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CN202729953U - Intermission biological reactor (IBR) continuous-flow integration sewage processing device - Google Patents

Intermission biological reactor (IBR) continuous-flow integration sewage processing device Download PDF

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Publication number
CN202729953U
CN202729953U CN201220372520.1U CN201220372520U CN202729953U CN 202729953 U CN202729953 U CN 202729953U CN 201220372520 U CN201220372520 U CN 201220372520U CN 202729953 U CN202729953 U CN 202729953U
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biological reaction
wall
partition wall
reaction zone
inner partition
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章北霖
王小涛
章北平
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Wuhan Fund Environment Protection Co ltd
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WUHAN FUND ENVIRONMENT PROTECTION ENGINEERING Co Ltd
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    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

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Abstract

本实用新型公开了IBR连续流一体化间歇生物反应污水处理装置，其包括装置外壁，其中设置有内隔墙，所述内隔墙将所述装置外壁围成的池体分隔成中部的生物反应区和净水分离区，所述生物反应区中设置有潜水泵，激波传质射流曝气器通过连接管与所述潜水泵连接，在其上端设置有激波传质射流曝气器进气管，在所述生物反应区中还设置有搅拌器，在其底部还设置有污泥排水管。本实用新型的连续流一体化间歇生物反应污水处理装置，结构紧凑，将污水处理的好氧反应过程、缺氧反应过程、沉淀过程、净水分离出水过程集中在一个池体单元结构内完成，同时实现进出水连续不间断运行，提高了工作效率，有占地少、投资省、运行费用低、处理效果好的显著效果。

Figure 201220372520

The utility model discloses an IBR continuous flow integrated intermittent biological reaction sewage treatment device, which includes an outer wall of the device, wherein an inner partition wall is arranged, and the inner partition wall separates the pool body surrounded by the outer wall of the device into a biological reaction in the middle Zone and clean water separation zone, the biological reaction zone is provided with a submersible pump, the shock wave mass transfer jet aerator is connected with the submersible pump through a connecting pipe, and the shock wave mass transfer jet aerator is installed at its upper end The air pipe is also provided with a stirrer in the biological reaction zone, and a sludge drainage pipe is also provided at the bottom thereof. The continuous flow integrated intermittent biological reaction sewage treatment device of the utility model has a compact structure, and the aerobic reaction process, anoxic reaction process, sedimentation process, and water purification and water separation process of sewage treatment are concentrated in one pool unit structure. At the same time, it realizes the continuous and uninterrupted operation of the water in and out, improves the work efficiency, and has the remarkable effects of less land occupation, less investment, lower operating costs and better treatment effects.

Figure 201220372520

Description

IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence
Technical field
The utility model relates to sewage disposal, relates in particular to IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence (Continuous-flow Intermi ssion Biological Reactor, abbreviation IBR).
Background technology
At sewage treatment area, biological method is the mode of the main flow of present sewage disposal.Technique and the device thereof of realizing the biological process sewage disposal have a lot, no matter it is building coagulation structure, steel construction or other type structure, mostly exist modular construction many, can not continuous flow, invest greatly, the defective such as efficient is low, working cost is high.
Therefore, need to provide IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence to address the above problem.
The utility model content
In order to address this problem, the utility model discloses IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence, described waste disposal plant comprises the device outer wall, in described device outer wall, be provided with internal partition wall, the pond body that described internal partition wall surrounds described device outer wall is separated into bio-reaction zone and the water purification disengaging zone at middle part, be provided with submersible pump on the described internal partition wall in the described bio-reaction zone, the mass transfer by shock wave jet aerator is connected with described submersible pump by pipe connecting, be provided with mass transfer by shock wave jet aerator inlet pipe in the upper end of described mass transfer by shock wave jet aerator, in described bio-reaction zone, also be provided with agitator, also be provided with the mud water shoot in the bottom of described bio-reaction zone.
Preferably, be provided with slip swash plate, air guide plate washer, inclined tube filter packing, water shoot and overflow weir notch in the described water purification disengaging zone, the position that links to each other with described internal partition wall at described slip swash plate offers the long strip type lower mud slot, the position that links to each other with described internal partition wall at described air guide plate washer offers the long strip type air drain, described inclined tube filter packing is arranged on the top of described slip swash plate and described air guide plate washer, offer described water shoot at described device outer wall, described water shoot is connected with described overflow weir notch.
Continuous Flow of the present utility model biological respinse waste disposal plant at integrated intermittence, compact construction, aerobic reaction process, hypoxia response process, precipitation process, the water purification separation exiting water process of sewage disposal are concentrated in the pond body unit structure and finish, realize that simultaneously Inlet and outlet water runs without interruption continuously, improved working efficiency, have occupation of land less, reduced investment, working cost is low, treatment effect is good unusual effect.
Introduced the concept of a series of reduced forms in the utility model content part, this will further describe in the embodiment part.The utility model content part does not also mean that key feature and the essential features that will attempt to limit technical scheme required for protection, does not more mean that the protection domain of attempting to determine technical scheme required for protection.
Below in conjunction with accompanying drawing, describe advantage of the present utility model and feature in detail.
Description of drawings
Fig. 1 is the synoptic diagram according to the Continuous Flow biological respinse waste disposal plant at integrated intermittence of an embodiment of the utility model.
Embodiment
In the following description, having provided a large amount of concrete details understands the utility model more thoroughly in order to provide.Yet, it will be apparent to one skilled in the art that the utility model can need not one or more these details and implemented.In other example, for fear of obscuring with the utility model, be not described for technical characterictics more well known in the art.
In order thoroughly to understand the utility model, detailed structure will be proposed in following description.Obviously, execution of the present utility model is not limited to the specific details that those skilled in the art has the knack of.Preferred embodiment of the present utility model is described in detail as follows, yet except these were described in detail, the utility model can also have other embodiments.
Below in conjunction with accompanying drawing embodiment of the present utility model is described in detail.
With reference to figure 1, it is the synoptic diagram according to the Continuous Flow biological respinse waste disposal plant at integrated intermittence of an embodiment of the utility model.Waste disposal plant of the present utility model can be concrete structure, steel construction or other material and combination construction thereof.Its mounting means can be ground type, and is buried or partly buried.
This waste disposal plant comprises device outer wall 1, and this device outer wall 1 surrounds the main body of waste disposal plant, wherein is used for holding sewage and purifying waste water of processing, and installation is within it equally for required miscellaneous equipment.Be provided with internal partition wall 2 at device in the outer wall 1, it will install bio-reaction zone and water purification disengaging zone (water, mud, gas three-phase separation area) that pond body that outer wall 1 surrounds is separated into the middle part, this water purification disengaging zone be arranged in reaction zone around or both sides or one side.
In bio-reaction zone, be provided with sewage water inlet pipe 11, need sewage to be processed to enter in the bio-reaction zone by this sewage water inlet pipe 11.There is shown sewage level 14.Also be provided with submersible pump 8 on the internal partition wall 2 in this bio-reaction zone, the quantity of submersible pump 8 can arrange as required.Mass transfer by shock wave jet aerator 10 is connected with submersible pump 8 by pipe connecting 9.Also be provided with mass transfer by shock wave jet aerator inlet pipe in the upper end of mass transfer by shock wave jet aerator 10.Also be provided with agitator 12 in bio-reaction zone, its quantity can arrange equally as required.The sewage that agitator 12 stirs in the reaction zone evenly rolls.Its effect will be discussed in more detail below.Also be provided with mud water shoot 13 in order to get rid of mud in the bottom of bio-reaction zone.
In the water purification disengaging zone, be provided with slip swash plate 3, air guide plate washer 4, inclined tube filter packing 5, water shoot 6 and overflow weir notch 7.The position that links to each other with internal partition wall 2 at slip swash plate 3 offers long strip type lower mud slot 22, and the position that links to each other with internal partition wall 2 at air guide plate washer 4 offers long strip type air drain 21.Inclined tube filter packing 5 is arranged on the top of slip swash plate 3 and air guide plate washer 4.Offer water shoot 6 at device outer wall 1, water shoot 6 is connected with overflow weir notch 7.
The working process of waste disposal plant of the present utility model below is described.
Bio-reaction zone is inner to be formed and working process:
The sewage that needs to process enters in the bio-reaction zone from sewage water inlet pipe 11 continually continuously, make the whole liquid level in the device keep stable, thereby and make the processing of water purification disengaging zone by hydraulic pressure after water purification liquid level 15 just overflow across the purpose that overflow weir notch 7 reaches continuous effluent.
The alternately continuously operation of three workflow stages is arranged in the bio-reaction zone:
The aerobic reaction stage: the submersible pump 8 that is installed on the internal partition wall is sucked at a high speed mass transfer by shock wave jet aerator 10 and from top to bottom fast injection with sewage by pipe connecting 9.Because suction function, the air that contains oxygen passes through mass transfer by shock wave jet aerator inlet pipe 101 and sucks, and the cutting of the turbulent flow of the fluid shock in mass transfer by shock wave jet aerator 10 and fusion, thereby reaches the purpose that chops up mud and biological floe and accelerated oxidation.The fluid that contains oxygen sprays at a high speed from mass transfer by shock wave ejector 10 lower ends, wash and drive mud and biological floe constantly rolling in reaction zone of body bottom, pond open, make oxygen, organism, sewage evenly mix, react, mixture is repeated above process continuously by submersible pump 8 continuous suctions again, and this process can reach COD degraded, Ammonia Nitrification, aerobic suction phosphorus texts by biology and chemical reaction.
The hypoxia response stage: according to the program of prior setting, the aerobic reaction stage stops behind the certain hour, and the hypoxia response stage begins.All quit work at this stage submersible pump 8 and mass transfer by shock wave jet aerator 10.The sewage that is installed in the agitator 12 stirring reaction zones in the reaction zone evenly rolls, and this stage mainly reaches COD degraded and the denitrifying purpose of ammonia nitrogen.
The anaerobic reaction stage: the hypoxia response stage enters this stage after stopping by the time of setting, this stage except sewage water inlet pipe 11 still water inlet, miscellaneous equipment such as submersible pump, mass transfer by shock wave jet aerator, agitator etc. all quit work.Sewage in the reaction zone is by gravitational settling, and mud sinks at the bottom of the pond.Still there are COD degraded and phosphor-removing effect in this stage.According to practical situation, unnecessary mud is discharged by mud vent pipe 12.
Aerobic reaction stage, hypoxia response stage, anaerobic reaction stage are in alternately continuously operation of reaction zone.
Water purification disengaging zone (water, mud, gas three-phase separation area) is inner to be formed and working process:
The mixed solution of crossing through biological respinse of bio-reaction zone flows into the water purification disengaging zone by the long strip type air drain 21 on the device internal partition wall 2 and long strip type lower mud slot 22, under the natural sedimentation effect, the bubble of light specific gravity rises, and rises along air guide plate washer 4 times along face and dissolves in the bio-reaction zone by long strip type air drain 21; Mud in the mixed solution is because of than great, and precipitation glides and flows into the bottom of bio-reaction zones by long strip type lower mud slot 22 along slip swash plate 3 downwards; Under Water Pressure, pass through the narrow orifice of slip swash plate 3 and air guide plate washer 4 to the upper reaches through what gas mud separated than clean water, and process inclined tube filter packing 5 further cement filtering separation, at this moment water purification up to standard overflows into overflow weir notch 7 and passes through water shoot 6 discharges after rising to the water purification liquid level through processing layer by layer also.
Three processes of the working process of water purification disengaging zone and bio-reaction zone are carried out simultaneously, so realized the purpose of continuous effluent.
The integrated biological respinse waste disposal plant of having a rest of asking of Continuous Flow of the present utility model, compact construction, aerobic reaction process, hypoxia response process, precipitation process, the water purification separation exiting water process of sewage disposal are concentrated in the pond body unit structure and finish, realize that simultaneously Inlet and outlet water runs without interruption continuously, improved working efficiency, have occupation of land less, reduced investment, working cost is low, treatment effect is good unusual effect.
The utility model is illustrated by above-described embodiment, but should be understood that, above-described embodiment just is used for for example and the purpose of explanation, but not is intended to the utility model is limited in the described scope of embodiments.It will be understood by those skilled in the art that in addition; the utility model is not limited to above-described embodiment; can also make more kinds of variants and modifications according to instruction of the present utility model, these variants and modifications all drop in the utility model scope required for protection.Protection domain of the present utility model is defined by the appended claims and equivalent scope thereof.

Claims (2)

1.IBR连续流一体化间歇生物反应污水处理装置，其特征在于，所述污水处理装置包括装置外壁，在所述装置外壁中设置有内隔墙，所述内隔墙将所述装置外壁围成的池体分隔成中部的生物反应区和净水分离区，所述生物反应区中的所述内隔墙上设置有潜水泵，激波传质射流曝气器通过连接管与所述潜水泵连接，在所述激波传质射流曝气器的上端设置有激波传质射流曝气器进气管，在所述生物反应区中还设置有搅拌器，在所述生物反应区的底部还设置有污泥排水管。1. IBR continuous flow integrated intermittent biological reaction sewage treatment device, it is characterized in that, described sewage treatment device comprises device outer wall, is provided with inner partition wall in described device outer wall, and described inner partition wall surrounds described device outer wall The formed pool body is divided into a biological reaction zone in the middle and a clean water separation zone. A submersible pump is arranged on the inner partition wall in the biological reaction zone, and the shock wave mass transfer jet aerator is connected to the submersible through a connecting pipe. The pump is connected, and the upper end of the shock wave mass transfer jet aerator is provided with a shock wave mass transfer jet aerator inlet pipe, and an agitator is also provided in the biological reaction zone, and at the bottom of the biological reaction zone A sludge drain pipe is also provided. 2.按照权利要求1所述的连续流一体化间歇生物反应污水处理装置，其特征在于，所述净水分离区中设置有滑泥斜板、导气档板、斜管过滤填料、排水管和溢流堰槽，在所述滑泥斜板与所述内隔墙相连的位置开设有长条型下泥槽，在所述导气档板与所述内隔墙相连的位置开设有长条型气槽，所述斜管过滤填料设置在所述滑泥斜板和所述导气档板的上方，在所述装置外壁上开设有所述排水管，所述排水管与所述溢流堰槽连接。2. According to the continuous flow integrated intermittent biological reaction sewage treatment device according to claim 1, it is characterized in that, in the water purification separation zone, there are sloping mud plates, air guide baffles, inclined pipe filter fillers, drain pipes and the overflow weir groove, a long mud groove is provided at the position where the mud slide plate is connected with the inner partition wall, and a long mud groove is provided at the position where the air guide baffle is connected with the inner partition wall. Strip-shaped air tank, the inclined pipe filter filler is arranged above the mud slide plate and the air guide baffle, and the drain pipe is opened on the outer wall of the device, and the drain pipe is connected to the overflow Weir flume connection.
CN201220372520.1U 2012-07-31 2012-07-31 Intermission biological reactor (IBR) continuous-flow integration sewage processing device Expired - Lifetime CN202729953U (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104150594A (en) * 2014-07-28 2014-11-19 武汉芳笛环保股份有限公司 Floating island precipitation type IBR bioreactor
CN104891657A (en) * 2015-06-08 2015-09-09 新乡市蓝海环境工程有限公司 CBR sewage biological treatment device and operating method thereof
CN105293701A (en) * 2015-11-06 2016-02-03 武汉芳笛环保股份有限公司 Carbon source reserve type immobilized bioreactor (IBR)
CN106186289A (en) * 2016-08-22 2016-12-07 上海同济建设科技股份有限公司 Integration high load capacity aerobic reactor
CN112551810A (en) * 2020-11-19 2021-03-26 武汉芳笛环保股份有限公司 Denitrification IBR denitrification and dephosphorization integrated reactor and reaction process thereof
CN117164096A (en) * 2023-10-11 2023-12-05 武汉芳笛环保股份有限公司 Sewage advanced treatment contact biochemical reactor

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104150594A (en) * 2014-07-28 2014-11-19 武汉芳笛环保股份有限公司 Floating island precipitation type IBR bioreactor
CN104150594B (en) * 2014-07-28 2016-09-21 武汉芳笛环保股份有限公司 A kind of chinampa precipitating type IBR bioreactor
CN104891657A (en) * 2015-06-08 2015-09-09 新乡市蓝海环境工程有限公司 CBR sewage biological treatment device and operating method thereof
CN105293701A (en) * 2015-11-06 2016-02-03 武汉芳笛环保股份有限公司 Carbon source reserve type immobilized bioreactor (IBR)
CN105293701B (en) * 2015-11-06 2022-11-01 武汉芳笛环保股份有限公司 Carbon source reserve type IBR bioreactor
CN106186289A (en) * 2016-08-22 2016-12-07 上海同济建设科技股份有限公司 Integration high load capacity aerobic reactor
CN112551810A (en) * 2020-11-19 2021-03-26 武汉芳笛环保股份有限公司 Denitrification IBR denitrification and dephosphorization integrated reactor and reaction process thereof
CN117164096A (en) * 2023-10-11 2023-12-05 武汉芳笛环保股份有限公司 Sewage advanced treatment contact biochemical reactor

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