CN201280444Y - High-efficiency whirlwind defoaming apparatus - Google Patents
High-efficiency whirlwind defoaming apparatus Download PDFInfo
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- CN201280444Y CN201280444Y CNU2008201606907U CN200820160690U CN201280444Y CN 201280444 Y CN201280444 Y CN 201280444Y CN U2008201606907 U CNU2008201606907 U CN U2008201606907U CN 200820160690 U CN200820160690 U CN 200820160690U CN 201280444 Y CN201280444 Y CN 201280444Y
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Abstract
The utility model discloses an efficient whirlwind defoaming device which mainly comprises a foam absorption pipeline, a foam entering pipeline, a whirlwind defoaming separation cylinder and a blower. The blower is utilized to adsorb wind, so that the whirlwind defoaming separation cylinder generates negative pressure and the foam absorption pipeline connected with the defoaming separation cylinder collects bubbles in a water tank; the bubbles absorbed into the whirlwind defoaming separation cylinder through the foam entering pipeline rotate in high speed along the outer cylinder body in the whirlwind defoaming separation cylinder and burst due to high-speed and vehement collision with the casing wall; the mixture of water and mud generated after the burst of the bubbles can reflow into the water tank along the casing wall of the outer cylinder body under the effects of gravity and rotational flow centrifugal force; and the air is sucked out of the whirlwind defoaming separation cylinder through the blower. The utility model can realize dual effects of bubble burst and water-air separation, reduce the burst time of the bubbles to the largest extent, effectively improve process effect, and eliminate the need of adding foam killer, besides, the entire processing procedure is controlled through a man-operated valve, and automatic control can also be achieved, thereby realizing simple operation.
Description
Technical field:
The utility model relates to a kind of device of efficient cyclone froth breaking.Be applicable to that mainly the aeration tank produces a large amount of foamy eliminations in the sewage disposal operational process, but widespread use in pharmaceutical wastewater, dyeing waste water and wastewater from chemical industry, the elimination of pond inner foam in the processes such as also applicable papermaking, fermentation.
Background technology:
In sewage treatment process, normal because sneaking into of air is easy to generate bubble.Especially trade effluents such as dyeing waste water, paper waste, wastewater from chemical industry the aeration tank foam often occurs and pile up, even the phenomenon in foam envelope pond occurs, not only influence the landscape effect of pond body, and influence the transmission of oxygen, unfavorable to microbial growth, even influence the quality of sewage disposal.
Handle the too much phenomenon of aeration tank foam at present, generally adopt to add defoamer and the high-pressure spraying water pipe is installed.It is very high to add the defoamer cost, defoamer itself is a kind of pollutent, a large amount of defoamers enter treatment system, increased the load of system, the water quality variation that may cause water outlet, COD raises, and process very short time foam can be piled up again again, cause adding the increase of froth breaking dosage, also increased processing cost.
The high-pressure spraying network of rivers is installed prevents that foam is excessive, but the capital cost height is also very high with tap water spray working cost.And HP shower network operation rear perimeter edge environment is bad, and water smoke fills the air, situations such as aisle sewage crossing current, and maintenance is also inconvenient.
In addition as treatment processs such as deaeration towers, effect is not clearly yet in actual motion.
The utility model content:
Main purpose of the present utility model provides a kind of method and apparatus of efficient cyclone froth breaking, overcomes the deficiency of aforesaid method, the bubble-related issues in effective cancellation pond, and not only economical rationality, and also treatment effect is obvious.
Efficient cyclone defoaming device described in the utility model comprises blower fan, whirlwind froth breaking separator cartridge, advances to steep pipeline and inhales the bubble pipeline that the bubble output hole of described whirlwind froth breaking separator cartridge connects blower fan; Advance to steep pipeline and be communicated with whirlwind froth breaking separator cartridge; Inhale the side of bubble pipelining in the pond, its suction port extends near the liquid level of pond, and its relief outlet connects into bubble pipeline.
Above-mentioned whirlwind froth breaking separator cartridge comprises outer cylinder body, outer lower cone, bubble output hole, inner barrel, lower cone and liquid guide flow pipe, the outer cylinder body upper end closed, enter to steep pipeline and outer cylinder body junction and be positioned at outer cylinder body top and tangent with the outer cylinder body periphery, outer lower cone is located at the outer cylinder body bottom, the liquid guide flow pipe is located at outer lower cone outlet at bottom place, the inner barrel edge is enclosed within outer cylinder body inside, inner barrel is respectively equipped with bubble output hole and lower cone in two ends up and down, wherein bubble output hole stretches out outer cylinder body and is connected with blower fan, and the outlet of lower cone then is positioned at outer cylinder body inside.
Having crack in a side of inhaling the bubble pipeline is used to collect bubble and carries out preliminary negative pressure bubble crushing; And advance to steep pipeline and the froth breaking tube tangent; The froth breaking tube is made up of urceolus and inner core edge cover, and urceolus is used for bubble crushing and separate bubble liquid, and inner core is used for the blower fan intake-gas and produces negative pressure.
The method of efficient cyclone froth breaking is: blower fan is to froth breaking tube intake-gas, make the froth breaking tube produce negative pressure, the suction bubble pipeline that is connected with the froth breaking tube, be installed in a side in pond, collect the bubble on the pond and carry out the broken bubble of preliminary negative pressure, bubble and bubble liquid are by being inhaled into the froth breaking pipeline fast with the tangent pipeline that advances to steep of whirlwind froth breaking separator cartridge, urceolus high speed rotating at whirlwind froth breaking separator cartridge, the fragmentation with the quick fierce collision of shell wall, the bubble liquid that produces behind the bubble breaking is under the effect of gravity, be back in the pond along shell wall, and gas is discharged from along inner core owing to the negative pressure of inner core generation.
It is simple, feasible to the utlity model has froth breaking, and apparatus structure is simple.Simple installation, running cost is lower, the defoaming effect ideal, and can not cause characteristics such as secondary environmental pollution.
Compare with existing technology, the advantage that the utility model had is:
(1) this is a kind of physical defoaming method, can guarantee that the bubble liquid behind the froth breaking can not increase the load of sewage disposal, can not influence the water quality of water outlet.
(2) this device is simple, effective minimizing floor space easy for installation and investment goods, and capital cost is low, and running cost is low.
(3) environment of this method froth breaking is fine, can not influence the view in froth breaking pond, and the mud mixture that produces behind the froth breaking is back in the pond, and gas effluxes, and can not cause secondary environmental pollution.
(4) simple to operation, can realize automatization control.
Description of drawings:
Fig. 1 is the elevation layout drawing of efficient cyclone defoaming device.
Fig. 2 is the front view of whirlwind froth breaking separator cartridge.
Fig. 3 is the sectional view of whirlwind froth breaking separator cartridge.
Fig. 4 is for inhaling the front view of bubble pipeline.
Fig. 5 is for inhaling the sectional view of bubble pipeline.
Embodiment:
As shown in Figure 1, a kind of device of efficient cyclone froth breaking by blower fan 1, whirlwind froth breaking separator cartridge 2, advance to steep pipeline 3, inhale bubble pipeline 4 and form.
As shown in Figure 1, blower fan 1 is to whirlwind froth breaking separator cartridge 3 suction airs, make whirlwind froth breaking separator cartridge 2 produce negative pressure, the suction bubble pipeline 4 that is connected with whirlwind froth breaking separator cartridge 2 will be collected the bubble in the pond and carry out the broken bubble of preliminary negative pressure, bubble enters whirlwind froth breaking separator cartridge 2 fast by the whirlwind froth breaking separator cartridge 2 outer cylinder bodies 5 tangent pipelines 3 that advance to steep, at outer cylinder body 5 high speed rotating, bump then fragmentation with the quick fierceness of shell wall, the bubble liquid that produces behind the bubble breaking is back in the pond by the hypocentrum 9 that is connected with outer cylinder body 5, and gas is discharged by blower fan 1 by inner barrel 8, can realize the double effects of gas-water separation and foam fragmentation.
As shown in Figure 2, whirlwind froth breaking separator cartridge is made up of outer cylinder body 5, outer lower cone 6, bubble output hole 7, inner barrel 8, lower cone 9, liquid guide flow pipe 10.Outer cylinder body 5 upper end closeds, advance to steep pipeline 3 and be positioned at outer cylinder body 5 tops and tangent with outer cylinder body 5 peripheries with outer cylinder body 5 junctions, outer lower cone 6 is located at outer cylinder body 5 bottoms, liquid guide flow pipe 10 is located at outer lower cone 6 outlet at bottom places, inner barrel 8 edges are enclosed within outer cylinder body 5 inside, inner barrel is respectively equipped with bubble output hole 7 and lower cone 9 in two ends about in the of 8, and wherein bubble output hole 7 stretches out outer cylinder body 5 and is connected with blower fan 1, and the outlet of lower cone 9 then is positioned at outer cylinder body 5 inside.During work, the air of inner barrel 8 is constantly extracted by blower fan 1 and forms negative pressure, makes bubble by entering outer cylinder body fast with the tangent pipeline 3 that advances to steep of outer cylinder body.
The outer cylinder body that advances to steep pipeline and whirlwind froth breaking separator cartridge as shown in Figure 3 is tangent, thereby foam can be rotated along outer cylinder body under negative pressure.
Inhale the bubble pipeline as shown in Figure 4 and Figure 5, have a lot of cracks, be used for collecting the foam in pond and carry out the broken bubble of preliminary negative pressure in a side of pipeline.
Claims (3)
1, a kind of efficient cyclone defoaming device is characterized in that: comprise blower fan (1), whirlwind froth breaking separator cartridge (2), advance to steep pipeline (3) and inhale bubble pipeline (4), the bubble output hole (7) of described whirlwind froth breaking separator cartridge (2) connects blower fan (1); Advance to steep pipeline (3) and be communicated with whirlwind froth breaking separator cartridge (2); Inhale and steep the side that pipeline (4) is installed in the pond, its suction port extends near the liquid level of pond, and its relief outlet connects into bubble pipeline (3).
2, efficient cyclone defoaming device according to claim 1, it is characterized in that: described whirlwind froth breaking separator cartridge comprises outer cylinder body (5), outer lower cone (6), bubble output hole (7), inner barrel (8), lower cone (9) and liquid guide flow pipe (10), outer cylinder body (5) upper end closed, advance to steep pipeline (3) and be positioned at outer cylinder body (5) top and tangent with outer cylinder body (5) periphery with outer cylinder body (5) junction, outer lower cone (6) is located at outer cylinder body (5) bottom, liquid guide flow pipe (10) is located at outer lower cone (6) outlet at bottom place, inner barrel (8) edge is enclosed within outer cylinder body (5) inside, inner barrel (8) two ends up and down is respectively equipped with bubble output hole (7) and lower cone (9), wherein bubble output hole (7) stretches out outer cylinder body (5) and is connected with blower fan (1), and the outlet of lower cone (9) then is positioned at outer cylinder body (5) inside.
3, efficient cyclone defoaming device according to claim 1 and 2 is characterized in that: have many cracks of collecting foam in the ponds and carrying out the broken bubble of preliminary negative pressure in a side of inhaling bubble pipeline (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201606907U CN201280444Y (en) | 2008-10-16 | 2008-10-16 | High-efficiency whirlwind defoaming apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201606907U CN201280444Y (en) | 2008-10-16 | 2008-10-16 | High-efficiency whirlwind defoaming apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201280444Y true CN201280444Y (en) | 2009-07-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201606907U Expired - Fee Related CN201280444Y (en) | 2008-10-16 | 2008-10-16 | High-efficiency whirlwind defoaming apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201280444Y (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874207A (en) * | 2015-06-02 | 2015-09-02 | 中冶南方工程技术有限公司 | Jet-stream defoaming device |
| CN105712458A (en) * | 2014-12-05 | 2016-06-29 | 中国石油化工股份有限公司 | Oil refining alkaline residue acidification reactor and acidification method thereof |
| CN105923756A (en) * | 2016-07-10 | 2016-09-07 | 赖柱彭 | Aeration tank system |
| CN106237660A (en) * | 2016-08-26 | 2016-12-21 | 苏州市展进机电设备有限公司 | A kind of negative pressure Defoaming machine |
| CN107428562A (en) * | 2015-03-23 | 2017-12-01 | 荷兰联合利华有限公司 | For reclaiming clean water and the apparatus and method of surfactant concentrate from buck |
| CN108315554A (en) * | 2018-04-06 | 2018-07-24 | 辽宁天利金业有限责任公司 | A kind of biological oxidation gold extraction system circulation whirlwind defoaming device |
| CN109718577A (en) * | 2018-12-25 | 2019-05-07 | 浙江国涛滤料科技有限公司 | High-efficiency diversion filter |
| CN110938535A (en) * | 2019-11-25 | 2020-03-31 | 郑州职业技术学院 | Biocontrol actinomycete fermentation tank |
| CN116870640A (en) * | 2023-09-06 | 2023-10-13 | 浙江百能科技有限公司 | Built-in defoaming device and method applied to separator |
| CN117299724A (en) * | 2023-11-29 | 2023-12-29 | 龙焱能源科技（杭州）有限公司 | Glass cleaning and bubble removing device |
| CN117466372A (en) * | 2023-12-28 | 2024-01-30 | 山西亚鑫新能科技有限公司 | Sulfur foam and desulfurization waste liquid separation device and method |
-
2008
- 2008-10-16 CN CNU2008201606907U patent/CN201280444Y/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105712458A (en) * | 2014-12-05 | 2016-06-29 | 中国石油化工股份有限公司 | Oil refining alkaline residue acidification reactor and acidification method thereof |
| CN105712458B (en) * | 2014-12-05 | 2019-03-19 | 中国石油化工股份有限公司 | A kind of refinery basic sewage acidification reaction device and its acidization tool |
| CN107428562A (en) * | 2015-03-23 | 2017-12-01 | 荷兰联合利华有限公司 | For reclaiming clean water and the apparatus and method of surfactant concentrate from buck |
| CN104874207A (en) * | 2015-06-02 | 2015-09-02 | 中冶南方工程技术有限公司 | Jet-stream defoaming device |
| CN105923756A (en) * | 2016-07-10 | 2016-09-07 | 赖柱彭 | Aeration tank system |
| CN105923756B (en) * | 2016-07-10 | 2019-01-18 | 赖柱彭 | A kind of aeration cell system |
| CN106237660A (en) * | 2016-08-26 | 2016-12-21 | 苏州市展进机电设备有限公司 | A kind of negative pressure Defoaming machine |
| CN108315554A (en) * | 2018-04-06 | 2018-07-24 | 辽宁天利金业有限责任公司 | A kind of biological oxidation gold extraction system circulation whirlwind defoaming device |
| CN109718577A (en) * | 2018-12-25 | 2019-05-07 | 浙江国涛滤料科技有限公司 | High-efficiency diversion filter |
| CN109718577B (en) * | 2018-12-25 | 2021-02-05 | 浙江国涛滤料科技有限公司 | High-efficiency flow guide filter |
| CN110938535A (en) * | 2019-11-25 | 2020-03-31 | 郑州职业技术学院 | Biocontrol actinomycete fermentation tank |
| CN110938535B (en) * | 2019-11-25 | 2023-03-21 | 郑州职业技术学院 | Biocontrol actinomycete fermentation tank |
| CN116870640A (en) * | 2023-09-06 | 2023-10-13 | 浙江百能科技有限公司 | Built-in defoaming device and method applied to separator |
| CN117299724A (en) * | 2023-11-29 | 2023-12-29 | 龙焱能源科技（杭州）有限公司 | Glass cleaning and bubble removing device |
| CN117466372A (en) * | 2023-12-28 | 2024-01-30 | 山西亚鑫新能科技有限公司 | Sulfur foam and desulfurization waste liquid separation device and method |
| CN117466372B (en) * | 2023-12-28 | 2024-03-01 | 山西亚鑫新能科技有限公司 | Sulfur foam and desulfurization waste liquid separation device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090729 Termination date: 20091116 |