CN201809227U - Multifunctional high-efficiency aerator - Google Patents
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- CN201809227U CN201809227U CN2010202676209U CN201020267620U CN201809227U CN 201809227 U CN201809227 U CN 201809227U CN 2010202676209 U CN2010202676209 U CN 2010202676209U CN 201020267620 U CN201020267620 U CN 201020267620U CN 201809227 U CN201809227 U CN 201809227U
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- 238000005276 aerator Methods 0.000 title claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 57
- 238000009792 diffusion process Methods 0.000 claims abstract description 34
- 238000003756 stirring Methods 0.000 claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 230000001939 inductive effect Effects 0.000 claims description 3
- 238000005273 aeration Methods 0.000 abstract description 44
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 23
- 239000001301 oxygen Substances 0.000 abstract description 23
- 229910052760 oxygen Inorganic materials 0.000 abstract description 23
- 239000007788 liquid Substances 0.000 abstract description 14
- 230000000694 effects Effects 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 13
- 230000008569 process Effects 0.000 abstract description 11
- 230000001965 increasing effect Effects 0.000 abstract description 10
- 239000007789 gas Substances 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000006213 oxygenation reaction Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000006872 improvement Effects 0.000 abstract description 3
- 239000002002 slurry Substances 0.000 abstract description 2
- 239000003570 air Substances 0.000 description 47
- 239000006260 foam Substances 0.000 description 12
- 239000010802 sludge Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000010354 integration Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000003434 inspiratory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 230000009466 transformation Effects 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
本实用新型是对自吸式增氧曝气装置的改进,其特征是吸气叶轮距水面深度为0.3m至水深1/3之间,吸气、扩散叶轮下方同轴有一层或多层搅拌叶轮。较现有技术,曝气、搅拌一体化,可以适用于各种水深环境,不仅降低了曝气能耗,而且提高了服务面积和氧转移率,充氧效果好,还同时能使气、固、液三相充分混合,还可以方便实现污水处理工艺的好氧、缺氧和厌氧条件自由切换,突破了现有技术自吸式增氧曝气,功能单一、运行模式单一的不足。增加消泡浆,不仅可以消除曝气池表面气泡,而且还增加了充氧。本实用新型自吸式增氧曝气装置,具有曝气动力消耗小,氧传质速率高,充氧效果好,同时兼具搅拌功能,运行工艺灵活多变。
The utility model is an improvement to the self-priming oxygen-increasing aeration device, which is characterized in that the depth of the suction impeller from the water surface is between 0.3m and 1/3 of the water depth, and there is one or more layers of stirring coaxially under the suction and diffusion impellers. impeller. Compared with the existing technology, aeration and stirring are integrated, and it can be applied to various water depth environments. It not only reduces the energy consumption of aeration, but also improves the service area and oxygen transfer rate. The oxygenation effect is good, and it can also make gas and solid The three-phase liquid and liquid are fully mixed, and it is also convenient to realize the free switching of aerobic, anoxic and anaerobic conditions in the sewage treatment process, breaking through the shortcomings of the existing technology of self-priming oxygen-increasing aeration, single function, and single operation mode. Increasing the defoaming slurry can not only eliminate the air bubbles on the surface of the aeration tank, but also increase the oxygenation. The self-priming oxygen-increasing aeration device of the utility model has the advantages of low aeration power consumption, high oxygen mass transfer rate, good oxygenation effect, simultaneous stirring function, and flexible and changeable operation process.
Description
技术领域technical field
实用新型是对自吸式增氧曝气装置的改进,尤其涉及一种消耗功率小,氧转移率高,曝气服务面积大,集曝气-搅拌于一体的多功能高效曝气器。The utility model is an improvement to the self-priming oxygen-increasing aeration device, and particularly relates to a multi-functional high-efficiency aerator with low power consumption, high oxygen transfer rate, large aeration service area, and integration of aeration and agitation.
背景技术Background technique
人们为提高叶轮式增氧机向水中溶氧效率,开发了水下叶轮自吸式增氧曝气装置。此结构曝气装置,水下吸气、扩散叶轮设置于中空或套筒转轴未端,通过叶轮的高速旋转在转轴附近区域产生相对低压区,使水面空气通过空心轴或套筒吸入,并由水中高速旋转叶轮将吸入空气打散、扩散到周围水体,实现曝气功能。因水下温度相对较低、负压吸入空气,以及水下气泡边上升边溶解,使得吸入空气在较大立体中溶解,溶氧增大,因而提高了溶氧动力效率。例如:In order to improve the oxygen-dissolving efficiency of the impeller-type aerator in water, people have developed an underwater impeller self-priming oxygen-increasing aeration device. In this structure aeration device, the underwater suction and diffusion impellers are set at the end of the hollow or sleeve shaft, and the high-speed rotation of the impeller creates a relatively low-pressure area near the shaft, so that the air on the water surface is sucked in through the hollow shaft or sleeve, and is released by the impeller. The high-speed rotating impeller in the water breaks up the inhaled air and diffuses it to the surrounding water body to realize the aeration function. Because the underwater temperature is relatively low, the negative pressure inhales air, and the underwater bubbles dissolve while rising, the inhaled air dissolves in a larger volume, and the dissolved oxygen increases, thus improving the kinetic efficiency of dissolved oxygen. For example:
中国专利CN2076985自吸式增氧机,在套筒转轴下方设置周边有导流筒的涡轮式浆叶及散气网罩,由涡轮浆叶旋转通过定向导流筒将吸入空气向下方扩散。Chinese patent CN2076985 self-priming aerator, under the shaft of the sleeve, a turbine-type paddle with a guide tube around it and an air-diffusing net cover are arranged, and the turbine blade rotates and diffuses the inhaled air downward through the directional guide tube.
中国专利CN1106363液体曝气装置,在导气转轴下端设置螺旋桨。In the Chinese patent CN1106363 liquid aeration device, a propeller is arranged at the lower end of the air guiding shaft.
中国专利CN2093174具有涡轮喷射装置的水池曝气机,由液面上的吸气涡轮及水下套筒轴未端散气叶轮组成,通过液面上吸气涡轮增加向下水中空气量。Chinese patent CN2093174 has a pool aerator with a turbine injection device, which is composed of a suction turbine on the liquid surface and an air diffuser impeller at the end of the underwater sleeve shaft, and the air volume in the water is increased through the suction turbine on the liquid surface.
中国专利CN2171598电动曝气器,改变了吸气、扩散叶轮,采用具有微细坑纹叶片多片叠起,在叶轮径向形成一排排小孔,吸入空气通过小孔排出形成小气泡。The Chinese patent CN2171598 electric aerator has changed the suction and diffusion impellers, and adopts multiple stacked blades with fine pits to form rows of small holes in the radial direction of the impeller, and the inhaled air is discharged through the small holes to form small bubbles.
上述水下旋转叶轮自吸式增氧曝氧装置,不论叶型如何,其一个共同特点:吸气、扩散叶轮均设置于转轴末端,并且只有一个叶轮。由此,只有吸气叶轮一次对吸入空气的切割,气泡打散性欠佳,气泡相对较大,溶氧效率不会太高,因气泡扩散性差,曝气服务面积小;其次,对于深池曝气必然要加大叶轮深度,吸气叶轮深度大,因吸气需克服的水压力与水深呈正比,吸气所需动力就大,从而增加了曝气动力消耗;吸气、扩散叶轮设置过浅,不仅底部溶氧效果差,而且会影响整体溶氧量及溶氧均匀度,不利于水处理工艺;再就是,单一吸气叶轮均只有吸气、散气作用,对水体搅拌能力有限,不易使污泥、空气、水三相充分混合,还必须另行配置搅拌混合装置。虽然通过改进叶型,例如采用涡轮式浆叶,其吸气量仍难以提高,造成溶氧效率不够高。The above-mentioned underwater rotary impeller self-priming aeration device has one common feature regardless of the blade type: the suction and diffusion impellers are all arranged at the end of the rotating shaft, and there is only one impeller. Therefore, only the suction impeller cuts the inhaled air once, the air bubbles are not well dispersed, the air bubbles are relatively large, the dissolved oxygen efficiency will not be too high, and the aeration service area is small due to the poor air bubble diffusion; secondly, for deep pools Aeration must increase the depth of the impeller, and the depth of the suction impeller is large. Because the water pressure to be overcome by suction is proportional to the water depth, the power required for suction is large, thereby increasing the power consumption of aeration; the settings of suction and diffusion impellers If it is too shallow, not only the effect of dissolved oxygen at the bottom is poor, but also it will affect the overall dissolved oxygen amount and uniformity of dissolved oxygen, which is not conducive to the water treatment process; moreover, the single suction impeller only has the function of suction and diffusion, and its ability to stir the water body is limited. , It is not easy to fully mix the three phases of sludge, air and water, and a stirring and mixing device must be configured separately. Although by improving the blade shape, such as the use of turbine blades, it is still difficult to increase the air intake, resulting in insufficient efficiency of dissolved oxygen.
此外,现有水下旋转叶轮自吸式增氧曝气装置,以及其他曝气装置,均唯一仅具有曝气功能,所以只能用于好氧工艺,应用范围、功能相对狭窄,不能满足某些水处理工艺要求。In addition, the existing underwater rotating impeller self-priming oxygen-increasing aeration device and other aeration devices only have aeration function, so they can only be used for aerobic process, the application range and function are relatively narrow, and cannot meet certain requirements. Some water treatment process requirements.
上述不足仍有值得改进的地方。The above-mentioned deficiencies still have room for improvement.
实用新型内容Utility model content
实用新型目的在于克服上述现有技术的不足,提供一种消耗功率小,氧转移率高,曝气服务面积大,集曝气-搅拌于一体,气液固混合效果好的多功能高效曝气器。The purpose of the utility model is to overcome the shortcomings of the above-mentioned prior art, and provide a multi-functional high-efficiency aeration device with low power consumption, high oxygen transfer rate, large aeration service area, integration of aeration-stirring, and good gas-liquid-solid mixing effect. device.
实用新型目的实现,主要构思是使吸气、扩散叶轮设置在水下0.3m至水深1/3处,吸入空气向池底扩散依靠同轴设置的搅拌叶轮,达到既减小吸气动力消耗,又能增强对水体中气泡切割作用,提高氧转移效率,同时搅拌叶轮还使气、固、液三相充分混合,并能扩大溶气服务面积,从而克服了现有技术的不足,实现实用新型目的。具体说,实用新型多功能高效曝气器,包括带引气套筒的转轴或中空转轴,设置在转轴上的吸气、扩散叶轮,其特征在于吸气叶轮距水面深度为0.3m至水深1/3之间,吸气、扩散叶轮下方同轴有一层或多层搅拌叶轮。The purpose of the utility model is realized. The main idea is to set the suction and diffusion impellers at a place from 0.3m underwater to 1/3 of the water depth, and the suction air diffuses to the bottom of the pool by means of coaxially arranged stirring impellers, so as to reduce the power consumption of suction, It can also enhance the cutting effect on air bubbles in the water body, improve the efficiency of oxygen transfer, and at the same time, the stirring impeller can fully mix the three phases of gas, solid and liquid, and can expand the service area of dissolved air, thereby overcoming the shortcomings of the existing technology and realizing the utility model Purpose. Specifically, the utility model multifunctional high-efficiency aerator includes a rotating shaft with an air-inducing sleeve or a hollow rotating shaft, and suction and diffusion impellers arranged on the rotating shaft. Between /3, there is one or more layers of stirring impellers coaxially below the suction and diffusion impellers.
实用新型所说:The utility model says:
吸气、扩散叶轮,其功能作用与现有技术相同,通过在水下旋转在叶轮中心附近产生相对大气压低的低压区,使水面空气通过套筒或空心轴吸入水中,并由叶轮切割、剪切成小气泡,随着叶轮旋转向水中扩散。根据此原理,现有技术中自吸式增氧曝气吸气叶轮均可使用,例如涡轮扇叶型、盘式叶轮等,其中较好为采用涡扇叶型,具有相对大的吸气效率。吸气叶轮,一种较好为采用有上下端板叶轮(类似离心泵闭式叶轮,叶片位于上下端板间),上下端板更有利于在两端板间的叶轮轴心区域产生低压区,有利于提高自吸气量,从而提高溶氧率。为避免加大吸气造成叶轮中心气穴过大,而降低吸气量,一种方式可以在叶轮下端板上开有镂空区,通过水流导流作用防止吸气聚集以减小气穴,提高吸气量。此外,为进一步提高吸气量,一种更好为叶轮叶片采用中空式叶片结构,并使中空叶片与转轴导气出口连通(通过中空叶片向水中导气),此结构更有利于降低叶轮附近的压力,能获得更大的吸气压差,有利于自吸入更多的空气。Suction and diffusion impeller, its function is the same as that of the prior art. By rotating underwater, a low-pressure zone with relatively low atmospheric pressure is generated near the center of the impeller, so that the air on the surface of the water is sucked into the water through the sleeve or hollow shaft, and is cut and sheared by the impeller. Cut into small air bubbles, which diffuse into the water as the impeller rotates. According to this principle, the self-priming aeration aeration suction impellers in the prior art can be used, such as turbofan blade type, disc impeller, etc., among which the turbofan blade type is better, which has a relatively large suction efficiency . Suction impeller, one is preferably an impeller with upper and lower end plates (similar to the closed impeller of a centrifugal pump, the blades are located between the upper and lower end plates), and the upper and lower end plates are more conducive to generating a low pressure area in the impeller axis area between the two end plates , which is conducive to increasing the self-inhalation capacity, thereby increasing the dissolved oxygen rate. In order to avoid excessive air pockets in the center of the impeller caused by increased suction and reduce the suction capacity, one way is to have a hollow area on the lower end plate of the impeller, and prevent the accumulation of suction through the water flow diversion to reduce the air pockets and improve the air intake. Inspiratory volume. In addition, in order to further increase the suction capacity, it is better to use a hollow blade structure for the impeller blades, and make the hollow blades communicate with the air guide outlet of the rotating shaft (guiding air into the water through the hollow blades), this structure is more conducive to reducing the impeller near the impeller. The pressure can obtain a greater suction pressure difference, which is conducive to self-inhalation of more air.
吸气叶轮设置深度为水下0.3m至水深1/3处,为试验经济恰当区间。如果设置过浅,会因叶轮旋转产生旋流造成液面内凹影响溶氧效率,严重过浅会造成不能吸气;设置深度过大,又会因水深大而造成吸气功率增大,增加能耗。根据较多使用水处理池深,其中较好设置深度为水面下0.8m至水深1/3处。The setting depth of the suction impeller is from 0.3m underwater to 1/3 of the water depth, which is an economically appropriate range for the test. If the setting is too shallow, the swirling flow generated by the rotation of the impeller will cause the liquid surface to be concave and affect the dissolved oxygen efficiency. If it is too shallow, it will cause inability to inhale; if the setting depth is too large, the suction power will increase due to the large water depth. energy consumption. According to the depth of the water treatment pool that is mostly used, the best setting depth is from 0.8m below the water surface to 1/3 of the water depth.
中空转轴或套筒水下出气口,可以同现有技术设置在吸气、扩散叶轮下方,本发明一种较好是将出气口设置在叶轮各叶片间,更可以提高吸气叶轮对气泡的打碎作用。The hollow rotating shaft or the underwater air outlet of the sleeve can be arranged under the suction and diffusion impellers as in the prior art. In the present invention, the air outlet is preferably arranged between the blades of the impeller, which can further improve the resistance of the air suction impeller to air bubbles. Shattering effect.
搅拌叶轮,主要功能是通过旋转使水体产生搅拌轴向推流,一方面将上层扩散至水体的气泡引向下方直至池底,再通过上浮增加氧溶解量,同时使气泡均匀分散在较大面积,扩大了曝气服务面积;另一方面搅拌叶轮还兼具混合搅拌及切割气泡作用,向下水流碰到池底反射上升或沿池壁上升,降流、升流形成池内循环,既可以避免曝气及搅拌死角,又下层浆叶可将池底污泥带起,使污泥呈悬浮状态,更有利于水、气、固三相充分接触混合,更是增大了氧气的传质速率和利用率。根据池深度及服务面积要求不同,搅拌叶轮可以相间设置多个。搅拌叶轮形式也可以多种,其中较好为轴流型。第一层搅拌叶轮与吸气、扩散叶轮间距,较好为≥50cm,间距过小会导致使用搅拌叶轮增多,浪费功率。The main function of the stirring impeller is to make the water body generate agitation and axial push flow through rotation. On the one hand, the air bubbles diffused from the upper layer to the water body are guided downward to the bottom of the pool, and then the dissolved oxygen is increased by floating up, and the air bubbles are evenly dispersed in a larger area. , expanding the aeration service area; on the other hand, the stirring impeller also has the function of mixing and cutting air bubbles. The downward water flow meets the bottom of the pool and rises up or rises along the pool wall. Aeration and agitation dead angle, and the lower layer of paddles can bring up the sludge at the bottom of the pool, making the sludge in a suspended state, which is more conducive to the full contact and mixing of water, gas and solid, and increases the mass transfer rate of oxygen and utilization. According to different pool depth and service area requirements, multiple stirring impellers can be arranged alternately. There are also various forms of stirring impellers, among which the axial flow type is preferred. The distance between the stirring impeller of the first layer and the suction and diffusion impellers is preferably ≥ 50 cm. If the distance is too small, the use of stirring impellers will increase and power will be wasted.
此外:also:
还可以将驱动转轴旋转的电机,设置为变频控制,可以增加曝气器的灵活性,通过变频器改变转速,实现曝气模式与搅拌模式的转变,即转速不同,曝气器分别工作在曝气、搅拌工作状态,或者以搅拌为主工作状态,以适应水处理工艺不同要求,而不用额外增加设备。The motor that drives the rotating shaft can also be set to frequency conversion control, which can increase the flexibility of the aerator, change the speed through the frequency converter, and realize the transformation between the aeration mode and the stirring mode, that is, the speed is different, and the aerators work separately in the aeration mode. Gas, stirring working state, or stirring-based working state, to meet the different requirements of water treatment process, without adding additional equipment.
还可以在吸气、扩散叶轮同轴上方增设略浸于水中消泡桨,消泡桨主要功能是将水面产生的泡沫切碎,其结构形式只需能将液面气泡打碎均可,没有特别限定,例如一种简单是在一圆盘或一或几根横杆外周设置若干竖向短杆,旋转产生切割作用将气泡打(切)碎。切碎气泡,通过池内循环的升流和降流使液面不断更新,同时将液面的泡沫带入池底,泡沫被带动使气泡表面的局部厚度产生变化,同时水流使泡沫表面压力不均,从而导致泡沫的破裂,不仅达到消泡目的,满足污水处理工艺要求,而且增加了向水中曝气量,由于旋流导致水面凹陷,周围水面泡沫不断流入被切碎带入水中,因而可以将池面的气泡均得到消除。It is also possible to add a defoaming paddle submerged in water slightly above the suction and diffusion impeller coaxially. The main function of the defoaming paddle is to chop the foam generated on the water surface. Its structure only needs to be able to break the bubbles on the liquid surface. Particularly limited, for example a kind of simplicity is that some vertical short rods are arranged on the periphery of a disk or one or several cross bars, and the rotation produces cutting action to break (cut) the air bubbles. The bubbles are chopped, and the liquid surface is continuously updated through the upflow and downflow of the circulation in the pool, and at the same time, the foam on the liquid surface is brought to the bottom of the pool, and the foam is driven to change the local thickness of the bubble surface, and the water flow makes the pressure on the foam surface uneven. , which leads to the bursting of the foam, not only achieves the purpose of defoaming, meets the requirements of the sewage treatment process, but also increases the amount of aeration into the water. Due to the swirling flow, the water surface is sunken, and the surrounding water surface foam continues to flow in and be chopped into the water, so it can be removed The air bubbles on the surface of the pool are all eliminated.
实用新型多功能高效曝气器,相对于现有技术自吸式增氧曝气装置,由于将吸气、扩散叶轮移上设置,以及在下方以较大间距配置一层或多层搅拌叶轮,使得曝气、搅拌一体化,可以适用于各种水深环境,不仅降低了曝气能耗,而且配合叶轮的搅拌切碎作用,提高了服务面积和氧转移率,提高了氧的传质速率,充氧效果好,还同时能使气、固、液三相充分混合。吸气、扩散叶轮增加上下端板,更有利于吸气低压区的产生,较相同叶型,可以提高吸气效果和吸气量。叶片中空结构,吸气效果更好。配以变频变速装置,可以方便实现污水处理工艺的好氧、缺氧和厌氧条件自由切换,突破了现有技术自吸式增氧曝气,功能单一、运行模式单一的不足。增加消泡浆,不仅可以消除曝气池表面气泡,而且气泡随循环水流被带入水中,还同时具有增氧作用。实用新型自吸式增氧曝气装置,曝气动力消耗小,氧传质速率高,充氧效果好,同时兼具搅拌功能,运行工艺灵活多变,为区别于现有技术特点和优势。Compared with the self-priming oxygen-increasing aeration device in the prior art, the utility model multi-functional and high-efficiency aerator has the suction and diffusion impellers moved up, and one or more layers of agitating impellers are arranged at a large distance below, The integration of aeration and stirring can be applied to various water depth environments. It not only reduces the energy consumption of aeration, but also cooperates with the stirring and chopping function of the impeller to increase the service area and oxygen transfer rate, and increase the oxygen mass transfer rate. The oxygenation effect is good, and at the same time, the three phases of gas, solid and liquid can be fully mixed. The upper and lower end plates are added to the suction and diffusion impellers, which is more conducive to the generation of suction low-pressure areas. Compared with the same blade shape, it can improve the suction effect and suction volume. The hollow structure of the blades has a better air-breathing effect. Equipped with a variable frequency and variable speed device, it can easily realize the free switching of aerobic, anoxic and anaerobic conditions in the sewage treatment process, breaking through the shortcomings of the existing technology of self-priming oxygen-increasing aeration, single function, and single operating mode. Adding defoaming slurry can not only eliminate the bubbles on the surface of the aeration tank, but also bring the bubbles into the water with the circulating water flow, and also have the effect of increasing oxygen. The utility model self-priming oxygen-increasing aeration device has low aeration power consumption, high oxygen mass transfer rate, good oxygenation effect, and at the same time has a stirring function, and the operation process is flexible and changeable, which is different from the existing technical characteristics and advantages.
以下结合二个示例性实施例,示例性说明及帮助进一步理解实用新型实质,但实施例具体细节仅是为了说明实用新型,并不代表实用新型构思下全部技术方案,因此不应理解为对实用新型总的技术方案限定,一些在技术人员看来,不偏离实用新型构思的非实质性增加和/或改动,例如以具有相同或相似技术效果的技术特征简单改变或替换,均属实用新型保护范围。Below in conjunction with two exemplary embodiments, illustrate and help to further understand the essence of the utility model, but the specific details of the embodiment are only for explaining the utility model, and do not represent all technical solutions under the concept of the utility model, so it should not be interpreted as a reference to the utility model. The general technical solution of the new model is limited. Some insubstantial additions and/or changes that do not deviate from the concept of the utility model in the eyes of technicians, such as simple changes or replacements with technical features that have the same or similar technical effects, all belong to the protection of utility models scope.
附图说明Description of drawings
图1为实用新型多功能高效曝气器结构示意图。Fig. 1 is a structural schematic diagram of the utility model multifunctional high-efficiency aerator.
图2为实用新型多功能高效曝气器曝气工作示意图。Figure 2 is a schematic diagram of the aeration work of the utility model multifunctional high-efficiency aerator.
图3为一种吸气、扩散叶轮俯视结构示意图。Fig. 3 is a top view structure diagram of an air suction and diffusion impeller.
图4为另一种吸气、扩散叶轮俯视结构示意图。Fig. 4 is a top view structure schematic diagram of another suction and diffusion impeller.
具体实施方式Detailed ways
实施例1:参见图1、2、3,实用新型多功能高效曝气器,包括设置于固定架4上部的变频电机1、减速机2、控制电机转速的变频器3,固定在减速机输出轴上的中空转轴10,转轴水面上段有吸气孔5,转轴上液面下自上而下相间依次同轴设置有消泡桨6、吸气、扩散叶轮7、上下相间距离1.1米的二层搅拌叶轮8,底部同心定位装置9。吸气叶轮7为涡轮扇叶型,上下二面各有端板11,各叶片12间有与中空转轴连通的出气口13,设置在池深1/3处(4米池深,水面下1.3米处),消泡桨6为水平杆或圆盘,外周有若干竖向短杆,设置位置使工作时短杆浸没于水中。Embodiment 1: Referring to Figures 1, 2, and 3, the utility model multifunctional high-efficiency aerator includes a variable frequency motor 1 arranged on the top of the fixed frame 4, a speed reducer 2, and a frequency converter 3 for controlling the speed of the motor, and is fixed on the output of the speed reducer. The hollow rotating shaft 10 on the shaft has an air suction hole 5 on the upper part of the water surface of the rotating shaft, and a defoaming paddle 6, an air suction and a diffusion impeller 7, and two 1.1-meter distances between the upper and lower sides of the rotating shaft are coaxially arranged in sequence from top to bottom. Layer stirring impeller 8, bottom concentric positioning device 9. The suction impeller 7 is a turbine blade type, with
曝气器工作(图2),由电机1带动空心轴10及轴上的吸气涡轮7、搅拌叶轮8和消泡桨6旋转,例如超过曝气临界转速(200-450r/min),在吸气、扩散叶轮7转轴中心附近产生足够大的负压,将水面上方空气通过空心轴10上的气孔5大量吸入,经由空心轴10从吸气、扩散涡轮7叶片间出气孔喷出,在吸气涡轮7剪力和动压变动力作用下,变成非常细小微气泡。同时下方二层搅拌叶轮8同轴旋转,产生向下旋流,将上层吸气、扩散叶轮7引入的气泡带入池底,向下水流碰到池底后反射上升,从而实现充分曝气,同时水流以降流与升流形式在池内循环,有效避免了死角产生,同时下层搅拌叶轮8将池底污泥带起,使污泥呈悬浮状态,气、液、固三相得到充分接触,增大了氧气的传质速率和利用率。消泡桨6旋转将水面旋流产生泡沫切碎,通过搅拌形成的升流和降流使液面不断更新,将液面泡沫带入池内水体,泡沫被带动使气泡表面局部厚度产生变化,同时水流使泡沫表面压力不均,从而导致泡沫破裂,不仅达到消泡目的,满足污水处理工艺要求,而且增加了向水中曝气量。The aerator works (Figure 2), and the motor 1 drives the hollow shaft 10 and the suction turbine 7 on the shaft, the stirring impeller 8 and the defoaming paddle 6 to rotate, for example, exceeding the aeration critical speed (200-450r/min), at Suction and diffusion impeller 7 near the center of the rotating shaft generate a large enough negative pressure, the air above the water surface is sucked in a large amount through the air hole 5 on the hollow shaft 10, and is ejected from the air outlet between the suction and diffusion turbine 7 blades through the hollow shaft 10. Under the action of the shearing force of the suction turbine 7 and the variable force of the dynamic pressure, it becomes very fine micro-bubbles. At the same time, the lower two-layer stirring impeller 8 rotates coaxially to generate a downward swirling flow, which brings the air bubbles introduced by the upper-layer suction and diffusion impeller 7 into the bottom of the pool, and the downward water flow hits the bottom of the pool and rises after reflection, thereby achieving full aeration. At the same time, the water flow circulates in the pool in the form of downflow and upflow, which effectively avoids the occurrence of dead angles. At the same time, the lower stirring impeller 8 lifts up the sludge at the bottom of the pool, making the sludge in a suspended state, and the three phases of gas, liquid, and solid are fully contacted, increasing Increased the mass transfer rate and utilization of oxygen. The defoaming paddle 6 rotates to chop the foam generated by the swirling flow on the water surface, and the liquid surface is continuously updated through the upflow and downflow formed by stirring, and the liquid surface foam is brought into the water body in the pool, and the foam is driven to change the local thickness of the bubble surface. The water flow makes the pressure on the foam surface uneven, which causes the foam to burst, which not only achieves the purpose of defoaming, meets the requirements of the sewage treatment process, but also increases the amount of aeration into the water.
当不需要曝气,降低电机转速,吸气、扩散叶轮7周边负压不足以将外界空气吸入,基本处于停止曝气工作状态,此时曝气器工作在主要以搅拌混合为主工作状态。When aeration is not needed, the motor speed is reduced, and the negative pressure around the suction and diffusion impeller 7 is not enough to suck in the outside air, and the aeration is basically stopped. At this time, the aerator is mainly in the working state of stirring and mixing.
曝气器由曝气模式切换为搅拌模式初期,水中还存在一定浓度溶解氧,此时,处理水为缺氧环境;当溶解氧逐渐消耗殆尽,池内为厌氧环境。由此实现通过变频器3的控制,使处理池在好氧-缺氧-厌氧模式之间切换,满足了污水脱氮除磷所需的三种环境。根据处理工艺要求,可以周期性改变电机运行状态,在同池实现好氧-缺氧-厌氧模式切换。When the aerator is switched from the aeration mode to the stirring mode, there is still a certain concentration of dissolved oxygen in the water. At this time, the treated water is an anoxic environment; when the dissolved oxygen is gradually exhausted, the pool is an anaerobic environment. In this way, the control of the frequency converter 3 enables the treatment tank to switch between aerobic-anoxic-anaerobic modes, satisfying the three environments required for denitrification and dephosphorization of sewage. According to the requirements of the treatment process, the operating state of the motor can be changed periodically, and the aerobic-anoxic-anaerobic mode switching can be realized in the same pool.
实施例2:参见图4,如实施例1,吸氧涡轮叶片14呈中空结构,下端板上镂空区15,中空转轴出气口13与各中空叶片连通。Embodiment 2: Referring to FIG. 4, as in Embodiment 1, the
对于本领域技术人员来说,在本专利构思及具体实施例启示下,能够从本专利公开内容及常识直接导出或联想到的一些变形,本领域普通技术人员将意识到也可采用其他方法,或现有技术中常用公知技术的替代,以及特征间的相互不同组合,例如吸气、扩散叶轮及搅拌叶轮采用其他叶型,中空转轴以转轴和引气套筒代替,对于产生泡沫不多,也可以省略消泡桨,等等的非实质性改动,同样可以被应用,都能实现本专利描述功能和效果,不再一一举例展开细说,均属于本专利保护范围。For those skilled in the art, under the inspiration of the patent concept and specific embodiments, some deformations that can be directly derived or associated from the patent disclosure and common sense, those of ordinary skill in the art will realize that other methods can also be used, Or the replacement of commonly known technologies in the prior art, and the different combinations of features, such as suction, diffusion impellers and stirring impellers using other blade shapes, the hollow shaft is replaced by a shaft and an air-inducing sleeve, which is not much for generating foam. It is also possible to omit non-substantial changes such as defoaming paddles, etc., which can also be applied, and can achieve the functions and effects described in this patent. No more examples are given to elaborate, and they all belong to the scope of protection of this patent.
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| CN102743994A (en) * | 2012-06-18 | 2012-10-24 | 江苏大学 | Sewage treatment mixer |
| CN104437221A (en) * | 2014-11-25 | 2015-03-25 | 潘春圃 | Stirrer with double impellers |
| CN104772083A (en) * | 2015-03-18 | 2015-07-15 | 四川中哲新材料科技有限公司 | Gas-liquid mixing and stirring device |
| CN104891657A (en) * | 2015-06-08 | 2015-09-09 | 新乡市蓝海环境工程有限公司 | CBR sewage biological treatment device and operating method thereof |
| CN105606783A (en) * | 2016-01-28 | 2016-05-25 | 中国环境科学研究院 | Device and method for simulating influence of different illumination conditions on water body nutritive salt |
| CN106186385A (en) * | 2016-09-29 | 2016-12-07 | 台州天渔增氧设备科技有限公司 | A kind of impeller of aeration oxygen increasing machine |
| CN108483687A (en) * | 2018-04-25 | 2018-09-04 | 成都澎湃新能源科技有限公司 | A Hybrid Oxygenator with Optimized Driving Structure |
| CN108706838A (en) * | 2018-07-28 | 2018-10-26 | 上海亚威环保科技有限公司 | Medical waste water zero discharge treatment device and method |
| CN108862694A (en) * | 2018-05-30 | 2018-11-23 | 四川奥恒环保科技有限公司 | Intelligent and high-efficiency sewage-treatment plant |
| CN109052649A (en) * | 2018-10-31 | 2018-12-21 | 青岛思普润水处理股份有限公司 | A kind of microkinetic combined sewage processing unit |
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| CN112850899A (en) * | 2021-03-03 | 2021-05-28 | 清研环境科技股份有限公司 | Vertical-partition anoxic-aerobic-precipitation integrated sewage treatment system and stirring-aeration integrated device thereof |
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| CN117903771A (en) * | 2023-03-01 | 2024-04-19 | 甘肃普瑞斯石油科技有限公司 | A preparation process for oilfield oil and water well formation acidification plugging removal fluid |
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| CN102743994A (en) * | 2012-06-18 | 2012-10-24 | 江苏大学 | Sewage treatment mixer |
| CN104437221A (en) * | 2014-11-25 | 2015-03-25 | 潘春圃 | Stirrer with double impellers |
| CN104772083A (en) * | 2015-03-18 | 2015-07-15 | 四川中哲新材料科技有限公司 | Gas-liquid mixing and stirring device |
| CN104891657A (en) * | 2015-06-08 | 2015-09-09 | 新乡市蓝海环境工程有限公司 | CBR sewage biological treatment device and operating method thereof |
| CN105606783A (en) * | 2016-01-28 | 2016-05-25 | 中国环境科学研究院 | Device and method for simulating influence of different illumination conditions on water body nutritive salt |
| CN106186385A (en) * | 2016-09-29 | 2016-12-07 | 台州天渔增氧设备科技有限公司 | A kind of impeller of aeration oxygen increasing machine |
| CN108483687A (en) * | 2018-04-25 | 2018-09-04 | 成都澎湃新能源科技有限公司 | A Hybrid Oxygenator with Optimized Driving Structure |
| CN108483687B (en) * | 2018-04-25 | 2024-06-07 | 陕西易阳泽智科技有限公司 | Mixed oxygenator with optimized driving structure |
| CN108862694A (en) * | 2018-05-30 | 2018-11-23 | 四川奥恒环保科技有限公司 | Intelligent and high-efficiency sewage-treatment plant |
| CN108706838A (en) * | 2018-07-28 | 2018-10-26 | 上海亚威环保科技有限公司 | Medical waste water zero discharge treatment device and method |
| CN109516540A (en) * | 2018-10-18 | 2019-03-26 | 文露 | A kind of environmental protection aerator |
| CN109052649B (en) * | 2018-10-31 | 2023-08-29 | 青岛思普润水处理股份有限公司 | Micro-power mixed sewage treatment device |
| CN109052649A (en) * | 2018-10-31 | 2018-12-21 | 青岛思普润水处理股份有限公司 | A kind of microkinetic combined sewage processing unit |
| CN112850899A (en) * | 2021-03-03 | 2021-05-28 | 清研环境科技股份有限公司 | Vertical-partition anoxic-aerobic-precipitation integrated sewage treatment system and stirring-aeration integrated device thereof |
| CN112897718A (en) * | 2021-04-02 | 2021-06-04 | 北控水务(中国)投资有限公司 | Feeding device of ultramicro bubble aeration equipment and sewage treatment system |
| CN113248009A (en) * | 2021-05-28 | 2021-08-13 | 华川技术有限公司 | Ecological reef with bubble cutting function |
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