CN102424470A - Aeration disc and aeration device for treating river water pollution - Google Patents
Aeration disc and aeration device for treating river water pollution Download PDFInfo
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- CN102424470A CN102424470A CN2011103332344A CN201110333234A CN102424470A CN 102424470 A CN102424470 A CN 102424470A CN 2011103332344 A CN2011103332344 A CN 2011103332344A CN 201110333234 A CN201110333234 A CN 201110333234A CN 102424470 A CN102424470 A CN 102424470A
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- 238000005273 aeration Methods 0.000 title claims abstract description 71
- 238000003903 river water pollution Methods 0.000 title claims abstract description 7
- 230000007423 decrease Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 21
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 18
- 239000001301 oxygen Substances 0.000 abstract description 18
- 229910052760 oxygen Inorganic materials 0.000 abstract description 18
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 5
- 239000010802 sludge Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- 239000010865 sewage Substances 0.000 description 9
- 244000005700 microbiome Species 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000004065 wastewater treatment Methods 0.000 description 5
- 239000012071 phase Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000006864 oxidative decomposition reaction Methods 0.000 description 3
- 101150006573 PAN1 gene Proteins 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 230000001706 oxygenating effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 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
Description
技术领域 technical field
本发明涉及一种曝气装置,尤其涉及一种河道水污染治理的曝气盘及曝气装置。The invention relates to an aeration device, in particular to an aeration pan and an aeration device for controlling river water pollution.
背景技术 Background technique
自1912年英国的克拉克和盖奇发现,对污水长时间曝气会产生污泥,同时水质得到明显改善,活性污泥法就和废水处理紧密联系起来。美国约有废水处理厂18000座,其中84%为二级生物处理厂。英国共有处理厂约3000座,几乎全是二级生物处理厂,日本有城市废水处理厂630座,村镇废水处理厂2000座,其中二级处理厂和高级处理厂占98%左右。瑞典人口不足千万,但有1540座城市废水处理厂,其中91%为二级生物处理厂。在发达国家普遍采用的二级生物处理流程中,尤以活性污泥法的应用最广。Since Clark and Gage in the UK discovered in 1912 that long-term aeration of sewage would produce sludge and the water quality would be significantly improved, the activated sludge method has been closely linked with wastewater treatment. There are about 18,000 wastewater treatment plants in the United States, 84% of which are secondary biological treatment plants. There are about 3,000 treatment plants in the UK, almost all of which are secondary biological treatment plants. Japan has 630 urban wastewater treatment plants and 2,000 village wastewater treatment plants, of which secondary treatment plants and advanced treatment plants account for about 98%. Sweden has a population of less than 10 million, but there are 1,540 municipal wastewater treatment plants, 91% of which are secondary biological treatment plants. Among the secondary biological treatment processes commonly used in developed countries, the activated sludge method is the most widely used.
活性污泥法的一个基本要素就是溶解氧,没有充足的溶解氧,好氧微生物就不能发挥氧化分解作用,溶解氧制约了活性污泥法的处理效果。而在一个典型的污水处理厂,曝气耗费往往占运行费用的60~80%。传统的曝气设备效率过低,曝气池运行的控制不佳都使曝气的能耗难以下降。并且随着季节、服务区域内经济发展,污水处理厂进水的组成都有很大的变化,但是现行的污水处理厂大多没有针对水质变动调整曝气量,从而会出现曝气不足导致出水的处理效果不好,曝气过度导致能量浪费,运行成本的浪费。因此,曝气量控制的好坏决定了活性污泥法的处理效果和运行能耗。One of the basic elements of the activated sludge method is dissolved oxygen. Without sufficient dissolved oxygen, aerobic microorganisms cannot perform oxidative decomposition, and dissolved oxygen restricts the treatment effect of the activated sludge method. In a typical sewage treatment plant, the cost of aeration often accounts for 60-80% of the operating cost. The efficiency of traditional aeration equipment is too low, and the poor control of the operation of the aeration tank makes it difficult to reduce the energy consumption of aeration. And with the seasons and economic development in the service area, the composition of the influent water of sewage treatment plants has changed greatly. However, most of the current sewage treatment plants have not adjusted the aeration volume in response to changes in water quality, so that insufficient aeration will lead to effluent problems. The treatment effect is not good, and excessive aeration leads to waste of energy and waste of operating costs. Therefore, the quality of aeration control determines the treatment effect and operating energy consumption of the activated sludge process.
分析导致需氧量变化的因素,找到影响曝气氧传质的因子,解决进水水质变化导致的需氧量的变化,把溶解氧控制在满足生物需要的最佳范围内,用最小的能耗达到生物活动的需求。开发高效低耗的曝气设备,掌握不同废水及操作条件对氧传质的影响,因地制宜,能够根据进水水质的不同自动调整曝气量,使得既保证溶解氧需求,又尽可能地降低能耗,是环境工作的重要研究任务之一。Analyze the factors that lead to the change of oxygen demand, find out the factors that affect the mass transfer of aeration oxygen, solve the change of oxygen demand caused by the change of influent water quality, control the dissolved oxygen in the optimal range that meets the biological needs, and use the minimum energy Consumption to meet the needs of biological activities. Develop high-efficiency and low-consumption aeration equipment, grasp the influence of different wastewater and operating conditions on oxygen mass transfer, adapt measures to local conditions, and automatically adjust the aeration volume according to the different influent water quality, so as to ensure the demand for dissolved oxygen and reduce energy consumption as much as possible. Energy consumption is one of the important research tasks of environmental work.
活性污泥法曝气基本物理化学模型就是三相流模型,它有三个基本要素,一是引起吸附和氧化分解作用的微生物,也就是活性污泥颗粒(固相);二是废水中的有机物和溶解氧(液相);三是溶解氧的主要来源,水中的微气泡(气相)。没有充足的溶解氧,好氧微生物就不能发挥好氧性氧化分解作用。因此一个有效的处理工艺,就必须使微生物,有机物和氧充分接触,只有这样才能使三相相互作用,达到处理各种有机物的目的。因而在充氧的同时,必须使活性污泥颗粒处于悬浮状态。充氧和混合是通过曝气设备来实现的。The basic physical and chemical model of activated sludge aeration is the three-phase flow model, which has three basic elements, one is the microorganisms that cause adsorption and oxidative decomposition, that is, activated sludge particles (solid phase); the other is the organic matter in wastewater and dissolved oxygen (liquid phase); the third is the main source of dissolved oxygen, microbubbles in water (gas phase). Without sufficient dissolved oxygen, aerobic microorganisms cannot perform aerobic oxidative decomposition. Therefore, an effective treatment process must fully contact microorganisms, organic matter and oxygen. Only in this way can the three-phase interaction be achieved to achieve the purpose of treating various organic matter. Therefore, while oxygenating, the activated sludge particles must be suspended. Oxygenation and mixing are achieved through aeration equipment.
曝气机作为一种有效的污水处理设备己得到了推广,它的主要功能是向污水中充入空气,同时使固、液、气三相充分混合,在水循环过程中,使空气中的氧溶入水中,并和有机物、微生物充分接触、混合,供微生物呼吸,使有机物得到氧化,从而改善了被污染的生态环境,使水质净化,创造出适合生物生长的环境。同时,污水处理厂的电能主要消耗在二级生化处理活性污泥曝气工艺上,在各种生化处理过程中,曝气技术作为一种不可或缺的环节,它的好坏不仅影响污水生化处理效果,而且直接影响污水厂的运行费用。而且曝气池引起的二次污染及其占地也不容忽视。因此,如何提高曝气中的氧传质效率,减小曝气池的占地面积,降低二次污染便引起了有关专业人士的重视。The aerator has been promoted as an effective sewage treatment equipment. Its main function is to fill the sewage with air, and at the same time fully mix the solid, liquid, and gas phases. During the water cycle, the oxygen in the air Dissolve in water, fully contact and mix with organic matter and microorganisms, for the respiration of microorganisms, and oxidize organic matter, thereby improving the polluted ecological environment, purifying water quality, and creating an environment suitable for biological growth. At the same time, the electric energy of the sewage treatment plant is mainly consumed in the secondary biochemical treatment activated sludge aeration process. In various biochemical treatment processes, aeration technology is an indispensable link, and its quality not only affects sewage biochemical Treatment effect, and directly affect the operating cost of the sewage plant. Moreover, the secondary pollution caused by the aeration tank and its land occupation cannot be ignored. Therefore, how to improve the oxygen mass transfer efficiency in aeration, reduce the floor area of the aeration tank, and reduce secondary pollution has attracted the attention of relevant professionals.
发明内容 Contents of the invention
本发明提供了一种河道水污染治理的曝气盘,该曝气盘结构简单,能使周围水体形成涡流,对水体充氧效率高。The invention provides an aeration pan for controlling river water pollution. The aeration pan has a simple structure, can form a vortex in the surrounding water body, and has high oxygenation efficiency for the water body.
一种河道水污染治理的曝气盘,包括支架、固定在所述支架上的至少三根处于同一平面的环形软管以及一根与所有环形软管连通的输气管,所述的环形软管的管壁上设有曝气孔。An aeration pan for river water pollution control, comprising a bracket, at least three annular hoses fixed on the bracket on the same plane, and an air pipe communicating with all the annular hoses, the annular hoses Aeration holes are arranged on the pipe wall.
所述的曝气孔在环形软管的管壁上呈线性蜂窝状分布。The aeration holes are distributed in a linear honeycomb shape on the pipe wall of the annular hose.
所有环形软管为圆形,且同心设置。All annular hoses are circular and arranged concentrically.
所述的支架为由四根通过环形软管中心的支架杆组成的米字型支架。The support is a rice-shaped support composed of four support rods passing through the center of the annular hose.
所述的曝气孔从靠近环形软管内腔的一端向外孔径逐渐减小,可以进一步避免污泥倒灌堵塞曝气孔。The diameter of the aeration hole gradually decreases from the end close to the inner cavity of the annular hose to the outside, which can further prevent the sludge from pouring back and blocking the aeration hole.
所述的曝气孔的孔径小于1mm,微孔曝气产生的气泡小,比表面积大,使供气量可变可调,同时氧溶解效率高,可满足大量高密度的优势菌群活动耗氧需求,曝气效率提高至原来的5倍。The pore size of the aeration hole is less than 1mm, the air bubbles produced by the micropore aeration are small, the specific surface area is large, the air supply volume is variable and adjustable, and the oxygen dissolution efficiency is high, which can meet the activity consumption of a large number of high-density dominant bacteria. Oxygen demand, aeration efficiency increased to 5 times the original.
所述的环形软管的管壁厚度为2~3mm。The wall thickness of the annular hose is 2-3 mm.
本发明还提供了一种曝气装置,包括上述曝气盘和涡轮风机,所述涡轮风机的出风口与所述输气管的进气端连通。The present invention also provides an aeration device, comprising the above-mentioned aeration pan and a turbo blower, the air outlet of the turbo blower communicates with the air inlet end of the air delivery pipe.
本发明曝气盘在曝气向水体充氧时,气体扩散在其周边形成涡流,同时上下层水体之间的发生对流,使得水体复氧加快,降低了能耗。When the aeration plate of the present invention aerates and oxygenates the water body, the gas diffuses to form a vortex around it, and at the same time convection occurs between the upper and lower water bodies, so that the reoxygenation of the water body is accelerated and the energy consumption is reduced.
本发明软管在曝气时鼓胀,曝气孔张开,而停止工作时则由于受静水压力作用曝气孔关闭,在不使用空气过滤设备的情况下可以避免污泥将其堵塞,结构简化。The flexible hose of the present invention bulges during aeration, and the aeration holes open, and when it stops working, the aeration holes are closed due to hydrostatic pressure, so that it can be prevented from being blocked by sludge without using air filtering equipment, and the structure is simplified .
附图说明 Description of drawings
图1为本发明曝气盘的结构示意图;Fig. 1 is the structural representation of aeration tray of the present invention;
图2为本发明装置中软管的径向截面图;Fig. 2 is the radial sectional view of flexible pipe in the device of the present invention;
图3为本发明曝气装置的结构示意图。Fig. 3 is a schematic structural view of the aeration device of the present invention.
具体实施方式 Detailed ways
如图1所示,一种河道水污染治理的曝气盘,包括米字型的支架102和以及固定在支架102上六个同心设置的环形软管101,环形软管101为圆形,管壁设有呈线性蜂巢状分布的曝气孔104,还包括一根与所有环形软管101连通的输气管103,输气管103沿环形软管101直径方向设置。软管可以选用如PE、PVC等材料制成。As shown in Figure 1, an aeration pan for river water pollution control includes a rice-
如图2所示的环形软管的径向截面,曝气孔104从靠近环形软管101内腔的一端向外孔径逐渐减小,且最大孔径不大于1mm,环形软管101的管壁厚度为3mm,根据需要可以调整为2~3mm。As shown in the radial section of the annular hose in Figure 2, the diameter of the
如图3所示,一种包含上述曝气盘的曝气装置,它包括曝气盘1和涡轮风机2,输气管103的进气端与涡轮风机2的出风口连通,本实施例涡轮风机2采用涡轮增压发动机驱动,动力强劲。As shown in Figure 3, a kind of aeration device that comprises above-mentioned aeration disc, it comprises
工作时,涡轮风机2通过输气管103向曝气盘1送入高压空气,软管涨开,并使曝气孔104扩大,气体从曝气孔104冲出后形成气泡,气泡直径在1~3mm,比表面积大,供气量可变可调,曝气效率也大幅度提高。When working, the
在空气从曝气孔冲出后,由于环形软管101的作用,使得曝气盘1周围的水体形成涡流,增强了上下层水体的对流,增加了水体复氧能力。After the air is flushed out from the aeration hole, due to the action of the
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102674533A (en) * | 2012-05-10 | 2012-09-19 | 武汉市政工程设计研究院有限责任公司 | Rotary microporous aeration circular coil system for treating sewage |
CN103818997A (en) * | 2013-12-31 | 2014-05-28 | 北京清大国华环保科技有限公司 | Method and device of composite aeration MBR (membrane bio-reactor) |
CN105104287A (en) * | 2015-08-17 | 2015-12-02 | 太仓市璜泾大文特种水产养殖专业合作社 | Oxygenation device for culturing soft-shelled turtles |
CN105417745A (en) * | 2015-12-21 | 2016-03-23 | 津水华清(天津)膜科技有限公司 | High-effective aeration pipeline |
CN108314178A (en) * | 2017-01-17 | 2018-07-24 | 中国石化集团四川维尼纶厂 | A kind of aeration tube assembly of polyvinyl alcohol immobilized microorganism Gel Treatment sewage |
CN110759494A (en) * | 2019-12-17 | 2020-02-07 | 四川捷途环保服务有限公司 | A aeration equipment for river course desilting |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2235967Y (en) * | 1995-12-03 | 1996-09-25 | 抚顺石油化工公司石油二厂 | Energy-saving blowing aerating dirt-water biochemical treatment device |
CN201334393Y (en) * | 2009-01-20 | 2009-10-28 | 达斯玛环境科技(北京)有限公司 | Perforated aerator pipe applied to sewage water biochemical treatment |
CN202265456U (en) * | 2011-10-28 | 2012-06-06 | 浙江工商大学 | Aeration disc and aeration device for water pollution regulation of riverways |
-
2011
- 2011-10-28 CN CN2011103332344A patent/CN102424470B/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2235967Y (en) * | 1995-12-03 | 1996-09-25 | 抚顺石油化工公司石油二厂 | Energy-saving blowing aerating dirt-water biochemical treatment device |
CN201334393Y (en) * | 2009-01-20 | 2009-10-28 | 达斯玛环境科技(北京)有限公司 | Perforated aerator pipe applied to sewage water biochemical treatment |
CN202265456U (en) * | 2011-10-28 | 2012-06-06 | 浙江工商大学 | Aeration disc and aeration device for water pollution regulation of riverways |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102674533A (en) * | 2012-05-10 | 2012-09-19 | 武汉市政工程设计研究院有限责任公司 | Rotary microporous aeration circular coil system for treating sewage |
CN103818997A (en) * | 2013-12-31 | 2014-05-28 | 北京清大国华环保科技有限公司 | Method and device of composite aeration MBR (membrane bio-reactor) |
CN105104287A (en) * | 2015-08-17 | 2015-12-02 | 太仓市璜泾大文特种水产养殖专业合作社 | Oxygenation device for culturing soft-shelled turtles |
CN105417745A (en) * | 2015-12-21 | 2016-03-23 | 津水华清(天津)膜科技有限公司 | High-effective aeration pipeline |
CN108314178A (en) * | 2017-01-17 | 2018-07-24 | 中国石化集团四川维尼纶厂 | A kind of aeration tube assembly of polyvinyl alcohol immobilized microorganism Gel Treatment sewage |
CN110759494A (en) * | 2019-12-17 | 2020-02-07 | 四川捷途环保服务有限公司 | A aeration equipment for river course desilting |
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