CN204933368U - Aerator - Google Patents
Aerator Download PDFInfo
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- CN204933368U CN204933368U CN201520618638.1U CN201520618638U CN204933368U CN 204933368 U CN204933368 U CN 204933368U CN 201520618638 U CN201520618638 U CN 201520618638U CN 204933368 U CN204933368 U CN 204933368U
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- ring pipe
- jet
- nozzle
- tankage
- air inlet
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Abstract
The utility model relates to field of chemical equipment, specifically provide a kind of aerator, comprise air inlet supervisor, the first ring pipe, air compressor, described first ring pipe is arranged in the bottom solution of tankage, described first ring pipe is provided with multiple first jet, described first ring pipe is responsible for described air inlet and is communicated with, and described air compressor is arranged at the outside of described tankage, and described air inlet supervisor stretches out described tankage and is communicated with described air compressor.This is put device and is mainly used in desulphurization system, improves the efficiency be uniformly mixed, and by forced oxidation, reaches desulfurized effect.
Description
Technical field
The utility model relates to a kind of chemical industry equipment, in particular to a kind of aerator.
Background technology
Desulphurization system in the industry often can relate to aeration; existing aeration mode mostly is and arranges agitating device; the mixing of solution is improved by arranging the stirring of mixer to slurries; but the distance that stirring arm stretches into is unsuitable excessive; center liquid there will be " blind area ", and mixer exists the shortcomings such as cost is high, maintenance cost is high.Therefore, there is the not high problem of efficiency in existing agitating device.
Utility model content
The purpose of this utility model is to provide a kind of aerator.Be mainly used in desulphurization system, improve the problem that existing agitating device efficiency is not high.
The utility model is achieved in that
A kind of aerator, comprise air inlet supervisor, the first ring pipe, air compressor, described first ring pipe is arranged in the bottom solution of tankage, described first ring pipe is provided with multiple first jet, described first ring pipe is responsible for described air inlet and is communicated with, described air compressor is arranged at the outside of described tankage, and described air inlet supervisor stretches out described tankage and is communicated with described air compressor.
Above-described aerator, preferably, also comprise the second ring pipe, the diameter of described second ring pipe is less than the diameter of described first ring pipe, described second ring pipe is arranged in the region surrounded of described first ring pipe, described second ring pipe is provided with multiple second nozzle, and described second ring pipe is responsible for described air inlet and is communicated with.
First ring pipe difficulty or ease cover the bottom of whole tankage, the gas of the multiple first jet ejections on the first ring pipe stirs the liquid in tankage, but the effect in some place is poor, second ring pipe be arranged so that this aerator can cover the bottom of whole container more all sidedly, a large amount of gas that multiple second nozzle that second ring pipe is arranged and the multiple first jet on the first ring pipe spray makes the solution bottom solution carry out flowing and mixes, bubble rises simultaneously, also aeration has been carried out to the solution on tankage top, liquid-to-air is fully contacted.
Above-described aerator, preferably, the center of circle of described first ring pipe, the second ring pipe is all positioned at the center bottom described tankage.The position of the first ring pipe and the second ring pipe directly can affect the effect of whole aeration, the center be all arranged at bottom tankage, the center of circle of the two makes the pipeline of the two be distributed in uniformly bottom tankage, more easily comprehensive covering container device bottom, make aeration evenly, better effects if.
Above-described aerator, preferably, described multiple first jet is arranged at the both sides of described first ring pipe horizontal direction, and described multiple second nozzle is arranged at the both sides of described second ring pipe horizontal direction.The above-mentioned set-up mode of first jet and second nozzle, can make, and the area covered during gas ejection is larger, is more evenly distributed, thus aeration better effects if, solution mixing is more even.
Above-described aerator, preferably, described multiple first jet is acute angle with the angle of the outer wall of described first ring pipe and towards consistent, described multiple second nozzle is acute angle with the angle of the outer wall of described second ring pipe and towards consistent, described first jet and described second nozzle towards consistent.
Being arranged so that of first jet and second nozzle direction, the air-flow of ejection forms the air-flow of annular, the gas of ejection can converge formation helical form and rise, thus makes the liquid in tankage also have certain Stirring ability, and liquid is mixed to get more even.
Above-described aerator, preferably, described multiple first jet is arranged along the circumferencial direction uniform intervals of described first ring pipe, described multiple second nozzle is arranged along the circumferencial direction uniform intervals of described second ring pipe.The uniform intervals of first jet and second nozzle is arranged so that the contact of air-flow and liquid is more abundant, and the mixed effect between liquid is better.
Above-described aerator, preferably, the quantity of described multiple first jet is greater than 30, and the quantity of described multiple second nozzle is greater than 10.
The quantity of first jet and second nozzle directly can affect the covering of the exhaust gas region to whole container bottom, thus affects the contact area of gas and liquid, the effect of the whole aeration of final impact.The quantity of first jet is greater than 30, the quantity of second nozzle is greater than 10, can meet the demand of aeration effect well, make the gas that sprays in tankage can well with liquid comes into contact, and impel liquid to mix.
Above-described aerator, preferably, the internal diameter of the shower nozzle of described first jet, second nozzle reduces gradually along jet direction.
The reduction of the diameter of the shower nozzle of first jet, second nozzle makes that the speed of the gas sprayed is faster, dynamics is larger, thus it is larger to the impact of liquid, liquid can be rolled, and then can mix better and contact fully with gas better, reach good aeration effect.
Above-described aerator, preferably, described first ring pipe, the second ring pipe, air inlet supervisor, first jet, second nozzle all adopt fiberglass to make.The pipeline that glass steel material is made and nozzle have good intensity, and good heat-resisting quantity, corrosion resistance, and therefore, this material makes this aerator use in the solution can have good performance, and Long-Time Service and not fragile.
Above-described aerator, preferably, the position that described air inlet supervisor is positioned at described tankage outside is provided with flow control valve.According to the size of the aeration situation adjusting gas flow of tankage, thus aeration effect better can be reached by flow control valve, also can be cost-saving.
The beneficial effect that the utility model realizes: air passed in ring pipe extrude by arranging ring pipe in the bottom of tankage, make air agitation liquid, reach the abundant mixing of liquid.Make air fully contact with liquid, further oxidation liquid simultaneously, the sulphite in liquid is oxidized to sulfate better, reach the effect of desulfurization.Improve the efficiency be uniformly mixed.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, be briefly described to the accompanying drawing used required in embodiment below, be to be understood that, the following drawings illustrate only some embodiment of the present utility model, therefore the restriction to scope should be counted as, for those of ordinary skill in the art, under the prerequisite not paying creative work, other relevant accompanying drawings can also be obtained according to these accompanying drawings.
The structural representation of the aerator that Fig. 1 provides for embodiment of the present utility model;
The structural representation of the first jet of the aerator that Fig. 2 provides for embodiment of the present utility model.
Wherein, Reference numeral is: air inlet supervisor 100; First ring pipe 200; First jet 210; Tankage 300; Air compressor 400; Second ring pipe 500; Second nozzle 510; Flow control valve 600.
Detailed description of the invention
Desulphurization system in industry often can relate to aeration; existing aeration mode mostly is and arranges agitating device; the mixing of solution is improved by arranging the stirring of mixer to slurries; but the distance that stirring arm stretches into is unsuitable excessive; center liquid there will be " blind area ", and mixer exists the shortcomings such as cost is high, maintenance cost is high.Therefore, mainly there is the not high problem of efficiency in existing agitating device.
Inventor, by Chemical Manufacture experience long-term in a large number, through a large amount of experiments and thinking, proposes a kind of aerator, is mainly used in desulphurization system, not only increase the effect be uniformly mixed, and the oxygenation efficiency by forcing oxygenation to improve pressure salt.
Also by reference to the accompanying drawings the utility model is described in further detail below by specific embodiment.
As shown in the figure, the aerator that embodiment of the present utility model provides, comprises air inlet supervisor the 100, first ring pipe 200, air compressor 400.
First ring pipe 200 is arranged in the bottom solution of tankage 300, first ring pipe 200 is welded with multiple first jet 210, first ring pipe 200 and air inlet are responsible for 100 and are communicated with, air compressor 400 is arranged at the outside of tankage 300, and air inlet is responsible for 100 propelling container equipment 300 and is communicated with air compressor 400.
This aerator is mainly used in desulphurization system, by air compressor 400, air is responsible for 100 by air inlet, again gas is passed into the first ring pipe 200 by air inlet supervisor 100, multiple first jet 210 of the first ring pipe 200 are again by the solution bottom gas injection container equipment 300, gas fully contacts with solution, and constantly rises, while gas motion, liquid also rolls thereupon, and liquid agitation is mixed.And air inputs continually, improve oxygen content in solution, solution also increases the contact with oxygen in the roll procedure continued, and sulphite is oxidized to sulfate better, reaches the effect of desulfurization.
In the present embodiment, also comprise the second ring pipe 500, the diameter of the second ring pipe 500 is less than the diameter of the first ring pipe 200, second ring pipe 500 is arranged in the region surrounded of the first ring pipe 200, second ring pipe 500 is provided with multiple second nozzle 510, second ring pipe 500 and is responsible for 100 with air inlet and is communicated with.
First ring pipe 200 is the bottoms being difficult to cover whole tankage 300, therefore, although the air that multiple first jet 210 of the first ring pipe 200 spray, liquid in tankage 300 can be stirred, but always having some places is that first jet 210 difficulty or ease are sprayed onto and cause mixing effect poor, therefore, only arrange the first ring pipe 200 to be difficult to reach good aeration agitation effect.By arranging the second ring pipe 500, and equally multiple second nozzle 510 is set on the second ring pipe 500, the air that first jet 210 and second nozzle 510 are sprayed can cover the bottom of whole tankage 300 more all sidedly, and air first makes the solution flowing of the bottom of tankage 300 and mutually mixes endlessly.Meanwhile, air constantly rises in the solution, the solution on tankage 300 top is also flowed thereupon, mixes, and fully contact with air.Certainly, in other embodiments, also according to the size of tankage 300, more ring pipe can be set, make aeration better effects if, be not limited with the present embodiment.
In the present embodiment, the center of circle of the first ring pipe 200, second ring pipe 500 is all positioned at the center of the bottom of tankage 300.The center of circle of the first ring pipe 200, second ring pipe 500 determines the position of the arrangement of ring pipe, thus the region that the air also determining ejection roughly covers, therefore, the position in the center of circle of the two directly can affect the effect of whole aeration, when the center of circle is all arranged at the center of the bottom of tankage 300, relative to being arranged at other positions, the distribution of pipeline is more even, the air covering ground of ejection is also larger, thus make the stirring of liquid and mix more even, comprehensive, aeration better effects if.
In the present embodiment, preferably, multiple first jet 210 is arranged at the both sides of the first ring pipe 200 horizontal direction, multiple second nozzle 510 is arranged at the both sides of the second ring pipe 500 horizontal direction, namely the direction of the air of first jet 210, second nozzle 510 ejection is all positioned on the horizontal plane of tankage 300, the area that the air sprayed is covered reaches maximum, and distribution is also more even, the better effects if of liquid mixing.And, multiple first jet 210 is acute angle with the angle of the outer wall of the first ring pipe 200 and towards consistent, multiple second nozzle 510 is acute angle with the angle of the outer wall of described second ring pipe 500 and towards consistent, and the entirety of first jet 210 and second nozzle 510 is towards consistent.This set, can make the air-flow of ejection form the air-flow of annular, produce centrifugal force, thus makes the rolling of the liquid in tankage 300 more violent, stir also evenly.And the gas of ejection can converge and rises in the shape of a spiral, thus the liquid on tankage 300 top is also rolled with the air-flow risen, reach all liq all fully contacts also mixing and stirring effect with air.
In the present embodiment, multiple first jet 210 is arranged along the circumferencial direction uniform intervals of described first ring pipe 200, multiple second nozzle 510 is arranged along the circumferencial direction uniform intervals of described second ring pipe 500.This set makes the contact of air-flow and liquid more abundant, and the mixed effect between liquid is better.And the quantity of first jet 210 is greater than 30, the quantity of second nozzle 510 is greater than 10.First jet 210 directly can affect the covering of the exhaust gas region of the bottom to whole tankage 300 with the quantity of second nozzle 510, thus affects the contact area of gas and liquid, the effect of the whole aeration of final impact.The quantity of first jet 210 is greater than 30, the quantity of second nozzle 510 is greater than 10, can meet the demand of aeration effect well, make ejection in tankage 300 gas can well with liquid comes into contact, and impel liquid to mix.
In the present embodiment, with reference to accompanying drawing 2, preferably, first jet 210, second nozzle 510 are cylindric, and shower nozzle is round table-like, and the front end of shower nozzle has multiple spray orifice, and the internal diameter of shower nozzle reduces gradually along jet direction.The reduction of the diameter of shower nozzle, the pressure of the gas at shower nozzle place is constantly increased, thus the speed of the gas of ejection is faster, dynamics is larger, thus it is larger to the impact of liquid, liquid is rolled more violent, and then enable liquid mix better and contact fully with gas better, reach good aeration effect.
In the present embodiment, the first ring pipe 200, second ring pipe 500, air inlet supervisor 100, first jet 210, second nozzle 510 all adopt fiberglass to make.The pipeline that glass steel material is made and nozzle have good mechanical strength, and good high temperature resistant, corrosion resistance, and therefore, this material makes this aerator use in the solution can have good performance, can Long-Time Service and not fragile.
In the present embodiment, the position that air inlet supervisor 100 is positioned at the outside of tankage 300 is provided with flow control valve 600.According to the size of the aeration situation of tankage 300 adjusting gas flow at any time, to reach aeration effect better, thus aeration cost can be saved by flow control valve 600.
In sum, by arranging ring pipe in tankage 300, and nozzle is set on ring pipe, air is constantly passed in ring pipe, sprays from nozzle, the liquid in tankage 300 is constantly rolled, complete the mixing of liquid, liquid-to-air fully contacts simultaneously, and the sulphite in oxidized liquid, reaches desulfurized effect.
For making the object of the utility model embodiment, technical scheme and advantage clearly, above in conjunction with the accompanying drawing in the utility model embodiment, carry out describing clearly and completely to the technical scheme in the utility model embodiment, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.The assembly of the utility model embodiment describing and indicate in usual accompanying drawing herein can be arranged with various different configuration and design.
Therefore, the detailed description of the above embodiment of the present utility model to providing in the accompanying drawings the claimed scope of the present utility model of not intended to be limiting, but only represent selected embodiment of the present utility model.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
In description of the present utility model, it should be noted that, term " " center ", " on ", D score, " left side ", " right side ", " vertically ", " level ", " interior ", orientation or the position relationship of the instruction such as " outward " are based on orientation shown in the drawings or position relationship, or this utility model product orientation of usually putting or position relationship when using, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.In addition, term " first ", " second ", " the 3rd " etc. only for distinguishing description, and can not be interpreted as instruction or hint relative importance.
In description of the present utility model, also it should be noted that, unless otherwise clearly defined and limited, term " setting ", " installation ", " being connected ", " connection " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or connect integratedly; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, concrete condition the concrete meaning of above-mentioned term in the utility model can be understood.
Claims (10)
1. an aerator, it is characterized in that, comprise air inlet supervisor, the first ring pipe, air compressor, described first ring pipe is arranged in the bottom solution of tankage, described first ring pipe is provided with multiple first jet, described first ring pipe is responsible for described air inlet and is communicated with, and described air compressor is arranged at the outside of described tankage, and described air inlet supervisor stretches out described tankage and is communicated with described air compressor.
2. aerator according to claim 1, it is characterized in that, also comprise the second ring pipe, the diameter of described second ring pipe is less than the diameter of described first ring pipe, described second ring pipe is arranged in the region surrounded of described first ring pipe, described second ring pipe is provided with multiple second nozzle, and described second ring pipe is responsible for described air inlet and is communicated with.
3. aerator according to claim 2, is characterized in that, the center of circle of described first ring pipe, the second ring pipe is all positioned at the center bottom described tankage.
4. aerator according to claim 3, is characterized in that, described multiple first jet is arranged at the both sides of described first ring pipe horizontal direction, and described multiple second nozzle is arranged at the both sides of described second ring pipe horizontal direction.
5. aerator according to claim 4, it is characterized in that, described multiple first jet is acute angle with the angle of the outer wall of described first ring pipe and towards consistent, described multiple second nozzle is acute angle with the angle of the outer wall of described second ring pipe and towards consistent, described first jet and described second nozzle towards consistent.
6. aerator according to claim 5, is characterized in that, described multiple first jet is arranged along the circumferencial direction uniform intervals of described first ring pipe, described multiple second nozzle is arranged along the circumferencial direction uniform intervals of described second ring pipe.
7. the aerator according to any one of claim 2-6, is characterized in that, the quantity of described multiple first jet is greater than 30, and the quantity of described multiple second nozzle is greater than 10.
8. the aerator according to any one of claim 2-6, is characterized in that, the internal diameter of the shower nozzle of described first jet, second nozzle reduces gradually along jet direction.
9. the aerator according to any one of claim 2-6, is characterized in that, described first ring pipe, the second ring pipe, air inlet supervisor, first jet, second nozzle all adopt fiberglass to make.
10. aerator according to claim 1, is characterized in that, the position that described air inlet supervisor is positioned at described tankage outside is provided with flow control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520618638.1U CN204933368U (en) | 2015-08-17 | 2015-08-17 | Aerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520618638.1U CN204933368U (en) | 2015-08-17 | 2015-08-17 | Aerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204933368U true CN204933368U (en) | 2016-01-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520618638.1U Expired - Fee Related CN204933368U (en) | 2015-08-17 | 2015-08-17 | Aerator |
Country Status (1)
| Country | Link |
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| CN (1) | CN204933368U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106868912A (en) * | 2017-01-11 | 2017-06-20 | 杨太松 | A kind of stalk cellulose paper pulp toilet paper flow mixing device |
| CN109173879A (en) * | 2018-11-02 | 2019-01-11 | 攀钢集团矿业有限公司 | A kind of sulfuric acid preparation agitating device and the method with Sulphuric acid |
| CN109205811A (en) * | 2018-11-26 | 2019-01-15 | 航天环境工程有限公司 | A kind of stirring aerating system and the application certainly of flue gas desulphurization system waste water regulating box |
| CN109236218A (en) * | 2018-10-16 | 2019-01-18 | 四川宏华石油设备有限公司 | A kind of mud device |
| CN112791672A (en) * | 2020-12-31 | 2021-05-14 | 江苏卅维装备科技有限公司 | Bubble column reaction combination unit |
| CN114524547A (en) * | 2022-03-03 | 2022-05-24 | 济南市环境研究院(济南市黄河流域生态保护促进中心) | Integrated urban domestic sewage treatment system and method for efficiently removing phosphorus |
-
2015
- 2015-08-17 CN CN201520618638.1U patent/CN204933368U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106868912A (en) * | 2017-01-11 | 2017-06-20 | 杨太松 | A kind of stalk cellulose paper pulp toilet paper flow mixing device |
| CN109236218A (en) * | 2018-10-16 | 2019-01-18 | 四川宏华石油设备有限公司 | A kind of mud device |
| CN109173879A (en) * | 2018-11-02 | 2019-01-11 | 攀钢集团矿业有限公司 | A kind of sulfuric acid preparation agitating device and the method with Sulphuric acid |
| CN109205811A (en) * | 2018-11-26 | 2019-01-15 | 航天环境工程有限公司 | A kind of stirring aerating system and the application certainly of flue gas desulphurization system waste water regulating box |
| CN112791672A (en) * | 2020-12-31 | 2021-05-14 | 江苏卅维装备科技有限公司 | Bubble column reaction combination unit |
| CN114524547A (en) * | 2022-03-03 | 2022-05-24 | 济南市环境研究院(济南市黄河流域生态保护促进中心) | Integrated urban domestic sewage treatment system and method for efficiently removing phosphorus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20180817 |
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| CF01 | Termination of patent right due to non-payment of annual fee |