CN205035234U - BioDopp biochemical reactor of embedded rectangle sedimentation tank - Google Patents
BioDopp biochemical reactor of embedded rectangle sedimentation tank Download PDFInfo
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Abstract
本实用新型提供一种内嵌矩形沉淀池的BioDopp生化反应器,由厌氧区、缺氧区、好氧区及矩形沉淀池构成,由空气提推器提供各功能区泥水混合物循环流动的动力,形成一个一体化生化反应器。矩形沉淀池采用边进边出的矩形沉淀池,设置在缺氧区上方。本实用新型与以往的BioDopp生化反应器相比,采用矩形沉淀池代替了原有的采用斜管或斜板填料的泥水分离装置,解决了原有泥水分离装置易堵塞,需要反洗装置,土建结构复杂,投资较大等问题。
The utility model provides a BioDopp biochemical reactor embedded with a rectangular sedimentation tank, which is composed of an anaerobic zone, anoxic zone, an aerobic zone and a rectangular sedimentation tank, and the air lifter provides the power for the circulation of muddy water mixture in each functional zone , forming an integrated biochemical reactor. The rectangular sedimentation tank adopts a rectangular sedimentation tank that enters and exits at the same time, and is set above the anoxic zone. Compared with the previous BioDopp biochemical reactor, the utility model adopts a rectangular sedimentation tank instead of the original mud-water separation device using inclined tube or inclined plate filler, which solves the problem that the original mud-water separation device is easy to block and needs backwashing device, civil engineering Complex structure, large investment and other issues.
Description
技术领域 technical field
本实用新型涉及一种内嵌矩形沉淀池的BioDopp生化反应器,属于水处理领域。 The utility model relates to a BioDopp biochemical reactor embedded with a rectangular sedimentation tank, which belongs to the field of water treatment.
背景技术 Background technique
BioDopp生化反应器是德国EBV公司Engelbart博士发明的一种新颖污水处理装置,其将各个单一功能单元(生物硝化、反硝化,释磷、吸磷,有机物氧化、沉淀等多个单元)组合在一个矩形池中,并且采用低溶解氧(通常为0.3~0.8mg/L)实现纵向同步硝化/反硝化脱氮,高污泥浓度(通常5~8g/L)确保处理高效持续稳定(低溶氧及高污泥浓度是其工艺两大特色)。BioDopp生化反应器较现有传统生化反应器具有以下优势:操作简单;低溶氧下高效生物脱氮和良好除磷效果,同池实现同步硝化/反硝化脱氮;运行高效、持续,出水稳定;低污泥产出,剩余污泥可比传统工艺少40~60%;维护工作量小;占地面积小,使用长方形水池节约了大量土地,污水处理厂只需一个常规污水处理厂一半面积;大大减少了管道投资,投资与运行成本低,投资、运行成本可减少一半左右。因而在污水处理中得到重视和推广。 BioDopp biochemical reactor is a novel sewage treatment device invented by Dr. Engelbart of German EBV company, which combines various single functional units (biological nitrification, denitrification, phosphorus release, phosphorus absorption, organic matter oxidation, precipitation, etc.) Rectangular tank, and adopts low dissolved oxygen (usually 0.3~0.8mg/L) to realize vertical synchronous nitrification/denitrification denitrification, high sludge concentration (usually 5~8g/L) to ensure efficient and stable treatment (low dissolved oxygen and high sludge concentration are two major features of its process). Compared with existing traditional biochemical reactors, BioDopp biochemical reactor has the following advantages: simple operation; high-efficiency biological nitrogen removal and good phosphorus removal effect under low dissolved oxygen, simultaneous nitrification/denitrification denitrification in the same tank; efficient and continuous operation, stable effluent ;Low sludge output, the remaining sludge can be reduced by 40-60% compared with traditional processes; the maintenance workload is small; the floor area is small, and the use of rectangular pools saves a lot of land, and the sewage treatment plant only needs half the area of a conventional sewage treatment plant; The pipeline investment is greatly reduced, the investment and operation costs are low, and the investment and operation costs can be reduced by about half. Therefore, it has been paid attention to and promoted in sewage treatment.
典型BioDopp生化反应器采用内置泥水分离装置,泥水分离装置中安装有斜板和斜管的组合填料,对泥水进行分离。采用组合填料可获取较大的表面负荷,并不受污泥负荷的影响。但斜板和斜管组合填料在实际运行过程中极易堵塞,直接影响泥水分离效果,需要采用定期反洗的手段来保证其运行效果,反洗系统较为复杂,且反洗时会影响出水效果;斜板和斜管为PP或PE材质,强度一般,不耐紫外线,使用寿命为3~5年,且更换维护较为困难;采用斜管和斜板组合填料,土建结构较为复杂,施工成本较大;斜板和斜管组合填料价格昂贵,投资较大。 A typical BioDopp biochemical reactor adopts a built-in mud-water separation device, which is equipped with a combination of inclined plates and inclined tubes to separate mud and water. The use of combined packing can obtain a larger surface load and is not affected by the sludge load. However, the combined packing of inclined plate and inclined tube is very easy to block during the actual operation process, which directly affects the effect of mud-water separation. Regular backwashing is required to ensure its operation effect. The backwashing system is relatively complicated, and the water outlet effect will be affected during backwashing. ; Inclined plates and tubes are made of PP or PE material, with average strength, not resistant to ultraviolet rays, and a service life of 3 to 5 years, and it is difficult to replace and maintain; the combination of inclined tubes and inclined plates is used as filler, the civil structure is more complicated, and the construction cost is relatively high. Large; the combination of inclined plate and inclined tube packing is expensive and requires a large investment.
发明内容 Contents of the invention
本实用新型的主要目的在于提供一种内嵌矩形沉淀池的BioDopp生化反应器,采用矩形沉淀池代替典型BioDopp生化反应器中安装有斜板和斜管填料的泥水分离装置,以解决典型BioDopp生化反应器泥水分离装置易堵塞,需要反洗装置,土建结构复杂,投资较大等问题。 The main purpose of this utility model is to provide a BioDopp biochemical reactor with a built-in rectangular sedimentation tank. The rectangular sedimentation tank is used to replace the mud-water separation device installed with inclined plates and inclined tube fillers in the typical BioDopp biochemical reactor to solve the problem of typical BioDopp biochemical The sludge-water separation device of the reactor is easy to block, requires backwashing device, complex civil structure, and large investment.
本实用新型所涉及的一种内嵌矩形沉淀池的BioDopp生化反应器由厌氧区、缺氧区、好氧区及矩形沉淀池构成;厌氧区与缺氧区连通,缺氧区与好氧区连通,好氧区与厌氧区连通,矩形沉淀池设置在缺氧区上方。 The utility model relates to a BioDopp biochemical reactor embedded with a rectangular sedimentation tank consisting of an anaerobic zone, anoxic zone, an aerobic zone and a rectangular sedimentation tank; the anaerobic zone is connected with the anoxic zone, and the anoxic zone is connected with the good The oxygen zone is connected, the aerobic zone is connected with the anaerobic zone, and the rectangular sedimentation tank is set above the anoxic zone.
进一步地,矩形沉淀池采用边进边出的矩形沉淀池,矩形沉淀池有效水深为3~6m,宽度为6~18m,缺氧区有效高度为2~4m,宽度与矩形沉淀池等宽。 Further, the rectangular sedimentation tank adopts a rectangular sedimentation tank that enters and exits at the same time. The effective water depth of the rectangular sedimentation tank is 3-6m, the width is 6-18m, the effective height of the anoxic zone is 2-4m, and the width is equal to the width of the rectangular sedimentation tank.
进一步地,一种内嵌矩形沉淀池的BioDopp生化反应器还包括矩形沉淀池进水槽、矩形沉淀池出水槽和集泥槽;矩形沉淀池进水槽与矩形沉淀池出水槽设置在矩形沉淀池的一侧,集泥槽设置在矩形沉淀池另一侧,集泥槽一端与进水槽连通,另一端与排泥管连接。 Further, a BioDopp biochemical reactor with a built-in rectangular sedimentation tank also includes a rectangular sedimentation tank inlet tank, a rectangular sedimentation tank outlet tank and a mud collection tank; the rectangular sedimentation tank inlet tank and the rectangular sedimentation tank outlet tank are arranged on the rectangular sedimentation tank On one side, the mud collecting tank is arranged on the other side of the rectangular sedimentation tank. One end of the mud collecting tank is connected with the water inlet tank, and the other end is connected with the mud discharge pipe.
进一步地,矩形沉淀池采用往复式吸刮泥机或链板式刮泥机或液压式刮泥机,收集的污泥通过泵送至集泥槽。 Further, the rectangular sedimentation tank adopts a reciprocating suction sludge scraper or a chain plate type sludge scraper or a hydraulic sludge scraper, and the collected sludge is pumped to the sludge collection tank.
进一步地,一种内嵌矩形沉淀池的BioDopp生化反应器还包括空气提推器,空气提推器设置在缺氧区与好氧区之间,且空气提推器与缺氧区以及空气提推器与好氧区均连通。 Further, a BioDopp biochemical reactor with embedded rectangular sedimentation tank also includes an air lifter, the air lifter is arranged between the anoxic zone and the aerobic zone, and the air lifter is connected to the anoxic zone and the air lifter. The thrusters are connected to the aerobic zone.
进一步地,厌氧区内设置潜水推流搅拌器,搅拌功率为2~6W/m3。 Further, a submersible plug flow mixer is installed in the anaerobic zone, and the stirring power is 2~6W/m 3 .
本实用新型所涉及的一种内嵌矩形沉淀池的BioDopp生化反应器延续了典型BioDopp生化反应器所具有的工艺优点的同时,使得整个反应器出水水质更稳定,结构更简单,所需设备数量大大减少,投资成本更低。 The utility model relates to a BioDopp biochemical reactor with a built-in rectangular sedimentation tank, while continuing the technological advantages of a typical BioDopp biochemical reactor, it makes the water quality of the whole reactor more stable, the structure is simpler, and the number of required equipment Greatly reduced, lower investment costs.
附图说明 Description of drawings
构成本申请的一部分的说明书附图用来提供对本实用新型的进一步理解,本实用新型的示意性实施例及其说明用于解释本实用新型,并不构成对本实用新型的不当限定。在附图中: The accompanying drawings constituting a part of this application are used to provide a further understanding of the utility model, and the schematic embodiments of the utility model and their descriptions are used to explain the utility model and do not constitute improper limitations to the utility model. In the attached picture:
图1示出了根据本实用新型的一种内嵌矩形沉淀池的BioDopp生化反应器的实施例的俯视结构示意图;以及 Fig. 1 shows the top view structural representation of the embodiment of the BioDopp biochemical reactor of a kind of built-in rectangular sedimentation tank according to the utility model; And
图2示出了图1的A-A剖视结构示意图; Fig. 2 shows the schematic diagram of the A-A sectional structure of Fig. 1;
图3示出了图1的B-B剖视结构示意图。 FIG. 3 shows a schematic diagram of the cross-sectional structure along B-B of FIG. 1 .
其中,上述附图包括以下附图标记: Wherein, the above-mentioned accompanying drawings include the following reference signs:
1、进水槽;2、厌氧区;3、缺氧区;4、空气提推器;5、好氧区;6、矩形沉淀池进水槽;7、矩形沉淀池;8、矩形沉淀池出水槽;9、集泥槽。 1. Inlet tank; 2. Anaerobic zone; 3. Anoxic zone; 4. Air lifter; 5. Aerobic zone; 6. Rectangular sedimentation tank inlet tank; 7. Rectangular sedimentation tank; Sink; 9. Mud collection tank.
具体实施方式 detailed description
下面结合附图和具体实施例对本实用新型作进一步说明,但不作为对本实用新型的限定。 The utility model will be further described below in conjunction with the accompanying drawings and specific embodiments, but not as a limitation of the utility model.
如图1、图2和图3所示,本实用新型的实施例提供了一种内嵌矩形沉淀池的BioDopp生化反应器。待处理污水进入到进水槽1,与集泥槽9中的回流污泥进行混合,然后自流进入到厌氧区2,在厌氧区2实现磷的释放和有机氨的氨化,同时去除部分目标污染物;厌氧区2的污水垂直向下流动与好氧区5回流的泥水混合物混合,进入到缺氧区3,在厌氧区2内设置潜水推流搅拌器,对缺氧区3内泥水混合物进行搅拌,在缺氧区3内实现脱除大部分总氮的功能;缺氧区3末端与空气提推器4底部连通,通过空气提推器4的提升作用,泥水混合物不断流入好氧区5;在好氧区5通过鼓风曝气系统营造好氧环境,去除COD、氨氮等目标污染物;好氧区5末端与矩形沉淀池进水槽6连通,部分泥水混合物进入到矩形沉淀池进水槽6,通过矩形沉淀池进水槽6将其均匀分布到矩形沉淀池7整个通长断面;泥水混合物在矩形沉淀池7实现泥水分离,底泥沉积在矩形沉淀池7底部,上清液通过矩形沉淀池出水槽8收集排出BioDopp生化反应器;矩形沉淀池7底部污泥被吸刮泥机收集后通过泵送至集泥槽9,集泥槽9中大部分污泥回流到进水槽1中,剩余污泥通过排泥管排出BioDopp生化反应器。 As shown in Figure 1, Figure 2 and Figure 3, the embodiment of the present invention provides a BioDopp biochemical reactor with a built-in rectangular sedimentation tank. The sewage to be treated enters the water inlet tank 1, mixes with the return sludge in the sludge collection tank 9, and then enters the anaerobic zone 2 by gravity, where the release of phosphorus and the ammoniation of organic ammonia are realized, and part of the sludge is removed at the same time. Target pollutants; the sewage in anaerobic zone 2 flows vertically downwards and mixes with the mud-water mixture returning from aerobic zone 5, and then enters anoxic zone 3, and a submersible plug-flow mixer is set in anaerobic zone 2, and the anoxic zone 3 The inner mud-water mixture is stirred to realize the function of removing most of the total nitrogen in the anoxic zone 3; the end of the anoxic zone 3 is connected to the bottom of the air lifter 4, and through the lifting effect of the air lifter 4, the mud-water mixture flows continuously Aerobic zone 5; in the aerobic zone 5, an aerobic environment is created through the blower aeration system to remove target pollutants such as COD and ammonia nitrogen; the end of the aerobic zone 5 is connected to the rectangular sedimentation tank inlet tank 6, and part of the mud-water mixture enters the rectangular sedimentation tank The inlet tank 6 of the sedimentation tank is evenly distributed to the entire length section of the rectangular sedimentation tank 7 through the inlet tank 6 of the rectangular sedimentation tank; The liquid is collected through the outlet tank 8 of the rectangular sedimentation tank and discharged from the BioDopp biochemical reactor; the sludge at the bottom of the rectangular sedimentation tank 7 is collected by the suction mud scraper and then pumped to the sludge collection tank 9, and most of the sludge in the sludge collection tank 9 is returned to the inlet. In tank 1, the remaining sludge is discharged from the BioDopp biochemical reactor through the sludge discharge pipe.
实施例1。 Example 1.
例1:某日处理15000吨市政污水的内嵌矩形沉淀池的BioDopp生化处理反应器,厌氧区2长为12m,宽为9m,有效水深为7.5m;缺氧区3长为54m,宽为12m,有效高度为2.5m;好氧区5长为66m,宽为10m,有效水深为7.5m;矩形沉淀池7长为54m,宽为12m,有效水深为4.8m。矩形沉淀池进水槽6与矩形沉淀池出水槽8在矩形沉淀池7的一侧,矩形沉淀池进水槽6长度为54m,宽为0.5m,有效水深为1.0m,矩形沉淀池出水槽8长度为56m,宽为0.5m,有效水深为0.8m;集泥槽9在矩形沉淀池7的另一侧,集泥槽9长度为65m,宽为0.3m,有效水深为0.5m;集泥槽9一端与进水槽1连通,进水槽1长度为12m,宽为1.0m,有效水深为0.8m;集泥槽9另一端连接排泥管,排泥泵采用干式安装,设置两台,1用1备,流量为80m3/h,扬程为12m。矩形沉淀池7采用往复式吸刮泥机,跨度为12m,行走速率为1m/min,配置吸泥泵3台,单台流量为200m3/h,扬程为6m,吸刮泥机收集的污泥通过泵送至集泥槽9;缺氧区3一端与厌氧区2连接,厌氧区2与缺氧区3底面同高,在厌氧区2设置2台潜水推流搅拌器,推流方向为缺氧区3方向,搅拌功率为4W/m3,潜水推流搅拌器叶轮直径1600mm,转速43rpm,功率3.5kW,缺氧区3的另一端与空气提推器4连通,空气提推器4分为4组,单组长度为3m,宽度为1m,液位抬升高度为50mm。 Example 1: A BioDopp biochemical treatment reactor embedded in a rectangular sedimentation tank that treats 15,000 tons of municipal sewage on a certain day, the anaerobic zone 2 is 12m long, 9m wide, and the effective water depth is 7.5m; the anoxic zone 3 is 54m long, wide The length of the aerobic zone 5 is 66m, the width is 10m, and the effective water depth is 7.5m; the rectangular sedimentation tank 7 is 54m long, 12m wide, and the effective water depth is 4.8m. The inlet tank 6 of the rectangular sedimentation tank and the outlet tank 8 of the rectangular sedimentation tank are on one side of the rectangular sedimentation tank 7. The inlet tank 6 of the rectangular sedimentation tank has a length of 54m, a width of 0.5m, and an effective water depth of 1.0m. The length of the outlet tank 8 of the rectangular sedimentation tank is 56m in width, 0.5m in width, and 0.8m effective water depth; the mud collection tank 9 is on the other side of the rectangular sedimentation tank 7, and the mud collection tank 9 has a length of 65m, a width of 0.3m, and an effective water depth of 0.5m; the mud collection tank One end of 9 is connected with the water inlet tank 1, the length of the water inlet tank 1 is 12m, the width is 1.0m, and the effective water depth is 0.8m; Use 1 as backup, the flow rate is 80m 3 /h, and the head is 12m. Rectangular sedimentation tank 7 adopts a reciprocating suction mud scraper with a span of 12m and a walking speed of 1m/min. It is equipped with 3 suction dredge pumps, each with a flow rate of 200m 3 /h and a head of 6m. The sludge collected by the suction mud scraper The mud is pumped to the mud collection tank 9; one end of the anoxic zone 3 is connected to the anaerobic zone 2, and the bottom surface of the anoxic zone 2 and the anoxic zone 3 is at the same height, and two submersible plug-flow mixers are set in the anaerobic zone 2 to push The flow direction is the direction of the anoxic zone 3, the stirring power is 4W/m 3 , the impeller diameter of the submersible plug flow mixer is 1600mm, the rotating speed is 43rpm, and the power is 3.5kW. The pusher 4 is divided into 4 groups, the length of each group is 3m, the width is 1m, and the liquid level lift height is 50mm.
实施例2。 Example 2.
例2:某日处理30000吨市政污水的内嵌矩形沉淀池的BioDopp生化处理反应器,厌氧区2长为18m,宽为8m,有效水深为8m;缺氧区3长为72m,宽为18m,有效高度为2.7m;好氧区5长为83m,宽为13.5m,有效水深为8m;矩形沉淀池7宽为长为72m,宽为18m,有效水深为5.1m。矩形沉淀池进水槽6与矩形沉淀池出水槽8在矩形沉淀池7的一侧,矩形沉淀池进水槽6长度为72m,宽为0.8m,有效水深为1.2m,矩形沉淀池出水槽8长度为74m,宽为0.8m,有效水深1.0m;集泥槽9在矩形沉淀池7的另一侧,集泥槽9长度为82m,宽为0.4m,有效水深为0.5m;集泥槽9一端与进水槽1连通,进水槽1长度为18m,宽为1.0m,有效水深为1.2m;集泥槽9另一端连接排泥管,排泥泵采用干式安装,设置两台,1用1备,流量为160m3/h,扬程为12m。矩形沉淀池7采用2台链板式刮泥机,单台链板式刮泥机工作长度为72m,宽度为9m,链板行走速率为1.5m/min,配置吸泥泵6台,单台流量为200m3/h,扬程为6m,吸泥泵收集的污泥通过泵送至集泥槽9;缺氧区3一端与厌氧区2连接,厌氧区2与缺氧区3底面同高,在厌氧区2设置3台潜水推流搅拌器,推流方向为缺氧区3方向,搅拌功率为3.6W/m3,潜水推流搅拌器叶轮直径2200mm,转速43rpm,功率5.5kW,缺氧区3的另一端与空气提推器4连通,空气提推器4分为6组,单组长度为3m,宽度为1m,液位抬升高度为80mm。 Example 2: A BioDopp biochemical treatment reactor embedded in a rectangular sedimentation tank that treats 30,000 tons of municipal sewage on a certain day, the anaerobic zone 2 is 18m long, 8m wide, and the effective water depth is 8m; the anoxic zone 3 is 72m long, and the width is The aerobic zone 5 is 83m long, 13.5m wide, and 8m effective water depth; the rectangular sedimentation tank 7 is 72m long, 18m wide, and 5.1m effective water depth. The inlet tank 6 of the rectangular sedimentation tank and the outlet tank 8 of the rectangular sedimentation tank are on one side of the rectangular sedimentation tank 7. The inlet tank 6 of the rectangular sedimentation tank has a length of 72m, a width of 0.8m, and an effective water depth of 1.2m. The length of the outlet tank 8 of the rectangular sedimentation tank is 74m in width, 0.8m in width, and 1.0m effective water depth; the mud collection tank 9 is on the other side of the rectangular sedimentation tank 7, and the mud collection tank 9 has a length of 82m, a width of 0.4m, and an effective water depth of 0.5m; the mud collection tank 9 One end is connected to the water inlet tank 1, the length of the water inlet tank 1 is 18m, the width is 1.0m, and the effective water depth is 1.2m; the other end of the mud collection tank 9 is connected to the mud discharge pipe, and the mud discharge pump is installed dry. 1 spare, the flow rate is 160m 3 /h, and the head is 12m. Rectangular sedimentation tank 7 adopts 2 sets of chain plate type mud scraper, the working length of a single chain plate type mud scraper is 72m, the width is 9m, the walking speed of the chain plate is 1.5m/min, and it is equipped with 6 sets of dredge pumps, and the flow rate of a single set is 200m 3 /h, the head is 6m, the sludge collected by the suction pump is pumped to the sludge collection tank 9; one end of the anoxic zone 3 is connected to the anaerobic zone 2, and the bottom of the anoxic zone 2 and the anoxic zone 3 are at the same height. Three submersible plug flow mixers are set in the anaerobic zone 2, the plug flow direction is the direction of the anoxic zone 3, the stirring power is 3.6W/m 3 , the impeller diameter of the submersible plug flow mixer is 2200mm, the speed is 43rpm, and the power is 5.5kW. The other end of the oxygen zone 3 is connected with the air lifter 4, and the air lifter 4 is divided into 6 groups, the length of each group is 3m, the width is 1m, and the liquid level lift height is 80mm.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应包含在本实用新型的保护范围之内。 The above is only a preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made, these improvements and Retouching should also be included within the protection scope of the present utility model.
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| CN115286174A (en) * | 2022-07-08 | 2022-11-04 | 北京首创生态环保集团股份有限公司 | Low-energy-consumption integrated sewage treatment system and method reaching IV-class standard |
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| CN115286174A (en) * | 2022-07-08 | 2022-11-04 | 北京首创生态环保集团股份有限公司 | Low-energy-consumption integrated sewage treatment system and method reaching IV-class standard |
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