avoids general biofilter aeration dress
It is placed in filter course, during aerator maintenance, the trouble of filtrate need to be understood, filter tank described in the utility model aerator installs,
Easy to maintenance;Water inlet through preposition aeration zone simultaneously is from top to bottom through the filter course of filtering area, and effluent quality is good, relatively by
Under supreme filter type, the impurity that can preferably stop to bubble through the water column is taken out of by gas and current and is caused asking of condition of water quality difference
Topic;It addition, the lower gas and water back purge system arranged to stream filtering area can remove the trapped substance in filtering layer well so that filtrate
Regeneration, it is ensured that the filter effect in filter tank.
Accompanying drawing explanation
Fig. 1: preposition aeration Downward-flow biofilter organigram
As shown in the figure: preposition aeration zone 1;Lower to stream filtering area 2;Water inlet pipe 1-1;Water intaking valve 1-2;Air hose 1-3;Aeration
Device 1-4;Scalable inlet valve 1-5;Water distribution drainage ditch 2-1;Filter material layer 2-2;Supporting layer 2-3;Filter 2-4;Catchment water distribution
Distribution layer 2-5;Backwash trachea 2-6;Backwash air valve 2-7;Drain pipe 2-8;Drain valve 2-9;Backwash water valve 2-10;Recoil
Wash water pipe 2-11;Scalable outlet valve 2-12;Outlet pipe 2-13;Blow-down pipe 2-14;Atmospheric valve 2-15.
Detailed description of the invention
In conjunction with Fig. 1, utility model is further described.
Water treatment procedure: close gas and water back purge system, pending water is entered preposition aeration zone 1 by water inlet pipe 1-1, exposes
Device of air 1-4 makes into water aeration, and the water reaching certain dissolved oxygen concentration is flowed into water distribution row by scalable inlet valve 1-5
Water channel 2-1, water distribution drainage ditch 2-1 are by water uniform water distribution to filter course, and current first pass through filter material layer 2-2 from top to bottom and carry out nitrification
With denitrification, remove organic pollutants, ammonia nitrogen and total nitrogen and float, then through supporting layer 2-3, filter 2-4 to catchmenting
Water and air distributing layer 2-5, discharges finally by outlet pipe 2-13.
Backwash cleaning process: first close water intaking valve 1-1, scalable inlet gate 1-5, scalable outlet valve 2-12, anti-
Rinse water valve 2-10, opening water discharge valve 2-9;It is then turned on backwash air valve 2-8, accesses air and filter material layer is carried out air recoil
Wash;Then open backwash water valve 2-10, access backwashing water by backwash water pipe 2-11 and filter material layer is carried out air and water
Backwash, backwashing wastewater is entered water distribution drainage ditch 2-1 and is discharged by drain pipe 2-7;Turn off source of the gas and backwash air valve 2-
8, filter material layer is only carried out water backwashing, discharges through drain pipe 2-7, backwash terminates, it is ensured that biofilter filtering efficiency.
The mode that this utility model utilizes aeration zone to separate with filtering area not only makes the construction of whole biofilter and maintenance
Simplifying, the lower filtered water inlet mode to stream also makes effluent quality more preferable, and the gas and water back purge system simultaneously configured can be effective
Clean biometric filter tank, it is ensured that biofilter Operating ettectiveness.
The foregoing is only preferred embodiment of the present utility model, all done within principle of the present utility model any
Simple modification, equivalents and remodeling, within must belonging to protection domain of the present utility model.
Claims (7)
1. a preposition aeration Downward-flow biofilter, it is characterised in that: described biofilter by preposition aeration zone (1) and lower to
Stream filtering area (2) composition, described preposition aeration zone (1) with lower to flow filtering area (2) be two adjacent compartments;Described preposition exposure
Aerator (1-4) is installed in gas district (1);Described lower to stream filtering area (2) be internally provided with defecator.
Preposition aeration Downward-flow biofilter the most according to claim 1, it is characterised in that: described preposition aeration zone (1)
Exterior bottom is provided with water inlet pipe (1-1);Described lower to stream filtering area (2) exterior bottom outlet pipe (2-13) is installed;Described
Preposition aeration zone (1) and lower interlayer top between stream filtering area (2) are provided with scalable inlet valve (1-5);Under described
It is provided with water distribution drainage ditch (2-1) to stream filtering area (2) upper inside wall.
Preposition aeration Downward-flow biofilter the most according to claim 2, it is characterised in that: on described water inlet pipe (1-1)
It is provided with water intaking valve (1-2), described outlet pipe (2-13) is provided with scalable outlet valve (2-12).
Preposition aeration Downward-flow biofilter the most according to claim 1, it is characterised in that: described lower to stream filtering area
(2) side is provided with gas and water back purge system.
Preposition aeration Downward-flow biofilter the most according to claim 4, it is characterised in that: described gas and water backwash fills
Put and include backwash trachea (2-6), drain pipe (2-7), backwash water pipe (2-11), blow-down pipe (2-14);Described backwash gas
(2-6) is provided with backwash air valve (2-8) to pipe, drain pipe (2-7) is provided with drain valve (2-9), set on backwash water pipe (2-11)
Backwash water valve (2-10), blow-down pipe (2-14) is had to be provided with atmospheric valve (2-15).
Preposition aeration Downward-flow biofilter the most according to claim 1, it is characterised in that: described lower to stream filtering area
(2) internal defecator is followed successively by filter material layer (2-2), supporting layer (2-3), filter (2-4) from top to bottom.
Preposition aeration Downward-flow biofilter the most according to claim 6, it is characterised in that: described filter (2-4) lower section
For the water and air distributing layer (2-5) that catchments.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620728225.3U CN205873993U (en) | 2016-07-12 | 2016-07-12 | Counter -current biological filter under leading aeration |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620728225.3U CN205873993U (en) | 2016-07-12 | 2016-07-12 | Counter -current biological filter under leading aeration |
Publications (1)
Publication Number | Publication Date |
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CN205873993U true CN205873993U (en) | 2017-01-11 |
Family
ID=57695496
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620728225.3U Expired - Fee Related CN205873993U (en) | 2016-07-12 | 2016-07-12 | Counter -current biological filter under leading aeration |
Country Status (1)
Country | Link |
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CN (1) | CN205873993U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107758831A (en) * | 2017-12-01 | 2018-03-06 | 江苏宜裕环保科技有限公司 | A kind of catalytic oxidizing equipment of high concentrated organic wastewater processing |
CN112010470A (en) * | 2020-10-22 | 2020-12-01 | 广东联盛水环境工程有限公司 | Integrated vacuum negative pressure particle filtering system |
-
2016
- 2016-07-12 CN CN201620728225.3U patent/CN205873993U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107758831A (en) * | 2017-12-01 | 2018-03-06 | 江苏宜裕环保科技有限公司 | A kind of catalytic oxidizing equipment of high concentrated organic wastewater processing |
CN112010470A (en) * | 2020-10-22 | 2020-12-01 | 广东联盛水环境工程有限公司 | Integrated vacuum negative pressure particle filtering system |
CN112010470B (en) * | 2020-10-22 | 2021-04-30 | 广东联盛水环境工程有限公司 | Integrated vacuum negative pressure particle filtering system |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170111 Termination date: 20210712 |
|
CF01 | Termination of patent right due to non-payment of annual fee |