CN202625981U - Vertical sedimentation basin - Google Patents
Vertical sedimentation basin Download PDFInfo
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- CN202625981U CN202625981U CN201220184853.1U CN201220184853U CN202625981U CN 202625981 U CN202625981 U CN 202625981U CN 201220184853 U CN201220184853 U CN 201220184853U CN 202625981 U CN202625981 U CN 202625981U
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- 238000004062 sedimentation Methods 0.000 title claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000010802 sludge Substances 0.000 claims abstract description 36
- 238000005273 aeration Methods 0.000 claims abstract description 22
- 239000010865 sewage Substances 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000006228 supernatant Substances 0.000 claims abstract description 5
- 230000000694 effects Effects 0.000 claims abstract description 4
- 238000010992 reflux Methods 0.000 claims 2
- 230000015556 catabolic process Effects 0.000 claims 1
- 238000006731 degradation reaction Methods 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 230000000050 nutritive effect Effects 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 4
- 239000002351 wastewater Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
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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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Activated Sludge Processes (AREA)
Abstract
本实用新型为一种竖流式沉淀池,涉及一种污水处理装置。目的是解决现有装置结构设置不合理且污水处理效果欠缺的技术问题。包括缺氧池、曝气池、沉淀池和清液收集池,曝气池上端通过中间进水管连接到沉淀池,中间进水管的出水口处连接有穿孔布水管,污水经穿孔布水管均匀的分配于沉淀池,沉淀池中的上清液通过溢流槽进入到清液收集池,沉淀池下端泥斗中的污泥一部分通过穿孔排泥管被泵入到曝气池中,其余部分外排。该沉淀池通过穿孔布水管和穿孔排泥管的设置,使污水在沉淀池中不仅能布水均匀,且能快速完全的处理沉淀的污泥,该结构设置使沉淀池的形状设计不再受到限制,能根据实际情况进行灵活处理,适用更为广泛。
The utility model relates to a vertical flow sedimentation tank, which relates to a sewage treatment device. The purpose of the method is to solve the technical problems of unreasonable structure setting of the existing device and lack of sewage treatment effect. Including anoxic tank, aeration tank, sedimentation tank and clear liquid collection tank, the upper end of the aeration tank is connected to the sedimentation tank through the middle water inlet pipe, and the outlet of the middle water inlet pipe is connected with a perforated water distribution pipe, and the sewage is evenly distributed through the perforated water distribution pipe Distributed in the sedimentation tank, the supernatant in the sedimentation tank enters the supernatant liquid collection tank through the overflow tank, part of the sludge in the mud hopper at the lower end of the sedimentation tank is pumped into the aeration tank through the perforated sludge discharge pipe, and the rest is pumped into the aeration tank. Row. Through the arrangement of perforated water distribution pipes and perforated sludge discharge pipes in the sedimentation tank, the sewage can not only distribute water evenly in the sedimentation tank, but also quickly and completely treat the settled sludge. This structure setting makes the shape design of the sedimentation tank no longer subject to Restrictions can be handled flexibly according to the actual situation, and the application is more extensive.
Description
技术领域 technical field
本实用新型涉及一种污水处理装置,特别是涉及一种用于污水处理的竖流式沉淀池。 The utility model relates to a sewage treatment device, in particular to a vertical flow sedimentation tank for sewage treatment.
背景技术 Background technique
目前普通竖流式沉淀池一般是指池中废水竖向流动的沉淀池。池体平面图形为圆形或方形,水由设在池中心的进水管自上而下进入池内(管中流速应小于30mm/s),管下设伞形挡板使废水在池中均匀分布后沿整个过水断面缓慢上升(对于生活污水一般为0.5-0.7mm/s,沉淀时间采用1-1.5h),悬浮物沉降进入池底锥形沉泥斗中,澄清水从池四周沿周边溢流堰流出。堰前设挡板及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(直径大于200mm)靠静水压将泥定期排出。 At present, the ordinary vertical flow sedimentation tank generally refers to the sedimentation tank in which the wastewater in the pool flows vertically. The plane figure of the pool body is circular or square, and the water enters the pool from top to bottom through the water inlet pipe located in the center of the pool (the flow rate in the pipe should be less than 30mm/s), and an umbrella-shaped baffle is set under the pipe to evenly distribute the wastewater in the pool After slowly rising along the entire cross-section (for domestic sewage, it is generally 0.5-0.7mm/s, and the settling time is 1-1.5h), the suspended matter settles into the conical sedimentation bucket at the bottom of the pool, and the clarified water flows from around the pool to the surrounding area. The overflow weir flows out. A baffle and a scum tank are installed in front of the weir to retain scum to ensure the quality of the effluent. On one side of the pool, a mud discharge pipe (diameter greater than 200mm) is set against the wall of the pool to discharge the mud regularly by hydrostatic pressure.
普通竖流式沉淀池的缺点: Disadvantages of ordinary vertical flow sedimentation tanks:
①处理效果容易受进水水质的影响产生较大的波动; ①The treatment effect is prone to large fluctuations due to the influence of influent water quality;
②进水管只适用于方形或者圆形池体,对于长方形池体容易造成进水不均匀。 ②The water inlet pipe is only suitable for square or round pools, and it is easy to cause uneven water intake for rectangular pools.
实用新型内容 Utility model content
本实用新型的目的是解决现有普通竖流式沉淀池结构设置不合理且处理水量大时效果欠缺的技术问题,提供一种竖流式沉淀池,该沉淀池通过穿孔布水管和穿孔排泥管的设置,使污水在沉淀池中不仅能布水均匀,且能快速完全的排除沉淀的污泥,该结构设置使沉淀池的形状设计不再受到限制,能根据实际情况进行灵活处理,适用更为广泛。 The purpose of this utility model is to solve the technical problem that the structure setting of the existing ordinary vertical flow sedimentation tank is unreasonable and the effect is insufficient when the water volume is large, and to provide a vertical flow sedimentation tank. The arrangement of the pipes enables the sewage to distribute water evenly in the sedimentation tank, and can quickly and completely remove the settled sludge. This structure setting makes the shape design of the sedimentation tank no longer restricted, and can be flexibly treated according to the actual situation. It is suitable for more extensive. the
为达到上述目的,本实用新型采用的技术方案是:一种竖流式沉淀池,包括缺氧池、曝气池、沉淀池和清液收集池,其中缺氧池用于使污水缺氧进行反硝化作用然后排入曝气池,曝气池用于降解污水中的有机物营养物质,曝气池上端通过中间进水管连接到沉淀池,污水经中间进水管排入到沉淀池中,沉淀池上端设置有溢流槽,沉淀池中的上清液通过溢流槽进入到清液收集池,沉淀池下端设置有用于收集污泥的泥斗。 In order to achieve the above purpose, the technical solution adopted by the utility model is: a vertical flow sedimentation tank, including anoxic tank, aeration tank, sedimentation tank and clear liquid collection tank, wherein the anoxic tank is used to make the sewage anoxic The denitrification is then discharged into the aeration tank. The aeration tank is used to degrade the organic nutrients in the sewage. The upper end of the aeration tank is connected to the sedimentation tank through the middle water inlet pipe, and the sewage is discharged into the sedimentation tank through the middle water inlet pipe. An overflow tank is provided at the end, and the supernatant in the sedimentation tank enters the clear liquid collection tank through the overflow tank, and a mud bucket for collecting sludge is provided at the lower end of the sedimentation tank.
在上述技术方案中,所述中间进水管的出水口处连接有穿孔布水管,穿孔布水管水平设置,从中间进水管排出的污水经过穿孔布水管均匀的分布于沉淀池底部,穿孔布水管的下方设置有与其平行排列的穿孔排泥管,穿孔排泥管中部通过管道与曝气池中的污泥回流泵连接,泥斗中的污泥一部分通过穿孔排泥管被泵入到曝气池中。 In the above technical solution, the water outlet of the middle water inlet pipe is connected with a perforated water distribution pipe, and the perforated water distribution pipe is arranged horizontally. The sewage discharged from the middle water inlet pipe is evenly distributed on the bottom of the sedimentation tank through the perforated water distribution pipe. There is a perforated sludge discharge pipe arranged parallel to it below, and the middle part of the perforated sludge discharge pipe is connected to the sludge return pump in the aeration tank through a pipeline, and part of the sludge in the mud hopper is pumped into the aeration tank through the perforated sludge discharge pipe middle.
在上述技术方案中,所述穿孔布水管的中心点与中间进水管连接,从中心点往两端分别开设有穿孔,离中心点越远的穿孔,穿孔之间的距离越短,穿孔排泥管的中心点通过管道与曝气池中的污泥回流泵连接,从中心点往两端也分别开设有穿孔,离中心点越远的穿孔,穿孔之间的距离越短,且穿孔排泥管上的穿孔的开口向下设置。 In the above technical solution, the central point of the perforated water distribution pipe is connected to the middle water inlet pipe, and perforations are respectively opened from the central point to both ends. The center point of the pipe is connected to the sludge return pump in the aeration tank through the pipe, and there are perforations respectively from the center point to both ends. The opening of the perforation on the tube is set downwards. the
从上述本实用新型的各项技术特征可以看出,其优点是:通过穿孔布水管穿孔的试验,确定了穿孔布水管的穿孔位置,能解决各种形状池体布水均匀的问题;通过穿孔排泥管穿孔的试验,确定了穿孔排泥管的穿孔位置,能及时抽走沉淀池底部积留的污泥,不存在死区,能很好解沉淀池的浮泥问题。该沉淀池通过穿孔布水管和穿孔排泥管的设置,使污水在沉淀池中不仅能布水均匀,且能快速完全的处理沉淀的污泥,该结构设置使沉淀池的形状设计不再受到限制,能根据实际情况进行灵活处理,适用更为广泛。 As can be seen from the technical characteristics of the above-mentioned utility model, its advantages are: through the perforation test of the perforated water distribution pipe, the perforation position of the perforated water distribution pipe is determined, and the problem of uniform water distribution in various shapes of pools can be solved; The perforation test of the mud discharge pipe has determined the perforation position of the perforated mud discharge pipe, which can remove the sludge accumulated at the bottom of the sedimentation tank in time. There is no dead zone, and it can solve the problem of floating mud in the sedimentation tank very well. Through the arrangement of perforated water distribution pipes and perforated sludge discharge pipes in the sedimentation tank, the sewage can not only distribute water evenly in the sedimentation tank, but also quickly and completely treat the settled sludge. This structure setting makes the shape design of the sedimentation tank no longer subject to Restrictions can be handled flexibly according to the actual situation, and the application is more extensive. the
附图说明 Description of drawings
本实用新型将通过附图比较以及结合实例的方式说明: The utility model will be illustrated by comparing the accompanying drawings and in conjunction with examples:
图1是本实用新型结构示意图; Fig. 1 is a structural representation of the utility model;
图2是图1的俯视结构示意图; Fig. 2 is a top view structural schematic diagram of Fig. 1;
图3是本实用新型穿孔布水管和穿孔排泥管的结构示意图; Fig. 3 is a structural schematic diagram of the perforated water distribution pipe and the perforated mud discharge pipe of the utility model;
其中附图标记1是缺氧池 2是曝气池 3是沉淀池
Wherein reference numeral 1 is
4是清液收集池 5是中间进水管 6是溢流槽
4 is the clear
7是泥斗 8是穿孔布水管 9是穿孔排泥管
7 is the
10是管道 11是污泥回流泵 12是穿孔。
10 is the
具体实施方式 Detailed ways
下面结合附图通过实施例对本实用新型做进一步的说明。 Below in conjunction with accompanying drawing, the utility model is described further by embodiment.
优选实施例 Preferred embodiment
如图1和图2所示的一种竖流式沉淀池,其工作过程为:生活污水原水先进入缺氧池,在缺氧池参与反硝化作用,然后进入曝气池,在曝气池中微生物的作用下降解掉废水中的有机物营养物质,泥水混合物通过溢流管流入中间进水管,并进入穿孔布水管,穿孔布水管将水均匀布于沉淀池底部,形成向上流,在向上流的过程中,在泥水分离区实现泥水分离,上清液进入溢流槽流入清液收集池。沉淀污泥一部分由穿孔排泥管由污泥回流泵泵抽至曝气池作为回流污泥,部分作为剩余污泥外排。沉降的活性污泥在沉淀池泥斗中收集,并通排污泵从穿孔排泥管均匀排出。 A vertical flow sedimentation tank as shown in Figure 1 and Figure 2, its working process is: the raw water of domestic sewage first enters the anoxic tank, participates in denitrification in the anoxic tank, then enters the aeration tank, and then enters the aeration tank Under the action of microorganisms in the wastewater, the organic matter and nutrients in the wastewater are degraded, and the muddy water mixture flows into the middle water inlet pipe through the overflow pipe, and then enters the perforated water pipe. In the process, the mud-water separation is realized in the mud-water separation area, and the supernatant enters the overflow tank and flows into the clear liquid collection tank. Part of the settled sludge is pumped by the perforated sludge discharge pipe to the aeration tank by the sludge return pump as return sludge, and part is discharged as excess sludge. The settled activated sludge is collected in the mud hopper of the sedimentation tank, and is evenly discharged from the perforated sludge discharge pipe through the sewage pump.
在本实用新型中,如图3所示,穿孔布水管材料一般采用聚氯乙烯材料,其上的穿孔可以采用交叉45°的布置,孔的间距和大小根据实际操作情况进行设置,使废水能够均匀的分布;采用穿孔排泥管排泥,其外观形态和穿孔布水管形态一致,穿孔排泥管穿孔开口向下,污泥由污泥回流泵的泵吸抽出,能达到均匀排泥的目的。 In this utility model, as shown in Figure 3, the perforated water pipe material is generally made of polyvinyl chloride material, and the perforations on it can be arranged at a cross 45°, and the spacing and size of the holes are set according to the actual operating conditions, so that the waste water can be Uniform distribution; the perforated sludge discharge pipe is used to discharge the sludge, and its appearance is consistent with the shape of the perforated water distribution pipe. The perforated sludge discharge pipe has a perforated opening downward, and the sludge is pumped out by the sludge return pump, which can achieve the purpose of uniform sludge discharge .
本说明书中公开的所有特征,除了互相排斥的特征以外,均可以以任何方式组合。 All features disclosed in this specification, except mutually exclusive features, can be combined in any way.
本说明书(包括任何附加权利要求、摘要和附图)中公开的任一特征,除非特别叙述,均可被其他等效或具有类似目的的替代特征加以替换。即,除非特别叙述,每个特征只是一系列等效或类似特征中的一个例子而已。 Any feature disclosed in this specification (including any appended claims, abstract and drawings), unless expressly stated otherwise, may be replaced by alternative features which are equivalent or serve a similar purpose. That is, unless expressly stated otherwise, each feature is one example only of a series of equivalent or similar features. the
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220184853.1U CN202625981U (en) | 2012-04-27 | 2012-04-27 | Vertical sedimentation basin |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220184853.1U CN202625981U (en) | 2012-04-27 | 2012-04-27 | Vertical sedimentation basin |
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| CN202625981U true CN202625981U (en) | 2012-12-26 |
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| CN201220184853.1U Expired - Fee Related CN202625981U (en) | 2012-04-27 | 2012-04-27 | Vertical sedimentation basin |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422435A (en) * | 2016-11-08 | 2017-02-22 | 上海中信水务产业有限公司 | baffled sedimentation tank and baffled sedimentation process |
| CN113024019A (en) * | 2020-09-09 | 2021-06-25 | 劲旅环境科技股份有限公司 | Purifying tank |
-
2012
- 2012-04-27 CN CN201220184853.1U patent/CN202625981U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422435A (en) * | 2016-11-08 | 2017-02-22 | 上海中信水务产业有限公司 | baffled sedimentation tank and baffled sedimentation process |
| CN113024019A (en) * | 2020-09-09 | 2021-06-25 | 劲旅环境科技股份有限公司 | Purifying tank |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180417 Address after: 325100 Wenzhou 1 Economic and Technological Development Zone, Binhai six road 2180, 1 108 rooms in the rising sun district. Patentee after: Zhejiang Renzhi Limited by Share Ltd Address before: 621000 Mianyang City, Sichuan Province, west section of the park road, No. 33 Patentee before: Sichuan Renzhi Oilfield Technology Services Co., Ltd. |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121226 Termination date: 20190427 |
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| CF01 | Termination of patent right due to non-payment of annual fee |
