CN211999351U - Small-size sewage treatment plant of integration - Google Patents

Small-size sewage treatment plant of integration Download PDF

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CN211999351U
CN211999351U CN202020270901.3U CN202020270901U CN211999351U CN 211999351 U CN211999351 U CN 211999351U CN 202020270901 U CN202020270901 U CN 202020270901U CN 211999351 U CN211999351 U CN 211999351U
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water
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陈志强
刘宝震
陈理想
唐英才
温沁雪
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Harbin Institute of Technology Shenzhen
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Abstract

一种一体化小型污水处理装置,属于污水处理技术领域。反应桶顶部有检查口并分成连通的化粪池一区、化粪池二区、调节区、生物反应区及清水区,进水管与化粪池一区连通,生物反应区内曝气盘在填料下端,曝气管下端与曝气盘连通,上端与电控箱连接,清水区内消毒框与泥/水交替排放气提系统连通,清水泵与排水管连通,电控箱的电磁阀系统一端与曝气泵连接,另一端与第一提气提机构、曝气管及泥/水交替排放气提系统连接,电磁阀系统通过定时器进行设定。本发明解决了小水量污水维护简易及达标排放的技术需求,适用于小水量乡村污水处理,也可用于小水量工业废水的处理。

Figure 202020270901

An integrated small sewage treatment device belongs to the technical field of sewage treatment. There is an inspection port on the top of the reaction tank and is divided into connected septic tank area 1, septic tank area 2, adjustment area, biological reaction area and clean water area. The lower end of the filler, the lower end of the aeration pipe is connected to the aeration pan, the upper end is connected to the electric control box, the disinfection box in the clean water area is connected to the mud/water alternate discharge air lift system, the clean water pump is connected to the drain pipe, and the electromagnetic valve system of the electric control box is connected One end is connected to the aeration pump, the other end is connected to the first stripping mechanism, the aeration pipe and the mud/water alternate discharge stripping system, and the solenoid valve system is set by a timer. The invention solves the technical requirements of simple maintenance and discharge of small water volume sewage, and is suitable for the treatment of small water volume rural sewage and also for the treatment of small water volume industrial waste water.

Figure 202020270901

Description

一种一体化小型污水处理装置An integrated small sewage treatment device

技术领域technical field

本实用新型涉及一种一体化小型污水处理装置,属于污水处理技术领域。The utility model relates to an integrated small sewage treatment device, which belongs to the technical field of sewage treatment.

背景技术Background technique

我国城镇污水处理主要采用集中收集处理模式,处理工艺多采用常规的厌氧-缺氧-好氧(简称AAO)或者循环式活性污泥(简称CASS)工艺。但是乡村污水与城镇污水比较而言,乡村污水水量小且日水量变化波动大,水质也极不稳定,城镇污水应用的AAO和CASS工艺难以适应这种水质水量的冲击。其次,乡村地区较为偏远,与城镇相比,缺少可以随时对大型污水处理工艺维护与调控的专业技术人员,很容易出现因为维护不及时造成的设施因故障而停运。与城镇相比,乡村更难以投入大量运行和维护费用在污水处理设施上。my country's urban sewage treatment mainly adopts the centralized collection and treatment mode, and the treatment process mostly adopts the conventional anaerobic-anoxic-aerobic (AAO) or circulating activated sludge (CASS) process. However, compared with urban sewage, rural sewage has small water volume and large fluctuations in daily water volume, and the water quality is also extremely unstable. Secondly, rural areas are relatively remote. Compared with cities and towns, there is a lack of professional and technical personnel who can maintain and control large-scale sewage treatment processes at any time. It is easy to cause facilities to be shut down due to failures due to untimely maintenance. Compared with cities and towns, it is more difficult for villages to invest a lot of operation and maintenance costs on sewage treatment facilities.

另一方面,乡村受制于自然条件和地理环境问题,村民居住多为户与户之间距离较远的分散形式,这就造成城镇采用的管道收集后再集中处理模式在乡村地区推广存在高投资成本的问题。因此,乡村地区更适于采用小型分散处理设施以解决紧邻多户村民污水的处理问题。如果分散污水处理装置的生物池仅采用好氧处理工艺,其出水氮磷会影响农村水体的富营养化。再考虑到乡村居民施工安装和设备运行维护的可承受能力,需要一种低成本运行和维护的小型污水处理设备,这种污水处理装置要兼顾占地面积小及运行维护费用低的需求。On the other hand, villages are subject to natural conditions and geographical environment problems, and villagers live in a scattered form with a long distance between households, which leads to the high investment in the promotion of the pipeline collection and then centralized processing model adopted in cities and towns in rural areas. question of cost. Therefore, it is more suitable for rural areas to use small decentralized treatment facilities to solve the problem of sewage treatment of villagers close to many households. If the biological pool of the decentralized sewage treatment device only adopts aerobic treatment process, the nitrogen and phosphorus in the effluent will affect the eutrophication of the rural water body. Considering the affordability of construction and installation and equipment operation and maintenance of rural residents, a small sewage treatment equipment with low-cost operation and maintenance is needed. This sewage treatment equipment should take into account the needs of small footprint and low operation and maintenance costs.

实用新型内容Utility model content

为解决背景技术中存在的问题,本实用新型提供一种一体化小型污水处理装置。In order to solve the problems existing in the background technology, the utility model provides an integrated small sewage treatment device.

实现上述目的,本实用新型采取下述技术方案:一种一体化小型污水处理装置,进水管、括反应桶以及电控箱;所述反应桶竖直设置且通过隔板分成化粪池一区、化粪池二区、调节区、生物反应区以及清水区,反应桶的顶部设有检查口;所述进水管化粪池一区连通设置,所述化粪池一区与化粪池二区以及化粪池二区与调节区均通过过流管连通设置,所述调节区通过第一气提机构与生物反应区连通设置,所述生物反应区内设有曝气管、曝气盘以及填料,所述曝气盘位于填料的下端,所述曝气管的下端与曝气盘的进气端连通设置,曝气管的上端与电控箱连接,所述清水区内设有排水管、消毒框、清水泵以及泥/ 水交替排放气提系统;所述消毒框内填充有氯片且与泥/水交替排放气提系统连通设置,所述清水泵放置于清水区的底部且与排水管的进水口连通设置,所述排水管的出水口伸出至地面,所述电控箱包括定时器、电磁阀系统以及曝气泵;所述电磁阀系统的一端与曝气泵连接,电磁阀系统的另一端分别与第一气提机构、曝气管以及泥/水交替排放气提系统连接,电磁阀系统通过定时器进行设定。To achieve the above purpose, the utility model adopts the following technical scheme: an integrated small sewage treatment device, a water inlet pipe, a reaction barrel and an electric control box; the reaction barrel is vertically arranged and divided into a septic tank area by a partition , the second area of the septic tank, the adjustment area, the biological reaction area and the clean water area, and the top of the reaction barrel is provided with an inspection port; The septic tank area and the second area of the septic tank are connected with the adjustment area through the flow pipe, and the adjustment area is connected with the biological reaction area through the first air stripping mechanism, and the biological reaction area is provided with an aeration pipe and an aeration plate. and packing, the aeration pan is located at the lower end of the packing, the lower end of the aeration pipe is arranged in communication with the air inlet end of the aeration pan, the upper end of the aeration pipe is connected with the electric control box, and there is drainage in the clean water area Pipe, disinfection frame, clean water pump and mud/water alternate discharge air lift system; the disinfection frame is filled with chlorine tablets and communicated with the mud/water alternate discharge air lift system, the clean water pump is placed at the bottom of the clean water area and It is arranged in communication with the water inlet of the drainage pipe, and the water outlet of the drainage pipe extends to the ground. The electric control box includes a timer, a solenoid valve system and an aeration pump; one end of the solenoid valve system is connected to the aeration pump. , the other end of the electromagnetic valve system is respectively connected with the first air stripping mechanism, the aeration pipe and the mud/water alternate discharge air stripping system, and the electromagnetic valve system is set by a timer.

与现有技术相比,本实用新型的有益效果是:Compared with the prior art, the beneficial effects of the present utility model are:

本实用新型将粪水分离功能的化粪池与具备脱氮除磷及有机物去除功能的污水处理生物池组合建设,粪水首先经进水管与气泵驱动反应桶连接,处理后的出水由出水管外排或回用;整体运行和维护成本低,设备体积小且结构紧凑,具备粪水分离、污染物中有机物及氮磷的去除能力,抗水质水量变化能力强,可以模块化生产,出水水质可以稳定保持COD低于50mg/L,氨氮10mg/L,满足多地乡村生活污水的排放标准,解决了小水量污水维护简易及达标排放的技术需求,适用于小水量乡村污水处理,也可用于小水量工业废水的处理。The utility model combines a septic tank with functions of manure water separation and a sewage treatment biological tank with functions of denitrification, phosphorus removal and organic matter removal. Effluent or reused; low overall operation and maintenance cost, small size and compact structure, capable of separating manure and water, removing organic matter and nitrogen and phosphorus from pollutants, strong resistance to changes in water quality and quantity, modular production, and effluent quality It can stably keep COD lower than 50mg/L and ammonia nitrogen 10mg/L, which can meet the discharge standards of rural domestic sewage in many places, and solve the technical requirements for simple maintenance and standard discharge of small water volume sewage. It is suitable for small water volume rural sewage treatment, and can also be used for Treatment of small volume industrial wastewater.

附图说明Description of drawings

图1是本实用新型的平面图;Fig. 1 is the plan view of the present utility model;

图2是检查口平面图;Figure 2 is a plan view of the inspection port;

图3是展开剖视图;Figure 3 is an expanded cross-sectional view;

图4是电控箱、气提机构和泥/水交替排放气提系统示意图。Figure 4 is a schematic diagram of an electric control box, a stripping mechanism and a mud/water alternate discharge stripping system.

具体实施方式Detailed ways

下面将结合本实用新型实施例中的附图,对本实用新型中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅是实用新型的一部分实施例,而不是全部的实施例,基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the utility model, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.

具体实施方式一:如图1~图4所示,本实用新型公开了一种一体化小型污水处理装置,进水管1、反应桶以及电控箱24;所述反应桶竖直设置且为圆柱体结构,亦可为截面为方形或者椭圆形的筒体结构,围绕圆心通过隔板依次分成化粪池一区2、化粪池二区3、调节区4、生物反应区5以及清水区6(如图1所示),反应桶的顶部设有检查口103(如图2所示,通过设置在顶部的检查口103可以定期对各个功能单元维护、清扫和管理,抽吸化粪池一区和二区底部的沉积固体物质);所述进水管1与化粪池一区2连通设置,所述化粪池一区2与化粪池二区3以及化粪池二区3与调节区4均通过过流管8连通设置(如图3所示,所述过流管8为倒L型结构,过流管8竖直设置且水平管穿过对应的隔板与相邻的区域连通,继而实现两个相邻区域的连通),所述调节区4通过第一气提机构9-1与生物反应区5连通设置,所述生物反应区5内设有曝气管10-2、曝气盘12以及填料13,所述曝气盘12位于填料13的下端,所述曝气管10-2的下端与曝气盘12的进气端连通设置,曝气管10-2的上端与电控箱24的电磁阀系统的电磁阀二22-2连接,所述清水区6内设有排水管 7、消毒框14、清水泵15以及泥/水交替排放气提系统;所述消毒框14内填充有氯片16用于处理后清水的接触消毒;且与泥/水交替排放气提系统连通设置,所述清水泵15放置于清水区6的底部且与排水管7的进水口连通设置,所述排水管7的出水口伸出至地面,用于处理后水的外排;如图4所示,所述电控箱24设置与地面上,本实用新型中的自控由电控箱24实现,包括定时器 21、电磁阀系统以及曝气泵23;所述电磁阀系统的一端与曝气泵23连接,电磁阀系统的另一端分别与第一气提机构9-1、曝气管10-2以及泥/水交替排放气提系统连接,电磁阀系统通过定时器21进行设定,电磁阀系统由定时器21 设定的时间程序控制。Embodiment 1: As shown in Figures 1 to 4, the utility model discloses an integrated small sewage treatment device, a water inlet pipe 1, a reaction barrel and an electric control box 24; the reaction barrel is vertically arranged and is a cylinder It can also be a cylindrical structure with a square or oval cross-section, and is divided into a septic tank area 2, a second septic tank area 3, an adjustment area 4, a biological reaction area 5 and a clean water area 6 in turn around the center of the circle through the partition plate. (As shown in Figure 1), the top of the reaction barrel is provided with an inspection port 103 (as shown in Figure 2, through the inspection port 103 set at the top, each functional unit can be regularly maintained, cleaned and managed, and a suction septic tank is District and the sedimentary solid matter at the bottom of the second district); the water inlet pipe 1 is set in communication with the first district 2 of the septic tank, and the first district 2 of the septic tank and the second district 3 of the septic tank and the second district 3 of the septic tank are connected with the adjustment The zones 4 are all communicated and arranged through the flow pipe 8 (as shown in FIG. 3 , the flow pipe 8 is an inverted L-shaped structure, the flow pipe 8 is arranged vertically and the horizontal pipe passes through the corresponding partition plate and the adjacent area. communication, and then realize the communication of two adjacent areas), the adjustment zone 4 is set in communication with the biological reaction zone 5 through the first air stripping mechanism 9-1, and the biological reaction zone 5 is provided with an aeration pipe 10-2 , an aeration plate 12 and a filler 13, the aeration plate 12 is located at the lower end of the filler 13, the lower end of the aeration pipe 10-2 is communicated with the air inlet end of the aeration plate 12, and the aeration pipe 10-2 The upper end is connected with the solenoid valve two 22-2 of the solenoid valve system of the electric control box 24, and the clean water area 6 is provided with a drain pipe 7, a disinfection frame 14, a clean water pump 15 and a mud/water alternate discharge air lift system; The disinfection frame 14 is filled with chlorine tablets 16 for contact disinfection of clean water after treatment; and is arranged in communication with the mud/water alternate discharge air lift system, the clean water pump 15 is placed at the bottom of the clean water area 6 and is connected to the inlet of the drain pipe 7. The water outlet is connected and arranged, and the water outlet of the drainage pipe 7 extends to the ground for the discharge of the treated water; as shown in FIG. The electric control box 24 is realized, including a timer 21, a solenoid valve system and an aeration pump 23; one end of the solenoid valve system is connected to the aeration pump 23, and the other end of the solenoid valve system is respectively connected to the first air lift mechanism 9-1 , the aeration pipe 10-2 and the mud/water alternate discharge air stripping system are connected, the solenoid valve system is set by the timer 21, and the solenoid valve system is controlled by the time program set by the timer 21.

具体实施方式二:如图4所示,本实施方式是对具体实施方式一作出的进一步说明,所述第一气提机构9-1包括通气管一10-1以及提升管11,所述通气管一10-1以及提升管11均竖直设置,通气管一10-1的上端与电磁阀一22-1 连接,通气管一10-1的下端与提升管11的下端连通设置,所述提升管11的上端穿过调节区4和生物反应区5之间的隔板与生物反应区5连通设置。Embodiment 2: As shown in FIG. 4 , this embodiment is a further description of Embodiment 1. The first air lift mechanism 9-1 includes a ventilation pipe 10-1 and a riser 11. The air pipe one 10-1 and the riser pipe 11 are both vertically arranged, the upper end of the air pipe one 10-1 is connected with the solenoid valve one 22-1, and the lower end of the air pipe one 10-1 is communicated with the lower end of the riser pipe 11. The upper end of the riser pipe 11 is communicated with the biological reaction zone 5 through the partition between the adjustment zone 4 and the biological reaction zone 5 .

具体实施方式三:如图4所示,本实施方式是对具体实施方式一作出的进一步说明,所述泥/水交替排放气提系统包括中位过水管17、连接斜管18、第二气提机构9-2(用于排泥)和第三气提机构9-3(用于抽提处理后污水);所述中位过水管17的上端穿过生物反应区5和清水区6之间的隔板与生物反应区5连通设置,中位过水管17的下端与连接斜管18的一端连通设置,所述连接斜管18的另一端与第二气提机构9-2连通设置,连接斜管18的中部与第三气提机构9-3连通设置。定时器21控制泥/水交替排放气提系统首先开启第二气提机构9-2,完成管道中泥水混合液排放到化粪池一区2;再开启第三气提机构9-3,抽提生物反应区5处理后的污水流入清水区消毒框14中。泥/水交替排放气提系统代替传统沉淀池,实现泥水分离,节省一体化处理装置池体容积。Embodiment 3: As shown in FIG. 4 , this embodiment is a further description of Embodiment 1. The mud/water alternate discharge air stripping system includes a mid-level water passage pipe 17, a connecting inclined pipe 18, a second gas The lifting mechanism 9-2 (used for sludge discharge) and the third air-lifting mechanism 9-3 (used for extracting the treated sewage); The partition between the two is communicated with the biological reaction zone 5, the lower end of the middle water passage pipe 17 is communicated with one end of the connecting inclined pipe 18, and the other end of the connecting inclined pipe 18 is communicated with the second air lift mechanism 9-2, The middle part of the connecting inclined pipe 18 is communicated with the third air-lifting mechanism 9-3. The timer 21 controls the mud/water alternate discharge air stripping system. First, the second air stripping mechanism 9-2 is turned on, and the mud-water mixture in the pipeline is discharged to the first zone 2 of the septic tank; The sewage treated in the biological reaction zone 5 flows into the disinfection frame 14 of the clean water zone. The mud/water alternate discharge air stripping system replaces the traditional sedimentation tank, realizes the separation of mud and water, and saves the tank volume of the integrated treatment device.

具体实施方式四:如图4所示,本实施方式是对具体实施方式三作出的进一步说明,所述第二气提机构9-2包括通气管二10-3以及污泥管19,所述通气管二10-3的上端与电磁阀三22-3连接,通气管二10-3的下端与污泥管19 的下端连通设置,所述污泥管19的底部与连接斜管18的另一端连通设置,污泥管19的上端穿过化粪池一区2与清水区6之间的隔板与化粪池一区2连通设置。Embodiment 4: As shown in FIG. 4 , this embodiment is a further description of Embodiment 3. The second air stripping mechanism 9-2 includes a second ventilation pipe 10-3 and a sludge pipe 19. The upper end of the second ventilation pipe 10-3 is connected with the third solenoid valve 22-3, the lower end of the second ventilation pipe 10-3 is communicated with the lower end of the sludge pipe 19, and the bottom of the sludge pipe 19 is connected to the other side of the inclined pipe 18. One end is connected and arranged, and the upper end of the sludge pipe 19 is communicated with the first area 2 of the septic tank through the partition between the first area 2 of the septic tank and the clean water area 6 .

具体实施方式五:如图4所示,本实施方式是对具体实施方式三作出的进一步说明,所述第三气提机构9-3包括通气管三10-4以及清水管20,所述通气管三10-4的上端与电磁阀四22-4连接,通气管三10-4的下端与清水管20 的下端连通设置,所述清水管20的底部与连接斜管18的中部连通设置,清水管20的上端与消毒框14连通设置。Embodiment 5: As shown in FIG. 4 , this embodiment is a further description of Embodiment 3. The third air-lifting mechanism 9-3 includes a ventilation pipe 10-4 and a clean water pipe 20. The upper end of the air pipe three 10-4 is connected with the solenoid valve four 22-4, the lower end of the air pipe three 10-4 is communicated with the lower end of the clean water pipe 20, and the bottom of the clean water pipe 20 is communicated with the middle part of the connection inclined pipe 18, The upper end of the clean water pipe 20 is arranged in communication with the disinfection frame 14 .

具体实施方式六:本实施方式是对具体实施方式一作出的进一步说明,所述清水泵15设有浮漂,通过浮漂的漂浮状态控制清水的启闭。Embodiment 6: This embodiment is a further description of Embodiment 1. The clean water pump 15 is provided with a float, and the opening and closing of clean water is controlled by the floating state of the float.

具体实施方式七:本实施方式是对具体实施方式一作出的进一步说明,所述反应桶的材质为钢或塑料或混凝土。Embodiment 7: This embodiment is a further description of Embodiment 1, and the material of the reaction barrel is steel, plastic or concrete.

具体实施方式八:本实施方式是对具体实施方式七作出的进一步说明,所述塑料为玻璃钢或PP材料(聚丙烯)或PVC材料。Embodiment 8: This embodiment is a further description of Embodiment 7, and the plastic is FRP or PP material (polypropylene) or PVC material.

具体实施方式九:本实施方式是对具体实施方式三作出的进一步说明,所述连接斜管18的倾斜角度为15°~30°。Embodiment 9: This embodiment is a further description of Embodiment 3, and the inclination angle of the connecting inclined pipe 18 is 15°˜30°.

具体实施方式十:本实施方式是对具体实施方式一作出的进一步说明,所述填料13占生物反应区5体积的3/4,位于设计水位以下20~25cm。Embodiment 10: This embodiment is a further description of Embodiment 1. The filler 13 occupies 3/4 of the volume of the biological reaction zone 5 and is located 20-25 cm below the design water level.

具体实施方式十一:本实施方式是对具体实施方式十作出的进一步说明,所述填料13为球形多孔悬浮填料或悬挂式固定填料。Embodiment 11: This embodiment is a further description of Embodiment 10, and the filler 13 is a spherical porous suspended filler or a suspended fixed filler.

本实用新型的污水处理方法,包括如下步骤:The sewage treatment method of the present invention comprises the following steps:

步骤一:小型生活污水可由卫生间、厨房等地方通过下水道直接连通进水管1,进入与进水管1连通的化粪池一区2内;Step 1: Small domestic sewage can be directly connected to the water inlet pipe 1 through the sewers in the toilet, kitchen and other places, and enter the first area 2 of the septic tank connected with the water inlet pipe 1;

步骤二:粪便在步骤一所述的化粪池一区2中沉淀(粪水在化粪池一区2 中静置完成固体颗粒物质和液体的分离:粪便等大颗粒物质沉淀到底部,上部为不含大颗粒物质的上清液),污水(上清液)经过对应的过流管8进入化粪池二区3内;Step 2: The feces are precipitated in the first zone 2 of the septic tank described in step 1 (the fecal water is left standing in the first zone 2 of the septic tank to complete the separation of solid particulate matter and liquid: the large particulate matter such as feces is precipitated to the bottom, and the upper It is the supernatant that does not contain large particulate matter), and the sewage (supernatant) enters the second area 3 of the septic tank through the corresponding flow pipe 8;

步骤三:污水在化粪池二区3内进一步沉淀(小固体颗粒物质和液体进一步实现固液分离,小固体颗粒物质沉淀到池底,)后,经过对应的过流管8 进入调节区4内;Step 3: The sewage is further precipitated in the second zone 3 of the septic tank (the solid-liquid separation is further achieved between the small solid particulate matter and the liquid, and the small solid particulate matter settles to the bottom of the tank), and then enters the adjustment zone 4 through the corresponding flow pipe 8 Inside;

步骤四:经过步骤二和步骤三两次沉淀的污水在调节区4内暂存,至定时器21预定时间开启电磁阀系统(电磁阀一22-1),启动第一气提机构9-1,将调节区4中的污水提升进入生物反应区5;Step 4: The sewage precipitated twice in Step 2 and Step 3 is temporarily stored in the adjustment zone 4, and the solenoid valve system (solenoid valve 1 22-1) is opened at the predetermined time of the timer 21, and the first air lift mechanism 9-1 is activated. , the sewage in the adjustment zone 4 is lifted into the biological reaction zone 5;

步骤五:步骤四所述定时时间结束后关闭电磁阀系统(电磁阀一22-1);Step 5: Close the solenoid valve system (solenoid valve 1 22-1) after the timing described in step 4 expires;

步骤六:污水在生物反应区5中,通过预定程序,启动电磁阀二22-2,进行间歇曝气模式的污水处理;Step 6: When the sewage is in the biological reaction zone 5, through a predetermined procedure, the solenoid valve 2 22-2 is activated to perform the sewage treatment in the intermittent aeration mode;

步骤七:通过步骤六的间歇曝气,连通生物反应区5的中位过水管17以及连接斜管18中进入泥水混合液;Step 7: Through the intermittent aeration of Step 6, the middle water passage 17 and the connecting inclined pipe 18 of the biological reaction zone 5 are connected to enter the mud-water mixture;

步骤八:关闭电磁阀二22-2,进行生物反应区5沉淀,沉淀期结束后,定时器21启动电磁阀系统的电磁阀三22-3,启动第二气提机构9-2,抽提和排放掉中位过水管17以及连接斜管18中残存的泥水混合液,并通过污泥管 19回流到化粪池一区2中;Step 8: Close the solenoid valve two 22-2, carry out precipitation in the biological reaction zone 5, after the precipitation period ends, the timer 21 activates the solenoid valve three 22-3 of the solenoid valve system, activates the second air stripping mechanism 9-2, and extracts And discharge the residual mud-water mixture in the neutral water-passing pipe 17 and the connecting inclined pipe 18, and return to the septic tank one area 2 through the sludge pipe 19;

步骤九:预定时间后关闭电磁阀系统的电磁阀三22-3,开启电磁阀四 22-4,启动第三气提机构9-3;Step 9: After a predetermined time, the solenoid valve three 22-3 of the solenoid valve system is closed, the solenoid valve four 22-4 is opened, and the third air lift mechanism 9-3 is activated;

步骤十:将处理并沉淀后的污水经由第三气提机构9-3抽吸到清水区6 上部的消毒框14中;Step ten: the treated and precipitated sewage is sucked into the disinfection frame 14 above the clean water area 6 through the third air stripping mechanism 9-3;

步骤十一:污水自上而下流经消毒框14中装填的氯片16,以接触消毒的方式消毒后进入清水区6中暂存;Step eleven: the sewage flows from top to bottom through the chlorine tablets 16 loaded in the disinfection frame 14, and enters the clean water area 6 for temporary storage after being disinfected by contact disinfection;

步骤十二:随着清水区6中水面逐渐升高,清水泵15自带的浮漂逐渐上浮到预设点后,启动抽水;Step 12: As the water level in the clean water area 6 gradually rises, the float that comes with the clean water pump 15 gradually rises to the preset point, and then starts pumping;

步骤十三:抽提的污水经过排水管7排放或者回用;Step 13: the extracted sewage is discharged or reused through the drain pipe 7;

步骤十四:随着清水区6中液面下降,当浮漂降低到池底时自动关闭清水泵15。Step 14: As the liquid level in the clean water area 6 drops, the clean water pump 15 is automatically turned off when the float is lowered to the bottom of the pool.

步骤六中所述间歇曝气模式是通过定时器21控制电磁阀系统(电磁阀 22-2)的启闭,从而控制曝气管10-2中通气与否,实现间隙曝气。运行采用 12h为一个运行周期,一天2个周期。每个周期包括进水期、间歇曝气一期、好氧期、间歇曝气二期及沉淀期等5个时间段。其中进水15min,间歇曝气期 1h,间歇曝气一期含4个循环(每个循环包括曝气5min,停止曝气10min,共四循环合计1小时);好氧期8小时,间歇曝气二期1小时,同样含四个循环(每个循环包括曝气5min,停止曝气10min,四循环合计1小时);沉淀期1 小时45min。实现在好氧活性污泥的作用下,污水中的大部分有机物被氧化为二氧化碳与水、氨氮被氧化为硝酸盐;停止曝气条件下的缺氧环境中,污泥中反硝化细菌将硝酸盐氮转化为氮气,最终实现总氮去除,缺氧与好氧交替运行的环境也有助于磷的去除。In the intermittent aeration mode described in step 6, the opening and closing of the electromagnetic valve system (the electromagnetic valve 22-2) is controlled by the timer 21, thereby controlling whether the aeration pipe 10-2 is ventilated or not, so as to realize the gap aeration. The operation adopts 12h as an operation cycle, 2 cycles a day. Each cycle includes five time periods, including the water intake period, the first period of intermittent aeration, the aerobic period, the second period of intermittent aeration and the precipitation period. Among them, the water inlet is 15 minutes, the intermittent aeration period is 1 hour, and the first period of intermittent aeration includes 4 cycles (each cycle includes aeration for 5 minutes, aeration is stopped for 10 minutes, and the total of four cycles is 1 hour); the aerobic period is 8 hours, and the intermittent aeration period is 8 hours. The second phase of aeration is 1 hour, and also includes four cycles (each cycle includes aeration for 5 minutes, aeration is stopped for 10 minutes, and the four cycles are 1 hour in total); the precipitation period is 1 hour and 45 minutes. Under the action of aerobic activated sludge, most of the organic matter in the sewage is oxidized to carbon dioxide and water, and ammonia nitrogen is oxidized to nitrate; in an anoxic environment under the condition of stopping aeration, the denitrifying bacteria in the sludge will convert the nitric acid. The salt nitrogen is converted into nitrogen, and the total nitrogen removal is finally realized. The environment of alternating anoxic and aerobic operation also contributes to the removal of phosphorus.

本实用新型使用时需满足最小覆土埋深及冰冻线的要求。装置整体埋于地下,地面仅有电控箱24。When the utility model is used, it needs to meet the requirements of the minimum buried depth of the covering soil and the freezing line. The whole device is buried underground, with only the electric control box 24 on the ground.

每个通气管均通过电磁阀系统连接曝气泵23,曝气泵23工作后,气体通过对应的通气管向下流动,在各个通气管和提升管11、污泥管19或清水管20 的连接处形成一定的吸引力,将混合液连通输入的气体一起通过混合液提升管提升到另一位置。Each ventilation pipe is connected to the aeration pump 23 through a solenoid valve system. After the aeration pump 23 works, the gas flows downward through the corresponding ventilation pipe. A certain attraction is formed at the connection, and the mixed liquid is connected to the input gas and is lifted to another position through the mixed liquid riser.

实施例1:Example 1:

反应桶直径1.5m,高1.5m,化粪池一区2、化粪池二区3、调节池4、生物反应区5及清水区6体积比2:1:1:2:2,运行效果为:进水COD为312~342 mg/L,出水COD为10.2~15.2mg/L;进水氨氮为14.3~18.7mg/L,出水氨氮为0.9~1.3mg/L;进水总氮为38~48mg/L,出水总氮为14.3~18.7mg/L;进水总磷为4.06~5.29mg/L,出水总磷为1.39~2.48mg/L。生物反应区污泥浓度为3573~4300mg/L。The diameter of the reaction tank is 1.5m and the height is 1.5m. The volume ratio of the first zone of septic tank 2, the second zone of septic tank 3, the adjustment tank 4, the biological reaction zone 5 and the clean water zone 6 is 2:1:1:2:2, the operation effect The COD of the influent is 312-342 mg/L, the COD of the effluent is 10.2-15.2 mg/L; the ammonia nitrogen of the influent is 14.3-18.7 mg/L, the ammonia nitrogen of the effluent is 0.9-1.3 mg/L; the total nitrogen of the influent is 38 ~48mg/L, total nitrogen in effluent is 14.3~18.7mg/L; total phosphorus in influent is 4.06~5.29mg/L, and total phosphorus in effluent is 1.39~2.48mg/L. The sludge concentration in the biological reaction zone is 3573-4300 mg/L.

污水首先经过进水管1与反应桶连接,污水重力流入化粪池一区2、化粪池二区3及调节区4。粪便沉淀在化粪池一区2和化粪池二区3的底部并定期清掏,沉淀后的污水随后进入调节区4。在调节区4内设置第一气提机构9-1,将污水提升至生物反应区5。在生物反应区5内设置填料13,底部设置曝气管 10-2,生物反应区5和清水区6之间隔板中部设置中位过水管17;清水区6 内部设置泥/水交替排放气提系统、装填消毒片(氯片16)的消毒框14及自带浮漂的清水泵15。泥/水交替排放气提系统将生物反应区5的中位过水管17 中的污泥及污水依此提升,泥/水交替排放气提系统包括中位过水管17、第二气提机构9-2、第三气提机构9-3及连接斜管18。第一气提机构9-1将污水提升至生物反应区5后,按照程序控制完成污染物的去除,随后通过沉淀完成泥水分离。虽然中位过水管17之上为清水区6,但中位过水管17和连接斜管18 中堆积好氧反应时进入的污泥,需要将这些污泥当作剩余污泥排放到化粪池一区2,首先启动第二气提机构9-2将连接斜管18中的污泥回流到化粪池一区2,随后启动第三气提机构9-3将生物反应区5的中位过水管17位置上的清水经装填消毒片的消毒框14后转移到清水区6暂存。清水区6中的清水泵15随后启动排水。曝气泵23分别连接第一气提机构9-1、泥/水交替排放气提系统和曝气管10-2,由定时器21控制电磁阀系统实现各气体管路开启。The sewage is first connected to the reaction barrel through the water inlet pipe 1, and the sewage gravity flows into the first area of the septic tank 2, the second area of the septic tank 3 and the adjustment area 4. The feces are deposited at the bottom of the first zone 2 of the septic tank and the bottom of the second zone 3 of the septic tank and are cleaned regularly, and the sedimented sewage then enters the adjustment zone 4. A first air stripping mechanism 9 - 1 is arranged in the conditioning zone 4 to lift the sewage to the biological reaction zone 5 . A filler 13 is arranged in the biological reaction zone 5, an aeration pipe 10-2 is arranged at the bottom, and a middle water passage pipe 17 is arranged in the middle of the partition plate between the biological reaction zone 5 and the clean water zone 6; System, disinfection frame 14 filled with disinfection tablets (chlorine tablets 16), and clean water pump 15 with its own float. The mud/water alternate discharge air stripping system lifts the sludge and sewage in the middle water passage pipe 17 of the biological reaction zone 5 accordingly. The mud/water alternate discharge air stripping system includes the middle water passage pipe 17 and the second air stripping mechanism 9 -2. The third air-lifting mechanism 9-3 and the connecting inclined pipe 18. After the first air stripping mechanism 9-1 lifts the sewage to the biological reaction zone 5, it completes the removal of pollutants according to the program control, and then completes the separation of mud and water through precipitation. Although the clear water area 6 is located above the median water passage pipe 17, the sludge entering during the aerobic reaction is accumulated in the median water passage pipe 17 and the connecting inclined pipe 18, and these sludges need to be discharged to the septic tank as excess sludge. First zone 2, firstly start the second air stripping mechanism 9-2 to return the sludge in the connecting inclined pipe 18 to the first zone 2 of the septic tank, and then start the third air stripping mechanism 9-3 to remove the middle position of the biological reaction zone 5 The clean water at the position of the water pipe 17 is transferred to the clean water area 6 for temporary storage after being filled with the disinfection frame 14 of the disinfection sheet. The clean water pump 15 in the clean water zone 6 then starts to drain. The aeration pump 23 is respectively connected to the first air stripping mechanism 9-1, the mud/water alternate discharge air stripping system and the aeration pipe 10-2, and the solenoid valve system is controlled by the timer 21 to realize the opening of each gas pipeline.

本实用新型的特点是提出一种化粪池与污水处理池合并建设的小型污水处理装置,采用曝气泵23驱动实现污水提升、污水缺氧混合与好氧处理、剩余污泥排放及污水提升。应用时,将曝气泵23、定时器21及电磁阀系统放置在电控箱24内,曝气泵23通过电磁阀系统分别与第一气提机构9-1、泥/水交替排放气提系统和曝气管10-2连接,电磁阀系统的开启由24小时计程的定时器21控制。采用定时器21实现曝气泵23连接的电磁阀系统在不同时段开启,进而分别完成污水提升、间歇曝气、污泥排放及清水提升。The feature of the utility model is to propose a small sewage treatment device constructed by merging a septic tank and a sewage treatment tank. The aeration pump 23 is used to drive to realize sewage lifting, anoxic mixing and aerobic treatment of sewage, excess sludge discharge and sewage lifting. . During application, the aeration pump 23, the timer 21 and the solenoid valve system are placed in the electric control box 24, and the aeration pump 23 is respectively discharged with the first air lift mechanism 9-1 and the mud/water alternately through the solenoid valve system. The system is connected to the aeration pipe 10-2, and the opening of the solenoid valve system is controlled by a timer 21 with a 24-hour schedule. The timer 21 is used to realize that the solenoid valve system connected to the aeration pump 23 is opened at different time periods, thereby completing sewage lifting, intermittent aeration, sludge discharge and clean water lifting respectively.

本方面运行和维护成本低,设备体积小且结构紧凑,具备粪水分离、污染物中有机物及氮磷的去除能力,抗水质水量变化能力强,可以模块化生产,解决了小型小水量污水维护简易及达标排放的技术需求。In this aspect, the operation and maintenance costs are low, the equipment is small in size and compact in structure, and it has the ability to separate manure and water, remove organic matter and nitrogen and phosphorus from pollutants, and has strong resistance to changes in water quality and quantity. Technical requirements for simple and standard discharge.

对于本领域技术人员而言,显然本实用新型不限于上述示范性实施例的细节,而且在不背离本实用新型的精神或基本特征的情况下,能够以其他的形式实现本实用新型。因此,无论从哪一点来看,均应将实施例看作是示范性的,而且是非限制性的,本实用新型的范围由所附权利要求而不是上述说明限定,因此旨在将落在权利要求的等同条件的含义和范围内的所有变化囊括在本实用新型内。不应将权利要求中的任何附图标记视为限制所涉及的权利要求。It will be apparent to those skilled in the art that the present invention is not limited to the details of the above-described exemplary embodiments, and that the present invention may be implemented in other forms without departing from the spirit or essential characteristics of the present invention. Therefore, the embodiments are to be considered in all respects as exemplary and not restrictive, and the scope of the present invention is defined by the appended claims rather than the foregoing description, and it is therefore intended that the All changes within the meaning and range of the required equivalents are embraced within the present invention. Any reference signs in the claims shall not be construed as limiting the involved claim.

此外,应当理解,虽然本说明书按照实施方式加以描述,但并非每个实施方式仅包含一个独立的技术方案,说明书的这种叙述方式仅仅是为清楚起见,本领域技术人员应当将说明书作为一个整体,各实施例中的技术方案也可以经适当组合,形成本领域技术人员可以理解的其他实施方式。In addition, it should be understood that although this specification is described in terms of embodiments, not each embodiment only includes an independent technical solution, and this description in the specification is only for the sake of clarity, and those skilled in the art should take the specification as a whole , the technical solutions in each embodiment can also be appropriately combined to form other implementations that can be understood by those skilled in the art.

Claims (11)

1. The utility model provides a small-size sewage treatment plant of integration, includes inlet tube (1), its characterized in that: the sewage treatment device also comprises a reaction barrel and an electric cabinet (24); the reaction barrel is vertically arranged and is divided into a septic tank first area (2), a septic tank second area (3), a regulating area (4), a biological reaction area (5) and a clear water area (6) through partition plates, and the top of the reaction barrel is provided with an inspection hole (103); the water inlet pipe (1) is communicated with the first septic tank area (2), the first septic tank area (2) and the second septic tank area (3) as well as the second septic tank area (3) and the adjusting area (4) are communicated through the overflow pipe (8), the adjusting area (4) is communicated with the biological reaction area (5) through a first air stripping mechanism (9-1), an aeration pipe (10-2), an aeration disc (12) and a filler (13) are arranged in the biological reaction zone (5), the aeration disc (12) is positioned at the lower end of the filler (13), the lower end of the aeration pipe (10-2) is communicated with the air inlet end of the aeration disc (12), the upper end of the aeration pipe (10-2) is connected with the electric cabinet (24), a drain pipe (7), a disinfection frame (14), a clean water pump (15) and a mud/water alternative discharge air stripping system are arranged in the clean water area (6); chlorine sheets (16) are filled in the disinfection frame (14) and are communicated with the mud/water alternative discharge air stripping system, the clean water pump (15) is placed at the bottom of the clean water area (6) and is communicated with a water inlet of the drain pipe (7), a water outlet of the drain pipe (7) extends out of the ground, and the electric cabinet (24) comprises a timer (21), an electromagnetic valve system and an aeration pump (23); one end of the solenoid valve system is connected with the aeration pump (23), the other end of the solenoid valve system is respectively connected with the first air stripping mechanism (9-1), the aeration pipe (10-2) and the mud/water alternative discharge air stripping system, and the solenoid valve system is set through a timer (21).
2. The integrated small-sized sewage treatment device according to claim 1, wherein: the first air stripping mechanism (9-1) comprises a first air pipe (10-1) and a lifting pipe (11), the first air pipe (10-1) and the lifting pipe (11) are both vertically arranged, the upper end of the first air pipe (10-1) is connected with a first electromagnetic valve (22-1), the lower end of the first air pipe (10-1) is communicated with the lower end of the lifting pipe (11), and the upper end of the lifting pipe (11) is communicated with the biological reaction zone (5).
3. The integrated small-sized sewage treatment device according to claim 1, wherein: the mud/water alternative discharge air stripping system comprises a middle water passing pipe (17), a connecting inclined pipe (18), a second air stripping mechanism (9-2) and a third air stripping mechanism (9-3); the upper end of the middle position water pipe (17) is communicated with the biological reaction zone (5), the lower end of the middle position water pipe (17) is communicated with one end of the connecting inclined pipe (18), the other end of the connecting inclined pipe (18) is communicated with the second air stripping mechanism (9-2), and the middle part of the connecting inclined pipe (18) is communicated with the third air stripping mechanism (9-3).
4. The integrated small-sized sewage treatment device according to claim 3, wherein: the second air lifting mechanism (9-2) comprises a second air pipe (10-3) and a sludge pipe (19), the upper end of the second air pipe (10-3) is connected with a third electromagnetic valve (22-3), the lower end of the second air pipe (10-3) is communicated with the lower end of the sludge pipe (19), the bottom of the sludge pipe (19) is communicated with the other end of the connecting inclined pipe (18), and the upper end of the sludge pipe (19) is communicated with the first septic tank area (2).
5. The integrated small-sized sewage treatment device according to claim 3, wherein: the third air lifting mechanism (9-3) comprises a vent pipe III (10-4) and a clean water pipe (20), the upper end of the vent pipe III (10-4) is connected with an electromagnetic valve IV (22-4), the lower end of the vent pipe III (10-4) is communicated with the lower end of the clean water pipe (20), the bottom of the clean water pipe (20) is communicated with the middle of a connecting inclined pipe (18), and the upper end of the clean water pipe (20) is communicated with the disinfection frame (14).
6. The integrated small-sized sewage treatment device according to claim 1, wherein: the clean water pump (15) is provided with a buoy.
7. The integrated small-sized sewage treatment device according to claim 1, wherein: the reaction barrel is made of steel, plastic or concrete.
8. The integrated small-sized sewage treatment device according to claim 7, wherein: the plastic is glass fiber reinforced plastic or PP material or PVC material.
9. The integrated small-sized sewage treatment device according to claim 3, wherein: the inclined angle of the connecting inclined pipe (18) is 15-30 degrees.
10. The integrated small-sized sewage treatment device according to claim 1, wherein: the filler (13) occupies 3/4 of the volume of the biological reaction zone (5) and is located 20-25 cm below the designed water level.
11. The integrated small-sized sewage treatment device according to claim 10, wherein: the filler (13) is spherical porous suspension filler or suspension type fixed filler.
CN202020270901.3U 2020-03-08 2020-03-08 Small-size sewage treatment plant of integration Active CN211999351U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
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CN111777259A (en) * 2020-03-08 2020-10-16 哈尔滨工业大学 An integrated small sewage treatment device and treatment method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111777259A (en) * 2020-03-08 2020-10-16 哈尔滨工业大学 An integrated small sewage treatment device and treatment method
CN111777259B (en) * 2020-03-08 2024-05-31 哈尔滨工业大学 An integrated small-scale sewage treatment device and treatment method

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