CN101696043A - Progressive air flotation device - Google Patents
Progressive air flotation device Download PDFInfo
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- CN101696043A CN101696043A CN200910197876A CN200910197876A CN101696043A CN 101696043 A CN101696043 A CN 101696043A CN 200910197876 A CN200910197876 A CN 200910197876A CN 200910197876 A CN200910197876 A CN 200910197876A CN 101696043 A CN101696043 A CN 101696043A
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- cell body
- supporting cell
- air
- air supporting
- flotation device
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Abstract
The invention discloses a progressive air flotation device, which can effectively overcome the drawbacks of the traditional serial two-stage air flotation device. In the progressive air flotation device, waste water enters from an aerator, and oil, suspended substances and other wastes in the waste water subjected to coagulation and flocculation reactions in a front stage first rise up to the surface of the waste water under the supporting action of air bubbles generated by the aerator, then are constantly removed to a waste collection tank by a slag scraper and finally are conveyed out by a screw conveyor; and the waste water moves forward under the action of gravity and overflows from a lower part into a second stage to be further mixed by a back-flow device and an air dissolution device to remove oil and wastes which rise up to the surface. Thus, the wastes are removed and the aim of the invention is fulfilled.
Description
Technical field
The present invention relates to the equipment of a kind of profit, solid-liquid separation, be particularly related to a kind of various oily(waste)water pre-treatment of industry such as iron and steel, petrochemical industry, emergency episode processing, progressive air flotation device of collection and treatment oil slick, oil in water emulsion, suspended substance, chemical oxygen demand (COD) efficiently of being used for.
Background technology
Air-floating apparatus is widely used in every field as the waste-oil scavenger of Wastewater Pretreatment, particularly in industries such as iron and steel, petrochemical industry, adopt one-level air supporting reaction also to be not enough to allow oil, suspended substance and other dirt be removed to the concentration that follow-up facility can bear, therefore, usually all be to adopt the method that two air-floating apparatus are together in series and handle by two-stage air supporting in industries such as iron and steel, petrochemical industry, though the method that this two-stage air supporting is handled can satisfy the requirement of follow-up facility, also there is following shortcoming:
1) floor space is big, and every air-floating apparatus all needs independently coagulation reaction tank is set, and also needs pipe connection between the air-floating apparatus, and floor space is too big;
2) working cost height, two air-floating apparatus all need to be equipped with independently reflux pump, agitator, slag scraper etc.;
3) investment is high, and aspects such as two same air-floating apparatus slave units, material, control are all higher.
Therefore, in view of having now in industries such as iron and steel, petrochemical industry all is to adopt two air-floating apparatus are together in series to carry out the more existing problems of treatment process by two-stage air supporting, need a kind of airfloat equipment that satisfies the Wastewater Pretreatment function especially, remedy existing weak point.
Summary of the invention
The object of the present invention is to provide a kind of progressive air flotation device, can effectively remedy the deficiency that the series connection of existing two-stage air-floating apparatus is handled, simple to operate, easy to maintenance, applied widely, remove the efficient height, can be applied to all trades and professions of wastewater treatment.
Technical problem solved by the invention can realize by the following technical solutions:
A kind of progressive air flotation device, it comprises the air supporting cell body, the air supporting cell body is provided with water-in and water outlet, it is characterized in that, water inlet at described air supporting cell body is provided with aerating apparatus, the current that the bottom of described aerating apparatus is connected with described air supporting cell body bottom are back to the reflux that described aerating apparatus precipitates the removal of dirt secondary circulation, above the intravital current liquid level of described air flotation slot, be provided with the slag scraper that the buoyant dirt above the current liquid level is struck off sewage sump, described sewage sump is arranged on the edge of described slag scraper, is provided with air-dissolving apparatus at the water outlet place of described air supporting cell body and is connected to the bottom of described air supporting cell body by pipeline.
In one embodiment of the present of invention, be provided with one in the bottom of described slag scraper the dirt in the sewage sump discharged the helix transporting device of described air supporting cell body.
In one embodiment of the present of invention, described air supporting cell body is made by materials such as carbon steel, stainless steel, concrete, and carries out corresponding rotproofing according to the occasion difference.
In one embodiment of the present of invention, described aerating apparatus is made of aerator and impeller, described aerator is vertically set on the water inlet of described air supporting cell body, and described impeller is arranged near place, described air supporting cell body bottom and by union lever and is connected with described aerator.
In one embodiment of the present of invention, described slag scraper is made by materials such as stainless steel, rubber, superpolymer, described slag scraper is by constituting around chain, the chain drive-belt motor rotating of two ends cycle rotation and the scraper plate that is arranged on the chain,, scum silica frost is struck off around the two ends cycle rotation by the described chain of described electric motor driving by described scraper plate.
In one embodiment of the present of invention, described reflux is that the mud with the extremely described air supporting cell body of partly precipitated bottom is back to the return line that described aerating apparatus floats once more.
In one embodiment of the present of invention, described air-dissolving apparatus is that a part water outlet with described air supporting cell body water outlet mixes once more with the waste water that preceding pars infrasegmentalis overflows, discharge the air dissolved pump that micro-bubble holds up remaining dirt, described air dissolved pump is communicated with described air supporting cell body bottom with the sufficient convergent divergent channel of air mixed with the waste water that preceding pars infrasegmentalis overflows by a part water outlet with described air supporting cell body water outlet.
Further, described convergent divergent channel is made by carbon steel, and it is abundant with mixing of water to be used for air.
Progressive air flotation device of the present invention has following characteristics with respect to existing air-floating apparatus:
1) adopts intensive design, merged the pneumatically supported effect of two-stage, optimize and combine in a set of equipment, saved floor space.
2) adopt a cover slag scraper, compare, saved energy consumption, saved running cost with the setting of the independent air-floating apparatus of two-stage.
3) compact design has been saved material, has saved intermediate connection tube road, valve etc. simultaneously.
4) operational management is convenient, and the parts that do not need repairing in the air supporting cell body, all moving partss can reach the complete assembly low pressure operation conveniently.
Progressive air flotation device of the present invention, can effectively remedy the deficiency of existing series connection two-stage air-floating apparatus, waste water enters from aerating apparatus, through of the support effect of leading portion coagulation-flocculation reacted wastewater through the bubble of aerating apparatus generation, dirts such as reacted oil and suspended substance rise to the waste water surface, constantly strike off in the sewage sump through slag scraper, send through helix transporting device; Waste water is moved forward by gravity, from the bottom overflow to secondary by reflux and the further mixing of air-dissolving apparatus oil and dirt come-up is struck off once more to the surface, thereby finishes the work of removing dirt, realizes purpose of the present invention.
Characteristics of the present invention can be consulted the detailed description of the graphic and following better embodiment of this case and be obtained to be well understood to.
Description of drawings
Fig. 1 is the structural representation of progressive air flotation device of the present invention;
Fig. 2 is the schematic top plan view of progressive air flotation device of the present invention.
Embodiment
For technique means, creation characteristic that the present invention is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the present invention.
Embodiment
As Fig. 1, shown in Figure 2, progressive air flotation device of the present invention, it comprises air supporting cell body 10, air supporting cell body 10 is provided with water-in 11 and water outlet 12, water-in 11 places at air supporting cell body 10 are provided with aerating apparatus 20, the bottom of aerating apparatus 20 is connected with reflux 30, reflux 30 is back to aerating apparatus 20 with the current of air supporting cell body 10 bottoms and precipitates the dirt secondary circulation and remove, be provided with slag scraper 40 above the current liquid level in air supporting cell body 10, slag scraper 40 strikes off the buoyant dirt of current liquid level top in the sewage sump 13, sewage sump 13 is arranged on the edge of slag scraper 40, is provided with air-dissolving apparatus 50 at water outlet 12 places of air supporting cell body 10 and is connected to the bottom of air supporting cell body 10 by pipeline.
Be provided with a helix transporting device 60 with the dirt vent gas floating trough body 10 in the sewage sump 13 in the bottom of slag scraper 40, helix transporting device 60 adopts stainless steel or carbon steel material, and successively running is released air supporting cell body 10 with scum silica frost from sewage sump 13.
Among the present invention, air supporting cell body 10 is made by materials such as carbon steel, stainless steel, concrete, and carries out corresponding rotproofing according to the occasion difference.
Aerating apparatus 20 is made of aerator 21 and impeller 22, and aerator 21 is vertically set on water-in 11 places of air supporting cell body 10, and impeller 22 is arranged near place, air supporting cell body 10 bottoms and by union lever 23 and is connected with aerator 21; Aerator 21 drives impeller 22 high speed rotating of below by union lever 23, dirt in the bubble that produces and the waste water that water-in 11 by air supporting cell body 10 flows in the air supporting cell bodies 10 through coagulation-flocculation react contact after, make the surface that floats to waste water on the dirts such as oil and suspended substance, struck off by slag scraper 40.
Device 7 is back to the casing middle part for air dissolved pump mixes the portion water of water side with pressurized air, and dirt further contacts come-up in the bubble of generation and the sewage, equally by 4 strike off.
Air-dissolving apparatus 50 is an air dissolved pump 51, air dissolved pump 51 mixes the part water outlet of air supporting cell body 10 water outlets 12 once more with the waste water that preceding pars infrasegmentalis overflows, waste water that the part water outlet and the preceding pars infrasegmentalis of air supporting cell body 10 water outlets 12 is overflowed by convergent divergent channel 52 and air mixed fully and discharge micro-bubble remaining dirt is held up, convergent divergent channel 52 is communicated with air supporting cell body 10 bottoms by pipeline.
Convergent divergent channel 52 is made by carbon steel, and it is abundant with mixing of water to be used for air.
During work, waste water enters from aerating apparatus 20, through of the support effect of leading portion coagulation-flocculation reacted wastewater through the bubble of 21 impeller of aerator in the aerating apparatus 20,22 generations, dirts such as reacted oil and suspended substance rise to the waste water surface, constantly strike off in the sewage sump 13 through slag scraper 40, send through helix transporting device 60; Waste water is moved forward by gravity, from the bottom overflow to secondary by reflux 30 and air-dissolving apparatus 50 further mixing oil and dirt come-up is struck off once more to the surface, thereby finishes the work of removing dirt.
More than show and described ultimate principle of the present invention and principal character and advantage of the present invention.The technician of the industry should understand; the present invention is not restricted to the described embodiments; that describes in the foregoing description and the specification sheets just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications; these changes and improvements all fall in the claimed scope of the invention, and the claimed scope of the present invention is defined by appending claims and equivalent thereof.
Claims (8)
1. progressive air flotation device, it comprises the air supporting cell body, the air supporting cell body is provided with water-in and water outlet, it is characterized in that, water inlet at described air supporting cell body is provided with aerating apparatus, the current that the bottom of described aerating apparatus is connected with described air supporting cell body bottom are back to the reflux that described aerating apparatus precipitates the removal of dirt secondary circulation, above the intravital current liquid level of described air flotation slot, be provided with the slag scraper that the buoyant dirt above the current liquid level is struck off sewage sump, described sewage sump is arranged on the edge of described slag scraper, is provided with air-dissolving apparatus at the water outlet place of described air supporting cell body and is connected to the bottom of described air supporting cell body by pipeline.
2. progressive air flotation device as claimed in claim 1 is characterized in that, is provided with one in the bottom of described slag scraper the dirt in the sewage sump discharged the helix transporting device of described air supporting cell body.
3. progressive air flotation device as claimed in claim 1 is characterized in that, described air supporting cell body is made by materials such as carbon steel, stainless steel, concrete, and carries out corresponding rotproofing according to the occasion difference.
4. progressive air flotation device as claimed in claim 1, it is characterized in that, described aerating apparatus is made of aerator and impeller, described aerator is vertically set on the water inlet of described air supporting cell body, and described impeller is arranged near place, described air supporting cell body bottom and by union lever and is connected with described aerator.
5. progressive air flotation device as claimed in claim 1, it is characterized in that, described slag scraper is made by materials such as stainless steel, rubber, superpolymer, described slag scraper is by constituting around chain, the chain drive-belt motor rotating of two ends cycle rotation and the scraper plate that is arranged on the chain,, scum silica frost is struck off around the two ends cycle rotation by the described chain of described electric motor driving by described scraper plate.
6. progressive air flotation device as claimed in claim 1 is characterized in that, described reflux is that the mud with the extremely described air supporting cell body of partly precipitated bottom is back to the return line that described aerating apparatus floats once more.
7. progressive air flotation device as claimed in claim 1, it is characterized in that, described air-dissolving apparatus is that a part water outlet with described air supporting cell body water outlet mixes once more with the waste water that preceding pars infrasegmentalis overflows, discharge the air dissolved pump that micro-bubble holds up remaining dirt, described air dissolved pump is communicated with described air supporting cell body bottom with the sufficient convergent divergent channel of air mixed with the waste water that preceding pars infrasegmentalis overflows by a part water outlet with described air supporting cell body water outlet.
8. progressive air flotation device as claimed in claim 7 is characterized in that described convergent divergent channel is made by carbon steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910197876A CN101696043A (en) | 2009-10-29 | 2009-10-29 | Progressive air flotation device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910197876A CN101696043A (en) | 2009-10-29 | 2009-10-29 | Progressive air flotation device |
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| CN101696043A true CN101696043A (en) | 2010-04-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN200910197876A Pending CN101696043A (en) | 2009-10-29 | 2009-10-29 | Progressive air flotation device |
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Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102603088A (en) * | 2011-10-31 | 2012-07-25 | 宜兴市紫晶环保设备有限公司 | Bi-stage air floater |
| CN102774921A (en) * | 2012-08-15 | 2012-11-14 | 北京英特环科水处理工程设备有限公司 | Nanometer (NM) gas floating system device |
| CN104341021A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Progressive air floatation apparatus |
| CN105481040A (en) * | 2016-01-25 | 2016-04-13 | 浙江瑞丰机械设备有限公司 | Electroplating oil-water separation device |
| CN105518457A (en) * | 2013-08-06 | 2016-04-20 | 巴克泰斯特有限公司 | Respirometer |
| CN105502550A (en) * | 2016-01-25 | 2016-04-20 | 浙江瑞丰机械设备有限公司 | Slag scrap-away device of electroplating oil-water separating device |
| CN106179772A (en) * | 2016-07-15 | 2016-12-07 | 河北润达环保科技有限公司 | A kind of highly difficult sewage multi-stage, efficient flotation device |
| CN107416934A (en) * | 2017-05-28 | 2017-12-01 | 韦爱龄 | Vibrating air floating pond |
| CN107416935A (en) * | 2017-05-28 | 2017-12-01 | 韦爱龄 | Rotary flotation tank |
| CN108821516A (en) * | 2018-07-26 | 2018-11-16 | 陈剑璋 | A kind of hospital gauze degreasing sewage-treatment plant |
| CN109160633A (en) * | 2018-09-20 | 2019-01-08 | 黄家仓 | A kind of trade effluent air floatation machine having processing pollution gas function |
| CN110563068A (en) * | 2019-11-05 | 2019-12-13 | 山东海普欧环保设备科技有限公司 | Aeration air-float machine |
| CN112358008A (en) * | 2021-01-12 | 2021-02-12 | 山东奥士德石油技术有限公司 | Polymer drives oil field sewage treatment plant |
| CN113877279A (en) * | 2021-09-27 | 2022-01-04 | 池州万维化工有限公司 | Kettle liquid filtering device for preparing 8-hydroxyquinoline |
| CN115353168A (en) * | 2022-10-20 | 2022-11-18 | 山东中加环境科技有限公司 | Petroleum sewage treatment device |
| CN117303489A (en) * | 2023-11-20 | 2023-12-29 | 三强环保集团有限公司 | Sequential air floating device |
-
2009
- 2009-10-29 CN CN200910197876A patent/CN101696043A/en active Pending
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102603088A (en) * | 2011-10-31 | 2012-07-25 | 宜兴市紫晶环保设备有限公司 | Bi-stage air floater |
| CN102603088B (en) * | 2011-10-31 | 2013-07-24 | 宜兴市紫晶环保设备有限公司 | Bi-stage air floater |
| CN102774921A (en) * | 2012-08-15 | 2012-11-14 | 北京英特环科水处理工程设备有限公司 | Nanometer (NM) gas floating system device |
| CN102774921B (en) * | 2012-08-15 | 2014-01-15 | 北京英特环科水处理工程设备有限公司 | Nanometer (NM) gas floating system device |
| CN104341021A (en) * | 2013-07-30 | 2015-02-11 | 麦王环境技术股份有限公司 | Progressive air floatation apparatus |
| CN105518457A (en) * | 2013-08-06 | 2016-04-20 | 巴克泰斯特有限公司 | Respirometer |
| CN105481040A (en) * | 2016-01-25 | 2016-04-13 | 浙江瑞丰机械设备有限公司 | Electroplating oil-water separation device |
| CN105502550A (en) * | 2016-01-25 | 2016-04-20 | 浙江瑞丰机械设备有限公司 | Slag scrap-away device of electroplating oil-water separating device |
| CN106179772A (en) * | 2016-07-15 | 2016-12-07 | 河北润达环保科技有限公司 | A kind of highly difficult sewage multi-stage, efficient flotation device |
| CN107416935A (en) * | 2017-05-28 | 2017-12-01 | 韦爱龄 | Rotary flotation tank |
| CN107416934A (en) * | 2017-05-28 | 2017-12-01 | 韦爱龄 | Vibrating air floating pond |
| CN108821516A (en) * | 2018-07-26 | 2018-11-16 | 陈剑璋 | A kind of hospital gauze degreasing sewage-treatment plant |
| CN109160633A (en) * | 2018-09-20 | 2019-01-08 | 黄家仓 | A kind of trade effluent air floatation machine having processing pollution gas function |
| CN109160633B (en) * | 2018-09-20 | 2021-08-24 | 四川发展环境科学技术研究院有限公司 | Air flotation machine for industrial sewage with pollution gas treatment function |
| CN110563068A (en) * | 2019-11-05 | 2019-12-13 | 山东海普欧环保设备科技有限公司 | Aeration air-float machine |
| CN112358008A (en) * | 2021-01-12 | 2021-02-12 | 山东奥士德石油技术有限公司 | Polymer drives oil field sewage treatment plant |
| CN112358008B (en) * | 2021-01-12 | 2021-03-26 | 山东奥士德石油技术有限公司 | Polymer drives oil field sewage treatment plant |
| CN113877279A (en) * | 2021-09-27 | 2022-01-04 | 池州万维化工有限公司 | Kettle liquid filtering device for preparing 8-hydroxyquinoline |
| CN115353168A (en) * | 2022-10-20 | 2022-11-18 | 山东中加环境科技有限公司 | Petroleum sewage treatment device |
| CN117303489A (en) * | 2023-11-20 | 2023-12-29 | 三强环保集团有限公司 | Sequential air floating device |
| CN117303489B (en) * | 2023-11-20 | 2024-03-19 | 三强环保集团有限公司 | Sequential air floating device |
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Application publication date: 20100421 |