CN205347124U - City river drain sewage treatment device - Google Patents
City river drain sewage treatment device Download PDFInfo
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- CN205347124U CN205347124U CN201521119928.8U CN201521119928U CN205347124U CN 205347124 U CN205347124 U CN 205347124U CN 201521119928 U CN201521119928 U CN 201521119928U CN 205347124 U CN205347124 U CN 205347124U
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Abstract
本实用新型涉及一种城市河道排污口污水处理设备,包括相互串联的一级处理单元和二级处理单元,城市河道排污口的污水依次流入所述一级处理单元和二级处理单元进行处理,所述一级处理单元包括依次连接的调节池、管道混合器、折板絮凝反应池和斜板沉淀池,所述二级处理单元包括依次连接的反硝化滤池、硝化曝气滤池和清水池。所述二级处理单元后还可以设置三级处理单元对污水进行进一步过滤。本实用新型充分考虑了河道排污口的地形特点,污水处理设备处理能力强,设备整体耐冲击负荷性能优良,能够适应河道排污口水量陡涨陡落的特点,整体采用串联形式,布置灵活,可以设置于地上也可半埋或全埋地使用,特别适合应用于狭长的城市河道两侧。
The utility model relates to sewage treatment equipment for urban river sewage outlets, comprising a primary treatment unit and a secondary treatment unit connected in series. The primary treatment unit includes a regulating tank, a pipeline mixer, a folded plate flocculation reaction tank, and an inclined plate sedimentation tank connected in sequence, and the secondary treatment unit includes a denitrification filter, a nitrification aeration filter and a clear water filter connected in sequence. pool. After the secondary treatment unit, a tertiary treatment unit can be installed to further filter the sewage. The utility model fully considers the terrain characteristics of the sewage outlet of the river, the sewage treatment equipment has strong processing capacity, the overall impact load resistance performance of the equipment is excellent, and can adapt to the characteristics of the steep rise and fall of the water volume of the sewage outlet of the river. It can be set on the ground and can also be half buried or fully buried, especially suitable for use on both sides of narrow and long urban rivers.
Description
技术领域 technical field
本实用新型涉及一种城市河道排污口污水处理设备,主要适用于用于排放生活污水及其他类似污水的河道排污口的污水处理。 The utility model relates to sewage treatment equipment for urban river channel sewage outlets, which is mainly suitable for sewage treatment at river channel sewage outlets for discharging domestic sewage and other similar sewage.
背景技术 Background technique
城市河道口污水处理方法从很大程度上说是固液分离的技术,现有的污水处理方法一般采用曝气沉砂池(最常见的混合反应池)和初沉池,来去除污水中的悬浮和胶体态物质,然后污水经物理和生物代谢等多种净化作用,从而达到污水排放的要求。 The sewage treatment method at urban river mouths is largely a solid-liquid separation technology. The existing sewage treatment methods generally use aerated grit chambers (the most common mixed reaction tanks) and primary sedimentation tanks to remove Suspended and colloidal substances, and then the sewage undergoes various purification functions such as physical and biological metabolism, so as to meet the requirements of sewage discharge.
但是现有的污水处理方法存在许多的不足之处: But there are many weak points in existing sewage treatment method:
首先,常用的混合反应池、初沉池等水处理单元停留时间长、水力负荷低、初期建设投资高、占地面积大。另外,在去除悬浮物的同时,污水的有机物浓度往往也随之下降,对污水的悬浮物处理程度过高时,CODcr去除量过高,致使后续反硝化工艺中为硝酸盐氮提供碳源减少,反硝化受到抑制,从而需要外加碳源,增加设备费用;若对悬浮物处理程度过低,又会引起后续反硝化生物滤池过快堵塞或需频繁的反冲洗。 First of all, commonly used mixing reaction tanks, primary sedimentation tanks and other water treatment units have long residence time, low hydraulic load, high initial construction investment, and large floor area. In addition, while removing suspended solids, the concentration of organic matter in sewage often also decreases. When the treatment of suspended solids in sewage is too high, the removal of COD cr is too high, resulting in a carbon source for nitrate nitrogen in the subsequent denitrification process. Reduced, denitrification is inhibited, which requires additional carbon sources and increases equipment costs; if the treatment of suspended solids is too low, it will cause the subsequent denitrification biological filter to block too quickly or require frequent backwashing.
其次,曝气生物滤池一般采用后置反硝化工艺,后置反硝化的管理复杂,运行成本高,为了使曝气生物滤池能有较长的运行周期,减少反冲洗次数降低能耗,需对进水进行预处理,否则原水中的大量杂质和SS进入曝气滤池,将会堵塞曝气、布水系统,给系统的运行带来严重的后果。在反硝化过程中由于要脱氮需外加碳源,为保证脱氮效果一般需过量投加碳源,因此会导致反硝化池出水总氮达标而有机物超标,反硝化滤池后一般还要增加除碳设备,增加设备成本。 Secondly, the post-denitrification process is generally adopted in the biological aerated filter. The management of the post-denitrification is complicated and the operation cost is high. The influent water needs to be pretreated, otherwise a large amount of impurities and SS in the raw water will enter the aeration filter, which will block the aeration and water distribution system, and bring serious consequences to the operation of the system. In the process of denitrification, an additional carbon source is required for denitrification. In order to ensure the denitrification effect, an excessive amount of carbon source is generally required. Therefore, the total nitrogen in the effluent of the denitrification tank will reach the standard and the organic matter will exceed the standard. After the denitrification filter, it will generally increase. Carbon removal equipment increases equipment costs.
发明内容 Contents of the invention
为了解决现有技术存在的问题,本实用新型的目的在于提供一种城市河道排污口污水处理设备,通过对现有技术的合理改进使设备整体达到体积小、占地面积省、投资低、处理效率高、工艺流程简单、操作管理方便等优点,设备整体采用串联形式,布置灵活,可以设置于地上也可半埋或全埋地使用,特别适合应用于狭长的城市河道两侧。 In order to solve the problems existing in the prior art, the purpose of this utility model is to provide a kind of sewage treatment equipment for urban river sewage outfalls. Through the reasonable improvement of the prior art, the equipment as a whole can achieve small volume, low floor space, low investment and easy treatment. It has the advantages of high efficiency, simple process, convenient operation and management, etc. The overall equipment adopts a serial form, and the layout is flexible. It can be installed on the ground or half-buried or fully buried. It is especially suitable for use on both sides of narrow and long urban rivers.
本实用新型的技术方案是: The technical scheme of the utility model is:
一种城市河道排污口污水处理设备,包括相互串联的一级处理单元、二级处理单元和三级处理单元,所述一级处理单元包括依次连接的调节池、管道混合器、折板絮凝反应池和斜板沉淀池,所述二级处理单元包括依次连接的反硝化滤池、硝化曝气滤池和清水池,所述三级处理单元设有过滤设备。城市河道排污口连接所述调节池,污水依次经过所述一级处理单元、二级处理单元和三级处理单元的设备进行处理后由所述三级处理单元排出。 A kind of sewage treatment equipment for sewage outfalls of urban rivers, including a primary treatment unit, a secondary treatment unit and a tertiary treatment unit connected in series, the primary treatment unit includes a regulating tank, a pipeline mixer, and a folding plate flocculation reaction connected in sequence pool and inclined plate sedimentation tank, the secondary treatment unit includes denitrification filter, nitrification aeration filter and clear water tank connected in sequence, and the tertiary treatment unit is equipped with filtering equipment. The urban river sewage outfall is connected to the adjustment pool, and the sewage is discharged from the third-level treatment unit after being treated by the equipment of the first-level treatment unit, the second-level treatment unit and the third-level treatment unit.
优选的,所述调节池的入水口处设有细格栅。 Preferably, a fine grill is provided at the water inlet of the regulating pool.
优选的,所述调节池与管道混合器之间设有用于向污水中添加絮凝剂的加药装置。 Preferably, a dosing device for adding flocculant to the sewage is provided between the regulating tank and the pipeline mixer.
优选的,所述管道混合器由管道状壳体和设置在所述管道状壳体内的多节固定叶片组成。 Preferably, the pipeline mixer is composed of a pipeline-shaped casing and multi-section fixed blades arranged in the pipeline-shaped casing.
优选的,所述折板絮凝反应池包括絮凝池体,所述絮凝池体内设有若干组相对的折板,所述折板的两边分别与所述絮凝池体内相对的两个内壁固定连接。 Preferably, the folded plate flocculation reaction tank includes a flocculation tank body, and several sets of opposite folded plates are arranged in the flocculation tank body, and the two sides of the folded plates are respectively fixedly connected with two opposite inner walls of the flocculation tank body.
优选的,所述斜板沉淀池包括沉淀池体,所述沉淀池体的中部为设有斜板装置的折流斜板区,所述沉淀池体的底部为泥斗,所述折流斜板区的上方留有构成清水区的空间,所述折流斜板区的下方和泥斗之间留有构成配水区的空间,所述配水区设有与所述折板絮凝反应池的出水口相连接的入水口,所述斜板装置由两组相对的上斜板和下斜板组成,所述上斜板设有下折边,所述下斜板设有上折边,所述上斜板的下折边和所述下折板的上折边相互交叉分布。 Preferably, the sloping plate sedimentation tank includes a sedimentation tank body, the middle part of the sedimentation tank body is a baffle sloping plate area provided with a sloping plate device, the bottom of the sedimentation tank body is a mud bucket, and the baffle slant A space for forming a clear water area is reserved above the plate area, and a space for forming a water distribution area is reserved under the baffle plate area and between the mud buckets. The water inlet connected to the nozzle, the said sloping plate device is composed of two sets of opposite upper sloping plates and lower sloping plates, the said upper sloping plate is provided with a lower hem, the said lower slanting plate is provided with an upper hem, the said The lower folded edge of the upper inclined plate and the upper folded edge of the lower folded plate intersect each other.
优选的,所述斜板沉淀池底部泥斗的排泥管道接入贮泥池,所述贮泥池的排泥管道接入污泥活化池,所述污泥活化池设有配套的曝气装置,所述污泥活化池的污泥出口通过污泥回流管连接所述折板絮凝反应池。 Preferably, the sludge discharge pipeline of the mud hopper at the bottom of the inclined plate sedimentation tank is connected to the sludge storage tank, and the sludge discharge pipeline of the sludge storage tank is connected to the sludge activation tank, and the sludge activation tank is provided with supporting aeration device, the sludge outlet of the sludge activation tank is connected to the folded plate flocculation reaction tank through a sludge return pipe.
优选的,所述硝化曝气滤池的出水和反硝化滤池的进水之间设有硝化液回流管道,所述硝化液回流管道上设有回流泵和流量计,所述硝化液回流管道的进水端连接所述硝化曝气滤池的出水区、所述硝化曝气滤池的出水管道或清水池,所述硝化液回流管的出水端连接所述反硝化滤池或者反硝化滤池的进水管道。 Preferably, a nitrification liquid return pipeline is provided between the outlet water of the nitrification aeration filter and the inflow of the denitrification filter, and a return pump and a flow meter are arranged on the nitrification liquid return pipeline, and the nitrification liquid return pipeline The water inlet end of the nitrification aeration filter is connected to the water outlet area of the nitrification aeration filter, the water outlet pipe of the nitrification aeration filter or the clear water pool, and the water outlet end of the nitrification liquid return pipe is connected to the denitrification filter or denitrification filter The pool's water inlet pipe.
优选的,还设有反冲洗水泵,所述反冲洗水泵设置在所述清水池与所述反硝化滤池和硝化曝气滤池之间的反冲洗入水管道上,所述反冲洗水泵用于向所述反硝化滤池和硝化曝气滤池提供反冲洗用水,所述反硝化滤池和硝化曝气滤池的反冲洗出水管道连接所述调节池。 Preferably, a backwash water pump is also provided, and the backwash water pump is arranged on the backwash water inlet pipeline between the clear water tank, the denitrification filter and the nitrification aeration filter, and the backwash water pump is used for Backwashing water is provided to the denitrification filter and the nitrification aeration filter, and the backwash outlet pipes of the denitrification filter and the nitrification aeration filter are connected to the regulating tank.
优选的,所述过滤设备的前面或后面还设有消毒池。 Preferably, a disinfection pool is also provided in front of or behind the filtering equipment.
本实用新型的有益效果为: The beneficial effects of the utility model are:
本实用新型将传统的一级处理单元(化学强化一级处理)与二级处理单元(曝气生物滤池)的工艺合理组合并改进应用,使设备整体达到了体积小、占地面积省、投资低、处理效率高、工艺流程简单、操作管理方便等优点。且设备整体耐冲击负荷性能优良,能够适应河道排污口水量陡涨陡落的特点,设备整体采用串联形式,布置灵活,可以设置于地上也可半埋或全埋地使用,特别适合应用于狭长的城市河道两侧。 The utility model rationally combines and improves the technology of the traditional primary treatment unit (chemically strengthened primary treatment) and secondary treatment unit (biological aerated filter), so that the overall equipment achieves small volume, low floor space, Low investment, high processing efficiency, simple process flow, convenient operation and management, etc. Moreover, the overall impact load resistance performance of the equipment is excellent, and it can adapt to the characteristics of the steep rise and fall of the water volume of the sewage outlet of the river. The overall equipment adopts the form of series connection, and the layout is flexible. on both sides of the urban river.
一级处理单元能够去除污水中的大量有机污染物和颗粒悬浮物,以减轻后续工艺的生物负荷,从而降低了整体工艺的耗氧量和剩余污泥的产量; The primary treatment unit can remove a large amount of organic pollutants and suspended particles in the sewage to reduce the biological load of the subsequent process, thereby reducing the oxygen consumption of the overall process and the output of excess sludge;
污水中的SS去除率可以达到90%以上,经其处理的污水完全满足二级处理单元对SS含量的要求,大大延长了反冲洗时间间隔,降低了反冲洗次数及运行费用;同时,一级处理单元降低了污水中有机污染物的浓度,从而可以降低二级处理单元的负荷,起到降低曝气量减少运行费用的效果;一级处理单元合理的控制了进入二级处理单元的碳源量,使异养菌的数量得以控制,给具有除氮作用的硝化菌成长创造了更多的条件,因此提高了除氮的效果。 The SS removal rate in sewage can reach more than 90%, and the treated sewage fully meets the requirements of the secondary treatment unit for SS content, which greatly prolongs the time interval of backwashing, reduces the number of backwashing times and operating costs; at the same time, the primary The treatment unit reduces the concentration of organic pollutants in the sewage, thereby reducing the load of the secondary treatment unit, reducing aeration and reducing operating costs; the primary treatment unit reasonably controls the carbon source entering the secondary treatment unit The quantity can control the number of heterotrophic bacteria and create more conditions for the growth of nitrifying bacteria with nitrogen removal effect, thus improving the effect of nitrogen removal.
二级处理单元采用曝气生物滤池工艺,根据脱氮需要将反硝化滤池前置,前置反硝化可以避免曝气生物滤池系统自身同步脱氮程度不足以满足总氮排放要求的缺点。采用A/O法与生物滤池相结合,同时反硝化、硝化反应在两个串联的反应单元中进行,硝化曝气滤池回流硝化液为反硝化滤池提供硝酸盐氮(NO3—N);同时,采用反硝化滤池前置还可以省去传统反硝化滤池后的除碳设备。 The secondary treatment unit adopts the biological aerated filter process, and the denitrification filter is pre-installed according to the denitrification needs. The pre-denitrification can avoid the disadvantage that the synchronous denitrification degree of the biological aerated filter system itself is not enough to meet the requirements of total nitrogen discharge. . The A/O method is combined with the biological filter, and the denitrification and nitrification reactions are carried out in two series-connected reaction units. The nitrification aeration filter returns the nitrification liquid to provide nitrate nitrogen (NO 3 -N) for the denitrification filter. ); at the same time, the use of the pre-denitrification filter can also save the carbon removal equipment after the traditional denitrification filter.
本实用新型还设有回流活化污泥的设备,能够减少污泥产量及絮凝剂投加量,同时将二级处理单元的反冲洗污泥引入调节池内,进一步降低整个系统的污泥产量。 The utility model is also equipped with equipment for reflux activated sludge, which can reduce the sludge output and flocculant dosage, and at the same time introduce the backwash sludge of the secondary treatment unit into the regulating tank, further reducing the sludge output of the whole system.
本实用新型充分考虑城市河道排污口需处理的污水量,三级处理单元采用单阀滤池或无阀滤池,运行费低,易于自动化控制,可人工设定反冲洗强度,滤料使用寿命长。 The utility model fully considers the amount of sewage to be treated at the sewage outlets of urban rivers. The three-stage treatment unit adopts a single-valve filter or a valveless filter, which has low operating costs and is easy to automatically control. The backwashing intensity can be manually set, and the service life of the filter material long.
附图说明 Description of drawings
图1是本实用新型的原理图; Fig. 1 is a schematic diagram of the utility model;
图2是本实用新型一级处理单元的原理图; Fig. 2 is the schematic diagram of the first-level processing unit of the utility model;
图3是本实用新型二级处理单元的原理图; Fig. 3 is the schematic diagram of the secondary processing unit of the present utility model;
图4是本实用新型三级处理单元的原理图; Fig. 4 is the schematic diagram of the three-level processing unit of the utility model;
图5是本实用新型CEPT设备的结构简图; Fig. 5 is the structural diagram of CEPT equipment of the present utility model;
图6是本实用新型折板絮凝反应池的结构简图; Fig. 6 is a schematic structural diagram of the folding plate flocculation reaction tank of the present invention;
图7是本实用新型折板絮凝反应池的上折板结构简图; Fig. 7 is a schematic diagram of the upper folded plate structure of the folded plate flocculation reaction tank of the present invention;
图8是本实用新型折板絮凝反应池的下折板结构简图; Fig. 8 is a schematic diagram of the lower folded plate structure of the folded plate flocculation reaction tank of the present invention;
图9是本实用新型斜板沉淀池的结构简图; Fig. 9 is a schematic structural diagram of the inclined plate sedimentation tank of the present invention;
图10是本实用新型折流斜板区的斜板的结构简图。 Fig. 10 is a schematic diagram of the structure of the inclined plate in the baffle area of the utility model.
具体实施方式 detailed description
下面结合附图对本实用新型做进一步说明。 Below in conjunction with accompanying drawing, the utility model is further described.
参见图1至图10,本实用新型公开了一种城市河道排污口污水处理设备,包括相互串联的一级处理单元、二级处理单元和三级处理单元,城市河道排污口的污水依次流入所述一级处理单元、二级处理单元和三级处理单元进行处理,所述一级处理单元包括依次连接的调节池和CEPT设备(包括管道混合器1、折板絮凝反应池3和斜板沉淀池4),所述二级处理单元包括依次连接的反硝化滤池(DN池)、硝化曝气滤池(CN池)和清水池,所述三级处理单元设有过滤设备。本实用新型采用一级处理单元、二级处理单元和三级处理单元的串联运行,一级处理单元为二级处理单元的稳定工作创造了良好条件,在保证出水水质达标的前提下,提高了设备整体的工作效率,设备整体具有体积小、占地面积省、投资低、处理效率高、工艺流程简单、操作管理方便等优点。 Referring to Fig. 1 to Fig. 10, the utility model discloses a kind of sewage treatment equipment at the sewage outlet of urban river, which includes a first-level treatment unit, a second-level treatment unit and a third-level treatment unit connected in series, and the sewage from the sewage outlet of the urban river flows into the unit sequentially. The first-level treatment unit, the second-level treatment unit and the third-level treatment unit are processed, and the first-level treatment unit includes the regulating tank and CEPT equipment connected in sequence (including pipeline mixer 1, folded plate flocculation reaction tank 3 and inclined plate sedimentation pool 4), the secondary treatment unit includes a denitrification filter (DN pool), a nitrification aeration filter (CN pool) and a clean water pool connected in sequence, and the tertiary treatment unit is provided with filtering equipment. The utility model adopts the series operation of the first-level treatment unit, the second-level treatment unit and the third-level treatment unit. The first-level treatment unit creates good conditions for the stable operation of the second-level treatment unit. The overall working efficiency of the equipment, the overall equipment has the advantages of small size, small footprint, low investment, high processing efficiency, simple process flow, and convenient operation and management.
所述调节池内设有细格栅,可以截流污水中较大的悬浮物和漂浮物,减轻后续处理压力。 The regulating tank is provided with a fine grid, which can intercept larger suspended matter and floating matter in the sewage, and reduce the subsequent treatment pressure.
所述调节池与管道混合器之间设有用于向污水中添加絮凝剂的加药装置,所述絮凝剂优选采用有机絮凝剂。 A dosing device for adding a flocculant to the sewage is provided between the adjustment tank and the pipeline mixer, and the flocculant is preferably an organic flocculant.
所述管道混合器由管道和设置在管道内的多节固定叶片组成,能够使水流成对分流,同时产生涡旋反向旋转及交叉流动,从而使絮凝剂和污水获得较好的混合效果。 The pipeline mixer is composed of a pipeline and multi-section fixed blades arranged in the pipeline, which can split the water flow in pairs, and simultaneously generate vortex reverse rotation and cross flow, so that the flocculant and sewage can obtain a better mixing effect.
图6所示为本实用新型的折板絮凝反应池,所述折板絮凝反应池由池体10和池体底部的储泥区12组成,所述池体内设有若干组相对的折板,折板分为上折板7和下折板8,相邻两折板分别固定在池体内相对的两个内壁上。图7至图8所示为本实用新型的上折板和下折板,折板上相邻段之间的夹角为90度,折板之间形成污水流通通道,可以增加污水絮凝反应的路程,保证水流达到絮凝所要求的紊流状态,使能量损失得到充分利用,缩短停留时间。污水经管道混合器1和进水管2流入池体内,在水流作用下使污水中的微絮粒相互接触碰撞,以形成更大絮粒,经絮凝反应后大的絮粒沉入池体底部,然后由排泥管11排至泥斗中,处理后的污水由出水口9流出。 Figure 6 shows the folded plate flocculation reaction tank of the present invention, the folded plate flocculation reaction tank is composed of a pool body 10 and a mud storage area 12 at the bottom of the pool body, and several groups of relative folded plates are arranged in the pool body, The folded plates are divided into an upper folded plate 7 and a lower folded plate 8, and two adjacent folded plates are respectively fixed on two opposite inner walls of the pool body. Figures 7 to 8 show the upper and lower folded plates of the present invention. The angle between adjacent segments on the folded plates is 90 degrees, and sewage circulation channels are formed between the folded plates, which can increase the efficiency of sewage flocculation reaction. To ensure that the water flow reaches the turbulent state required for flocculation, so that the energy loss can be fully utilized and the residence time shortened. The sewage flows into the tank through the pipeline mixer 1 and the water inlet pipe 2. Under the action of the water flow, the micro flocs in the sewage contact and collide with each other to form larger flocs. After the flocculation reaction, the large flocs sink to the bottom of the pool. Then it is discharged into the mud hopper by the mud discharge pipe 11, and the treated sewage flows out from the water outlet 9.
图9所示为本实用新型的斜板沉淀池,所述斜板沉淀池自上而下由清水区14、折流斜板区15、配水区16和泥斗17组成,所述清水区上设有出水堰5,所述配水区的入水口19与所述折板絮凝反应池的出水口相连接,清水通过入水口流入配水区,所述泥斗位于所述斜板沉淀池的底部,泥斗内的污泥通过排泥管道18流入贮泥池。图10所示为本实用新型折流斜板区的斜板20,所述折流斜板区由两组相对的斜板组成,两组斜板之间采用交错间隔排列,每组斜板均包含若干个相互平行的板子,相邻斜板间的距离相等且可调节。斜板沉淀池具有沉淀效率高、池体容积小、占地面积少等优点,污水进入配水区,自下而上通过折流斜板区,水中的絮凝颗粒沉淀于斜板上并在重力作用下落入泥斗,清水则通过折流斜板区进入清水区,溢流通过出水管道6进入下一处理单元。 Fig. 9 shows the inclined plate settling tank of the present utility model, and described inclined plate settling tank is made up of clear water area 14, baffle inclined plate area 15, water distribution area 16 and mud bucket 17 from top to bottom, and the upper part of described clear water area A water outlet weir 5 is provided, and the water inlet 19 of the water distribution area is connected with the water outlet of the folded plate flocculation reaction tank, and clear water flows into the water distribution area through the water inlet, and the mud bucket is located at the bottom of the inclined plate sedimentation tank, The sludge in the mud bucket flows into the sludge storage tank through the sludge discharge pipe 18. Figure 10 shows the slant plate 20 in the baffle slant plate area of the present invention. The baffle slant plate area is composed of two groups of opposite slant plates, and the two groups of slant plates are arranged in a staggered interval, and each group of slant plates It includes several parallel boards, and the distance between adjacent inclined boards is equal and adjustable. The inclined plate sedimentation tank has the advantages of high sedimentation efficiency, small tank volume, and less floor space. The sewage enters the water distribution area and passes through the baffled inclined plate area from bottom to top. Falling into the mud bucket, the clear water enters the clear water area through the baffle sloping plate area, and the overflow enters the next processing unit through the outlet pipe 6.
还设有连接所述斜板沉淀池的排泥管道接入贮泥池,所述贮泥池的排泥管道接入污泥活化池,所述污泥活化池设有配套的曝气装置,所述污泥活化池的污泥出口连接所述折板絮凝反应池。贮泥池能够收集所述斜板沉淀池中反应产生的污泥,一部分污泥排出后可用作堆肥等二次利用;另一部分污泥送入污泥活化池中经曝气后送入折板絮凝反应池的池体内,作为生物絮凝剂使用,能够减少设备絮凝剂的投放量。 There is also a sludge discharge pipeline connected to the inclined plate sedimentation tank connected to the sludge storage tank, the sludge discharge pipeline of the sludge storage tank is connected to the sludge activation tank, and the sludge activation tank is provided with a supporting aeration device, The sludge outlet of the sludge activation tank is connected to the flap flocculation reaction tank. The sludge storage tank can collect the sludge produced by the reaction in the inclined plate sedimentation tank, and a part of the sludge can be used for secondary use such as compost after being discharged; The tank body of the plate flocculation reaction tank is used as a biological flocculant, which can reduce the amount of equipment flocculant input.
还设有回流泵和流量计,所述回流泵和流量计设置在所述硝化曝气滤池和反硝化滤池之间的回流管道上,所述回流泵和流量计用于向所述反硝化滤池中回流消化液。 A return pump and a flow meter are also provided, and the return pump and flow meter are arranged on the return pipeline between the nitrification aeration filter and the denitrification filter, and the return pump and flow meter are used to provide The digestate is refluxed in the nitrification filter.
还设有反冲洗水泵,所述反冲洗水泵设置在所述清水池与所述反硝化滤池和硝化曝气滤池之间的反冲洗管道上,所述反冲洗水泵用于向所述反硝化滤池和硝化曝气滤池提供反冲洗用水,所述反硝化滤池和硝化曝气滤池的反冲洗出水管道连接所述调节池。 A backwash water pump is also provided, and the backwash water pump is arranged on the backwash pipeline between the clear water tank, the denitrification filter and the nitrification aeration filter, and the backwash water pump is used to provide The nitrification filter and the nitrification aeration filter provide backwash water, and the backwash outlet pipes of the denitrification filter and the nitrification aeration filter are connected to the regulating tank.
所述清水池的出水管道连接河道或三级处理单元,所述三级处理单元为过滤设备,所述过滤设备优选采用单阀滤池或无阀滤池。 The outlet pipe of the clean water pool is connected to a river course or a tertiary treatment unit, and the tertiary treatment unit is a filter device, and the filter device preferably adopts a single-valve filter or a valveless filter.
根据实际需要,可以设置消毒设施,也可以不设置消毒设置,当设有消毒设施时,所述消毒设施可以采用任意适宜的方式,例如可以是采用液氯消毒的消毒池,也可以能够对管道中的水进行消毒的臭氧消毒设备等,所述消毒设施可以设置在过滤设备的前面,也可以设置在过滤设备的后面。 According to actual needs, disinfection facilities may or may not be provided. When disinfection facilities are provided, the disinfection facilities may adopt any suitable method, for example, it may be a disinfection tank that adopts liquid chlorine disinfection, or it may be able to Ozone disinfection equipment for sterilizing the water in the water, etc., the disinfection facilities can be set in front of the filter equipment, and can also be set behind the filter equipment.
本实用新型的工作过程为:生活污水由城市河道排污口排入调节池中进行调节,通过设置细格栅截流污水中较大的悬浮物和漂浮物,调节池可以调节污水的出水量,使出水量平稳。经调节池调节后的污水进入进水管,污水流入管道混合器,同时加药装置将絮凝剂加入管道混合器中进行充分混合,混合后的液体流入折板絮凝反应池中。污水在紊流状态下经过折板所围成的污水流通通道,污水中的微絮粒相互接触碰撞形成更大絮粒,处理后的污水流入斜板沉淀池中的配水区。随着污水水面的上升,污水进入折流斜板区进一步处理,污水中的絮凝颗粒沉淀于斜板上并在重力作用下落入泥斗,清水则通过折流斜板区进入清水区,通过出水堰流入下一处理单元。 The working process of the utility model is as follows: the domestic sewage is discharged into the regulating pool from the sewage outlet of the urban river for regulation, and the large suspended matter and floating matter in the sewage are intercepted by setting a fine grid, and the regulating pond can regulate the water output of the sewage, so that The water output is stable. The sewage regulated by the regulating tank enters the water inlet pipe, and the sewage flows into the pipeline mixer. At the same time, the dosing device adds the flocculant into the pipeline mixer for full mixing, and the mixed liquid flows into the flap flocculation reaction tank. The sewage passes through the sewage circulation channel surrounded by the folded plates in the turbulent state, and the micro flocs in the sewage contact and collide with each other to form larger flocs, and the treated sewage flows into the water distribution area in the inclined plate sedimentation tank. As the water level of the sewage rises, the sewage enters the baffle plate area for further treatment. The flocculated particles in the sewage settle on the slant plate and fall into the mud bucket under the action of gravity. The clean water enters the clean water area through the baffle plate area and passes through the outlet water. The weir flows into the next processing unit.
经一级处理单元处理后的污水流入反硝化滤池中进行脱氮,然后进入设有填料层的硝化曝气滤池,实现污水的硝化和除碳过程。硝化曝气滤池内的出水一部分回流至反硝化滤池中为反硝化滤池的反硝化作用提供NO3—N,另一部分流入清水池中经溢流排入河道或进入三级处理单元。本实用新型还配有反冲洗水泵,当反硝化滤池和硝化曝气滤池需要冲洗时可以关闭一级处理单元的进水,打开反冲洗水泵进行冲洗,冲洗后的污水回流至一级处理单元。 The sewage treated by the primary treatment unit flows into the denitrification filter for denitrification, and then enters the nitrification aeration filter with a packing layer to realize the process of nitrification and carbon removal of sewage. Part of the effluent from the nitrification aeration filter flows back to the denitrification filter to provide NO 3 -N for the denitrification of the denitrification filter, and the other part flows into the clear water tank and overflows into the river or enters the tertiary treatment unit. The utility model is also equipped with a backwash water pump. When the denitrification filter and the nitrification aeration filter need to be flushed, the water inlet of the primary treatment unit can be closed, the backwash water pump can be turned on for flushing, and the sewage after flushing is returned to the primary treatment. unit.
三级处理单元将污水进行进一步过滤,过滤后的污水直接排入河道或经消毒后排入河道。 The tertiary treatment unit further filters the sewage, and the filtered sewage is directly discharged into the river or after being disinfected.
本实用新型的污水处理设备处理能力强,经一级处理单元和二级处理单元处理后的城市河道排污口污水,其水质可以达到国标《城镇污水处理厂污染物排放标准》(GB18918-2002)规定的一级B排放标准;再经三级处理单元过滤后出水水质可达到北京地方标准《水污染物综合排放标准》(DB11/307-2013)规定的B排放限值(村庄生活污水处理站)。本实用新型充分考虑了河道排污口的地形特点,设备整体耐冲击负荷性能优良,能够适应河道排污口水量陡涨陡落的特点,设备整体采用串联形式,布置灵活,可以设置于地上也可半埋或全埋地使用,特别适合应用于狭长的城市河道两侧。 The sewage treatment equipment of the utility model has a strong treatment capacity, and the water quality of the urban river sewage outlet sewage treated by the primary treatment unit and the secondary treatment unit can reach the national standard "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB18918-2002) The specified first-level B discharge standard; after being filtered by the third-level treatment unit, the effluent water quality can reach the B discharge limit specified in the Beijing local standard "Integrated Water Pollutant Discharge Standard" (DB11/307-2013) (village domestic sewage treatment station ). The utility model fully considers the terrain characteristics of the river sewage outlet, the overall equipment has excellent impact load resistance performance, and can adapt to the characteristics of the steep rise and fall of the water volume of the river sewage outlet. Buried or fully buried, it is especially suitable for use on both sides of narrow and long urban rivers.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107673561A (en) * | 2017-11-07 | 2018-02-09 | 中交生态环保投资有限公司 | A kind of black and odorous water in-situ treatment system and processing method |
| CN109264934A (en) * | 2018-11-20 | 2019-01-25 | 广州鹏凯环境科技股份有限公司 | It is a kind of for handling the integrated high-efficiency sewage treatment device of city domestic sewage |
| CN109607814A (en) * | 2018-12-04 | 2019-04-12 | 大连理工大学 | An alkaline hydrolysis process of excess sludge for preparing biological flocculants |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107673561A (en) * | 2017-11-07 | 2018-02-09 | 中交生态环保投资有限公司 | A kind of black and odorous water in-situ treatment system and processing method |
| CN107673561B (en) * | 2017-11-07 | 2018-09-11 | 中交生态环保投资有限公司 | A kind of black and odorous water in-situ treatment system and processing method |
| CN109264934A (en) * | 2018-11-20 | 2019-01-25 | 广州鹏凯环境科技股份有限公司 | It is a kind of for handling the integrated high-efficiency sewage treatment device of city domestic sewage |
| CN109607814A (en) * | 2018-12-04 | 2019-04-12 | 大连理工大学 | An alkaline hydrolysis process of excess sludge for preparing biological flocculants |
| CN109607814B (en) * | 2018-12-04 | 2021-11-19 | 大连理工大学 | Alkaline hydrolysis process for preparing excess sludge of biological flocculant |
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