CN203613066U - Technical device for preventing tubular membrane of external membrane bio-reactor (MBR) from being blocked - Google Patents
Technical device for preventing tubular membrane of external membrane bio-reactor (MBR) from being blocked Download PDFInfo
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- CN203613066U CN203613066U CN201320416712.2U CN201320416712U CN203613066U CN 203613066 U CN203613066 U CN 203613066U CN 201320416712 U CN201320416712 U CN 201320416712U CN 203613066 U CN203613066 U CN 203613066U
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Abstract
Description
技术领域technical field
本实用新型涉及城市垃圾卫生填埋场、垃圾焚烧发电厂、垃圾中转站等的垃圾渗滤液处理领域,具体涉及一种防止外置式MBR管式膜的堵塞的工艺装置。The utility model relates to the field of garbage leachate treatment in urban garbage sanitary landfills, garbage incineration power plants, garbage transfer stations, etc., in particular to a process device for preventing the blockage of an external MBR tubular membrane.
背景技术Background technique
垃圾渗滤液是一种污染物浓度高,水质极为复杂的一种废水。目前根据国家环保部的要求,出水达到GB16889-2008的排放标准,根据国家的相关规范,一般采用“预处理+外置式MBR膜生物反应系统+深度处理”的处理工艺。Landfill leachate is a kind of wastewater with high concentration of pollutants and extremely complicated water quality. At present, according to the requirements of the Ministry of Environmental Protection, the effluent meets the discharge standard of GB16889-2008. According to the relevant national regulations, the treatment process of "pretreatment + external MBR membrane bioreaction system + advanced treatment" is generally adopted.
使用的外置式MBR膜生物反应系统的工艺一般是A/O(反硝化罐/硝化罐)+外置式管式膜组成。该外置式MBR膜生物反应系统是目前的MBR工艺的一种形式。The process of the external MBR membrane biological reaction system used is generally composed of A/O (denitrification tank/nitrification tank) + external tubular membrane. The external MBR membrane biological reaction system is a form of the current MBR process.
MBR工艺是指,膜-生物反应器(Membrane Bio-Reactor,MBR),为膜分离技术与生物处理技术有机结合之新型态废水处理系统。以膜组件取代传统生物处理技术末端二沉池,在膜-生物反应器中保持高活性污泥浓度,提高生物处理有机负荷,从而减少污水处理设施占地面积,并通过保持低污泥负荷减少剩余污泥量。The MBR process refers to the membrane-bioreactor (Membrane Bio-Reactor, MBR), which is a new type of wastewater treatment system that combines membrane separation technology and biological treatment technology. Replace the terminal secondary sedimentation tank of traditional biological treatment technology with membrane modules, maintain a high concentration of active sludge in the membrane-bioreactor, increase the organic load of biological treatment, thereby reducing the footprint of sewage treatment facilities, and reduce the sludge load by maintaining low sludge load amount of residual sludge.
因此目前一般用于垃圾渗滤液的外置式MBR就是由反硝化罐、硝化罐和管式膜组件三大部分组成。但是在运行的过程中,经常会有管式膜堵塞,管式膜出水水量降低,出水量小的问题,并且管式膜若发生了堵塞,需要停机清洗,则造成这个污水系统停止运行的问题。更糟糕的是管式膜堵塞严重的时候,需要人工使用工具把管式膜的污染掏出来,非常麻烦,并且需要好几天才能掏干净。管式膜的堵塞问题一度成为外置式MBR发展的瓶颈。Therefore, the external MBR generally used for landfill leachate is composed of three parts: denitrification tank, nitrification tank and tubular membrane module. However, in the process of operation, the tubular membrane is often blocked, the water output of the tubular membrane is reduced, and the water output is small. If the tubular membrane is blocked, it needs to be shut down for cleaning, which will cause the problem of stopping the operation of the sewage system. . What's worse is that when the tubular membrane is seriously clogged, it is necessary to manually use tools to remove the pollution of the tubular membrane, which is very troublesome and takes several days to remove. The clogging problem of the tubular membrane once became the bottleneck of the development of the external MBR.
实用新型内容Utility model content
本实用新型所要解决的技术问题是提供一种防止外置式MBR管式膜的堵塞的工艺装置,防止外置式管式膜的堵塞,提高管式膜的产水量。The technical problem to be solved by the utility model is to provide a process device for preventing the clogging of the external MBR tubular membrane, prevent the clogging of the external tubular membrane, and increase the water production of the tubular membrane.
为解决上述技术问题,本实用新型提供一种防止外置式MBR管式膜的堵塞的工艺装置,包括反硝化罐、硝化罐和管式膜组件,其特征在于,还包括竖流式沉淀池,硝化罐内的硝化池上部的液体通过沉淀池的上端流入沉淀池内,沉淀池的中上部出水进入管式膜组件。In order to solve the above technical problems, the utility model provides a process device for preventing the clogging of the external MBR tubular membrane, which includes a denitrification tank, a nitrification tank and a tubular membrane module, and is characterized in that it also includes a vertical flow sedimentation tank, The liquid in the upper part of the nitrification tank in the nitrification tank flows into the sedimentation tank through the upper end of the sedimentation tank, and the effluent from the middle and upper parts of the sedimentation tank enters the tubular membrane module.
优选的,沉淀池下部与硝化池连通,这样,沉淀池内的泥可流动到硝化池内,不致于成为死泥。Preferably, the lower part of the sedimentation tank communicates with the nitrification tank, so that the mud in the sedimentation tank can flow into the nitrification tank without becoming dead mud.
进一步优化的,为了防止沉淀池的泥成为死泥,所述沉淀池的底部通过回流管连通所述反硝化罐,所述回流管上设有污泥回流泵。Further optimized, in order to prevent the sludge in the sedimentation tank from becoming dead sludge, the bottom of the sedimentation tank is connected to the denitrification tank through a return pipe, and a sludge return pump is arranged on the return pipe.
更加优选的,在所述回流管上设有调节阀,根据沉淀池的运行情况,打开调节阀和回流泵,将泥回流到反硝化罐。More preferably, a regulating valve is provided on the return pipe, and the regulating valve and the return pump are opened to return the sludge to the denitrification tank according to the operation conditions of the sedimentation tank.
最优选的,所述沉淀池为一上下端开放的直筒状装置,所述直筒状装置竖直位于硝化罐内。Most preferably, the sedimentation tank is a straight cylindrical device with open upper and lower ends, and the straight cylindrical device is vertically located in the nitrification tank.
本实用新型的垃圾渗滤液处理装置运行可靠,集成度高,有效的截留了活性污泥,防止了外置式管式膜的堵塞,又使得管式膜组件的负荷降低,提高了管式膜的产水率。The landfill leachate treatment device of the utility model has reliable operation and high integration, effectively retains activated sludge, prevents the clogging of the external tubular membrane, reduces the load of the tubular membrane module, and improves the efficiency of the tubular membrane. Water production rate.
附图说明Description of drawings
下面结合附图和具体实施方式对本实用新型的技术方案作进一步具体说明。The technical solution of the present utility model will be further specifically described below in conjunction with the accompanying drawings and specific embodiments.
图1为本实用新型的具体实施方式结构主视图。Fig. 1 is the structural front view of the specific embodiment of the present utility model.
图2为本实用新型的具体实施方式结构中硝化罐与管式膜组件连接的俯视图。Fig. 2 is a top view of the connection between the nitrification tank and the tubular membrane module in the structure of the specific embodiment of the present invention.
具体实施方式Detailed ways
结合图1、2所示,进水首先进入反硝化罐10内,反硝化罐10的上部出水进入硝化罐20,反硝化罐10与硝化罐20的底部通过回流管连通,回流管上设有回流泵5和调节阀6。设有鼓风机4的曝气管通到硝化罐20内硝化池1的底部。硝化罐20内内设有一竖流式的沉淀池2,沉淀池2为一上下端开放的直圆筒3,硝化池1上部的液体通过直圆筒3的上端流入沉淀池2内,沉淀池2的中上部出水通过硝化罐20壁进入管式膜组件30。沉淀池2的下部与硝化池1连通,这样,沉淀池2内的泥可流动到硝化池1内,不致于成为死泥。另外,为了防止沉淀池的泥成为死泥,单独设置了调节阀7,根据沉淀池2的运行情况,打开调节阀7和回流泵5,将泥回流到前端反硝化罐20。As shown in Figures 1 and 2, the incoming water first enters the
通过沉淀池2将硝化罐内的活性污泥进行初步收集,以减少进入管式膜的负荷,同时还让一部分的污泥进入管式膜系统。经实践运行检验证明,本实用新型的垃圾渗滤液处理装置运行可靠,集成度高,有效的截留了活性污泥,防止了外置式管式膜的堵塞,又使得管式膜组件的负荷降低,提高了管式膜的产水率。The activated sludge in the nitrification tank is initially collected through the
当然,本领域的技术人员容易想到,沉淀池2并非必需设在硝化罐20内。沉淀池2单独设置于硝化罐20外,与硝化罐20进行上下连通,即可达成与上述具体实施方式同样的技术效果,故不再赘述。Of course, those skilled in the art can easily imagine that the
最后所应说明的是,以上具体实施方式仅用以说明本实用新型的技术方案而非限制,尽管参照较佳实施例对本实用新型进行了详细说明,本领域的普通技术人员应当理解,可以对本实用新型的技术方案进行修改或者等同替换,而不脱离本实用新型技术方案的精神和范围,其均应涵盖在本实用新型的权利要求范围当中。Finally, it should be noted that the above specific embodiments are only used to illustrate the technical solutions of the present utility model without limitation. Although the utility model has been described in detail with reference to preferred embodiments, those of ordinary skill in the art should understand that this utility model can be Any modification or equivalent replacement of the technical solution of the utility model without departing from the spirit and scope of the technical solution of the utility model shall be covered by the claims of the utility model.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104773921A (en) * | 2015-04-14 | 2015-07-15 | 江南大学 | Tube membrane device for sewage treatment |
| CN105800779A (en) * | 2016-05-21 | 2016-07-27 | 桂林理工大学 | Method for achieving stable operation of anaerobic membrane bioreactor |
| CN106517490A (en) * | 2016-11-15 | 2017-03-22 | 胡明成 | Sewage treatment system with external MBR (Membrane Bioreactor) |
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2013
- 2013-07-12 CN CN201320416712.2U patent/CN203613066U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104773921A (en) * | 2015-04-14 | 2015-07-15 | 江南大学 | Tube membrane device for sewage treatment |
| CN105800779A (en) * | 2016-05-21 | 2016-07-27 | 桂林理工大学 | Method for achieving stable operation of anaerobic membrane bioreactor |
| CN105800779B (en) * | 2016-05-21 | 2018-09-11 | 桂林理工大学 | A method of realizing anaerobic membrane bioreactor stable operation |
| CN106517490A (en) * | 2016-11-15 | 2017-03-22 | 胡明成 | Sewage treatment system with external MBR (Membrane Bioreactor) |
| CN106517490B (en) * | 2016-11-15 | 2019-06-07 | 胡明成 | A kind of external MBR sewage disposal system |
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