CN1569691A - Jet Aerating Reactor - Google Patents
Jet Aerating Reactor Download PDFInfo
- Publication number
- CN1569691A CN1569691A CNA2004100224545A CN200410022454A CN1569691A CN 1569691 A CN1569691 A CN 1569691A CN A2004100224545 A CNA2004100224545 A CN A2004100224545A CN 200410022454 A CN200410022454 A CN 200410022454A CN 1569691 A CN1569691 A CN 1569691A
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- nozzle body
- self
- sustained oscillation
- chamber
- upper spray
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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
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Abstract
The invention discloses a jet aeration reactor for industrial or urban sewage treatment, which comprises a nozzle, a top nozzle member, a self-induced vibration mixing chamber, a lower nozzle member and short tube, wherein the air intake duct is arranged on the top nozzle member and is in communication with the induction chamber in the top nozzle member, the nozzle through-hole, the induction chamber in the top nozzle member, the self-oscillation mixing chamber, the lower nozzle member and the short tube are in communication.
Description
Technical field:
The present invention relates to trade effluent or city domestic sewage treatment unit.This device is widely used in printing and dyeing, weaves, butchers, process hides, papermaking, sugaring, pharmacy, brewage, industry such as beer, food-processing, also can be used for industries such as underground water deferrization, fish pond and live fish transportation oxygenation.
Background technology:
Water, the gas mixed effect of the jet-flow aeration reactor existence of using at present are not good, and oxygenation capacity is not ideal enough, and jet boundary zone promotion poor-performing and service area are little.Utility model patent number is 89201391.5, its invention and created name is " a tooth-wheel bit oscillation pulsed water jet nozzle ", this nozzle is made up of upper and lower two nozzle bodies, the upper spray nozzle body is made up of flow-guiding mouth, upper spray nozzle, chamber three parts, the profile of upper spray nozzle body is a ladder right cylinder, intravital mouth body runner is made up of two index curved surfaces and three cylindrical surface, the top of following nozzle body is a curved surface Rotary-table, low profile is that ladder is cylindrical, jump ring is installed in its smallest cylinder surface, and the body inner flow passage of following nozzle body is a cylindrical hole.This nozzle is specially adapted to oil and gasser tooth-wheel bit.
Summary of the invention:
The object of the present invention is to provide a kind of jet-flow aeration reactor, this reactor is under the condition that adds supplementary unit, make water, gas thorough mixing in this reactor, make the continuous water, the gas two phase flow that become a mandarin change pulsating water, gas two phase flow into, improve water, gas mixing condition, improve the convection current diffusibility, utilize its pulse characteristic to increase the promotion and the service area of borderline region.
For achieving the above object, the present invention is according to the ultimate principle design technical scheme of " tooth-wheel bit oscillation pulsed water jet nozzle ".Nozzle 1 is sealedly and fixedly connected with upper spray nozzle body 3, and the conical ends that makes nozzle 1 extend in the induction chamber in the upper spray nozzle body 3, the exit end of nozzle 1 to the distance of the inlet end of self-sustained oscillation mixing chamber 4 be nozzle 1 the outlet interior diameter 0.5-2.5 doubly, the through hole that communicates with induction chamber in the upper spray nozzle body 3 is arranged in the nozzle 1, induction chamber in the upper spray nozzle body 3 is that inlet end is big, the solid of revolution that exit end is little, the inner profile curve of this solid of revolution is a straight-line segment, cambered outwards transition arc is formed by connecting with the equation of higher degree curve that concaves is smooth successively, air suction pipe 2 is fixedlyed connected with upper spray nozzle body 3 and is communicated with induction chamber in the upper spray nozzle body 3, the inlet end of the exit end of upper spray nozzle body 3 and self-sustained oscillation mixing chamber 4 is sealedly and fixedly connected, self-sustained oscillation mixing chamber 4 is a solid of revolution, the self-sustained oscillation hybrid chamber that opening is arranged in this solid of revolution, the interior diameter of self-sustained oscillation hybrid chamber be self-sustained oscillation mixing chamber (4) the ingate diameter 5.5-8.8 doubly, induction chamber in the upper spray nozzle body 3 communicates with the self-sustained oscillation hybrid chamber, following nozzle body 5 is a Rotary-table, its cone angle is 100-120 °, following nozzle body 5 is sealedly and fixedly connected with the opening end of self-sustained oscillation mixing chamber 4, and make the taper impact walls of Rotary-table be positioned at the self-sustained oscillation hybrid chamber, the inlet end of following nozzle body (5) to the distance of the inlet end of self-sustained oscillation hybrid chamber be self-sustained oscillation mixing chamber (4) the ingate diameter 2.2-3 doubly, the middle part of following nozzle body 5 has a through hole relative with the ingate of self-sustained oscillation hybrid chamber, the ingate diameter ratio of the diameter of the middle part through hole of following nozzle body (5) and self-sustained oscillation mixing chamber (4) is 1.2-2, exit end at the through hole that descends nozzle body 5 is installed short tube 6, and it is 25 ° of-35 ° of through holes that cone angle is arranged in the short tube 6.The present invention realizes goal of the invention like this: after the pressure water that penetrates from nozzle 1 sprays into induction chamber in the upper spray nozzle body 3, in induction chamber, form negative pressure, extraneous air from air suction pipe 2 be drawn into induction chamber and and pressure water enter together in the self-sustained oscillation hybrid chamber, when the impact walls under it arrives on the nozzle body also interacts with it, produce the pressure oscillation ripple in the impact zone, this ripple is upstream propagated with the velocity of sound, bring out new vorticity pulsation again, when the pressure pulsation that makes disengaging zone and impact zone anti-phase each other, will form the working cycle that vorticity disturbance-amplification-new vorticity pulsation produces, constantly repeat this process, in the self-sustained oscillation hybrid chamber, form intensive self-sustained oscillation, and with mix pulsating water very uniformly, the gas two phase flow is through the through hole and the ejection of short tube through hole of nozzle body 5 down.
The present invention compared with prior art has following technique effect:
This reactor is under the condition that adds supplementary unit, rely on the induction chamber in the upper spray nozzle body 3, special shape and specific border condition that self-sustained oscillation mixing chamber 4 and following nozzle body 5 self have, make water, gas is thorough mixing in the self-sustained oscillation hybrid chamber, and with the continuous water of incoming flow, the gas two phase flow changes pulsating water into, the gas two phase flow, and the amplitude that goes out flowing pressure is than the high 15-30% of incoming flow, not only improved water widely, gas mixing condition, the transformation efficiency height of oxygen, and strengthened the turbulent fluctuation of aerobic water body, improved the convection current diffusibility, the number of bubbles that produces is many, diameter is little, and the bubble coalescence phenomenon significantly reduces, and has increased the service area of aeration reactor, short tube helps producing cavitation stream, has strengthened water, the separation of gas.
Description of drawings:
Fig. 1 is a sectional arrangement drawing of the present invention.
Among Fig. 1:
1-nozzle 2-air suction pipe 3-upper spray nozzle body
Nozzle body 6-short tube under the 4-self-sustained oscillation mixing chamber 5-
Embodiment:
Nozzle 1, upper spray nozzle body 3, self-sustained oscillation mixing chamber 4, nozzle body 5 and short tube 6 are installed on the same medullary ray successively down, and air suction pipe 2 is vertically mounted on the outside surface of open circles shell of column of upper spray nozzle body.Through hole in the nozzle 1 is made up of cylindrical hole and round taper hole, and the cone angle of this round taper hole is 12.5 °-13.5 °.The mode of connection of nozzle 1 and upper spray nozzle body 3 is for being threaded or welding or flange are connected.The purpose of the inner profile curve of design upper spray nozzle intravital induction chamber is in order to improve the orifice coefficient that water, gas two phase flow enter self-sustained oscillation mixing chamber ingate, this inner profile curve is straight-line segment, cambered outwards transition arc and smooth successively being formed by connecting of equation of higher degree curve that concave, upper spray nozzle body 3 is to be the solid of revolution of bus with this inner profile curve, and this turns round intravital induction chamber and is made of curved surface truncated cone-shaped cylindrical and that diminish gradually.Wherein the radius of cambered outwards transition arc determines that by the interior diameter of upper spray nozzle body 3 equation of higher degree that concaves is monobasic 2 times or 3 times or 4 times or 5 equation of n th order n, is generally monobasic 4 equation of n th order n.The mode of connection of self-sustained oscillation mixing chamber 4 and upper spray nozzle body 3 is for being threaded or flange is connected.The opening end of self-sustained oscillation mixing chamber 4 is fixedly connected into integral body with following nozzle body 5.Generally speaking, the opening end of self-sustained oscillation mixing chamber 4 and following nozzle body 5 are for being threaded, and there is columniform through hole at the middle part of following nozzle body, and short tube 6 is threaded whole with following nozzle body 5.The through hole that truncated cone-shaped is arranged in the short tube.
Claims (3)
1, a kind of jet-flow aeration reactor, it is characterized in that nozzle (1) and upper spray nozzle body (3) are sealedly and fixedly connected, and the conical end that makes nozzle (1) extend in the interior induction chamber of upper spray nozzle body (3), the exit end of nozzle (1) to the distance of the inlet end of self-sustained oscillation mixing chamber (4) be nozzle (1) the outlet interior diameter 0.5-2.5 doubly, have in the nozzle (1) with upper spray nozzle body (3) in the through hole that communicates of induction chamber, induction chamber in the upper spray nozzle body (3) is that inlet end is big, the solid of revolution that exit end is little, the inner profile curve of this solid of revolution is a straight-line segment, cambered outwards transition arc is formed by connecting with the equation of higher degree curve that concaves is smooth successively, air suction pipe (2) fixedly connected with upper spray nozzle body (3) and with upper spray nozzle body (3) in induction chamber communicate, the inlet end of the exit end of upper spray nozzle body (3) and self-sustained oscillation mixing chamber (4) is sealedly and fixedly connected, self-sustained oscillation mixing chamber (4) is a solid of revolution, the self-sustained oscillation hybrid chamber that opening is arranged in this solid of revolution, the interior diameter of self-sustained oscillation hybrid chamber be self-sustained oscillation mixing chamber (4) the ingate diameter 5.5-8.8 doubly, induction chamber in the upper spray nozzle body (3) communicates with the self-sustained oscillation hybrid chamber, following nozzle body (5) is a Rotary-table, its cone angle is 100 °-120 °, following nozzle body (5) is sealedly and fixedly connected with the opening end of self-sustained oscillation mixing chamber (4), and the impact walls that makes Rotary-table is positioned at the self-sustained oscillation hybrid chamber, the inlet end of following nozzle body (5) to the distance of the inlet end of self-sustained oscillation hybrid chamber be self-sustained oscillation mixing chamber (4) the ingate diameter 2.2-3 doubly, the middle part of following nozzle body (5) has the interior ingate of a through hole and the inlet end of self-sustained oscillation mixing chamber (4) relative, the ingate diameter ratio of the diameter of the middle part through hole of following nozzle body (5) and self-sustained oscillation mixing chamber (4) is 1.2-2, exit end at the through hole that descends nozzle body (5) is installed short tube (6), and it is 25 ° of-35 ° of through holes that cone angle is arranged in the short tube (6).
2, jet-flow aeration reactor according to claim 1 is characterized in that nozzle (1), upper spray nozzle body (3), self-sustained oscillation mixing chamber (4), following nozzle body (5) and short tube (6) are installed on the same medullary ray successively.
3, jet-flow aeration reactor according to claim 1 is characterized in that the through hole in the nozzle (1) is made up of cylindrical hole and round taper hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100224545A CN1233573C (en) | 2004-05-02 | 2004-05-02 | Jet Aerating Reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100224545A CN1233573C (en) | 2004-05-02 | 2004-05-02 | Jet Aerating Reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1569691A true CN1569691A (en) | 2005-01-26 |
| CN1233573C CN1233573C (en) | 2005-12-28 |
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ID=34480131
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100224545A Expired - Fee Related CN1233573C (en) | 2004-05-02 | 2004-05-02 | Jet Aerating Reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1233573C (en) |
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1325806C (en) * | 2005-12-26 | 2007-07-11 | 重庆大学 | Pipe pulse stream generator |
| CN102161020A (en) * | 2011-03-28 | 2011-08-24 | 北京航空航天大学 | Self-excited vibration jet impact type nozzle with conical reflecting surface resonant cavity |
| CN102588353A (en) * | 2012-02-14 | 2012-07-18 | 重庆工商大学 | Self excited oscillation type jet vacuum pump |
| CN102865256A (en) * | 2012-09-19 | 2013-01-09 | 上海大学 | Self-oscillation pulsed liquid-gas jet pump |
| CN102909142A (en) * | 2011-08-05 | 2013-02-06 | 李远明 | Water gun for aerated pulse water jet |
| CN103004677A (en) * | 2012-12-04 | 2013-04-03 | 大连金砣水产食品有限公司 | Shipborne jet gun |
| CN103102021A (en) * | 2013-02-27 | 2013-05-15 | 湛江市科海科技有限公司 | High oxygen ejector |
| CN103224296A (en) * | 2013-04-25 | 2013-07-31 | 辽阳博仕流体设备有限公司 | Air-supply-type self-excited oscillation pulse jet aerator |
| CN103253761A (en) * | 2013-04-15 | 2013-08-21 | 浙江工业大学 | Self-oscillation micropore aerator |
| CN103990394A (en) * | 2014-04-30 | 2014-08-20 | 重庆优楷科技有限公司 | Centrifugation jet apparatus applied to sewage processing |
| CN104006041A (en) * | 2013-02-25 | 2014-08-27 | 中国石油天然气集团公司 | Pipe pulse stream generator |
| CN104226179A (en) * | 2014-09-20 | 2014-12-24 | 中北大学 | Device and process for continuously preparing methanol emulsified diesel fuel |
| CN103657497B (en) * | 2012-08-30 | 2015-10-28 | 宝山钢铁股份有限公司 | For three grades of hybrid systems of liquid mixing |
| CN105645510A (en) * | 2015-12-30 | 2016-06-08 | 陕西师范大学 | Circulation flow reactor with guiding body component |
| CN109052614A (en) * | 2018-07-19 | 2018-12-21 | 西安交通大学 | A kind of system and method evaporating wall type reactor water film coverage rate for adjusting supercritical water oxidation |
| CN109133317A (en) * | 2018-07-19 | 2019-01-04 | 西安交通大学 | A method of wall type reactor water film thickness is evaporated for optimizing regulation supercritical water oxidation |
| CN109748410A (en) * | 2019-02-19 | 2019-05-14 | 东北师范大学 | A kind of device and the application of the method for synergy gas-liquid mass transfer and realization this method |
| CN113769598A (en) * | 2021-08-24 | 2021-12-10 | 北京协同创新食品科技有限公司 | Jet flow mixing nozzle |
| CN115463600A (en) * | 2022-10-18 | 2022-12-13 | 安徽理工大学 | Efficient mixing and pulp mixing device and method for medicament and ore pulp |
| CN115928646A (en) * | 2022-11-04 | 2023-04-07 | 重庆科技学院 | Ring self-oscillation gas lift device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102069049B (en) * | 2010-11-24 | 2014-06-18 | 华北水利水电学院 | Self-excitation aspiration pulse jet nozzle |
-
2004
- 2004-05-02 CN CNB2004100224545A patent/CN1233573C/en not_active Expired - Fee Related
Cited By (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1325806C (en) * | 2005-12-26 | 2007-07-11 | 重庆大学 | Pipe pulse stream generator |
| CN102161020B (en) * | 2011-03-28 | 2013-03-06 | 北京航空航天大学 | Self-excited vibration jet impact type nozzle with conical reflecting surface resonant cavity |
| CN102161020A (en) * | 2011-03-28 | 2011-08-24 | 北京航空航天大学 | Self-excited vibration jet impact type nozzle with conical reflecting surface resonant cavity |
| CN102909142A (en) * | 2011-08-05 | 2013-02-06 | 李远明 | Water gun for aerated pulse water jet |
| CN102588353A (en) * | 2012-02-14 | 2012-07-18 | 重庆工商大学 | Self excited oscillation type jet vacuum pump |
| CN102588353B (en) * | 2012-02-14 | 2016-02-03 | 重庆工商大学 | Self excited oscillation type jet vacuum pump |
| CN103657497B (en) * | 2012-08-30 | 2015-10-28 | 宝山钢铁股份有限公司 | For three grades of hybrid systems of liquid mixing |
| CN102865256A (en) * | 2012-09-19 | 2013-01-09 | 上海大学 | Self-oscillation pulsed liquid-gas jet pump |
| CN103004677A (en) * | 2012-12-04 | 2013-04-03 | 大连金砣水产食品有限公司 | Shipborne jet gun |
| CN104006041B (en) * | 2013-02-25 | 2016-10-19 | 中国石油天然气集团公司 | A kind of pipe pulse stream generator |
| CN104006041A (en) * | 2013-02-25 | 2014-08-27 | 中国石油天然气集团公司 | Pipe pulse stream generator |
| CN103102021A (en) * | 2013-02-27 | 2013-05-15 | 湛江市科海科技有限公司 | High oxygen ejector |
| CN103253761A (en) * | 2013-04-15 | 2013-08-21 | 浙江工业大学 | Self-oscillation micropore aerator |
| CN103224296A (en) * | 2013-04-25 | 2013-07-31 | 辽阳博仕流体设备有限公司 | Air-supply-type self-excited oscillation pulse jet aerator |
| CN103224296B (en) * | 2013-04-25 | 2015-01-07 | 辽阳博仕流体设备有限公司 | Air-supply-type self-excited oscillation pulse jet aerator |
| CN103990394A (en) * | 2014-04-30 | 2014-08-20 | 重庆优楷科技有限公司 | Centrifugation jet apparatus applied to sewage processing |
| CN104226179A (en) * | 2014-09-20 | 2014-12-24 | 中北大学 | Device and process for continuously preparing methanol emulsified diesel fuel |
| CN105645510A (en) * | 2015-12-30 | 2016-06-08 | 陕西师范大学 | Circulation flow reactor with guiding body component |
| CN109052614A (en) * | 2018-07-19 | 2018-12-21 | 西安交通大学 | A kind of system and method evaporating wall type reactor water film coverage rate for adjusting supercritical water oxidation |
| CN109133317A (en) * | 2018-07-19 | 2019-01-04 | 西安交通大学 | A method of wall type reactor water film thickness is evaporated for optimizing regulation supercritical water oxidation |
| CN109052614B (en) * | 2018-07-19 | 2020-07-28 | 西安交通大学 | System and method for adjusting water film coverage rate of supercritical water oxidation evaporation wall type reactor |
| CN109748410A (en) * | 2019-02-19 | 2019-05-14 | 东北师范大学 | A kind of device and the application of the method for synergy gas-liquid mass transfer and realization this method |
| CN109748410B (en) * | 2019-02-19 | 2020-07-24 | 东北师范大学 | Method for enhancing gas-liquid mass transfer, device for implementing method and application |
| CN113769598A (en) * | 2021-08-24 | 2021-12-10 | 北京协同创新食品科技有限公司 | Jet flow mixing nozzle |
| CN115463600A (en) * | 2022-10-18 | 2022-12-13 | 安徽理工大学 | Efficient mixing and pulp mixing device and method for medicament and ore pulp |
| CN115463600B (en) * | 2022-10-18 | 2023-07-21 | 安徽理工大学 | Efficient mixing and pulp mixing device and method for medicament and ore pulp |
| CN115928646A (en) * | 2022-11-04 | 2023-04-07 | 重庆科技学院 | Ring self-oscillation gas lift device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1233573C (en) | 2005-12-28 |
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