CN204569520U - A kind of flocculating settling equipment - Google Patents

A kind of flocculating settling equipment Download PDF

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CN204569520U
CN204569520U CN201520260913.7U CN201520260913U CN204569520U CN 204569520 U CN204569520 U CN 204569520U CN 201520260913 U CN201520260913 U CN 201520260913U CN 204569520 U CN204569520 U CN 204569520U
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flocculation
coagulation
settling
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李亚萍
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Binzhou University
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Abstract

本实用新型公开了一种絮凝沉降设备,主要涉及污水处理装置领域。包括混凝罐、絮凝池和沉降池,混凝罐、絮凝池和沉降池按照工艺流程从前往后的顺序依次连通,混凝罐为封闭罐体,且包括内层的上水区和外层的混合区,上水区的下端设置混凝搅拌器;絮凝池的顶端设置布水管,絮凝池内设有絮凝搅拌装置;还包括缓流通道,缓流通道内设置顶端留有通道的隔板;沉降池的底部设有泥斗,沉降池的中上部设有斜板,沉降池的顶部设有多个排水槽,沉降池外壁还设有集水槽。本实用新型的有益效果在于:它在混凝阶段的搅拌激烈迅速,使絮凝剂与颗粒物产生有效的碰撞,在絮凝阶段的搅拌柔和均匀,使絮凝反应充分,沉降效率高效果好。

The utility model discloses a flocculation settling device, which mainly relates to the field of sewage treatment devices. Including coagulation tank, flocculation tank and settling tank, the coagulation tank, flocculation tank and settling tank are connected in sequence according to the process flow from front to back, the coagulation tank is a closed tank, and includes the upper water area of the inner layer and the outer layer In the mixing area, a coagulation agitator is set at the lower end of the upper water area; a water distribution pipe is set at the top of the flocculation tank, and a flocculation stirring device is installed in the flocculation tank; it also includes a slow flow channel, and a partition with a channel at the top is set in the slow flow channel; There is a mud bucket at the bottom of the tank, a sloping plate at the middle and upper part of the settling tank, multiple drainage grooves at the top of the settling tank, and a water collection tank on the outer wall of the settling tank. The beneficial effect of the utility model lies in that: the stirring in the coagulation stage is intense and rapid, so that the flocculant and the particle can effectively collide;

Description

一种絮凝沉降设备A flocculation settling equipment

技术领域technical field

本实用新型涉及污水处理装置领域,具体是一种絮凝沉降设备。The utility model relates to the field of sewage treatment devices, in particular to flocculation and sedimentation equipment.

背景技术Background technique

污水处理,是指为使污水达到排水某一水体或再次使用的水质要求,并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,与经济的可持续发展、环境质量和人们的生活关系紧密。Sewage treatment refers to the process of purifying sewage to meet the water quality requirements of a certain water body for drainage or reuse. Sewage treatment is widely used in construction, agriculture, transportation, energy, petrochemical, environmental protection, urban landscape, medical treatment, catering and other fields, and is closely related to sustainable economic development, environmental quality and people's lives.

污水处理一般分为三级:一级处理,系应用物理处理法去除污水中不溶解的污染物和寄生虫卵;二级处理,系应用生物处理法将污水中各种复杂的有机物氧化降解为简单的物质;三级处理,系应用化学沉淀法、生物化学法、物理化学法等,去除污水中的磷、氮、难降解的有机物、无机盐等。以上三级处理工艺中,均需要用到相应的絮凝沉降装置,进一步而言,絮凝沉降装置是污水处理的反应区和净化区,是整个污水处理系统的核心。Sewage treatment is generally divided into three levels: primary treatment, which uses physical treatment to remove insoluble pollutants and parasite eggs in sewage; secondary treatment, which uses biological treatment to oxidize and degrade various complex organic substances in sewage into Simple substances; tertiary treatment, the application of chemical precipitation, biochemical, physical and chemical methods, etc., to remove phosphorus, nitrogen, refractory organic matter, inorganic salts, etc. in sewage. In the above three-stage treatment process, the corresponding flocculation and sedimentation device is required. Furthermore, the flocculation and sedimentation device is the reaction zone and purification zone of sewage treatment, and is the core of the entire sewage treatment system.

絮凝沉降工艺的主要过程一般为,根据污水情况选择并投加絮凝剂后,水中的胶体及分散颗粒在分子力的相互作用下生成絮状体且在沉降过程中互相碰撞凝聚,其尺寸和质量不断变大,沉速不断增加,当絮凝体长大到一定体积后即在重力作用下脱离水相沉淀,从而去除废水中的大量悬浮物,从而达到净化的效果。The main process of the flocculation and sedimentation process is generally, after the flocculant is selected and added according to the sewage situation, the colloids and dispersed particles in the water form flocs under the interaction of molecular forces and collide and coagulate with each other during the sedimentation process. When the floc grows to a certain volume, it will separate from the water phase and precipitate under the action of gravity, thereby removing a large amount of suspended solids in the wastewater, thereby achieving the effect of purification.

在絮凝沉降的反应过程中,对水体的搅拌处理非常重要。絮凝沉降的流程主要分为:混合、絮凝、沉降三个主要过程。混合的目的是使胶体颗粒凝聚脱稳,在混合过程中,必须要使混凝剂的有效成分迅速均匀地与水中胶体颗粒接触产生凝聚作用,所以混合过程要求强烈、快速、短时,在尽可能短的时间内使混凝剂均匀分散到原水中,故要求水流能产生激烈的湍流。混凝的目的是使细小颗粒之间有效碰撞,从而逐渐增长为大颗粒,最终达到重力沉降实现固液分离,这就要求水流的湍流柔和而均匀。沉降的目的是使絮凝物逐步自水中沉淀下来,最终完成固液分离,实现水质净化。During the reaction process of flocculation and sedimentation, the stirring treatment of water body is very important. The process of flocculation and sedimentation is mainly divided into three main processes: mixing, flocculation and sedimentation. The purpose of mixing is to coagulate and destabilize the colloidal particles. During the mixing process, the active ingredients of the coagulant must be quickly and evenly contacted with the colloidal particles in the water to produce coagulation, so the mixing process requires strong, fast and short time. It is possible to evenly disperse the coagulant into the raw water in a short period of time, so the water flow is required to generate intense turbulence. The purpose of coagulation is to effectively collide between fine particles, thereby gradually growing into large particles, and finally achieve gravity settlement to achieve solid-liquid separation, which requires soft and uniform turbulence of water flow. The purpose of sedimentation is to make the flocs gradually settle down from the water, and finally complete the solid-liquid separation to realize water purification.

现有技术的絮凝沉降装置,在混合、絮凝阶段对水体流动的控制尚不完善,仍然处于探讨和优化的阶段。The flocculation and sedimentation device of the prior art is not perfect in the control of the water flow in the mixing and flocculation stages, and is still in the stage of exploration and optimization.

在混合阶段,由于污水的处理压力往往较大,流速较快,池内的搅拌压力较大,传统的开放式混凝池很难做到搅拌激烈和充分混合,使得混凝剂的利用程度有限,影响水体的絮凝效果。In the mixing stage, because the sewage treatment pressure is often high, the flow rate is fast, and the stirring pressure in the tank is relatively high, it is difficult to achieve vigorous stirring and full mixing in the traditional open coagulation tank, which makes the utilization of the coagulant limited. Affect the flocculation effect of water body.

在絮凝阶段,为了保证处理量,絮凝池一般较大较深,这就给水体的上下翻动和混合均匀带来难度,现有技术的絮凝池或使用较大的框式搅拌器,虽然径向混合较好,但是剪切力较大不利于絮凝物的形成,且上下混合较差,搅拌不充分,或使用头部轴向搅拌叶片的搅拌器,虽然水流的上下搅动有所改善,但搅拌影响的范围小,搅拌不均匀,转速快则容易打碎叶片附近的絮凝物,如果转速低则搅拌效果不良,影响处理效果。In the flocculation stage, in order to ensure the processing capacity, the flocculation tank is generally larger and deeper, which brings difficulties to the up and down turning and mixing of the water body. The flocculation tank of the prior art may use a larger frame agitator, although The mixing is good, but the high shear force is not conducive to the formation of flocs, and the up and down mixing is poor, the stirring is not sufficient, or the agitator with the axial stirring blade on the head is used, although the up and down agitation of the water flow has been improved, but the agitation The range of influence is small, the stirring is uneven, and the flocs near the blades are easily broken if the rotating speed is fast. If the rotating speed is low, the stirring effect will be poor, which will affect the treatment effect.

除了以上问题,现有絮凝沉降装置的沉降池多为敞口的露天池,水处理到这一阶段絮凝物都已形成,处于重力沉淀阶段,然而露天的装置使水体大面积的暴露在外界环境中,难免落入毛絮、落叶、灰尘等而造成新的污染,大大影响水处理的质量。然而现有装置尚未针对这一问题给出解决方案。In addition to the above problems, the settling tanks of the existing flocculation and settling devices are mostly open open-air tanks. At this stage of water treatment, the flocs have been formed and are in the gravity sedimentation stage. However, the open-air devices expose a large area of the water body to the external environment. In the water, it is inevitable to fall into fluff, fallen leaves, dust, etc. and cause new pollution, which greatly affects the quality of water treatment. However, existing devices have not yet provided a solution to this problem.

实用新型内容Utility model content

本实用新型的目的在于提供一种絮凝沉降设备,它在混凝阶段的搅拌激烈迅速,使絮凝剂与颗粒物产生有效的碰撞,混合效果好,它在絮凝阶段的搅拌柔和均匀,水体翻卷混合充分,絮凝效果好,且在沉降前端增设缓流阶段,使絮凝反应充分,沉降效率高效果好,有效的提高了水处理的质量。The purpose of this utility model is to provide a kind of flocculation and sedimentation equipment, which stirs violently and quickly in the coagulation stage, so that the flocculant and the particles can effectively collide, and the mixing effect is good. , The flocculation effect is good, and a slow flow stage is added at the front end of the settlement, so that the flocculation reaction is sufficient, the settlement efficiency is high, and the effect is good, which effectively improves the quality of water treatment.

本实用新型为实现上述目的,通过以下技术方案实现:The utility model realizes above-mentioned purpose by following technical scheme:

一种絮凝沉降设备,包括混凝罐、絮凝池和沉降池,所述混凝罐、絮凝池和沉降池按照工艺流程从前往后的顺序依次连通,且所述沉降池的后端设置出水总管,所述混凝罐的前端设置原水总管,所述原水总管上还设有Y型过滤器和闸阀,还包括加药管路,所述加药管路通过闸阀与原水总管连通,A flocculation settling equipment, including a coagulation tank, a flocculation tank and a settling tank, the coagulation tank, the flocculation tank and the settling tank are connected in sequence according to the process flow from front to back, and the rear end of the settling tank is provided with a water main pipe , the front end of the coagulation tank is provided with a raw water main pipe, and the raw water main pipe is also provided with a Y-shaped filter and a gate valve, and also includes a dosing pipeline, and the dosing pipeline is communicated with the raw water main pipe through a gate valve,

所述混凝罐为封闭罐体,且包括内层的上水区和外层的混合区,所述混合区与原水总管相连通,所述上水区的顶壁上设有与絮凝池相连通的管路,所述管路上设有水泵和闸阀,所述上水区的侧壁为窄端向下的喇叭口结构,所述上水区的下端设置与混合区相连通的开口,所述开口内设置混凝搅拌器,所述混凝搅拌器为斜叶开启式蜗轮搅拌器;The coagulation tank is a closed tank and includes an upper water area of the inner layer and a mixing area of the outer layer. The mixing area is connected with the raw water main pipe, and the top wall of the upper water area is provided with a The pipeline is connected, and the pipeline is provided with a water pump and a gate valve. The side wall of the upper water area is a trumpet structure with the narrow end facing down. The lower end of the upper water area is provided with an opening that communicates with the mixing area. A coagulation agitator is arranged in the opening, and the coagulation agitator is an open-type worm gear agitator with inclined blades;

所述絮凝池的顶端设置布水管,所述布水管的进水端与管路相连通,所述布水管的出水端指向絮凝池,所述絮凝池内设有絮凝搅拌装置,所述絮凝搅拌装置包括搅拌轴、下压叶桨和上翻叶桨,所述搅拌轴位于絮凝池的中央且为顺时针转动,所述下压叶桨和上翻叶桨分别为三片且环绕搅拌轴均匀分布,所述下压叶桨为逆时针倾斜的折叶且位于搅拌轴上部,所述上翻叶桨为顺时针倾斜的折叶且位于搅拌轴下部;The top of the flocculation tank is provided with a water distribution pipe, the water inlet end of the water distribution pipe is connected to the pipeline, the water outlet end of the water distribution pipe points to the flocculation tank, and a flocculation stirring device is arranged in the flocculation tank, and the flocculation stirring device It includes a stirring shaft, a downward pressing paddle and an upward turning blade. The stirring shaft is located in the center of the flocculation tank and rotates clockwise. , the downward-pressing paddle is a counterclockwise inclined hinge and is located on the upper part of the stirring shaft, and the upward turning blade is a clockwise inclined hinge and is located on the lower part of the stirring shaft;

还包括缓流通道,所述缓流通道夹置于絮凝池和沉降池之间,且其一侧的底端与絮凝池的底端相连通,另一侧的底端设有布水网孔且其通过布水网孔与沉降池相连通,所述缓流通道内设置顶端留有通道的隔板;It also includes a slow flow channel, the slow flow channel is sandwiched between the flocculation tank and the sedimentation tank, and the bottom end of one side is connected with the bottom end of the flocculation tank, and the bottom end of the other side is provided with a water distribution mesh and It communicates with the sedimentation tank through the water distribution mesh, and a partition plate with a channel at the top is set in the slow flow channel;

所述布水网孔位于沉降池池壁的中部,所述沉降池的底部设有泥斗,所述沉降池的中上部设有斜板,所述沉降池的顶部设有多个排水槽,所述沉降池外壁还设有集水槽,所述排水槽的一端穿过沉降池的池壁与集水槽相连通,所述出水总管与集水槽相连通。The water distribution mesh is located in the middle of the settling tank wall, the bottom of the settling tank is provided with a mud bucket, the middle and upper part of the settling tank is provided with a sloping plate, and the top of the settling tank is provided with a plurality of drainage grooves. The outer wall of the settling tank is also provided with a sump, one end of the drainage tank passes through the wall of the settling tank and communicates with the sump, and the outlet main pipe communicates with the sump.

所述出水总管与集水槽相连通的一端设有集水滤管,所述集水滤管上设有过滤微孔,所述出水总管上设有闸阀和水泵。The end of the water outlet main pipe connected to the water collection tank is provided with a water collection filter pipe, the water collection filter pipe is provided with filtering pores, and the water outlet main pipe is provided with a gate valve and a water pump.

所述布水管包括母管和支管,所述支管为多个且其一端均与母管相连通,所述支管环绕母管均匀分布。The water distribution pipe includes a main pipe and branch pipes. There are multiple branch pipes and one end of the branch pipes is connected to the main pipe. The branch pipes are evenly distributed around the main pipe.

所述混凝罐、絮凝池的顶端均设有搅拌电机。The tops of the coagulation tank and the flocculation tank are equipped with stirring motors.

所述混凝搅拌器的转速为100~200r/min。The rotational speed of the coagulation agitator is 100-200 r/min.

所述絮凝搅拌装置的转速为50~100r/min。The rotational speed of the flocculation stirring device is 50-100 r/min.

对比现有技术,本实用新型的有益效果在于:Compared with the prior art, the beneficial effects of the utility model are:

1、采用混凝罐代替传统的混凝池。由于混凝罐为密封罐体,且内部分区布局:混合区在外围且与原水总管连通,加过絮凝剂的原水进入混合区,进行初步的混合和预备,所述混凝搅拌器高速运转,斜叶开启式蜗轮搅拌方式一方面阻力小,利于高速旋转,另一方面高速搅拌的叶片能够使水体形成向上且激烈的涡流,带动混合区的水体上行并自开口进入上水区。通过上述结构和操作,使进入上水区的原水中的细小颗粒和絮凝剂产生充分的混合和激烈的碰撞,不但保证了原水与混凝剂的均匀混合,且过程快速、短时、激烈,满足混凝的工艺要求,有利于下一步絮凝反应的进行。1. The coagulation tank is used instead of the traditional coagulation tank. Since the coagulation tank is a sealed tank, and the internal partition layout: the mixing zone is on the periphery and connected to the raw water main pipe, the raw water added with flocculant enters the mixing zone for preliminary mixing and preparation, and the coagulation agitator operates at high speed, On the one hand, the slanted-blade open-type worm wheel stirring method has low resistance and is conducive to high-speed rotation. On the other hand, the high-speed stirring blades can make the water body form an upward and intense vortex, driving the water body in the mixing area to go up and enter the upper water area from the opening. Through the above structure and operation, the fine particles and flocculant in the raw water entering the upper water area are fully mixed and violently collided, which not only ensures the uniform mixing of the raw water and the coagulant, but also the process is fast, short-term and intense. Satisfies the technical requirements of coagulation and is conducive to the next step of flocculation reaction.

2、所述布水管的设置,能够将水均匀的注入絮凝池中,有利于后续的分散和混合,避免同质水体的集中。2. The arrangement of the water distribution pipe can uniformly inject water into the flocculation tank, which is beneficial to the subsequent dispersion and mixing, and avoids the concentration of homogeneous water bodies.

3、所述絮凝搅拌装置的设置,具有以下优势:3. The setting of the flocculation and stirring device has the following advantages:

所述叶桨均为3片,有利于进行强度适中的搅拌操作;The blades are all 3 pieces, which is conducive to the stirring operation with moderate strength;

所述下压叶桨在上部并呈逆时针倾斜,结合搅拌轴顺时针的转动,能够将水体卷入并下压,使上部的水体向轴心并向下翻卷;所述上翻叶桨在下部并呈顺时针倾斜,结合搅拌轴顺时针的转动,能够将水体卷入并上扬,使下部的水体向轴心并向上翻卷;所述下压叶桨和上翻叶桨相配合,能够使水体实现自四角向中央的对流翻卷,使处于絮凝反应下的水体上下翻滚效果好,混合充分且柔和,有利于絮凝反应的进行。The down-pressing paddle is on the upper part and is inclined counterclockwise, combined with the clockwise rotation of the stirring shaft, the water body can be involved and pressed down, so that the upper part of the water body rolls toward the axis and downward; the up-turning paddle is in the The lower part is inclined clockwise, combined with the clockwise rotation of the stirring shaft, the water body can be drawn in and raised, so that the water body in the lower part can roll up towards the axis; The water body realizes the convective rolling from the four corners to the center, which makes the water body under the flocculation reaction roll up and down well, and the mixing is sufficient and soft, which is conducive to the flocculation reaction.

4、所述缓流通道的设置,一方面给絮凝反应留出充足的反应时间,保证颗粒物的充分絮凝结合,另一方面可以通过使杂乱混流的水体进行通道式的流动和梳理,消耗掉过多的势能和动能,使水流平稳,有利于下一步沉降。4. The setting of the slow flow channel, on the one hand, allows sufficient reaction time for the flocculation reaction to ensure the full flocculation and combination of particles, and on the other hand, it can make the messy and mixed flow of water flow and comb through the channel, so as to consume too much The potential energy and kinetic energy of the water make the water flow stable, which is conducive to the next step of settlement.

5、所述布水网孔的设置,用于进一步分散水流和缓和冲力,使水流柔和细密的注入沉降池,避免扰动沉降池内平静的水体,保证沉降的持续高效。5. The setting of the water distribution mesh is used to further disperse the water flow and buffer the impulse force, so that the water flow can be injected into the settlement tank softly and finely, so as to avoid disturbing the calm water body in the settlement tank and ensure the continuous and efficient settlement.

6、所述沉降池自中部入水,有利于斜板发挥作用和泥斗收集杂质。所述斜板的设置,缩短了沉降距离,增加了聚结面积,提高了处理量和分离效率,同时减少了水体的相互扰动,有利于絮凝物的沉积聚结,所述斜板上沉积的杂质和水中沉淀出的杂质顺着斜板落入下方的泥斗中,便于集中清理收集。6. The sedimentation tank enters water from the middle, which is beneficial to the role of the inclined plate and the collection of impurities by the mud bucket. The setting of the sloping plate shortens the settling distance, increases the coalescence area, improves the processing capacity and separation efficiency, and reduces the mutual disturbance of water bodies, which is beneficial to the deposition and coalescence of flocs. Impurities and impurities precipitated in the water fall along the inclined plate into the mud hopper below, which is convenient for centralized cleaning and collection.

7、所述集水滤管的设置解决了絮凝沉降末段新增污染源的问题,通过添加的过滤微孔来物理滤除掉由于露天操作而可能落入的毛絮、落叶、灰尘等悬浮物,进一步保证水处理质量。7. The setting of the water collection filter pipe solves the problem of new pollution sources in the final stage of flocculation and settlement, and physically filters out suspended matter such as flocs, fallen leaves, and dust that may fall due to open-air operation through the added filter micropores, and further Guarantee the quality of water treatment.

8、所述布水管采用发散布局,平面布水效果好,出水均匀分散。8. The water distribution pipe adopts a divergent layout, the plane water distribution effect is good, and the water outlet is evenly dispersed.

9、所述搅拌电机的设置,为混凝搅拌器和絮凝搅拌装置提供电力传动。9. The setting of the stirring motor provides electric drive for the coagulation stirrer and the flocculation stirring device.

10、所述混凝搅拌器的转速为100~200r/min,搅拌有力,上行效果好,湍流激烈混合充分。10. The rotation speed of the coagulation agitator is 100-200r/min, with powerful stirring, good upward effect, and sufficient turbulent mixing.

11、所述絮凝搅拌装置的转速为50~100r/min,搅拌柔和充分,保证絮凝物的完整和凝集。11. The rotating speed of the flocculation stirring device is 50-100r/min, and the stirring is gentle and sufficient, so as to ensure the integrity and coagulation of the flocs.

附图说明Description of drawings

附图1是本实用新型的示意图。Accompanying drawing 1 is the schematic diagram of the utility model.

附图2是本实用新型絮凝搅拌装置的示意图。Accompanying drawing 2 is the schematic diagram of the flocculation stirring device of the present utility model.

附图3是本实用新型布水管的刨面图。Accompanying drawing 3 is the plane view of the water distribution pipe of the present utility model.

附图中所示标号:Labels shown in the accompanying drawings:

1、混凝罐;2、絮凝池;3、沉降池;4、出水总管;5、原水总管;6、Y型过滤器;7、闸阀;8、加药管路;9、上水区;10、混合区;11、管路;12、水泵;13、开口;14、混凝搅拌器;15、布水管;16、絮凝搅拌装置;17、搅拌轴;18、下压叶桨;19、上翻叶桨;20、缓流通道;21、布水网孔;22、隔板;23、泥斗;24、斜板;25、排水槽;26、集水槽;27、集水滤管;28、过滤微孔;29、母管;30、支管;31、搅拌电机。1. Coagulation tank; 2. Flocculation tank; 3. Settling tank; 4. Outlet main; 5. Raw water main; 6. Y-type filter; 7. Gate valve; 8. Dosing pipeline; 9. Sheung Shui area; 10. Mixing area; 11. Pipeline; 12. Water pump; 13. Opening; 14. Coagulation agitator; 15. Water distribution pipe; 16. Flocculation and stirring device; 17. Stirring shaft; Upturning paddle; 20, slow flow channel; 21, water distribution mesh; 22, clapboard; 23, mud bucket; 24, inclined plate; 25, drainage groove; 28. Microporous filter; 29. Main pipe; 30. Branch pipe; 31. Stirring motor.

具体实施方式Detailed ways

下面结合具体实施例,进一步阐述本实用新型。应理解,这些实施例仅用于说明本实用新型而不用于限制本实用新型的范围。此外应理解,在阅读了本实用新型讲授的内容之后,本领域技术人员可以对本实用新型作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further set forth the utility model. It should be understood that these embodiments are only used to illustrate the present utility model and are not intended to limit the scope of the present utility model. In addition, it should be understood that after reading the content taught by the utility model, those skilled in the art can make various changes or modifications to the utility model, and these equivalent forms also fall within the scope defined by the appended claims of the application.

本实用新型所述是一种絮凝沉降设备,主体结构包括混凝罐1、絮凝池2和沉降池3,所述混凝罐1、絮凝池2和沉降池3按照工艺流程从前往后的顺序依次连通,且所述沉降池3的后端设置出水总管4,所述混凝罐1的前端设置原水总管5,所述原水总管5上还设有Y型过滤器6和闸阀7,还包括加药管路8,所述加药管路8通过闸阀7与原水总管5连通。The utility model is a flocculation settling equipment, the main structure includes a coagulation tank 1, a flocculation tank 2 and a settling tank 3, and the coagulation tank 1, flocculation tank 2 and settling tank 3 are in the order from the front to the back of the process flow connected successively, and the rear end of the settling tank 3 is provided with a water main pipe 4, and the front end of the coagulation tank 1 is provided with a raw water main pipe 5, and the raw water main pipe 5 is also provided with a Y-shaped filter 6 and a gate valve 7, and also includes A medicine adding pipeline 8 , the medicine adding pipeline 8 communicates with the raw water main pipe 5 through the gate valve 7 .

所述混凝罐1为封闭罐体,且包括内层的上水区9和外层的混合区10,所述混合区10与原水总管5相连通,所述上水区9的顶壁上设有与絮凝池2相连通的管路11,所述管路11上设有水泵12和闸阀7,所述上水区9的侧壁为窄端向下的喇叭口结构,所述上水区9的下端设置与混合区10相连通的开口13,所述开口13内设置混凝搅拌器14,所述混凝搅拌器14为斜叶开启式蜗轮搅拌器;采用混凝罐1代替传统的混凝池。由于混凝罐1为密封罐体,且内部分区布局:混合区10在外围且与原水总管5连通,加过絮凝剂的原水进入混合区10,进行初步的混合和预备,所述混凝搅拌器14高速运转,斜叶开启式蜗轮搅拌方式一方面阻力小,利于高速旋转,另一方面高速搅拌的叶片能够使水体形成向上且激烈的涡流,带动混合区10的水体上行并自开口13进入上水区9。通过上述结构和操作,使进入上水区9的原水中的细小颗粒和絮凝剂产生充分的混合和激烈的碰撞,不但保证了原水与混凝剂的均匀混合,且过程快速、短时、激烈,满足混凝的工艺要求,有利于下一步絮凝反应的进行。The coagulation tank 1 is a closed tank, and includes an inner upper water zone 9 and an outer mixing zone 10, the mixing zone 10 communicates with the raw water main pipe 5, and on the top wall of the upper water zone 9 There is a pipeline 11 communicating with the flocculation tank 2, the pipeline 11 is provided with a water pump 12 and a gate valve 7, the side wall of the upper water area 9 is a bell mouth structure with the narrow end downward, and the upper water The lower end of the zone 9 is provided with an opening 13 communicating with the mixing zone 10, and a coagulation agitator 14 is arranged in the opening 13, and the coagulation agitator 14 is an open-type worm gear agitator with inclined blades; a coagulation tank 1 is used to replace the traditional coagulation pond. Because the coagulation tank 1 is a sealed tank, and the internal partition layout: the mixing zone 10 is on the periphery and communicates with the raw water main pipe 5, the raw water added with the flocculant enters the mixing zone 10 for preliminary mixing and preparation, and the coagulation and stirring The device 14 runs at high speed, and the slanted-blade open-type worm gear stirring method has small resistance on the one hand, which is beneficial to high-speed rotation, and on the other hand, the blades of high-speed stirring can make the water body form an upward and intense vortex, driving the water body in the mixing zone 10 to go up and enter from the opening 13 Sheung Shui District 9. Through the above structure and operation, the fine particles and flocculant in the raw water entering the upper water zone 9 are fully mixed and violently collided, which not only ensures the uniform mixing of the raw water and the coagulant, but also the process is fast, short-term and intense. , to meet the technical requirements of coagulation, which is conducive to the next step of flocculation reaction.

所述絮凝池2的顶端设置布水管15,所述布水管15的进水端与管路11相连通,所述布水管15的出水端指向絮凝池2,所述布水管15的设置,能够将水均匀的注入絮凝池2中,有利于后续的分散和混合,避免同质水体的集中。所述絮凝池2内设有絮凝搅拌装置16,所述絮凝搅拌装置16包括搅拌轴17、下压叶桨18和上翻叶桨19,所述搅拌轴17位于絮凝池2的中央且为顺时针转动,所述下压叶桨18和上翻叶桨19分别为三片且环绕搅拌轴17均匀分布,有利于进行强度适中的搅拌操作;所述下压叶桨18为逆时针倾斜的折叶且位于搅拌轴17上部,结合搅拌轴17顺时针的转动,能够将水体卷入并下压,使上部的水体向轴心并向下翻卷;所述上翻叶桨19为顺时针倾斜的折叶且位于搅拌轴17下部;结合搅拌轴17顺时针的转动,能够将水体卷入并上扬,使下部的水体向轴心并向上翻卷;所述下压叶桨18和上翻叶桨19相配合,能够使水体实现自四角向中央的对流翻卷,使处于絮凝反应下的水体上下翻滚效果好,混合充分且柔和,有利于絮凝反应的进行。The top of the flocculation tank 2 is provided with a water distribution pipe 15, the water inlet end of the water distribution pipe 15 is connected with the pipeline 11, and the water outlet end of the water distribution pipe 15 points to the flocculation tank 2, and the setting of the water distribution pipe 15 can Evenly injecting water into the flocculation tank 2 is beneficial to subsequent dispersion and mixing, and avoids concentration of homogeneous water bodies. The flocculation tank 2 is provided with a flocculation stirring device 16, and the flocculation stirring device 16 includes a stirring shaft 17, a pressing blade paddle 18 and an upturning blade paddle 19, and the stirring shaft 17 is located in the center of the flocculation tank 2 and along Rotate clockwise, said down-pressing paddle 18 and upturning-up paddle 19 are three pieces respectively and are evenly distributed around the stirring shaft 17, which is conducive to a stirring operation with moderate strength; The blade is located at the top of the stirring shaft 17, combined with the clockwise rotation of the stirring shaft 17, the water body can be involved and pressed down, so that the water body at the top can be turned down towards the axis; Folding and located at the bottom of the stirring shaft 17; combined with the clockwise rotation of the stirring shaft 17, the water body can be involved and raised, so that the water body at the bottom can be rolled up towards the axis; Cooperating with each other, the water body can realize convective rolling from the four corners to the center, so that the water body under the flocculation reaction can roll up and down well, and the mixing is sufficient and soft, which is conducive to the flocculation reaction.

还包括缓流通道20,所述缓流通道20夹置于絮凝池2和沉降池3之间,且其一侧的底端与絮凝池2的底端相连通,另一侧的底端设有布水网孔21且其通过布水网孔21与沉降池3相连通,所述缓流通道20内设置顶端留有通道的隔板22;所述缓流通道20的设置,一方面给絮凝反应留出充足的反应时间,保证颗粒物的充分絮凝结合,另一方面可以通过使杂乱混流的水体进行通道式的流动和梳理,消耗掉过多的势能和动能,使水流平稳,有利于下一步沉降。所述布水网孔21的设置,用于进一步分散水流和缓和冲力,使水流柔和细密的注入沉降池3,避免扰动沉降池3内平静的水体,保证沉降的持续高效。It also includes a slow flow channel 20, the slow flow channel 20 is sandwiched between the flocculation tank 2 and the sedimentation tank 3, and the bottom end on one side communicates with the bottom end of the flocculation tank 2, and the bottom end on the other side is provided There is a water distribution mesh 21 and it communicates with the settling tank 3 through the water distribution mesh 21. The partition plate 22 with a passage at the top is set in the slow flow channel 20; the setting of the slow flow channel 20, on the one hand, gives The flocculation reaction allows sufficient reaction time to ensure the full flocculation and combination of particles. On the other hand, the chaotic and mixed flow of water can be channeled and combed to consume too much potential energy and kinetic energy, so that the water flow is stable, which is beneficial to the next step. settlement. The setting of the water distribution mesh 21 is used to further disperse the water flow and buffer the impact force, so that the water flow can be injected into the settlement tank 3 softly and finely, so as to avoid disturbing the calm water body in the settlement tank 3 and ensure the continuous and efficient settlement.

所述布水网孔21位于沉降池3池壁的中部,所述沉降池3自中部入水,有利于斜板24发挥作用和泥斗23收集杂质。所述沉降池3的底部设有泥斗23,所述沉降池3的中上部设有斜板24,缩短了沉降距离,增加了聚结面积,提高了处理量和分离效率,同时减少了水体的相互扰动,有利于絮凝物的沉积聚结,所述斜板24上沉积的杂质和水中沉淀出的杂质顺着斜板24落入下方的泥斗23中,便于集中清理收集。所述沉降池3的顶部设有多个排水槽25,所述沉降池3外壁还设有集水槽26,所述排水槽25的一端穿过沉降池3的池壁与集水槽26相连通,所述出水总管4与集水槽26相连通。The water distribution mesh 21 is located in the middle of the wall of the settling tank 3, and the settling tank 3 enters water from the middle, which is beneficial for the inclined plate 24 to play a role and the mud bucket 23 to collect impurities. The bottom of the settling tank 3 is provided with a mud bucket 23, and the middle and upper part of the settling tank 3 is provided with a sloping plate 24, which shortens the settling distance, increases the coalescence area, improves the processing capacity and separation efficiency, and reduces the amount of water Mutual disturbance is conducive to the deposition and coalescence of flocs. The impurities deposited on the sloping plate 24 and the impurities precipitated in the water fall along the sloping plate 24 into the mud bucket 23 below, which is convenient for centralized cleaning and collection. The top of the settling tank 3 is provided with a plurality of drains 25, and the outer wall of the settling tank 3 is also provided with a sump 26, and one end of the drain 25 passes through the wall of the settling tank 3 and communicates with the sump 26, The water outlet main pipe 4 communicates with the sump 26 .

本装置的工艺流程为:原水经过原水总管5进入混凝罐1的混合区10,经过混凝搅拌器14的搅拌带动作用进入混凝罐1的上水区9,再由管路11上的水泵12将处理中的水自上水区9的顶部抽取并进入布水管15,经过布水管15的分配注入絮凝池2,在混凝搅拌装置的搅拌作用下,水体自四角向中间翻卷混合,充分反应后自底端流入缓流通道20,在隔板22的阻流作用下水体呈S型流动,熟化的水体自缓流通道20底部的布水网孔21进入沉降池3的中部,并在斜板24的辅助阻挡和沉降作用下完成絮凝物的沉淀和清水的上溢,杂质沉淀入泥斗23,处理完成的清水自排水槽25进入集水槽26,并最终进入出水总管4,完成水质的净化处理。The process flow of this device is: the raw water enters the mixing zone 10 of the coagulation tank 1 through the raw water main pipe 5, enters the upper water zone 9 of the coagulation tank 1 through the agitation of the coagulation agitator 14, and then enters the upper water zone 9 of the coagulation tank 1, and then flows through the pipeline 11 The water pump 12 draws the treated water from the top of the upper water area 9 and enters the water distribution pipe 15. After being distributed by the water distribution pipe 15, it is injected into the flocculation tank 2. Under the agitation of the coagulation and stirring device, the water body is rolled and mixed from the four corners to the middle. After fully reacting, it flows into the slow-flow channel 20 from the bottom, and the water body flows in an S shape under the blocking effect of the dividing plate 22, and the mature water body enters the middle part of the settling tank 3 from the water distribution mesh 21 at the bottom of the slow-flow channel 20, and Under the auxiliary blocking and settling action of the inclined plate 24, the precipitation of flocs and the overflow of clean water are completed, and impurities are deposited into the mud bucket 23, and the treated clean water enters the water collection tank 26 from the drainage tank 25, and finally enters the water outlet main pipe 4, and completes Water purification treatment.

所述出水总管4与集水槽26相连通的一端设有集水滤管27,所述集水滤管27上设有过滤微孔28,所述出水总管4上设有闸阀7和水泵12。所述集水滤管27的设置解决了絮凝沉降末段新增污染源的问题,通过添加的过滤微孔28来物理滤除掉由于露天操作而可能落入的毛絮、落叶、灰尘等悬浮物,进一步保证水处理质量。One end of the water outlet main pipe 4 communicating with the sump 26 is provided with a water collection filter pipe 27 , and the water collection filter pipe 27 is provided with filtering micropores 28 , and the water outlet main pipe 4 is provided with a gate valve 7 and a water pump 12 . The setting of the water collection filter pipe 27 solves the problem of new pollution sources in the final stage of flocculation and sedimentation, and physically filters out suspended matter such as flocs, fallen leaves, and dust that may fall due to open-air operation through the added filter micropores 28, and further Guarantee the quality of water treatment.

所述布水管15包括母管29和支管30,所述支管30为多个且其一端均与母管29相连通,所述支管30环绕母管29均匀分布。所述布水管15采用发散布局,平面布水效果好,出水均匀分散。The water distribution pipe 15 includes a main pipe 29 and branch pipes 30 . There are multiple branch pipes 30 and one end of them all communicates with the main pipe 29 . The branch pipes 30 are evenly distributed around the main pipe 29 . The water distribution pipe 15 adopts a divergent layout, and the effect of plane water distribution is good, and the outlet water is evenly dispersed.

所述混凝罐1、絮凝池2的顶端均设有搅拌电机31。为混凝搅拌器14和絮凝搅拌装置16提供电力传动。The tops of the coagulation tank 1 and the flocculation tank 2 are equipped with stirring motors 31 . Electric drive is provided for the coagulation agitator 14 and the flocculation agitation device 16 .

所述混凝搅拌器14的转速为100~200r/min。搅拌有力,上行效果好,湍流激烈混合充分。The rotational speed of the coagulation agitator 14 is 100-200 r/min. The stirring is powerful, the upward effect is good, and the turbulent flow is intense and fully mixed.

所述絮凝搅拌装置16的转速为50~100r/min。搅拌柔和充分,保证絮凝物的完整和凝集。The rotational speed of the flocculation and stirring device 16 is 50-100 r/min. Stir gently and fully to ensure the integrity and coagulation of flocs.

实施例1:本实用新型所述是一种絮凝沉降设备,主体结构包括混凝罐1、絮凝池2和沉降池3,所述混凝罐1、絮凝池2和沉降池3按照工艺流程从前往后的顺序依次连通,且所述沉降池3的后端设置出水总管4,所述混凝罐1的前端设置原水总管5,所述原水总管5上还设有Y型过滤器6和闸阀7,还包括加药管路8,所述加药管路8通过闸阀7与原水总管5连通。Embodiment 1: The utility model describes a kind of flocculation settling equipment, the main structure includes a coagulation tank 1, a flocculation tank 2 and a settling tank 3, and the coagulation tank 1, the flocculation tank 2 and the settling tank 3 are from The order from front to back is sequentially connected, and the rear end of the settling tank 3 is provided with an outlet main pipe 4, and the front end of the coagulation tank 1 is provided with a raw water main pipe 5, and the raw water main pipe 5 is also provided with a Y-shaped filter 6 and a gate valve. 7. It also includes a dosing pipeline 8, and the dosing pipeline 8 communicates with the raw water main pipe 5 through the gate valve 7.

所述混凝罐1为封闭罐体,且包括内层的上水区9和外层的混合区10,所述混合区10与原水总管5相连通,所述上水区9的顶壁上设有与絮凝池2相连通的管路11,所述管路11上设有水泵12和闸阀7,所述上水区9的侧壁为窄端向下的喇叭口结构,所述上水区9的下端设置与混合区10相连通的开口13,所述开口13内设置混凝搅拌器14,所述混凝搅拌器14为斜叶开启式蜗轮搅拌器且转速为下压叶桨180r/min;采用混凝罐1代替传统的混凝池。由于混凝罐1为密封罐体,且内部分区布局:混合区10在外围且与原水总管5连通,加过絮凝剂的原水进入混合区10,进行初步的混合和预备,所述混凝搅拌器14高速运转,斜叶开启式蜗轮搅拌方式一方面阻力小,利于高速旋转,另一方面高速搅拌的叶片能够使水体形成向上且激烈的涡流,带动混合区10的水体上行并自开口13进入上水区9。通过上述结构和操作,使进入上水区9的原水中的细小颗粒和絮凝剂产生充分的混合和激烈的碰撞,不但保证了原水与混凝剂的均匀混合,且过程快速、短时、激烈,满足混凝的工艺要求,有利于下一步絮凝反应的进行。The coagulation tank 1 is a closed tank, and includes an inner upper water zone 9 and an outer mixing zone 10, the mixing zone 10 communicates with the raw water main pipe 5, and on the top wall of the upper water zone 9 There is a pipeline 11 communicating with the flocculation tank 2, the pipeline 11 is provided with a water pump 12 and a gate valve 7, the side wall of the upper water area 9 is a bell mouth structure with the narrow end downward, and the upper water The lower end of the zone 9 is provided with an opening 13 communicating with the mixing zone 10, and a coagulation agitator 14 is arranged in the opening 13, and the coagulation agitator 14 is an open-type worm gear agitator with inclined blades and the rotating speed is a downward pressure paddle 180r /min; the coagulation tank 1 is used instead of the traditional coagulation pool. Because the coagulation tank 1 is a sealed tank, and the internal partition layout: the mixing zone 10 is on the periphery and communicates with the raw water main pipe 5, the raw water added with the flocculant enters the mixing zone 10 for preliminary mixing and preparation, and the coagulation and stirring The device 14 runs at high speed, and the slanted-blade open-type worm gear stirring method has small resistance on the one hand, which is beneficial to high-speed rotation, and on the other hand, the blades of high-speed stirring can make the water body form an upward and intense vortex, driving the water body in the mixing zone 10 to go up and enter from the opening 13 Sheung Shui District 9. Through the above structure and operation, the fine particles and flocculant in the raw water entering the upper water zone 9 are fully mixed and violently collided, which not only ensures the uniform mixing of the raw water and the coagulant, but also the process is fast, short-term and intense. , to meet the technical requirements of coagulation, which is conducive to the next step of flocculation reaction.

所述絮凝池2的顶端设置布水管15,所述布水管15包括母管29和支管30,所述支管30为多个且其一端均与母管29相连通,所述支管30环绕母管29均匀分布。所述布水管15采用发散布局,平面布水效果好,出水均匀分散。所述母管29的进水端与管路11相连通,所述子管的出水端指向絮凝池2,所述布水管15的设置,能够将水均匀的注入絮凝池2中,有利于后续的分散和混合,避免同质水体的集中。所述絮凝池2内设有絮凝搅拌装置16,所述絮凝搅拌装置16包括搅拌轴17、下压叶桨18和上翻叶桨19,所述搅拌轴17位于絮凝池2的中央且为顺时针转动,所述絮凝搅拌装置16的转速为60r/min,所述下压叶桨18和上翻叶桨19分别为三片且环绕搅拌轴17均匀分布,有利于进行强度适中的搅拌操作;所述下压叶桨18为逆时针倾斜的折叶且位于搅拌轴17上部,结合搅拌轴17顺时针的转动,能够将水体卷入并下压,使上部的水体向轴心并向下翻卷;所述上翻叶桨19为顺时针倾斜的折叶且位于搅拌轴17下部;结合搅拌轴17顺时针的转动,能够将水体卷入并上扬,使下部的水体向轴心并向上翻卷;所述下压叶桨18和上翻叶桨19相配合,能够使水体实现自四角向中央的对流翻卷,使处于絮凝反应下的水体上下翻滚效果好,混合充分且柔和,有利于絮凝反应的进行。The top of the flocculation tank 2 is provided with a water distribution pipe 15, the water distribution pipe 15 includes a main pipe 29 and a branch pipe 30, the branch pipes 30 are multiple and one end thereof is connected with the main pipe 29, and the branch pipe 30 surrounds the main pipe 29 evenly distributed. The water distribution pipe 15 adopts a divergent layout, and the effect of plane water distribution is good, and the outlet water is evenly dispersed. The water inlet end of the main pipe 29 is connected with the pipeline 11, and the water outlet end of the sub-pipe points to the flocculation tank 2. The setting of the water distribution pipe 15 can evenly inject water into the flocculation tank 2, which is beneficial to the follow-up Dispersion and mixing to avoid concentration of homogeneous water bodies. The flocculation tank 2 is provided with a flocculation stirring device 16, and the flocculation stirring device 16 includes a stirring shaft 17, a pressing blade paddle 18 and an upturning blade paddle 19, and the stirring shaft 17 is located in the center of the flocculation tank 2 and along Clockwise rotation, the rotating speed of the flocculation stirring device 16 is 60r/min, the pressing blade paddle 18 and the turning blade paddle 19 are three pieces respectively and are evenly distributed around the stirring shaft 17, which is conducive to the stirring operation with moderate intensity; The press-down paddle 18 is a counterclockwise inclined hinge and is located on the top of the stirring shaft 17. Combining the clockwise rotation of the stirring shaft 17, the water body can be drawn in and pressed down, so that the upper water body rolls down towards the axis. The upturned blade paddle 19 is a clockwise inclined hinge and is located at the bottom of the stirring shaft 17; combined with the clockwise rotation of the stirring shaft 17, the water body can be involved and raised, so that the water body in the lower part is rolled up towards the axis; The combination of the down-pressing blade paddle 18 and the up-turning blade paddle 19 can make the water body convect and roll from the four corners to the center, so that the water body under the flocculation reaction can roll up and down well, and the mixing is sufficient and soft, which is beneficial to the flocculation reaction. conduct.

还包括缓流通道20,所述缓流通道20夹置于絮凝池2和沉降池3之间,且其一侧的底端与絮凝池2的底端相连通,另一侧的底端设有布水网孔21且其通过布水网孔21与沉降池3相连通,所述缓流通道20内设置顶端留有通道的隔板22;所述缓流通道20的设置,一方面给絮凝反应留出充足的反应时间,保证颗粒物的充分絮凝结合,另一方面可以通过使杂乱混流的水体进行通道式的流动和梳理,消耗掉过多的势能和动能,使水流平稳,有利于下一步沉降。所述布水网孔21的设置,用于进一步分散水流和缓和冲力,使水流柔和细密的注入沉降池3,避免扰动沉降池3内平静的水体,保证沉降的持续高效。It also includes a slow flow channel 20, the slow flow channel 20 is sandwiched between the flocculation tank 2 and the sedimentation tank 3, and the bottom end on one side communicates with the bottom end of the flocculation tank 2, and the bottom end on the other side is provided There is a water distribution mesh 21 and it communicates with the settling tank 3 through the water distribution mesh 21. The partition plate 22 with a passage at the top is set in the slow flow channel 20; the setting of the slow flow channel 20, on the one hand, gives The flocculation reaction allows sufficient reaction time to ensure the full flocculation and combination of particles. On the other hand, the chaotic and mixed flow of water can be channeled and combed to consume too much potential energy and kinetic energy, so that the water flow is stable, which is beneficial to the next step. settlement. The setting of the water distribution mesh 21 is used to further disperse the water flow and buffer the impact force, so that the water flow can be injected into the settlement tank 3 softly and finely, so as to avoid disturbing the calm water body in the settlement tank 3 and ensure the continuous and efficient settlement.

所述布水网孔21位于沉降池3池壁的中部,所述沉降池3自中部入水,有利于斜板24发挥作用和泥斗23收集杂质。所述沉降池3的底部设有泥斗23,所述沉降池3的中上部设有斜板24,缩短了沉降距离,增加了聚结面积,提高了处理量和分离效率,同时减少了水体的相互扰动,有利于絮凝物的沉积聚结,所述斜板24上沉积的杂质和水中沉淀出的杂质顺着斜板24落入下方的泥斗23中,便于集中清理收集。所述沉降池3的顶部设有多个排水槽25,所述沉降池3外壁还设有集水槽26,所述排水槽25的一端穿过沉降池3的池壁与集水槽26相连通,所述出水总管4与集水槽26相连通。所述出水总管4与集水槽26相连通的一端设有集水滤管27,所述集水滤管27上设有过滤微孔28,所述出水总管4上设有闸阀7和水泵12。所述集水滤管27的设置解决了絮凝沉降末段新增污染源的问题,通过添加的过滤微孔28来物理滤除掉由于露天操作而可能落入的毛絮、落叶、灰尘等悬浮物,进一步保证水处理质量。The water distribution mesh 21 is located in the middle of the wall of the settling tank 3, and the settling tank 3 enters water from the middle, which is beneficial for the inclined plate 24 to play a role and the mud bucket 23 to collect impurities. The bottom of the settling tank 3 is provided with a mud bucket 23, and the middle and upper part of the settling tank 3 is provided with a sloping plate 24, which shortens the settling distance, increases the coalescence area, improves the processing capacity and separation efficiency, and reduces the amount of water Mutual disturbance is conducive to the deposition and coalescence of flocs. The impurities deposited on the sloping plate 24 and the impurities precipitated in the water fall along the sloping plate 24 into the mud bucket 23 below, which is convenient for centralized cleaning and collection. The top of the settling tank 3 is provided with a plurality of drains 25, and the outer wall of the settling tank 3 is also provided with a sump 26, and one end of the drain 25 passes through the wall of the settling tank 3 and communicates with the sump 26, The water outlet main pipe 4 communicates with the sump 26 . One end of the water outlet main pipe 4 communicating with the sump 26 is provided with a water collection filter pipe 27 , and the water collection filter pipe 27 is provided with filtering micropores 28 , and the water outlet main pipe 4 is provided with a gate valve 7 and a water pump 12 . The setting of the water collection filter pipe 27 solves the problem of new pollution sources in the final stage of flocculation and sedimentation, and physically filters out suspended matter such as flocs, fallen leaves, and dust that may fall due to open-air operation through the added filter micropores 28, and further Guarantee the quality of water treatment.

本装置的工艺流程为:原水经过原水总管5进入混凝罐1的混合区10,经过混凝搅拌器14的搅拌带动作用进入混凝罐1的上水区9,再由管路11上的水泵12将处理中的水自上水区9的顶部抽取并进入布水管15,经过布水管15的分配注入絮凝池2,在混凝搅拌装置的搅拌作用下,水体自四角向中间翻卷混合,充分反应后自底端流入缓流通道20,在隔板22的阻流作用下水体呈S型流动,熟化的水体自缓流通道20底部的布水网孔21进入沉降池3的中部,并在斜板24的辅助阻挡和沉降作用下完成絮凝物的沉淀和清水的上溢,杂质沉淀入泥斗23,处理完成的清水自排水槽25进入集水槽26,并经过集水滤管27的物理过滤最终进入出水总管4,完成水质的净化处理。The process flow of this device is: the raw water enters the mixing zone 10 of the coagulation tank 1 through the raw water main pipe 5, enters the upper water zone 9 of the coagulation tank 1 through the agitation of the coagulation agitator 14, and then enters the upper water zone 9 of the coagulation tank 1, and then flows through the pipeline 11 The water pump 12 draws the treated water from the top of the upper water area 9 and enters the water distribution pipe 15. After being distributed by the water distribution pipe 15, it is injected into the flocculation tank 2. Under the agitation of the coagulation and stirring device, the water body is rolled and mixed from the four corners to the middle. After fully reacting, it flows into the slow-flow channel 20 from the bottom, and the water body flows in an S shape under the blocking effect of the dividing plate 22, and the mature water body enters the middle part of the settling tank 3 from the water distribution mesh 21 at the bottom of the slow-flow channel 20, and Under the auxiliary blocking and settling action of the inclined plate 24, the sedimentation of the flocs and the overflow of the clear water are completed, and the impurities are deposited into the mud bucket 23. The physical filtration finally enters the water outlet main pipe 4 to complete the water purification treatment.

实施例2:本实用新型所述是一种絮凝沉降设备,主体结构包括混凝罐1、絮凝池2和沉降池3,所述混凝罐1、絮凝池2和沉降池3按照工艺流程从前往后的顺序依次连通,且所述沉降池3的后端设置出水总管4,所述混凝罐1的前端设置原水总管5,所述原水总管5上还设有Y型过滤器6和闸阀7,还包括加药管路8,所述加药管路8通过闸阀7与原水总管5连通。Embodiment 2: The utility model describes a kind of flocculation settling equipment, the main structure includes a coagulation tank 1, a flocculation tank 2 and a settling tank 3, and the coagulation tank 1, the flocculation tank 2 and the settling tank 3 are from The order from front to back is sequentially connected, and the rear end of the settling tank 3 is provided with an outlet main pipe 4, and the front end of the coagulation tank 1 is provided with a raw water main pipe 5, and the raw water main pipe 5 is also provided with a Y-shaped filter 6 and a gate valve. 7. It also includes a dosing pipeline 8, and the dosing pipeline 8 communicates with the raw water main pipe 5 through the gate valve 7.

所述混凝罐1为封闭罐体,且包括内层的上水区9和外层的混合区10,所述混合区10与原水总管5相连通,所述上水区9的顶壁上设有与絮凝池2相连通的管路11,所述管路11上设有水泵12和闸阀7,所述上水区9的侧壁为窄端向下的喇叭口结构,所述上水区9的下端设置与混合区10相连通的开口13,所述开口13内设置混凝搅拌器14,所述混凝搅拌器14为斜叶开启式蜗轮搅拌器且转速为120r/min;采用混凝罐1代替传统的混凝池。由于混凝罐1为密封罐体,且内部分区布局:混合区10在外围且与原水总管5连通,加过絮凝剂的原水进入混合区10,进行初步的混合和预备,所述混凝搅拌器14高速运转,斜叶开启式蜗轮搅拌方式一方面阻力小,利于高速旋转,另一方面高速搅拌的叶片能够使水体形成向上且激烈的涡流,带动混合区10的水体上行并自开口13进入上水区9。通过上述结构和操作,使进入上水区9的原水中的细小颗粒和絮凝剂产生充分的混合和激烈的碰撞,不但保证了原水与混凝剂的均匀混合,且过程快速、短时、激烈,满足混凝的工艺要求,有利于下一步絮凝反应的进行。The coagulation tank 1 is a closed tank, and includes an inner upper water zone 9 and an outer mixing zone 10, the mixing zone 10 communicates with the raw water main pipe 5, and on the top wall of the upper water zone 9 There is a pipeline 11 communicating with the flocculation tank 2, the pipeline 11 is provided with a water pump 12 and a gate valve 7, the side wall of the upper water area 9 is a bell mouth structure with the narrow end downward, and the upper water The lower end of the zone 9 is provided with an opening 13 communicating with the mixing zone 10, and a coagulation agitator 14 is arranged in the opening 13, and the coagulation agitator 14 is an open-type worm gear agitator with inclined blades and the rotating speed is 120r/min; The coagulation tank 1 replaces the traditional coagulation tank. Because the coagulation tank 1 is a sealed tank, and the internal partition layout: the mixing zone 10 is on the periphery and communicates with the raw water main pipe 5, the raw water added with the flocculant enters the mixing zone 10 for preliminary mixing and preparation, and the coagulation and stirring The device 14 runs at high speed, and the slanted-blade open-type worm gear stirring method has small resistance on the one hand, which is beneficial to high-speed rotation, and on the other hand, the blades of high-speed stirring can make the water body form an upward and intense vortex, driving the water body in the mixing zone 10 to go up and enter from the opening 13 Sheung Shui District 9. Through the above structure and operation, the fine particles and flocculant in the raw water entering the upper water zone 9 are fully mixed and violently collided, which not only ensures the uniform mixing of the raw water and the coagulant, but also the process is fast, short-term and intense. , to meet the technical requirements of coagulation, which is conducive to the next step of flocculation reaction.

所述絮凝池2的顶端设置布水管15,所述布水管15的进水端与管路11相连通,所述布水管15的出水端指向絮凝池2,所述布水管15的设置,能够将水均匀的注入絮凝池2中,有利于后续的分散和混合,避免同质水体的集中。所述絮凝池2内设有絮凝搅拌装置16,所述絮凝搅拌装置16包括搅拌轴17、下压叶桨18和上翻叶桨19,所述搅拌轴17位于絮凝池2的中央且为顺时针转动,所述絮凝搅拌装置16的转速为80r/min,所述下压叶桨18和上翻叶桨19分别为三片且环绕搅拌轴17均匀分布,有利于进行强度适中的搅拌操作;所述下压叶桨18为逆时针倾斜的折叶且位于搅拌轴17上部,结合搅拌轴17顺时针的转动,能够将水体卷入并下压,使上部的水体向轴心并向下翻卷;所述上翻叶桨19为顺时针倾斜的折叶且位于搅拌轴17下部;结合搅拌轴17顺时针的转动,能够将水体卷入并上扬,使下部的水体向轴心并向上翻卷;所述下压叶桨18和上翻叶桨19相配合,能够使水体实现自四角向中央的对流翻卷,使处于絮凝反应下的水体上下翻滚效果好,混合充分且柔和,有利于絮凝反应的进行。The top of the flocculation tank 2 is provided with a water distribution pipe 15, the water inlet end of the water distribution pipe 15 is connected with the pipeline 11, and the water outlet end of the water distribution pipe 15 points to the flocculation tank 2, and the setting of the water distribution pipe 15 can Evenly injecting water into the flocculation tank 2 is beneficial to subsequent dispersion and mixing, and avoids concentration of homogeneous water bodies. The flocculation tank 2 is provided with a flocculation stirring device 16, and the flocculation stirring device 16 includes a stirring shaft 17, a pressing blade paddle 18 and an upturning blade paddle 19, and the stirring shaft 17 is located in the center of the flocculation tank 2 and along Clockwise rotation, the rotating speed of the flocculation stirring device 16 is 80r/min, the pressing blade paddle 18 and the turning blade paddle 19 are three pieces respectively and are evenly distributed around the stirring shaft 17, which is conducive to the stirring operation with moderate intensity; The press-down paddle 18 is a counterclockwise inclined hinge and is located on the top of the stirring shaft 17. Combining the clockwise rotation of the stirring shaft 17, the water body can be drawn in and pressed down, so that the upper water body rolls down towards the axis. The upturned blade paddle 19 is a clockwise inclined hinge and is located at the bottom of the stirring shaft 17; combined with the clockwise rotation of the stirring shaft 17, the water body can be involved and raised, so that the lower part of the water body can be rolled up towards the axis; The combination of the down-pressing blade paddle 18 and the up-turning blade paddle 19 can make the water body convect and roll from the four corners to the center, so that the water body under the flocculation reaction can roll up and down well, and the mixing is sufficient and soft, which is beneficial to the flocculation reaction. conduct.

还包括缓流通道20,所述缓流通道20夹置于絮凝池2和沉降池3之间,且其一侧的底端与絮凝池2的底端相连通,另一侧的底端设有布水网孔21且其通过布水网孔21与沉降池3相连通,所述缓流通道20内设置顶端留有通道的隔板22;所述缓流通道20的设置,一方面给絮凝反应留出充足的反应时间,保证颗粒物的充分絮凝结合,另一方面可以通过使杂乱混流的水体进行通道式的流动和梳理,消耗掉过多的势能和动能,使水流平稳,有利于下一步沉降。所述布水网孔21的设置,用于进一步分散水流和缓和冲力,使水流柔和细密的注入沉降池3,避免扰动沉降池3内平静的水体,保证沉降的持续高效。It also includes a slow flow channel 20, the slow flow channel 20 is sandwiched between the flocculation tank 2 and the sedimentation tank 3, and the bottom end on one side communicates with the bottom end of the flocculation tank 2, and the bottom end on the other side is provided There is a water distribution mesh 21 and it communicates with the settling tank 3 through the water distribution mesh 21. The partition plate 22 with a passage at the top is set in the slow flow channel 20; the setting of the slow flow channel 20, on the one hand, gives The flocculation reaction allows sufficient reaction time to ensure the full flocculation and combination of particles. On the other hand, the chaotic and mixed flow of water can be channeled and combed to consume too much potential energy and kinetic energy, so that the water flow is stable, which is beneficial to the next step. settlement. The setting of the water distribution mesh 21 is used to further disperse the water flow and buffer the impact force, so that the water flow can be injected into the settlement tank 3 softly and finely, so as to avoid disturbing the calm water body in the settlement tank 3 and ensure the continuous and efficient settlement.

所述布水网孔21位于沉降池3池壁的中部,所述沉降池3自中部入水,有利于斜板24发挥作用和泥斗23收集杂质。所述沉降池3的底部设有泥斗23,所述沉降池3的中上部设有斜板24,缩短了沉降距离,增加了聚结面积,提高了处理量和分离效率,同时减少了水体的相互扰动,有利于絮凝物的沉积聚结,所述斜板24上沉积的杂质和水中沉淀出的杂质顺着斜板24落入下方的泥斗23中,便于集中清理收集。所述沉降池3的顶部设有多个排水槽25,所述沉降池3外壁还设有集水槽26,所述排水槽25的一端穿过沉降池3的池壁与集水槽26相连通,所述出水总管4与集水槽26相连通。所述出水总管4与集水槽26相连通的一端设有集水滤管27,所述集水滤管27上设有过滤微孔28,所述出水总管4上设有闸阀7和水泵12。所述集水滤管27的设置解决了絮凝沉降末段新增污染源的问题,通过添加的过滤微孔28来物理滤除掉由于露天操作而可能落入的毛絮、落叶、灰尘等悬浮物,进一步保证水处理质量。The water distribution mesh 21 is located in the middle of the wall of the settling tank 3, and the settling tank 3 enters water from the middle, which is beneficial for the inclined plate 24 to play a role and the mud bucket 23 to collect impurities. The bottom of the settling tank 3 is provided with a mud bucket 23, and the middle and upper part of the settling tank 3 is provided with a sloping plate 24, which shortens the settling distance, increases the coalescence area, improves the processing capacity and separation efficiency, and reduces the amount of water Mutual disturbance is conducive to the deposition and coalescence of flocs. The impurities deposited on the sloping plate 24 and the impurities precipitated in the water fall along the sloping plate 24 into the mud bucket 23 below, which is convenient for centralized cleaning and collection. The top of the settling tank 3 is provided with a plurality of drains 25, and the outer wall of the settling tank 3 is also provided with a sump 26, and one end of the drain 25 passes through the wall of the settling tank 3 and communicates with the sump 26, The water outlet main pipe 4 communicates with the sump 26 . One end of the water outlet main pipe 4 communicating with the sump 26 is provided with a water collection filter pipe 27 , and the water collection filter pipe 27 is provided with filtering micropores 28 , and the water outlet main pipe 4 is provided with a gate valve 7 and a water pump 12 . The setting of the water collection filter pipe 27 solves the problem of new pollution sources in the final stage of flocculation and sedimentation, and physically filters out suspended matter such as flocs, fallen leaves, and dust that may fall due to open-air operation through the added filter micropores 28, and further Guarantee the quality of water treatment.

本装置的工艺流程为:原水经过原水总管5进入混凝罐1的混合区10,经过混凝搅拌器14的搅拌带动作用进入混凝罐1的上水区9,再由管路11上的水泵12将处理中的水自上水区9的顶部抽取并进入布水管15,经过布水管15的分配注入絮凝池2,在混凝搅拌装置的搅拌作用下,水体自四角向中间翻卷混合,充分反应后自底端流入缓流通道20,在隔板22的阻流作用下水体呈S型流动,熟化的水体自缓流通道20底部的布水网孔21进入沉降池3的中部,并在斜板24的辅助阻挡和沉降作用下完成絮凝物的沉淀和清水的上溢,杂质沉淀入泥斗23,处理完成的清水自排水槽25进入集水槽26,并经过集水滤管27的物理过滤最终进入出水总管4,完成水质的净化处理。The process flow of this device is: the raw water enters the mixing zone 10 of the coagulation tank 1 through the raw water main pipe 5, enters the upper water zone 9 of the coagulation tank 1 through the agitation of the coagulation agitator 14, and then enters the upper water zone 9 of the coagulation tank 1, and then flows through the pipeline 11 The water pump 12 draws the treated water from the top of the upper water area 9 and enters the water distribution pipe 15. After being distributed by the water distribution pipe 15, it is injected into the flocculation tank 2. Under the agitation of the coagulation and stirring device, the water body is rolled and mixed from the four corners to the middle. After fully reacting, it flows into the slow-flow channel 20 from the bottom, and the water body flows in an S shape under the blocking effect of the dividing plate 22, and the mature water body enters the middle part of the settling tank 3 from the water distribution mesh 21 at the bottom of the slow-flow channel 20, and Under the auxiliary blocking and settling action of the inclined plate 24, the sedimentation of the flocs and the overflow of the clear water are completed, and the impurities are deposited into the mud bucket 23. The physical filtration finally enters the water outlet main pipe 4 to complete the water purification treatment.

Claims (6)

1.一种絮凝沉降设备,包括混凝罐(1)、絮凝池(2)和沉降池(3),所述混凝罐(1)、絮凝池(2)和沉降池(3)按照工艺流程从前往后的顺序依次连通,且所述沉降池(3)的后端设置出水总管(4),所述混凝罐(1)的前端设置原水总管(5),所述原水总管(5)上还设有Y型过滤器(6)和闸阀(7),还包括加药管路(8),所述加药管路(8)通过闸阀(7)与原水总管(5)连通,其特征在于:1. a flocculation settling equipment, comprising coagulation tank (1), flocculation tank (2) and settling tank (3), described coagulation tank (1), flocculation tank (2) and settling tank (3) according to technology The flow is connected sequentially from the front to the back, and the rear end of the settling tank (3) is provided with a water outlet main pipe (4), and the front end of the coagulation tank (1) is provided with a raw water main pipe (5), and the raw water main pipe (5 ) is also provided with a Y-type filter (6) and a gate valve (7), and also includes a dosing pipeline (8), and the dosing pipeline (8) is communicated with the raw water main pipe (5) through the gate valve (7), It is characterized by: 所述混凝罐(1)为封闭罐体,且包括内层的上水区(9)和外层的混合区(10),所述混合区(10)与原水总管(5)相连通,所述上水区(9)的顶壁上设有与絮凝池(2)相连通的管路(11),所述管路(11)上设有水泵(12)和闸阀(7),所述上水区(9)的侧壁为窄端向下的喇叭口结构,所述上水区(9)的下端设置与混合区(10)相连通的开口(13),所述开口(13)内设置混凝搅拌器(14),所述混凝搅拌器(14)为斜叶开启式蜗轮搅拌器;The coagulation tank (1) is a closed tank body, and includes an upper water zone (9) of the inner layer and a mixing zone (10) of the outer layer, and the mixing zone (10) is communicated with the raw water main pipe (5), The top wall of the upper water area (9) is provided with a pipeline (11) connected to the flocculation tank (2), and the pipeline (11) is provided with a water pump (12) and a gate valve (7). The side wall of the upper water area (9) is a bell-mouth structure with the narrow end facing down, and the lower end of the upper water area (9) is provided with an opening (13) communicating with the mixing area (10), and the opening (13) ) is provided with a coagulation agitator (14), and the coagulation agitator (14) is an open-type worm gear agitator with inclined blades; 所述絮凝池(2)的顶端设置布水管(15),所述布水管(15)的进水端与管路(11)相连通,所述布水管(15)的出水端指向絮凝池(2),所述絮凝池(2)内设有絮凝搅拌装置(16),所述絮凝搅拌装置(16)包括搅拌轴(17)、下压叶桨(18)和上翻叶桨(19),所述搅拌轴(17)位于絮凝池(2)的中央且为顺时针转动,所述下压叶桨(18)和上翻叶桨(19)分别为三片且环绕搅拌轴(17)均匀分布,所述下压叶桨(18)为逆时针倾斜的折叶且位于搅拌轴(17)上部,所述上翻叶桨(19)为顺时针倾斜的折叶且位于搅拌轴(17)下部;The top of the flocculation tank (2) is provided with a water distribution pipe (15), the water inlet end of the water distribution pipe (15) communicates with the pipeline (11), and the water outlet end of the water distribution pipe (15) points to the flocculation tank ( 2), the flocculation tank (2) is provided with a flocculation stirring device (16), and the flocculation stirring device (16) includes a stirring shaft (17), a pressing blade paddle (18) and an upward turning blade paddle (19) , the stirring shaft (17) is located in the center of the flocculation tank (2) and rotates clockwise, and the pressing blade paddle (18) and the turning blade paddle (19) are three pieces respectively and surround the stirring shaft (17) Evenly distributed, the pressed blade paddle (18) is a hinged blade inclined counterclockwise and is located on the top of the stirring shaft (17), and the upward turning blade paddle (19) is a hinged blade inclined clockwise and is located on the stirring shaft (17) ) lower part; 还包括缓流通道(20),所述缓流通道(20)夹置于絮凝池(2)和沉降池(3)之间,且其一侧的底端与絮凝池(2)的底端相连通,另一侧的底端设有布水网孔(21)且其通过布水网孔(21)与沉降池(3)相连通,所述缓流通道(20)内设置顶端留有通道的隔板(22);It also includes a slow flow channel (20), the slow flow channel (20) is sandwiched between the flocculation tank (2) and the settling tank (3), and the bottom end on one side is connected to the bottom end of the flocculation tank (2) The bottom end of the other side is provided with a water distribution mesh (21) and it communicates with the settling tank (3) through the water distribution mesh (21), and the top of the slow flow channel (20) is provided with a Channel partitions (22); 所述布水网孔(21)位于沉降池(3)池壁的中部,所述沉降池(3)的底部设有泥斗(23),所述沉降池(3)的中上部设有斜板(24),所述沉降池(3)的顶部设有多个排水槽(25),所述沉降池(3)外壁还设有集水槽(26),所述排水槽(25)的一端穿过沉降池(3)的池壁与集水槽(26)相连通,所述出水总管(4)与集水槽(26)相连通。The water distribution mesh (21) is located in the middle part of the settling tank (3) wall, the bottom of the settling tank (3) is provided with a mud bucket (23), and the middle and upper part of the settling tank (3) is provided with a slope plate (24), the top of the settling tank (3) is provided with a plurality of drains (25), and the outer wall of the settling tank (3) is also provided with a sump (26), one end of the drain (25) The pool wall passing through the settling tank (3) is communicated with the sump (26), and the water outlet main pipe (4) is communicated with the sump (26). 2.根据权利要求1所述一种絮凝沉降设备,其特征在于:所述出水总管(4)与集水槽(26)相连通的一端设有集水滤管(27),所述集水滤管(27)上设有过滤微孔(28),所述出水总管(4)上设有闸阀(7)和水泵(12)。2. A kind of flocculation settling equipment according to claim 1, characterized in that: one end of the water outlet main pipe (4) communicated with the sump (26) is provided with a water collection filter pipe (27), and the water collection filter The pipe (27) is provided with filter micropores (28), and the water outlet main pipe (4) is provided with a gate valve (7) and a water pump (12). 3.根据权利要求1所述一种絮凝沉降设备,其特征在于:所述布水管(15)包括母管(29)和支管(30),所述支管(30)为多个且其一端均与母管(29)相连通,所述支管(30)环绕母管(29)均匀分布。3. A kind of flocculation settling equipment according to claim 1, characterized in that: said water distribution pipe (15) comprises a main pipe (29) and branch pipes (30), said branch pipes (30) are multiple and one end of which is It communicates with the main pipe (29), and the branch pipes (30) are evenly distributed around the main pipe (29). 4.根据权利要求1所述一种絮凝沉降设备,其特征在于:所述混凝罐(1)、絮凝池(2)的顶端均设有搅拌电机(31)。4. The flocculation settling equipment according to claim 1, characterized in that: the tops of the coagulation tank (1) and the flocculation tank (2) are equipped with stirring motors (31). 5.根据权利要求1所述一种絮凝沉降设备,其特征在于:所述混凝搅拌器(14)的转速为100~200r/min。5. The flocculation and sedimentation equipment according to claim 1, characterized in that: the rotational speed of the coagulation agitator (14) is 100-200 r/min. 6.根据权利要求1所述一种絮凝沉降设备,其特征在于:所述絮凝搅拌装置(16)的转速为50~100r/min。6 . The flocculation and sedimentation equipment according to claim 1 , characterized in that: the rotational speed of the flocculation stirring device ( 16 ) is 50-100 r/min.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105753121A (en) * 2016-04-11 2016-07-13 武汉理工大学 Adjustable novel water treatment coagulating reaction system
CN107462488A (en) * 2017-08-29 2017-12-12 上海市基础工程集团有限公司 Floccule body state estimating apparatus
CN107902738A (en) * 2017-11-20 2018-04-13 宣城环化化工科技有限公司 A kind of sewage purification flocculation plant
CN109626614A (en) * 2018-12-25 2019-04-16 苏州科太环境技术有限公司 A kind of recycle device suitable for desized wastewater
CN111807569A (en) * 2020-08-26 2020-10-23 焦作市华康糖醇科技有限公司 Pre-oxidation and coagulating sedimentation device in wastewater treatment process
CN112374649A (en) * 2020-11-11 2021-02-19 杭州国泰环保科技股份有限公司 Intelligent control effluent disposal system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105753121A (en) * 2016-04-11 2016-07-13 武汉理工大学 Adjustable novel water treatment coagulating reaction system
CN107462488A (en) * 2017-08-29 2017-12-12 上海市基础工程集团有限公司 Floccule body state estimating apparatus
CN107902738A (en) * 2017-11-20 2018-04-13 宣城环化化工科技有限公司 A kind of sewage purification flocculation plant
CN107902738B (en) * 2017-11-20 2020-03-06 广德樊缇卡信息咨询有限公司 Sewage purification flocculation device
CN109626614A (en) * 2018-12-25 2019-04-16 苏州科太环境技术有限公司 A kind of recycle device suitable for desized wastewater
CN109626614B (en) * 2018-12-25 2020-07-10 苏州科太环境技术有限公司 Recycling device suitable for desizing wastewater
CN111807569A (en) * 2020-08-26 2020-10-23 焦作市华康糖醇科技有限公司 Pre-oxidation and coagulating sedimentation device in wastewater treatment process
CN112374649A (en) * 2020-11-11 2021-02-19 杭州国泰环保科技股份有限公司 Intelligent control effluent disposal system

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