CN209039146U - An Improved Air Supply Type Low Pressure Jet Aerator - Google Patents
An Improved Air Supply Type Low Pressure Jet Aerator Download PDFInfo
- Publication number
- CN209039146U CN209039146U CN201821657064.9U CN201821657064U CN209039146U CN 209039146 U CN209039146 U CN 209039146U CN 201821657064 U CN201821657064 U CN 201821657064U CN 209039146 U CN209039146 U CN 209039146U
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- Prior art keywords
- air
- mixing chamber
- low pressure
- jet nozzle
- nozzle
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- 238000005276 aerator Methods 0.000 title claims abstract description 17
- 230000004888 barrier function Effects 0.000 claims abstract description 5
- 230000008676 import Effects 0.000 claims abstract 3
- 239000007788 liquid Substances 0.000 abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 238000005273 aeration Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 239000007789 gas Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 239000007791 liquid phase Substances 0.000 abstract description 2
- 230000000903 blocking effect Effects 0.000 description 6
- 239000012071 phase Substances 0.000 description 4
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Nozzles (AREA)
Abstract
Description
技术领域technical field
本实用新型设计水处理技术领域,具体涉及一种改进型供气式低压射流曝气器。The utility model is designed in the technical field of water treatment, in particular to an improved air supply type low pressure jet aerator.
背景技术Background technique
射流曝气技术是继空气扩散曝气技术和机械曝气技术后问世的第三种曝气技术,它是通过射流曝气器将空气或空气和污水——污泥的混合流充入好氧生化池中,来提升好氧生化池内的污水中的氧气含量,其拥有传质效率高和混合搅拌强的优点 ,但是现有的射流曝气器的气水混合还不是特别充分,导致充氧的效率还是比较低,另外气水混合气泡与污水的接触面积比较小,导致氧的传递效率低下,整体曝气效果不是很理想,无法满足一些高标准的曝气处理要求。Jet aeration technology is the third aeration technology that came out after air diffusion aeration technology and mechanical aeration technology. It has the advantages of high mass transfer efficiency and strong mixing and stirring, but the gas-water mixing of the existing jet aerator is not particularly sufficient, resulting in oxygenation In addition, the contact area between gas-water mixed bubbles and sewage is relatively small, resulting in low oxygen transfer efficiency, and the overall aeration effect is not very ideal, which cannot meet some high-standard aeration treatment requirements.
发明内容SUMMARY OF THE INVENTION
为了克服上述现有技术的不足,本实用新型的目的是提供一种改进型供气式低压射流曝气器,具有充氧效率高、氧的传递效率高的特点。In order to overcome the above-mentioned deficiencies of the prior art, the purpose of the present invention is to provide an improved air supply type low pressure jet aerator, which has the characteristics of high oxygenation efficiency and high oxygen transfer efficiency.
为了实现上述目的,本实用新型采用的技术方案是:In order to achieve the above purpose, the technical scheme adopted by the present utility model is:
一种改进型供气式低压射流曝气器,包括进液管,进液管一端为进口,另一端为一级喷嘴,一级喷嘴插入混合室一端,一级喷嘴前端位于混合室内设有阻隔球,混合室上端连通进气口,混合室另一端为二级喷嘴。An improved air supply type low-pressure jet aerator, comprising a liquid inlet pipe, one end of the liquid inlet pipe is an inlet, the other end is a primary nozzle, the primary nozzle is inserted into one end of a mixing chamber, and the front end of the primary nozzle is located in the mixing chamber and is provided with a barrier The upper end of the mixing chamber is connected to the air inlet, and the other end of the mixing chamber is a secondary nozzle.
所述的阻隔球位于混合室内中心点,距离一级喷嘴30mm处。The blocking ball is located at the center point of the mixing chamber, 30 mm away from the primary nozzle.
所述的一级喷嘴、二级喷嘴为锥形管口。The primary and secondary nozzles are conical nozzles.
所述的进气口连接鼓风机。The air inlet is connected to the blower.
所述的进液管的进口连接循环水泵。The inlet of the liquid inlet pipe is connected to the circulating water pump.
本实用新型的有益效果是:The beneficial effects of the present utility model are:
水体通过一级喷嘴射流喷出,通过阻隔球打散水体,与气体能在混合室内充分混合,然后通过二级喷嘴排出,结构简单,能增加湍流动能,促使气液混合效果,提高射流曝气器的工作效率。The water body is sprayed out through the first-stage nozzle jet, dispersed by the blocking ball, fully mixed with the gas in the mixing chamber, and then discharged through the second-stage nozzle. The structure is simple, which can increase the turbulent kinetic energy, promote the gas-liquid mixing effect, and improve the jet aeration. efficiency of the device.
附图说明Description of drawings
图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2为本实用新型的气液混合效果图。Fig. 2 is a gas-liquid mixing effect diagram of the utility model.
其中,1为进口;2为一级喷嘴;3为混合室;4为二级喷嘴;5为进气口;6为阻隔球;7为进液管。Among them, 1 is the inlet; 2 is the primary nozzle; 3 is the mixing chamber; 4 is the secondary nozzle; 5 is the air inlet; 6 is the blocking ball; 7 is the liquid inlet pipe.
具体实施方式Detailed ways
以下结合附图对本实用新型进一步叙述。The utility model is further described below in conjunction with the accompanying drawings.
如图1所示,一种改进型供气式低压射流曝气器,包括进液管7,进液管7一端为进口1,另一端为一级喷嘴2,一级喷嘴2插入混合室3一端,一级喷嘴2前端位于混合室3内设有阻隔球6,混合室3上端连通进气口5,混合室3另一端为二级喷嘴4。As shown in Figure 1, an improved air supply type low pressure jet aerator includes a liquid inlet pipe 7, one end of the liquid inlet pipe 7 is an inlet 1, the other end is a primary nozzle 2, and the primary nozzle 2 is inserted into the mixing chamber 3 At one end, the front end of the primary nozzle 2 is located in the mixing chamber 3 with a blocking ball 6 , the upper end of the mixing chamber 3 is connected to the air inlet 5 , and the other end of the mixing chamber 3 is the secondary nozzle 4 .
所述的阻隔球6位于混合室3内中心点,距离一级喷嘴2的30mm处。The blocking ball 6 is located at the center point in the mixing chamber 3 , at a distance of 30 mm from the primary nozzle 2 .
所述的一级喷嘴2、二级喷嘴4为锥形管口。The primary nozzle 2 and the secondary nozzle 4 are conical nozzles.
所述的进气口5连接鼓风机。The air inlet 5 is connected to the blower.
所述的进液管7的进口1连接循环水泵。The inlet 1 of the liquid inlet pipe 7 is connected to the circulating water pump.
本实用新型工作时,利用鼓风机鼓入的空气通过进气管5将空气通入射流器,曝气池中的泥水混合物在相对低的压力下,由循环泵送入进口1,进入射流曝气器经一级喷嘴2高速喷出,水柱经过阻隔球6被打散,与空气充分接触,由二级喷嘴4喷出,特殊的设计使进水在较低的压力下与空气充分混合,其能量的消耗因而远小于传统的射流曝气器;在此状态下,空气被雾化成直径极其微小的气泡,迅速有效地转移到液相和生物相,完成氧气的快速转移过程。When the utility model works, the air blown by the blower is used to pass the air into the aerator through the air inlet pipe 5, and the mud-water mixture in the aeration tank is sent into the inlet 1 by the circulating pump under a relatively low pressure, and enters the jet aerator. The water column is sprayed out at a high speed through the primary nozzle 2, and the water column is dispersed through the blocking ball 6, fully contacting with the air, and ejected from the secondary nozzle 4. The special design makes the incoming water fully mix with the air at a lower pressure, and its energy The consumption of the air is thus much smaller than that of the traditional jet aerator; in this state, the air is atomized into bubbles with extremely small diameters, which are quickly and efficiently transferred to the liquid and biological phases to complete the rapid oxygen transfer process.
如图2所示,为改进型供气式低压射流曝气器水相体积云图。图中红色区域表示液相区域,蓝色部分表示气相区域,中间过度色区域表示气液混合区域,且颜色不同,气液两相所占的比例不同。从图中能够明显看出新型供气式低压射流曝气器工作时的气——液混合效果显著。As shown in Figure 2, it is the volume cloud map of the water phase of the improved air-supplied low-pressure jet aerator. The red area in the figure represents the liquid phase area, the blue part represents the gas phase area, and the intermediate over-color area represents the gas-liquid mixing area, and the colors are different, and the proportions of the gas-liquid two phases are different. It can be clearly seen from the figure that the gas-liquid mixing effect of the new air-supplied low-pressure jet aerator is remarkable.
Claims (3)
Priority Applications (1)
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CN201821657064.9U CN209039146U (en) | 2018-10-12 | 2018-10-12 | An Improved Air Supply Type Low Pressure Jet Aerator |
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CN201821657064.9U CN209039146U (en) | 2018-10-12 | 2018-10-12 | An Improved Air Supply Type Low Pressure Jet Aerator |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2737273C1 (en) * | 2020-03-23 | 2020-11-26 | Андрей Леонидович Волков | Volkov's cavitation aerator |
CN112158950A (en) * | 2020-10-15 | 2021-01-01 | 上海复森环境科技发展有限公司 | All-round mixed anaerobic reactor of intermittent type formula |
-
2018
- 2018-10-12 CN CN201821657064.9U patent/CN209039146U/en active Active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2737273C1 (en) * | 2020-03-23 | 2020-11-26 | Андрей Леонидович Волков | Volkov's cavitation aerator |
WO2021194374A1 (en) * | 2020-03-23 | 2021-09-30 | Андрей Леонидович ВОЛКОВ | Volkov cavitational aerator |
CN112158950A (en) * | 2020-10-15 | 2021-01-01 | 上海复森环境科技发展有限公司 | All-round mixed anaerobic reactor of intermittent type formula |
CN112158950B (en) * | 2020-10-15 | 2025-04-15 | 上海复森环境科技发展有限公司 | Intermittent omnibearing Mixed anaerobic reactor |
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Effective date of registration: 20200703 Address after: No. a0705, 7th floor, block B, Kairui, northwest corner of Fengcheng 12th road and Mingguang Road, Xi'an Economic Development Zone, Shaanxi Province 710016 Patentee after: XI AN LONGHUA ENVIRONMENTAL PROT TECHNOLOGY Co.,Ltd. Address before: 710021 Shaanxi province Xi'an Weiyang university campus of Shaanxi University of Science and Technology Patentee before: SHAANXI University OF SCIENCE & TECHNOLOGY |