[go: up one dir, main page]

CN205473193U - Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed - Google Patents

Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed Download PDF

Info

Publication number
CN205473193U
CN205473193U CN201620026325.1U CN201620026325U CN205473193U CN 205473193 U CN205473193 U CN 205473193U CN 201620026325 U CN201620026325 U CN 201620026325U CN 205473193 U CN205473193 U CN 205473193U
Authority
CN
China
Prior art keywords
pool
tank
aerobic
pipe
anoxic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn - After Issue
Application number
CN201620026325.1U
Other languages
Chinese (zh)
Inventor
陈盈楠
梁志伟
王存豹
何李宜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hangzhou Mutual Inductance Information Technology Co ltd
Original Assignee
Hangzhou Mutual Inductance Information Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hangzhou Mutual Inductance Information Technology Co ltd filed Critical Hangzhou Mutual Inductance Information Technology Co ltd
Priority to CN201620026325.1U priority Critical patent/CN205473193U/en
Application granted granted Critical
Publication of CN205473193U publication Critical patent/CN205473193U/en
Withdrawn - After Issue legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

本实用新型公开了一种结构填料强化的农村生活与餐饮废水处理装置。该装置包括依次连接的除油池、厌氧池、缺氧池、好氧池、好氧回流池和沉淀池,所述除油池上设置有进水口,除油池内设有悬浮吸油填料;所述厌氧池、缺氧池、好氧池内分别设有生物填料;在除油池和厌氧池之间以及缺氧池和好氧池之间均设有导流管;其中好氧回流池中的曝气支管上设有曝气头,曝气头上方设置扬水管,扬水管管体侧壁通过回流管与缺氧池相连,通过气提回流方式实现污水回流;本实用新型在总体布局上采用一体化的处理工艺,具有施工简单、投资省的优点,同时又具有较高的处理能力,可以实现75%以上的总氮,65%以上的总磷去除和90%以上的COD降解,非常适合农村生活污水的分散处理。

The utility model discloses a rural life and catering waste water treatment device reinforced by structural packing. The device includes a degreasing tank, an anaerobic tank, anoxic tank, an aerobic tank, an aerobic reflux tank and a sedimentation tank connected in sequence, the degreasing tank is provided with a water inlet, and a suspended oil-absorbing filler is arranged in the degreasing tank; The above-mentioned anaerobic pool, anoxic pool, and aerobic pool are respectively provided with biological fillers; diversion pipes are arranged between the degreasing pool and the anaerobic pool, and between the anoxic pool and the aerobic pool; wherein the aerobic return pool An aeration head is provided on the aeration branch pipe, and a water raising pipe is arranged above the aeration head, and the side wall of the water raising pipe body is connected with the anoxic pool through a return pipe, and the sewage backflow is realized through the air lift backflow method; the utility model adopts the The integrated treatment process has the advantages of simple construction and low investment. At the same time, it has a high treatment capacity, which can achieve more than 75% of total nitrogen, more than 65% of total phosphorus removal and more than 90% of COD degradation. It is very suitable for Decentralized treatment of rural domestic sewage.

Description

一种结构填料强化的农村生活与餐饮废水处理装置A rural life and catering wastewater treatment device strengthened by structural packing

技术领域 technical field

本实用新型涉及一种污水处理设备,具体为一种结构填料强化的农村生活与餐饮废水处理装置。 The utility model relates to a sewage treatment device, in particular to a rural life and catering waste water treatment device reinforced by structural fillers.

背景技术 Background technique

近年来,随着我国农村地区经济和居民生活水平的飞速提升,农村污水排放量不断增加,多数农村地区一般远离城市排污城市管网,排出的污水经化粪池处理后直接排入临近水体严重污染了水环境,尤其氮磷污染严重造成水体富营养化。 In recent years, with the rapid improvement of the economy and residents' living standards in rural areas of our country, the discharge of rural sewage has continued to increase. Most rural areas are generally far away from urban sewage pipe networks, and the discharged sewage is directly discharged into adjacent water bodies after being treated in septic tanks. The water environment has been polluted, especially nitrogen and phosphorus pollution has seriously caused eutrophication of the water body.

目前,农村生活污水处理技术有:土地处理系统、人工湿地污水处理系统、生物接触氧化槽、生态塘污水处理系统、土壤渗滤污水处理系统等技术,存在占地面积大、维护不方便、冬季运行效果差等问题,严重影响了农村环境整治效果。 At present, rural domestic sewage treatment technologies include: land treatment system, artificial wetland sewage treatment system, biological contact oxidation tank, ecological pond sewage treatment system, soil infiltration sewage treatment system and other technologies, which have the disadvantages of large area occupation, inconvenient maintenance, and winter Problems such as poor operation effect have seriously affected the effect of rural environmental improvement.

现有的农村生活污水处理技术中,一体化污水处理装置存在占地面积小、自动化程度较高、管理方便、工期较短等优点,但目前该技术也存在许多问题。主要问题为由于设置除油池后会影响后续的碳氮比从而影响去除效果,使得一体化装置中没有针对农村生活污水中油污较多的特点而专门设置除油池,COD去除效果不理想;而且生物处理效率较低,尤其表现为氮磷去除率很低,而氮磷污染是导致水体富营养化的主要原因。 Among the existing rural domestic sewage treatment technologies, the integrated sewage treatment device has the advantages of small footprint, high degree of automation, convenient management, and short construction period, but there are still many problems in this technology at present. The main problem is that the installation of the degreasing tank will affect the subsequent carbon-nitrogen ratio and thus affect the removal effect, so that the integrated device does not have a special degreasing tank for the characteristics of more oil pollution in rural domestic sewage, and the COD removal effect is not ideal; Moreover, the efficiency of biological treatment is low, especially the removal rate of nitrogen and phosphorus is very low, and nitrogen and phosphorus pollution is the main cause of water eutrophication.

发明内容 Contents of the invention

本实用新型的目的就在于为了解决上述问题而提供一种结构填料强化的农村生活与餐饮废水处理装置。具体技术方案如下: The purpose of this utility model is to provide a rural life and catering wastewater treatment device reinforced by structural fillers in order to solve the above problems. The specific technical scheme is as follows:

一种结构填料强化的农村生活与餐饮废水处理装置,包括依次连接的除油 池、厌氧池、缺氧池、好氧池、好氧回流池和沉淀池,所述除油池上设置有进水口,除油池内设有悬浮吸油填料;所述厌氧池、缺氧池、好氧池内分别设有生物填料;在除油池和厌氧池之间以及缺氧池和好氧池之间均设有导流管,所述好氧池和好氧回流池中均设有曝气主管和曝气支管,其中好氧回流池中的曝气支管上设有曝气头,曝气头上方设置扬水管,扬水管管体侧壁通过回流管与缺氧池相连,通过气提回流方式实现污水回流;好氧池和好氧回流池顶部设有出气口;在沉淀池右上方连接一个出水口。 A rural life and catering wastewater treatment device reinforced by structural fillers, including a degreasing pond, anaerobic pond, anoxic pond, aerobic pond, aerobic reflux pond and sedimentation pond connected in sequence, and the degreasing pond is provided with an advanced Suspended oil-absorbing fillers are provided in the degreasing pool; biological fillers are respectively provided in the anaerobic pool, anoxic pool, and aerobic pool; There is a diversion pipe, and the aerobic tank and the aerobic return tank are equipped with an aeration main pipe and an aeration branch pipe, wherein the aeration branch pipe in the aerobic return tank is provided with an aeration head, and the aeration head is installed above the aeration head. The side wall of the water pipe and the lifting pipe body is connected to the anoxic tank through the return pipe, and the sewage backflow is realized by air lift and backflow; there is an air outlet on the top of the aerobic tank and the aerobic return tank; a water outlet is connected to the upper right of the sedimentation tank.

作为优选,所述的扬水管底部通过扩张口罩于曝气头上方;好氧回流池和沉淀池之间通过上部进水,但两个池体之间的隔板下部悬空使两者底部连通,沉淀池底部设置斜板,且斜板最低位置处于隔板下部悬空处附近,使沉淀的污泥通过隔板下部进入扬水管底部扩张口,使得部分污泥在不另外设置污泥回流管和污泥回流泵的情况下,通气提回流的方式经由扬水管和回流管回流到缺氧池中,既既避免回流泵从而节约了能源,又强化脱氮除磷处理效果增大装置污水处理效率。 As a preference, the bottom of the lifting pipe is above the aeration head through the expansion mask; the aerobic reflux tank and the sedimentation tank are fed through the upper part, but the lower part of the partition between the two tanks is suspended so that the bottom of the two is connected, and the sedimentation A sloping plate is set at the bottom of the tank, and the lowest position of the sloping plate is near the suspended part of the lower part of the partition, so that the settled sludge enters the expansion port at the bottom of the lifting pipe through the lower part of the partition, so that part of the sludge can be separated without additional sludge return pipes and sludge In the case of the reflux pump, the method of ventilation and reflux returns to the anoxic tank through the water pipe and the return pipe, which not only avoids the reflux pump and saves energy, but also strengthens the effect of nitrogen and phosphorus removal and increases the sewage treatment efficiency of the device.

作为优选,所述的厌氧池、缺氧池、好氧池中的生物填料分别为竹制填料、聚氨酯类填料和发泡玻璃。竹制填料为竹球形状,易于生物挂膜,能较好的去除水中的有机物和部分氮磷且利于聚磷菌释磷;发泡玻璃具有孔隙率大,不易结团等优点,能较好的吸附氮磷。在竹制填料、聚氨酯类填料和发泡玻璃三种填料存在协同作用效应,可大大提高COD和氮磷的去除率。 As a preference, the biological fillers in the anaerobic tank, anoxic tank and aerobic tank are bamboo fillers, polyurethane fillers and foamed glass respectively. The bamboo filler is in the shape of a bamboo ball, which is easy to form a biofilm, and can better remove organic matter and some nitrogen and phosphorus in the water, and is conducive to the release of phosphorus by phosphorus-accumulating bacteria. adsorption of nitrogen and phosphorus. There is a synergistic effect among the three fillers of bamboo filler, polyurethane filler and foamed glass, which can greatly improve the removal rate of COD and nitrogen and phosphorus.

作为优选,所述的悬浮吸油填料为发泡玻璃和复合微生物菌剂的组合填料。悬浮吸油填料可将油脂类大分子有机物降解为小分子有机物,既不影响后续的碳氮比,又减轻了减轻后续环节污染物负荷。 Preferably, the suspended oil-absorbing filler is a combined filler of foamed glass and composite microbial agent. Suspended oil-absorbing fillers can degrade oily macromolecular organic matter into small molecular organic matter, which does not affect the subsequent carbon-nitrogen ratio and reduces the pollutant load in subsequent links.

将发泡玻璃作为载体,放入含有复合微生物菌剂的培养液中进行挂膜,从而得到所述的组合填料。现有的农村生活与餐饮废水主要问题为由于设置除油池后会影响后续的碳氮比从而影响去除效果,使得一体化装置中没有针对农村生 活污水中油污较多的特点而专门设置除油池,COD去除效果不理想;而且生物处理效率较低,尤其表现为氮磷去除率很低,而氮磷污染是导致水体富营养化的主要原因。但本实用新型中的除油池并不是直接将油脂去除,而是利用悬浮吸油填料中附着的复合微生物菌剂的协同效应,将大量油脂类有机物大分子降解为小分子有机物。因此,经过该处理后,可以在不影响后续的碳氮比的前提下减轻后续环节污染物负荷,提高可降解性。 The foamed glass is used as a carrier, which is put into the culture solution containing the composite microbial agent for film formation, so as to obtain the combined filler. The main problem of the existing rural domestic and catering wastewater is that the installation of the degreasing tank will affect the subsequent carbon-nitrogen ratio and thus affect the removal effect, so that there is no special degreasing in the integrated device for the characteristics of more oil pollution in rural domestic sewage The removal effect of COD is not ideal; and the efficiency of biological treatment is low, especially the removal rate of nitrogen and phosphorus is very low, and nitrogen and phosphorus pollution is the main cause of water eutrophication. However, the degreasing tank in the utility model does not directly remove the grease, but uses the synergistic effect of the composite microbial agent attached to the suspended oil-absorbing filler to degrade a large amount of oily organic macromolecules into small molecular organic matter. Therefore, after this treatment, the pollutant load in subsequent links can be reduced without affecting the subsequent carbon-nitrogen ratio, and the degradability can be improved.

本实用新型在总体布局上采用一体化的处理工艺,具有施工简单、投资省的优点,同时又具有较高的处理能力,可以实现75%以上的总氮,65%以上的总磷去除和90%以上的COD降解。该系统在处理过程中通过气提回流方式实现泥水回流,避免了设置回流管和回流泵,使得该系统仅需要提供微动力,具有处理及运行成本低,运行操作简单方便等优点,非常适合农村生活污水的分散处理。 The utility model adopts an integrated treatment process in the overall layout, which has the advantages of simple construction and low investment, and at the same time has a high treatment capacity, which can realize more than 75% of total nitrogen, more than 65% of total phosphorus removal and 90% More than % COD degradation. During the treatment process, the system realizes the return of muddy water through air lift and return flow, avoiding the need to set return pipes and return pumps, so that the system only needs to provide micro power, has the advantages of low processing and operation costs, simple and convenient operation, etc., and is very suitable for rural areas Decentralized treatment of domestic sewage.

附图说明 Description of drawings

图1是一种结构填料强化的农村生活与餐饮废水处理装置的结构示意图; Fig. 1 is a structural schematic diagram of a rural life and catering wastewater treatment device reinforced by structural packing;

图2是本实用新型的曝气主管和曝气支管连接示意图。 Fig. 2 is a schematic diagram of the connection between the aeration main pipe and the aeration branch pipe of the utility model.

具体实施方式 detailed description

下面结合附图对本实用新型作进一步说明: Below in conjunction with accompanying drawing, the utility model is further described:

如图1所示,一种结构填料强化的农村生活与餐饮废水处理装置,包括依次连接的除油池3、厌氧池4、缺氧池6、好氧池7、好氧回流池8和沉淀池9,所述除油池上设置有进水口1,除油池3内设有悬浮吸油填料2;所述厌氧池4、缺氧池6、好氧池7内分别设有生物填料5;在除油池3和厌氧池4之间以及缺氧池6和好氧池7之间均设有导流管17,所述好氧池7和好氧回流池8中均设有连通的曝气主管12和曝气支管16,其中好氧回流池8中的曝气支管16上设有曝气头10,曝气头10上方设置扬水管11,扬水管11管体侧壁通过回流管13与缺氧池6相连,通过气提回流方式实现污水回流;好氧池7和好氧回流池8顶部设有出气口18;在沉淀池9右上方连接一个出水口14。 As shown in Figure 1, a rural life and catering wastewater treatment device strengthened by structural packing includes degreasing pool 3, anaerobic pool 4, anoxic pool 6, aerobic pool 7, aerobic return pool 8 and A sedimentation tank 9, the degreasing tank is provided with a water inlet 1, and the degreasing tank 3 is provided with a suspended oil-absorbing filler 2; the anaerobic tank 4, the anoxic tank 6, and the aerobic tank 7 are respectively provided with biological fillers 5 ; Between the degreasing pool 3 and the anaerobic pool 4 and between the anoxic pool 6 and the aerobic pool 7, a guide tube 17 is provided, and the aerobic pool 7 and the aerobic return pool 8 are all provided with a communication The aeration main pipe 12 and the aeration branch pipe 16, wherein the aeration branch pipe 16 in the aerobic reflux tank 8 is provided with an aeration head 10, and the aeration pipe 11 is arranged above the aeration head 10, and the side wall of the pipe body of the aeration pipe 11 passes through the backflow The pipe 13 is connected with the anoxic tank 6, and the sewage reflux is realized by air lift and reflux; the top of the aerobic tank 7 and the aerobic reflux tank 8 is provided with an air outlet 18;

扬水管11底部通过扩张口罩于曝气头10上方;好氧回流池8和沉淀池9之间通过上部进水,但两个池体之间的隔板15下部悬空使两者底部连通,沉淀池9底部设置斜板,且斜板最低位置处于隔板15下部悬空处附近,使沉淀的污泥通过隔板15下部进入扬水管11底部扩张口。 The bottom of the water raising pipe 11 is above the aeration head 10 through the expansion mask; the water enters between the aerobic reflux tank 8 and the sedimentation tank 9 through the upper part, but the lower part of the partition plate 15 between the two tanks is suspended to make the bottom of the two connected, and the sedimentation A sloping plate is arranged at the bottom of the pool 9, and the lowest position of the sloping plate is near the suspended part of the lower part of the dividing plate 15, so that the settled sludge enters the expansion port at the bottom of the lifting pipe 11 through the lower part of the dividing plate 15.

厌氧池4、缺氧池6、好氧池7中的生物填料5分别为竹制填料、聚氨酯类填料和发泡玻璃。其中发泡玻璃的制备方法为:将粉体配合料的各原料均匀混合后得到粉体配合料;将配合料装入模具中,按照以下烧制温度烧成:以10-15℃/min的升温速率升温至400-500℃,保温20-30min;再以10-15℃/min的升温速率升温至1000-1100℃,保温10-20min;然后以20-25℃/min的降温速率降温至850-900℃,最后自然冷却到常温,得到该水处理悬浮式填料,即发泡玻璃。 The biological fillers 5 in the anaerobic tank 4, the anoxic tank 6 and the aerobic tank 7 are bamboo fillers, polyurethane fillers and foamed glass respectively. The preparation method of the foamed glass is as follows: uniformly mix the raw materials of the powder batch to obtain the powder batch; put the batch into the mold, and fire according to the following firing temperature: at 10-15°C/min The heating rate is raised to 400-500°C, and the temperature is kept for 20-30min; then the temperature is raised to 1000-1100°C at a heating rate of 10-15°C/min, and the temperature is kept for 10-20min; then the temperature is lowered to 20-25°C/min 850-900°C, and finally cooled naturally to normal temperature to obtain the water-treated suspended filler, that is, foamed glass.

其中粉体配合料的各原料成分及质量份数分为两种方案: Among them, the raw material components and mass parts of powder batch materials are divided into two schemes:

方案一: Option One:

玻璃粉末:16-20份; Glass powder: 16-20 parts;

大理石粉末:1-3份; Marble powder: 1-3 parts;

方案二: Option II:

玻璃粉末:16-20份; Glass powder: 16-20 parts;

大理石粉末:1-3份; Marble powder: 1-3 parts;

沸石粉末:2-4份; Zeolite powder: 2-4 parts;

其中玻璃粉末、大理石粉末和沸石粉末均为200目以上的粉末。 Among them, glass powder, marble powder and zeolite powder are all powders with a mesh size of 200 or more.

悬浮吸油填料2为上述发泡玻璃和复合微生物菌剂的组合填料。所述的复合微生物菌剂是由体积百分比:10%~30%的洋葱假单胞菌、10%~30%的微球菌、10%~20%的地衣芽孢杆菌、10%~20%的解淀粉芽孢杆菌、10%~20%的扩张青霉菌、10%~20%的解脂亚罗酵母复配组成复合微生物菌剂。组合填料的制备方法为:将发泡玻璃作为载体,放入含有复合微生物菌剂的培养液中进行挂膜, 从而得到所述的组合填料。 Suspended oil-absorbing filler 2 is a combined filler of the above-mentioned foamed glass and composite microbial agent. The composite microbial bacterial agent is composed of 10% to 30% of Pseudomonas cepacia, 10% to 30% of Micrococcus, 10% to 20% of Bacillus licheniformis, 10% to 20% of Amylobacter bacillus, 10% to 20% of Penicillium expansica, and 10% to 20% of Yarrowia lipolytica are compounded to form a compound microbial bacterial agent. The preparation method of the composite filler is as follows: the foamed glass is used as a carrier, put into a culture solution containing a composite microbial agent for film formation, so as to obtain the composite filler.

一种利用所述装置的农村生活与餐饮废水处理工艺,步骤如下: A process for treating rural life and catering wastewater using the device, the steps are as follows:

1)农村生活污水通过自然流方式进入一体化装置,首先通过进水口1从上端进入除油池3,水力停留时间约为3~5h,在悬浮吸油填料2中附着的复合微生物菌剂作用下将大量油脂类有机物大分子降解为小分子有机物,在不影响后续的碳氮比的前提下减轻后续环节污染物负荷; 1) Rural domestic sewage enters the integrated device through natural flow, and first enters the degreasing pool 3 from the upper end through the water inlet 1, and the hydraulic retention time is about 3 to 5 hours. Degrade a large amount of oily organic macromolecules into small molecular organics, and reduce the pollutant load in subsequent links without affecting the subsequent carbon-to-nitrogen ratio;

2)处理后的废水通过坡度约为60度的斜向导流管17进入厌氧池4,水力停留时间为1~3h,期间利用厌氧池4中设置的挂有厌氧微生物膜的竹制填料,去除水中的有机物和部分氮磷且利于聚磷菌释磷;之后污水从厌氧池4下端进入缺氧池6,水力停留时间约为2~5h,在缺氧池6中对污水中有机物进行进一步去除的同时实现脱氮;缺氧池6的出水从下端流入好氧池7,水力停留时间约为6~10h,好氧池7中设置发泡玻璃,能进一步吸附氮磷;之后污水进入好氧回流池8,硝化反应后的污水和污泥在曝气下通过气提回流方式进入扬水管11和回流管13回流至缺氧池6中进行反硝化反应,曝气量为1.2L/min,设计回流比为2.5:1; 2) The treated wastewater enters the anaerobic pool 4 through the inclined guide pipe 17 with a slope of about 60 degrees, and the hydraulic retention time is 1 to 3 hours. Filler, removes organic matter and part of nitrogen and phosphorus in water and is conducive to the release of phosphorus by phosphorus-accumulating bacteria; then the sewage enters the anoxic pool 6 from the lower end of the anaerobic pool 4, and the hydraulic retention time is about 2 to 5 hours. The organic matter is further removed while denitrification is realized; the effluent from the anoxic pool 6 flows into the aerobic pool 7 from the lower end, and the hydraulic retention time is about 6-10 hours. The aerobic pool 7 is equipped with foam glass, which can further absorb nitrogen and phosphorus; The sewage enters the aerobic reflux tank 8, and the sewage and sludge after the nitrification reaction enter the water lift pipe 11 and the reflux pipe 13 under aeration to return to the anoxic pool 6 for denitrification reaction, and the aeration rate is 1.2 L/min, the design reflux ratio is 2.5:1;

3)最终处理后的污水从上端进入沉淀池9,水力停留时间约为2~5h,沉淀的污泥通过隔板15下部进入扬水管11底部扩张口,在曝气下通过气提回流方式进入扬水管11和回流管13回流至缺氧池6中,实现污泥回流;沉淀后的上清液则从出水口14排出。 3) The final treated sewage enters the sedimentation tank 9 from the upper end, and the hydraulic retention time is about 2 to 5 hours. The settled sludge enters the expansion port at the bottom of the lifting pipe 11 through the lower part of the partition plate 15, and enters by means of air lift and reflux under aeration. The pumping pipe 11 and the return pipe 13 return to the anoxic tank 6 to realize the return of the sludge; the supernatant after sedimentation is discharged from the water outlet 14 .

实施例 Example

本实施例中,结构填料强化的农村生活与餐饮废水处理装置采用如图1~2所示的装置,包括依次连接的除油池3、厌氧池4、缺氧池6、好氧池7、好氧回流池8、和沉淀池9,设计日处理废水4t,满足12-15户农村家庭生活污水处理,总水力停留时间HRT为14~28h。其中总装置长2m,宽1m,高1.05m,除油池3、厌氧池4、缺氧池6、好氧池7、沉淀池9水力停留时间HRT分别为3~5h、 1~3h、2~5h、6~10h、2~5h;所述除油池3上设置有与污水源连接的进水口1,进水口1为直径5cm的圆管;除油池3内设有悬浮吸油填料2,该填料为发泡玻璃和复合微生物菌剂的组合填料。扬水管11直径8cm,埋深80cm,设计提升高度5cm,曝气量1.2L/min,设计回流比约为2.5:1。沉淀池9底部设计为30度坡度,沉淀的污泥一部分可以回流至缺氧池6内;在沉淀池9右上方连接一个直径5cm的出水口14。 In this embodiment, the rural life and catering wastewater treatment device strengthened by structural packing adopts the device shown in Figures 1-2, including degreasing pool 3, anaerobic pool 4, anoxic pool 6, and aerobic pool 7 connected in sequence , aerobic reflux tank 8, and sedimentation tank 9 are designed to treat 4t of wastewater per day, which can meet the domestic sewage treatment of 12-15 rural households, and the total hydraulic retention time HRT is 14-28h. Among them, the total device is 2m long, 1m wide, and 1.05m high. The hydraulic retention time HRT of oil removal pool 3, anaerobic pool 4, anoxic pool 6, aerobic pool 7, and sedimentation pool 9 are 3~5h, 1~3h, respectively. 2~5h, 6~10h, 2~5h; the degreasing tank 3 is provided with a water inlet 1 connected to the sewage source, and the water inlet 1 is a circular pipe with a diameter of 5cm; the degreasing tank 3 is provided with a suspended oil-absorbing filler 2. The filler is a combined filler of foamed glass and composite microbial agent. The lift pipe 11 has a diameter of 8cm, a buried depth of 80cm, a design lifting height of 5cm, an aeration rate of 1.2L/min, and a design reflux ratio of about 2.5:1. The bottom of the sedimentation tank 9 is designed with a slope of 30 degrees, and part of the settled sludge can flow back into the anoxic tank 6; a water outlet 14 with a diameter of 5 cm is connected to the upper right of the sedimentation tank 9 .

农村生活污水通过自然流方式进入一体化装置,首先通过进水口1从上端进入除油池3,在悬浮吸油填料2的帮助下将大量油脂类有机物大分子降解为小分子有机物,既不影响后续的碳氮比,又减轻后续环节污染物负荷;然后处理后的废水通过坡度约为60度的斜向导流管17进入厌氧池4,厌氧池4中设置竹制填料,竹制填料上挂有厌氧微生物膜,能较好的去除水中的有机物和部分氮磷且利于聚磷菌释磷;之后污水从下端进入缺氧池6与气提回流污水混合,缺氧池6中添加活性污泥和生物填料,实现反硝化反应;缺氧池6的出水从下端流入好氧池7进行有机物的降解和硝化反应,好氧池7中添加好氧活性污泥和生物填料,实现接触氧化;之后污水进入好氧回流池8将硝化后的污水和部分污泥在曝气下进入扬水管11通过气提回流的方式回流至缺氧池6进行反硝化反应,使得回流污水与气体进行更好的分离;最终处理后的污水通过沉淀池9沉淀后从出水口14排出,可以实现75%的总氮、65%的总磷去除和90%的COD降解。 Rural domestic sewage enters the integrated device through natural flow, and first enters the oil removal tank 3 from the upper end through the water inlet 1. With the help of the suspended oil-absorbing filler 2, a large amount of oily organic matter is degraded into small molecular organic matter, which does not affect the subsequent carbon-to-nitrogen ratio, and reduce the subsequent link pollutant load; then the treated waste water enters the anaerobic tank 4 through the inclined guide pipe 17 with a slope of about 60 degrees, and the bamboo filler is set in the anaerobic tank 4, and the bamboo filler An anaerobic microbial film is hung, which can better remove organic matter and part of nitrogen and phosphorus in the water and is conducive to the release of phosphorus by phosphorus-accumulating bacteria; then the sewage enters the anoxic pool 6 from the lower end to mix with the backflow sewage of the gas strip, and the anoxic pool 6 is added with active Sludge and biological filler to realize denitrification reaction; the effluent from the anoxic tank 6 flows from the lower end into the aerobic tank 7 for degradation and nitrification of organic matter, and aerobic activated sludge and biological filler are added to the aerobic tank 7 to realize contact oxidation Afterwards, the sewage enters the aerobic reflux pool 8, and the nitrified sewage and part of the sludge enter the water lift pipe 11 under aeration and return to the anoxic pool 6 for denitrification reaction, so that the reflux sewage and gas are more Good separation; the final treated sewage is settled through the sedimentation tank 9 and then discharged from the water outlet 14, which can achieve 75% of total nitrogen, 65% of total phosphorus removal and 90% of COD degradation.

以上所述,仅是本实用新型较佳实例,并非对本实用新型的技术范围作任何限制,故凡是根据本实用新型的技术实质对以上实施例所作的任何细微修改,等同变化与修改,均任属于本实用新型技术方案的范围内。 The above is only a preferred example of the utility model, and does not limit the technical scope of the utility model in any way, so any minor modifications made to the above embodiments according to the technical essence of the utility model, equivalent changes and modifications, are all acceptable. It belongs to the scope of the technical solution of the utility model.

Claims (4)

1.一种结构填料强化的农村生活与餐饮废水处理装置,其特征在于:包括依次连接的除油池(3)、厌氧池(4)、缺氧池(6)、好氧池(7)、好氧回流池(8)和沉淀池(9),所述除油池上设置有进水口(1),除油池(3)内设有悬浮吸油填料(2);所述厌氧池(4)、缺氧池(6)、好氧池(7)内分别设有生物填料(5);在除油池(3)和厌氧池(4)之间以及缺氧池(6)和好氧池(7)之间均设有导流管(17),所述好氧池(7)和好氧回流池(8)中均设有曝气主管(12)和曝气支管(16),其中好氧回流池(8)中的曝气支管(16)上设有曝气头(10),曝气头(10)上方设置扬水管(11),扬水管(11)管体侧壁通过回流管(13)与缺氧池(6)相连,通过气提回流方式实现污水回流;好氧池(7)和好氧回流池(8)顶部设有出气口(18);在沉淀池(9)右上方连接一个出水口(14)。1. A rural living and catering waste water treatment device reinforced by structural packing, characterized in that: it comprises degreasing pond (3), anaerobic pond (4), anoxic pond (6), aerobic pond (7) connected successively ), an aerobic reflux tank (8) and a sedimentation tank (9), the degreasing tank is provided with a water inlet (1), and the degreasing tank (3) is provided with a suspended oil-absorbing filler (2); the anaerobic tank (4), the anoxic pool (6), and the aerobic pool (7) are respectively provided with biological fillers (5); between the degreasing pool (3) and the anaerobic pool (4) and the anoxic pool (6) A draft pipe (17) is provided between the aerobic pool (7) and an aeration main pipe (12) and an aeration branch pipe ( 16), wherein the aeration branch pipe (16) in the aerobic reflux tank (8) is provided with an aeration head (10), the aeration head (10) is provided with a water lift pipe (11), and the water lift pipe (11) body The side wall is connected to the anoxic pool (6) through the return pipe (13), and the sewage backflow is realized by the air lift backflow method; the top of the aerobic pool (7) and the aerobic backflow pool (8) is provided with an air outlet (18); A water outlet (14) is connected to the top right of the settling tank (9). 2.根据权利要求1所述结构填料强化的农村生活与餐饮废水处理装置,其特征在于:所述的扬水管(11)底部通过扩张口罩于曝气头(10)上方;好氧回流池(8)和沉淀池(9)之间通过上部进水,但两个池体之间的隔板(15)下部悬空使两者底部连通,沉淀池(9)底部设置斜板,且斜板最低位置处于隔板(15)下部悬空处附近,使沉淀的污泥通过隔板(15)下部进入扬水管(11)底部扩张口。2. according to claim 1, the rural life and catering waste water treatment device strengthened by structural packing, is characterized in that: the bottom of the described lifting pipe (11) is above the aeration head (10) through the expansion mask; the aerobic backflow pool ( 8) and the sedimentation tank (9) enter water through the upper part, but the lower part of the partition (15) between the two tanks is suspended to connect the bottom of the two, and the bottom of the sedimentation tank (9) is equipped with a sloping plate, and the sloping plate is the lowest The position is near the suspended part of the lower part of the dividing plate (15), so that the settled sludge enters the expansion port at the bottom of the lifting pipe (11) through the lower part of the dividing plate (15). 3.根据权利要求1所述结构填料强化的农村生活与餐饮废水处理装置,其特征在于:所述的厌氧池(4)、缺氧池(6)、好氧池(7)中的生物填料(5)分别为竹制填料、聚氨酯类填料和发泡玻璃。3. The rural life and catering wastewater treatment device strengthened by structural packing according to claim 1, characterized in that: the biological The fillers (5) are bamboo fillers, polyurethane fillers and foamed glass respectively. 4.根据权利要求1所述结构填料强化的农村生活与餐饮废水处理装置,其特征在于:所述的悬浮吸油填料(2)为经过挂膜的发泡玻璃。4. The rural living and catering wastewater treatment device strengthened by structural fillers according to claim 1, characterized in that: the suspended oil-absorbing filler (2) is foamed glass with a film attached.
CN201620026325.1U 2016-01-12 2016-01-12 Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed Withdrawn - After Issue CN205473193U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620026325.1U CN205473193U (en) 2016-01-12 2016-01-12 Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620026325.1U CN205473193U (en) 2016-01-12 2016-01-12 Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed

Publications (1)

Publication Number Publication Date
CN205473193U true CN205473193U (en) 2016-08-17

Family

ID=56667013

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620026325.1U Withdrawn - After Issue CN205473193U (en) 2016-01-12 2016-01-12 Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed

Country Status (1)

Country Link
CN (1) CN205473193U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105645683A (en) * 2016-01-12 2016-06-08 浙江大学 Structural-filler-reinforced rural domestic and catering wastewater treatment plant and method
CN108358397A (en) * 2018-03-26 2018-08-03 新乡市环境保护科学设计研究院 A kind of Multi-functional effluent treatment unit for improving the ecological environment
CN109320028A (en) * 2018-12-10 2019-02-12 重庆固润科技发展有限公司 The system and method for kitchen garbage and sanitary sewage integration in-situ treatment
WO2022196828A1 (en) * 2021-03-19 2022-09-22 株式会社村上開明堂 Oil-treating carrier and oil-treating method
CN115716698A (en) * 2022-12-22 2023-02-28 贵州大学 A rural domestic sewage treatment system and purification method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105645683A (en) * 2016-01-12 2016-06-08 浙江大学 Structural-filler-reinforced rural domestic and catering wastewater treatment plant and method
CN105645683B (en) * 2016-01-12 2018-03-16 浙江大学 The life in the countryside that structured packing is strengthened and restaurant wastewater treatment device and its method
CN108358397A (en) * 2018-03-26 2018-08-03 新乡市环境保护科学设计研究院 A kind of Multi-functional effluent treatment unit for improving the ecological environment
CN109320028A (en) * 2018-12-10 2019-02-12 重庆固润科技发展有限公司 The system and method for kitchen garbage and sanitary sewage integration in-situ treatment
WO2022196828A1 (en) * 2021-03-19 2022-09-22 株式会社村上開明堂 Oil-treating carrier and oil-treating method
CN115716698A (en) * 2022-12-22 2023-02-28 贵州大学 A rural domestic sewage treatment system and purification method

Similar Documents

Publication Publication Date Title
CN205473193U (en) Life in countryside and food and beverage effluent treatment plant that structured packing is reinforceed
CN105645683B (en) The life in the countryside that structured packing is strengthened and restaurant wastewater treatment device and its method
CN101973679B (en) Distributed sewage treatment and regeneration technology
CN102701448B (en) Rural domestic sewage reutilization treatment device
CN206266394U (en) Integrated scattered domestic sewage treatment device
CN211644786U (en) Biochemical wetland ecological purification system for new rural domestic sewage
CN102976548A (en) Zero emission district sewage resource treatment apparatus
CN105110567A (en) Process for advanced treatment of southern large-scale swine wastewater
CN205398371U (en) Rural miniaturized integration sewage treatment unit
CN104355490B (en) The removal device of pollution substance and minimizing technology in a kind of domestic sewage in rural areas
CN104030524B (en) Seasonal aeration domestic sewage deep denitrification process and device
CN105347499A (en) Method for absorbing tail water of municipal wastewater plant by immersed vertical flow artificial wetlands
CN109626760A (en) Rain dirt mixed flow drains total system and method
CN212025101U (en) MBR integration sewage treatment plant
CN203112657U (en) Constant-effluent variable-load SVBR (Steady outflow Variable load Biological Reactor) sewage treater
CN206033519U (en) Rural domestic sewage of solar energy drips and strains processing system
CN105502801B (en) Seasonal frost region Expressway Service combined sewage water processing system devices and methods therefor
CN106145356A (en) Integral type sewage processing means and processing method
CN203781915U (en) Nitrification and denitrification integrated rural domestic sewage treatment system
CN112158943B (en) A biological trickle device and its application based on dry garbage filler from domestic sources
CN221565924U (en) Domestic sewage treatment device adopting IBMW technology
CN210796140U (en) Domestic sewage treatment device
CN210215089U (en) Bypass processing system of black and odorous water body
CN204675952U (en) The buried sewage treatment equipment that a kind of low noise sound pitch is integrated
CN107529525A (en) A kind for the treatment of method for rural sewage and system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160817

Termination date: 20170112

CF01 Termination of patent right due to non-payment of annual fee
AV01 Patent right actively abandoned

Granted publication date: 20160817

Effective date of abandoning: 20180316

AV01 Patent right actively abandoned