CN103193359B - Deposition and biological filter combined water purification system - Google Patents
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Abstract
本发明公开了一种沉淀协同生物滤池组合式净水系统及净水方法。一种沉淀协同生物滤池组合式净水系统的沉淀池位于曝气生物滤池内部,沉淀池与曝气生物滤池通过溢流的形式相连接,生物滤池底部接有曝气装置,原水进水管上设有加药装置。本发明的净水方法,包括如下步骤:(1)原水通过静态混合器与混凝剂混合;(2)絮凝;(3)沉淀;(4)过滤、生物处理、出净水。本发明的沉淀协同生物滤池组合式净水系统其沉淀部分、曝气生物滤池部分相互独立,水处理中各个阶段互不影响,并且在沉淀、过滤以及生物的协同作用下,各阶段能达到预定的处理效果,出水水质稳定。
The invention discloses a sedimentation cooperative biological filter combined water purification system and a water purification method. A sedimentation cooperative biological filter combined water purification system, the sedimentation tank is located inside the biological aerated filter, the sedimentation tank and the biological aerated filter are connected by overflow, and the bottom of the biological filter is connected with an aeration device, and the raw water A dosing device is provided on the water inlet pipe. The water purification method of the present invention comprises the following steps: (1) raw water is mixed with a coagulant through a static mixer; (2) flocculation; (3) precipitation; (4) filtration, biological treatment, and water purification. In the sedimentation synergistic biological filter combined water purification system of the present invention, the sedimentation part and the biological aerated filter part are independent of each other, and each stage in the water treatment does not affect each other, and under the synergistic effect of sedimentation, filtration and biology, each stage can The predetermined treatment effect is achieved, and the effluent water quality is stable.
Description
技术领域 technical field
本发明涉及一种沉淀协同生物滤池组合式净水系统及净水方法,可用于城市生活污水的处理的净水系统及净水方法。 The invention relates to a combined water purification system and water purification method of a sedimentation cooperative biological filter, which can be used for the treatment of urban domestic sewage. the
背景技术 Background technique
城市的土地资源日趋紧张,城市污水处理厂的用地收到控制。因此建设占地面积小,处理效率高的新型污水处理技术,适合我国国情,是污水处理研究的重点,对促进水环境的修复具有重要的现实意义。 The urban land resources are becoming more and more tense, and the land use of urban sewage treatment plants is under control. Therefore, the construction of a new sewage treatment technology with a small footprint and high treatment efficiency is suitable for my country's national conditions, is the focus of sewage treatment research, and has important practical significance for promoting the restoration of the water environment. the
曝气生物滤池是由普通生物滤池演变出的一种形式,其集悬浮物的截留和生物氧化于一体,具有占地面积小,出水水质好,无污泥膨胀等优点,但对进水的SS要求比较严格,因此需对水进行预处理。 Biological aerated filter is a form evolved from ordinary biological filter. It integrates the interception of suspended solids and biological oxidation, and has the advantages of small footprint, good effluent quality, and no sludge bulking. The SS requirements of water are relatively strict, so the water needs to be pretreated. the
污水中磷营养物质含量增加,污水处理后排放至自然水体仍含有大量的磷,是导致富营养化的主要原因。从目前研究可知,单纯采用曝气生物滤池除磷效果较差,必须采用有效的化学强化除磷。本发明的目的在于解决上述曝气生物滤池存在的问题,提供了一种沉淀协同生物滤池组合式净水系统及净水方法。 The content of phosphorus nutrients in sewage increases, and after sewage treatment is discharged into natural water bodies, it still contains a large amount of phosphorus, which is the main cause of eutrophication. From the current research, it can be seen that the phosphorus removal effect of simply using the biological aerated filter is poor, and effective chemically enhanced phosphorus removal must be used. The purpose of the present invention is to solve the problems existing in the above-mentioned biological aerated filter, and provide a combined water purification system and water purification method of the sedimentation cooperative biological filter. the
发明内容 Contents of the invention
为解决上述问题,本发明包括沉淀曝气生物滤池,混凝装置,溶气室。所述的沉淀曝气生物滤池包括沉淀池和曝气生物滤池,沉淀池位于曝气生物滤池内部,上部相连通,沉淀处理后的水通过溢流从沉淀池上部进入曝气生物滤池,曝气生物滤池水流为下向流,滤池底部与溶气室相连通,原水进水管与沉淀池的上部连接,原水进水管上设有混凝装置。 In order to solve the above problems, the present invention includes a sedimentation biological aerated filter, a coagulation device, and a dissolved air chamber. The sedimentation biological aerated filter includes a sedimentation tank and a biological aerated filter. The sedimentation tank is located inside the biological aerated filter, and the upper part is connected. The water after the sedimentation treatment enters the biological aerated filter from the upper part of the sedimentation tank through overflow. The water flow in the biological aerated filter is downward, the bottom of the filter is connected with the dissolved air chamber, the raw water inlet pipe is connected with the upper part of the sedimentation tank, and the raw water inlet pipe is equipped with a coagulation device. the
所述的沉淀池为竖流式,外壁为圆柱型,曝气生物滤池建于其外侧为圆柱型,沉淀池的外壁作为滤池的内壁,互不联通,沉淀池水由上部溢流至滤池,两池的运行互不干扰,运行稳定。 The settling tank is of vertical flow type, the outer wall is cylindrical, the biological aerated filter is built on its outer side and is cylindrical, the outer wall of the settling tank is used as the inner wall of the filter, and is not connected to each other, and the water of the settling tank overflows from the upper part to the filter. pool, the operation of the two pools does not interfere with each other, and the operation is stable. the
所述的沉淀池与曝气生物滤池为圆柱型,内径比为1∶3,因沉淀池置于曝气生物滤池内部,实际有效表面积比为1∶8,沉淀池与曝气生物滤池高度相同。 The sedimentation tank and the biological aerated filter are cylindrical, and the inner diameter ratio is 1:3. Since the sedimentation tank is placed inside the biological aerated filter, the actual effective surface area ratio is 1:8. The sedimentation tank and the biological aerated filter The pools are the same height. the
所述的混凝装置为管式静态混合器,设于原水进水管上,用于混凝剂的投加,结构简单、体积小巧、不需专门占用场地、安装容易、投资少、使用寿命长、混合效率高,达到瞬间混合节省能源的目的。 The coagulation device is a tubular static mixer, which is installed on the raw water inlet pipe and is used for adding coagulant. It has a simple structure, small size, no need to occupy special space, easy installation, low investment and long service life. , High mixing efficiency, achieving the purpose of instant mixing and saving energy. the
所述的溶气室包括气体发生装置空气压缩机、曝气头。空气压缩机连接容器室的曝气管,曝气管与曝气头相连,能够很好的保证水中氧气含量不低于2mg/l,为微生物降解有机物提供充足的氧气。 The gas dissolving chamber includes a gas generating device, an air compressor, and an aeration head. The air compressor is connected to the aeration pipe in the container room, and the aeration pipe is connected to the aeration head, which can well ensure that the oxygen content in the water is not less than 2mg/l, and provide sufficient oxygen for the microbial degradation of organic matter. the
一种采用上述的沉淀协同生物滤池组合式净水系统的净水方法,包括如下步骤:(1)向集水池引入污水,并在原水进水管加入混凝剂,通过管式静态混合器使污水与混凝剂完全混合;(2)加药后的水经进水管进入沉淀池,在静态混合器形成的絮体在此沉淀,去除部分污染物及大部分磷;(3)沉淀后的水流入曝气生物滤池,水流以下向流形式流过滤池;(4)向溶气室通入压缩空气,气水体积比为1∶1;(5)沉淀池底部的污泥排入污泥浓缩池,过滤后的水从净水出水管排出;(6)运行一段时间后对曝气生物滤池进行反冲洗,先气洗5分钟,然后气水联合洗3分钟,再水洗10分钟。 A water purification method using the above-mentioned sedimentation cooperative biological filter combined water purification system, comprising the following steps: (1) introducing sewage to the sump, and adding coagulant to the raw water inlet pipe, and using a tubular static mixer to The sewage is completely mixed with the coagulant; (2) The water after dosing enters the sedimentation tank through the water inlet pipe, and the flocs formed in the static mixer settle here to remove some pollutants and most of the phosphorus; (3) The settled The water flows into the biological aerated filter tank, and the water flows downward into the filter tank in the form of downward flow; (4) Compressed air is introduced into the dissolved air chamber, and the air-water volume ratio is 1:1; (5) The sludge at the bottom of the sedimentation tank is discharged into the sewage Mud concentration tank, the filtered water is discharged from the clean water outlet pipe; (6) Backwash the biological aerated filter after running for a period of time, first air washing for 5 minutes, then air-water combined washing for 3 minutes, and then water washing for 10 minutes . the
本发明的有益效果:一种沉淀协同生物滤池组合式净水系统的沉淀池和曝气生物滤池相互独立,水质处理的各个阶段能在相对的位置完成,并且本发明结构紧凑,模块化结构便于后期改扩建,以及设备化生产,也可用于污水量较小的工厂企业。通过对污水的物理、化学及生物处理,达到污水净化的目的,满足同时脱氮除磷的要求,有助于保护环境,节约资源。 Beneficial effects of the present invention: the settling pond and the biological aerated filter of a sedimentation synergistic biological filter combined water purification system are independent of each other, and each stage of water quality treatment can be completed at opposite positions, and the present invention has compact structure and modularization The structure is convenient for later reconstruction and expansion, as well as equipment production, and can also be used in factories and enterprises with small sewage volumes. Through the physical, chemical and biological treatment of sewage, the purpose of sewage purification is achieved, and the requirements of simultaneous nitrogen and phosphorus removal are met, which helps to protect the environment and save resources. the
附图说明 Description of drawings
图1为本发明一种沉淀协同生物滤池组合式净水系统的流程图;图2为本发明的A-A剖面图,结合本图做进一步的说明。 Fig. 1 is a flow chart of a sedimentation synergistic biological filter combined water purification system of the present invention; Fig. 2 is an A-A sectional view of the present invention, which is further explained in conjunction with this figure. the
附图1为本发明的流程示意图;图2为本发明的A-A剖面图。
Accompanying
图1中:1集水池,2污水泵,3污水管,4静态混合器,5沉淀池,6曝气生物滤池,7填料,8承托层,9净水出水管,10空气压缩机,11曝气管,12曝气头,13清水池,14反冲洗清水水泵,15反冲洗进水管,16排泥管,17混合池,18计量泵,19加药管,20反冲洗出水管;图2中:9净水出水管,11曝气管,11曝气管上装有曝气头。 In Figure 1: 1 sump, 2 sewage pump, 3 sewage pipe, 4 static mixer, 5 sedimentation tank, 6 biological aerated filter, 7 filler, 8 supporting layer, 9 clean water outlet pipe, 10 air compressor , 11 aeration pipe, 12 aeration head, 13 clean water tank, 14 backwash water pump, 15 backwash inlet pipe, 16 mud discharge pipe, 17 mixing tank, 18 metering pump, 19 dosing pipe, 20 backwash outlet pipe ; Among Fig. 2: 9 clean water outlet pipes, 11 aeration pipes, 11 aeration pipes are equipped with aeration heads. the
具体实施方式 Detailed ways
实施例一: Embodiment one:
附图为本发明的一种具体实施例,该实施例包括收集污水的集水池1,集水池1通过污水泵2经污水管3进入沉淀池5,配制混凝剂的混合池17,通过投加混凝剂的计量泵18,与静态混合器4相连接,在静态混合器中混凝剂与污水充分混合后一起经3污水管进入沉淀池,沉淀池底部接有排泥管16,经过沉淀池5处理后的水通过溢流进入曝气生物滤池6,曝气池底部接有曝气管11与空气压缩机10相连接,以及反冲洗管15与反冲洗泵14相连接,曝气池上部接有反冲洗出水管20。
Accompanying drawing is a kind of concrete embodiment of the present invention, and this embodiment comprises the
将污水都集中到集水池1,通过污水泵2经3污水管进入沉淀池5。污水管上装有静态混合器4,混凝剂通过18计量泵加压进入静态混合器,在静态混合器中混凝剂与污水充分混合后一起经3污水管进入沉淀池,进行初步沉淀,沉淀池底部接有排泥管16,将沉淀后的污泥排出,污泥经简单处理后通过车运走,经过沉淀池3处理后的水通过溢流进入曝气生物滤池6,填料区7为复合沸石滤料,填料高1200mm,填料区下方为起承托作用的承托层8,位于填料区下方的溶气室21内置有曝气头12,曝气头12与曝气管11相连,位于曝气头下方部位上设净水出水管9和反冲洗进水管15,通过空气压缩机10向曝气池内通气,为微生物提供充足的氧气,当达到预定的运行时间后,对滤池进行反冲洗,首先由空气压缩机进行气洗然后冲洗水泵和空气压缩机对滤池进行气水联合冲洗,再冲洗水泵进行水洗,反冲洗后的水经反冲洗出水管排出。
Concentrate the sewage into the
采用上述沉淀曝气生物滤池系统的净水方法包括如下步骤:(1)向沉淀池引入污水,进水水力负荷为5m3/m2·h,并在原水进水管上的管式静态混合器上加入混凝剂,使污水与混凝剂充分混合,形成絮体;(2)加药后的水进入沉淀池5,在重力作用下,絮体沉淀至沉淀池底部,水力停留时间1.5h;(3)沉淀处理后的水进入曝气生物滤池,在滤池内污水经过滤料的截留,微生物的分解进入出水区,水力停留时间1.25h;(4)原水在流经填料时,通过空气压缩机向溶气室曝气,为微生物的生长及对有机物的分解提供充足的氧气,空气压缩机压力0.3MPa,气水体积比为1∶1;(5)沉淀池底部的污泥排入污泥浓缩池,经简单处理后通过车运走,过滤后的水从净水出水管排出; The water purification method using the above-mentioned sedimentation biological aerated filter system includes the following steps: (1) introduce sewage into the sedimentation tank, the hydraulic load of the water intake is 5m 3 /m 2 h, and pipe static mixing on the raw water inlet pipe Add a coagulant to the device to fully mix the sewage and the coagulant to form flocs; (2) The water after dosing enters the sedimentation tank 5, and under the action of gravity, the flocs settle to the bottom of the sedimentation tank, and the hydraulic retention time is 1.5 h; (3) The water after sedimentation treatment enters the biological aerated filter tank, and the sewage in the filter tank is intercepted by the filter material, and the microbial decomposition enters the water outlet area, and the hydraulic retention time is 1.25h; (4) When the raw water flows through the filler , through the air compressor to aerate the dissolved air chamber to provide sufficient oxygen for the growth of microorganisms and the decomposition of organic matter, the pressure of the air compressor is 0.3MPa, and the volume ratio of gas to water is 1:1; The mud is discharged into the sludge thickening tank, and after simple treatment, it is transported away by car, and the filtered water is discharged from the clean water outlet pipe;
实施例二: Embodiment two:
本具体实施例的沉淀曝气生物滤池净水系统与具体实施例一的沉淀曝气生物滤池净水系统相同。
The water purification system of the sedimentation biological aerated filter in this specific embodiment is the same as the water purification system of the sedimentation biological aerated filter in the
本净水方法与具体实施例一净水方法区别在于:曝气的气水体积比为2∶1。 The difference between this water purification method and the specific embodiment one water purification method is that the air-water volume ratio of the aeration is 2:1. the
实施例三: Embodiment three:
本具体实施例的沉淀曝气生物滤池净水系统与具体实施例一的沉淀曝气生物滤池净水系统相同。
The water purification system of the sedimentation biological aerated filter in this specific embodiment is the same as the water purification system of the sedimentation biological aerated filter in the
本净水方法与具体实施例一净水方法区别在于:曝气的气水体积比为3∶1。
The difference between this water purification method and the water purification method in
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| CN104118934B (en) * | 2014-07-03 | 2016-06-22 | 济南大学 | A kind of air water co-flow magnetic force enhanced biological filters water cleaning systems and process for purifying water |
| CN104118938B (en) * | 2014-07-03 | 2016-06-22 | 济南大学 | A kind of magnetic anaerobic-aerobic biofiltration water cleaning systems and process for purifying water |
| CN105819618B (en) * | 2016-03-29 | 2018-11-27 | 江苏建筑职业技术学院 | Suspended matter equipment and its minimizing technology in a kind of flocculation aeration composite algorithm processing sewage |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2270909A (en) * | 1992-09-24 | 1994-03-30 | Copa Holdings Ltd | Sewage treatment |
| CN2441794Y (en) * | 2000-09-05 | 2001-08-08 | 胡志忠 | Integrated processor for waste water |
| CN1491903A (en) * | 2003-08-15 | 2004-04-28 | 常建一 | Integrated aeration boilogical filter tank |
| CN202519125U (en) * | 2012-01-09 | 2012-11-07 | 济南大学 | Synergistic precipitation and biological filter combined reactor |
-
2012
- 2012-01-09 CN CN201210004046.1A patent/CN103193359B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2270909A (en) * | 1992-09-24 | 1994-03-30 | Copa Holdings Ltd | Sewage treatment |
| CN2441794Y (en) * | 2000-09-05 | 2001-08-08 | 胡志忠 | Integrated processor for waste water |
| CN1491903A (en) * | 2003-08-15 | 2004-04-28 | 常建一 | Integrated aeration boilogical filter tank |
| CN202519125U (en) * | 2012-01-09 | 2012-11-07 | 济南大学 | Synergistic precipitation and biological filter combined reactor |
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| CN103193359A (en) | 2013-07-10 |
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