CN104961232A - Vertical integral sewage treatment plant - Google Patents
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- CN104961232A CN104961232A CN201510332597.4A CN201510332597A CN104961232A CN 104961232 A CN104961232 A CN 104961232A CN 201510332597 A CN201510332597 A CN 201510332597A CN 104961232 A CN104961232 A CN 104961232A
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- 239000010865 sewage Substances 0.000 title claims abstract description 40
- 239000010802 sludge Substances 0.000 claims abstract description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 230000015556 catabolic process Effects 0.000 claims abstract description 5
- 238000006731 degradation reaction Methods 0.000 claims abstract description 5
- 229910000838 Al alloy Inorganic materials 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims 1
- 238000010276 construction Methods 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 abstract description 19
- 238000009825 accumulation Methods 0.000 abstract description 13
- 238000005273 aeration Methods 0.000 abstract description 11
- 239000006228 supernatant Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 9
- 238000010586 diagram Methods 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 239000000693 micelle Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000009440 infrastructure construction Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
本发明涉及一种竖式一体化污水处理装置,包括厌氧区、好氧区以及沉淀区;所述的三个区为三个套筒相互嵌套组合结构,其中,沉淀区在外,好氧区居中,厌氧区在内;污水通过进水管流入厌氧区,与厌氧区中活性污泥混合进行厌氧降解,通过溢流方式经厌氧区顶部流入好氧区;好氧区与厌氧区顶部设有三相分离器,进行气液分离,产生的气体从排气管排出系统;好氧区下部设有曝气装置,实现对污水的好氧降解;好氧区与沉淀区底部相通,曝气处理后的污水从好氧区底部进入沉淀区并向上运动,而污泥向下进入污泥集聚区,实现固液分离;沉淀区顶部设有环形集水区,环形集水区与出水管相连,处理后的上清水经出水管流出。
The invention relates to a vertical integrated sewage treatment device, which includes an anaerobic zone, an aerobic zone and a sedimentation zone; the three zones are a nested combination structure of three sleeves, wherein the sedimentation zone is outside, and the aerobic zone is outside. The area is in the middle, and the anaerobic area is included; the sewage flows into the anaerobic area through the water inlet pipe, mixes with the activated sludge in the anaerobic area for anaerobic degradation, and flows into the aerobic area through the top of the anaerobic area through overflow; the aerobic area and The top of the anaerobic zone is equipped with a three-phase separator for gas-liquid separation, and the gas generated is discharged from the system through the exhaust pipe; the lower part of the aerobic zone is equipped with an aeration device to realize the aerobic degradation of sewage; the bottom of the aerobic zone and the sedimentation zone In the same way, the sewage after aeration treatment enters the sedimentation area from the bottom of the aerobic area and moves upward, while the sludge enters the sludge accumulation area downwards to realize solid-liquid separation; there is an annular catchment area on the top of the sedimentation area, and the annular water collection area It is connected with the outlet pipe, and the treated supernatant water flows out through the outlet pipe.
Description
技术领域 technical field
本发明涉及一种适用于农村散居型污水处理的一体化装置,属于环境保护领域。 The invention relates to an integrated device suitable for rural scattered sewage treatment, which belongs to the field of environmental protection.
背景技术 Background technique
随着经济的发展,农药、化肥的广泛使用以及农村生活污水排放量的增大,使大量的含氮及其它生物营养物质不断地排入河流和湖库,使水体富营养化程度加快加重,目前我国农村污水排放量大且污水有效处理率低,水域污染严重,处理难以达到国家标准。 With the development of the economy, the widespread use of pesticides and chemical fertilizers and the increase in the discharge of rural domestic sewage, a large amount of nitrogen and other biological nutrients are continuously discharged into rivers and lakes, which accelerates the degree of eutrophication of water bodies. At present, my country's rural sewage discharge is large and the effective treatment rate of sewage is low. The water area is seriously polluted, and the treatment is difficult to meet the national standard.
虽然我国已经采取了大量措施来解决农村水污染问题,但是在技术设备方面存在着基建造价和运行成本较高、处理效率有待提高等问题。我国的农村污水处理设备还存在着效率低、能耗高、维修率高、自动化程度低等缺点。尽管随着改革开放步伐的加快,我国也引进了一些国外的设备,然而这些设备价格十分昂贵不利于我国农村污水处理设备制造业的发展。本发明具有成本低,简单有效,自动化程度高,适合于农村等散居型住户使用的优点。 Although our country has taken a lot of measures to solve the problem of rural water pollution, there are still some problems in terms of technical equipment, such as high infrastructure construction cost and operating cost, and treatment efficiency needs to be improved. my country's rural sewage treatment equipment still has shortcomings such as low efficiency, high energy consumption, high maintenance rate, and low degree of automation. Although with the accelerated pace of reform and opening up, my country has also introduced some foreign equipment, but the price of these equipment is very expensive, which is not conducive to the development of my country's rural sewage treatment equipment manufacturing industry. The invention has the advantages of low cost, simplicity and effectiveness, high degree of automation, and is suitable for scattered households in rural areas.
发明内容 Contents of the invention
本发明所要解决的技术问题是提供一种简单有效,操作容易的农村污水处理系统。 The technical problem to be solved by the invention is to provide a simple, effective and easy-to-operate rural sewage treatment system.
本发明为解决上述技术问题采用的技术方案是: 一种竖式一体化污水处理装置,装置包括厌氧区、好氧区以及沉淀区;所述的三个区为三个套筒相互嵌套组合结构,其中,由外而内依次设置沉淀区、好氧区及厌氧区;污水通过进水管从厌氧区底部流入,与厌氧区中活性污泥混合进行厌氧降解,通过溢流方式经厌氧区顶部流入好氧区;好氧区与厌氧区顶部设有三相分离器,用于气液分离,产生的气体从排气管排出系统;好氧区下部设有曝气装置;好氧区与沉淀区底部相通;沉淀区顶部设有环形集水区,环形集水区与出水管相连;沉淀区底部为污泥集聚区。 The technical scheme that the present invention adopts for solving the above-mentioned technical problems is: a kind of vertical integrated sewage treatment device, and device comprises anaerobic zone, aerobic zone and sedimentation zone; Described three zones are that three sleeves are nested mutually Combined structure, in which, from the outside to the inside, the sedimentation zone, aerobic zone and anaerobic zone are set in sequence; the sewage flows in from the bottom of the anaerobic zone through the water inlet pipe, and is mixed with the activated sludge in the anaerobic zone for anaerobic degradation, and through the overflow The method flows into the aerobic area through the top of the anaerobic area; the aerobic area and the top of the anaerobic area are equipped with a three-phase separator for gas-liquid separation, and the generated gas is discharged from the system through the exhaust pipe; the lower part of the aerobic area is equipped with an aeration device The aerobic area is connected to the bottom of the sedimentation area; the top of the sedimentation area is provided with an annular water collection area, which is connected to the outlet pipe; the bottom of the sedimentation area is a sludge accumulation area.
进一步的,所述厌氧区为一上、下连通的通道,通道上端与所述好氧区连通,通道下端通过一污泥防反冲装置与污泥集聚区相连通。 Further, the anaerobic zone is a channel connecting up and down, the upper end of the channel communicates with the aerobic zone, and the lower end of the channel communicates with the sludge accumulation area through a sludge anti-recoil device.
进一步的,所述污泥防反冲装置为中部宽,两头窄的中空结构。 Further, the sludge anti-recoil device is a hollow structure with a wide middle and narrow ends.
进一步的,所述厌氧区通道的径高比为1:4~8。 Further, the diameter-to-height ratio of the channels in the anaerobic zone is 1:4-8.
进一步的,所述好氧区的底部设有污泥导流板,所述污泥导流板与所述污泥防反冲装置的外壁之间形成污泥沉降通道。 Further, a sludge deflector is provided at the bottom of the aerobic zone, and a sludge settlement channel is formed between the sludge deflector and the outer wall of the sludge anti-recoil device.
进一步的,所述的曝气装置包括主进气管道、环形管道、喷气头,其中,主进气管道连通环形管道,在环形管道上设有多于一个的喷气头。 Further, the aeration device includes a main air intake pipe, an annular pipe, and an air injection head, wherein the main air intake pipe communicates with the annular pipe, and more than one air injection head is arranged on the annular pipe.
进一步的,所述喷气头为多孔吹气铝合金结构。 Further, the air spray head is a porous blown aluminum alloy structure.
进一步的,所述沉淀区为上宽下窄的结构。 Further, the precipitation zone is a structure with a wide top and a narrow bottom.
进一步的,所述污泥集聚区的底部中心设有排泥管。 Further, a sludge discharge pipe is provided at the center of the bottom of the sludge accumulation area.
本发明竖式一体化污水处理装置的有益效果: Beneficial effects of the vertical integrated sewage treatment device of the present invention:
本发明的有益效果: Beneficial effects of the present invention:
第一、厌氧区底部装有污泥防反冲装置,为中部宽,两头窄的中空结构。上部上窄下宽的外部结构与导流板形成污泥沉降通道,有利于污泥与水分离;下部上宽下窄的外部结构,在污泥进入污泥集聚区时能够防止污泥反冲上浮;中空结构使污水在厌氧区反应中产生的老化菌胶团下沉进入污泥集聚区,有效提高了污泥处理效果。 First, the bottom of the anaerobic zone is equipped with a sludge anti-recoil device, which is a hollow structure with a wide middle and narrow ends. The outer structure with narrow top and wide bottom at the upper part and the deflector form a sludge settlement channel, which is conducive to the separation of sludge and water; the outer structure with a narrow top and narrow bottom at the lower part can prevent sludge recoil when sludge enters the sludge accumulation area Floating; the hollow structure makes the aging bacteria micelles produced in the reaction of the sewage in the anaerobic zone sink into the sludge accumulation zone, effectively improving the sludge treatment effect.
第二、好氧区设有导流板,与厌氧区底部的污泥防反冲装置之间形成污泥沉降通道,有利于好氧处理后的污泥杂质进入污泥集聚区,增强了污水处理效果。 Second, the aerobic zone is equipped with a deflector, which forms a sludge settlement channel between the sludge anti-recoil device at the bottom of the anaerobic zone, which is conducive to the sludge impurities after aerobic treatment entering the sludge accumulation zone, enhancing the The effect of sewage treatment.
第三、曝气装置为活性污泥和生物膜中的微生物提供足量的氧气,确保微生物的活性。 Third, the aeration device provides sufficient oxygen for the microorganisms in the activated sludge and biofilm to ensure the activity of the microorganisms.
第四、系统顶部设有环形集水区,便于处理后的上清水收集排出。 Fourth, the top of the system is equipped with a ring-shaped water collection area, which is convenient for collecting and discharging the treated supernatant water.
第五、沉淀区造型设计为上宽下窄的结构,提高了污水中固形物的沉淀效果。 Fifth, the shape of the sedimentation area is designed as a structure with a wide top and a narrow bottom, which improves the sedimentation effect of solids in sewage.
附图说明 Description of drawings
图1为本发明中所述的竖式一体化污水处理装置的外部结构示意图; Fig. 1 is a schematic diagram of the external structure of the vertical integrated sewage treatment device described in the present invention;
图2为本发明中所述的竖式一体化污水处理装置的内部结构图; Fig. 2 is the internal structure diagram of the vertical integrated sewage treatment device described in the present invention;
图3为本发明所述的竖式一体化污水处理装置的曝气装置结构图; Fig. 3 is the structural diagram of the aeration device of the vertical integrated sewage treatment device according to the present invention;
图4为本发明所述的竖式一体化污水处理装置的污泥防反冲装置结构示意图; Fig. 4 is a schematic structural view of the sludge anti-recoil device of the vertical integrated sewage treatment device according to the present invention;
其中,1为进水管,2为污泥防反冲装置,3为排泥管,4为导流板,5为曝气管,5-1为进气主管道,5-2为环形管道,5-3为喷气头,6为厌氧区,7为好氧区,8为沉淀区,9为三相分离器,10为环形集水区,11为排气管,12为出水管,13为池壁,14为污泥集聚区。 Among them, 1 is the water inlet pipe, 2 is the sludge anti-recoil device, 3 is the mud discharge pipe, 4 is the deflector, 5 is the aeration pipe, 5-1 is the main air intake pipe, 5-2 is the ring pipe, 5-3 is the jet head, 6 is the anaerobic zone, 7 is the aerobic zone, 8 is the sedimentation zone, 9 is the three-phase separator, 10 is the annular water collection zone, 11 is the exhaust pipe, 12 is the outlet pipe, 13 is the pool wall, and 14 is the sludge accumulation area.
具体实施方式 Detailed ways
下面结合附图对本发明提供的竖式一体化污水处理装置进行进一步说明。 The vertical integrated sewage treatment device provided by the present invention will be further described below in conjunction with the accompanying drawings.
如图2所示,为本发明提供的竖式一体化污水处理装置示意图从内到外由三个部分组成,内层为厌氧区6、中层为好氧区7、外层为沉淀区8。污水从进水管1流入,与厌氧区6中活性污泥混合进行厌氧降解,其底部装有污泥防反冲装置2。污水经厌氧区6顶部流入好氧区7;好氧区7与厌氧区6顶部设有三相分离器9,进行气液分离,产生的气体从排气管11排出系统;好氧区7下部设有曝气装置5;好氧区7与沉淀区8底部相通,曝气处理后的污水从底部进入沉淀区8并向上运动,而污泥在底部导流板4的作用下,向下进入污泥集聚区14,实现固液分离。沉淀区8顶部设有环形集水区10,与出水管12相连,处理后的上清水经出水管12流出。 As shown in Figure 2, the schematic diagram of the vertical integrated sewage treatment device provided by the present invention is composed of three parts from the inside to the outside, the inner layer is an anaerobic zone 6, the middle layer is an aerobic zone 7, and the outer layer is a sedimentation zone 8 . Sewage flows in from the water inlet pipe 1, and is mixed with the activated sludge in the anaerobic zone 6 for anaerobic degradation, and a sludge anti-recoil device 2 is installed at the bottom. The sewage flows into the aerobic zone 7 through the top of the anaerobic zone 6; the aerobic zone 7 and the top of the anaerobic zone 6 are provided with a three-phase separator 9 for gas-liquid separation, and the generated gas is discharged from the system through the exhaust pipe 11; the aerobic zone 7 The lower part is equipped with an aeration device 5; the aerobic zone 7 is connected to the bottom of the sedimentation zone 8, and the sewage after aeration treatment enters the sedimentation zone 8 from the bottom and moves upwards, while the sludge flows downward under the action of the deflector 4 at the bottom. Enter the sludge accumulation area 14 to realize solid-liquid separation. The top of the sedimentation area 8 is provided with an annular water collection area 10, which is connected with the water outlet pipe 12, and the treated supernatant water flows out through the water outlet pipe 12.
沉淀区8造型设计为上宽下窄的斗型结构,提高了污水中固形物的沉淀效果。 The shape of the sedimentation zone 8 is designed as a bucket-shaped structure with a wide top and a narrow bottom, which improves the sedimentation effect of solids in sewage.
如图3所示,曝气装置5由主进气管道5-1、环形管道5-2、喷气头5-3所组成。主进气管道5-1连通环形管道5-2,在环形管道5-2上设有多于一个的喷气头5-3,喷气头为多孔吹气铝合金喷气喷头。该装置能够保证好氧区7曝气量的需求,为活性污泥和生物膜中微生物的生长提供了足够的氧气,确保微生物的活性。 As shown in Figure 3, the aeration device 5 is composed of a main air intake pipe 5-1, an annular pipe 5-2, and an air spray nozzle 5-3. The main air intake pipe 5-1 communicates with the annular pipe 5-2, and more than one air spray head 5-3 is arranged on the annular pipe 5-2, and the air spray head is a multi-hole blown aluminum alloy air spray nozzle. The device can ensure the aeration requirement of the aerobic zone 7, provide sufficient oxygen for the growth of microorganisms in the activated sludge and biofilm, and ensure the activity of microorganisms.
如图4所示,为本发明提供的竖式一体化污水处理装置的底部示意图,系统好氧区7底部设有的导流板4与厌氧区6底部的污泥防反冲装置2之间形成污泥沉降通道,有利于好氧处理后的污泥沉降到污泥集聚区14;厌氧区6底部与污泥集聚区14相通,厌氧区处理后产生的老化菌胶团通过污泥防反冲装置2的中空结构下沉进入污泥集聚区。菌胶团是活性污泥和生物膜的重要组成部分,有较强的吸附和氧化有机物的能力,老化的菌胶团由于吸附了许多杂质,密度比水大。厌氧区通道径高比为1:4~8,中空结构对于厌氧效果影响在允许范围内;增强了污水处理效果。 As shown in Figure 4, it is a bottom schematic diagram of the vertical integrated sewage treatment device provided by the present invention, between the deflector 4 provided at the bottom of the aerobic zone 7 of the system and the sludge anti-recoil device 2 at the bottom of the anaerobic zone 6 The sludge settlement channel is formed between them, which is beneficial for the sludge after aerobic treatment to settle to the sludge accumulation area 14; the bottom of the anaerobic area 6 communicates with the sludge accumulation area 14, and the aging bacteria micelles produced after the treatment in the anaerobic area pass through the sludge accumulation area 14. The hollow structure of the mud anti-recoil device 2 sinks into the sludge accumulation area. Bacterial micelles are an important part of activated sludge and biofilm, and have a strong ability to adsorb and oxidize organic matter. The aged bacterial micelles have a higher density than water due to the adsorption of many impurities. The channel diameter-to-height ratio in the anaerobic zone is 1:4~8, and the effect of the hollow structure on the anaerobic effect is within the allowable range; the effect of sewage treatment is enhanced.
Claims (9)
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| CN108249573A (en) * | 2018-04-17 | 2018-07-06 | 青岛沃安环境科技有限公司 | A kind of biologic purifying pot for sewage disposal |
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| CN108249573A (en) * | 2018-04-17 | 2018-07-06 | 青岛沃安环境科技有限公司 | A kind of biologic purifying pot for sewage disposal |
| CN108249573B (en) * | 2018-04-17 | 2024-04-30 | 青岛沃安环境科技有限公司 | Biological purification tank for sewage treatment |
| CN109133349A (en) * | 2018-08-25 | 2019-01-04 | 中持水务股份有限公司 | AO integrated reaction equipment suitable for garbage leachate wastewater processing |
| CN111995054A (en) * | 2020-09-14 | 2020-11-27 | 兰州交通大学 | A sewage treatment device |
| CN117105399A (en) * | 2023-10-11 | 2023-11-24 | 华夏碧水环保科技股份有限公司 | Three-phase separation reaction precipitation device for treating rural domestic sewage |
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