CN204752314U - Lateral aeration biological filter tank structure - Google Patents
Lateral aeration biological filter tank structure Download PDFInfo
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- CN204752314U CN204752314U CN201520311088.9U CN201520311088U CN204752314U CN 204752314 U CN204752314 U CN 204752314U CN 201520311088 U CN201520311088 U CN 201520311088U CN 204752314 U CN204752314 U CN 204752314U
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Abstract
本实用新型公开了一种侧向曝气生物滤池结构,包括滤池本体,所述滤池本体至上而下依次分为清水区、滤料区和厌氧污泥区,所述厌氧污泥区底部设置有进水沉淀区,在进水沉淀区底部设置有底部排泥口,所述厌氧污泥区侧面设置有下部排泥口,所述进水沉淀区上还设置有进水口,所述进水口连接有进水泵,所述滤池本体上部位于清水区两侧分别设置有内斗式容器和外斗式容器,所述滤池本体中部侧面布置有曝气管,所述厌氧污泥区底部与进水沉淀区之间设置有悬浮物滤网,所述进水沉淀区底部对称设置有两块斜板,本实用新型在整个滤池的中下部设置了一个厌氧污泥区,部分清水区的出水回流至厌氧污泥区,实现了系统的硝化和反硝化。
The utility model discloses a lateral aeration biological filter structure, which comprises a filter body, and the filter body is sequentially divided into a clear water area, a filter material area and an anaerobic sludge area from top to bottom. The bottom of the mud area is provided with a water inlet sedimentation area, and a bottom sludge discharge port is provided at the bottom of the water intake sedimentation area. The side of the anaerobic sludge area is provided with a lower mud discharge port. , the water inlet is connected with an inlet pump, the upper part of the filter body is located on both sides of the clear water area, and an inner bucket container and an outer bucket container are respectively arranged, and an aeration pipe is arranged on the side of the middle part of the filter body, and the drain A suspended solids filter is set between the bottom of the oxygen sludge area and the influent sedimentation area. Two slant plates are arranged symmetrically at the bottom of the influent sedimentation area. In the mud area, part of the effluent from the clean water area returns to the anaerobic sludge area, realizing the nitrification and denitrification of the system.
Description
技术领域 technical field
本实用新型涉及一种侧向曝气生物滤池结构,属于环境工程污水处理技术领域。 The utility model relates to a lateral aeration biological filter structure, which belongs to the technical field of environmental engineering sewage treatment.
背景技术 Background technique
曝气生物滤池是上世纪90年代初在普通生物滤池的基础上,借鉴给水滤池工艺而开发的污水处理新工艺,最初滤池只用于污水的三级处理,后逐渐发展成用于二级处理装置,是一种耐冲击负荷高、生物量大、产泥量少的污水处理工艺。其工作原理是:反应器内填充可使微生物附着生长的滤料,利用滤料上形成的生物膜的生物作用和挂膜滤料的吸附截留作用等来降解污水中的污染有机物。虽然曝气生物滤池有着很多的优点,如耐冲击强,工艺流程短,基建投资少等,但是在实际的使用过程中,还是面临了以下的问题: Biological aerated filter is a new sewage treatment process developed on the basis of ordinary biological filter in the early 1990s, referring to the water supply filter process. Initially, the filter was only used for the tertiary treatment of sewage, and then gradually developed into a For the secondary treatment device, it is a sewage treatment process with high impact load resistance, large biomass and low sludge production. Its working principle is: the reactor is filled with a filter material that can allow microorganisms to attach and grow, and the biological action of the biofilm formed on the filter material and the adsorption and interception of the film-hanging filter material are used to degrade the polluting organic matter in the sewage. Although the biological aerated filter has many advantages, such as strong impact resistance, short process flow, and low infrastructure investment, etc., in the actual use process, it still faces the following problems:
(1)现有曝气生物滤池对进水悬浮物要求较高,一般要求对污水进行预处理,否则滤料及容易堵塞,这不仅增加了工艺的复杂性,还增加了工艺应用的风险; (1) Existing biological aerated filters have high requirements for influent suspended solids, and generally require pretreatment of sewage, otherwise the filter material will be easily blocked, which not only increases the complexity of the process, but also increases the risk of process application;
(2)滤料层需要定期进行反冲洗,用来去除滤层中截留的水中悬浮物和脱落的生物膜,并洗脱滤料上老化的生物膜;但是传统的冲洗方式不能有效的吹脱老化的生物膜,最终会导致装置处理污水能力降低; (2) The filter material layer needs to be backwashed regularly to remove the suspended solids in the filter layer and the shedding biofilm, and to elute the aged biofilm on the filter material; however, the traditional flushing method cannot effectively blow off Aging biofilm will eventually lead to a reduction in the capacity of the device to treat sewage;
(3)现有曝气生物滤池的除磷效果差,需要辅其它方式进行除磷;由于曝气生物滤池工艺中不存在厌氧和好氧的交替环境,所以无法形成聚磷菌,所以只是在同化作用中微生物消耗了少量的磷用以合成自身物质;为使处理后的水质的总磷含量达到国家允许的排放标准,往往需要在后续加以辅助除磷工艺,这大大地增加了工艺的运行成本; (3) The phosphorus removal effect of the existing biological aerated filter is poor, and it needs to be supplemented by other methods for phosphorus removal; because there is no alternating anaerobic and aerobic environment in the biological aerated filter process, it is impossible to form phosphorus accumulating bacteria. Therefore, microorganisms only consume a small amount of phosphorus in the assimilation to synthesize their own substances; in order to make the total phosphorus content of the treated water meet the discharge standards allowed by the country, it is often necessary to follow up with an auxiliary phosphorus removal process, which greatly increases operating costs of the process;
(4)整个工艺运行过程中污泥无机成分高,不利于后续利用。 (4) During the operation of the whole process, the sludge has high inorganic components, which is not conducive to subsequent utilization.
实用新型内容 Utility model content
为解决上述问题,本实用新型提供了一种侧向曝气生物滤池结构。从而节约工艺投资和后续处理,提高了出水水质。 In order to solve the above problems, the utility model provides a lateral aerated biological filter structure. Thereby, process investment and subsequent treatment are saved, and the effluent water quality is improved.
本实用新型是通过如下技术方案予以实现的。 The utility model is realized through the following technical solutions.
一种侧向曝气生物滤池结构,包括滤池本体,所述滤池本体至上而下依次分为清水区、滤料区和厌氧污泥区,所述厌氧污泥区底部设置有进水沉淀区,在进水沉淀区底部设置有底部排泥口,所述厌氧污泥区侧面设置有下部排泥口,所述进水沉淀区上还设置有进水口,所述进水口连接有进水泵,所述滤池本体上部位于清水区两侧分别设置有内斗式容器和外斗式容器。 A lateral aerated biological filter structure, including a filter body, the filter body is divided into a clear water area, a filter material area and an anaerobic sludge area from top to bottom, and the bottom of the anaerobic sludge area is provided with In the water inlet sedimentation area, a bottom sludge outlet is provided at the bottom of the water inlet sedimentation area, and a lower mud outlet is provided on the side of the anaerobic sludge area. A water inlet is also arranged on the water inlet sedimentation area, and the water inlet A water inlet pump is connected, and the upper part of the filter body is located on both sides of the clean water area, and an inner bucket container and an outer bucket container are respectively arranged.
所述滤池本体中部侧面布置有曝气管,且曝气管通过反冲洗泵与清水区相连。 An aeration pipe is arranged on the side of the middle part of the filter body, and the aeration pipe is connected to the clean water area through a backwash pump.
所述厌氧污泥区底部与进水沉淀区之间设置有悬浮物滤网。 A suspended solids filter is set between the bottom of the anaerobic sludge zone and the influent sedimentation zone.
所述进水沉淀区底部对称设置有两块斜板,且两块斜板均向中间倾斜10°。 Two inclined plates are arranged symmetrically at the bottom of the water inlet and sedimentation area, and both inclined plates are inclined to the middle by 10°.
所述滤料区与厌氧污泥区之间设置有滤料承托网。 A filter material supporting net is arranged between the filter material area and the anaerobic sludge area.
所述滤料区与清水区之间设置有滤料阻隔网。 A filter material blocking net is arranged between the filter material area and the clean water area.
所述厌氧污泥区还通过回流管与曝气管连通。 The anaerobic sludge area is also communicated with the aeration pipe through the return pipe.
本实用新型的有益效果是: The beneficial effects of the utility model are:
与现有技术相比,本实用新型通过在底部设置了一个进水沉淀区,同时沉淀区的底部设置了两个10°的向中间倾斜的斜板,这样的设计可以有效的对进水的水质进行沉淀,让进水中的悬浮物和部分无机物能有效的絮凝沉降,通过底部排泥口排出。同时进水采用分布式的多点式向下进水,可以有效均匀的对整个反应器进行布水,让水中的悬浮物充分絮凝沉降。由于在整个滤池的中下部设置了一个厌氧污泥区,部分清水区的出水回流至厌氧污泥区,实现了系统的硝化和反硝化。厌氧污泥区的排泥口能够有效的排除部分污泥,实现了除磷的目的。同时大大提高了滤池的处理能力。 Compared with the prior art, the utility model sets a water inlet sedimentation area at the bottom, and at the same time, the bottom of the sedimentation area is provided with two 10° sloping plates inclined to the middle, such a design can effectively control the water inlet The water quality is settled, so that the suspended solids and some inorganic substances in the influent can effectively flocculate and settle, and are discharged through the bottom mud discharge port. At the same time, the water inlet adopts distributed multi-point downward water inlet, which can effectively and evenly distribute water to the entire reactor, so that the suspended matter in the water can be fully flocculated and settled. Since an anaerobic sludge area is set in the middle and lower part of the entire filter, part of the effluent from the clear water area flows back to the anaerobic sludge area, realizing the nitrification and denitrification of the system. The sludge outlet in the anaerobic sludge area can effectively remove part of the sludge and achieve the purpose of phosphorus removal. At the same time, the processing capacity of the filter is greatly improved.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
图中:1-进水沉淀区,2-厌氧污泥区,3-滤池本体,4-滤料区,5-曝气管,6-清水区,7-滤料阻隔网,8-滤料承托网,9-悬浮物滤网,10-进水泵,11-反冲洗泵,12-回流管,13-斜板,14-底部排泥口,15-下部排泥口,16-内斗式容器,17-外斗式容器,18-进水口。 In the figure: 1-influent sedimentation area, 2-anaerobic sludge area, 3-filter body, 4-filter material area, 5-aeration pipe, 6-clear water area, 7-filter material barrier net, 8- Filter support net, 9-suspended solids filter, 10-inlet pump, 11-backwash pump, 12-return pipe, 13-slope plate, 14-bottom mud outlet, 15-lower mud outlet, 16- Inner bucket container, 17-outer bucket container, 18-water inlet.
具体实施方式 Detailed ways
下面结合附图进一步描述本实用新型的技术方案,但要求保护的范围并不局限于所述。 The technical solution of the utility model is further described below in conjunction with the accompanying drawings, but the scope of protection is not limited to the description.
如图1所示,本实用新型所述的一种侧向曝气生物滤池结构,包括滤池本体3,所述滤池本体3至上而下依次分为清水区6、滤料区4和厌氧污泥区2,所述厌氧污泥区2底部设置有进水沉淀区1,在进水沉淀区1底部设置有底部排泥口14,所述厌氧污泥区2侧面设置有下部排泥口15,所述进水沉淀区1上还设置有进水口18,所述进水口18连接有进水泵10,所述滤池本体3上部位于清水区6两侧分别设置有内斗式容器16和外斗式容器17。所述内斗式容器16和外斗式容器17均采用过流式进水,其中内斗式容器16用于二次沉降和排泥,有效的提高整个反应器的出水水质,最外侧的外斗式容器17用于整个系统的出水。本技术方案通过在滤池本体3底部设置了一个进水沉淀区,可让进水中的悬浮物和部分无机物能有效絮凝沉降,并通过底部排泥口14排出。同时实现进水方式为多点式向下进水,可以有效均匀的对整个反应器进行布水,让水中的悬浮物充分絮凝沉降。 As shown in Figure 1, a kind of lateral aerated biological filter structure described in the utility model includes a filter body 3, and the filter body 3 is divided into a clear water area 6, a filter material area 4 and Anaerobic sludge area 2, the bottom of the anaerobic sludge area 2 is provided with an inflow sedimentation area 1, and a bottom sludge outlet 14 is provided at the bottom of the water inflow sedimentation area 1, and the side of the anaerobic sludge area 2 is provided with The lower part of the mud discharge port 15, the water inlet and sedimentation area 1 is also provided with a water inlet 18, the water inlet 18 is connected to the water inlet pump 10, and the upper part of the filter body 3 is respectively provided with inner buckets on both sides of the clear water area 6 Type container 16 and outer bucket type container 17. Both the inner bucket container 16 and the outer bucket container 17 adopt a flow-through water inlet, wherein the inner bucket container 16 is used for secondary settlement and sludge discharge, which effectively improves the effluent water quality of the entire reactor. The bucket container 17 is used for the water outlet of the whole system. In this technical solution, an inlet sedimentation zone is set at the bottom of the filter body 3, so that the suspended solids and some inorganic substances in the inlet water can be effectively flocculated and settled, and discharged through the bottom mud discharge port 14. At the same time, the water inlet method is multi-point downward water inlet, which can effectively and evenly distribute water to the entire reactor, so that the suspended matter in the water can be fully flocculated and settled.
所述滤池本体3中部侧面布置有曝气管5,且曝气管通过反冲洗泵11与清水区6相连。这样采用对冲的运行方式,不仅可以有效的在滤料区4内充分的布氧,同时侧向的对冲设计可以让整个装置在反冲洗阶段,有效的吹脱老化的生物质,使得整个系统有着良好的生物处理效果。 An aeration pipe 5 is arranged on the side of the middle part of the filter body 3 , and the aeration pipe is connected to the clean water area 6 through a backwash pump 11 . In this way, the hedging operation method can not only effectively distribute oxygen in the filter material area 4, but also the lateral hedging design can allow the whole device to effectively blow off the aged biomass during the backwashing stage, so that the whole system has Good biological treatment effect.
所述厌氧污泥区2底部与进水沉淀区1之间设置有悬浮物滤网9。有效起到了拦截悬浮物的作用。 A suspended solids filter 9 is provided between the bottom of the anaerobic sludge zone 2 and the influent sedimentation zone 1 . Effectively played a role in intercepting suspended solids.
所述进水沉淀区1底部对称设置有两块斜板13,且两块斜板13均向中间倾斜10°。这样的设计可以有效的对进水的水质进行沉淀,让进水中的悬浮物和部分无机物能有效的絮凝沉降,并更好地通过底部排泥口14排出。 Two sloping plates 13 are arranged symmetrically at the bottom of the water inflow sedimentation area 1, and both sloping plates 13 are inclined 10° towards the middle. Such a design can effectively settle the water quality of the influent, so that the suspended solids and some inorganic substances in the influent can be effectively flocculated and settled, and can be better discharged through the mud discharge port 14 at the bottom.
所述滤料区4与厌氧污泥区2之间设置有滤料承托网8。 A filter material supporting net 8 is arranged between the filter material area 4 and the anaerobic sludge area 2 .
所述滤料区4与清水区6之间设置有滤料阻隔网7。 A filter material blocking net 7 is arranged between the filter material area 4 and the clean water area 6 .
所述厌氧污泥区2还通过回流管12与曝气管5连通。 The anaerobic sludge zone 2 is also communicated with the aeration pipe 5 through the return pipe 12 .
如图1所示,本实用新型的工作原理是:整个滤池的进水设置在滤池本体3的底部,在工作时,通过向下的分布式进水进入进水沉淀区1,经过充分的絮凝沉降后,由于进水泵10的压力,污水由下至上通过整个滤池。在厌氧污泥区内,污水在厌氧污泥的作用下进行厌氧处理,同时通过各个排泥口定期排放污泥,达到除磷的目的。同时由于反冲洗泵11的作用,部分处理后的出水通过回流管12回流至厌氧污泥区,实现整个系统的硝化和反硝化。在滤料区4内,整个系统在曝气管5的作用下,实现了污水的好氧处理,去除水中的有机物。整个滤池设计了滤料承托网8和滤料阻隔网7,可以有效的保留滤料区内的载体数量,使得载体不会流失。滤池最上部的清水区6两侧设计两个斗式容器,均采用过流式进水,第一个斗式容器用于二次沉降和排泥,有效的提高整个反应器的出水水质,最外侧的斗式容器用于这个系统的出水。 As shown in Figure 1, the working principle of the present utility model is: the water inlet of the whole filter is arranged at the bottom of the filter body 3, and when working, enters the water inlet sedimentation zone 1 through the downward distributed water inlet, and after fully After the flocculation and settlement, due to the pressure of the water inlet pump 10, the sewage passes through the whole filter tank from bottom to top. In the anaerobic sludge area, the sewage is anaerobically treated under the action of anaerobic sludge, and the sludge is regularly discharged through each sludge outlet to achieve the purpose of phosphorus removal. At the same time, due to the action of the backwash pump 11, part of the treated effluent flows back to the anaerobic sludge area through the return pipe 12, so as to realize the nitrification and denitrification of the whole system. In the filter area 4, under the action of the aeration pipe 5, the whole system realizes the aerobic treatment of the sewage and removes the organic matters in the water. The entire filter tank is designed with a filter material supporting net 8 and a filter material blocking net 7, which can effectively retain the carrier quantity in the filter material area, so that the carrier will not be lost. Two bucket containers are designed on both sides of the clear water zone 6 at the top of the filter, both of which adopt over-flow water inlet. The first bucket container is used for secondary settlement and sludge discharge, which effectively improves the effluent water quality of the entire reactor. The outermost bucket container is used for the effluent of this system.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955513A (en) * | 2017-03-10 | 2017-07-18 | 福建工程学院 | A kind of Aerated gas-water back-impacting filter wash pond |
| CN109231446A (en) * | 2018-10-11 | 2019-01-18 | 北京城市排水集团有限责任公司 | A kind of anti-filtrate leakage device of denitrification bio-filter and its operation method |
| CN109592783A (en) * | 2019-01-22 | 2019-04-09 | 湖南中科环保技术有限公司 | A kind of high load capacity filters sewage disposal system ecologically |
| CN114590894A (en) * | 2020-12-07 | 2022-06-07 | 中国石油化工股份有限公司 | Biological aerated filter reactor and treatment method |
-
2015
- 2015-05-14 CN CN201520311088.9U patent/CN204752314U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106955513A (en) * | 2017-03-10 | 2017-07-18 | 福建工程学院 | A kind of Aerated gas-water back-impacting filter wash pond |
| CN106955513B (en) * | 2017-03-10 | 2019-11-15 | 福建工程学院 | A new air-water backwash filter |
| CN109231446A (en) * | 2018-10-11 | 2019-01-18 | 北京城市排水集团有限责任公司 | A kind of anti-filtrate leakage device of denitrification bio-filter and its operation method |
| CN109231446B (en) * | 2018-10-11 | 2024-05-31 | 北京城市排水集团有限责任公司 | Device for preventing filter material leakage of denitrification biological filter and operation method thereof |
| CN109592783A (en) * | 2019-01-22 | 2019-04-09 | 湖南中科环保技术有限公司 | A kind of high load capacity filters sewage disposal system ecologically |
| CN114590894A (en) * | 2020-12-07 | 2022-06-07 | 中国石油化工股份有限公司 | Biological aerated filter reactor and treatment method |
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