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CN201915003U - Novel side channel-type integrated bioreactor sewage treatment device - Google Patents

Novel side channel-type integrated bioreactor sewage treatment device Download PDF

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Publication number
CN201915003U
CN201915003U CN201020628838.2U CN201020628838U CN201915003U CN 201915003 U CN201915003 U CN 201915003U CN 201020628838 U CN201020628838 U CN 201020628838U CN 201915003 U CN201915003 U CN 201915003U
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zone
wall
anoxic
treatment device
anaerobic
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李德豪
殷旭东
朱越平
谢文玉
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Guangdong University of Petrochemical Technology
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Guangdong University of Petrochemical Technology
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Abstract

一种新型侧沟式一体化生物反应废水处理装置,底板(19)的外周有O型的外墙(1)和环形的沉淀池(9),中部位置有O型的内墙(14)形成厌氧区,C型的隔板(5)内侧与内墙14之间形成缺氧区(4),外侧与外墙1之间形成好氧区(2),隔板5缺口与外墙1之间形成混合区(15);内墙底部有进水口(16),位于缺氧区一侧有出水口(17),沉淀池有排水口(9);好氧区设置有曝气管(3),位于同一侧的好氧区、缺氧区的入口和厌氧区中间分别安装有搅拌推流器(6)。本实用新型结构紧凑、简洁,运行操作与维护十分简便,所需劳动力少,且易于实现远程自动控制。

Figure 201020628838

A novel side ditch type integrated biological reaction wastewater treatment device, the outer periphery of the bottom plate (19) has an O-shaped outer wall (1) and an annular sedimentation tank (9), and the middle part is formed by an O-shaped inner wall (14) Anaerobic zone, the anoxic zone (4) is formed between the inner side of the C-shaped partition (5) and the inner wall 14, and the aerobic zone (2) is formed between the outer side and the outer wall 1, and the gap of the partition 5 and the outer wall 1 A mixing zone (15) is formed between them; there is a water inlet (16) at the bottom of the inner wall, a water outlet (17) on one side of the anoxic zone, and a drain (9) in the sedimentation tank; an aeration pipe ( 3), the entrance of the aerobic zone, the anoxic zone, and the middle of the anaerobic zone on the same side are respectively equipped with stirring flowmakers (6). The utility model has the advantages of compact and simple structure, very simple operation and maintenance, less labor force required, and easy remote automatic control.

Figure 201020628838

Description

Novel lateral sulcus formula integral biological reaction waste treatment unit
Technical field
The utility model relates to a kind of novel lateral sulcus formula integral biological reaction waste treatment unit.
Background technology
At present more single, the poor processing effect of the improvement ubiquity treatment process of China's sewage, floor space is big, investment is high characteristics, and integrated sewage treating apparatus has reduced investment, takes up an area of less, advantages such as energy consumption is low, treatment effect good, simple and convenient management, is a kind of new direction of sewage disposal of suitable China's national situation.
The internal recycle of mixed solution and the automatic backflow of mud are realized in each functional zone of integrated apparatus under the effect of stirring impeller, be a kind of novel process of efficient economy type.
Summary of the invention
The purpose of this utility model provides the novel lateral sulcus formula novel all-in-one biological respinse wastewater treatment equipment that a kind of each functional zone subregion is obvious, can reduce operation energy consumption, minimizing floor space.
To achieve the above object, the technical solution adopted in the utility model is:
A kind of novel lateral sulcus formula integral biological reaction waste treatment unit, the periphery of base plate has the exterior wall and the annular settling tank of O type, medium position has the interior wall of O type to form anaerobic zone, form the oxygen-starved area between the dividing plate inboard of C type and the interior wall, form aerobic zone between the outside and the exterior wall, form the mixing zone between dividing plate breach and the exterior wall; Water-in is arranged at the interior wall bottom, and being positioned at oxygen-starved area one side has water outlet, and settling tank has water port; Aerobic zone is provided with aeration tube, is positioned at the aerobic zone of the same side, the inlet and the middle stirring impeller that is separately installed with of anaerobic zone of oxygen-starved area.
Be provided with anaerobic-anoxic mud circulation passage between anaerobic zone and the oxygen-starved area, circulation passage top is provided with inlet, outlet, and the bottom is provided with anoxic-anaerobism exchange mouth.Settling tank is supported built on stilts by at least three pillar stiffeners, be the window that settling tank and aerobic zone link between the pillar stiffener.Be extended with the inclined-plane that links and extend inwards with the exterior wall base plate under this settling tank one side direction, the horizontal sextant angle on this inclined-plane is 50~60 °.The settling tank bottom is the awl bucket of annular array, and the awl bucket is for falling platform-type structure, and its conical surface and horizontal plane angle are 60~75 °.
The utility model compact construction, succinct, operation is very easy with maintenance, and required labor force is few, and is easy to realize remote auto control.
Settling tank of the present utility model is installed in the device outside, lay ringwise, need not the outer second pond of building, the platform-type structure of falling of bucket is bored in the settling tank bottom, can effectively alleviate the turbulent flow influence of minimizing bottom flow to settling tank, and the while, the middle negative pressure that produces made mud can realize backflow certainly owing to bottom flow flows, floor space and working cost have been reduced, and help keeping the dissolved oxygen of water outlet, guarantee effluent quality, also can reduce the resistance of fluid flow.
Aerobic and anoxic of the present utility model, functional zone subregions such as mixing are clear and definite, and control helps finishing synchronously organic removal and biological carbon and phosphorous removal easily.At aerobic zone, mixed solution has been an oxygen condition, and the absorption of phosphorus also takes place for degradation of organic substances and ammonia nitrogen is oxidized to nitric nitrogen nitrate nitrogen and nitrite nitrogen effectively.Being anoxic condition in the oxygen-starved area, is carbon source with the organism, under the effect of denitrifying bacteria is nitrogen and removing from water with nitrate-nitrogen reduction.In the ammonification of anaerobic zone generation organonitrogen, and degradation of organic substances carries out the release of phosphorus.
The utility model is provided with anaerobic-anoxic mud circulation passage, helps improving the anaerobic zone sludge concentration, thereby has strengthened system's anti-shock loading and dephosphorization ability.
The utility model helps mixed solution repeatedly circulation between aerobic-anoxic-mixing zone, and refluxes automatically and realize the denitrogenation purpose.
Description of drawings
Fig. 1 is the floor map of the utility model device;
Fig. 2 is the diagrammatic cross-section of the utility model device.
Embodiment
See figures.1.and.2, the periphery of base plate 19 has the exterior wall 1 and the annular settling tank 8 of O type, medium position has the interior wall 14 of O type to form anaerobic zone, form oxygen-starved area 4 between dividing plate 5 inboards of C type and the interior wall 14, form aerobic zone 2 between the outside and the exterior wall 1, form mixing zone 15 between dividing plate 5 breach and the exterior wall 1; Water-in 16 is arranged at interior wall 14 bottoms, and being positioned at oxygen-starved area 4 one sides has water outlet 17, and settling tank 8 has water port 7; Aerobic zone 2 is provided with aeration tube 3, is positioned at the aerobic zone 2 of the same side, the inlet and the middle stirring impeller 6 that is separately installed with of anaerobic zone of oxygen-starved area 4.
Be provided with anaerobic-anoxic mud circulation passage 11 between anaerobic zone and the oxygen-starved area 4, circulation passage 11 tops are provided with inlet 10, outlet 12, and the bottom is provided with anoxic-anaerobism exchange mouth 13.
Settling tank 8 is supported built on stilts by three pillar stiffeners 18, the window that links for settling tank 8 and aerobic zone 2 between the pillar stiffener 18.Be extended with the inclined-plane 20 that links and extend inwards with base plate 19 under these settling tank 8 one side direction, the horizontal sextant angle on this inclined-plane 20 is 50~60 °.Settling tank 8 bottoms are the awl bucket 9 of annular array, and awl bucket 9 is for falling platform-type structure, and its conical surface and horizontal plane angle are 60~75 °.
Principle of work of the present utility model is: organic degraded, the ammonification of organonitrogen, the release of phosphorus take place by 16 water inlets of interior wall 14 foot water-ins in sewage in anaerobic zone, enter into oxygen-starved area 4 by water outlet 17 then.Microbial population in 4 ingress, oxygen-starved area are stirred under the promotion of impeller 6 with it carries out thorough mixing.The mixed solution part of oxygen-starved area 4 flows out the oxygen-starved area, another part flow into anaerobic-anoxic mud circulation passage 11 by the inlet 10 that is arranged on anaerobic-anoxic mud circulation passage 11 tops, deposit herein, supernatant liquor liquid flow into mixing zone 15 by the outlet 12 on top, below the inlet 13 of the higher mud of concentration by the bottom be back in the anaerobic zone in the interior wall 14.4 mixed solutions are anoxic condition in the oxygen-starved area, carry out the utilization degraded of denitrification denitrogenation and partial organic substances; Entering mixing zone 15 then mixes with mixed solution from oxygen-starved area 4, aerobic zone 2, another part enters aerobic zone 2 respectively through aerobic zone 2 inlets, the aeration tube of laying between partition wall 5 in aerobic zone 2 bottom being installed in and the exterior wall 13 carries out aeration, make mixed solution be oxygen condition, in aerobic zone 2, carry out the nitration reaction of organic matter removal, ammonia nitrogen, the absorption of phosphorus.
Part mixed solution enters settling tank 8 by the awl bucket 9 of settling tank 8 bottoms, under the action of gravity of absorption, collision and the active sludge self of sludge suspension layer, carry out solid-liquid separation, mixed solution is after solid-liquid separation, discharge by water outlet 7 through overflow weir with the supernatant liquor of water inlet equivalent, mud is then under the drive of self gravitation and bottom streaming fluid, certainly be back in the device by awl bucket 9, settling tank 8 part mud are back in the device and realize that with mixed solution aerobic-anoxic blended repeatedly circulates under the promotion of stirring impeller 6 in this device, and sewage is purified.

Claims (5)

1.一种新型侧沟式一体化生物反应废水处理装置,其特征在于,底板(19)的外周有O型的外墙(1)和环形的沉淀池(9),中部位置有O型的内墙(14)形成厌氧区,C型的隔板(5)内侧与内墙(14)之间形成缺氧区(4),外侧与外墙(1)之间形成好氧区(2),隔板(5)缺口与外墙(1)之间形成混合区(15);内墙(14)底部有进水口(16),位于缺氧区(4)一侧有出水口(17),沉淀池(9)有排水口(9);好氧区(2)设置有曝气管(3),位于同一侧的好氧区(2)、缺氧区(4)的入口和厌氧区中间分别安装有搅拌推流器(6)。1. A novel side ditch type integrated biological reaction wastewater treatment device is characterized in that the outer periphery of the bottom plate (19) has an O-shaped outer wall (1) and an annular sedimentation tank (9), and the middle position has an O-shaped The inner wall (14) forms an anaerobic zone, an anoxic zone (4) is formed between the inner side of the C-shaped partition (5) and the inner wall (14), and an aerobic zone (2) is formed between the outer side and the outer wall (1). ), a mixing zone (15) is formed between the gap of the partition (5) and the outer wall (1); there is a water inlet (16) at the bottom of the inner wall (14), and there is a water outlet (17) on one side of the anoxic zone (4) ), the sedimentation tank (9) has a drain outlet (9); the aerobic zone (2) is provided with an aeration pipe (3), and the entrance and anaerobic zone (2) and anoxic zone (4) are located on the same side Stirring flowmakers (6) are respectively installed in the middle of the oxygen zone. 2.根据权利要求1所述的新型侧沟式一体化生物反应废水处理装置,其特征在于,厌氧区和缺氧区之间设有厌氧-缺氧污泥循环通道(11),循环通道(11)上部设有入口(10)、出口(12),下部设有缺氧-厌氧交换口(13)。2. The novel side ditch type integrated biological reaction wastewater treatment device according to claim 1, characterized in that an anaerobic-anoxic sludge circulation passage (11) is provided between the anaerobic zone and the anoxic zone, and the circulation An inlet (10) and an outlet (12) are arranged at the upper part of the channel (11), and an anoxic-anaerobic exchange port (13) is arranged at the lower part. 3.根据权利要求1所述的新型侧沟式一体化生物反应废水处理装置,其特征在于,沉淀池(8)由至少三根支撑柱(18)支撑架空,支撑柱(18)之间为沉淀池(8)与好氧区(2)相联的窗口。3. The new side ditch type integrated biological reaction wastewater treatment device according to claim 1, characterized in that the settling tank (8) is supported by at least three supporting columns (18), and the supporting columns (18) are supported by sedimentation tanks. Pool (8) is connected with the window of aerobic zone (2). 4.根据权利要求3所述的新型侧沟式一体化生物反应废水处理装置,其特征在于,该沉淀池(8)一侧向下延伸有与底板(19)相联且向里延伸的斜面(20),该斜面(20)的水平夹角为50~60°。4. The new side ditch integrated biological reaction wastewater treatment device according to claim 3, characterized in that, one side of the sedimentation tank (8) extends downwards with a slope connected to the bottom plate (19) and extending inwards (20), the horizontal angle of the slope (20) is 50-60°. 5.根据权利要求3所述的新型侧沟式一体化生物反应废水处理装置,其特征在于,沉淀池(8)下部为环形排列的锥斗(9),锥斗(9)为倒平台式结构,其锥面与水平面夹角为60~75°。5. The novel side ditch type integrated biological reaction wastewater treatment device according to claim 3, characterized in that, the lower part of the sedimentation tank (8) is a ring-shaped cone bucket (9), and the cone bucket (9) is an inverted platform type Structure, the angle between the conical surface and the horizontal plane is 60-75°.
CN201020628838.2U 2010-11-26 2010-11-26 Novel side channel-type integrated bioreactor sewage treatment device Expired - Fee Related CN201915003U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102515349A (en) * 2011-12-06 2012-06-27 江苏金梓环境科技有限公司 Treatment equipment for synchronous nitrogen and phosphorus removal of domestic sewage
CN108002537A (en) * 2018-01-31 2018-05-08 武汉都市环保工程技术股份有限公司 Oxidation ditch integrated sewage treatment device and system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102515349A (en) * 2011-12-06 2012-06-27 江苏金梓环境科技有限公司 Treatment equipment for synchronous nitrogen and phosphorus removal of domestic sewage
CN108002537A (en) * 2018-01-31 2018-05-08 武汉都市环保工程技术股份有限公司 Oxidation ditch integrated sewage treatment device and system

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Granted publication date: 20110803

Termination date: 20111126