CN202128952U - Composite flocculating and settling tank suitable for low-turbidity water - Google Patents

Composite flocculating and settling tank suitable for low-turbidity water Download PDF

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CN202128952U
CN202128952U CN201120205256U CN201120205256U CN202128952U CN 202128952 U CN202128952 U CN 202128952U CN 201120205256 U CN201120205256 U CN 201120205256U CN 201120205256 U CN201120205256 U CN 201120205256U CN 202128952 U CN202128952 U CN 202128952U
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flocculation
zone
area
water
low
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张振
刘慧�
官涤
王春丽
孙勇
米海蓉
任芝军
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Harbin Engineering University
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Abstract

本实用新型提供的是一种适用于低浊水质的复合絮凝沉淀池。包括上部的沉淀区、中部的絮凝区及下部的排泥区;沉淀区中布置有斜管沉淀层,斜管沉淀层上方为清水区及带有出水口的集水装置,斜管沉淀层下方为配水区;絮凝区中设有由电机带动的水平轴机械搅拌器,进水孔设置于絮凝区的下部;排泥区设贮泥斗、穿孔排泥管,每个搅拌器下对应一个贮泥斗。本实用新型可以同时完成絮凝和沉淀两个过程,尤其是对低浊原水的处理具有广阔前景和应用价值。

Figure 201120205256

The utility model provides a compound flocculation sedimentation tank suitable for low turbidity water quality. Including the upper sedimentation area, the middle flocculation area and the lower mud discharge area; the sedimentation area is equipped with an inclined tube sedimentation layer, above the inclined tube sedimentation layer is a clear water area and a water collection device with a water outlet, and below the inclined tube sedimentation layer It is a water distribution area; the flocculation area is equipped with a horizontal shaft mechanical agitator driven by a motor, and the water inlet is set at the lower part of the flocculation area; the mud discharge area is equipped with a mud storage bucket and a perforated mud discharge pipe, and each agitator corresponds to a storage mud bucket. The utility model can simultaneously complete two processes of flocculation and sedimentation, and has broad prospects and application value especially for the treatment of low-turbidity raw water.

Figure 201120205256

Description

一种适用于低浊水质的复合絮凝沉淀池A compound flocculation sedimentation tank suitable for low turbidity water quality

技术领域 technical field

本实用新型涉及的是一种给水处理装置,具体地说是一种复合絮凝沉淀池。The utility model relates to a water supply treatment device, in particular to a compound flocculation sedimentation tank.

背景技术 Background technique

目前国内给水厂针对地表水水源的处理工艺流程通常包括混合、絮凝、沉淀、过滤及消毒。原水与混凝剂混合后通过絮凝设备形成絮凝体,经沉淀池,絮凝体依靠重力作用从水中分离出来。At present, domestic water supply plants usually use mixing, flocculation, sedimentation, filtration and disinfection to treat surface water sources. After the raw water is mixed with the coagulant, the flocs are formed through the flocculation equipment, and the flocs are separated from the water by gravity after passing through the sedimentation tank.

絮凝是给水处理的重要环节之一。传统絮凝池的形式主要包括水力絮凝池和机械絮凝池两种。机械絮凝池是通过搅拌器浆板对水流进行搅动来完成絮凝过程。因转速可调,所以其适应水量的变化能力强,对G值的适应范围广。同时,相对水力絮凝池而言,机械絮凝池的设计絮凝时间较长,约20~25min左右。Flocculation is one of the important steps in water treatment. Traditional flocculation tanks mainly include hydraulic flocculation tanks and mechanical flocculation tanks. The mechanical flocculation tank completes the flocculation process by agitating the water flow through the agitator paddle. Due to the adjustable speed, it has a strong ability to adapt to changes in water volume and a wide range of adaptation to G value. At the same time, compared with the hydraulic flocculation tank, the design flocculation time of the mechanical flocculation tank is longer, about 20 to 25 minutes.

斜管沉淀池利用浅池理论设计,所以相对于平流沉淀池而言具有停留时间短的特点,一般也在30min以内。这一沉淀池是把水平面呈一定角度(一般60°左右)的众多斜管放置与沉淀池中构成。水从下向上流动,颗粒则沉于斜管底部,当颗粒累积到一定程度时就会自动滑下。据调查显示,部分水厂斜管沉淀池在运行过程中易出现配水不均等问题。The inclined tube sedimentation tank is designed using the shallow pool theory, so it has the characteristics of short residence time compared with the advection sedimentation tank, generally within 30 minutes. This settling tank is formed by placing many inclined pipes with a horizontal plane at a certain angle (generally about 60°) in the settling tank. The water flows from bottom to top, and the particles sink to the bottom of the inclined tube. When the particles accumulate to a certain extent, they will slide down automatically. According to the investigation, the inclined tube sedimentation tanks of some water plants are prone to problems such as uneven water distribution during operation.

我国部分地区地表水尤其是水库水呈现出浊度较低的特点,低浊水中的杂质是以细小的胶体分散体系溶于水中,由于浊度较低,胶体颗粒数目较少,颗粒碰撞而聚集的机会就少,因此形成的絮体细、少而且轻,导致后续的沉淀效果较差,进而影响出水水质。The surface water in some areas of our country, especially the reservoir water, shows the characteristics of low turbidity. The impurities in the low turbidity water are dissolved in the water in a fine colloidal dispersion system. Due to the low turbidity, the number of colloidal particles is small, and the particles collide and gather. Therefore, the formed flocs are fine, less and light, resulting in poor subsequent sedimentation effect, which in turn affects the quality of effluent water.

发明内容 Contents of the invention

本实用新型的目的在于提供一种可以同时完成絮凝和沉淀两个过程,特别适用于处理浊度较低的原水,能有效节约占地的适用于低浊水质的复合絮凝沉淀池。The purpose of the utility model is to provide a composite flocculation-sedimentation tank suitable for low-turbidity water quality, which can complete two processes of flocculation and sedimentation at the same time, is especially suitable for treating raw water with low turbidity, and can effectively save land occupation.

本实用新型的目的是这样实现的:The purpose of this utility model is achieved in that:

包括上部的沉淀区、中部的絮凝区及下部的排泥区;沉淀区中布置有斜管沉淀层,斜管沉淀层上方为清水区及带有出水口的集水装置,斜管沉淀层下方为配水区;絮凝区中设有由电机带动的水平轴机械搅拌器,进水孔设置于絮凝区的下部;排泥区设贮泥斗、穿孔排泥管,每个搅拌器下对应一个贮泥斗。Including the upper sedimentation area, the middle flocculation area and the lower mud discharge area; the sedimentation area is equipped with an inclined tube sedimentation layer, above the inclined tube sedimentation layer is a clear water area and a water collection device with a water outlet, and below the inclined tube sedimentation layer It is a water distribution area; the flocculation area is equipped with a horizontal shaft mechanical agitator driven by a motor, and the water inlet is set at the lower part of the flocculation area; the mud discharge area is equipped with a mud storage bucket and a perforated mud discharge pipe, and each agitator corresponds to a storage mud bucket.

本实用新型还可以包括:The utility model can also include:

1、斜管沉淀层中的每根斜管均为六边形。1. Each inclined tube in the inclined tube sedimentation layer is hexagonal.

2、所述水平轴机械搅拌器包括串联的多台,每台水平轴机械搅拌器中间用隔墙隔开,水平轴机械搅拌器与隔墙间保持一定距离。2. The horizontal-axis mechanical agitator includes multiple units connected in series, each horizontal-axis mechanical agitator is separated by a partition wall, and a certain distance is kept between the horizontal-axis mechanical agitator and the partition wall.

3、水平轴机械搅拌器的叶轮上设置有内外侧桨板,桨板的宽长比小于1;桨板的长度不小于叶轮直径75%;桨板的总面积不超过水流截面积的25%;桨板的长度不大于叶轮直径的75%。3. The impeller of the horizontal axis mechanical agitator is provided with inner and outer paddles, the width-to-length ratio of the paddles is less than 1; the length of the paddles is not less than 75% of the diameter of the impeller; the total area of the paddles does not exceed 25% of the cross-sectional area of the water flow ; The length of the paddle is not greater than 75% of the diameter of the impeller.

4、所述的沉淀区、絮凝区分别包括二级或二级以上,前一级沉淀区的出水口与后一级絮凝区的进水孔相连,所述排泥区设置在最后一级絮凝区的下部。4. The sedimentation zone and flocculation zone respectively include two or more stages, the water outlet of the previous stage of sedimentation zone is connected to the water inlet hole of the latter stage of flocculation zone, and the mud discharge zone is set at the last stage of flocculation lower part of the area.

5、前一级沉淀区的出水口与后一级絮凝区的进水孔之间设置有中间区。5. There is an intermediate zone between the water outlet of the previous stage of sedimentation zone and the water inlet hole of the latter stage of flocculation zone.

6、絮凝区中水平轴机械搅拌器有并排的两排,两排水平轴机械搅拌器之间有隔板。6. There are two rows of horizontal-axis mechanical agitators in the flocculation zone, and there is a partition between the two rows of horizontal-axis mechanical agitators.

本实用新型结合了机械絮凝池和斜管沉淀池的特点和功能,同时根据两者在水力停留时间上相近这一条件,提出了一种新型的复合絮凝沉淀池。根据絮凝区的不同,复合絮凝沉淀池又分为单级絮凝的基本型和多级絮凝的改进型两种。The utility model combines the characteristics and functions of the mechanical flocculation tank and the inclined tube sedimentation tank, and at the same time, according to the condition that the hydraulic retention time of the two is similar, a new type of composite flocculation sedimentation tank is proposed. According to the different flocculation areas, the composite flocculation sedimentation tank is divided into two types: the basic type of single-stage flocculation and the improved type of multi-stage flocculation.

自上而下分为三个功能区域,即沉淀区,絮凝区及排泥区。It is divided into three functional areas from top to bottom, namely, sedimentation area, flocculation area and mud discharge area.

沉淀区采用斜管沉淀工艺,每个斜管均为六边形,倾斜一定角度设置于沉淀区内。斜管上方为清水区及集水装置,斜管下方为配水区,而较高的配水区以及絮凝区的协同作用可以克服传统斜管沉淀池配水不均匀等问题。The sedimentation area adopts the inclined tube sedimentation process, and each inclined tube is hexagonal, and is installed in the sedimentation area at a certain angle. Above the inclined tube is the clear water area and water collection device, and below the inclined tube is the water distribution area, and the synergistic effect of the higher water distribution area and the flocculation area can overcome the problems of uneven water distribution in traditional inclined tube sedimentation tanks.

进水孔设置于絮凝区的下部,为配水均匀,可从池体较长一侧进水,絮凝区设有水平轴机械搅拌器,由电机带动,若设置多台搅拌器,可在中间用隔墙隔开,搅拌器与隔墙间保持一定距离。设置内外侧桨板各4块,桨板的设计尽量满足以下条件:①桨板宽长比小于1;②桨板长度不小于叶轮直径75%,宽度小于300mm且大于100mm;③桨板的总面积不超过水流截面积的25%;④桨板长度不大于叶轮直径的75%。The water inlet hole is set at the lower part of the flocculation area, in order to distribute water evenly, and the water can be taken in from the longer side of the tank body. The flocculation area is equipped with a horizontal shaft mechanical agitator, which is driven by a motor. The partition wall is separated, and a certain distance is kept between the agitator and the partition wall. Set up 4 inner and outer paddles each, and the design of the paddles shall meet the following conditions as far as possible: ①The width-to-length ratio of the paddles is less than 1; ②The length of the paddles is not less than 75% of the diameter of the impeller, and the width is The area does not exceed 25% of the cross-sectional area of the water flow; ④The length of the paddle is not greater than 75% of the diameter of the impeller.

排泥区设贮泥斗,每个搅拌器下对应一个,采用穿孔排泥管排泥。There is a mud storage bucket in the mud discharge area, one corresponding to each agitator, and a perforated mud discharge pipe is used to discharge mud.

原水经投药混合后,从絮凝区的下部进入池中,水流自下向上流动,经过絮凝后进入沉淀区,沉淀区的颗粒杂质沿斜管滑入絮凝区增加了原水在絮凝过程中的浊度,而水中颗粒数量的提高增强了颗粒间的碰撞作用,同时,从沉淀区滑落的较大颗粒可以作为载体吸附较小絮体。由于搅拌速度较慢,当形成的絮体大到一定程度时,将下沉到排泥区,通过穿孔排泥管排出。The raw water enters the tank from the lower part of the flocculation zone after being mixed with chemicals. The water flows from bottom to top and enters the sedimentation zone after flocculation. The particulate impurities in the sedimentation zone slide into the flocculation zone along the inclined tube, which increases the turbidity of the raw water during the flocculation process. , and the increase in the number of particles in the water enhances the collision between particles, and at the same time, the larger particles that slide down from the sedimentation zone can act as a carrier to adsorb smaller flocs. Due to the slow stirring speed, when the formed flocs are large to a certain extent, they will sink to the mud discharge area and be discharged through the perforated mud discharge pipe.

根据絮凝效果,也可以沿水流方向在复合絮凝沉淀池中设置多系列搅拌器,G值依次降低,即改进型复合絮凝沉淀池。According to the flocculation effect, multiple series of agitators can also be installed in the composite flocculation sedimentation tank along the direction of water flow, and the G value will decrease in turn, that is, the improved composite flocculation sedimentation tank.

改进型复合絮凝沉淀池设置三级絮凝或多级絮凝,沿水流方向以串联的形式连接两级或多级处理段,每级处理段自上而下设置沉淀区及絮凝区,设置方式与基本型相似,但在絮凝区的下部可不设排泥区。各级处理段中絮凝区内搅拌器转速及G值依次降低,并用隔板隔开,隔板下方设置过水孔。在最后一级絮凝之前可设置中间区,来水经前部处理段处理后在中间区重新混合,从最后一级处理段絮凝区的下方进入,最后一级处理段与基本型的设置形式大体一致。The improved compound flocculation sedimentation tank is equipped with three-stage flocculation or multi-stage flocculation, and two or more stages of treatment sections are connected in series along the water flow direction, and each stage of treatment section is set up from top to bottom. The type is similar, but there is no mud discharge area in the lower part of the flocculation area. The rotation speed and G value of the agitator in the flocculation area of each treatment section are reduced in turn, and are separated by partitions, and water holes are set under the partitions. Before the final stage of flocculation, an intermediate zone can be set up. The incoming water is remixed in the intermediate zone after being treated by the front treatment section, and enters from the bottom of the last stage of flocculation zone. unanimous.

对这一新型复合絮凝沉淀池的改进,除上述改进型在最后一级处理段之间设置一个中间区外,还可以有多种方式,例如:1、不加入中间区,而将多级处理段均以串联的形式连接,其斜管的上部设置统一的集水槽;2、在每级处理段之间均加入一段中间区。具体的实施方案应根据原水水质及实际处理效果而定。For the improvement of this new type of composite flocculation sedimentation tank, in addition to setting an intermediate zone between the last stage of the above-mentioned improved type, there are also many ways, for example: 1. Instead of adding the intermediate zone, multi-stage treatment The sections are all connected in series, and a unified sump is set on the upper part of the inclined pipe; 2. An intermediate zone is added between each treatment section. The specific implementation plan should be determined according to the raw water quality and the actual treatment effect.

本实用新型的优越性和有益效果:Advantages and beneficial effects of the utility model:

①在絮凝区形成的絮体,经沉淀区沉淀后沿斜管重新进入絮凝区,有效提高了原水的浊度,解决了低浊原水在絮凝过程中因颗粒间的碰撞机会少而无法形成密实絮体这一问题。① The flocs formed in the flocculation zone, after settling in the sedimentation zone, re-enter the flocculation zone along the inclined pipe, which effectively increases the turbidity of the raw water, and solves the problem that the low-turbidity raw water cannot form compactness due to the lack of collision opportunities between particles during the flocculation process. The problem of flocs.

另外,滑落的絮体已经在斜管上经过了一定时间的累积,这种大而密实的絮体进入絮凝区后其本身就具有对较小絮体较好的吸附能力,在絮凝过程中充当载体的作用。密实絮体的形成不仅可以使水中杂质颗粒有效的沉淀,还可以提高对吸附在絮体表面的非溶解性有机物的去除效果,同时还可以解决目前很多净水厂斜管沉淀池在运行过程中出现的跑矾花等问题;In addition, the falling flocs have been accumulated on the inclined tube for a certain period of time. After entering the flocculation zone, the large and dense flocs themselves have better adsorption capacity for smaller flocs, and act as The role of the carrier. The formation of dense flocs can not only effectively precipitate the impurity particles in the water, but also improve the removal effect of insoluble organic matter adsorbed on the surface of the flocs. There are problems such as running alum flowers;

②经絮凝后的水在搅拌器的带动下均匀的自下而上进入斜管中,可以解决传统斜管沉淀池容易出现的配水不均等问题;②The flocculated water enters the inclined tube evenly from bottom to top under the drive of the agitator, which can solve the problem of uneven water distribution that is easy to occur in traditional inclined tube sedimentation tanks;

③原水经投药混合进入复合絮凝沉淀池后可以同时完成絮凝和沉淀两个过程,使传统的给水处理工艺得到了一定程度的简化,同时一个复合絮凝沉淀池取代了絮凝池和沉淀池,有效节约了占地。③The raw water can be mixed into the compound flocculation and sedimentation tank after being dosed and mixed, and the two processes of flocculation and sedimentation can be completed at the same time, which simplifies the traditional water supply treatment process to a certain extent. occupied land.

④当原水浊度较小时,这一新型复合絮凝沉淀池与传统的处理工艺相比,可以较好的提高出水的浊度去除率以及有机物去除率,改善处理效果。④ When the turbidity of the raw water is small, compared with the traditional treatment process, this new type of composite flocculation sedimentation tank can better improve the turbidity removal rate and organic matter removal rate of the effluent, and improve the treatment effect.

附图说明 Description of drawings

图1是本实用新型的功能区域示意图;Fig. 1 is the functional area schematic diagram of the present utility model;

图2是本实用新型的基本型结构示意图;Fig. 2 is the basic structural representation of the utility model;

图3是絮凝区平面示意图;Fig. 3 is a schematic plan view of the flocculation zone;

图4是层沉淀区平面示意图;Fig. 4 is a schematic plan view of layer precipitation area;

图5是排泥区平面示意图;Figure 5 is a schematic plan view of the mud discharge area;

图6是本实用新型的一种改进型结构示意图;Fig. 6 is a kind of improved structure schematic diagram of the utility model;

图7是搅拌桨示意图。Figure 7 is a schematic diagram of a stirring paddle.

具体实施方式 Detailed ways

下面结合附图举例对本实用新型做更详细的描述:The utility model is described in more detail below in conjunction with accompanying drawing example:

结合图1,本实用新型的复合絮凝沉淀池,可以分为三个功能区域,即沉淀区、絮凝区以及排泥区。Referring to Figure 1, the composite flocculation-sedimentation tank of the present invention can be divided into three functional areas, namely, the sedimentation area, the flocculation area and the mud discharge area.

结合图2,配水区4、斜管5、集水渠7、集水槽8以及清水区6属于沉淀区。3为絮凝区,在絮凝区中设置有搅拌器2。1为进水孔,设置于絮凝区的下部。10为排泥区,在池体的最下部,其中9为穿孔排泥管。Referring to Figure 2, the water distribution area 4, the inclined pipe 5, the water collecting channel 7, the sump 8 and the clean water area 6 belong to the sedimentation area. 3 is a flocculation zone, in which an agitator 2 is set. 1 is a water inlet, which is set in the lower part of the flocculation zone. 10 is the mud discharge area, at the bottom of the pool body, wherein 9 is the perforated mud discharge pipe.

结合图3,絮凝区中搅拌器2分若干段串联设置,由两台电机12控制,电机12与搅拌器2之间设置防水套管11,搅拌器与隔墙间留有一定的间距。Referring to Fig. 3, the agitator 2 in the flocculation zone is arranged in series in several sections, controlled by two motors 12, a waterproof casing 11 is set between the motor 12 and the agitator 2, and a certain distance is left between the agitator and the partition wall.

结合图4,沉淀区中5为设置于沉淀区内的六边形斜管。斜管的上部为集水渠7,处理后的水由其收集后汇入一侧集水槽8中,并通过出水管13进入下一个处理单元。走道板14设置于该池最上方,用于操作人员行走,以及冲洗、维护设备。Referring to FIG. 4 , 5 in the precipitation zone is a hexagonal inclined tube arranged in the precipitation zone. The upper part of the inclined pipe is a water collection channel 7, and the treated water is collected by the water collection channel 8 on one side, and enters the next processing unit through the water outlet pipe 13. The walkway plate 14 is arranged on the uppermost part of the pool, and is used for walking by operators, washing and maintaining equipment.

结合图5,底层排泥区中进水孔1位于该区域的上方,排泥区10主要由若干个排泥斗组成,9为其中的穿孔排泥管,用于向外排放污泥。Referring to Fig. 5, the inlet hole 1 in the bottom mud discharge area is located above the area, and the mud discharge area 10 is mainly composed of several mud discharge buckets, and 9 is a perforated mud discharge pipe therein, which is used to discharge sludge outward.

实施例1Example 1

图1-图5给出的是一种基本型絮凝沉淀池,水流方向如图2箭头所示,水经加药充分混合后由进水孔1进入絮凝区3的下部,并自下而上流动,经在搅拌器2缓慢搅拌下形成絮体后进入配水区4,配水区4的设置目的使为了水流能够均匀进入斜管5,在斜管5流动过程中,水质杂质沉于斜管5上,水流向上进入清水区6,再由集水槽8汇入集水渠7中,从出水管13进入下一个处理单元。Figure 1-Figure 5 shows a basic type of flocculation sedimentation tank, the direction of water flow is shown by the arrow in Figure 2, after the water is fully mixed with chemicals, it enters the lower part of the flocculation zone 3 from the water inlet 1, and flows from bottom to top Flow, after forming flocs under the slow stirring of the agitator 2, it enters the water distribution area 4. The purpose of setting the water distribution area 4 is to allow the water flow to enter the inclined pipe 5 evenly. During the flow of the inclined pipe 5, the water impurities sink in the inclined pipe 5 Above, the water flows upward into the clear water area 6, and then merges into the water collection channel 7 from the sump 8, and enters the next processing unit from the outlet pipe 13.

实施例2Example 2

图6给出的是一种改进型复合絮凝沉淀池。其特点是在池内设置多级絮凝,图6中为3级絮凝,在第1、2级絮凝后,第3级絮凝前设置中间区16。设置中间区的目的是,由于前两级絮凝过程中搅拌器2的搅拌速度快,絮体形成少,经斜管5沉淀后可能仍然无法达到满意的浊度去除效果,所以水在第1、2级絮凝后由集水渠7汇集后经中间区重新进入第3级絮凝。图6中箭头所示为水流运动方向。Figure 6 shows an improved composite flocculation sedimentation tank. It is characterized in that multi-stage flocculation is set in the pool, in Figure 6 it is 3-stage flocculation, after the 1st and 2nd stage flocculation, an intermediate zone 16 is set before the 3rd stage flocculation. The purpose of setting the intermediate zone is that, due to the fast stirring speed of the agitator 2 in the first two stages of flocculation process, the formation of flocs is less, and the satisfactory turbidity removal effect may still not be achieved after sedimentation in the inclined tube 5, so the water in the first, After the second-stage flocculation, it is collected by the water collection channel 7 and then re-enters the third-stage flocculation through the middle area. The arrows in Figure 6 show the direction of water flow.

中间区16的设置与否,以及采用单级絮凝还是多级絮凝,配水区4的高度等均应根据原水水质及实际絮凝情况做调整。Whether the intermediate zone 16 is set or not, whether single-stage flocculation or multi-stage flocculation is used, and the height of the water distribution zone 4 should be adjusted according to the raw water quality and actual flocculation conditions.

实施例3Example 3

絮凝区3,在搅拌器2的缓慢搅拌过程中会生成体积密度均较小的絮体,这些絮体随水流向上进入沉淀区并在斜管5中沉积,当沉积到一定程度会以较大的形态重新滑落至絮凝区3中;这些较大的絮体随搅拌器2旋转,并在这一过程中吸附新生成的较小絮体;在吸附的过程中絮体的体积密度会进一步增大,最后向下沉降至排泥区10,由穿孔排泥管9排出,这一过程要求搅拌器搅拌速度足够慢。In the flocculation zone 3, flocs with a small volume density will be generated during the slow stirring process of the agitator 2, and these flocs will enter the sedimentation zone with the water flow upwards and deposit in the inclined tube 5. The shape of the flocs slides back into the flocculation zone 3; these larger flocs rotate with the agitator 2, and in this process absorb the newly formed smaller flocs; the bulk density of the flocs will further increase during the adsorption process. Large, finally sink down to the mud discharge area 10, and be discharged from the perforated mud discharge pipe 9. This process requires the stirring speed of the agitator to be slow enough.

Claims (8)

1. a composite flocculation sedimentation basin that is applicable to low-cloudy water matter is characterized in that: comprise the settling zone on top, the flocculation zone at middle part and the sludge discharging area of bottom; Be furnished with the tube settling layer in the settling zone, tube settling layer top is clear water zone and the captation that has delivery port, and tube settling layer below is water distributing area; Be provided with the trunnion axis mechanical agitator by driven by motor in the flocculation zone, the inlet opening is arranged at the bottom of flocculation zone; Sludge discharging area is established storage bucket, perforated sludge discharge pipe, the corresponding down storage bucket of each agitator.
2. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 1 is characterized in that: every inclined tube in the tube settling layer is hexagon.
3. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 2; It is characterized in that: said trunnion axis mechanical agitator comprises many of series connection; Separate with partition wall in the middle of every trunnion axis mechanical agitator, keep certain distance between trunnion axis mechanical agitator and partition wall.
4. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 3 is characterized in that: outside paddle board in the impeller of trunnion axis mechanical agitator is provided with, and the breadth length ratio of paddle board is less than 1; The length of paddle board is not less than impeller diameter 75%; The gross area of paddle board be no more than water flow section long-pending 25%; The length of paddle board is not more than 75% of impeller diameter.
5. according to any one described composite flocculation sedimentation basin that is applicable to low-cloudy water matter of claim 1-4; It is characterized in that: described settling zone, flocculation zone comprise secondary respectively or more than the secondary; The delivery port of previous stage settling zone links to each other with the inlet opening of back one-level flocculation zone, and said sludge discharging area is arranged on the bottom of afterbody flocculation zone.
6. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 5 is characterized in that: be provided with the mesozone between the inlet opening of the delivery port of previous stage settling zone and back one-level flocculation zone.
7. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 5 is characterized in that: the trunnion axis mechanical agitator comprises two rows side by side in the flocculation zone, between the two row of horizontal shaft mechanical agitators dividing plate is arranged.
8. the composite flocculation sedimentation basin that is applicable to low-cloudy water matter according to claim 6 is characterized in that: the trunnion axis mechanical agitator comprises two rows side by side in the flocculation zone, between the two row of horizontal shaft mechanical agitators dividing plate is arranged.
CN201120205256U 2011-06-17 2011-06-17 Composite flocculating and settling tank suitable for low-turbidity water Expired - Fee Related CN202128952U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102258890A (en) * 2011-06-17 2011-11-30 哈尔滨工程大学 Composite flocculating and settling pond for low-turbidity water
CN109475791A (en) * 2016-07-06 2019-03-15 格雷迪安特公司 Solids treatment and correlation technique in water treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102258890A (en) * 2011-06-17 2011-11-30 哈尔滨工程大学 Composite flocculating and settling pond for low-turbidity water
CN109475791A (en) * 2016-07-06 2019-03-15 格雷迪安特公司 Solids treatment and correlation technique in water treatment system

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