CN207451665U - A kind of high tower air floatation machine - Google Patents

A kind of high tower air floatation machine Download PDF

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Publication number
CN207451665U
CN207451665U CN201721210829.XU CN201721210829U CN207451665U CN 207451665 U CN207451665 U CN 207451665U CN 201721210829 U CN201721210829 U CN 201721210829U CN 207451665 U CN207451665 U CN 207451665U
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bubble release
air
bubble
pipe
inner cylinder
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Expired - Fee Related
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CN201721210829.XU
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Chinese (zh)
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不公告发明人
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Abstract

A kind of high tower air floatation machine includes air supporting reaction tank, clear water reserviors, scum silica frost pond, bubble release pipe, slag-scraper, air dissolving system, first bubble release, the second bubble release, water inlet pipe, water inlet and dosing mouth.Inner cylinder is equipped in the air supporting reaction tank, inner cylinder includes the small bore area connected up and down and big cross-sectional area.The water outlet of air dissolving system is connected by three-way connection with first bubble release, the second bubble release respectively, and first bubble release is mounted in bubble release pipe, and the second bubble release installs the bottom of inner cylinder.Sewage occurs reverse-impact and rotation mixing in bubble release Guan Zhongyu microbubbles and sticks in the same direction in inner cylinder, improve the interaction of microbubble particle, enhance the Adhering capacity of microbubble, enhance the stability of bubble flco, microbubble particles collision efficiency is significantly increased, the adaptability of sewage quality variation is significantly increased.And air floatation machine has the advantages that floor space is small, compact-sized.

Description

A kind of high tower air floatation machine
Technical field
The utility model is related to field of sewage treatment equipment, more particularly relate to a kind of high tower air floatation machine.
Background technology
Air-dissolving air-float technology is a kind of solid-liquid separation technique, it has treatment effeciency high, starts that the time is short and floor space The characteristics of small, is widely used in water treatment field.Complete air-dissolving air-float technology includes flocculation process, molten gas outgassing mistake Journey and bubble-flco aggregation are formed and three big basic process of separation process.
It is flowed to according to dissolved air water and sewage and the way of contact, dissolved air flotation process is divided into concurrent technique and reverse flow work Skill.Concurrent air floatation machine generally comprises flocculation tank, contact chamber and separate tank.Sewage is introduced into flocculation tank and flocculation Agent is sufficiently mixed generation flocculation reaction, Nian Jie with minute bubbles completion in dissolved air water subsequently into contact chamber, forms edge after bubble flco The inclined-plane set between contact chamber and reaction tank enters separate tank and floats up to liquid level, forms scum silica frost and excludes.Bubble exists with particle Collision and adhesion process, microbubble and the sewage co-flow flowed up, contact of the bubble with suspended matter are completed in contact chamber Time is shorter, and the adhesion effect of bubble is poor, particularly when the relatively more and looser flco feelings of Oil in Sewage Water or suspended particulate Condition.
Counter-current air floating device generally sets up level-one contact chamber, wherein upward microbubble and the raw water to flow downward carry out The flowing of opposite direction, the suspended matter of decline are inversely contacted with the bubble risen, bubble are made to be adhered to suspended matter, in the process micro- gas Bubble can complete good collision process with particulate matter, but due to the downward flow force effect of raw water, microbubble cannot with particle Adherency is formed well occurs desorption phenomenon under the action of raw water out-phase flow force after stable bubble flco or adherency, The bubble flco of formation cannot complete floating separation process well.
Utility model content
Include air supporting reaction tank, clear water reserviors to solve the above problems, the utility model provides a kind of high tower air floatation machine, float Slag bath, bubble release pipe, slag-scraper, air dissolving system, first bubble release, the second bubble release, water inlet pipe, water inlet And dosing mouth;The air supporting reaction tank and clear water reserviors are separated by partition plate;The partition plate is equipped with clear water hole;The clear water reserviors are equipped with Water outlet;The scum silica frost pond is arranged on above air supporting reaction tank;The slag-scraper is located at the top of air supporting reaction tank, by air supporting The scum silica frost generated in reaction tank is scraped in scum silica frost pond;The scum silica frost pond is equipped with slag notch;Inner cylinder is equipped in the air supporting reaction tank; The inner cylinder includes the small bore area connected up and down and big cross-sectional area;The top in the small bore area and the bottom of big cross-sectional area are Open state.
The upper end that the water inlet discharges pipe with feeding opening with static mixer, bubble successively by three-way connection is connected.
The air dissolving system water inlet end is connected with clear water reserviors, and water outlet is discharged by three-way connection with first bubble respectively Device, the second bubble release are connected.
The first bubble release is mounted in bubble release pipe;The bottom of the second bubble release installation inner cylinder Portion.
The bottom of water inlet pipe one end connection bubble release pipe, one end is mounted on the bottom of inner cylinder.
Further, the bubble release pipe includes air outlet pipe, VERTICAL TUBE, cyclone pipe, the air outlet pipe, VERTICAL TUBE, rotation Flow tube is sequentially connected logical.
Further, the first bubble release be mounted on bubble release pipe in VERTICAL TUBE, the intersection of cyclone pipe.
Further, the air dissolving system includes reflux pump, dissolving, air compressor machine;The water inlet and clear water reserviors of reflux pump It is connected, the water outlet of reflux pump is connected with the water inlet of dissolving, and the water outlet of dissolving is by three-way connection respectively with the One bubble release, the second bubble release are connected;The air inlet of dissolving is connected with air compressor machine.
Further, it is equipped with first between the three-way connection of water outlet connection of the dissolving and first bubble release The second shut-off valve is equipped between shut-off valve and the second bubble release.
Further, the big cross-sectional area bottom is sectional area gradually increased setting upward;The big cross-sectional area with The linkage section in small bore area is the setting that sectional area is gradually reduced upward.
Further, the water inlet pipe is mounted on one end of inner cylinder bottom equipped with nozzle.
Further, the slag-scraper includes chain, two sprocket wheels and multiple scum boards, and two chains are connected by chain It takes turns, multiple scum boards is fixedly installed on chain, sprocket wheel drives the scum board on chain, the scum silica frost in air supporting reaction tank is scraped into floating Slag bath.
The utility model has the following advantages that:
1st, sewage occurs reverse-impact and rotation mixing in bubble release Guan Zhongyu microbubbles and is sticked in the same direction in inner cylinder It is attached, the interaction of microbubble-particle is improved, enhances the Adhering capacity of microbubble, the stability of bubble flco is enhanced, makes Microbubble particles collision efficiency significantly increases, and the adaptability of sewage quality variation is significantly increased.
2nd, merging flocculation tank, contact chamber and separate tank becomes air supporting reaction tank, reduces the occupation of land face of air floatation machine Product, makes air floatation machine more compact.
Description of the drawings
Fig. 1 is that the structure for the air floatation machine that the utility model embodiment 1 provides regards schematic diagram.
Marginal data:
1st, air supporting reaction tank;2nd, clear water reserviors;3rd, scum silica frost pond;4th, partition plate;41st, clear water hole;5th, inner cylinder;51st, small bore area; 52nd, big cross-sectional area;6th, bubble release pipe;61st, air outlet pipe;62nd, VERTICAL TUBE;63rd, cyclone pipe;7th, slag-scraper;8th, reflux pump; 9th, dissolving;10th, air compressor machine;11st, water inlet pipe;12nd, nozzle;13rd, first bubble release;14th, the first shut-off valve;15th, first Bubble release;16th, the first shut-off valve;17th, static mixer.
Specific embodiment
In order to which those skilled in the art is allowed to more fully understand and realize the technical solution of the utility model, below in conjunction with explanation Book the drawings and specific embodiments are described in further details.
Embodiment 1
As shown in Figure 1, the utility model, which provides a kind of high tower air floatation machine, includes air supporting reaction tank 1, clear water reserviors 2, scum silica frost Pond 3, bubble release pipe 6, slag-scraper 7, air dissolving system, first bubble release 13, the second bubble release 15, water inlet pipe 11st, water inlet and dosing mouth;The air supporting reaction tank 1 and clear water reserviors 2 are separated by partition plate 4;The partition plate 4 is equipped with clear water hole; The clear water reserviors 2 are equipped with water outlet;The scum silica frost pond 3 is arranged on 1 top of air supporting reaction tank;The slag-scraper 7 is located at air supporting The top of reaction tank 1, slag-scraper 7 include chain, two sprocket wheels and multiple scum boards, and two sprocket wheels, chain are connected by chain Multiple scum boards are fixedly installed on item, sprocket wheel drives the scum board on chain, the scum silica frost in air supporting reaction tank 1 is scraped into scum silica frost pond 3.The scum silica frost pond 3 is equipped with slag notch;Inner cylinder 5 is equipped in the air supporting reaction tank 1;The inner cylinder 5 includes connecting up and down small Cross-sectional area 51 and big cross-sectional area 52;The top in the small bore area 51 and the bottom of big cross-sectional area 52 are open state, big section 52 bottom of area is sectional area gradually increased setting upward, the linkage section in big cross-sectional area 52 and small bore area 51 for sectional area to The setting that top is gradually reduced.
The water inlet discharges the upper end phase of pipe 6 with feeding opening with static mixer 17, bubble successively by three-way connection Even.
The air dissolving system includes reflux pump 8, dissolving 9, air compressor machine 10;The water inlet of reflux pump 8 and 2 phase of clear water reserviors Even, the water outlet of reflux pump 8 is connected with the water inlet of dissolving 9;The water outlet of dissolving 9 by three-way connection one end successively The first shut-off valve 14, first bubble release 13 are connected, the other end is sequentially connected the second shut-off valve 16, the second bubble release 15;The air inlet of dissolving 9 is connected with air compressor machine 10.
Bubble release pipe 6 includes air outlet pipe 61, VERTICAL TUBE 62, cyclone pipe 63, the air outlet pipe 61, VERTICAL TUBE 62, Cyclone pipe 63 is sequentially connected logical.
The first bubble release 13 be mounted on bubble release pipe 6 in VERTICAL TUBE 62, the intersection of cyclone pipe 63;Institute State the bottom of the second bubble release 15 installation inner cylinder 5.
The bottom of 11 one end of water inlet pipe connection bubble release pipe 6, one end connection nozzle 12, the nozzle 11 are mounted on The bottom of inner cylinder 5.
In the embodiment, the specific implementation process of sewage disposal is as follows:
For sewage after air supporting water inlet flows into air floatation machine, the flocculant flowed into dosing mouth passes through static mixer 17 together Mixing, then flow into VERTICAL TUBE 62 from the top of bubble release pipe 6;A part of dissolved air water in dissolving 9 is released by first bubble It puts device 13 and discharges microbubble, the dissolved air water with microbubble flows into the bottom of VERTICAL TUBE 62, and sewage is with microbubble in VERTICAL TUBE 62 With respect to reverse flow, complete the abundant collisional mixing of microbubble and the wadding grain in sewage, microbubble participate in coacervation process and and The copolymerization of wadding grain is simultaneously big, so as to generate copolymerisation, forms bubble wadding copolymer;Microbubble and sewage co-flow again, by eddy flow Pipe 63 further rotates mixing, and completion is effectively sticked, then in being diffused into air supporting reaction tank 1 by water inlet pipe 11, nozzle 12 5 bottoms of cylinder.Another part dissolved air water in dissolving 9 is by the second shut-off valve 16, the second bubble release 15 in 5 bottom of inner cylinder Microbubble is discharged, the collision of the floc particle in the sewage mixed liquor that microbubble is flowed out with nozzle 12 is sticked, and is total in inner cylinder 5 It is same to flow up.The big cross-sectional area 52 of inner cylinder 5 including bottom and the small bore area 51 at top, dissolved air water at big cross-sectional area 52, Since sectional area is big, the current rate of climb is uniformly slow so that the mesh of flco network structure is more uniform, in small bore area 51 When, since sectional area is small, unit area microbubble density becomes larger, and the mesh of flco network structure becomes smaller, and air flotation effect is more preferably.The The copolymerisation that the microbubble of one bubble release 13 release is generated with sewage in VERTICAL TUBE 62 with respect to reverse flow, makes generation Flco bubble be clipped in wadding grain among, microbubble has played cohesion so that microbubble is embedded in inside flco securely, from And the collision of microbubble and floc particle in the release of the second bubble release 15 is caused to stick the bubble flco to be formed in floating It is not easy to be desorbed in the process, scum silica frost is stable and is not easy.Bubble flco floats up to liquid level in inner cylinder 5, forms scum silica frost.By scraping slag The sprocket wheel of device 7 rotates, and the scum board on chain is driven to move horizontally, scum silica frost is scraped in scum silica frost pond 3.Sewage is discharged in bubble Reverse-impact occurs with microbubble in pipe 6 and rotation is mixed and sticked in the same direction in inner cylinder 5, improves microbubble-particle Interaction enhances the Adhering capacity of microbubble, enhances the stability of bubble flco, makes microbubble particles collision efficiency notable Enhancing significantly increases the adaptability of sewage quality variation.Since sewage and microbubble during bubble discharges pipe 6 when reacting, Part microbubble can form gas, this portion gas is discharged by exhaust pipe 61.By adjusting the first shut-off valve 14 and second section The only openings of sizes of valve 16 can control the stream for the dissolved air water for flowing into first bubble release 13 and the second bubble release 15 Amount, so as to adapt to the water quality of different operating modes.
The clear water that completion is handled in inner cylinder 5 flows into the region between 1 pool wall of air supporting reaction tank and 5 barrel of inner cylinder, and passes through The clear water hole 41 that is set on partition plate 4 flows into clear water reserviors 2, and 2 middle part of clear water reserviors is distinguished water and returns pump to dissolving 9 by reflux pump 8, simultaneously Air compressor machine 10 pressurizes to dissolving 9 and input air, and air dissolves in clear water in dissolving 9 and forms dissolved air water, and dissolved air water flows into First bubble release 13, the second bubble release 15 release microbubble Xun Huan and are reacted;Another part is clear in clear water reserviors 2 Water is flowed out by water outlet, completion processing.
A kind of high tower air floatation machine provided by the utility model is described in detail above.Tool used herein Body example is set forth the technical solution of the utility model and embodiment, and the explanation of above example is only intended to help Understand the technical solution of the utility model and its core concept.It should be pointed out that come for those skilled in the art Say, on the premise of the technical solution of the utility model is not departed from, can also to the utility model, some improvement and modification can also be carried out, These improvement and modification are also fallen into the protection domain of the utility model claims.

Claims (8)

1. a kind of high tower air floatation machine, which is characterized in that discharge pipe including air supporting reaction tank, clear water reserviors, scum silica frost pond, bubble, scrape Slag device, air dissolving system, first bubble release, the second bubble release, water inlet pipe, water inlet and dosing mouth;The air supporting Reaction tank and clear water reserviors are separated by partition plate;The partition plate is equipped with clear water hole;The clear water reserviors are equipped with water outlet;The scum silica frost pond It is arranged on above air supporting reaction tank;The slag-scraper is located at the top of air supporting reaction tank, floating by what is generated in air supporting reaction tank Slag is scraped in scum silica frost pond;The scum silica frost pond is equipped with slag notch;Inner cylinder is equipped in the air supporting reaction tank;The inner cylinder is included up and down The small bore area and big cross-sectional area of connection;The top in the small bore area and the bottom of big cross-sectional area are open state;
The upper end that the water inlet discharges pipe with feeding opening with static mixer, bubble successively by three-way connection is connected;
The air dissolving system water inlet end is connected with clear water reserviors, water outlet by three-way connection respectively with first bubble release, Two bubble releases are connected;
The first bubble release is mounted in bubble release pipe;
The bottom of the second bubble release installation inner cylinder;
The bottom of water inlet pipe one end connection bubble release pipe, one end is mounted on the bottom of inner cylinder.
2. a kind of high tower air floatation machine according to claim 1, which is characterized in that the bubble release pipe includes outlet Pipe, VERTICAL TUBE, cyclone pipe, the air outlet pipe, VERTICAL TUBE, cyclone pipe are sequentially connected logical.
3. a kind of high tower air floatation machine according to claim 2, which is characterized in that the first bubble release is mounted on VERTICAL TUBE, the intersection of cyclone pipe in bubble release pipe.
4. a kind of high tower air floatation machine according to claim 1, which is characterized in that the air dissolving system include reflux pump, Dissolving, air compressor machine;The water inlet of reflux pump is connected with clear water reserviors, and the water outlet of reflux pump is connected with the water inlet of dissolving Logical, the water outlet of dissolving is connected by three-way connection with first bubble release, the second bubble release respectively;Dissolving Air inlet is connected with air compressor machine.
5. a kind of high tower air floatation machine according to claim 4, which is characterized in that the water outlet connection of the dissolving It is equipped between three-way connection and first bubble release between the first shut-off valve and the second bubble release and is equipped with the second cut-off Valve.
6. a kind of high tower air floatation machine according to claim 1, which is characterized in that the big cross-sectional area bottom is sectional area Gradually increased setting upward;The linkage section of the big cross-sectional area and small bore area sets for what sectional area was gradually reduced upward It puts.
7. a kind of high tower air floatation machine according to claim 1, which is characterized in that the water inlet pipe is mounted on inner cylinder bottom One end be equipped with nozzle.
8. a kind of high tower air floatation machine according to claim 1, which is characterized in that the slag-scraper includes chain, two A sprocket wheel and multiple scum boards connect two sprocket wheels by chain, multiple scum boards are fixedly installed on chain, and sprocket wheel drives chain On scum board, the scum silica frost in air supporting reaction tank is scraped into scum silica frost pond.
CN201721210829.XU 2017-09-15 2017-09-15 A kind of high tower air floatation machine Expired - Fee Related CN207451665U (en)

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Application Number Priority Date Filing Date Title
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107459091A (en) * 2017-09-15 2017-12-12 湖南美奕机电科技有限公司 A kind of high tower air floatation machine
CN113354022A (en) * 2021-05-26 2021-09-07 江西台标环保有限公司 Sewage air-flotation treatment device based on liquid level buoyancy change intermittent scraping and deslagging

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107459091A (en) * 2017-09-15 2017-12-12 湖南美奕机电科技有限公司 A kind of high tower air floatation machine
CN113354022A (en) * 2021-05-26 2021-09-07 江西台标环保有限公司 Sewage air-flotation treatment device based on liquid level buoyancy change intermittent scraping and deslagging
CN113354022B (en) * 2021-05-26 2022-09-23 汉川市银泉环保科技有限公司 Sewage air floatation treatment device based on liquid level buoyancy change intermittent scraping and deslagging

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

Granted publication date: 20180605

Termination date: 20210915

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