CN203295268U - Multichannel vortex jet aerator - Google Patents
Multichannel vortex jet aerator Download PDFInfo
- Publication number
- CN203295268U CN203295268U CN2013200160162U CN201320016016U CN203295268U CN 203295268 U CN203295268 U CN 203295268U CN 2013200160162 U CN2013200160162 U CN 2013200160162U CN 201320016016 U CN201320016016 U CN 201320016016U CN 203295268 U CN203295268 U CN 203295268U
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- Prior art keywords
- jet
- pipe
- jet pipe
- air chamber
- integrated
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- 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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- 238000005276 aerator Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000001746 injection moulding Methods 0.000 claims description 5
- 238000005520 cutting process Methods 0.000 claims description 3
- 238000005273 aeration Methods 0.000 abstract description 19
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 13
- 239000001301 oxygen Substances 0.000 abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 abstract description 13
- 239000010865 sewage Substances 0.000 abstract description 4
- 238000005260 corrosion Methods 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 230000002421 anti-septic effect Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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Classifications
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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
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
本实用新型公开了一种多通道旋涡射流曝气器，属于污水处理设备领域，其结构由：进气管、气室、筒体、一体化射流管、出气孔、水室、进水管等构成，其中气室的上端部设置有进气管，筒体设置于气室的下部，筒体内部为水室，水室与进水管联通，筒体四周均匀分布六个一体化射流管，且一体化射流管斜插于筒体内的水室中，且与筒体的垂直线呈60°夹角，一体化射流管由射流管进气口、喉管、旋涡器、混合管构成，旋涡器与喉管的一端相连，射流管进气口设置于喉管另一端的上侧，射流管进气口与气室内的出气孔卡接固定且联通。本实用新型具有良好的防腐性能，经久耐用，寿命大大延长，增加了曝气池的利用率及溶氧效率，应用范围扩大。
The utility model discloses a multi-channel vortex jet aerator, which belongs to the field of sewage treatment equipment. The upper end of the air chamber is provided with an air inlet pipe, the cylinder is arranged at the lower part of the air chamber, and the inside of the cylinder is a water chamber, which is connected with the water inlet pipe. Six integrated jet pipes are evenly distributed around the cylinder, and the integrated jet The tube is obliquely inserted into the water chamber in the cylinder, and forms an angle of 60° with the vertical line of the cylinder. The integrated jet tube is composed of a jet tube inlet, a throat, a vortex, and a mixing tube. The vortex and the throat One end of the throat is connected, the air inlet of the jet pipe is arranged on the upper side of the other end of the throat, and the air inlet of the jet pipe is clamped, fixed and communicated with the air outlet in the air chamber. The utility model has good anti-corrosion performance, is durable in use, greatly prolongs the service life, increases the utilization rate of the aeration tank and the dissolved oxygen efficiency, and expands the application range.
Description
Technical field
The utility model relates to a kind of improvement of environmental protection industry (epi) sewage treatment area air supply jet aerator, is specifically related to a kind of multichannel swirl jet aerator.
Technical background
In the sewage aerobic treating processes, need to utilize aerator to the sewage oxygen supply, aerator of a great variety, comprise the multiple aeration forms such as micro-pore aeration, mesopore aeration, surface aerating machine aeration, brush aeration and jet-flow aeration.And jet aerator has long service life, safeguards the advantages such as simple, easy for installation as a kind of aerated product of routine, should be used widely, but in Practical Project, use less.
It mainly contains following several respects reason: 1) in the market jet aerator is most of adopts traditional Venturi tube or la farr pipe principle design, and dissolved oxygen efficiency is lower, causes energy consumption higher; 2) most of jet-flow aeration pipe is comprised of inner nozzle and external diffusion pipe, and error is larger on the angle that adds the connection in man-hour and position, causes Multi-way jet-flow aerator aeration homogeneity not good; 3) most of jet aerator is metal material, and not only antiseptic property is poor, affects work-ing life, and is also very heavy, and cost is higher simultaneously; 4) particularly the Multi-way jet-flow aerator be the linear layout of level or circular level uniform, being that institute's oxygenation air-flow is horizontal direction, is dead angle in following part aeration tank, this plane, can't obtain sufficient oxygen and stir kinetic energy, cause the aeration tank rate of utilization to descend, aggravated the increase of energy consumption.
Summary of the invention
In order to solve deficiency of the prior art, the utility model provides a kind of multichannel swirl jet aerator, has that dissolved oxygen efficiency is high, energy consumption is low, aeration is even, corrosion-resistant, advantages of simple structure and simple.
The utility model is to realize by following technical scheme:
A kind of multichannel swirl jet aerator, its primary structure is by formations such as inlet pipe, air chamber, cylindrical shell, integrated jet pipe, production well, hydroecium, water inlet pipes, wherein the upper end of air chamber is provided with inlet pipe, cylindrical shell is arranged at the bottom of air chamber, inner barrel is hydroecium, hydroecium and water inlet pipe UNICOM, and the cylindrical shell surrounding is uniformly distributed six integrated jet pipes, and in the hydroecium of integrated jet pipe oblique cutting in cylindrical shell, and be 60 ° of angles with the vertical line of cylindrical shell.
Described integrated jet pipe, its structure consists of: jet pipe inlet mouth, trunnion, wortex device, mixing tube, wortex device is connected with an end of trunnion, the jet pipe inlet mouth is arranged at the upside of the trunnion the other end, mixing tube is arranged at the other end of integrated jet pipe, production well in jet pipe inlet mouth and air chamber connects and fixes and UNICOM, and trunnion, mixing tube are by the injection molding once shaped.
Described wortex device, wastewater streams through the time, can produce strong eddy current, form negative pressuren zone in air chamber, thereby can suck a large amount of air by inlet pipe.
The characteristics such as in the utility model, parts adopt the PP material to make, and have good antiseptic property, and quality is light, and is durable in use.
Working process of the present utility model is: high pressure waste water is entered by the water inlet pipe of bottom, evenly enters each integrated jet pipe, through the strong eddy current of wortex device generation of its ingress, during eddy current process trunnion, because high-velocity jet forms negative pressuren zone at the trunnion end; Air with pressure enters air chamber by inlet pipe, by the production well of air chamber and the ejector inlet mouth at trunnion place, imported in integrated jet pipe, namely at the negative pressuren zone air water, fully contact, under the eddy current state, fully mix, dissolve in, then enter mixing tube and continue to mix, dissolve and diffusion, reach the purpose that increases dissolved oxygen efficiency.In addition, because integrated jet pipe and cylindrical shell are 60 ° of angles, at the bottom of causing air-water mixture by integrated jet pipe ejection to rush at aeration tank, fully stir the pond bottom sediment, both avoid the deposition of dead angle mud at the bottom of pond, increased again the stroke of microbubble in water, be conducive to improve dissolved oxygen efficiency.
The utility model passes through traditional Venturi tube, be improved to integrated jet pipe, when high pressure waste water process wortex device, can produce strong eddy current, negative pressure due to generation at a high speed during through trunnion sucks a large amount of air from air chamber, under the eddy current state, greatly improve the contact area of gas and waste water, increased dissolved oxygen efficiency; Integrated jet pipe is different from traditional jet pipe on the other hand, and mixing tube, trunnion are synthesized to an integral body, during the processing injection moulding, guarantees that precision is consistent, has not only improved the homogeneity of aeration, can also reach mixing comparatively fully of air water.
Owing to having adopted above technical scheme, the utility model is compared with currently available products, has following beneficial effect:
1), the utility model device all made by the PP material, and good antiseptic property is arranged, quality is light, and is durable in use, the life-span extends greatly;
2), integrated jet pipe and cylindrical shell be 60 ° of angles, prevents that place, dead angle, bottom, aeration tank from existing and the deposition of mud, increased utilization ratio and the dissolved oxygen efficiency of aeration tank;
3), wortex device is set in integrated jet pipe, form strong eddy current, increased the gas-to-liquid contact area, improved dissolved oxygen efficiency, save energy consumption;
4), trunnion, mixing tube once-forming in integrated jet pipe, guaranteed precision, improved the homogeneity of aeration;
5), the one-piece construction of equipment is simple, be connected firmly, and is and easy to operate, range of application enlarges.
The accompanying drawing explanation
Fig. 1, be cross-sectional view of the present utility model.
Fig. 2, be the utility model vertical view.
Fig. 3, be the structural representation of integrated jet pipe in the utility model.
In figure: 1-inlet pipe, 2-air chamber, 3-cylindrical shell, the integrated jet pipe of 4-, 5-production well, 6-hydroecium, 7-water inlet pipe, 8-jet pipe inlet mouth, 9-trunnion, 10-wortex device, 11-mixing tube.
As shown in Figures 1 to 3, a kind of multichannel swirl jet aerator, its primary structure is by formations such as inlet pipe 1, air chamber 2, cylindrical shell 3, integrated jet pipe 4, production well 5, hydroecium 6, water inlet pipes 7, wherein the upper end of air chamber 2 is provided with inlet pipe 1, cylindrical shell 3 is arranged at the bottom of air chamber 2, cylindrical shell 3 inside are hydroecium 6, hydroecium 6 and water inlet pipe 7 UNICOMs, cylindrical shell 3 surroundings are uniformly distributed six integrated jet pipes 4, and in the hydroecium 6 of integrated jet pipe 4 oblique cuttings in cylindrical shell 3, and be 60 ° of angles with the vertical line of cylindrical shell 3.
Described integrated jet pipe 4, its structure consists of: jet pipe inlet mouth 8, trunnion 9, wortex device 10, mixing tube 11, wortex device 10 is connected with an end of trunnion 9, jet pipe inlet mouth 8 is arranged at the upside of trunnion 9 the other ends, mixing tube 11 is arranged at the other end of integrated jet pipe 4, jet pipe inlet mouth 8 connects and fixes and UNICOM with the production well 5 in air chamber 2, and trunnion 9, mixing tube 11 are by the injection molding once shaped.
Described wortex device 10, wastewater streams through the time, can produce strong eddy current, greatly increase the gas-to-liquid contact area, the interior formation negative pressuren zone of air chamber 2, thus can suck a large amount of air by inlet pipe 1.
The characteristics such as in the utility model, parts adopt the PP material to make, and have good antiseptic property, and quality is light, and is durable in use.
Working process of the present utility model is: high pressure waste water is entered by the water inlet pipe 7 of bottom, evenly enter each integrated jet pipe 4, wortex device 10 through its ingress produces strong eddy current, during eddy current process trunnion 9, because high-velocity jet forms negative pressuren zones at trunnion 9 ends; Air with pressure enters air chamber 2 by inlet pipe 1, by the production well 5 of air chamber 2 and the ejector inlet mouth 8 at trunnion 9 places, imported in integrated jet pipe 4, namely at the negative pressuren zone air water, fully contact, under the eddy current state, fully mix, dissolve in, then enter mixing tube 11 and continue to mix, dissolve and diffusion, reach the purpose that increases dissolved oxygen efficiency.In addition, because integrated jet pipe 4 is 60 ° of angles with cylindrical shell 6, at the bottom of causing rushing at aeration tank by the air-water mixture that integrated jet pipe 4 sprays, fully stir the pond bottom sediment, both avoid the deposition of dead angle mud at the bottom of pond, increased again the stroke of microbubble in water, favourable raising dissolved oxygen efficiency.
The utility model passes through traditional Venturi tube, be improved to integrated jet pipe 4, when high pressure waste water process wortex device 10, can produce strong eddy current, negative pressure due to generation at a high speed during through trunnion 9 sucks a large amount of air from air chamber 2, under the eddy current state, greatly improve the contact area of gas and waste water, increased dissolved oxygen efficiency; Integrated jet pipe 4 is different from traditional jet pipe on the other hand, and mixing tube 11, trunnion 9 are synthesized to an integral body, during the processing injection moulding, guarantees that precision is consistent, has not only improved the homogeneity of aeration, can also reach mixing comparatively fully of air water.
Finally it should be noted that: above specification sheets is only in order to illustrate the technical solution of the utility model and use characteristic, although this specification sheets has been described in detail the utility model with reference to the above embodiments, but, those of ordinary skill in the art should be appreciated that still and can modify or be equal to replacement the utility model; And all do not break away from technical scheme and the improvement thereof of spirit and scope of the present utility model, and it all should be encompassed in claim scope of the present utility model.
Claims (2)
1. multichannel swirl jet aerator, its primary structure is by inlet pipe (1), air chamber (2), cylindrical shell (3), integrated jet pipe (4), production well (5), hydroecium (6), water inlet pipe (7) forms, it is characterized in that: wherein the upper end of air chamber (2) is provided with inlet pipe (1), cylindrical shell (3) is arranged at the bottom of air chamber (2), cylindrical shell (3) inside is hydroecium (6), hydroecium (6) and water inlet pipe (7) UNICOM, cylindrical shell (3) surrounding is uniformly distributed six integrated jet pipes (4), and in the hydroecium (6) of integrated jet pipe (4) oblique cutting in cylindrical shell (3), and be 60 ° of angles with the vertical line of cylindrical shell (3).
2. a kind of multichannel swirl jet aerator as claimed in claim 1, it is characterized in that: described integrated jet pipe (4), its structure is by jet pipe inlet mouth (8), trunnion (9), wortex device (10), mixing tube (11) forms, wortex device (10) is connected with an end of trunnion (9), jet pipe inlet mouth (8) is arranged at the upside of trunnion (9) the other end, mixing tube (11) is arranged at the other end of integrated jet pipe (4), jet pipe inlet mouth (8) connects and fixes and UNICOM with the production well (5) in air chamber (2), trunnion (9), mixing tube (11) is by the injection molding once shaped.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200160162U CN203295268U (en) | 2013-01-14 | 2013-01-14 | Multichannel vortex jet aerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200160162U CN203295268U (en) | 2013-01-14 | 2013-01-14 | Multichannel vortex jet aerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203295268U true CN203295268U (en) | 2013-11-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200160162U Expired - Fee Related CN203295268U (en) | 2013-01-14 | 2013-01-14 | Multichannel vortex jet aerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203295268U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556380A (en) * | 2015-01-05 | 2015-04-29 | 江苏苏亿环境工程有限公司 | Multifunctional sludge nitrification biological filter tower |
| CN106927565A (en) * | 2017-05-09 | 2017-07-07 | 周晓川 | A kind of hydrolysis acidification pool |
| CN107857310A (en) * | 2017-11-02 | 2018-03-30 | 东南大学 | Desulphurization denitration waste liquid degradation treatment equipment |
| CN109158046A (en) * | 2018-11-14 | 2019-01-08 | 辽阳博仕流体设备有限公司 | A kind of blended absorbent exhaust gas processing device |
| CN109485168A (en) * | 2019-01-08 | 2019-03-19 | 威海百克环保工程有限公司 | A kind of jet mixing aerator |
| TWI672998B (en) * | 2018-06-13 | 2019-10-01 | 吉拓環保工程有限公司 | Multi-connected aerator |
-
2013
- 2013-01-14 CN CN2013200160162U patent/CN203295268U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556380A (en) * | 2015-01-05 | 2015-04-29 | 江苏苏亿环境工程有限公司 | Multifunctional sludge nitrification biological filter tower |
| CN106927565A (en) * | 2017-05-09 | 2017-07-07 | 周晓川 | A kind of hydrolysis acidification pool |
| CN107857310A (en) * | 2017-11-02 | 2018-03-30 | 东南大学 | Desulphurization denitration waste liquid degradation treatment equipment |
| TWI672998B (en) * | 2018-06-13 | 2019-10-01 | 吉拓環保工程有限公司 | Multi-connected aerator |
| CN109158046A (en) * | 2018-11-14 | 2019-01-08 | 辽阳博仕流体设备有限公司 | A kind of blended absorbent exhaust gas processing device |
| CN109485168A (en) * | 2019-01-08 | 2019-03-19 | 威海百克环保工程有限公司 | A kind of jet mixing aerator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shanghai Kai Fan petrochemical equipment Co., Ltd Assignor: Shanghai Bizone Environmental Protection Equipment & Engineering Co., Ltd. Contract record no.: 2015310000013 Denomination of utility model: Multichannel vortex jet aerator Granted publication date: 20131120 License type: Exclusive License Record date: 20150115 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| EC01 | Cancellation of recordation of patent licensing contract |
Assignee: Shanghai Kai Fan petrochemical equipment Co., Ltd Assignor: Shanghai Bizone Environmental Protection Equipment & Engineering Co., Ltd. Contract record no.: 2015310000013 Date of cancellation: 20151218 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| 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: 20131120 Termination date: 20190114 |