CN206156839U - Bed of packings efflux aeration tank - Google Patents
Bed of packings efflux aeration tank Download PDFInfo
- Publication number
- CN206156839U CN206156839U CN201621192528.4U CN201621192528U CN206156839U CN 206156839 U CN206156839 U CN 206156839U CN 201621192528 U CN201621192528 U CN 201621192528U CN 206156839 U CN206156839 U CN 206156839U
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- CN
- China
- Prior art keywords
- aeration tank
- distributor
- packed bed
- ejector
- bend pipe
- 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.)
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- 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
Abstract
The utility model discloses a bed of packings efflux aeration tank comprises aeration tank cell body, bed of packings, circulating water pump, ejector, distributor and connecting tube, aeration tank cell body upper portion is equipped with water inlet and delivery port, aeration tank cell body middle part is equipped with the partition wall, the partition wall below was equipped with the water hole, circulating water pump's intake is located the bed of packings below, circulating water pump and distributor are connected respectively to the ejector both ends, the distributor is established in aeration tank cell body bottom, and this distributor comprises the person in charge and a plurality of return bend, and return bend one end links to each other with the person in charge, and the terminal export of return bend appears for the pointed cone. The utility model discloses utilize hydraulic circulation, inhale the outside air through the ejector, lose one's temper, water flash mixed, again through distributor evenly distributed to bottom of the pool, stirring bottom of the pool mud to reaching the effect of carrying out oxygen suppliment and the stirring of even circulating mixed to the aeration tank, creating suitable growing environment for good oxygen microorganism, the organic matter in messenger's sewage obtains decomposing to be got rid of.
Description
Technical field
The utility model is related to environmentally friendly water treatment field technical field, and more specifically, more particularly to one kind can be used to give birth to
The packed bed jet aeration tanks that sewage living and organic industrial sewage are processed.
Background technology
Aerobic biological process method is the device that a kind of utilization aerobic microbiological carries out sewage disposal, and it is by activated sludge
The metabolism of aerobic microbiological absorbs degraded organic pollutants, so that sewage is purified.
In sewage disposal system, the premise that Aerobic biological process can play one's part to the full is that have necessarily in Aerobic Pond
Dwell time of sewage, the oxygen amount and sewage that meet required for aerobic microbiological be fully contacted with activated sludge and mix.Pass through
The purpose mixed to sewage oxygen supply and muddy water can be reached to a large amount of aerations of Aerobic Pond.The selection direct relation of aerating system
Oxygenation capacity, treatment effect and the management operation of whole Aerobic Pond.Existing aerating system adopts blast aeration mostly, that is, lead to
Cross air blast or air compressor to provide source of the gas, while improving oxygen-transfer efficiency using the aerator installed under water.Current
Engineer applied in, boring aeration system directly the perforate aeration on air duct, simple structure are widely used.Air demand one
Regularly, the appropriate aperture for reducing perforated pipe can increase its efficiency of oxygen supply, but there is eyelet and local line clogging and aeration is uniform
The poor problem of property.Pore on the gas distribution diaphragm of microporous diaphragm aerator can be changeable with the increase and decrease of tolerance, so as to
Make aeration become more uniform, while also reducing the possibility of blocking, have a disadvantage in that gas distribution diaphragm is easy in use
There is situation that is aging damaged and coming off, Maintenance and Repair inconvenience.
Utility model content
The purpose of this utility model is to provide a kind of packed bed jet aeration tanks, and by ejector air is sucked, and is made
Air and sewage, sludge quickly mix, and reach the purpose of oxygen supply and mixing.In combination with the use of packed bed, using on bubble
Rise and biofilm contact mass transfer, improve the utilization rate of oxygen, while strengthening Aerobic Process for Treatment effect.
In order to achieve the above object, the technical solution adopted in the utility model is as follows:
A kind of packed bed jet aeration tanks, by aeration tank pond body, packed bed, water circulating pump, ejector, distributor and connection
Pipeline is constituted, and the aeration tank pond body top is provided with water inlet and delivery port, and the aeration tank pond body middle part is provided with partition wall, described
Partition wall lower section is provided with water hole;The intake of the water circulating pump is located at packed bed lower section;The ejector two ends connect respectively
Water circulating pump and distributor;The distributor is located at aeration tank pond body bottom, and the distributor is constituted by being responsible for some bend pipes, curved
Pipe one end is connected with supervisor, and the end outlet of bend pipe is sharp cone distal.
Further, the ejector is made up of nozzle, air entry, mixing chamber, trunnion and anemostat, the nozzle, mixed
Air chamber, trunnion and anemostat set gradually, and the air entry is located at the side of nozzle, and the anemostat is connected to distributor.
Further, the water inlet and delivery port are located at aeration tank pond body two ends, and positioned at packed bed top.
Further, the water hole is located at partition wall bottom and away from aeration tank water inlet and the side of delivery port.
Further, the bend pipe is symmetrically interspersed in supervisor both sides.
Further, the supervisor and bend pipe are anticorrosion pipeline.
Compared with prior art, the utility model has the advantage of:
1st, the utility model carries out oxygenation to sewage using ejector, and air is quickly mixed in ejector with sludge, sewage
Close, afterwards the mixture Jing distributors of gas, liquid, solid three-phase enter bottom of pond, while stirring pool bottom sludge, whole process is formed efficiently
Material transmission, oxygen utilization rate is high, and stirring and mixing effect is good, without sludgd deposition.
2nd, the utility model arranges packed bed in aeration tank, for the carrier that microorganism provides growth and breeding, buffers jet
Percussion of the produced shearing force to sludge flco, it is to avoid sludge is broken, sludge settling property is good;Simultaneously jet is to filling out
Material wash away can promote on filler it is aging it is biomembranous come off, update, improve mass-transfer efficiency, strengthen Aerobic Process for Treatment effect.
3rd, sewage is completed from import to the processing procedure for exporting in baffling mode in the utility model, and flow process is longer, will not
There is laterally short stream.Meanwhile, under the souring of jet, sewage, sludge are thoroughly mixed in aeration tank, aeration tank impact resistance
Load-bearing capacity is stronger.
4th, the utility model is improve at sewage aerobic biology by jet-flow aeration in combination with Biological Contact Oxidation Process
Reason efficiency, it is excellent with efficiency of oxygen supply height, high treating effect, convenient, the capital expenditure saving of running management etc. without the need for external gas source
Point.
Description of the drawings
In order to be illustrated more clearly that the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise for not paying creative work
Under, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is the structural representation of the utility model preferred embodiment.
Fig. 2 is the top view of aeration tank pond body.
Fig. 3 is the 1-1 sectional views in Fig. 2.
Fig. 4 is the structure schematic diagram of ejector.
Fig. 5 is the structure of distributor simplified schematic diagram of the aeration tank bottom in Fig. 1.
Description of reference numerals:1st, aeration tank pond body;2nd, packed bed;3rd, water circulating pump;4th, ejector;5th, distributor;6th, enter
The mouth of a river;7th, delivery port;8th, partition wall;9th, water hole, 4-1, air entry;4-2, nozzle;4-3, mixing chamber;4-4, trunnion;4-5, expansion
Dissipate pipe;5-1, supervisor;5-2, bend pipe.
Specific embodiment
Preferred embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings, so that advantage of the present utility model
Can be easier to be readily appreciated by one skilled in the art with feature, it is apparent clear and definite so as to make to protection domain of the present utility model
Define.
Refering to shown in Fig. 1-Fig. 5, the utility model provides a kind of packed bed jet aeration tanks, by aeration tank pond body 1, filler
Bed 2, water circulating pump 3, ejector 4, distributor 5 and connecting pipe composition, the top of aeration tank pond body 1 is provided with the He of water inlet 6
Delivery port 7, the middle part of the aeration tank pond body 1 is provided with partition wall 8, and the lower section of the partition wall 8 is provided with water hole 9;The water circulating pump 3
Intake is located at the lower section of packed bed 2;The two ends of the ejector 4 connect respectively water circulating pump 3 and distributor 5;The distributor 5 sets
The bottom of pond body 1 in aeration tank, the distributor 5 by supervisor 5-1 and some bend pipe 5-2 constitute, bend pipe 5-2 one end be responsible for 5-1 phases
Even, the end outlet of bend pipe 5-2 is sharp cone distal, and the bend pipe 5-2 is symmetrically interspersed in supervisor 5-1 both sides.
The ejector 4 is made up of nozzle 4-2, air entry 4-1, mixing chamber 4-3, trunnion 4-4 and anemostat 4-5, described
Nozzle 4-2, mixing chamber 4-3, trunnion 4-4 and anemostat 4-5 set gradually, and the air entry 4-1 is located at the side of nozzle 4-2,
The anemostat 4-5 is connected to distributor 5.
The water inlet 6 and delivery port 7 are located at the two ends of aeration tank pond body 1, and positioned at the top of packed bed 2.Sewage is from water inlet
Mouth 6 enters aeration tank, and packed bed 2 is first from up to down passed through in vertical direction, flows through afterwards after water hole 9 again from bottom to top
Through packed bed 2, Jing delivery ports 7 flow out, and complete whole handling process.
The water hole 9 is located at the bottom of partition wall 8 and away from aeration tank water inlet 6 and the side of delivery port 7.
Preferably, the supervisor 5-1 and bend pipe 5-2 is anticorrosion pipeline.
During normal operation, the activated sludge at aeration tank bottom 1 and the pressurization of mixed liquor Jing water circulating pumps 3 of sewage are promoted to and penetrate
Stream device 4, Jing nozzles 4-2 sprays at a high speed, into mixing chamber 4-3, and forms local decompression in mixing chamber 4-3 and trunnion 4-4.
Under differential pressure action, air Jing air entry 4-1 are inhaled in ejector 4, and with mixing chamber 4-3 in muddy water mixed solution Rapid contact
Mixing mass transfer, the air-water mixture Jing anemostats 4-5 of formation introduces the supervisor 5-1 of distributor 5, and is sprayed by bend pipe 5-2.Cause
Bend pipe 5-2 ends bore reduces, mixture velocity increase, Jing after bend pipe sprays, because inertia impulsive force forms eddy flow, disturbance in bottom of pond
Pool bottom sludge, mixes to muddy water.So iterative cycles, realize carrying out sewage aeration aerating and stirring.
With fine gas bubbles rapid increase, flow velocity reduces the air that distributor 5 is discharged Jing after packed bed 2, outstanding in sewage
The filled retention of float, suspended sludge utilizes oxygen and absorbs the organic contamination in sewage with the biomembrane for being attached to filler surface
Thing carries out metabolism, is purified sewage.
Although being described in conjunction with the accompanying embodiment of the present utility model, patent owner can want in appended right
Various modifications or modification are made within the scope of asking, as long as less than the protection model described by claim of the present utility model
Enclose, all should be within protection domain of the present utility model.
Claims (6)
1. a kind of packed bed jet aeration tanks, it is characterised in that:By aeration tank pond body, packed bed, water circulating pump, ejector, point
Cloth device and connecting pipe are constituted, and the aeration tank pond body top is provided with water inlet and delivery port, and the aeration tank pond body middle part sets
There is partition wall, the partition wall lower section is provided with water hole;The intake of the water circulating pump is located at packed bed lower section;The ejector two
End connects respectively water circulating pump and distributor;The distributor is located at aeration tank pond body bottom, the distributor by be responsible for it is some
Bend pipe is constituted, and bend pipe one end is connected with supervisor, and the end outlet of bend pipe is sharp cone distal.
2. packed bed jet aeration tanks according to claim 1, it is characterised in that:The ejector by nozzle, air entry,
Mixing chamber, trunnion and anemostat composition, the nozzle, mixing chamber, trunnion and anemostat set gradually, and the air entry is located at spray
The side of mouth, the anemostat is connected to distributor.
3. packed bed jet aeration tanks according to claim 1, it is characterised in that:The water inlet and delivery port are located at exposure
Gas pond pond body two ends, and positioned at packed bed top.
4. packed bed jet aeration tanks according to claim 1, it is characterised in that:The water hole be located at partition wall bottom and
Away from aeration tank water inlet and the side of delivery port.
5. packed bed jet aeration tanks according to claim 1, it is characterised in that:The bend pipe is symmetrically interspersed in master
Pipe both sides.
6. packed bed jet aeration tanks according to claim 1, it is characterised in that:The supervisor and bend pipe are corrosion-resistant
Pipeline.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621192528.4U CN206156839U (en) | 2016-11-06 | 2016-11-06 | Bed of packings efflux aeration tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621192528.4U CN206156839U (en) | 2016-11-06 | 2016-11-06 | Bed of packings efflux aeration tank |
Publications (1)
Publication Number | Publication Date |
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CN206156839U true CN206156839U (en) | 2017-05-10 |
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Family Applications (1)
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CN201621192528.4U Active CN206156839U (en) | 2016-11-06 | 2016-11-06 | Bed of packings efflux aeration tank |
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CN (1) | CN206156839U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110642372A (en) * | 2019-09-29 | 2020-01-03 | 北交源生态环境科技(北京)有限公司 | Intermittent aeration method for MBBR aeration |
-
2016
- 2016-11-06 CN CN201621192528.4U patent/CN206156839U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110642372A (en) * | 2019-09-29 | 2020-01-03 | 北交源生态环境科技(北京)有限公司 | Intermittent aeration method for MBBR aeration |
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