CN201848130U - Activated sludge settling tank - Google Patents
Activated sludge settling tank Download PDFInfo
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- CN201848130U CN201848130U CN2010206125633U CN201020612563U CN201848130U CN 201848130 U CN201848130 U CN 201848130U CN 2010206125633 U CN2010206125633 U CN 2010206125633U CN 201020612563 U CN201020612563 U CN 201020612563U CN 201848130 U CN201848130 U CN 201848130U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
Description
技术领域technical field
本实用新型涉及一种沉淀池,尤其是涉及污水处理过程中活性污泥的沉淀池,属于给排水工程技术领域。The utility model relates to a sedimentation tank, in particular to a sedimentation tank for activated sludge in the sewage treatment process, and belongs to the technical field of water supply and drainage engineering.
背景技术Background technique
在污水处理过程中,活性污泥法由于处理成本低,在污水处理行业中得到了广泛的运用。活性污泥的沉淀、浓缩和回流受到扰动后会上浮,影响了沉淀池的出水。因此,沉淀池的沉淀和浓缩、回流效果是在污水处理行业发展中的一个重要课题。In the sewage treatment process, the activated sludge method has been widely used in the sewage treatment industry due to its low treatment cost. The sedimentation, concentration and reflux of activated sludge will float up after being disturbed, which affects the effluent of the sedimentation tank. Therefore, the sedimentation, concentration and reflux effect of the sedimentation tank is an important topic in the development of the sewage treatment industry.
沉淀池是活性污泥工艺中的关键构筑物之一。活性污泥中的微生物处理污水中的污染物后,和污水一同进入沉淀池,通过沉淀池的沉淀,浓缩后部分污泥回流,剩余污泥排放。回流污泥的方式主要依靠水泵进行提升回流。沉淀、浓缩、回流污泥效果直接影响了活性污泥工艺处理的运行。The sedimentation tank is one of the key structures in the activated sludge process. After the microorganisms in the activated sludge treat the pollutants in the sewage, they enter the sedimentation tank together with the sewage, pass through the sedimentation in the sedimentation tank, and after concentration, part of the sludge returns, and the remaining sludge is discharged. The way of returning sludge mainly relies on water pumps to lift and return. The effects of sedimentation, concentration and return sludge directly affect the operation of activated sludge process.
现有常用的沉淀池主要有三种,一种为竖流式沉淀池,此种类型的沉淀池主要用于中小型污水处理厂,存在水深高,容量较小,对于冲击负荷和温度的变化适应能力差,施工难度大,造价高等缺点。一种为平流式沉淀池,此种类型的沉淀池存在这配水不均匀,排泥操作量大,占地面积大等缺点。另一种为辐流式沉淀池,此种类型的沉淀池存在着机械设备在水下,易腐蚀,且设备刮板与池底的间距的大小决定了污泥浓缩和刮泥的效果,对于施工的质量要求很高。实际运行资料表明,三种沉淀池均存在悬浮物的去除率不高,去除率一般只有50%~60%。因此,结合三种沉淀池的优点对现有沉淀池的改进是很有必要的。There are mainly three types of sedimentation tanks commonly used at present. One is vertical flow sedimentation tank. This type of sedimentation tank is mainly used in small and medium-sized sewage treatment plants. It has high water depth and small capacity. The ability is poor, the construction is difficult, and the cost is high. One is a flat flow sedimentation tank, which has the disadvantages of uneven water distribution, large amount of sludge discharge, and large floor space. The other is the radial flow sedimentation tank. In this type of sedimentation tank, there are mechanical equipment under water, which is easy to corrode, and the distance between the equipment scraper and the bottom of the pool determines the effect of sludge concentration and scraping. For The quality of the construction was high. Actual operation data show that the removal rate of suspended solids in all three kinds of sedimentation tanks is not high, and the removal rate is generally only 50% to 60%. Therefore, it is necessary to improve the existing sedimentation tanks by combining the advantages of the three types of sedimentation tanks.
发明内容Contents of the invention
本实用新型的目的是提供一种不需要机械设备、浓缩和回流效果好、悬浮物去除效率高的一种活性污泥沉淀池。The purpose of the utility model is to provide an activated sludge sedimentation tank which does not require mechanical equipment, has good concentration and reflux effects, and has high removal efficiency of suspended matter.
为了实现以上目的,本实用新型采用的技术方案是:一种活性污泥沉淀池,包括沉淀池池体、进水区、出水区、排泥口、沉淀区、积泥区,所述沉淀区和出水区分为两端,呈“L”型布置,沉淀区设置一与水平方向呈60~70度的斜板,沉淀区与水平呈60~75度设置,沉淀区与积泥区的泥斗相连,进水区与泥斗呈偏心布置,进水区设置有喇叭口,出水区有出水堰和出水管道。In order to achieve the above purpose, the technical solution adopted by the utility model is: an activated sludge sedimentation tank, including a sedimentation tank body, a water inlet area, a water outlet area, a mud discharge port, a sedimentation area, and a mud accumulation area, and the sedimentation area The water outlet area is divided into two ends, arranged in an "L" shape. The sedimentation area is equipped with a sloping plate at 60-70 degrees to the horizontal direction, and the sedimentation area is set at 60-75 degrees to the horizontal direction. Connected, the water inlet area and the mud bucket are arranged eccentrically, the water inlet area is equipped with a bell mouth, and the water outlet area has an outlet weir and an outlet pipe.
所述出水堰为齿形出水堰,出水堰上设置挡板。The water outlet weir is a toothed water outlet weir, and a baffle plate is arranged on the water outlet weir.
所述积泥区的泥斗为锥形泥斗,泥斗与水平呈75~89度设置,泥斗内四周布置有排泥管道,排泥位置在泥斗上部。The mud hopper in the mud accumulation area is a conical mud hopper, and the mud hopper is set at 75-89 degrees to the horizontal. There are mud discharge pipes arranged around the mud hopper, and the mud discharge position is on the upper part of the mud hopper.
所述积泥区泥斗中心位置设置有回流管道,回流管道距离池底距离在200mm~1000mm之间。A return pipe is provided at the center of the mud hopper in the mud accumulation area, and the distance between the return pipe and the bottom of the pool is between 200 mm and 1000 mm.
本实用新型结合了竖流式沉淀池和平流式沉淀池的优点,沉淀区的面积大大超过了进水区的面积,沉淀流速大大减缓,沉淀时间较长,有利于悬浮物的沉淀。带有一定倾角的沉淀区和设置的斜板,对污泥的浓缩起了较大的作用,在气提动力的作用下回流,确保了浓缩和回流的连续性,不需要机械设备刮泥浓缩,也不需要水泵等设备进行提升回流。四周布置的排泥管道在气提动力的作用下,可以正常排泥不留死角,避免了死角的污泥厌氧消化上浮。The utility model combines the advantages of the vertical flow sedimentation tank and the flat flow sedimentation tank. The area of the sedimentation area greatly exceeds the area of the water intake area, the sedimentation flow rate is greatly slowed down, and the sedimentation time is longer, which is beneficial to the sedimentation of suspended matter. The settling area with a certain inclination and the set inclined plate play a greater role in the concentration of sludge, and the reflux under the action of air lift power ensures the continuity of concentration and reflux, without the need for mechanical equipment to scrape sludge and concentrate , and does not require equipment such as water pumps for lifting backflow. Under the action of air lift power, the sludge discharge pipelines arranged around can discharge sludge normally without leaving dead angles, avoiding the anaerobic digestion and floating of sludge in dead angles.
综上所述,本实用新型具有结构简单、悬浮物去除效率高、不需要机械设备,运行管理方便的优点。In summary, the utility model has the advantages of simple structure, high removal efficiency of suspended solids, no need for mechanical equipment, and convenient operation and management.
附图说明Description of drawings
图1为本实用新型的结构平面示意图;Fig. 1 is a structural plan view of the utility model;
图2为本实用新型的结构立面示意图;Fig. 2 is the structural elevation schematic diagram of the utility model;
图是,1是进水管道,2是排泥管道,3是沉淀区,4是积泥区,5是出水堰,6是回流管道,7是进水区,8是出水管道。In the picture, 1 is the water inlet pipe, 2 is the mud discharge pipe, 3 is the sedimentation area, 4 is the mud accumulation area, 5 is the outlet weir, 6 is the return pipe, 7 is the water inlet area, and 8 is the water outlet pipe.
具体实施方式Detailed ways
以下结合附图和具体实施方式对本实用新型予以详细说明。The utility model will be described in detail below in conjunction with the accompanying drawings and specific embodiments.
从图1、图2可知,本实用新型包括沉淀池池体、进水区7、出水区、排泥管道2、回流管道6,沉淀区和出水区分为两端,呈“L”型布置,沉淀区设置与水平方向呈60~70度的斜板,用以增大沉淀面积,沉淀区与水平呈60~75度设置,沉淀区与积泥区泥斗相连。出水区有两个,布置在“L”型的两端,每个出水区包括出水管道8和出水堰5,出水堰采用齿形出水堰,出水堰上设置污泥和浮渣挡板。污泥浮渣通过出水区的浮渣口排除。进水区7与泥斗呈偏心布置,设置一进水喇叭口,污水呈辐射状进入沉淀区。积泥区为锥形泥斗,泥斗与水平呈75~89度设置,泥斗内设置排泥管道2,排泥管道呈四周布置,排泥位置在泥斗上部,采用气提排泥的方式。在泥斗中心位置设置回流管道6,污泥管道距离池底距离200mm~1000mm之间。It can be seen from Fig. 1 and Fig. 2 that the utility model includes a sedimentation tank body, a
工作过程:活性污泥和污水从进水管道1中进入沉淀池池体,从图2中的进水区7的喇叭口呈辐射状进入沉淀区3,活性污泥在沉淀区3中的斜板作用下,活性污泥在流速变缓的情况下下沉,由于沉淀区底部与水平呈60~75度角,污泥下滑至积泥区4,积泥区通过四周布管,在气提的动力下利用排泥管道2排除。污泥回流通过气提,利用回流管道6回流至活性污泥工艺单元。经过泥水分离后的污水经过出水堰5和进入下一个处理流程单元。Working process: activated sludge and sewage enter the sedimentation tank body from the
本实用新型的气提动力可来自于鼓风曝气的风管或者空压机。需要的气量根据需要处理的污水量来决定,需要气提深度可根据运行需要进行调节。The air lifting power of the utility model can come from the wind pipe or the air compressor of blast aeration. The required gas volume is determined according to the amount of sewage to be treated, and the required gas lift depth can be adjusted according to operational needs.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206125633U CN201848130U (en) | 2010-11-18 | 2010-11-18 | Activated sludge settling tank |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206125633U CN201848130U (en) | 2010-11-18 | 2010-11-18 | Activated sludge settling tank |
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| CN201848130U true CN201848130U (en) | 2011-06-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010206125633U Expired - Lifetime CN201848130U (en) | 2010-11-18 | 2010-11-18 | Activated sludge settling tank |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103482744A (en) * | 2013-09-27 | 2014-01-01 | 乾通环境科技(苏州)有限公司 | Horizontal flow sedimentation tank with sludge modification return system, and return method thereof |
| CN104264778A (en) * | 2014-09-25 | 2015-01-07 | 旭泰(太仓)精细化工有限公司 | Sewage discharging cofferdam |
| CN105854361A (en) * | 2016-05-14 | 2016-08-17 | 芜湖卓越空调零部件有限公司 | Sewerage |
-
2010
- 2010-11-18 CN CN2010206125633U patent/CN201848130U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103482744A (en) * | 2013-09-27 | 2014-01-01 | 乾通环境科技(苏州)有限公司 | Horizontal flow sedimentation tank with sludge modification return system, and return method thereof |
| CN103482744B (en) * | 2013-09-27 | 2016-01-20 | 乾通环境科技(苏州)有限公司 | A kind of horizontal sedimentation tank with sludge modification return-flow system and reflow method thereof |
| CN104264778A (en) * | 2014-09-25 | 2015-01-07 | 旭泰(太仓)精细化工有限公司 | Sewage discharging cofferdam |
| CN105854361A (en) * | 2016-05-14 | 2016-08-17 | 芜湖卓越空调零部件有限公司 | Sewerage |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110601 |
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| CX01 | Expiry of patent term |