CN201058829Y - A high-efficiency sewage treatment gas mixing device - Google Patents
A high-efficiency sewage treatment gas mixing device Download PDFInfo
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- CN201058829Y CN201058829Y CNU2006201514249U CN200620151424U CN201058829Y CN 201058829 Y CN201058829 Y CN 201058829Y CN U2006201514249 U CNU2006201514249 U CN U2006201514249U CN 200620151424 U CN200620151424 U CN 200620151424U CN 201058829 Y CN201058829 Y CN 201058829Y
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- 239000010865 sewage Substances 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 99
- 239000007789 gas Substances 0.000 claims abstract description 27
- 230000006837 decompression Effects 0.000 claims abstract description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000001301 oxygen Substances 0.000 claims abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 15
- 238000012856 packing Methods 0.000 claims 1
- 238000005273 aeration Methods 0.000 abstract description 19
- 239000007788 liquid Substances 0.000 abstract description 6
- 241000251468 Actinopterygii Species 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000002306 biochemical method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000238557 Decapoda Species 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000007269 microbial metabolism Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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- 230000004083 survival effect 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
本实用新型提供一种简便高效能连续产生细密气泡的气液混合装置,用于污水或废水处理以及鱼塘等场合的曝气系统中。其中包括气体引入组件1、气水混合组件2和气泡减压细化组件3等组成。需要处理的原水在气体引入部的射流喷嘴处将空气或氧气引入水中;通过气水混合部使气水均匀混合;再经过二级旋转减压气泡释放装置,使很细密的气泡混合到原水中。
The utility model provides a simple and high-efficiency gas-liquid mixing device for continuously generating fine air bubbles, which is used in aeration systems for sewage or waste water treatment, fish ponds and other occasions. It includes a gas introduction component 1, a gas-water mixing component 2, and a bubble decompression refinement component 3. The raw water to be treated introduces air or oxygen into the water at the jet nozzle of the gas introduction part; the gas and water are uniformly mixed through the gas-water mixing part; and then passes through the secondary rotary decompression bubble release device to mix very fine bubbles into the raw water .
Description
技术领域technical field
本实用新型涉及水处理技术,确切地说,为一种高效污水处理混气装置,是一种用于污水或工业废水以及鱼塘等水处理曝气过程中能够在水中产生细密气泡,进而增加溶解氧的旋混曝气装置。The utility model relates to water treatment technology, to be precise, it is a high-efficiency sewage treatment aeration device, which can generate fine air bubbles in water during the aeration process of sewage or industrial waste water and fish ponds, thereby increasing the Rotary Mixed Aeration Device for Dissolved Oxygen.
背景技术Background technique
生活污水以及工业废水处理,去除水中有机物最有效的方法为生化法。目前生化法中通常采用的接触氧化、活性污泥等方法,均要通过曝气方式向污水中扩散输送空气充氧,增加水中的溶解氧。溶解氧维持活性污泥中微生物代谢的需要,以及促使接触氧化填料壁的微生物生成新的生物膜。生化法污水处理就是利用微生物细菌,以污水中有机物作为养料代谢繁殖,达到降解有机污染物、净化水的目的,亦即生物降解技术。另外,人工养殖鱼虾等水产品,也要通过曝气向池塘中增加溶解氧,维持水生物的生存需要。因此,向水中均匀混入空气或氧气的曝气扩散技术,在污水处理及水产养殖中起着极为重要的作用。For domestic sewage and industrial wastewater treatment, the most effective method to remove organic matter in water is biochemical method. At present, methods such as contact oxidation and activated sludge commonly used in biochemical methods all need to diffuse and transport air into the sewage through aeration to oxygenate and increase the dissolved oxygen in the water. Dissolved oxygen is required to maintain microbial metabolism in activated sludge and to promote the formation of new biofilms by microorganisms that contact the walls of the oxidized filler. Biochemical sewage treatment is to use microbial bacteria to metabolize and reproduce organic matter in sewage as nutrients to degrade organic pollutants and purify water, that is, biodegradation technology. In addition, artificially cultured fish and shrimp and other aquatic products must also increase dissolved oxygen into the pond through aeration to maintain the survival needs of aquatic organisms. Therefore, the aeration and diffusion technology that evenly mixes air or oxygen into the water plays an extremely important role in sewage treatment and aquaculture.
以往向水中混气曝气方式主要有鼓风曝气、高速搅拌曝气以及射流溶气等方法。鼓风曝气是用鼓风机通过管道末端排布的曝气头向水中扩散气相流体,产生立体连续的气液接触界面,是曝气的主要方式。但曝气头的气孔过大,产生的气泡大而影响气液接触面积,气孔过小又会加大压阻而增加动力消耗,而且容易堵塞,使维护变得困难;高速搅拌曝气产生不均匀的片状气泡,效果不理想;而直接射流溶气的效率低,产生的气泡数量少不细密。In the past, the mixed air aeration methods in water mainly include blast aeration, high-speed stirring aeration, and jet dissolved air. Blast aeration is to use the blower to diffuse the gas-phase fluid into the water through the aeration head arranged at the end of the pipeline to produce a three-dimensional continuous gas-liquid contact interface, which is the main way of aeration. However, if the pores of the aeration head are too large, the generated bubbles will be large and affect the gas-liquid contact area. If the pores are too small, the pressure resistance will increase and the power consumption will be increased, and it will be easily blocked, making maintenance difficult; Uniform flaky bubbles are not ideal; while the efficiency of direct jet dissolved air is low, and the number of bubbles produced is small and not dense.
发明内容Contents of the invention
本实用新型的目的是针对现有曝气设备存在的不足,提供一种简便廉价低能耗和高可靠性,能连续产生细密气泡的气液混合装置。The purpose of the utility model is to provide a gas-liquid mixing device that is simple, cheap, low in energy consumption, high in reliability and capable of continuously generating fine air bubbles, aiming at the deficiencies of the existing aeration equipment.
本实用新型在技术上是按下述方式实现的。需要处理的原水经过水泵加压进入到一个直径由粗到细的管道,水在细管道处流速加快,与大气之间形成负压。细管道出口扩张处设一个与大气相通的导管,在负压作用下,空气自然吸入到原水中。溶入空气的水经混合器碰撞、扰流、阻挡作用,形成微小气泡,再通过二级旋转减压气泡释放装置的减压、导流、旋流作用,形成雾状含有细密气泡的气液混合水。当这种气液混合水进入到水池后,微细气泡以较大的比表面积扩散上升与水接触,有效增加水中的溶解氧。The utility model is technically realized in the following manner. The raw water to be treated is pressurized by the water pump and enters a pipe with a diameter ranging from thick to thin. The water flows faster in the thin pipe and forms a negative pressure with the atmosphere. A conduit communicating with the atmosphere is provided at the expanded part of the thin pipe outlet, and under the action of negative pressure, the air is naturally sucked into the raw water. The water dissolved in the air is collided, disturbed and blocked by the mixer to form tiny bubbles, and then through the decompression, diversion and swirl of the two-stage rotating decompression bubble release device, a mist-like gas-liquid containing fine bubbles is formed mixed with water. When the gas-liquid mixed water enters the pool, the fine bubbles diffuse and rise to contact the water with a large specific surface area, effectively increasing the dissolved oxygen in the water.
本实用新型为一种高效污水处理混气装置,其特征在于其中组成包括气体引入组件1、气水混合组件2和气泡减压细化组件3。The utility model is an efficient sewage treatment gas mixing device, which is characterized in that the components include a
气体引入组件1是一圆形管状体,水泵打入的原水通过螺纹管道连接腔14、变径室15,进入射流区16;射流区出口处设与大气或氧气瓶相通的进气管11,流动的原水在扩张腔17处的负压区,通过进气管喷嘴12将空气或氧气吸入到原水中。The
气水混合组件2是一两端带螺纹压帽的圆管型装置,压帽23和28将连接管13和39,通过密封圈24和27密封连接;气水混合组件2的内部放置气水混合器25和第一级旋转减压气泡释放装置26。The air-
气水混合器25,是一内表面加工成多条不连续螺纹状凸起21的圆管,圆管装入气水混合器25内部。The air-water mixer 25 is a round tube whose inner surface is processed into a plurality of discontinuous thread-
旋转减压气泡释放装置,与气水混合器25等直径的圆管内部,焊接两个或两个以上风扇叶片状翅片22,翅片高度超过中心线。Rotating decompression bubble release device, inside the circular tube with the same diameter as the air-water mixer 25, two or more fan blade-
气泡减压细化组件3是由两片法兰夹住一圆管32,圆管内部放置第二级旋转减压气泡释放装置37;法兰两端通过螺纹连接水管39和35,法兰用螺栓夹紧固定。The air bubble
本实用新型提供的混气装置,结构上主要由气体引入组件、气水混合组件和气泡减压细化组件等组成。需要处理的原水在气体引入部的射流喷嘴处将空气或氧气引入水中;通过气水混合部使气水均匀混合;再经过二级旋转减压气泡释放装置,使很细密的气泡混合到原水中。以下结合附图,对本实用新型做进一步说明。The gas mixing device provided by the utility model is structurally mainly composed of a gas introduction component, a gas-water mixing component, and a bubble decompression and refinement component. The raw water to be treated introduces air or oxygen into the water at the jet nozzle of the gas introduction part; the gas and water are uniformly mixed through the gas-water mixing part; and then passes through the secondary rotary decompression bubble release device to mix very fine bubbles into the raw water . Below in conjunction with accompanying drawing, the utility model is described further.
附图说明Description of drawings
图1是本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
气体引入组件1;气水混合组件2;气泡减压细化组件3;进气管11;进气管喷嘴12;连接管13、39、35;连接腔14;变径室15;射流区16;扩张腔17;螺纹状凸起21;翅片22、36;压帽23、28;密封圈24、27;气水混合器25;减压气泡释放装置26、37;法兰31、33;圆管32;螺栓34、38;
图2是本实用新型的一个具体实施方式示意图。Fig. 2 is a schematic diagram of a specific embodiment of the present invention.
水池51;进水管52;高效污水处理混气装置53;水泵54;出水管55;溶气水56;布水管57
本实用新型提供的混气装置中,气体引入组件1、气水混合组件2和气泡减压细化组件3是组合在一起,而又相互独立的3个部分。原水经过水泵的加压提升,进入气体引入组件1。该组件内部连接腔14经过变径室15的过渡,在射流区16处直径变细,变径比为5∶1-3∶1之间。水在射流区流速增加,增加值与直径变化的平方成反比,高流速区相对于大气为负压。原水在扩张腔17处减压,在此处设置一个与大气或氧气瓶相通的进气管11,通过进气管喷嘴12将空气或氧气吸入到原水中。In the gas mixing device provided by the utility model, the
气体引入组件1、气水混合组件2通过连接管13连接。溶入气体的水在气水混合器25内与螺纹状凸起21高速碰撞、搅拌,成紊流状态,形成含有微小气泡的均匀气水混合体。压帽23和28通过密封圈24和27将混合组件两端密封。气水混合组件2内还安装一个旋转减压气泡释放装置26,它是一个外径与气水混合组件2内径活动配合的圆管段。在其内圆表面焊接至少两个以上的风扇叶片状翅片22,翅片高度超过中心线,两个翅片轴向间要有一定距离,该距离要大于翅片几何尺寸宽度一倍以上,防止堵塞发生。混气水与翅片接触,在翅片的导流和旋流作用下,旋转减压后改变了流体形态。旋流作用,使溶解在水中的气泡沿直径方向向管壁加速运动,和管壁高速碰撞后使气泡进一步细化并使水流旋转;翅片的阻挡作用使水流的压力降低约0.1~0.3Mpa,压力降低使水中的气泡呈雾状从而变得更加细密。The
通过连接管39,气水混合体进入到减压细化组件3中。连接管39的一端用压帽28与气水混合组件2连接,另一端通过螺纹与法兰相连。两片法兰夹住一圆管32,圆管内部放置第二级旋转减压气泡释放装置37,它的作用与前述气泡释放装置26相同,只是翅片旋转角度与26相反,起到反旋减压效果。两片法兰用螺栓夹紧固定。通过连接管39出来的混气水可以引入曝气池、气浮槽或水塘,有很高的含氧量和多量的细密气泡。Through the connecting
本实用新型提供的高效污水处理混气装置,结构设计独特。由于采用经多种结构作用和大孔排气,所以压力损失小动力消耗也小,且不容易堵塞。其结构简单安装容易,同时可以省却体积庞大的空气压缩和储气设备,实用效果明显。The high-efficiency sewage treatment gas mixing device provided by the utility model has a unique structural design. Due to the use of various structural effects and large hole exhaust, the pressure loss is small and the power consumption is small, and it is not easy to block. Its structure is simple and easy to install, and at the same time, bulky air compression and gas storage equipment can be saved, and the practical effect is obvious.
具体实施方式Detailed ways
图2是本实用新型的一个具体实施方式示意图。Fig. 2 is a schematic diagram of a specific embodiment of the present invention.
水泵54通过进水管52,从水池51中吸水进入本实用新型提供的高效污水处理混气装置53。水泵出口压力不小于0.4Mpa。经过混气装置53后的混气水,通过出水管55与布水管57连接。布水管长度视水池长度确定。布水管上距出水管由近到远,按直径由小到大,间隔一定距离开一排孔,最小孔的直径不小于5mm,避免造成堵塞。布水管57距水池底距离不小于100mm,开孔向下而不至于停泵期间污泥浸入布水管内。通过并联方式连接多条布水管,使整个水池布水均匀。水池接近水泵进水口处设置一个挡水堰,其作用是不使溶气水进入水泵产生气蚀。加入本混气装置后,溶气水56表面可以看到很细密的气泡,水中的溶解氧值提高了87%。The
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102381755A (en) * | 2011-11-03 | 2012-03-21 | 王杰 | Aeration device with low gas pressure loss |
| CN102847453A (en) * | 2012-08-28 | 2013-01-02 | 河海大学 | Microbubble generator used for irrigation |
| CN102942251A (en) * | 2012-11-20 | 2013-02-27 | 苏州香山红叶环境技术有限公司 | Multi-nozzle jet-flow micro-nano bubble aerator |
| CN103102021A (en) * | 2013-02-27 | 2013-05-15 | 湛江市科海科技有限公司 | High oxygen ejector |
| CN107473365A (en) * | 2017-09-11 | 2017-12-15 | 梁芳新 | A kind of high energy oxygengenerating plant and water treatment system |
| CN108328754A (en) * | 2018-02-01 | 2018-07-27 | 苏州碳酸泉贸易有限公司 | A kind of microminiature nanometer micro-bubble generation device |
| CN109011305A (en) * | 2018-08-19 | 2018-12-18 | 李胎恩 | A kind of band is saved oneself turntable outlet pressure-reducing and-stabilizing hydrant |
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| CN109382010A (en) * | 2018-11-24 | 2019-02-26 | 深圳康诚博信科技有限公司 | The miscible device of air water and the miscible method of air water |
| CN109475827A (en) * | 2016-07-25 | 2019-03-15 | 丸福水产株式会社 | Mixed treatment body, mixed treatment method, mixed production fluid, fluid mixer, fluid mixed treatment device, fish and shellfish culture system and fish and shellfish culture method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102381755A (en) * | 2011-11-03 | 2012-03-21 | 王杰 | Aeration device with low gas pressure loss |
| CN102847453A (en) * | 2012-08-28 | 2013-01-02 | 河海大学 | Microbubble generator used for irrigation |
| CN102942251A (en) * | 2012-11-20 | 2013-02-27 | 苏州香山红叶环境技术有限公司 | Multi-nozzle jet-flow micro-nano bubble aerator |
| CN102942251B (en) * | 2012-11-20 | 2014-01-01 | 苏州香山红叶环境技术有限公司 | Multi-nozzle jet-flow micro-nano bubble aerator |
| CN103102021A (en) * | 2013-02-27 | 2013-05-15 | 湛江市科海科技有限公司 | High oxygen ejector |
| CN109475827B (en) * | 2016-07-25 | 2021-11-05 | 丸福水产株式会社 | Mixed treatment body, mixed treatment method, mixed production fluid, fluid mixer, fluid mixed treatment device, fish and shellfish culture system and fish and shellfish culture method |
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| CN107473365A (en) * | 2017-09-11 | 2017-12-15 | 梁芳新 | A kind of high energy oxygengenerating plant and water treatment system |
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