CN201128697Y - Membrane method bubble-free aerator - Google Patents
Membrane method bubble-free aerator Download PDFInfo
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- CN201128697Y CN201128697Y CNU2007200304642U CN200720030464U CN201128697Y CN 201128697 Y CN201128697 Y CN 201128697Y CN U2007200304642 U CNU2007200304642 U CN U2007200304642U CN 200720030464 U CN200720030464 U CN 200720030464U CN 201128697 Y CN201128697 Y CN 201128697Y
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- 239000012528 membrane Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 29
- 238000005276 aerator Methods 0.000 title abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000004140 cleaning Methods 0.000 claims abstract description 41
- 238000005273 aeration Methods 0.000 claims abstract description 34
- 238000004506 ultrasonic cleaning Methods 0.000 claims abstract description 17
- 239000000835 fiber Substances 0.000 claims description 9
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 5
- 239000008358 core component Substances 0.000 claims description 4
- 239000003822 epoxy resin Substances 0.000 claims description 4
- 229920000647 polyepoxide Polymers 0.000 claims description 4
- 239000003292 glue Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000002000 scavenging effect Effects 0.000 claims 5
- 125000004122 cyclic group Chemical group 0.000 claims 3
- 210000000056 organ Anatomy 0.000 claims 2
- 230000000241 respiratory effect Effects 0.000 claims 2
- 238000007654 immersion Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 47
- 238000006213 oxygenation reaction Methods 0.000 abstract description 26
- 239000010865 sewage Substances 0.000 abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 6
- 239000000306 component Substances 0.000 description 11
- 239000012510 hollow fiber Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000010802 sludge Substances 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 238000011161 development Methods 0.000 description 4
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- 238000007254 oxidation reaction Methods 0.000 description 3
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- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
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- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
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- 229920000642 polymer Polymers 0.000 description 1
- 238000011160 research Methods 0.000 description 1
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- 239000000126 substance Substances 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 238000004065 wastewater treatment 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
膜法无泡曝气机,属于污水处理设备技术领域,包括无泡曝气膜片组、液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统、机座及支架;无泡曝气膜片组安装固定在液体充氧循环系统的水箱内,液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统分别安装固定在支架、机座上。本实用新型具有自动化程度高、溶氧效率高、能源消耗低、造价低、在线膜片清洗彻底的特点。
The membrane method bubble-free aerator belongs to the technical field of sewage treatment equipment, including a bubble-free aeration diaphragm group, a liquid oxygenation circulation system, an air supply system, an online ultrasonic cleaning system for the diaphragm, an electrical control system, a base and a bracket; The bubble-free aeration diaphragm group is installed and fixed in the water tank of the liquid oxygenation circulation system, and the liquid oxygenation circulation system, air supply system, diaphragm online ultrasonic cleaning system, and electrical control system are respectively installed and fixed on the bracket and machine base. The utility model has the characteristics of high degree of automation, high efficiency of dissolved oxygen, low energy consumption, low cost and thorough online membrane cleaning.
Description
技术领域technical field
本实用新型涉及一种膜法无泡曝气机,属于污水处理设备技术领域。The utility model relates to a membrane method bubble-free aerator, which belongs to the technical field of sewage treatment equipment.
背景技术Background technique
水资源匮乏是我国的基本国情,随着国民经济的持续快速发展,水资源紧缺以及工业废水、生活污水对环境的污染越来越成为亟待解决的重要课题,为此,我国将环境治理和环境保护作为一项基本国策纳入法制管理体系。开源节流、治理污染,也已成为各级政府工作的重要任务之一。因而,这就迫切期待适合时代发展、符合我国国情的污水资源处理再利用技术及其装备的创新开发应用,以缓解水资源的短缺和环境的保护。20世纪80年代以来,人们就一直探索和研究污水处理和再利用问题。其中,污水生物处理新工艺与新技术的研究、开发和应用,已在全球范围内得到很快的发展,并出现了很多新的污水生物处理工艺技术。例如活性污泥法、接触氧化法、氧化沟法、兼氧水解工艺及以上各类工艺的组合工艺等,这些技术大部分已在我国各地的工程实践中得到广泛的应用。目前常用的污水处理技术主要有“活性污泥法”等,但这些方法存在处理效率低、能耗高等缺点。在已有的污水处理大多采用二级处理工艺,即污水通过粗隔栅、集水调节池、沉砂池、絮凝沉淀池、活性污泥曝气池、二级沉淀池后进行排水。The scarcity of water resources is the basic national condition of our country. With the sustained and rapid development of the national economy, the shortage of water resources and the pollution of the environment by industrial wastewater and domestic sewage have become more and more important issues to be solved urgently. For this reason, my country will integrate environmental governance and environmental Protection is included in the legal management system as a basic national policy. It has also become one of the important tasks of governments at all levels to increase revenue and reduce expenditure and control pollution. Therefore, it is urgent to look forward to the innovative development and application of sewage resource treatment and reuse technology and equipment suitable for the development of the times and in line with my country's national conditions, so as to alleviate the shortage of water resources and protect the environment. Since the 1980s, people have been exploring and researching the problem of sewage treatment and reuse. Among them, the research, development and application of new processes and technologies for sewage biological treatment have been rapidly developed around the world, and many new sewage biological treatment process technologies have emerged. For example, activated sludge method, contact oxidation method, oxidation ditch method, facultative hydrolysis process and the combination of the above processes, etc. Most of these technologies have been widely used in engineering practice in various parts of our country. At present, the commonly used sewage treatment technologies mainly include "activated sludge method", etc., but these methods have disadvantages such as low treatment efficiency and high energy consumption. Most of the existing sewage treatment adopts the secondary treatment process, that is, the sewage is drained after passing through the coarse screen, the water collection adjustment tank, the grit chamber, the flocculation sedimentation tank, the activated sludge aeration tank, and the secondary sedimentation tank.
活性污泥法污水处理工艺的核心处理单元是活性污泥曝气池(好氧氧化反应池)。它是通过有泡曝气来强化氧气溶解到污泥混合液中,供好氧微生物用于降解污水中的有机物。对于污水中可溶性快速降解COD,很容易除去,而对于不溶性及难溶性物质所造成的COD,却很难除去,为了去除这部分COD,必须经过长时间的曝气,其结果使处理设施的占地面积、基建投资和运行费用大大增加。在目前普遍采用的有泡曝气法中,无论是穿孔曝气还是微孔曝气,都存在着较多的缺点:(1)有泡曝气法是通过气泡的不断产生,以扩大气泡与液体的接触时间与面积,实现提高水液体中溶解氧浓度,但由于气泡与液体界面阻力的作用,氧气利用效率低、能耗高;(2)活性污泥曝气池在处理含有易挥发性或含硫化合物的污水时,由于强烈的有泡曝气作用,使挥发性气体上升到水面后又进入空气,造成空气污染,造成治理不彻底的结果;(3)除上述有泡曝气法的缺点外,对于我们已申报的“膜式充氧装置”(专利申请号:200720019241.6)经实践发现也存在有中空纤维膜在线清洗不清洁,影响其溶氧性能和应用效率,和采用柱式圆筒形膜组件造价高等缺陷。The core treatment unit of the activated sludge sewage treatment process is the activated sludge aeration tank (aerobic oxidation reaction tank). It uses bubble aeration to enhance the dissolution of oxygen into the sludge mixture, which is used by aerobic microorganisms to degrade organic matter in sewage. It is easy to remove the soluble and fast-degradable COD in sewage, but it is difficult to remove the COD caused by insoluble and insoluble substances. In order to remove this part of COD, it must be aerated for a long time. The land area, infrastructure investment and operating costs have greatly increased. In the bubble aeration method commonly used at present, both perforated aeration and microporous aeration have many disadvantages: (1) The bubble aeration method uses the continuous generation of bubbles to expand the size of the bubbles and The contact time and area of the liquid can increase the concentration of dissolved oxygen in the water liquid, but due to the effect of air bubbles and liquid interface resistance, the oxygen utilization efficiency is low and the energy consumption is high; (2) The activated sludge aeration tank contains volatile or sewage containing sulfur compounds, due to the strong bubble aeration, the volatile gas rises to the water surface and then enters the air, causing air pollution and resulting in incomplete treatment; (3) In addition to the above-mentioned bubble aeration method In addition to the shortcomings of the "membrane oxygenation device" that we have declared (patent application number: 200720019241.6), it has been found through practice that the hollow fiber membrane is not cleaned online, which affects its oxygen dissolution performance and application efficiency. Cylindrical membrane modules have disadvantages such as high cost.
发明内容Contents of the invention
针对以上现有产品技术缺陷,本实用新型提供一种自动化程度高、溶氧效率高、能源消耗低、造价低、在线膜片清洗彻底的膜法无泡曝气机。Aiming at the technical defects of the above existing products, the utility model provides a membrane method bubble-free aerator with high degree of automation, high efficiency of dissolved oxygen, low energy consumption, low cost, and thorough online membrane cleaning.
一种膜法无泡曝气机,包括无泡曝气膜片组、液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统、机座及支架;无泡曝气膜片组安装固定在液体充氧循环系统的水箱内,液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统分别安装固定在支架、机座上。A membrane method bubble-free aerator, including a bubble-free aeration membrane group, a liquid oxygenation circulation system, an air supply system, an online ultrasonic cleaning system for the membrane, an electrical control system, a machine base and a bracket; the bubble-free aeration membrane The film group is installed and fixed in the water tank of the liquid oxygenation circulation system, and the liquid oxygenation circulation system, air supply system, diaphragm online ultrasonic cleaning system, and electrical control system are respectively installed and fixed on the bracket and machine base.
所述的无泡曝气膜片组是膜法无泡曝气机的核心部件,其结构为帘形浸没式,每一膜片由数十至数百根中空纤维膜组成纤维束,并由若干纤维束组成,各纤维束通过环氧树脂胶与特制管件粘结,上下两端对称,结构相同;每根中空纤维膜的中心孔和特制管件的中心孔垂直相交并相通,构成对膜片的进气和出气通道。The bubble-free aeration membrane group is the core component of the membrane-type bubble-free aerator, and its structure is a curtain-shaped submerged type. Each membrane is composed of tens to hundreds of hollow fiber membranes to form fiber bundles, and is composed of Composed of a number of fiber bundles, each fiber bundle is bonded to a special pipe fitting through epoxy resin glue, the upper and lower ends are symmetrical, and the structure is the same; the center hole of each hollow fiber membrane and the center hole of the special pipe fitting are vertically intersected and communicated to form a diaphragm inlet and outlet channels.
所述的液体充氧循环系统由污水泵、电磁阀、循环水箱、手动截止阀和相应管道组成,污水泵安装固定在机座上,循环水箱安装固定在机座上面的支架上,电磁阀、手动截止阀安装在系统管道上。The liquid oxygenation circulation system is composed of a sewage pump, a solenoid valve, a circulating water tank, a manual stop valve and corresponding pipelines. The sewage pump is installed and fixed on the machine base, and the circulating water tank is installed and fixed on the bracket above the machine base. The solenoid valve, A manual shut-off valve is installed on the system piping.
所述的空气供给系统由空气压缩泵、空气处理器、压力表、节流阀和相应管路组成,空气压缩泵、空气处理器分别安装固定在机座上,空气压缩泵的出气口装有空气处理器,压缩空气通过膜片组后的管路上安装有节流阀,用于调节系统压缩空气工作压力,在通气管路与膜片组连接的前后端装有压力表。The air supply system is composed of an air compression pump, an air processor, a pressure gauge, a throttle valve and corresponding pipelines. The air compression pump and the air processor are respectively installed and fixed on the base, and the air outlet of the air compression pump is equipped with For the air processor, a throttle valve is installed on the pipeline after the compressed air passes through the diaphragm group, which is used to adjust the working pressure of the compressed air in the system, and a pressure gauge is installed at the front and rear ends of the ventilation pipeline connected to the diaphragm group.
所述的膜片在线超声波清洗系统由清洗泵、超声波换能器、电磁阀、清洗水箱、液位计、呼吸器、排污阀和相应管路组成,清洗泵通过其连接管路悬空安装在清洗水箱的下部,清洗水箱安装固定在机座上面的支架上,清洗泵的清洗液进出口管路上装有四个控制清洗液在清洗箱和循环水箱间的流向转换的电磁阀,清洗箱上还装有液位计、呼吸器、排污阀;在清洗水箱的顶部还装有绿、黄、红三色信号灯。The diaphragm on-line ultrasonic cleaning system is composed of a cleaning pump, an ultrasonic transducer, a solenoid valve, a cleaning water tank, a liquid level gauge, a respirator, a sewage valve and corresponding pipelines. The lower part of the water tank, the cleaning water tank is installed and fixed on the bracket above the base, and the cleaning liquid inlet and outlet pipelines of the cleaning pump are equipped with four solenoid valves that control the flow direction conversion of the cleaning liquid between the cleaning tank and the circulating water tank. It is equipped with a liquid level gauge, a respirator, and a drain valve; there are also green, yellow, and red signal lights on the top of the cleaning water tank.
所述的电气控制系统由控制箱和电器元件箱两部分组成,它们列安装在机座上的支架中,控制箱装有压力表、控制按钮、指示灯以及微电脑控制器;电器元件箱装有动力电器元件、超声波发生器、PLC控制器和电器保护元件。The electrical control system is composed of two parts, the control box and the electrical component box, which are installed in the bracket on the machine base. The control box is equipped with pressure gauges, control buttons, indicator lights and microcomputer controllers; the electrical component box is equipped with Power electrical components, ultrasonic generators, PLC controllers and electrical protection components.
本实用新型的创新点主要有以下五个方面:The innovation of the utility model mainly contains the following five aspects:
1、采用高分子强疏水性中空纤维膜材料及其气体分离特性,制成帘形浸没式膜片组件,实现单位体积膜表面积大、膜的气通量高、以及制造价格低的目的。同时在使用时膜纤维可随水流在循环水箱中飘动,能有效地改善液相传质过程,又能减少膜外侧表面沉积物的污染。1. Using polymer strong hydrophobic hollow fiber membrane material and its gas separation characteristics to make a curtain-shaped submerged membrane module to achieve the purpose of large membrane surface area per unit volume, high gas flux of the membrane, and low manufacturing price. At the same time, the membrane fiber can float in the circulating water tank with the water flow during use, which can effectively improve the mass transfer process of the liquid phase and reduce the pollution of sediments on the outer surface of the membrane.
2、应用无泡充氧技术,既解决了有泡曝气所带来的二次空气环境污染,同时也极大地提高了液体溶氧效率。适用于各种水深的水产养殖和工业废水、生活污水处理中的无泡充氧。膜法无泡曝气机完全不同于其它各种传统曝气设备必须产生气泡与液体接触而实施充氧的方式,可实现100%的溶氧率,较有泡充氧充氧率提高8倍以上。2. The application of bubble-free oxygenation technology not only solves the secondary air environmental pollution caused by bubble aeration, but also greatly improves the efficiency of liquid oxygen dissolution. It is suitable for bubble-free oxygenation in aquaculture, industrial wastewater and domestic sewage treatment of various water depths. Membrane bubble-free aerator is completely different from other traditional aeration equipment, which must generate bubbles and contact with liquid to carry out oxygenation. It can achieve 100% dissolved oxygen rate, which is 8 times higher than that of bubble oxygenation. above.
3、本实用新型的液体充氧循环系统采用自溢式回水设计,可最大限度的实现对液体的充氧效果。既被处理液体经污水泵从循环水箱的底部进入,在水面达到水箱顶部靠自溢进入回水管,而后排入曝气池,这样液体在循环水箱中由于没有污水泵产生的压力作用,所以箱内水流相对平缓,增加了对液体的充氧时间,有利于液体的充分氧合。3. The liquid oxygenation circulation system of the utility model adopts a self-overflow return water design, which can realize the oxygenation effect on the liquid to the greatest extent. The liquid to be treated enters from the bottom of the circulating water tank through the sewage pump, reaches the top of the water tank on the water surface and enters the return pipe by self-overflow, and then is discharged into the aeration tank. The inner water flow is relatively gentle, which increases the oxygenation time of the liquid and is conducive to the full oxygenation of the liquid.
4、本实用新型的在线清洗系统采用了超声波清洗设计,有效地解决了膜组件在线清洗不彻底的技术难题,可长期保持中空纤维膜良好的气体分离特性,从而实现其长期的充氧能力。4. The online cleaning system of this utility model adopts the ultrasonic cleaning design, which effectively solves the technical problem of incomplete online cleaning of the membrane module, and can maintain the good gas separation characteristics of the hollow fiber membrane for a long time, thereby realizing its long-term oxygenation capacity.
5、本实用新型运行过程中无任何物资的相变,而且在电器控制方面应用微电脑控制,自动化程度高,可最大限度的降低能源消耗,节电达60%以上,能大幅度地降低废水处理成本,以提高运营企业的经济效益和社会效益。5. There is no phase change of any materials during the operation of the utility model, and the application of microcomputer control in electrical control has a high degree of automation, which can minimize energy consumption, save electricity by more than 60%, and can greatly reduce waste water treatment. Cost, in order to improve the economic and social benefits of operating enterprises.
本实用新型的膜法无泡曝气机通过以下措施实现:The membrane method bubble-free aerator of the utility model is realized through the following measures:
无泡曝气膜片组:该件是膜法无泡曝气机的核心部件,其结构为帘形浸没式,其作用是有条件的把空气中的氧气分离出来并溶入到它周围的液体中。Bubble-free aeration diaphragm group: This piece is the core component of the membrane-type non-bubble aerator. Its structure is a curtain-shaped submerged type, and its function is to conditionally separate the oxygen in the air and dissolve it into its surroundings. in liquid.
液体充氧循环系统:作用是提供一定流量的被处理液体从曝气池里抽出通过循环水箱充氧后返回曝气池,实现液体循环。其中的电磁阀a用于控制循环水箱中液体倒流和便于泵与水箱的连接;电磁阀b用于控制循环水箱中液体在膜片组清洗前充分排放干净;手动截止阀用于控制循环水箱中液体的排放和便于管路的连接。Liquid oxygenation circulation system: the function is to provide a certain flow rate of treated liquid to be pumped out from the aeration tank through the circulating water tank for oxygenation and then return to the aeration tank to realize liquid circulation. The solenoid valve a is used to control the backflow of the liquid in the circulating water tank and facilitate the connection between the pump and the water tank; the solenoid valve b is used to control the liquid in the circulating water tank to be fully discharged before the diaphragm group is cleaned; the manual stop valve is used to control the liquid in the circulating water tank Liquid discharge and easy connection of pipelines.
空气供给系统:作用是提供一定流量和压力的空气通过膜片组件,实现充氧的空气供给。其中的空气处理器,用于对压缩空气进行过滤和在工作环境温度过低时加热;节流阀用于调节系统压缩空气工作压力;压力表用于监视膜片组前后的气体压力。Air supply system: the function is to provide air with a certain flow rate and pressure to pass through the diaphragm assembly to realize oxygenated air supply. The air processor is used to filter the compressed air and heat the working environment when the temperature is too low; the throttle valve is used to adjust the working pressure of the compressed air in the system; the pressure gauge is used to monitor the gas pressure before and after the diaphragm group.
膜片在线超声波清洗系统:作用是提供一定量的清洗液进入循环水箱,并开启超声波清洗膜片组件,实现对膜片组件外表面的在线清洗,以保持膜片组件的良好气体分离特性,在对膜片组件清洗完毕后再重新开启泵组和开关相应的电磁阀,将清洗液抽回到清洗箱。清洗箱上还装有液位计、呼吸器、排污阀,以分别用于监视清洗液的多少,清洗液的正常进入、排出和清洗液污染后的排出。Diaphragm online ultrasonic cleaning system: the function is to provide a certain amount of cleaning liquid into the circulating water tank, and turn on the ultrasonic cleaning of the diaphragm assembly to realize online cleaning of the outer surface of the diaphragm assembly, so as to maintain the good gas separation characteristics of the diaphragm assembly. After cleaning the diaphragm assembly, turn on the pump set and switch the corresponding solenoid valve again, and pump the cleaning liquid back into the cleaning tank. The cleaning tank is also equipped with a liquid level gauge, a respirator, and a drain valve, which are used to monitor the amount of cleaning liquid, the normal entry and discharge of cleaning liquid, and the discharge of cleaning liquid after contamination.
电气控制系统:作用是提供对液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统的自动化控制。该系统分为控制箱和电器元件箱两部分。控制箱上压力表、控制按钮、指示灯、微电脑控制器以及电器元件箱中的动力电器元件、超声波发生器、PLC控制器等,两部分组成完整的电气控制系统。Electrical control system: the role is to provide automatic control of the liquid oxygenation circulation system, air supply system, and diaphragm online ultrasonic cleaning system. The system is divided into two parts, the control box and the electrical component box. The pressure gauge, control button, indicator light, microcomputer controller on the control box and the power electrical components, ultrasonic generator, PLC controller, etc. in the electrical component box form a complete electrical control system.
除此以外,还设有绿、黄、红三色信号灯,指示各系统运行状况。In addition, there are also green, yellow and red signal lights to indicate the operating status of each system.
工作原理:working principle:
本实用新型可实现自动化运行,也可按各系统实现单独控制,分别启动配合运行。自动化运行模式和单独控制运行模式通过转换开关切换控制。The utility model can realize automatic operation, and can also realize individual control according to each system, respectively start and coordinate operation. The automatic operation mode and the individual control operation mode are switched and controlled by a transfer switch.
1、自动化运行模式:各系统按设定的运行程序在微电脑控制器控制下自动运行。按动启动按钮,液体充氧循环系统开启,被处理液体开始被泵入循环水箱,约5分钟后空气供给系统自动开启,为膜片组件供压缩空气,其气体压力由手动节流阀调节,整个设备进入正常运行状态,此时,电磁阀a打开,电磁阀b关闭,绿色信号点亮;在微电脑设定程序控制下,设备在24小时中运行23小时后,液体充氧循环系统和空气供给系统自动停止运行,膜片在线超声波清洗系统开启超声波清洗开始工作,此时,电磁阀c、f打开,电磁阀d、e关闭。清洗1小时后,电磁阀c、f关闭,电磁阀d、e打开,清洗液被从循环水箱抽送回清洗箱,黄色信号点亮;至此完成一个工作循环并自动进入下一个工作循环。在运行过程中如出现系统压力升高、电机过载、管路阻塞等故障时,电气控制系统将自动切断电源并报警,此时红色信号灯电亮。1. Automatic operation mode: each system operates automatically under the control of the microcomputer controller according to the set operation program. Press the start button, the liquid oxygenation circulation system is turned on, and the liquid to be treated starts to be pumped into the circulation water tank. After about 5 minutes, the air supply system is automatically opened to supply compressed air to the diaphragm assembly. The gas pressure is adjusted by the manual throttle valve. The whole equipment enters the normal operation state. At this time, the solenoid valve a is opened, the solenoid valve b is closed, and the green signal is on; under the control of the microcomputer setting program, after the equipment runs for 23 hours in 24 hours, the liquid oxygenation circulation system and the air The supply system stops running automatically, and the diaphragm on-line ultrasonic cleaning system turns on the ultrasonic cleaning to start working. At this time, the solenoid valves c and f are opened, and the solenoid valves d and e are closed. After cleaning for 1 hour, the solenoid valves c and f are closed, the solenoid valves d and e are opened, the cleaning liquid is pumped from the circulating water tank back to the cleaning tank, and the yellow signal lights up; a working cycle is completed and the next working cycle is automatically entered. During the operation, if there are failures such as system pressure rise, motor overload, pipeline blockage, etc., the electrical control system will automatically cut off the power supply and give an alarm, and the red signal light will be on at this time.
2、单独控制运行模式:各系统采用手动控制启动,在欲开启任何系统工作时,可分别手动按动相应按钮启动即可。2. Independent control operation mode: Each system is started by manual control. When you want to start any system, you can manually press the corresponding button to start it.
本实用新型具有自动化程度高、溶氧效率高、能源消耗低、造价低、在线膜片清洗彻底的特点。The utility model has the characteristics of high degree of automation, high efficiency of dissolved oxygen, low energy consumption, low cost and thorough online membrane cleaning.
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为本实用新型的后视图。Fig. 2 is the rear view of the utility model.
图3为本实用新型的工作原理图。Fig. 3 is a working principle diagram of the utility model.
图4为本实用新型的膜片组件的结构示意图。Fig. 4 is a schematic structural diagram of the diaphragm assembly of the present invention.
其中:1、循环水箱,2、膜片组件,3、节流阀,4、呼吸器,5、清洗箱,6、信号灯,7、液位计,8、排污阀,9、电气控制箱,10、机座,11、清洗泵,12、空气处理器,13、空气压缩泵,14、污水泵,15、电磁阀(a、b、c、d、e、f),16、超声波换能器,17、手动截止阀,18、电器元件箱,19、支架,20、压力表,2-1、膜片组件的特制管件,2-2、中空纤维膜,2-3、环氧树脂,A、污水进水口,B、处理后污水出水口。Among them: 1. Circulating water tank, 2. Diaphragm assembly, 3. Throttle valve, 4. Breather, 5. Cleaning box, 6. Signal light, 7. Liquid level gauge, 8. Drainage valve, 9. Electrical control box, 10. Engine base, 11. Cleaning pump, 12. Air processor, 13. Air compressor pump, 14. Sewage pump, 15. Solenoid valve (a, b, c, d, e, f), 16. Ultrasonic transducer Device, 17. Manual shut-off valve, 18. Electrical component box, 19. Bracket, 20. Pressure gauge, 2-1. Special fittings for diaphragm assembly, 2-2. Hollow fiber membrane, 2-3. Epoxy resin, A. Sewage inlet, B. Treated sewage outlet.
具体实施方式Detailed ways
实施例:Example:
本实用新型的结构如图1至图4所示,包括无泡曝气膜片组、液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统、机座及支架等;无泡曝气膜片组安装固定在液体充氧循环系统的水箱内,液体充氧循环系统、空气供给系统、膜片在线超声波清洗系统、电气控制系统分别安装固定在支架、机座上。The structure of the utility model is shown in Figures 1 to 4, including a bubble-free aeration diaphragm group, a liquid oxygenation circulation system, an air supply system, an online ultrasonic cleaning system for the diaphragm, an electrical control system, a base and a bracket, etc.; The bubble-free aeration diaphragm group is installed and fixed in the water tank of the liquid oxygenation circulation system, and the liquid oxygenation circulation system, air supply system, diaphragm online ultrasonic cleaning system, and electrical control system are respectively installed and fixed on the bracket and machine base.
所述的无泡曝气膜片组是实用新型的核心部件,其外形为帘形浸没式,每一膜片组2由数十至数百根中空纤维膜2-2组成纤维束,并由若干纤维束组成,各纤维束通过环氧树脂胶2-3与特制管件2-1粘结,上下两端对称,结构相同。每根中空纤维膜2-2的中心孔和特制管件2-1的中心孔垂直相交并相通,构成对膜片的进气和出气通道。The bubble-free aeration membrane group is the core component of the utility model, and its shape is a curtain-shaped submerged type. Each
所述的液体充氧循环系统由污水泵14、电磁阀15(a、b)、循环水箱1、手动截止阀17和相应管道组成。污水泵14安装固定在机座10上,循环水箱1安装固定在机座10上面的支架19上。其系统管路中装有电磁阀15(a、b)和手动截止阀17。The liquid oxygenation circulation system is composed of a
所述的空气供给系统由空气压缩泵13、空气处理器12、压力表20(共两个)、节流阀3和相应管路组成。空气压缩泵13、空气处理器12分别安装固定在机座10上,压缩空气的出气口装有空气处理器12,管路上安装有节流阀3,在通气管路与膜片组连接的前后端装有压力表20。The air supply system is composed of an
所述的膜片在线超声波清洗系统由清洗泵11、超声波换能器16、电磁阀15(c、d、e、f)、清洗箱5、液位计7、呼吸器4、排污阀8和相应管路组成。清洗泵11通过其连接管路悬空安装在清洗箱5的下部。清洗箱5与循环水箱1一样安装固定在机座10上面的支架19上。清洗泵11的清洗液进出口管路上装有四个电磁阀15(c、d、e、f),清洗箱5上还装有液位计7、呼吸器4、排污阀8。The diaphragm on-line ultrasonic cleaning system consists of cleaning
所述的电气控制系统所述的电气控制系统由控制箱9和电器元件箱18两部分组成。它们垂直并列安装在机座10上的支架19中。控制箱9装有压力表、控制按钮、指示灯以及微电脑控制器等,电器元件箱18装有动力电器元件、超声波发生器、PLC控制器和电器保护元件等,在清洗箱5的顶部装有绿、黄、红三色信号灯6。The electrical control system The electrical control system is composed of two parts, the
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| CNU2007200304642U CN201128697Y (en) | 2007-11-12 | 2007-11-12 | Membrane method bubble-free aerator |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241431A (en) * | 2010-09-27 | 2011-11-16 | 中国人民解放军总装备部航天医学工程研究所 | Oxygen supply device for space wastewater treatment |
| CN102861514A (en) * | 2012-09-25 | 2013-01-09 | 河北科技大学 | Offline cleaning method for removing pollutants of SPG (shirasu porous glass) membrane used in biological wastewater treatment |
| CN103864205A (en) * | 2014-03-18 | 2014-06-18 | 强成诚 | Micro-aeration biological film filler |
| CN103864212A (en) * | 2014-03-18 | 2014-06-18 | 强成诚 | Micro-aeration filler biological membrane type wastewater treatment device |
| CN104876296A (en) * | 2015-04-23 | 2015-09-02 | 浙江海洋学院 | Bubbling machine capable of automatically interrupting after falling down |
| CN105300749A (en) * | 2014-06-09 | 2016-02-03 | 鞍钢股份有限公司 | Pretreatment device and method for detecting chemical oxygen demand of wastewater |
| CN108025257A (en) * | 2015-05-19 | 2018-05-11 | 氧膜有限公司 | For promoting the film connector of the mass transfer in membrane aeration biomembrane reactor (MABR) |
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2007
- 2007-11-12 CN CNU2007200304642U patent/CN201128697Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241431A (en) * | 2010-09-27 | 2011-11-16 | 中国人民解放军总装备部航天医学工程研究所 | Oxygen supply device for space wastewater treatment |
| CN102861514A (en) * | 2012-09-25 | 2013-01-09 | 河北科技大学 | Offline cleaning method for removing pollutants of SPG (shirasu porous glass) membrane used in biological wastewater treatment |
| CN102861514B (en) * | 2012-09-25 | 2014-12-24 | 河北科技大学 | Offline cleaning method for removing pollutants of SPG (shirasu porous glass) membrane used in biological wastewater treatment |
| CN103864205A (en) * | 2014-03-18 | 2014-06-18 | 强成诚 | Micro-aeration biological film filler |
| CN103864212A (en) * | 2014-03-18 | 2014-06-18 | 强成诚 | Micro-aeration filler biological membrane type wastewater treatment device |
| CN105300749A (en) * | 2014-06-09 | 2016-02-03 | 鞍钢股份有限公司 | Pretreatment device and method for detecting chemical oxygen demand of wastewater |
| CN105300749B (en) * | 2014-06-09 | 2018-02-27 | 鞍钢股份有限公司 | Pretreatment device and method for detecting chemical oxygen demand of wastewater |
| CN104876296A (en) * | 2015-04-23 | 2015-09-02 | 浙江海洋学院 | Bubbling machine capable of automatically interrupting after falling down |
| CN104876296B (en) * | 2015-04-23 | 2016-11-09 | 浙江海洋学院 | Fall down self-cutting type bubbling machine |
| CN108025257A (en) * | 2015-05-19 | 2018-05-11 | 氧膜有限公司 | For promoting the film connector of the mass transfer in membrane aeration biomembrane reactor (MABR) |
| CN108025257B (en) * | 2015-05-19 | 2021-09-28 | 氧膜有限公司 | Membrane connector for facilitating mass transfer in membrane-aerated biofilm reactors (MABRs) |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
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Granted publication date: 20081008 Termination date: 20101112 |
