CN209564650U - A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge - Google Patents
A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge Download PDFInfo
- Publication number
- CN209564650U CN209564650U CN201821969376.3U CN201821969376U CN209564650U CN 209564650 U CN209564650 U CN 209564650U CN 201821969376 U CN201821969376 U CN 201821969376U CN 209564650 U CN209564650 U CN 209564650U
- Authority
- CN
- China
- Prior art keywords
- mud
- pond body
- sedimentation tank
- high efficiency
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 46
- 238000004062 sedimentation Methods 0.000 title claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 230000006837 decompression Effects 0.000 claims abstract description 33
- 239000004568 cement Substances 0.000 claims abstract description 9
- 239000004503 fine granule Substances 0.000 claims abstract 10
- 239000012752 auxiliary agent Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- CHQOEHPMXSHGCL-UHFFFAOYSA-N trimethaphan Chemical compound C12C[S+]3CCCC3C2N(CC=2C=CC=CC=2)C(=O)N1CC1=CC=CC=C1 CHQOEHPMXSHGCL-UHFFFAOYSA-N 0.000 claims 4
- 229940035742 trimethaphan Drugs 0.000 claims 4
- 238000005189 flocculation Methods 0.000 abstract description 6
- 230000016615 flocculation Effects 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 3
- 239000000725 suspension Substances 0.000 abstract 1
- 239000010419 fine particle Substances 0.000 description 12
- 238000000926 separation method Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000010865 sewage Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000005345 coagulation Methods 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
技术领域technical field
本实用新型属于污水处理设备技术领域,涉及沉淀池,具体涉及一种适用于细颗粒污泥的高效率竖流沉淀池。The utility model belongs to the technical field of sewage treatment equipment and relates to a sedimentation tank, in particular to a high-efficiency vertical flow sedimentation tank suitable for fine particle sludge.
背景技术Background technique
随着社会的发展,水污染越来越严重,但是人们的生活质量对水质的要求越来越高。沉淀法可以去除水中的砂粒、化学沉淀物、混凝形成的絮体和生物处理后的污泥。沉淀过程简单易行,分离效果良好,是水处理的重要过程,应用广泛,几乎是水处理过程中不可缺少的有个单元。沉淀作用有自然沉淀和絮凝沉淀两种,现有沉淀池主要分为平流沉淀池、竖流沉淀池和辐流沉淀池三种。With the development of society, water pollution is becoming more and more serious, but people's quality of life has higher and higher requirements for water quality. The sedimentation method can remove sand particles, chemical sediments, flocs formed by coagulation and sludge after biological treatment in water. The precipitation process is simple and easy, and the separation effect is good. It is an important process of water treatment and is widely used. It is almost an indispensable unit in the water treatment process. There are two types of sedimentation: natural sedimentation and flocculation sedimentation. The existing sedimentation tanks are mainly divided into three types: advection sedimentation tanks, vertical flow sedimentation tanks and radial flow sedimentation tanks.
竖流沉淀池是指池中污水竖向流动,水由设在池中心的进水管自上而下进入池内,管内设伞型挡板使废水在池中均匀分布后沿着整个过水断面缓慢上升,悬浮物由于重力进入池底锥形污泥斗中,澄清水从池四周沿周边溢流堰流出。堰前设挡板或者浮渣槽以截留浮渣,保证出水水质。池的一边靠池壁设排泥管靠静水压力将泥定期排出。竖流式沉淀池的优点是占地面积小,常用于处理水量小于20000m3/d的污水处理厂。竖流沉淀池的池体一般为圆柱形或者正方形。The vertical flow sedimentation tank refers to the vertical flow of sewage in the pool. The water enters the pool from top to bottom through the water inlet pipe set in the center of the pool. An umbrella-shaped baffle is set in the tube to make the waste water evenly distributed in the pool and then slowly flow along the entire cross-section. As it rises, the suspended matter enters the conical sludge hopper at the bottom of the pool due to gravity, and the clarified water flows out from the surrounding overflow weir around the pool. A baffle or a scum tank is installed in front of the weir to intercept the scum and ensure the quality of the effluent. On one side of the pool, a mud discharge pipe is set against the wall of the pool to discharge the mud regularly by hydrostatic pressure. The advantage of the vertical flow sedimentation tank is that it occupies a small area and is often used in sewage treatment plants with a water volume of less than 20,000m 3 /d. The tank body of the vertical flow sedimentation tank is generally cylindrical or square.
虽然竖流沉淀池具有占地面积小、操作简便等特点,但仍然存在以下问题:由于沉淀池池体高径比比较大,沉降下来的细颗粒污泥污泥容易分散堆积在锥形污泥斗的侧面,形成四周高、中间低的沉降层,剩余污泥难以及时从底部排泥口排出,容易在污泥斗侧面堆积形成死区。并且可能存在局部布水不均匀,容易死造成沉淀池出现短流甚至是死角现象,影响沉淀池细颗粒污泥悬浮杂质去除效果;混凝过程通常需要搅拌作用,需要消耗大量电能,容易将污泥搅起,影响上部清水;细颗粒污泥容易随水流出,沉淀效果不理想。Although the vertical flow sedimentation tank has the characteristics of small footprint and easy operation, there are still the following problems: due to the relatively large height-to-diameter ratio of the sedimentation tank, the settled fine-grained sludge is easy to disperse and accumulate in the conical sludge hopper The sides of the sludge hopper form a settlement layer with high surroundings and low middle. It is difficult for the remaining sludge to be discharged from the sludge outlet at the bottom in time, and it is easy to accumulate on the side of the sludge hopper to form a dead zone. And there may be local uneven water distribution, which is easy to cause short flow or even dead angle in the sedimentation tank, which affects the removal effect of fine-grained sludge suspended impurities in the sedimentation tank; the coagulation process usually requires stirring, which consumes a lot of electric energy, and it is easy to dispose of the sewage The mud is stirred up, which affects the upper clear water; the fine-grained sludge is easy to flow out with the water, and the sedimentation effect is not ideal.
发明内容Contents of the invention
针对现有技术中存在的不足,本实用新型的目的在于,提供一种适用于细颗粒污泥的高效率竖流沉淀池,以解决现有技术中的缺少适用于细颗粒污泥的高效竖流沉淀池,现有竖流沉淀池容易形成死区,细颗粒污泥随水流出而导致的细颗粒污泥去除效率较低的问题。Aiming at the deficiencies in the prior art, the purpose of this utility model is to provide a high-efficiency vertical flow sedimentation tank suitable for fine particle sludge to solve the lack of high-efficiency vertical flow sedimentation tank suitable for fine particle sludge in the prior art. Flow sedimentation tank, the existing vertical flow sedimentation tank is easy to form a dead zone, the problem of low fine particle sludge removal efficiency caused by fine particle sludge flowing out with water.
为了解决上述技术问题,本申请采用如下技术方案予以实现:In order to solve the above-mentioned technical problems, the application adopts the following technical solutions to achieve:
一种适用于细颗粒污泥的高效率竖流沉淀池,包括池体,还包括安装在池体内的中心筒、反射板、滤网和导泥挡泥板;A high-efficiency vertical flow sedimentation tank suitable for fine particle sludge, including a tank body, and also includes a central cylinder installed in the tank body, a reflector, a filter screen and a mud guide fender;
所述的中心筒、反射板、滤网和导泥挡泥板将所述的池体分隔为进水区、水泥分离区、集水区、导泥区和集泥区,所述的进水区包括中心筒侧壁和顶板内的腔体,所述的水泥分离区包括反射板和滤网之间的池体内的腔体,所述的集水区包括滤网和池体顶部开口之间的池体内的腔体,所述的导泥区包括反射板和导泥挡泥板之间的池体内的腔体,所述的集泥区包括导泥挡泥板和池体底部之间的池体内的腔体;The central tube, reflector, filter screen and mud guide fender divide the tank body into a water inlet area, a cement separation area, a water collection area, a mud guide area and a mud collection area. The area includes the cavity in the side wall of the central cylinder and the top plate, the cement separation area includes the cavity in the pool body between the reflector and the filter screen, and the water collection area includes the cavity between the filter screen and the top opening of the pool body The cavity in the pool body, the mud guide area includes the cavity in the pool body between the reflector and the mud guide fender, and the mud collection area includes the cavity between the mud guide fender and the bottom of the pool body cavities in the pool body;
所述的进水区内安装有减压降速器、进水管和扰流板,所述的减压降速器和扰流板安装于所述的中心筒内,所述的进水管安装于所述的减压降速器底部并连通所述的池体外的进水水源;The decompression decelerator, water inlet pipe and spoiler are installed in the water inlet area, the decompression decelerator and spoiler are installed in the central cylinder, and the water inlet pipe is installed in the The bottom of the decompression decelerator is connected to the water inlet outside the pool;
所述的集水区内沿所述的池体内壁设置有集水槽,所述的集水槽内圈槽壁顶端安装有溢流堰,所述的集水槽内还安装有连通池体外出水贮池的出水管;In the water collection area, a water collection tank is arranged along the inner wall of the pool, and an overflow weir is installed on the top of the inner wall of the water collection tank, and an outlet water storage tank connected to the outside of the pool is also installed in the water collection tank. the outlet pipe;
所述的集泥区安装有穿过所述的池体连通外部污泥贮池的排泥管。The mud collection area is installed with a mud discharge pipe passing through the pool body to communicate with an external sludge storage tank.
本实用新型还具有如下技术特征:The utility model also has the following technical characteristics:
具体的,所述的进水区内还安装有连通外部助剂贮箱的加药管,所述的加药管通入所述的减压降速器内。Specifically, a dosing pipe connected to an external auxiliary agent storage tank is also installed in the water inlet area, and the dosing pipe leads into the decompression decelerator.
具体的,所述的扰流板为多个间隔固接于所述的中心筒内壁或减压降速器外壁上的圆环板,所述的减压降速器、中心筒内侧筒壁和扰流板。Specifically, the spoiler is a plurality of annular plates fixed at intervals on the inner wall of the central cylinder or the outer wall of the decompression decelerator, the decompression decelerator, the inner wall of the central cylinder and the outer wall of the decompression decelerator. spoiler.
具体的,所述的减压降速器下部为圆锥体,上部为顶端开口的圆柱体。Specifically, the lower part of the decompression decelerator is a cone, and the upper part is a cylinder with an open top.
具体的,所述的减压降速器与中心筒的半径比为2:3,所述的减压降速器下部圆锥体的锥体底角α为60~65°。Specifically, the radius ratio of the decompression decelerator to the central cylinder is 2:3, and the cone base angle α of the lower cone of the decompression decelerator is 60-65°.
具体的,所述的导泥挡泥板为多片与所述的池体铰接的扇形板,倾斜拼接为圆锥形导泥筒。Specifically, the mud-guiding fender is a plurality of fan-shaped plates hinged to the pool body, which are spliced obliquely to form a conical mud-guiding cylinder.
具体的,所述的导泥挡泥板与所述的池体铰接并且可由液压杆驱动绕铰接点摆动。Specifically, the mud guide fender is hinged to the pool body and can be driven by a hydraulic rod to swing around the hinge point.
本实用新型与现有技术相比,有益的技术效果是:Compared with the prior art, the utility model has beneficial technical effects as follows:
(Ⅰ)本实用新型的适用于细颗粒污泥的高效率竖流沉淀池设置了减压降速器,减压降速器下端呈漏斗形,即圆锥体,上端为等截面的圆柱。污水从减压降速器下端进入,随着过流断面面积的增大,流速会减小,药品从上端加入,与污水对流,可以很好的混合絮凝,无需搅拌以及动力设施。减压降速器上端为具有一定高度的等截面,水流经过絮凝后由减压降速器上端溢流,可以起到均匀布水的效果。减压降速器的设置为后续的沉淀提供了保障,增加了混凝反应,可以增大颗粒粒径,同时通过增大过流断面减小了水流速度,使得水流上升速度与颗粒沉降速度的差值增大,减少了沉淀时间。混凝与沉淀共用一个构筑物,减少了占地面积且节约成本;(I) The high-efficiency vertical flow sedimentation tank suitable for fine particle sludge of the present utility model is provided with a decompression deceleration device. The lower end of the decompression deceleration device is funnel-shaped, that is, a cone, and the upper end is a cylinder of equal cross-section. Sewage enters from the lower end of the decompression decelerator. As the cross-sectional area of the flow increases, the flow rate will decrease. The medicine is added from the upper end and convects with the sewage, which can be well mixed and flocculated without stirring and power facilities. The upper end of the decompression decelerator is an equal section with a certain height, and the water flow overflows from the upper end of the decompression decelerator after flocculation, which can achieve the effect of uniform water distribution. The setting of the decompression deceleration device provides guarantee for the subsequent precipitation, increases the coagulation reaction, can increase the particle size, and at the same time reduces the water flow velocity by increasing the cross-flow section, so that the relationship between the rising speed of the water flow and the settling velocity of the particles The difference increases, reducing the settling time. Coagulation and sedimentation share one structure, which reduces floor space and saves costs;
(Ⅱ)本实用新型的适用于细颗粒污泥的高效率竖流沉淀池设置了扰流板,若是水流直接经中心筒后通过反射板反射上升,会导致流速过大,不利于沉淀分离,因此中心筒内设置交错矩形扰流板有利于加水流路径,增加扰流,缓解水流的冲击,减缓流速,同时有利于颗粒进一步絮凝沉降;(II) The high-efficiency vertical flow sedimentation tank suitable for fine particle sludge of the present utility model is equipped with a spoiler. If the water flow directly passes through the central cylinder and then rises through the reflection of the reflector, the flow rate will be too large, which is not conducive to sedimentation and separation. Therefore, setting staggered rectangular spoilers in the center tube is beneficial to add water flow path, increase turbulence, alleviate the impact of water flow, slow down the flow velocity, and at the same time facilitate the further flocculation and sedimentation of particles;
(Ⅲ)本实用新型的适用于细颗粒污泥的高效率竖流沉淀池还通过多组设置扇形导泥挡泥板,导泥挡泥板是由花瓣状的块状拼接成的环状板,可以用液压传动进行收缩,调整导泥挡泥板的倾斜角度。导泥挡泥板位于污泥斗上方,能够将沉淀下的悬浮物导向污泥斗中部,可以更快、更稳定地向污泥斗中部聚集,缓解由于池体高径比大而污泥在污泥斗侧面聚集的现象,避免污泥在污泥斗侧面堆积形成死区。同时由于导泥挡泥板的倾斜角度可以调节,因此污泥很难在导泥挡泥板上淤积。并且可以阻挡由于排泥时搅动的水中杂质再次上浮。而且导向过程类似柔性倾倒,可以提升沉降效果,进一步提升水质。(Ⅲ) The high-efficiency vertical flow sedimentation tank suitable for fine particle sludge of the present utility model is also equipped with fan-shaped mud-guiding fenders in multiple groups, and the mud-guiding fenders are ring-shaped plates spliced by petal-shaped blocks. , can use hydraulic transmission to shrink and adjust the inclination angle of the mud guide fender. The mud guide fender is located above the sludge hopper, which can guide the sedimented suspended matter to the middle of the sludge hopper, so that it can accumulate to the middle of the sludge hopper faster and more stably, and relieve the sludge in the sludge due to the large height-to-diameter ratio of the tank body. The phenomenon of accumulation on the side of the sludge hopper avoids the accumulation of sludge on the side of the sludge hopper to form a dead zone. Simultaneously, because the inclination angle of the mud-guiding fender can be adjusted, it is difficult for sludge to deposit on the mud-guiding fender. And it can prevent the impurities in the water stirred during mud discharge from floating up again. Moreover, the guiding process is similar to flexible dumping, which can improve the settlement effect and further improve the water quality.
(Ⅳ)本实用新型的适用于细颗粒污泥的高效率竖流沉淀池还通过多组设置在池体内壁设置了分隔集水区和水泥分离区的滤网,为圆环状,所有出水都会通过滤网过滤。滤网可以阻挡由水流带动的絮凝悬浮物,防止细小悬浮物流入出水,影响出水水质,可以进一步降低出水浊度。(Ⅳ) The high-efficiency vertical flow sedimentation tank suitable for fine particle sludge of the present utility model is also provided with multiple sets of filters on the inner wall of the tank to separate the water collection area and the cement separation area. will be filtered through the filter. The filter screen can block the flocculated suspended matter driven by the water flow, prevent the fine suspended matter from flowing into the effluent, affect the effluent water quality, and further reduce the turbidity of the effluent.
附图说明Description of drawings
图1是本实用新型整体结构俯视示意图;Fig. 1 is a schematic view of the overall structure of the utility model;
图2是图1的A-A面的剖视结构示意图;Fig. 2 is the sectional structure schematic diagram of A-A plane of Fig. 1;
图3是图1的B-B面的剖视结构示意图;Fig. 3 is the sectional structure schematic diagram of B-B plane of Fig. 1;
图中各个标号的含义为:1-池体,2-中心筒,3-反射板,4-滤网,5-导泥挡泥板;The meaning of each label in the figure is: 1-pool body, 2-central tube, 3-reflector, 4-filter, 5-mud guide fender;
11-进水区,12-水泥分离区,13-集水区,14-导泥区,15-集泥区;11-water intake area, 12-cement separation area, 13-water collection area, 14-mud guide area, 15-mud collection area;
111-减压降速器,112-进水管,113-扰流板,114-加药管;111-decompression reducer, 112-inlet pipe, 113-spoiler, 114-dosing pipe;
131-集水槽,132-溢流堰,133-出水管;131-sump, 132-overflow weir, 133-outlet pipe;
151-排泥管。151 - mud discharge pipe.
以下结合实施例对本实用新型的具体内容作进一步详细解释说明。Below in conjunction with embodiment the specific content of the present utility model is described in further detail.
具体实施方式Detailed ways
遵从上述技术方案,以下给出本实用新型的具体实施例,需要说明的是本实用新型并不局限于以下具体实施例,凡在本申请技术方案基础上做的等同变换均落入本实用新型的保护范围。下面结合实施例对本实用新型做进一步详细说明。Comply with above-mentioned technical scheme, provide the specific embodiment of the present utility model below, it should be noted that the utility model is not limited to the following specific embodiment, all equivalent transformations done on the basis of the technical solution of the present application all fall into the utility model scope of protection. Below in conjunction with embodiment the utility model is described in further detail.
实施例:Example:
本实施例给出一种适用于细颗粒污泥的高效率竖流沉淀池,如图1至图3 所示,包括池体1,还包括安装在池体1内的中心筒2、反射板3、滤网4和导泥挡泥板5;This embodiment provides a high-efficiency vertical flow sedimentation tank suitable for fine-grained sludge, as shown in Figures 1 to 3, including a tank body 1, a central cylinder 2 installed in the tank body 1, and a reflector 3. Filter screen 4 and mud guide fender 5;
中心筒2、反射板3、滤网4和导泥挡泥板5将池体1分隔为进水区11、水泥分离区12、集水区13、导泥区14和集泥区15,进水区11包括中心筒2 侧壁和顶板内的腔体,水泥分离区12包括反射板3和滤网4之间的池体1内的腔体,集水区13包括滤网4和池体1顶部开口之间的池体1内的腔体,导泥区14包括反射板3和导泥挡泥板5之间的池体1内的腔体,集泥区15包括导泥挡泥板5和池体1底部之间的池体1内的腔体;The central cylinder 2, the reflection plate 3, the filter screen 4 and the mud guide fender 5 divide the pool body 1 into a water inlet area 11, a cement separation area 12, a water collection area 13, a mud guide area 14 and a mud collection area 15. The water area 11 includes the cavity in the side wall of the central cylinder 2 and the roof, the cement separation area 12 includes the cavity in the pool body 1 between the reflector 3 and the filter screen 4, and the water collection area 13 includes the filter screen 4 and the pool body 1 The cavity in the pool body 1 between the top openings, the mud guide area 14 includes the cavity in the pool body 1 between the reflector 3 and the mud guide fender 5, and the mud collection area 15 includes the mud guide fender 5 and the cavity in the pool body 1 between the bottom of the pool body 1;
进水区11内安装有减压降速器111、进水管112和扰流板113,减压降速器111和扰流板113安装于中心筒2内,进水管112安装于减压降速器111 底部并连通池体1外的进水水源;The decompression deceleration device 111, water inlet pipe 112 and spoiler 113 are installed in the water inlet area 11, the decompression deceleration device 111 and the spoiler 113 are installed in the central cylinder 2, and the water inlet pipe 112 is installed in the decompression deceleration The bottom of the device 111 is connected to the water inlet source outside the pool body 1;
集水区13内沿池体1内壁设置有集水槽131,集水槽131内圈槽壁顶端安装有溢流堰132,,所述的集水槽131内还安装有连通池体1外出水贮池的出水管133;In the water collection area 13, a water collection tank 131 is arranged along the inner wall of the pool body 1, and an overflow weir 132 is installed on the top of the inner wall of the water collection tank 131. In the water collection tank 131, a water storage tank connected to the outside of the pool body 1 is also installed. The water outlet pipe 133;
集泥区15安装有穿过池体1连通外部污泥贮池的排泥管151。The mud collection area 15 is equipped with a mud discharge pipe 151 passing through the tank body 1 and communicating with an external sludge storage tank.
作为本实施例的一种具体方案,本实施例的进水区11内还安装有连通外部助剂贮箱的加药管114,加药管114通入减压降速器111内。As a specific solution of this embodiment, a dosing pipe 114 connected to an external auxiliary agent storage tank is also installed in the water inlet area 11 of this embodiment, and the dosing pipe 114 leads into the decompression deceleration device 111 .
作为本实施例的一种具体方案,本实施例的扰流板113为多个间隔固接于中心筒2内壁或减压降速器111外壁上的圆环板,减压降速器111、中心筒2 内侧筒壁和扰流板。As a specific solution of this embodiment, the spoiler 113 of this embodiment is a plurality of annular plates fixed at intervals on the inner wall of the central cylinder 2 or the outer wall of the decompression decelerator 111, the decompression decelerator 111, Central cylinder 2 inner cylinder wall and spoiler.
作为本实施例的一种具体方案,本实施例的减压降速器111下部为圆锥体,上部为顶端开口的圆柱体。As a specific solution of this embodiment, the lower part of the decompression decelerator 111 of this embodiment is a cone, and the upper part is a cylinder with an open top.
作为本实施例的一种更加具体的方案,本实施例的减压降速器111与中心筒2的半径比为2:3,减压降速器111下部圆锥体的锥体底角α为60~65°。As a more specific solution of this embodiment, the radius ratio between the decompression decelerator 111 and the central cylinder 2 of the present embodiment is 2:3, and the cone base angle α of the lower cone of the decompression decelerator 111 is 60-65°.
作为本实施例的一种具体方案,本实施例的导泥挡泥板5为多片与池体1 铰接的扇形板,倾斜拼接为圆锥形导泥筒。As a specific solution of this embodiment, the mud-guiding fender 5 of this embodiment is a plurality of fan-shaped plates hinged with the pool body 1 , which are spliced obliquely to form a conical mud-guiding cylinder.
作为本实施例的一种具体方案,本实施例的导泥挡泥板5与池体1铰接并且可由液压杆驱动绕铰接点摆动。As a specific solution of this embodiment, the mud guide fender 5 of this embodiment is hinged to the pool body 1 and can be driven by a hydraulic rod to swing around the hinge point.
本实用新型的适用于细颗粒污泥的高效率竖流沉淀池的使用通过以下步骤进行:The use of the high-efficiency vertical flow sedimentation tank suitable for fine particle sludge of the present utility model is carried out through the following steps:
步骤一:从进水管112通入待处理的含有细颗粒污泥的污水,同时从加药管114中通入絮凝药剂;Step 1: Pass the sewage containing fine particle sludge to be treated from the water inlet pipe 112, and pass the flocculant agent from the dosing pipe 114 at the same time;
步骤二:根据出水浊度调整进水管112中的进水流量和/或加药管114内的絮凝药剂的流速,定时通过液压控制装置(可以采用市售可用的控制装置) 控制导泥挡泥板5摆动多次,将絮凝沉淀后分离并暂时粘附在导泥挡泥板5 上的细颗粒污泥抖落至集泥区15,待集泥区15中的沉淀污泥集聚到一定量后和/或在设定时间间隔,将沉淀污泥由排泥管151抽排并进行后续处理;同时从溢流堰132溢出并在集水槽131内汇集的出水则由出水管133排出至出水贮池;Step 2: Adjust the flow rate of the water in the inlet pipe 112 and/or the flow rate of the flocculation agent in the dosing pipe 114 according to the turbidity of the outlet water, and control the mud guide and mud retaining through the hydraulic control device (commercially available control device can be used) at regular intervals The plate 5 swings several times, and the fine-grained sludge that is separated after flocculation and sedimentation and temporarily adheres to the mud guide fender 5 is shaken off to the sludge collection area 15, and the settled sludge in the sludge collection area 15 is to be accumulated to a certain amount. Finally and/or at a set time interval, the settled sludge is pumped out through the sludge discharge pipe 151 and subjected to subsequent treatment; at the same time, the effluent overflowing from the overflow weir 132 and collected in the sump 131 is discharged to the effluent through the outlet pipe 133. reservoir;
步骤三:重复步骤二的操作,并定时观察扰流板113和滤网4上的絮凝污泥附着情况,视需要进行清理或更换。Step 3: Repeat the operation of Step 2, and regularly observe the adhesion of the flocculated sludge on the spoiler 113 and the filter screen 4, and clean or replace it as necessary.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821969376.3U CN209564650U (en) | 2018-11-27 | 2018-11-27 | A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821969376.3U CN209564650U (en) | 2018-11-27 | 2018-11-27 | A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209564650U true CN209564650U (en) | 2019-11-01 |
Family
ID=68321181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821969376.3U Expired - Fee Related CN209564650U (en) | 2018-11-27 | 2018-11-27 | A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209564650U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111437628A (en) * | 2020-04-07 | 2020-07-24 | 吉林省舒兰合成药业股份有限公司 | Material liquid layering container |
| CN112774312A (en) * | 2021-01-13 | 2021-05-11 | 开滦(集团)有限责任公司唐山矿业分公司 | Solid-liquid separation and purification device for underground coal mine |
| CN113893607A (en) * | 2021-09-30 | 2022-01-07 | 内蒙古大中矿业股份有限公司 | Tailing overflow clarification process for iron ore filling |
| CN114602240A (en) * | 2022-03-08 | 2022-06-10 | 上海山美环保装备股份有限公司 | Efficient fine sand recovery device with centralized liquid inlet at sustainable end part |
| CN116161732A (en) * | 2022-12-29 | 2023-05-26 | 湖北福人金身药业有限公司 | A treatment system before microbial decomposition of industrial wastewater |
-
2018
- 2018-11-27 CN CN201821969376.3U patent/CN209564650U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111437628A (en) * | 2020-04-07 | 2020-07-24 | 吉林省舒兰合成药业股份有限公司 | Material liquid layering container |
| CN112774312A (en) * | 2021-01-13 | 2021-05-11 | 开滦(集团)有限责任公司唐山矿业分公司 | Solid-liquid separation and purification device for underground coal mine |
| CN113893607A (en) * | 2021-09-30 | 2022-01-07 | 内蒙古大中矿业股份有限公司 | Tailing overflow clarification process for iron ore filling |
| CN114602240A (en) * | 2022-03-08 | 2022-06-10 | 上海山美环保装备股份有限公司 | Efficient fine sand recovery device with centralized liquid inlet at sustainable end part |
| CN114602240B (en) * | 2022-03-08 | 2023-09-26 | 上海山美环保装备股份有限公司 | A high-efficiency fine sand recovery device with continuous liquid inflow at the end |
| CN116161732A (en) * | 2022-12-29 | 2023-05-26 | 湖北福人金身药业有限公司 | A treatment system before microbial decomposition of industrial wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209564650U (en) | A High Efficiency Vertical Flow Sedimentation Tank Suitable for Fine Granular Sludge | |
| CN108996740A (en) | A kind of just rain processing system and method | |
| CN114084981A (en) | Simple and efficient integrated coagulating and clarifying tank and working method | |
| CN107473339B (en) | A kind of mine water magnetic coagulation treatment device and process | |
| CN211367069U (en) | Integrated water purifier | |
| CN212334700U (en) | A high-efficiency clarification and separation device | |
| CN207632577U (en) | A kind of high-efficient vertical flow settling pond | |
| CN211367234U (en) | A clarification and separation device | |
| CN212504366U (en) | High turbid water treatment device and sewage treatment system | |
| CN220034208U (en) | Radial flow type secondary sedimentation tank capable of screening aerobic granular sludge | |
| CN110204103B (en) | Suspension medium layer filtering system based on hydraulic fluidization layering | |
| CN218860496U (en) | Floating and sinking type water purification system | |
| CN105999776A (en) | Sludge layer filtering and settling pond and method thereof | |
| CN207645963U (en) | A kind of integrating device of improved efficient sedimentation tank and sand filter | |
| CN202951293U (en) | Defecator for treating desulfurization waste water | |
| CN101879382B (en) | Sewage second-level settling pond | |
| CN108002497A (en) | From the tower High-efficient Water processing equipment that flows back | |
| CN206985883U (en) | Deck runoff pollution processing integrated apparatus | |
| CN211595130U (en) | Variable-speed upflow expansion type coagulation reaction and central water distribution integrated precipitation device | |
| CN117263318A (en) | Device and method for separating scum in polycrystalline silicon wastewater sedimentation tank | |
| CN211885522U (en) | High-efficient sewage precipitation device | |
| CN111498971B (en) | High-efficient clarification separator | |
| CN115317964A (en) | Device and method for enhancing mud-water separation | |
| CN207845358U (en) | A kind of full-automatic separation of solid and liquid sewage disposal system | |
| CN201394384Y (en) | Sewage two-stage sedimentation tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191101 |