CN203144220U - Gravity type hydraulic aeration fine filter - Google Patents
Gravity type hydraulic aeration fine filter Download PDFInfo
- Publication number
- CN203144220U CN203144220U CN201320139623.8U CN201320139623U CN203144220U CN 203144220 U CN203144220 U CN 203144220U CN 201320139623 U CN201320139623 U CN 201320139623U CN 203144220 U CN203144220 U CN 203144220U
- Authority
- CN
- China
- Prior art keywords
- aeration
- pipe
- tank
- fine filter
- chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005273 aeration Methods 0.000 title claims abstract description 66
- 230000005484 gravity Effects 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 101
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 36
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 36
- 239000001301 oxygen Substances 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 238000000926 separation method Methods 0.000 claims abstract description 16
- 230000007704 transition Effects 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 7
- 229920011532 unplasticized polyvinyl chloride Polymers 0.000 claims description 4
- 230000001174 ascending effect Effects 0.000 claims description 3
- 230000000630 rising effect Effects 0.000 claims description 3
- 238000011001 backwashing Methods 0.000 abstract description 8
- 230000009286 beneficial effect Effects 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 description 44
- 239000012535 impurity Substances 0.000 description 13
- 239000006260 foam Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000001914 filtration Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000013505 freshwater Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000013475 authorization Methods 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 230000009182 swimming Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
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)
Abstract
本实用新型公开了一种重力式水力曝气精滤机,包括一个曝气溶氧箱和设在曝气溶氧箱下端周围的四个精滤罐,曝气溶氧箱内设有进水配水箱、曝气溶氧室和曝气槽,曝气槽下端通过曝气条与进水配水箱、曝气溶氧室分隔,进水配水箱的侧面连接有进水管,曝气溶氧室的下端设有气液分离管,气液分离管内设有上端与曝气溶氧室贯通的气液汇合管,精滤罐内从上到下分别为清水箱、过滤室和集水室,过滤室的顶部设有虹吸管,气液分离管的上端侧面通过连接管与虹吸管连通,过滤室内设有精滤层,集水室与清水箱之间通过反冲管连通,集水室的上端侧面设有出水管。本实用新型具有结构简单、具有自动反冲洗功能,使用维护成本低的有益效果。
The utility model discloses a gravity type hydraulic aeration fine filter machine, which comprises an aeration dissolved oxygen box and four fine filter tanks arranged around the lower end of the aeration dissolved oxygen box. Water distribution tank, aeration and dissolved oxygen chamber and aeration tank. The lower end of the aeration tank is separated from the water inlet distribution tank and aeration and dissolved oxygen chamber by the aeration bar. A gas-liquid separation pipe is provided at the lower end of the gas-liquid separation pipe, and a gas-liquid confluence pipe is provided at the upper end of the gas-liquid separation pipe to connect with the aeration and dissolved oxygen chamber. The fine filter tank is divided into a clean water tank, a filter chamber and a water collection chamber from top to bottom. The top of the chamber is provided with a siphon pipe, the upper side of the gas-liquid separation pipe is connected with the siphon pipe through a connecting pipe, the filter chamber is provided with a fine filter layer, the water collection chamber and the clean water tank are connected through a recoil pipe, and the upper end side of the water collection chamber is provided There is a water outlet. The utility model has the beneficial effects of simple structure, automatic backwashing function and low maintenance cost.
Description
技术领域technical field
本实用新型涉及一种河湖水、游泳池等水体处理设备,尤其涉及一种重力式水力曝气精滤机。The utility model relates to equipment for treating rivers, lakes, swimming pools and other water bodies, in particular to a gravity type hydraulic aeration fine filter.
背景技术Background technique
目前,在游泳池、景观河湖、淡水养殖场、海水淡化、工业循环水和娱乐用水场所,对污水的处理方法通常采用的有两种方式:1、将污水全部排放掉,然后补入干净的水;2、采用过滤设备,将污水中的杂质和有害物质过滤掉,经过循环消毒系统重新利用。第一种方式中,需要定期进行换水,耗费人力物力,成本非常高,在世界缺水的今天,采用第一种方法显然是一种巨大的浪费,因此,现在大多数都采用第二种方式,然而目前市场上流传有很多种污水过滤设备,但是该种污水处理设备结构复杂,成本高,耗电量大,虽然不会浪费水资源,然而污水处理成本很高,过滤设备需要定期清洗,十分麻烦,很难普及和推广使用。At present, in swimming pools, landscape rivers and lakes, freshwater farms, seawater desalination, industrial circulating water and recreational water sites, there are usually two ways to treat sewage: 1. Discharge all the sewage and then fill it with clean water. Water; 2. Use filtering equipment to filter out impurities and harmful substances in the sewage, and reuse them through the circulation disinfection system. In the first method, water needs to be changed regularly, which consumes manpower and material resources, and the cost is very high. In today's world of water shortage, it is obviously a huge waste to adopt the first method. Therefore, most of them now use the second method. However, there are many kinds of sewage filtration equipment in the market, but this kind of sewage treatment equipment has complex structure, high cost, and large power consumption. Although it will not waste water resources, the cost of sewage treatment is very high, and the filtration equipment needs to be cleaned regularly. , very troublesome, difficult to popularize and promote the use of.
例如,中国专利授权公告号:CN2589042Y,授权公告日2003年12月3日,公开了一种污水处理设备,包括污水收集槽、泵、过滤筒、清水槽、清水塔和电脑控制箱,污水收集槽,过滤时,由泵将污水输入污水收集槽中,再由泵将污水收集槽内污水输入过滤筒中过滤杂质,过滤后的清水经过滤筒下方的出水管流入清水槽,清水槽内的清水由泵输入清水塔内,逆洗时,由泵将清水槽内的清水经过滤筒底部的入水管输入过滤筒中,过滤筒内的积存物经污泥排出管输入到沉淀塔中,沉淀塔内的积存物再被泵抽送到暴晒槽内,电脑控制箱对整个设备全面自动控制。该种污水处理设备能有效的处理污水,其不足之处是该种污水处理设备结构复杂,污水的输送、流动都是通过泵带动的,耗电量大,过滤筒需要定期清洗、更换,成本高。For example, the Chinese patent authorization announcement number: CN2589042Y, the date of the authorization announcement was December 3, 2003, which disclosed a sewage treatment equipment, including a sewage collection tank, a pump, a filter cartridge, a clean water tank, a clean water tower and a computer control box. When filtering, the pump will input the sewage into the sewage collection tank, and then the pump will input the sewage in the sewage collection tank into the filter cartridge to filter impurities, and the filtered clean water will flow into the clean water tank through the outlet pipe under the filter cartridge, and the clean water in the clean water tank The pump is input into the clean water tower. When backwashing, the pump sends the clean water in the clear water tank into the filter cartridge through the water inlet pipe at the bottom of the filter cartridge, and the accumulation in the filter cartridge is sent into the sedimentation tower through the sludge discharge pipe. The accumulated material is then pumped into the exposure tank, and the computer control box fully and automatically controls the entire equipment. This kind of sewage treatment equipment can effectively treat sewage. The disadvantage is that the structure of this kind of sewage treatment equipment is complex. The transportation and flow of sewage are driven by pumps, which consume a lot of power. high.
实用新型内容Utility model content
本实用新型为了克服现有技术中的污水处理设备结构复杂,耗电量大,过滤机构需要定期清洗、更换,维护成本高的不足,提供了一种结构简单、具有自动反冲洗功能,使用维护成本低的重力式水力曝气精滤机。In order to overcome the problems of complex structure, high power consumption, regular cleaning and replacement of filter mechanism and high maintenance cost in the existing sewage treatment equipment, the utility model provides a simple structure, automatic backwashing function, easy to use and maintain. Low-cost gravity hydraulic aeration fine filter.
为了实现上述目的,本实用新型采用如下技术方案:In order to achieve the above object, the utility model adopts the following technical solutions:
一种重力式水力曝气精滤机,包括一个曝气溶氧箱和设在曝气溶氧箱下端周围的四个精滤罐,所述的曝气溶氧箱内设有进水配水箱、曝气溶氧室和曝气槽,所述的曝气槽的上端与大气贯通,曝气槽下端通过曝气条与进水配水箱、曝气溶氧室分隔,所述的进水配水箱的侧面连接有进水管,所述的曝气溶氧室的下端设有气液分离管,所述的气液分离管内设有上端与曝气溶氧室贯通的气液汇合管,所述的精滤罐内从上到下分别为清水箱、过滤室和集水室,所述的过滤室的顶部设有虹吸管,所述的气液分离管的上端侧面通过连接管与虹吸管连通,所述的过滤室内设有精滤层,所述的集水室与清水箱之间通过反冲管连通,所述的集水室的上端侧面设有出水管。污水从进水管中进入进水配水箱内,然后经过曝气条进入曝气槽内,污水与外界空气接触,污水中的二氧化碳、氨气、氮气等有害气体从水中逸出,同时空气中的氧气溶解到水中形成溶解氧,污水中的氮、磷、溶解蛋白等有机物被氧气氧化形成泡沫,夹杂着泡沫的污水经过气液汇合筒进入气液分离管内,泡沫浮在水面上然后从连接管处进入过滤室内,泡沫和污水中的固体颗粒被精滤层阻挡,过滤后的水进入集水室并通过反冲管满入清水箱,当清水箱内的清水满了之后从出水管中排出来,这样就实现了污水的过滤处理,随着固体杂质以及氧化后的泡沫积聚在精滤层的顶部,逐渐增大精滤层的水流阻力,从而使得连接管内的水进入过滤室内水位上升满入虹吸管内,随着虹吸管内水位的上升形成虹吸现象,从而处理后的清水逆流反洗过滤介质,随着精滤层内杂质的排出,清水箱内的水位降低,虹吸作用被破坏,滤料自动复位,重新开始过滤污水,整个过程都是自动形成,无需人工控制,因此,该种重力式水力曝气精滤机结构简单,具有自动反冲洗功能,从而有效的使用、维护的成本,污水处理成本低,适用范围很广。A gravity-type hydraulic aeration fine filter, comprising an aeration dissolved oxygen box and four fine filter tanks arranged around the lower end of the aeration dissolved oxygen box, the aeration dissolved oxygen box is provided with a water distribution tank , an aeration dissolved oxygen chamber and an aeration tank, the upper end of the aeration tank is connected to the atmosphere, the lower end of the aeration tank is separated from the water inlet distribution tank and the aeration and dissolved oxygen chamber by an aeration bar, the water inlet distribution The side of the box is connected with a water inlet pipe, and the lower end of the aeration and dissolved oxygen chamber is provided with a gas-liquid separation pipe, and the gas-liquid confluence pipe with the upper end connected with the aeration and dissolved oxygen chamber is arranged inside the gas-liquid separation pipe. The inside of the fine filter tank is respectively a clean water tank, a filter chamber and a water collection chamber from top to bottom. The top of the filter chamber is provided with a siphon pipe, and the upper side of the gas-liquid separation pipe communicates with the siphon pipe through a connecting pipe. The filter chamber is provided with a fine filter layer, the water collection chamber is communicated with the fresh water tank through a recoil pipe, and the upper side of the water collection chamber is provided with a water outlet pipe. Sewage enters the water distribution tank from the water inlet pipe, and then enters the aeration tank through the aeration bar. The sewage is in contact with the outside air, and harmful gases such as carbon dioxide, ammonia, and nitrogen in the sewage escape from the water, and at the same time, the pollutants in the air Oxygen dissolves into the water to form dissolved oxygen. Nitrogen, phosphorus, dissolved protein and other organic matter in the sewage are oxidized by oxygen to form foam. The sewage mixed with foam enters the gas-liquid separation pipe through the gas-liquid confluence cylinder. The foam floats on the water surface and then flows from the connecting pipe. The solid particles in the foam and sewage are blocked by the fine filter layer. The filtered water enters the water collection chamber and fills the clean water tank through the recoil pipe. When the clean water in the clean water tank is full, it is discharged from the outlet pipe. With the accumulation of solid impurities and oxidized foam on the top of the fine filter layer, the water flow resistance of the fine filter layer gradually increases, so that the water in the connecting pipe enters the filter chamber and the water level rises to full As the water level in the siphon rises, a siphon phenomenon is formed, so that the treated clean water counterflows and backwashes the filter medium. With the discharge of impurities in the fine filter layer, the water level in the clean water tank decreases, and the siphon effect is destroyed. Automatically reset and restart to filter sewage. The whole process is formed automatically without manual control. Therefore, this gravity-type hydraulic aeration fine filter has a simple structure and automatic backwashing function, so that the cost of effective use and maintenance is reduced. The processing cost is low and the application range is very wide.
作为优选,所述的精滤层的下侧设有精密滤板。污水经过精滤层的过滤后,然后通过精密滤板二次过滤,防止精滤层被杂质渗透后,杂质会直接进入集水室、清水箱内,保证良好的污水处理效果。Preferably, a precision filter plate is provided on the lower side of the fine filter layer. After the sewage is filtered through the fine filter layer, it is then filtered through the fine filter plate for the second time to prevent the fine filter layer from being penetrated by impurities, and the impurities will directly enter the water collection chamber and clean water tank to ensure a good sewage treatment effect.
作为优选,所述的虹吸管整体呈U形,包括虹吸上升管、虹吸过渡管和虹吸下降管,所述的虹吸过渡管的一端与虹吸下降管的上端连通,另一端与虹吸上升管的上端连通,所述的虹吸下降管的下端连接有排污管。当虹吸现象发生的时候,清水逆流,过滤室顶部的水和杂质沿着虹吸上升管上升,经过虹吸过渡管进入虹吸下降管内,虹吸下降管内的水在重力的作用下向下流动,从而把过滤室顶部的空气抽出形成负压,从而保证精滤层内的杂质随着水流进入虹吸管并最终从排污管中排出来,从而实现滤砂的反冲洗。Preferably, the siphon pipe is U-shaped as a whole, including a siphon rising pipe, a siphon transition pipe and a siphon descending pipe, one end of the siphon transition pipe communicates with the upper end of the siphon descending pipe, and the other end communicates with the upper end of the siphon rising pipe , The lower end of the siphon downpipe is connected with a sewage pipe. When the siphon phenomenon occurs, the clean water flows backwards, and the water and impurities at the top of the filter chamber rise along the siphon ascending pipe, pass through the siphon transition pipe and enter the siphon descending pipe, and the water in the siphon descending pipe flows downward under the action of gravity, thus filtering The air at the top of the chamber is pumped out to form a negative pressure, so as to ensure that the impurities in the fine filter layer enter the siphon with the water flow and are finally discharged from the sewage pipe, so as to realize the backwashing of the filter sand.
作为优选,曝气溶氧箱和精滤罐都由UPVC材料制成。UPVC材料制成的产品具有耐腐蚀性,流体阻力小,机械强度高,卫生无毒,质地轻、安装方便,密封性能好等诸多优点,用UPVC材料制成的曝气溶氧箱和个精滤罐都具有上述特点,因此该种重力式水力曝气精滤机安装方便、密封性能好,使用寿命长。Preferably, both the aeration dissolved oxygen box and the fine filter tank are made of UPVC material. Products made of UPVC materials have many advantages such as corrosion resistance, small fluid resistance, high mechanical strength, sanitation and non-toxicity, light texture, convenient installation, good sealing performance, etc. The filter tanks all have the above characteristics, so this kind of gravity hydraulic aeration fine filter is easy to install, has good sealing performance and long service life.
因此,本实用新型具有结构简单、具有自动反冲洗功能,使用维护成本低的有益效果。Therefore, the utility model has the beneficial effects of simple structure, automatic backwashing function, and low maintenance cost.
同时,本实用新型还具有安装方便,耐腐蚀、不生锈,密封性能好,使用寿命长的有益效果。At the same time, the utility model also has the beneficial effects of convenient installation, corrosion resistance, no rust, good sealing performance and long service life.
附图说明Description of drawings
图1为本实用新型污水处理状态结构示意图。Fig. 1 is a schematic structural diagram of the sewage treatment state of the utility model.
图2为本实用新型反冲洗状态结构示意图。Fig. 2 is a structural schematic diagram of the backwashing state of the utility model.
图中:曝气溶氧箱1 进水配水箱11 曝气溶氧室12 曝气槽13 曝气条14 精滤罐2 清水箱21 过滤室22 集水室23 反冲管24 进水管3 气液分离管4 气液汇合管41 虹吸管5 虹吸上升管51 虹吸过渡管52 虹吸下降管53 连接管6 精滤层7 精密滤板71 出水管8 排污管9In the figure: aeration dissolved
具体实施方式Detailed ways
下面结合附图和具体实施方式对本实用新型作进一步描述:Below in conjunction with accompanying drawing and specific embodiment the utility model is further described:
如图1所示的一种重力式水力曝气精滤机,包括一个曝气溶氧箱1和设在曝气溶氧箱下端周围的四个精滤罐2,曝气溶氧箱1内设有进水配水箱11、曝气溶氧室12和曝气槽13,曝气槽13的上端与大气贯通,曝气槽13下端通过曝气条14与进水配水箱11、曝气溶氧室12分隔,进水配水箱11的侧面连接有进水管3,污水从进水管3中进入进水配水箱11内,进水配水箱11内的污水向上穿过曝气条14进入曝气槽13中与空气充分接触,曝气条14能将水充分细分,从而增大污水与空气的接触面,便于污水内的二氧化碳、氨氮等有毒气体排出,同时有利于空气中的氧气溶解入水中;曝气溶氧室12的下端设有气液分离管4,气液分离管4内设有上端与曝气溶氧室12贯通的气液汇合管41,精滤罐2内从上到下分别为清水箱21、过滤室22和集水室23,过滤室22的顶部设有虹吸管5,气液分离管4的上端侧面通过连接管6与虹吸管5连通,所述的过滤室22内设有精滤层7,精滤层由多层过滤介质组成,精滤层7的下侧设有精密滤板71,集水室23与清水箱21之间通过反冲管24连通,集水室23的上端侧面设有出水管8,氧气溶解入污水之后在气液汇合管41与污水内的氮、磷、溶解蛋白等有机物发生氧化反应,并产生很多泡沫,泡沫经过气液分离管4后与污水分离,漂浮在污水上面,污水和泡沫一起经过连接管6进入过滤室内,泡沫以及污水中的各种杂质在精滤层的过滤下积聚在精滤层7的上侧,经过精滤层7和精密滤板71的双重过滤后的清水积聚在集水室23内,随着集水室内的清水的积聚,清水最后经过反冲管24进入清水箱21内,然后通过出水管8排出清水,从而实现污水的处理。A kind of gravity type hydraulic aeration fine filter machine as shown in Figure 1, comprises an aeration dissolved
如图2所示,虹吸管5整体呈U形,包括虹吸上升管51、虹吸过渡管52和虹吸下降管53,虹吸过渡管52的一端与虹吸下降管53的上端连通,另一端与虹吸上升管51的上端连通,虹吸下降管53的下端连接有排污管9,随着固体杂质以及氧化后形成的泡沫积聚在精滤层7的顶部,逐渐增大精滤层对水流阻力,从而使得连接管6内的水进入过滤室内水位上升满入虹吸上升管51、虹吸过渡管52最后流入虹吸下降管53中,虹吸下降管53内的水在重力的作用下向下流动,从而把过滤室22顶部的空气抽出形成负压,产生虹吸现象,集水室23内的清水向上逆流,如图中箭头所示,清水不断的冲刷精滤层内的杂质,从而使得精滤层内的杂质随着水流进入虹吸管并最终从排污管中排出来,从而实现滤砂的反冲洗,随着精滤层内杂质的排出,清水箱内的水位降低,虹吸作用被破坏,滤料自动复位,重新开始过滤污水,整个过程都是自动形成,无需人工控制。因此,本实用新型具有结构简单、具有自动反冲洗功能,使用维护成本低的有益效果。本实施例中,曝气溶氧箱1和精滤罐2都由UPVC材料制成,用UPVC材料制成的曝气溶氧箱和个精滤罐都具有上述特点,因此该种重力式水力曝气精滤机同时还具有安装方便、密封性能好,使用寿命长的有益效果。As shown in Figure 2, the siphon
以上所述实施例仅表达了本实用新型的具体实施方式,其描述较为具体和详细,但并不能因此而理解为对本实用新型专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干变形和改进,这些都属于本实用新型的保护范围。The above-mentioned embodiments only express the specific implementation manners of the utility model, and the description thereof is relatively specific and detailed, but it should not be construed as limiting the patent scope of the utility model. It should be noted that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention, and these all belong to the protection scope of the present invention.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320139623.8U CN203144220U (en) | 2013-03-26 | 2013-03-26 | Gravity type hydraulic aeration fine filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320139623.8U CN203144220U (en) | 2013-03-26 | 2013-03-26 | Gravity type hydraulic aeration fine filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203144220U true CN203144220U (en) | 2013-08-21 |
Family
ID=48971763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320139623.8U Expired - Fee Related CN203144220U (en) | 2013-03-26 | 2013-03-26 | Gravity type hydraulic aeration fine filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203144220U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107935273A (en) * | 2017-12-29 | 2018-04-20 | 河南碧波环保设备有限公司 | Gravity installation intelligent control backwashing sewage water processing system |
| CN108706775A (en) * | 2018-06-11 | 2018-10-26 | 广州海山游乐科技股份有限公司 | A kind of water treatment system and processing method |
| CN110156226A (en) * | 2019-05-27 | 2019-08-23 | 郑州泓道泳池设备制造有限公司 | Hydraulic automatic gravity type dissolved oxygen fine filter |
-
2013
- 2013-03-26 CN CN201320139623.8U patent/CN203144220U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107935273A (en) * | 2017-12-29 | 2018-04-20 | 河南碧波环保设备有限公司 | Gravity installation intelligent control backwashing sewage water processing system |
| CN108706775A (en) * | 2018-06-11 | 2018-10-26 | 广州海山游乐科技股份有限公司 | A kind of water treatment system and processing method |
| CN110156226A (en) * | 2019-05-27 | 2019-08-23 | 郑州泓道泳池设备制造有限公司 | Hydraulic automatic gravity type dissolved oxygen fine filter |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101575153B (en) | On-line purification equipment for metal machining fluid and purification method thereof | |
| CN100375648C (en) | On-line chemical cleaning method for membrane-bioreactor | |
| KR101189747B1 (en) | Water supply and discharge purifying system for water tank type inland aquaculture | |
| CN206188537U (en) | Preliminary treatment adds multistage dull and stereotyped ceramic membrane oiliness effluent disposal system | |
| CN104108830A (en) | Novel recycled water advanced treatment and recycling system | |
| CN204897574U (en) | Oily waste water contact filtration combination formula advanced treatment unit that flocculates a little | |
| CN201400630Y (en) | Chemical fiber wastewater treatment system | |
| CN105129969B (en) | Perimeter filter water outlet biochemical sedimentation basin | |
| CN203144220U (en) | Gravity type hydraulic aeration fine filter | |
| CN204490636U (en) | A wastewater advanced pretreatment grease trap | |
| CN107673505B (en) | Air-flotation built-in ceramic membrane water purification system and method | |
| CN107434330B (en) | Artificial rapid infiltration sewage treatment method | |
| CN211411281U (en) | A processing system for power plant contains coal waste water | |
| CN201873554U (en) | Air stripping-type oil-water separation device | |
| CN106587454A (en) | Vehicle-mounted sudden water pollution accident emergency-purification system | |
| CN207130053U (en) | A kind of RO concentrated waters and the water reuse (treatment processing system of recirculated water draining | |
| CN206570138U (en) | Equipment for processing industrial sewage | |
| CN206544953U (en) | A kind of emulsion processing equipment | |
| CN205740593U (en) | A kind of molten pneumoelectric catalytic oxidizing equipment of oil extraction waste water reinjection technology | |
| CN104984572A (en) | Efficient active flowing bed purifier | |
| CN204550323U (en) | A kind of percolate concentrates liquid processing device | |
| CN201268648Y (en) | Multifunctional universal sewage treatment system | |
| CN115536215A (en) | High-efficient recovery system of chemical plant area rainwater | |
| CN204097251U (en) | A kind of internal-circulation type electric flocculation membrane wastewater treatment equipment | |
| CN206279057U (en) | A kind of reservoir aquaculture wastewater processing unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130821 Termination date: 20210326 |
