CN210012657U - A sectional water inlet type air lift and return integrated sewage treatment device - Google Patents

A sectional water inlet type air lift and return integrated sewage treatment device Download PDF

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CN210012657U
CN210012657U CN201920405123.1U CN201920405123U CN210012657U CN 210012657 U CN210012657 U CN 210012657U CN 201920405123 U CN201920405123 U CN 201920405123U CN 210012657 U CN210012657 U CN 210012657U
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water inlet
tank
aerobic tank
aerobic
anoxic
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孙敏
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Suzhou Juyao Environmental Protection Technology Co Ltd
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Abstract

The utility model discloses a sectional water inlet type air-lift backflow integrated sewage treatment device, which comprises a treatment box, a water inlet and a gas pipe, wherein eight baffles are arranged inside the treatment box, and the eight baffles divide the interior of the treatment box into a first buffer chamber, an anoxic tank a, an aerobic tank a, an anoxic tank b, an aerobic tank b, an anoxic tank c, an aerobic tank c, a second buffer zone and a secondary sedimentation tank in sequence, the water inlet comprises a first water inlet, a second water inlet and a third water inlet, the first water inlet is arranged on the upper end surface of the anoxic tank a, the second water inlet is arranged on the upper end surface of the anoxic tank b, after the utility model is sectioned, the microbial biomass in a reactor is in gradient degressive, the microbial biomass in the device is effectively maintained, the decontamination effect of the device is ensured, the concentration of precipitated sludge is effectively reduced, and the phenomenon that the amount of the returned sludge is less to cause sludge floating is avoided, ensuring the quality of the effluent.

Description

一种分段进水式气升回流一体化污水处理装置A sectional water inlet type air lift and return integrated sewage treatment device

技术领域technical field

本实用新型涉及污水处理技术领域,具体为一种分段进水式气升回流一体化污水处理装置。The utility model relates to the technical field of sewage treatment, in particular to a sectional water inlet type air lift and return integrated sewage treatment device.

背景技术Background technique

目前我国广大农村及偏远地区的生活污水导致的水污染问题日益突出。针对当前的水污染问题,分散式污水处理是其必要的补充。At present, the problem of water pollution caused by domestic sewage in the vast rural and remote areas of our country has become increasingly prominent. In view of the current water pollution problem, decentralized sewage treatment is a necessary supplement.

目前国内外有很多分散式污水处理技术工艺,如厌氧沼气池、净化槽、生物膜法、人工湿地、土地处理系统、稳定塘和小型污水处理厂等。At present, there are many decentralized sewage treatment technologies at home and abroad, such as anaerobic digesters, purification tanks, biofilm methods, constructed wetlands, land treatment systems, stabilization ponds and small sewage treatment plants.

申请号为200910182634.2的专利中提出了一种气升回流一体化污水处理装置,具有操作运行简单、维护较方便、占地面积小、可设计成地埋式、勿需回流泵,能耗低、污泥龄比较长,排放剩余污泥少等特点。但是实际运行中发现:通过气提作用回流的硝化液和污泥量时有不足,仅为进水流量的75%-120%,时常无法达到传统A2/O工艺中所需的回流量(200%-300%),因此,该装置的硝化液和污泥回流量不足,影响其脱氮效果。The patent with the application number of 200910182634.2 proposes an integrated sewage treatment device with air lift and return, which has the advantages of simple operation, convenient maintenance, small footprint, can be designed as a buried type, no need for a return pump, low energy consumption, The sludge age is relatively long and the discharge of excess sludge is less. However, in actual operation, it is found that the amount of nitrification liquid and sludge returned by air stripping is sometimes insufficient, which is only 75%-120% of the influent flow, and often cannot reach the required return flow in the traditional A2/O process (200%). %-300%), therefore, the nitrification solution and sludge return flow of the device is insufficient, which affects its denitrification effect.

实用新型内容Utility model content

本实用新型的目的在于提供一种分段进水式气升回流一体化污水处理装置,旨在改善现有技术中该装置的硝化液和污泥回流量不足,影响其脱氮效果的问题。The purpose of the utility model is to provide a sub-water inlet type air lift and return integrated sewage treatment device, which aims to improve the problem of insufficient nitrification liquid and sludge return flow in the device in the prior art, which affects its denitrification effect.

本实用新型是这样实现的:The utility model is realized in this way:

一种分段进水式气升回流一体化污水处理装置,包括处理箱、进水口和气管,所述处理箱的内部安装有八个挡板,八个所述挡板将处理箱的内部依次分为第一缓冲室、缺氧池a、好氧池a、缺氧池b、好氧池b、缺氧池c、好氧池c、第二缓冲区和二次沉淀池,所述进水口包括第一进水口、第二进水口和第三进水口,所述第一进水口开设在缺氧池a的上端面,所述第二进水口开设在缺氧池b的上端面,所述第三进水口开设在缺氧池c的上端面,所述好氧池a和好氧池b的内部靠近中间的位置安装有第一斜板和第二斜板,所述好氧池c的内部靠近缺氧池c的一侧中部安装有第一斜板,所述第一斜板与第二斜板的下方设置为气室,所述二次沉淀池与第一缓冲室之间连通有回流管,所述气管位于处理箱的一侧下方,所述气管上与好氧池a、好氧池b和好氧池c对应的位置安装有曝气管,且曝气管远离气管的一端插入有好氧池a、好氧池b和好氧池c的内部。A sectional water inlet type air lift and return integrated sewage treatment device, comprising a treatment box, a water inlet and an air pipe, eight baffles are installed inside the treatment box, and the eight baffles divide the inside of the treatment box into The first buffer chamber, anoxic tank a, aerobic tank a, anoxic tank b, aerobic tank b, anoxic tank c, aerobic tank c, second buffer zone and secondary sedimentation tank, the water inlet includes The first water inlet, the second water inlet and the third water inlet, the first water inlet is opened on the upper end surface of the anoxic pool a, the second water inlet is opened on the upper end surface of the anoxic pool b, and the first water inlet is opened on the upper end surface of the anoxic pool b. The three water inlets are opened on the upper end face of the anoxic pool c. The inside of the aerobic pool a and the aerobic pool b are installed with a first inclined plate and a second inclined plate near the middle. The inside of the aerobic pool c A first inclined plate is installed in the middle part of one side near the anoxic tank c, and the bottom of the first inclined plate and the second inclined plate is set as an air chamber, and a backflow is communicated between the secondary sedimentation tank and the first buffer chamber. Pipe, the gas pipe is located under one side of the treatment box, and the aeration pipe is installed at the position corresponding to the aerobic pool a, the aerobic pool b and the aerobic pool c on the gas pipe, and the aeration pipe is inserted away from the end of the gas pipe. There are aerobic pool a, aerobic pool b and aerobic pool c inside.

进一步的,所述第一缓冲室靠近缺氧池a一侧的挡板上靠近上端的位置开设有开口,八个所述挡板上均开设有开口,且八个开口上下交替设置。Further, the baffle plate on the side of the first buffer chamber close to the anoxic tank a is provided with an opening near the upper end, and the eight baffle plates are all provided with openings, and the eight openings are arranged alternately up and down.

进一步的,所述处理箱靠近二次沉淀池的一侧设置为倾斜状态,所述二次沉淀池远离第二缓冲区的一侧靠近上方的位置安装有出水管。Further, the side of the treatment tank close to the secondary sedimentation tank is set in an inclined state, and a water outlet pipe is installed at a position close to the upper side of the secondary sedimentation tank away from the second buffer zone.

进一步的,所述好氧池a与好氧池b内部的第一斜板与第二斜板相对倾斜设置。Further, the first inclined plate and the second inclined plate in the aerobic pool a and the aerobic pool b are arranged relatively inclined.

与现有技术相比,本实用新型的有益效果是:本实用新型分段后,反应器内微生物量呈现梯度递减,不仅有效保持装置内的微生物量,保证该装置的除污效果,而且有效降低沉淀污泥浓度,避免了回流污泥量少导致污泥上浮,保证出水水质。Compared with the prior art, the beneficial effect of the present utility model is: after the utility model is segmented, the microbial biomass in the reactor presents a gradient decrease, which not only effectively maintains the microbial biomass in the device, ensures the decontamination effect of the device, but also effectively Reduce the concentration of sedimented sludge, avoid the sludge floating due to the small amount of returned sludge, and ensure the quality of the effluent.

附图说明Description of drawings

为了更清楚地说明本实用新型实施方式的技术方案,下面将对实施方式中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本实用新型的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to illustrate the technical solutions of the embodiments of the present invention more clearly, the accompanying drawings required in the embodiments will be briefly introduced below. It should be understood that the following drawings only show some embodiments of the present invention. Therefore, it should not be regarded as a limitation of the scope. For those of ordinary skill in the art, other related drawings can also be obtained from these drawings without any creative effort.

图1是本实用新型的整体结构示意图;Fig. 1 is the overall structure schematic diagram of the present utility model;

图2是本实用新型的俯视图。Figure 2 is a plan view of the present invention.

图中:1、处理箱;101、第一缓冲室;102、缺氧池a;103、好氧池a;104、缺氧池b;105、好氧池b;106、缺氧池c;107、好氧池c;108、第二缓冲区;109、二次沉淀池;2、出水管;3、开口;4、进水口;41、第一进水口;42、第二进水口;43、第三进水口;5、曝气管;6、气管;7、挡板;8、气室;9、回流管;10、第一斜板;11、第二斜板。In the figure: 1, treatment box; 101, first buffer chamber; 102, anoxic tank a; 103, aerobic tank a; 104, anoxic tank b; 105, aerobic tank b; 106, anoxic tank c; 107, aerobic tank c; 108, second buffer zone; 109, secondary sedimentation tank; 2, outlet pipe; 3, opening; 4, water inlet; 41, first water inlet; 42, second water inlet; 43 , the third water inlet; 5, aeration pipe; 6, gas pipe; 7, baffle plate; 8, air chamber; 9, return pipe; 10, the first inclined plate; 11, the second inclined plate.

具体实施方式Detailed ways

为使本实用新型实施方式的目的、技术方案和优点更加清楚,下面将结合本实用新型实施方式中的附图,对本实用新型实施方式中的技术方案进行清楚、完整地描述,显然,所描述的实施方式是本实用新型一部分实施方式,而不是全部的实施方式。基于本实用新型中的实施方式,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施方式,都属于本实用新型保护的范围。因此,以下对在附图中提供的本实用新型的实施方式的详细描述并非旨在限制要求保护的本实用新型的范围,而是仅仅表示本实用新型的选定实施方式。基于本实用新型中的实施方式,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施方式,都属于本实用新型保护的范围。In order to make the purposes, technical solutions and advantages of the embodiments of the present invention more clear, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described The embodiments of the present invention are a part of the embodiments of the present invention, but not all of 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. Accordingly, the following detailed description of the embodiments of the invention provided in the accompanying drawings is not intended to limit the scope of the invention as claimed, but is merely representative of selected embodiments of the invention. 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.

参照图1和图2所示,一种分段进水式气升回流一体化污水处理装置,包括处理箱1、进水口4和气管6,处理箱1的内部安装有八个挡板7,挡板7用于将处理箱1隔开,形成不同的腔室,八个挡板7将处理箱1的内部依次分为第一缓冲室101、缺氧池a102、好氧池a103、缺氧池b 104、好氧池b105、缺氧池c106、好氧池c107、第二缓冲区108和二次沉淀池109,第一缓冲室101作为污泥回流点,缺氧池a102、缺氧池b104和缺氧池c106利用厌氧菌的作用,使有机物发生水解、酸化和甲烷化,去除废水中的有机物,并提高污水的可生化性,有利于后续的好氧处理,好氧池a103、好氧池b105和好氧池c107是让活性污泥进行有氧呼吸,进一步把有机物分解成无机物,去除污染物的功能,第一缓冲室101靠近缺氧池a102一侧的挡板7上靠近上端的位置开设有开口3,开口3用于各个腔室的相互连通,八个挡板7上均开设有开口3,且八个开口3上下交替设置,相互连通的通道呈S状;Referring to Figures 1 and 2, a segmented water inlet type air lift and return integrated sewage treatment device includes a treatment box 1, a water inlet 4 and an air pipe 6, and eight baffles 7 are installed inside the treatment box 1. The baffles 7 is used to separate the processing box 1 to form different chambers, and the eight baffles 7 divide the interior of the processing box 1 into a first buffer chamber 101, anoxic pool a102, aerobic pool a103, and anoxic pool b. 104, aerobic tank b105, anoxic tank c106, aerobic tank c107, second buffer chamber 108 and secondary sedimentation tank 109, the first buffer chamber 101 is used as a sludge return point, anoxic tank a102, anoxic tank b104 and Anoxic tank c106 utilizes the action of anaerobic bacteria to hydrolyze, acidify and methanize organic matter, remove organic matter in wastewater, and improve the biodegradability of sewage, which is beneficial to subsequent aerobic treatment. Aerobic tank a103, aerobic Pool b105 and aerobic pool c107 are to allow activated sludge to perform aerobic respiration, further decompose organic matter into inorganic matter, and remove pollutants. The opening 3 is provided at the position of 1, and the opening 3 is used for the interconnection of each chamber. The eight baffles 7 are all provided with openings 3, and the eight openings 3 are alternately arranged up and down, and the interconnected passages are S-shaped;

参照图1所示,处理箱1靠近二次沉淀池109的一侧设置为倾斜状态,倾斜的侧边可使得沉淀时污泥能够沿着倾斜侧壁向下沉淀,二次沉淀池109远离第二缓冲区108的一侧靠近上方的位置安装有出水管2,出水管2用于最终出水;Referring to FIG. 1 , the side of the treatment tank 1 close to the secondary sedimentation tank 109 is set in an inclined state, and the inclined side can make the sludge to settle down along the inclined side wall during precipitation, and the secondary sedimentation tank 109 is far away from the second sedimentation tank. A water outlet pipe 2 is installed near the upper position on one side of the second buffer zone 108, and the water outlet pipe 2 is used for the final water outlet;

参照图1所示,进水口4包括第一进水口41、第二进水口42和第三进水口43,第一进水口41、第二进水口42和第三进水口43用于进水,第一进水口41、第二进水口42进水流量可以灵活分配,比如,冬季为了延长水力停留时间,满足较好的硝化效果,可以适当加大第一进水口41、第二进水口42的进水量,第一进水口41开设在缺氧池a102的上端面,第二进水口42开设在缺氧池b104的上端面,第三进水口43开设在缺氧池c106的上端面,好氧池a103和好氧池b105的内部靠近中间的位置安装有第一斜板10和第二斜板11,好氧池a103与好氧池b105内部的第一斜板10与第二斜板11相对倾斜设置,好氧池c107的内部靠近缺氧池c106的一侧中部安装有第一斜板10,第一斜板10与第二斜板11的下方设置为气室8,第一斜板10与第二斜板11用于形成气室8;1 , the water inlet 4 includes a first water inlet 41, a second water inlet 42 and a third water inlet 43, the first water inlet 41, the second water inlet 42 and the third water inlet 43 are used for water intake, The water inlet flow of the first water inlet 41 and the second water inlet 42 can be distributed flexibly. For example, in order to prolong the hydraulic retention time in winter and meet the better nitrification effect, the first water inlet 41 and the second water inlet 42 can be appropriately increased. In the amount of water, the first water inlet 41 is opened on the upper end face of the anoxic pond a102, the second water inlet 42 is opened on the upper end face of the anoxic pond b104, and the third water inlet 43 is opened on the upper end face of the anoxic pond c106, aerobic A first inclined plate 10 and a second inclined plate 11 are installed in the interior of the pool a103 and the aerobic pool b105 near the middle. The first inclined plate 10 and the second inclined plate 11 in the aerobic pool a103 and the aerobic pool b105 are opposite Inclined arrangement, the inside of the aerobic pool c107 is installed with the first inclined plate 10 in the middle of one side close to the anoxic pool c106, the bottom of the first inclined plate 10 and the second inclined plate 11 is set as the air chamber 8, the first inclined plate 10 And the second inclined plate 11 is used to form the air chamber 8;

继续参照图1所示,二次沉淀池109与第一缓冲室101之间连通有回流管9,回流管9用于污泥回流,气管6位于处理箱1的一侧下方,气管6用于鼓风机鼓入气体,进而使得好氧池内部含氧量增大,气管6上与好氧池a103、好氧池b 105和好氧池c107对应的位置安装有曝气管5,曝气管5用于将气管6内部的气体导入好氧池的内部,且曝气管5远离气管6的一端插入有好氧池a103、好氧池b105和好氧池c107的内部。Continuing to refer to FIG. 1 , a return pipe 9 is communicated between the secondary sedimentation tank 109 and the first buffer chamber 101 , the return pipe 9 is used for sludge return, the gas pipe 6 is located under one side of the treatment box 1 , and the gas pipe 6 is used for The blower blows gas, and then makes the oxygen content inside the aerobic pond to increase, and the position corresponding to the aerobic pond a103, the aerobic pond b 105 and the aerobic pond c107 on the trachea 6 is provided with the aeration pipe 5, and the aeration pipe 5 It is used to introduce the gas inside the air pipe 6 into the inside of the aerobic tank, and the end of the aeration pipe 5 away from the air pipe 6 is inserted into the inside of the aerobic tank a103, the aerobic tank b105 and the aerobic tank c107.

工作原理:在使用本装置时,将污水通过第一进水口41、第二进水口42和第三进水口43进入缺氧池a102、缺氧池b104和缺氧池c106的内部,反应装置前端分变为分段进水,第一进水口41、第二进水口42和第三进水口43的进水流量可以灵活分配,比如,冬季为了延长水力停留时间,满足较好的硝化效果,可以适当加大第一进水口41、第二进水口42的进水量,分段后缺氧池a102、缺氧池b104和缺氧池c106区段可优先利用进水中易降解的有机碳源来反硝化脱氮,分段进水后硝化液和污泥回流量仅需进水流量的50%就可以达到较好的脱氮效果,分段后,反应器内微生物量呈现梯度递减,不仅有效保持装置内的微生物量,保证该装置的除污效果,而且有效降低沉淀污泥浓度,避免了回流污泥量少导致污泥上浮,影响出水水质Working principle: When using this device, the sewage enters the anoxic tank a102, the anoxic tank b104 and the anoxic tank c106 through the first water inlet 41, the second water inlet 42 and the third water inlet 43, and the front end of the reaction device. The water intake is divided into sections, and the influent flow of the first water inlet 41, the second water inlet 42 and the third water inlet 43 can be flexibly distributed. The inflow volume of the first water inlet 41 and the second water inlet 42 is large, and the sections of the anoxic tank a102, the anoxic tank b104 and the anoxic tank c106 can preferentially utilize the easily degradable organic carbon source in the influent water for denitrification. For denitrification, the return flow of nitrification solution and sludge only needs to be 50% of the influent flow rate after the staged water inflow to achieve a good denitrification effect. The microbial biomass ensures the decontamination effect of the device, and effectively reduces the concentration of sedimented sludge, avoiding the floating of sludge caused by the small amount of returned sludge, which affects the quality of effluent.

气管6的一端应当连接鼓风机,鼓风机鼓风,空气经过气管6进入曝气管5的内部,最后进入好氧池a103、好氧池b105和好氧池c107的内部。One end of the air pipe 6 should be connected to a blower, the blower blows air, and the air enters the inside of the aeration pipe 5 through the air pipe 6, and finally enters the inside of the aerobic pool a103, the aerobic pool b105 and the aerobic pool c107.

以上所述仅为本实用新型的优选实施方式而已,并不用于限制本实用新型,对于本领域的技术人员来说,本实用新型可以有各种更改和变化。凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.

Claims (4)

1. The utility model provides a formula air-lift backward flow integration sewage treatment plant is intake in segmentation, is including handling case (1), water inlet (4) and trachea (6), its characterized in that: the treatment box comprises a treatment box body (1), wherein eight baffle plates (7) are arranged in the treatment box body (1), the eight baffle plates (7) divide the interior of the treatment box body (1) into a first buffer chamber (101), an anoxic tank a (102), an aerobic tank a (103), an anoxic tank b (104), an aerobic tank b (105), an anoxic tank c (106), an aerobic tank c (107), a second buffer zone (108) and a secondary sedimentation tank (109) in sequence, a water inlet (4) comprises a first water inlet (41), a second water inlet (42) and a third water inlet (43), the first water inlet (41) is formed in the upper end face of the anoxic tank a (102), the second water inlet (42) is formed in the upper end face of the anoxic tank b (104), the third water inlet (43) is formed in the upper end face of the anoxic tank c (106), a first inclined plate (10) and a second inclined plate (11) are arranged in positions, close to the middle, in the interiors of the aerobic tank a (103) and the aerobic tank b (105), the inside of aerobic tank c (107) is close to one side mid-mounting of oxygen deficiency pond c (106) has first swash plate (10), the below of first swash plate (10) and second swash plate (11) sets up to air chamber (8), it has back flow pipe (9) to communicate between secondary sedimentation tank (109) and first surge chamber (101), trachea (6) are located the one side below of handling case (1), aeration pipe (5) are installed with the position that aerobic tank a (103), aerobic tank b (105) and aerobic tank c (107) correspond on trachea (6), and aeration pipe (5) keep away from the inside that trachea (6) were inserted aerobic tank a (103), aerobic tank b (105) and aerobic tank c (107).
2. The sectional water inlet type air-lift backflow integrated sewage treatment device according to claim 1, wherein the baffle (7) on one side of the first buffer chamber (101) close to the anoxic tank a (102) is provided with an opening (3) at a position close to the upper end, eight baffles (7) are provided with openings (3), and the eight openings (3) are alternately arranged up and down.
3. The device for treating sewage through integration of air lift and reflux with sectional water inlet type according to claim 1, wherein one side of the treatment tank (1) close to the secondary sedimentation tank (109) is arranged in an inclined state, and a water outlet pipe (2) is arranged at a position close to the upper part of one side of the secondary sedimentation tank (109) far away from the second buffer zone (108).
4. The sewage treatment device integrating the sectional water inlet type air-lift backflow as claimed in claim 1, wherein the first inclined plate (10) and the second inclined plate (11) inside the aerobic tank a (103) and the aerobic tank b (105) are arranged in an inclined manner.
CN201920405123.1U 2019-03-28 2019-03-28 A sectional water inlet type air lift and return integrated sewage treatment device Expired - Fee Related CN210012657U (en)

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CN201920405123.1U CN210012657U (en) 2019-03-28 2019-03-28 A sectional water inlet type air lift and return integrated sewage treatment device

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Application Number Priority Date Filing Date Title
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112209582A (en) * 2020-11-11 2021-01-12 宜宾学院 Device for realizing gas-liquid-solid three-phase separation in sewage treatment and application method thereof
CN115385437A (en) * 2022-08-12 2022-11-25 福建省闽环智能科技有限公司 Composite water treatment equipment
CN119528341A (en) * 2025-01-22 2025-02-28 中建环能科技股份有限公司 Integrated biochemical precipitation reactor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112209582A (en) * 2020-11-11 2021-01-12 宜宾学院 Device for realizing gas-liquid-solid three-phase separation in sewage treatment and application method thereof
CN115385437A (en) * 2022-08-12 2022-11-25 福建省闽环智能科技有限公司 Composite water treatment equipment
CN115385437B (en) * 2022-08-12 2023-09-12 福建省闽环智能科技有限公司 Composite water treatment equipment
CN119528341A (en) * 2025-01-22 2025-02-28 中建环能科技股份有限公司 Integrated biochemical precipitation reactor

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