CN202519126U - Square aerated biofilter reactor integrating denitrification dephosphorization functions - Google Patents
Square aerated biofilter reactor integrating denitrification dephosphorization functions Download PDFInfo
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- CN202519126U CN202519126U CN2012200059251U CN201220005925U CN202519126U CN 202519126 U CN202519126 U CN 202519126U CN 2012200059251 U CN2012200059251 U CN 2012200059251U CN 201220005925 U CN201220005925 U CN 201220005925U CN 202519126 U CN202519126 U CN 202519126U
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Abstract
本实用新型属于污水处理领域,涉及一种一体化脱氮除磷方型曝气生物滤池反应器,该反应器可设备化生产,可用于污水量较小的工厂企业,以及城镇污水的处理。该反应器包括调节池(1),调节池通过污水计量泵(2)与立式沉淀池(5)连接,在连接污水计量泵(2)与立式沉淀池(5)的管段上安装有管式静态混合器(4),立式沉淀池(5)底部接有排泥管(19),立式沉淀池上部出水溢流进入方型曝气生物滤池(6),方型曝气生物滤池(6)底部安装曝气盘(12)、曝气管(11)、反冲洗进水管(15)、出水管(9),空气压缩机(10)和曝气管(11)连接,反冲洗水泵(14)和反冲洗进水管(15)连接,立式沉淀池(5)置于方型曝气生物滤池(6)内部,方型曝气生物滤池(6)内部填料为碳酸钙型生物滤料。本实用新型结构简单,安排紧凑,通过对污水的化学沉淀除磷、物理截留、及生物氧化处理,达到污水净化的目的。
The utility model belongs to the field of sewage treatment, and relates to an integrated nitrogen and phosphorus removal square-shaped biological aerated filter reactor, which can be produced by equipment, and can be used for factories and enterprises with a small amount of sewage, as well as for the treatment of urban sewage . The reactor includes a regulating tank (1), which is connected with the vertical sedimentation tank (5) through the sewage metering pump (2), and is installed on the pipe section connecting the sewage metering pump (2) and the vertical sedimentation tank (5). A tubular static mixer (4), a sludge discharge pipe (19) connected to the bottom of the vertical sedimentation tank (5), the overflow from the upper part of the vertical sedimentation tank enters the square biological aerated filter (6), and the square aeration Aeration pan (12), aeration pipe (11), backwash water inlet pipe (15), water outlet pipe (9) are installed at the bottom of biological filter (6), and air compressor (10) is connected with aeration pipe (11) , the backwash water pump (14) is connected to the backwash water inlet pipe (15), the vertical sedimentation tank (5) is placed inside the square biological aerated filter (6), and the inner packing of the square biological aerated filter (6) It is a calcium carbonate type biological filter material. The utility model has simple structure and compact arrangement, and achieves the purpose of sewage purification through chemical precipitation, phosphorus removal, physical interception and biological oxidation treatment of sewage.
Description
技术领域 technical field
本发明涉及一种一体化脱氮除磷方型曝气生物滤池反应器,可用于城市废水的处理装置。 The invention relates to an integrated nitrogen and phosphorus removal square type aerated biological filter tank reactor, which can be used as a treatment device for urban waste water. the
背景技术 Background technique
污水中氮和磷的去除已经引起人们的广泛关注,脱氮除磷研究对水环境保护有着重要的意义。目前我国污水处理厂脱氮除磷技术普遍存在着能耗高、效率低以及运行不稳定的缺点。针对此现状,研究适合我国国情且经济有效的脱氮除磷工艺和方法,特别是发展以最小的COD氧化、最低的CO2释放、最少的剩余污泥产量、磷的回收和处理水回用为目标的可持续污水处理技术变得势在必行。 The removal of nitrogen and phosphorus in sewage has attracted widespread attention, and the research on nitrogen and phosphorus removal is of great significance to the protection of water environment. At present, the nitrogen and phosphorus removal technologies of sewage treatment plants in my country generally have the disadvantages of high energy consumption, low efficiency and unstable operation. In view of this situation, research is suitable for China's national conditions and cost-effective denitrification and phosphorus removal processes and methods, especially the development of the least COD oxidation, the lowest CO2 release, the least excess sludge production, phosphorus recovery and treatment water reuse The goal of sustainable wastewater treatment technology becomes imperative.
曝气生物滤池是20世纪80年代末在欧美发展起来的一种新型污水处理技术,具有处理效率高、占地面积小、基建及运行费用低、管理方便和抗冲击负荷能力强等特点,在污水的有机物去除、硝化去氨、反硝化脱氮有着较好的应用前景。 Biological aerated filter is a new type of sewage treatment technology developed in Europe and the United States in the late 1980s. It has the characteristics of high treatment efficiency, small footprint, low infrastructure and operating costs, convenient management, and strong shock load resistance. It has a good application prospect in the removal of organic matter in sewage, nitrification and denitrification, denitrification and denitrification. 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,曝气生物滤池由于缺乏生物除磷所必需的交替厌氧一好氧条件,通常认为常规运行条件下单级曝气生物滤池仅靠生物同化和物理过滤除磷效率常在20%左右,最高可达35%。单级BAF的除磷效率一直是困扰其工程应用的技术难题。本专利将化学沉淀和曝气生物滤池有机组合成一体化脱氮除磷反应器,有效地提高了曝气生物滤池脱氮除磷的效果。 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. According to the current research, due to the lack of alternating anaerobic and aerobic conditions necessary for biological phosphorus removal, it is generally believed that under normal operating conditions, single-stage biological aerated filters only rely on biological assimilation and physical filtration for phosphorus removal efficiency. Around 20%, up to 35%. The phosphorus removal efficiency of single-stage BAF has always been a technical problem that plagues its engineering application. This patent organically combines the chemical precipitation and the biological aerated filter into an integrated nitrogen and phosphorus removal reactor, which effectively improves the nitrogen and phosphorus removal effect of the biological aerated filter. the
发明内容 Contents of the invention
本实用新型目的在于解决上述曝气生物滤池存在的除磷效率低的问题,提供了一种一体化脱氮除磷方型曝气生物滤池反应器。反应器包括调节池(1),调节池通过污水计量泵(2)与立式沉淀池(5)连接,在连接污水计量泵(2)与立式沉淀池(5)的管段上安装有管式静态混合器(4),立式沉淀池(5)底部接有排泥管(19),立式沉淀池上部出水溢流进入方型曝气生物滤池(6),方型曝气生物滤池(6)底部安装曝气盘(12)、曝气管(11)、反冲洗进水管(15)、出水管(9),空气压缩机(10)和曝气管(11)连接,反冲洗水泵(14)和反冲洗进水管(15)连接,立式沉淀池(5)置于方型曝气生物滤池(6)内部,方型曝气生物滤池(6)内部填料为碳酸钙型生物滤料。 The purpose of the utility model is to solve the problem of low phosphorus removal efficiency in the biological aerated filter, and provides an integrated square-shaped biological aerated filter reactor for nitrogen and phosphorus removal. The reactor includes a regulating tank (1), which is connected to the vertical sedimentation tank (5) through the sewage metering pump (2), and pipes are installed on the pipe section connecting the sewage metering pump (2) and the vertical sedimentation tank (5). type static mixer (4), the bottom of the vertical sedimentation tank (5) is connected with a mud discharge pipe (19), and the overflow of the upper part of the vertical sedimentation tank enters the square biological aerated filter (6), and the square biological aerated Aeration pan (12), aeration pipe (11), backwash water inlet pipe (15), water outlet pipe (9) are installed at the bottom of filter tank (6), and air compressor (10) is connected with aeration pipe (11), The backwash water pump (14) is connected to the backwash water inlet pipe (15), the vertical sedimentation tank (5) is placed inside the square biological aerated filter (6), and the inner filler of the square biological aerated filter (6) is Calcium carbonate type biological filter material. the
为解决上述问题,本实用新型包括混凝装置、立式沉淀池和方型曝气生物滤池。混凝装置采用管式静态混合器,设于原水进水管上,用于混凝剂的投加。立式沉淀池上部为沉淀区、下部为污泥区,两区之间为缓冲区,水从中心管自上而下进入池内,出口处设伞型挡板,使水在池内均匀分布,底部接有排泥管。立式沉淀池的上部出水通过四周溢流进入方型曝气生物滤池,滤池包括承托层、填料区、配气配水区及曝气装置。曝气装置置于配气配水区,配气配水区接有曝气盘、出水管、反冲洗进水管。 In order to solve the above problems, the utility model includes a coagulation device, a vertical sedimentation tank and a square biological aerated filter. The coagulation device adopts a tubular static mixer, which is installed on the raw water inlet pipe for the addition of coagulant. The upper part of the vertical sedimentation tank is a sedimentation area, the lower part is a sludge area, and the buffer zone is between the two areas. Connected with mud pipe. The upper effluent of the vertical sedimentation tank enters the square biological aerated filter through the overflow around it. The filter includes a supporting layer, a filling area, an air distribution and water distribution area and an aeration device. The aeration device is placed in the air distribution and water distribution area, and the air distribution and water distribution area is connected with an aeration pan, a water outlet pipe, and a backwash water inlet pipe. the
所述的混凝装置为管式静态混合器,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 with simple structure, small size, no need to occupy special space, easy installation, low investment, long service life, high mixing efficiency, and achieves the purpose of instant mixing and energy saving. the
沉淀部分的进水是由污水泵加压经混凝装置的混合液体,经过沉淀部分,原水中SS含量大大减少,为后续方型曝气生物滤池提供最佳的进水水质参数,并且去除掉水中大部分磷。 The influent of the sedimentation part is pressurized by the sewage pump and passed through the mixed liquid of the coagulation device. After passing through the sedimentation part, the SS content in the raw water is greatly reduced, providing the best influent water quality parameters for the subsequent square biological aerated filter, and removing Remove most of the phosphorus from the water. the
所述的生物滤池有过滤区和出水区,过滤区内置碳酸钙型生物滤料,下部承托层为鹅卵石,底部经多孔的承托板与出水区相连,沉淀处理后的水经由立式沉淀池上部四周溢流进入 滤池,为了曝气均匀,出水区内设有曝气盘,经曝气管与空气压缩机相连接。底部的出水区作为曝气时的配气区,也作为反冲洗时的配水区,反冲洗管经反冲洗水泵加压与反冲洗用水相连。 The biofilter has a filter area and a water outlet area. The filter area has a built-in calcium carbonate type biological filter material. The lower supporting layer is pebbles. The bottom is connected to the water outlet area through a porous supporting plate. The overflow around the upper part of the sedimentation tank enters the filter tank. In order to aerate evenly, an aeration plate is installed in the water outlet area, which is connected to the air compressor through the aeration pipe. The water outlet area at the bottom is used as the air distribution area during aeration, and also as the water distribution area during backwashing. The backwashing pipe is pressurized by the backwashing water pump and connected to the backwashing water. the
立式沉淀池外壁为方型,曝气生物滤池建于其外侧为方型,立式沉淀池的外壁作为滤池的内壁,互不联通,立式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 outer wall of the vertical sedimentation tank is square, the outer wall of the biological aerated filter is square, and the outer wall of the vertical sedimentation tank is used as the inner wall of the filter, which is not connected to each other. The operation of the two pools does not interfere with each other, and the operation is stable. the
本实用新型结构紧凑,模块化结构便于后期改扩建,以及设备化生产,可用于污水量较小的工厂企业。通过对污水的化学沉淀除磷、物理截留、及生物氧化处理,达到污水净化的目的,有助于保护环境,节约资源。 The utility model has a compact structure, and the modular structure is convenient for later reconstruction and expansion, as well as equipment production, and can be used in factories and enterprises with a small amount of sewage. Through chemical precipitation, phosphorus removal, physical interception, and biological oxidation treatment of sewage, the purpose of sewage purification is achieved, which helps to protect the environment and save resources. the
附图说明 Description of drawings
图1为本实用新型一种一体化脱氮除磷方型曝气生物滤池反应器的示意图。 Fig. 1 is a schematic diagram of an integrated square biological aerated filter reactor for denitrification and dephosphorization of the present invention. the
图2为图1中A-A剖面图。 Fig. 2 is a sectional view of A-A in Fig. 1 . the
图中:1调节池,2污水计量泵,3污水管,4管式静态混合器,5立式沉淀池,6方型曝气生物滤池,7填料,8承托层,9出水管,10空气压缩机,11曝气管,12曝气盘,13水箱,14反冲洗水泵,15反冲洗水管,16排泥管,17混合池,18计量泵,19加药管,20反冲洗出水管。 In the figure: 1 regulating tank, 2 sewage metering pump, 3 sewage pipe, 4 pipe static mixer, 5 vertical sedimentation tank, 6 square biological aerated filter, 7 filler, 8 supporting layer, 9 outlet pipe, 10 air compressor, 11 aeration pipe, 12 aeration plate, 13 water tank, 14 backwash water pump, 15 backwash water pipe, 16 mud discharge pipe, 17 mixing tank, 18 metering pump, 19 dosing pipe, 20 backwash out water pipe. the
具体实施方式 Detailed ways
附图为本实用新型的一种具体实施例,该实施例包括收集污水的调节池1,调节池1通过污水计量泵2经污水管3进入立式沉淀池5,配制混凝剂的混合池17,通过投加混凝剂的计量泵18,与管式静态混合器4相连接,在管式静态混合器中混凝剂与污水充分混合后一起经3污水管进入立式沉淀池5,立式沉淀池底部接有排泥管16,经过立式沉淀池5处理后的水通过溢流进入方型曝气生物滤池6,方型曝气池底部的配气配水区设有曝气盘12,曝气盘通过曝气管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 utility model, and this embodiment comprises the adjusting pool 1 of collecting sewage, adjusting pool 1 enters vertical settling tank 5 through sewage metering pump 2 through sewage pipe 3, the mixing tank of preparation coagulant 17. The metering pump 18 for adding the coagulant is connected to the tubular static mixer 4. In the tubular static mixer, the coagulant and the sewage are fully mixed and then enter the vertical sedimentation tank 5 through the sewage pipe 3. The bottom of the vertical sedimentation tank is connected with a mud discharge pipe 16, and the water treated by the vertical sedimentation tank 5 enters the square biological aerated filter 6 through overflow, and the air distribution and water distribution area at the bottom of the square aeration tank is equipped with aeration The
将污水在调节池1调节水量和水质,通过污水计量泵2经3污水管进入立式沉淀池5。污水管上装有管式静态混合器4,混凝剂通过18计量泵加压进入管式静态混合器,在静态混合器中混凝剂与污水充分混合后一起经3污水管立式沉淀池5,进行初步沉淀,立式沉淀池底部接有排泥管16,将沉淀后的污泥经过一定的周期间歇排出,污泥经简单处理后通过车运走,经过立式沉淀池5处理后的水通过溢流进入方型曝气生物滤池6,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,当达到预定的水头损失时,对滤池进行反冲洗,首先由空气压缩机10进行气洗,然后打开反冲洗水泵14加压对滤池进行气水联合冲洗,之后关闭空气压缩机10,再用反冲洗水泵14加压对滤池进行水洗,反冲洗的水经反冲洗出水管排出。 The sewage is adjusted in the regulating tank 1 to adjust the water volume and water quality, and enters the vertical sedimentation tank 5 through the sewage metering pump 2 and the sewage pipe 3. The sewage pipe is equipped with a tubular static mixer 4, and the coagulant is pressurized into the tubular static mixer through the 18 metering pump. In the static mixer, the coagulant and the sewage are fully mixed and then pass through the 3 sewage pipe vertical sedimentation tank 5 , for preliminary sedimentation, the bottom of the vertical sedimentation tank is connected with a sludge discharge pipe 16, and the sludge after sedimentation is discharged intermittently in a certain period of time, and the sludge is transported away by car after simple treatment, and the sludge treated by the vertical sedimentation tank 5 The water enters the square biological aerated filter 6 through the overflow, and is ventilated into the aeration tank through the air compressor 10 to provide sufficient oxygen for the microorganisms. When the predetermined head loss is reached, the filter is backwashed. The compressor 10 performs air washing, then turns on the backwash water pump 14 to pressurize the filter tank for air-water combined washing, then closes the air compressor 10, and uses the backwash water pump 14 to pressurize the filter tank to wash the filter tank with water, and the backwash water passes through Backwash the outlet pipe to discharge. the
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288205A (en) * | 2013-06-19 | 2013-09-11 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN104261508A (en) * | 2014-10-17 | 2015-01-07 | 北京昊业同宇科技有限公司 | Wastewater phosphorous removal equipment and method based on medium adsorption |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103288205A (en) * | 2013-06-19 | 2013-09-11 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN103288205B (en) * | 2013-06-19 | 2014-10-22 | 河南城建学院 | Integrated composite type bio-membrane reactor |
| CN104261508A (en) * | 2014-10-17 | 2015-01-07 | 北京昊业同宇科技有限公司 | Wastewater phosphorous removal equipment and method based on medium adsorption |
| CN104261508B (en) * | 2014-10-17 | 2016-01-13 | 北京昊业同宇科技有限公司 | Based on sewage dephosphorization equipment and the method for media adsorbs |
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