CN221876768U - Sewage treatment pool - Google Patents
Sewage treatment pool Download PDFInfo
- Publication number
- CN221876768U CN221876768U CN202420449475.8U CN202420449475U CN221876768U CN 221876768 U CN221876768 U CN 221876768U CN 202420449475 U CN202420449475 U CN 202420449475U CN 221876768 U CN221876768 U CN 221876768U
- Authority
- CN
- China
- Prior art keywords
- zone
- aeration
- sewage treatment
- sludge
- sedimentation
- 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.)
- Active
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 40
- 238000005273 aeration Methods 0.000 claims abstract description 43
- 238000004062 sedimentation Methods 0.000 claims abstract description 37
- 239000010802 sludge Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000005192 partition Methods 0.000 claims description 18
- 239000012535 impurity Substances 0.000 claims description 14
- 230000007246 mechanism Effects 0.000 claims description 13
- 238000005276 aerator Methods 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 229910052760 oxygen Inorganic materials 0.000 claims description 9
- 239000001301 oxygen Substances 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 8
- 238000004065 wastewater treatment Methods 0.000 claims description 4
- 239000005416 organic matter Substances 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 12
- 244000005700 microbiome Species 0.000 abstract description 4
- 238000001179 sorption measurement Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000053 physical method Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000006641 stabilisation Effects 0.000 description 3
- 238000011105 stabilization Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000725 suspension Substances 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
- Activated Sludge Processes (AREA)
Abstract
本实用新型提出一种污水处理池,属于污水处理技术领域;通过设置沉淀区、中间区、曝气区以及二次沉淀区,并在二次沉淀区设置连通中间区的淤泥管道,实现污水处理中活性污泥法的运行,活性污泥中微生物对污水中的有机物进行吸附;本实用新型的污水处理池有机物的去除率高,曝气池耐冲击负荷能力较低,适用于处理进水水质稳定、要求较高的大城市污水处理厂。
The utility model provides a sewage treatment pool, belonging to the technical field of sewage treatment; by setting a sedimentation zone, an intermediate zone, an aeration zone and a secondary sedimentation zone, and setting a sludge pipeline connected to the intermediate zone in the secondary sedimentation zone, the operation of an activated sludge method in sewage treatment is realized, and microorganisms in the activated sludge adsorb organic matter in the sewage; the sewage treatment pool of the utility model has a high removal rate of organic matter, and the aeration tank has a low impact load resistance capacity, and is suitable for treating large urban sewage treatment plants with stable influent water quality and high requirements.
Description
技术领域Technical Field
本实用新型属于污水处理技术领域,具体涉及一种污水处理池。The utility model belongs to the technical field of sewage treatment, and in particular relates to a sewage treatment pool.
背景技术Background Art
污水处理是指为使污水达到排水或再次使用的水质要求对其进行净化的过程;污水处理被广泛应用于建筑、农业、交通、能源、石化、环保、城市景观、医疗、餐饮等各个领域;Wastewater treatment refers to the process of purifying wastewater to meet the water quality requirements for drainage or reuse; wastewater treatment is widely used in various fields such as construction, agriculture, transportation, energy, petrochemicals, environmental protection, urban landscape, medical care, and catering;
现有技术下污水处理常使用的方式包括物理处理和化学处理;物理方法包括利用各种孔径大小不同的滤材,利用吸附或阻隔方式,将水中的杂质排除在外,吸附方式中较重要者为以活性炭进行吸附,阻隔方法则是将水通过滤材,让体积较大的杂质无法通过,进而获得较为干净的水。另外,物理方法也包括沉淀法,就是让比重较小的杂质浮于水面捞出,或是比重较大的杂质沉淀于下,进而取得;化学方法则是利用各种化学药品将水中杂质转化为对人体伤害较小的物质,或是将杂质集中;在对污水进行处理时,经常需要向污水池内喷洒处理药剂。现有的用药方式一般采用管道放在水池上开口进行药物喷雾,这种喷雾形式效率缓慢,处理剂需要在污水表面慢慢地向深处混合,不能使处理剂对污水快速地混合进行消毒处理,从而使工作效率降低;然而无论是化学方法还是物理方法都不能有效地对污水中有机物的去除,常常会出现,由于一些有机物的存在,使污水池易于腐败发臭,夏季气温较高时尤甚,这样对沉砂的处理和周围环境产生不利影响;因此,对水质进行调节,并未经过有效处理后的污水进行排放,净化城市环境,急需一种新型污水处理池。Under the existing technology, the commonly used methods for sewage treatment include physical treatment and chemical treatment; physical methods include using filter materials with different pore sizes, using adsorption or barrier methods to remove impurities in the water. The most important adsorption method is adsorption with activated carbon, and the barrier method is to pass water through the filter material so that larger impurities cannot pass through, thereby obtaining cleaner water. In addition, physical methods also include sedimentation, which is to let impurities with smaller specific gravity float on the water surface and be fished out, or impurities with larger specific gravity settle below, thereby obtaining; chemical methods use various chemicals to convert impurities in the water into substances that are less harmful to the human body, or to concentrate impurities; when treating sewage, it is often necessary to spray treatment agents into the sewage pool. The existing method of using medicine generally uses a pipe placed on an opening on the pool to spray the medicine. This spray form has a slow efficiency. The treatment agent needs to be mixed slowly from the surface of the sewage to the depth, and the treatment agent cannot be quickly mixed with the sewage for disinfection, thereby reducing work efficiency; however, neither chemical methods nor physical methods can effectively remove organic matter in sewage. It often happens that due to the presence of some organic matter, the sewage pool is prone to corruption and odor, especially in summer when the temperature is high, which has an adverse effect on the treatment of sand settling and the surrounding environment; therefore, a new type of sewage treatment pool is urgently needed to regulate water quality and discharge sewage that has not been effectively treated to purify the urban environment.
实用新型内容Utility Model Content
本实用新型针对现有技术下存在污水处理中有机物不能有效去除的问题,提供了一种污水处理池,通过在二次沉淀区以及曝气区之前设置淤泥管道,实现对水体中有机物的分离。The utility model aims at the problem that organic matter cannot be effectively removed in sewage treatment under the prior art, and provides a sewage treatment pool, which realizes the separation of organic matter in water by arranging sludge pipes before the secondary sedimentation zone and the aeration zone.
为了达到上述目的,本申请采用的技术方案为:In order to achieve the above purpose, the technical solution adopted in this application is:
一种污水处理池,包括池体,所述池体左侧设置有入水口,池体右侧设置有出水口,所述池体包括一次沉淀区、中间区、曝气区和二次沉淀区;所述沉淀区和中间区之间由第一隔板隔开,所述中间区和曝气区之间由第二隔板隔开,所述曝气区与二次沉淀区之间由第三隔板隔开;所述第一隔板、第二隔板以及第三隔板上均设置有水流通道;A sewage treatment tank comprises a tank body, wherein a water inlet is arranged on the left side of the tank body, a water outlet is arranged on the right side of the tank body, and the tank body comprises a primary sedimentation zone, an intermediate zone, an aeration zone and a secondary sedimentation zone; the sedimentation zone and the intermediate zone are separated by a first partition, the intermediate zone and the aeration zone are separated by a second partition, and the aeration zone and the secondary sedimentation zone are separated by a third partition; the first partition, the second partition and the third partition are all provided with water flow channels;
所述一次沉淀区设置有沉淀机构;所述曝气区底部固定安装有曝气机构;所述二次沉淀区底部连通有淤泥管道;所述淤泥管道出口与中间区底部连通。The primary sedimentation zone is provided with a sedimentation mechanism; the bottom of the aeration zone is fixedly installed with an aeration mechanism; the bottom of the secondary sedimentation zone is connected with a sludge pipeline; the outlet of the sludge pipeline is connected with the bottom of the intermediate zone.
作为优选,所述沉淀机构包括电机、转动轴和桨叶;所述电机通过L型支架与池体左侧壁固定连接,转动轴与电机输出端固定连接,桨叶固定安装在转动轴上。Preferably, the sedimentation mechanism comprises a motor, a rotating shaft and a paddle; the motor is fixedly connected to the left side wall of the pool body via an L-shaped bracket, the rotating shaft is fixedly connected to the output end of the motor, and the paddle is fixedly mounted on the rotating shaft.
作为优选,所述曝气机构包括气体输送管道、曝气器和供氧曝气风机;所述曝气器固定安装在曝气区底部,气体输送管道一端连接供氧曝气风机,另一端伸入曝气区底部与曝气器连通。Preferably, the aeration mechanism comprises a gas delivery pipeline, an aerator and an oxygen supply aeration fan; the aerator is fixedly installed at the bottom of the aeration area, one end of the gas delivery pipeline is connected to the oxygen supply aeration fan, and the other end extends into the bottom of the aeration area and communicates with the aerator.
作为优选,所述一次沉淀区底部还开设有杂质出口。Preferably, an impurity outlet is also provided at the bottom of the primary precipitation zone.
作为优选,所述淤泥管道右侧还开设有淤泥出口。Preferably, a sludge outlet is also provided on the right side of the sludge pipe.
与现有技术相比,本实用新型的优点和积极效果在于:Compared with the prior art, the advantages and positive effects of the utility model are:
本实用新型的一种污水处理池,通过设置沉淀区、中间区、曝气区以及二次沉淀区,并在二次沉淀区设置连通中间区的淤泥管道,实现污水处理中活性污泥法的运行,活性污泥中微生物对污水中的有机物进行吸附;本实用新型的污水处理池有机物的去除率高,曝气池耐冲击负荷能力较低,适用于处理进水水质稳定、要求较高的大城市污水处理厂。The utility model discloses a sewage treatment pool, which realizes the operation of activated sludge method in sewage treatment by arranging a sedimentation zone, an intermediate zone, an aeration zone and a secondary sedimentation zone, and arranging a sludge pipe connected to the intermediate zone in the secondary sedimentation zone, so that the microorganisms in the activated sludge adsorb the organic matter in the sewage. The sewage treatment pool of the utility model has a high removal rate of organic matter, and the aeration tank has a low impact load resistance capacity, and is suitable for treating sewage treatment plants in large cities with stable influent water quality and high requirements.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作一简单地介绍,显而易见地,下面描述中的附图是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the utility model or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are some embodiments of the utility model. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative labor.
图1为本实用新型的结构示意图;Fig. 1 is a schematic diagram of the structure of the utility model;
以上各图中,1、池体;2、一次沉淀区;3、中间区;4、曝气区;5、二次沉淀区;6、第一隔板;7、第二隔板;8、第三隔板;9、淤泥管道;10、电机;11、转动轴;12、桨叶;13、气体输送管道;14、曝气器;15、曝气风机;16、杂质出口;17、淤泥出口。In the above figures, 1, tank body; 2, primary sedimentation zone; 3, intermediate zone; 4, aeration zone; 5, secondary sedimentation zone; 6, first baffle; 7, second baffle; 8, third baffle; 9, sludge pipeline; 10, motor; 11, rotating shaft; 12, paddle; 13, gas delivery pipeline; 14, aerator; 15, aeration fan; 16, impurity outlet; 17, sludge outlet.
具体实施方式DETAILED DESCRIPTION
为了能够更清楚地理解本实用新型的上述目的、特征和优点,下面结合附图和实施例对本实用新型作进一步说明。需要说明的是,在不冲突的情况下,本申请的实施例及实施例中的特征可以相互组合。In order to more clearly understand the above-mentioned purpose, features and advantages of the utility model, the utility model is further described below in conjunction with the accompanying drawings and embodiments. It should be noted that the embodiments of the present application and the features in the embodiments can be combined with each other without conflict.
在下面的描述中阐述了很多具体细节以便于充分理解本实用新型,但是,本实用新型还可以采用不同于在此描述的其他方式来实施,因此,本实用新型并不限于下面公开说明书的具体实施例的限制。In the following description, many specific details are set forth to facilitate a full understanding of the present invention. However, the present invention may also be implemented in other ways than those described herein. Therefore, the present invention is not limited to the specific embodiments of the following disclosure.
实施例1,如图1所示,本实施例的一种污水处理池,所述池体1左侧设置有入水口,池体1右侧设置有出水口;所述池体1在本实施例中,从左到右依次包括一次沉淀区2、中间区3、曝气区4和二次沉淀区5;所述沉淀区2和中间区3之间由第一隔板6隔开,所述中间区3和曝气区4之间由第二隔板7隔开,所述曝气区4与二次沉淀区5之间由第三隔板8隔开;所述第一隔板6、第二隔板7以及第三隔板8上均设置有水流通道;Embodiment 1, as shown in FIG1 , a sewage treatment pool of this embodiment, the pool body 1 is provided with a water inlet on the left side, and the pool body 1 is provided with a water outlet on the right side; the pool body 1 in this embodiment includes, from left to right, a primary sedimentation zone 2, an intermediate zone 3, an aeration zone 4, and a secondary sedimentation zone 5; the sedimentation zone 2 and the intermediate zone 3 are separated by a first partition 6, the intermediate zone 3 and the aeration zone 4 are separated by a second partition 7, and the aeration zone 4 and the secondary sedimentation zone 5 are separated by a third partition 8; the first partition 6, the second partition 7, and the third partition 8 are all provided with water flow channels;
所述一次沉淀区2设置有沉淀机构;所述曝气区4底部固定安装有曝气机构;所述二次沉淀区5底部连通有淤泥管道9;所述淤泥管道9出口与中间区底部连通;淤泥管道9的设置使活性淤泥重新回到污水处理池曝气步骤之前;这是因为:活性污泥对有机物的降解主要在曝气阶段进行,可分为两个阶段,吸附阶段和稳定阶段;在吸附阶段,主要是污水中的有机物转移到活性污泥上去,这是由于活性污泥具有巨大的比表面积,而表面上含有多糖类的黏性物质所致;在稳定阶段,主要是转移到活性污泥上的有机物为微生物所利用。当污水中有机物处于悬浮状态和胶态时,吸附阶段很短,一般在15 min-45 min左右,而稳定阶段较长;利用活性污泥法能够简化污水预处理,有机物的去除率高,适用于处理进水水质稳定、要求较高的大城市污水处理厂;The primary sedimentation zone 2 is provided with a sedimentation mechanism; the bottom of the aeration zone 4 is fixedly installed with an aeration mechanism; the bottom of the secondary sedimentation zone 5 is connected to a sludge pipe 9; the outlet of the sludge pipe 9 is connected to the bottom of the intermediate zone; the setting of the sludge pipe 9 allows the activated sludge to return to the sewage treatment tank before the aeration step; this is because: the degradation of organic matter by activated sludge is mainly carried out in the aeration stage, which can be divided into two stages, the adsorption stage and the stabilization stage; in the adsorption stage, it is mainly the organic matter in the sewage that is transferred to the activated sludge, which is due to the huge specific surface area of the activated sludge and the sticky substances containing polysaccharides on the surface; in the stabilization stage, it is mainly the organic matter transferred to the activated sludge that is used by microorganisms. When the organic matter in the sewage is in a suspended state and a colloidal state, the adsorption stage is very short, generally about 15 min-45 min, and the stabilization stage is longer; the use of the activated sludge method can simplify sewage pretreatment, and the removal rate of organic matter is high. It is suitable for treating large urban sewage treatment plants with stable influent water quality and high requirements;
所述沉淀机构包括电机10、转动轴11和桨叶12;所述电机10通过L型支架与池体1左侧壁固定连接,转动轴11与电机输出端固定连接,桨叶12固定安装在转动轴上;沉淀机构的设置实现污水与杂质颗粒的初步分离;The sedimentation mechanism comprises a motor 10, a rotating shaft 11 and a paddle 12; the motor 10 is fixedly connected to the left side wall of the tank body 1 through an L-shaped bracket, the rotating shaft 11 is fixedly connected to the motor output end, and the paddle 12 is fixedly mounted on the rotating shaft; the sedimentation mechanism is set to achieve preliminary separation of sewage and impurity particles;
所述曝气机构包括气体输送管道13、曝气器14和供氧曝气风机15;所述曝气器14固定安装在曝气区底部,气体输送管道13一端连接供氧曝气风机15,另一端伸入曝气区底部与曝气器14连通;通过铺设在曝气池底部的曝气器14,使空气以细小气泡的形式进入污水中,目的是增加污水中的溶解氧含量,还使混合液处于剧烈搅动的状态,呈悬浮状态;溶解氧、活性污泥与污水互相混合、充分接触,使活性污泥反应得以正常进行;The aeration mechanism includes a gas delivery pipeline 13, an aerator 14 and an oxygen supply aeration fan 15; the aerator 14 is fixedly installed at the bottom of the aeration zone, one end of the gas delivery pipeline 13 is connected to the oxygen supply aeration fan 15, and the other end extends into the bottom of the aeration zone and communicates with the aerator 14; through the aerator 14 laid at the bottom of the aeration tank, air enters the sewage in the form of fine bubbles, the purpose is to increase the dissolved oxygen content in the sewage, and also make the mixed liquid in a state of violent stirring and suspension; the dissolved oxygen, activated sludge and sewage are mixed and fully contacted with each other, so that the activated sludge reaction can proceed normally;
曝气区4是活性污泥法的心脏,其作用是搅拌混合液使泥、水充分接触和向微生物供氧;使同时进曝气池的泥和水充分混合并一直保持到流出池子,而不和已在池中的混合液相混以免发生短路现象,使同时入池的废水有相同的曝气时间;曝气器14使池液回流,提供动力使活性淤泥从二次沉淀区5通过淤泥管道9进入到中间区;The aeration zone 4 is the heart of the activated sludge process. Its function is to stir the mixed liquid so that the mud and water are fully in contact and to supply oxygen to the microorganisms; to make the mud and water entering the aeration tank at the same time fully mixed and kept until they flow out of the tank, and not mixed with the mixed liquid already in the tank to avoid short circuit phenomenon, so that the wastewater entering the tank at the same time has the same aeration time; the aerator 14 refluxes the tank liquid and provides power to make the activated sludge enter the intermediate zone from the secondary sedimentation zone 5 through the sludge pipeline 9;
所述一次沉淀区2底部还开设有杂质出口16;使用时,如果发现一次沉淀区底部出现杂质堆积现象,打开杂质出口16上的开关阀,排出杂质;The bottom of the primary precipitation zone 2 is also provided with an impurity outlet 16; when in use, if impurities are found to be accumulated at the bottom of the primary precipitation zone, the switch valve on the impurity outlet 16 is opened to discharge the impurities;
所述淤泥管道9右侧还开设有淤泥出口17;淤泥出口是去除有机物的途径之一,同时维持系统的稳定运行。The right side of the sludge pipe 9 is also provided with a sludge outlet 17; the sludge outlet is one of the ways to remove organic matter while maintaining the stable operation of the system.
以上所述,仅是本实用新型的较佳实施例而已,并非对本实用新型作其他形式的限制,任何熟悉本专业的技术人员可能利用上述揭示的技术内容加以变更或改型为等同变化的等效实施例应用于其他领域,但是凡是未脱离本实用新型技术方案内容,依据本实用新型的技术实质对以上实施例所做的任何简单修改、等同变化与改型,仍属于本实用新型技术方案的保护范围。The above description is only a preferred embodiment of the present invention and does not limit the present invention in other forms. Any technician familiar with the profession may use the technical content disclosed above to change or modify it into an equivalent embodiment with equivalent changes and apply it to other fields. However, any simple modification, equivalent change and modification made to the above embodiment based on the technical essence of the present invention without departing from the content of the technical solution of the present invention still falls within the protection scope of the technical solution of the present invention.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202420449475.8U CN221876768U (en) | 2024-03-08 | 2024-03-08 | Sewage treatment pool |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202420449475.8U CN221876768U (en) | 2024-03-08 | 2024-03-08 | Sewage treatment pool |
Publications (1)
Publication Number | Publication Date |
---|---|
CN221876768U true CN221876768U (en) | 2024-10-22 |
Family
ID=93090943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202420449475.8U Active CN221876768U (en) | 2024-03-08 | 2024-03-08 | Sewage treatment pool |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN221876768U (en) |
-
2024
- 2024-03-08 CN CN202420449475.8U patent/CN221876768U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2019196053A1 (en) | High-efficiency energy-saving integrated water treatment device | |
CN107055954B (en) | Biochar circulation type copolymerization air flotation tank water purification system and method | |
JP3245878U (en) | Sewage treatment equipment | |
CN103086574B (en) | Aquatic product processing wastewater treatment equipment | |
CN107417032A (en) | A kind of sewage disposal system and sewage water treatment method | |
CN105585184B (en) | A kind of the circulated sprinkling liquid processing method and device of the discharge of dyeing waste water deodoration system | |
CN206289080U (en) | A kind of sewage-treatment plant | |
CN203159389U (en) | Aquatic product processing wastewater treatment equipment | |
CN204324936U (en) | Vertical-flow ozone air-float equipment | |
CN201400629Y (en) | Floor processing wastewater treatment and reuse system | |
CN211445407U (en) | Purify ecological dam device in black and odorous river course | |
CN221876768U (en) | Sewage treatment pool | |
CN211170292U (en) | Urban sewage treatment device | |
CN201338976Y (en) | Medical institution sewage treatment integrated device | |
CN206359396U (en) | A kind of MBR Treated sewage reusings processing unit | |
CN201268648Y (en) | Multifunctional universal sewage treatment system | |
CN211394142U (en) | Drinking water treatment device | |
CN116395844A (en) | Sewage treatment integrated device | |
CN211521959U (en) | Multistage sewage treatment pond | |
CN211770513U (en) | Improved laboratory scale sequencing batch reactor system | |
CN106673381A (en) | Sludge treatment device and method | |
CN207276382U (en) | A kind of the dirty water decontamination handles station | |
CN2457145Y (en) | Purifying equipment for living waste water | |
CN205398397U (en) | Integrated sewage treatment device | |
CN221940273U (en) | A multi-stage treatment device for chemical wastewater |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |