CN202201753U - High-efficiency energy-saving aerator - Google Patents
High-efficiency energy-saving aerator Download PDFInfo
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- CN202201753U CN202201753U CN2011201633605U CN201120163360U CN202201753U CN 202201753 U CN202201753 U CN 202201753U CN 2011201633605 U CN2011201633605 U CN 2011201633605U CN 201120163360 U CN201120163360 U CN 201120163360U CN 202201753 U CN202201753 U CN 202201753U
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- 238000005276 aerator Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 230000008602 contraction Effects 0.000 claims abstract 3
- 238000010008 shearing Methods 0.000 claims description 13
- 230000001154 acute effect Effects 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 15
- 239000001301 oxygen Substances 0.000 abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 abstract description 15
- 238000009792 diffusion process Methods 0.000 abstract description 3
- 238000006213 oxygenation reaction Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000007269 microbial metabolism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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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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- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
本实用新型主要公开了一种高效节能增氧机,包括电机、增压叶轮、剪切叶轮、螺旋叶轮、文丘里管;文丘里管由上而下依次包括入口收缩部分、圆筒形喉部和圆锥形扩散段;电机位于文丘里管的上端外侧,电机输出轴伸入文丘里管内部,由上而下依次安装有位于入口收缩部分上方的增压叶轮、位于圆锥形扩散段下方的剪切叶轮,以及剪切叶轮之下的螺旋叶轮;在文丘里管内增压叶轮的上方开设有进水口,在文丘里管圆筒形喉部处设置有引入外界空气或氧气的进气道。本实用新型是适用于好氧生物处理所需要的高效节能增氧机,增氧效率高、溶氧气泡小、停留时间长、节能效果好。
The utility model mainly discloses a high-efficiency and energy-saving aerator, including a motor, a booster impeller, a shear impeller, a spiral impeller, and a venturi tube; the venturi tube includes an inlet contraction part, a cylindrical throat, and a conical diffusion section from top to bottom; the motor is located outside the upper end of the venturi tube, and the motor output shaft extends into the interior of the venturi tube, and the booster impeller located above the inlet contraction part, the shear impeller located below the conical diffusion section, and the spiral impeller below the shear impeller are installed from top to bottom; a water inlet is provided above the booster impeller in the venturi tube, and an air inlet for introducing outside air or oxygen is provided at the cylindrical throat of the venturi tube. The utility model is a high-efficiency and energy-saving aerator suitable for aerobic biological treatment, with high oxygenation efficiency, small dissolved oxygen bubbles, long residence time, and good energy-saving effect.
Description
技术领域 technical field
本实用新型涉及用于废水生物处理及养殖过程中的增氧设备技术领域,特别与一种高效节能增氧机有关。 The utility model relates to the technical field of oxygen increasing equipment used in wastewater biological treatment and breeding process, in particular to a high-efficiency energy-saving oxygen increasing machine. the
背景技术 Background technique
水污染是当今世界面临的主要资源和环境问题之一,废水主要具有感官性污染,致毒性危害等特点,对环境水体的污染程度大。好氧微生物法以其经济、安全,而且处理的污染物阈值低、残留少、无二次污染等优点,成为各种可生化废水的主要处理方法。 Water pollution is one of the major resource and environmental problems facing the world today. Wastewater mainly has the characteristics of sensory pollution, toxicity and hazards, and has a large degree of pollution to environmental water bodies. The aerobic microbial method has become the main treatment method for various biochemical wastewater due to its advantages of economy, safety, low pollutant threshold value, less residue, and no secondary pollution. the
但在处理过程中,一些菌群的浓度很高,其代谢效率和氧气的消耗量非常大,目前的普通增氧设备的氧气交换速度很难维持水体中的溶解氧含量,曝气反应池中混合液主流的溶解氧浓度通常只保持在1-2mg/L的低水平,要满足生化过程所需的氧量,只好增加增氧机的台数,处理成本大幅度提高。 However, during the treatment process, the concentration of some bacterial flora is very high, and its metabolic efficiency and oxygen consumption are very large. The oxygen exchange rate of the current ordinary aeration equipment is difficult to maintain the dissolved oxygen content in the water body. In the aeration reaction tank The dissolved oxygen concentration in the mainstream of the mixed liquid is usually kept at a low level of 1-2mg/L. To meet the oxygen required by the biochemical process, the number of aerators has to be increased, which greatly increases the processing cost. the
为了解决上述问题,本发明人设计出高效节能增氧机,本案由此产生。 In order to solve the above problems, the inventor has designed a high-efficiency energy-saving aerator, and this case results from this. the
实用新型内容 Utility model content
本实用新型的主要目的是提供一种适用于好氧生物处理所需要的高效节能增氧机,具有增氧效率高、溶氧气泡小、停留时间长、节能效果好的特点。 The main purpose of the utility model is to provide a high-efficiency energy-saving aerator suitable for aerobic biological treatment, which has the characteristics of high oxygenation efficiency, small dissolved oxygen bubbles, long residence time and good energy-saving effect. the
为了达到上述目的,本实用新型通过以下技术方案来实现: In order to achieve the above object, the utility model is realized through the following technical solutions:
高效节能增氧机,包括电机、增压叶轮、剪切叶轮、螺旋叶轮、文丘里管;文丘里管由上而下依次包括入口收缩部分、圆筒形喉部和圆锥形扩散段;电机位于文丘里管的上端外侧,电机输出轴伸入文丘里管内部,由上而下依次安装有位于入口收缩部分上方的增压叶轮、位于圆锥形扩散段下方的剪切叶轮,以及剪切叶轮之下的螺旋叶轮;在文丘里管内增压叶轮的上方开设有进水口,在文丘里管圆筒形喉部处设置有引入外界空气的进气道。 High-efficiency energy-saving aerator, including motor, booster impeller, shear impeller, spiral impeller, Venturi tube; Venturi tube includes inlet constriction, cylindrical throat and conical diffusion section from top to bottom; the motor is located at On the outer side of the upper end of the Venturi tube, the output shaft of the motor extends into the inside of the Venturi tube. The booster impeller located above the inlet constriction, the shear impeller located below the conical diffuser section, and the shear impeller are installed in sequence from top to bottom. The lower spiral impeller; a water inlet is opened above the booster impeller in the Venturi tube, and an air inlet for introducing external air is provided at the cylindrical throat of the Venturi tube.
所述的进水口内铺设有进水格网。 A water inlet grid is laid inside the water inlet. the
所述的剪切叶轮和螺旋叶轮之间设置中间格网。 An intermediate grid is set between the shearing impeller and the spiral impeller. the
所述的文丘里管的外侧、进水口上方设置有进水导流板。 A water inlet deflector is arranged on the outside of the Venturi tube and above the water inlet. the
所述的进水导流板的下底面与文丘里管的外侧面形成锐角夹角,形成导流角度。 The lower bottom surface of the water inlet deflector forms an acute angle with the outer surface of the Venturi tube to form a diversion angle. the
所述的进气道为剪切叶轮的切向方向。 The air inlet is in the tangential direction of the shearing impeller. the
所述的进气道外接进气管,引入外界空气。 The air intake duct is externally connected to an air intake pipe to introduce outside air. the
所述的螺旋叶轮下方设置有出水导流板。 A water outlet deflector is arranged below the spiral impeller. the
其技术方案是这样实现的:该增氧机悬浮于水体上,电机带动增压叶轮、剪切叶轮及螺旋叶轮工作;被处理液体由进水口经过格网的过滤后进入腔体内,被增压叶轮搅碎,并经增压叶轮的前端与墙体之间的间隙被快速推下,进入文丘里管;随着液体进入到文丘里管喉部,管内的压力减小,空气/氧气由外界通过进气管被大量吸入,经过进气道成切向方向进入文丘里管,气水混合,经剪切叶轮作用产生大量超微气泡,此状态下的液体流经格网,经整流后,经螺旋叶轮被射向更深的水体中;因为这些大量的超微气泡的浮力不足以克服水体的表面张力,所以它们可以在水体中停留很长时间;一些直径较大的气泡在上升过程中,再次被吸入进水口进入增氧机,被重复处理,延长其在水中的停留时间。 The technical solution is realized as follows: the aerator is suspended on the water body, and the motor drives the booster impeller, the shearing impeller and the spiral impeller; The impeller is crushed and quickly pushed down through the gap between the front end of the booster impeller and the wall and enters the Venturi tube; as the liquid enters the throat of the Venturi tube, the pressure in the tube decreases, and the air/oxygen is released from the outside It is sucked in a large amount through the inlet pipe, enters the Venturi tube in a tangential direction through the inlet pipe, and the gas and water are mixed, and a large number of ultra-fine bubbles are generated by the shearing impeller. The liquid in this state flows through the grid, and after rectification, it passes through the spiral The impeller is shot into a deeper water body; because the buoyancy of these large numbers of ultramicro-bubbles is not enough to overcome the surface tension of the water body, they can stay in the water body for a long time; The suction inlet enters the aerator and is repeatedly treated to prolong its residence time in the water. the
采用上述方案后,本实用新型具有诸多有益效果: After adopting the above scheme, the utility model has many beneficial effects:
1、本实用新型的气源可以是纯氧,也可以是空气,通用性强;2、本实用新型可以在低压下能有充足的进气量;3、溶氧气泡小、分散均匀,在水中停留时间较长,显著提高氧的转移速率;4、本实用新型增氧效率高,可满足各种废水好氧生物处理的需氧量,加快微生物代谢,节约水力停留时间,提高废水的处理效率的同时,节约处理成本;4、本实用新型耗能低、性能稳定、无堵塞障碍、使用方便;5、应用领域广,各种废水好氧生物处理领域、养殖业、湖泊及河道治理。 1. The gas source of the utility model can be pure oxygen or air, which has strong versatility; 2. The utility model can have sufficient air intake under low pressure; 3. The dissolved oxygen bubbles are small and evenly dispersed. The residence time in water is longer, which significantly improves the oxygen transfer rate; 4. The utility model has high oxygenation efficiency, which can meet the oxygen demand of various wastewater aerobic biological treatment, accelerate microbial metabolism, save hydraulic residence time, and improve wastewater treatment. 4. The utility model has low energy consumption, stable performance, no blockage, and is easy to use; 5. It has a wide range of applications, including aerobic biological treatment of various wastewater, aquaculture, lake and river treatment.
附图说明 Description of drawings
图1为本实用新型较佳实施例的结构示意图; Fig. 1 is the structural representation of preferred embodiment of the utility model;
具体实施方式 Detailed ways
结合附图,对本实用新型较佳实施例做进一步详细说明。 In conjunction with the accompanying drawings, the preferred embodiments of the utility model are further described in detail. the
高效节能增氧机,主要涉及的部件包括电机1、进水导流板2、进水口3、进水格网4、增压叶轮5、文丘里管6、剪切叶轮7、中间格网8、螺旋叶轮9、出水导流板10、进气道11、电机输出轴12、进气管13。
High-efficiency energy-saving aerator, the main components involved include motor 1,
文丘里管6利用异形管使流经该管流体的速度发生变化从而产生差压的流量检测元件,轴向截面由入口收缩部分61、圆筒形喉部62和圆锥形扩散段63组成。在入口收缩部分61的上方侧壁上设置有进水口3,进水口3内铺设有进水格网4,圆锥形扩散段63的底部开口就是出水口。
The Venturi
电机1位于文丘里管6的上端外侧,电机输出轴12伸入文丘里管6内部。在电机输出轴12由上而下依次安装了增压叶轮5、剪切叶轮7、螺旋叶轮9。增压叶轮5位于进水口3的下方,同时是在入口收缩部分61的上方。水从进水口3进入腔体内,流入下方的增压叶轮5搅碎。剪切叶轮7位于圆锥形扩散段63的下方,而螺旋叶轮9又位于剪切叶轮7的下方,两者中间夹有中间格网8。
The motor 1 is located outside the upper end of the Venturi
文丘里管6的圆筒形喉部62,腔壁上安装了进气道11,进气道11的安装方向为剪切叶轮7的切向方向。进气道11外部连接进气管13,引入外部空气或者氧气。
The
为了使气体在水中停留时间更长或更深入,在文丘里管6的外侧,同时是进水口3上方设置有进水导流板2,而在螺旋叶轮9的下方设置有出水导流板10。进水导流板2的下底面与文丘里管6的外侧面形成一个锐角a,排出的气体随着进水导流板2下底面被逐渐导入进水口3中,再次利用。出水导流板10是周边高,中间出口低,使得内部的气水混合液能集中流向中间出口,借助螺旋叶轮9被射向更深的水体中。
In order to make the gas stay longer or deeper in the water, a
本实用新型的工作原理如下: The working principle of the utility model is as follows:
本实用新型使用时悬浮于水体上,电机1带动增压叶轮5、剪切叶轮7及螺旋叶轮9工作。液体由进水口3经过进水格网4的过滤后进入腔体内,被增压叶轮5搅碎,并经增压叶轮5的前端与墙体之间的间隙被快速推下,进入文丘里管6;随着液体进入到文丘里管6的圆筒形喉部62,文丘里管6内的压力减小,空气/氧气由外界通过进气管13被大量吸入,经过进气道11成切向方向进入文丘里管6,气水混合,并进入剪切叶轮7,产生大量的超微小气泡并存在于液体中,此状态下的液体流经中间格网8,经整流后,经螺旋叶轮9被射向更深的水体中。
When the utility model is in use, it is suspended on the water body, and the motor 1 drives the booster impeller 5, the shearing impeller 7 and the
因为这些大量的超微小气泡的浮力不足以克服水体的表面张力,所以它们可以在水体中停留很长时间。一些直径较大的气泡在上升过程中,被进水导流板2阻挡,随水流通过进水口3再次进入增氧机,被重复利用,延长其在水中的停留时间。
Because the buoyancy of these large numbers of ultrafine bubbles is not enough to overcome the surface tension of the water body, they can stay in the water body for a long time. Some air bubbles with larger diameters are blocked by the
上述实施例仅用于解释说明本实用新型的实用新型构思,而非对本实用新型权利保护的限定,凡利用此构思对本实用新型进行非实质性的改动,均应落入本实用新型的保护范围。 The above-mentioned embodiments are only used to explain the utility model concept of the present utility model, but not to limit the protection of the utility model rights. Any non-substantial changes made to the utility model by using this concept should fall within the protection scope of the utility model . the
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104585124A (en) * | 2015-01-26 | 2015-05-06 | 上海理工大学 | Aquaculture oxygenating system |
CN105923799A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body micro-nano oxygenating system |
CN105923745A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body oxygenating system |
CN107847883A (en) * | 2015-07-09 | 2018-03-27 | 艾里尔科技创新有限公司 | Method and apparatus for performing reaction |
CN109704447A (en) * | 2019-03-05 | 2019-05-03 | 苏州方舟环保科技有限公司 | A kind of river water acid-base adjustment device |
CN111387131A (en) * | 2020-04-08 | 2020-07-10 | 中国水产科学研究院渔业机械仪器研究所 | An emergency aeration and oxygenation system |
CN112723454A (en) * | 2020-12-04 | 2021-04-30 | 周美蓉 | Efficient jet air flotation machine for sewage treatment |
CN116119846A (en) * | 2023-04-17 | 2023-05-16 | 山东国宏生物科技有限公司 | Cyclone aeration device for soybean protein wastewater treatment aerobic section |
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2011
- 2011-05-20 CN CN2011201633605U patent/CN202201753U/en not_active Expired - Fee Related
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104585124A (en) * | 2015-01-26 | 2015-05-06 | 上海理工大学 | Aquaculture oxygenating system |
CN107847883A (en) * | 2015-07-09 | 2018-03-27 | 艾里尔科技创新有限公司 | Method and apparatus for performing reaction |
CN105923799A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body micro-nano oxygenating system |
CN105923745A (en) * | 2016-06-28 | 2016-09-07 | 湖南农业大学 | Water body oxygenating system |
CN105923745B (en) * | 2016-06-28 | 2019-01-15 | 湖南农业大学 | Water oxygenation system |
CN105923799B (en) * | 2016-06-28 | 2019-03-29 | 湖南农业大学 | The micro-nano aeration system of water body |
CN109704447A (en) * | 2019-03-05 | 2019-05-03 | 苏州方舟环保科技有限公司 | A kind of river water acid-base adjustment device |
CN111387131A (en) * | 2020-04-08 | 2020-07-10 | 中国水产科学研究院渔业机械仪器研究所 | An emergency aeration and oxygenation system |
CN111387131B (en) * | 2020-04-08 | 2021-09-17 | 中国水产科学研究院渔业机械仪器研究所 | Emergency aeration oxygenation system |
CN112723454A (en) * | 2020-12-04 | 2021-04-30 | 周美蓉 | Efficient jet air flotation machine for sewage treatment |
CN112723454B (en) * | 2020-12-04 | 2022-09-06 | 成都市蜀科科技有限责任公司 | Efficient jet air flotation machine for sewage treatment |
CN116119846A (en) * | 2023-04-17 | 2023-05-16 | 山东国宏生物科技有限公司 | Cyclone aeration device for soybean protein wastewater treatment aerobic section |
CN116119846B (en) * | 2023-04-17 | 2023-10-27 | 山东国宏生物科技有限公司 | Cyclone aeration device for soybean protein wastewater treatment aerobic section |
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