WO2023197640A1 - Energy-saving self-oxygenation distributed biofilm sewage treatment apparatus - Google Patents

Energy-saving self-oxygenation distributed biofilm sewage treatment apparatus Download PDF

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Publication number
WO2023197640A1
WO2023197640A1 PCT/CN2022/137840 CN2022137840W WO2023197640A1 WO 2023197640 A1 WO2023197640 A1 WO 2023197640A1 CN 2022137840 W CN2022137840 W CN 2022137840W WO 2023197640 A1 WO2023197640 A1 WO 2023197640A1
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cage
sewage treatment
biofilm
filler
energy
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PCT/CN2022/137840
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French (fr)
Chinese (zh)
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刘长青
栾亚男
殷悦
张峰
安昱宁
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青岛理工大学
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/08Aerobic processes using moving contact bodies
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
    • 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

Definitions

  • the invention relates to the field of sewage treatment devices, and in particular to an energy-saving self-oxygenating dispersed biofilm sewage treatment device.
  • the small-scale decentralized sewage treatment processes in rural areas of my country mainly use A2O, oxidation ditch, MBBR (moving bed biofilm reactor), biological turntable, constructed wetland, duckweed pond and ecological filter.
  • A2O oxidation ditch
  • MBBR moving bed biofilm reactor
  • biological turntable constructed wetland
  • duckweed pond and ecological filter.
  • the existing technology has common problems such as excessive aeration, high energy consumption, high operating costs, complex processes, difficult maintenance, large floor space, and the outlet water quality is greatly affected by fluctuations in incoming water.
  • MBBR is a technology that is more suitable for rural sewage treatment needs. Its principle is to use suspended fillers as biofilm carriers and put them into good/anoxic reactors according to a certain proportion. The suspended fillers are used for water flow, aeration and stirring in the system.
  • a fluidized state is formed under the action of the filler.
  • the fluidization process of the filler can fully contact the sewage.
  • Microorganisms are more likely to attach and grow on the filler with a high specific surface area, thereby achieving better treatment results.
  • MBBR has the characteristics of high volumetric load, good denitrification effect, strong biofilm resistance to load impact, small footprint, and large biomass. and other advantages, it is currently widely used in urban sewage plants.
  • the current MBBR process mostly uses excessive aeration to meet the effluent quality requirements, resulting in higher aeration energy consumption, operating costs and aeration equipment carrying loads, which increases equipment failure rates and maintenance costs. How to use the advantages of MBBR technology Applying it to the treatment of rural domestic sewage under the conditions of low energy consumption and low operating cost has become an urgent problem to be solved.
  • the present invention constructs an energy-saving self-oxygenating dispersed biofilm sewage treatment device, which can effectively effectively solve the problems raised in the above background technology.
  • the present invention adopts the following technical solutions:
  • Energy-saving self-oxygenating dispersed biofilm sewage treatment device including an integrated shell, a reaction tank with a cover on the top, a drive motor box installed on the right side of the reaction tank, a drive motor installed inside the motor box, and a drive motor installed on the drive The drive shaft on the motor, the distribution box installed outside the motor box, and the biological cage installed on the drive shaft.
  • the biological cage includes a mesh cylindrical packing cage and a porous chassis on the left and right sides.
  • the cylindrical cage is made of stainless steel with an opening rate of 70%-80%.
  • the mesh aperture size is 3-8mm.
  • the porous chassis on the left and right sides are open.
  • the porosity is 30%-50%, and the pore size is 3-5mm.
  • the biological cage includes filler in the cage.
  • the filler is attached with biofilm for biological denitrification.
  • the filler filling rate is 40%-80% of the effective volume of the reaction tank.
  • porous partitions are provided at corresponding positions on the inner wall of the biological cage.
  • the length of the partitions is consistent with the cylindrical cage body, the width is 1/6-1/4 of the diameter of the cage body, and the opening rate is 60%-75%.
  • the hole diameter is 3-5mm, and fixed slots are provided at the connection between the partition and the chassis on the left and right sides for fixing and removing the partition.
  • a quarter of the biological tumbling cage is an openable and closable cage.
  • Three stainless steel hinges are installed on one side of the opening and closing cage to connect with the tumbling cage.
  • Stainless steel fixing buckles are welded on the other side and the corresponding position of the tumbling cage.
  • stainless steel butterfly bolts for fixation.
  • the chassis on both sides of the biological cage is provided with square buckles for fixing the drive shaft.
  • the opening size corresponds to the thickness of the drive shaft and is locked on the drive shaft through bolts.
  • the biological cage is connected to the motor through the drive shaft.
  • reaction tank with a cover plate on the top is equipped with a stainless steel hinge that can be opened to facilitate observation, opening and maintenance.
  • the upper part of the integrated housing is provided with a water inlet pipe and an overflow outlet pipe
  • the lower part is provided with a vent pipe and a drainage pipe groove.
  • the position and number of the inlet and outlet pipes can be changed according to the water inlet and outlet mode and water level requirements.
  • top cover of the drive motor box is equipped with a stainless steel hinge to facilitate opening and maintenance.
  • the drive motor should be a slow speed adjustable motor and can be driven by solar energy to further save electric energy and reduce operating costs.
  • the size of the reaction tank and biological cage of the above-mentioned energy-saving self-oxygenating dispersed biofilm sewage treatment device can be reasonably designed and adjusted according to the actual sewage treatment water volume demand.
  • the filler in the biological cage can be made of high-density polyethylene, Polyurethane sponge, bio-ball filler and other different types of fillers.
  • the opening size of the mesh cylindrical cage should not be larger than the filler diameter or the minimum side length.
  • the porous partitions in the cage carry part of the biological filler out of the water surface, and during the slow rotation process driven by the motor, the porous partitions on the porous partitions
  • the biological filler falls into the reaction pool, and brings in oxygen from the air during the falling process, realizing the self-oxygenation process of the reaction pool.
  • the porous partition at the opposite position has brought another part of the biological filler into the air, which can achieve a continuous self-oxygenation process, and different quantities and positions can be designed according to the different requirements for the size of dissolved oxygen in the actual sewage treatment process.
  • the porous partition card slot allows the regulation of dissolved oxygen by increasing or decreasing the number of partitions and installing partitions at different positions.
  • the biofilm filler used in the present invention has a large specific surface area, large biomass, sufficient space for microbial growth, strong load impact resistance, and can better adapt to rural domestic sewage with large changes in water quality and quantity.
  • part of the filler is suspended on the water surface, which reduces the driving resistance of the motor, further saves energy consumption and reduces operating costs.
  • the openable and closable biological turret of the present invention provides convenience for staff to replace fillers and perform maintenance and repair.
  • the immersion depth of the biological turret can be flexibly set according to different processing requirements and different processing scenarios.
  • the difficulty of equipment maintenance is low. For the village Non-professionals can take up the job with simple training.
  • the new self-oxygenating dispersed biofilm sewage treatment device of the present invention has simple operation, less equipment, low failure rate, and convenient maintenance. It abandons traditional blasting and aeration equipment, which greatly reduces operating energy consumption and operating costs.
  • the energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention is more flexible in applicability scenarios and can be flexibly combined with other treatment processes and different types of reactors to be used in areas with backward basic economic levels, large fluctuations in water quality and quantity, Scattered rural areas, remote areas and temporarily built prefabricated houses will have broad application prospects in the field of low energy consumption decentralized sewage treatment.
  • Figure 1 is a schematic structural diagram of an energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention
  • Figure 3 is the left side view of the biological cage
  • Figure 4 is a schematic diagram of the self-oxygenation operation during the rotation of the biological cage.
  • the energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention includes an integrated treatment device housing 1, a sewage treatment reaction tank body 2, a biological cage structure 3, and a motor box located in the motor box 10. The drive motor 11 and the distribution box 15 outside the motor box 10 are driven.
  • the reaction tank body 2 is provided with an inlet pipe 4, an overflow outlet pipe 12 and an emptying pipe 13, and is provided with an openable and closable transparent cover 8.
  • the arrangement of the transparent cover is conducive to real-time observation and opening of the biological cage 3. Overhaul.
  • the reaction tank body 2 adopts an easy-to-process rectangular tank body, and the material is generally carbon steel anti-corrosion material, which has low cost.
  • the biological cage structure 3 includes a mesh filler cage 305, a biofilm filler 304, and a porous partition 303.
  • the left and right sides of the biological cage 3 are porous chassis 306, with an opening rate of 30% and a hole diameter of 5 mm.
  • a square drive shaft buckle 307 is provided at the center of the porous chassis. The purpose of the square buckle is to make the packing cage drive The shaft rotates accordingly.
  • the biological turret 3 is connected to the drive motor 11 by a transverse drive shaft 6 in the center. The position of the drive shaft 6 is located 3 to 5cm above the inner liquid level 5.
  • the drive shaft can be adjusted according to the actual water drop situation of the biological turret 3. 6 position adjustment.
  • the mesh filler cage 305 is mostly made of stainless steel with higher strength.
  • the mesh cylindrical structure is conducive to uniform water distribution.
  • the opening rate is 80% and the pore size is 8mm.
  • One quarter of the mesh filler cage 305 is set to Open and close the cage body 301.
  • the opening and closing part is connected to the cage body through a stainless steel hinge 302 to facilitate the addition and replacement of the filler.
  • the stainless steel fixing buckle 9 and stainless steel butterfly bolts are welded to the biological cage 3. 901 for fixation.
  • Porous partitions 303 are provided at relative positions on the inner wall of the biological turret 3.
  • the porous partitions 303 are connected to the biological turret 3 through fixed slots on the left and right chassis, and can be increased or decreased according to the actual demand for the degree of oxygen drop. It is usually the same length as the biological cage 3, and the width is 1/5 of the diameter of the biological cage 3. Two rows of holes are opened at equal intervals, the opening rate is 65%, and the hole size is 5mm.
  • the biofilm filler 304 is a high-density polyethylene lightweight filler.
  • the biofilm filler 304 has a biofilm attached to its surface, and the filling rate is set to 50% of the effective volume of the reaction tank 2 .
  • the biofilm filler 304 can be used for microbial film culture before the device is operated, or activated sludge can be used in the biological cage 3 for microbial film culture.
  • the motor box 10 is mostly made of anti-corrosion stainless steel, and the motor box 10 is provided with a stainless steel hinge 7 for opening the cover.
  • the distribution box 15 is mostly made of anti-corrosion stainless steel.
  • the biological cage 3 is driven by the motor 11, and as the drive shaft 6 slowly rotates in the clockwise direction at a speed of 10 rpm, the porous partition 303 will partially rotate out of the water.
  • the biofilm filler 304 is carried out of the water surface 5. After reaching a certain height, the biofilm filler 304 carried out of the water surface by the porous partition 303 carries oxygen and falls to the water surface 5, and forms dissolved oxygen in falling water, completing the self-oxygenation process. At this time
  • the porous partition 303 at the opposite position below the water surface 5 brings another part of the biofilm filler 304 out of the water surface 5 to ensure the continuity of the self-oxygenation process and continue to provide sufficient dissolved oxygen for the reaction tank 2 .
  • part of the biofilm filler 304 is suspended below the water surface 5, which reduces the driving resistance of the motor 11 to a certain extent and further reduces the loss of electrical energy.
  • Part of the biofilm filler 304 far away from the water surface 5 is in an anoxic state, realizing the simultaneous occurrence of aerobic and anoxic reactions in a single reaction tank.
  • This embodiment only uses the driving energy consumption of the motor to achieve the self-oxygenation goal, and the average dissolved oxygen level reaches 8.5 mg/L, which reduces the consumption of aeration energy for oxygenation in the biological treatment process of sewage. Significantly reduces power consumption and operating costs in the sewage treatment process.
  • the core technology of the present invention is that during the slow rotation process of the biological cage 3 filled with biofilm filler 304, part of the filler leaves the water surface and falls into the water to form dissolved oxygen in the falling water, completing the self-oxygenation process and eliminating the need for sewage organisms.
  • the power consumed by the blast aeration system during the treatment process reduces operating costs.
  • the biofilm filler 304 has a large specific surface area, which is conducive to the attachment and growth of denitrifying microorganisms.
  • the unique structure of the biofilm filler 304 provides an excellent living environment for microorganisms.
  • biofilm filler 304 with a certain thickness can form aerobic-anoxic-anaerobic oxygen environment changes in the micro-environment, which helps to form synchronized nitrification and denitrification, improve denitrification efficiency, and effectively ensure the quality of effluent water. Meet the standards.
  • the rotation speed of the motor 11 and the immersion depth of the biological cage 3 of the present invention can be adjusted according to the actual oxygen demand and processing requirements. The operation is simple and the control mode is flexible. It can be flexibly combined with different processes according to the actual processing requirements and different processing scenarios.
  • the field of wastewater treatment has broad prospects.

Abstract

Disclosed in the present invention is an energy-saving self-oxygenation distributed biofilm sewage treatment apparatus, relating to the field of sewage treatment devices. The present invention comprises an integrated treatment apparatus housing, a reaction tank body and a rotating biological cage structure, wherein the rotating biological cage structure comprises a mesh filler cage body, biofilm fillers, and porous partitions which carry the biofilm fillers to fall into water for self-oxygenation. During the slow rotation of the rotating biological cage, the porous partitions carry the fillers to fall into water to realize a self-oxygenation process, thus solving the problem of energy consumption caused by air blowing and aeration used for sewage treatment at the current stage. The device of the present invention is simple and easy to operate, involves a self-oxygenation process with low energy consumption, and has a large biomass, a high load impact resistance and generally low operation costs. Therefore, the present invention is expected to be widely used in economically underdeveloped rural areas where there are great fluctuations in water quality and water quantity, dispersed distribution, and a lack of professionals to perform maintenance.

Description

一种节能自充氧分散式生物膜污水处理装置An energy-saving self-oxygenating dispersed biofilm sewage treatment device 技术领域Technical field
本发明涉及污水处理装置领域,具体涉及一种节能自充氧分散式生物膜污水处理装置。The invention relates to the field of sewage treatment devices, and in particular to an energy-saving self-oxygenating dispersed biofilm sewage treatment device.
背景技术Background technique
改革开放四十余年来,我国迅速发展,同时不断加大的环保力度也使环境污染现状得到改善,城镇污水处理率已达到97%以上。而作为一个农业大国,我国的农村污水处理系统却发展缓慢,农村地区的废水日产量约为2100万至2400万吨,并且随着国家新农村政策的实施,农村生活水平不断提升,农村废水日产量也不断增加。由于农村地域范围较广,人口分布较分散,不同地区村庄之间的发展情况等差异较大,导致生活污水的水质水量差异较大,并且存在随时间波动较大的现象,对污水处理系统产生较大冲击。目前已建成的农村污水处理站多交由村里维护,相对复杂的污水处理工艺在缺乏专业技术人员的农村并不适用,导致国内农村污水处理设施普遍存在闲置、停运等情况。此外,在基层财政紧张的情况下,现有的农村污水处理技术普遍具有运行能耗较高的特点,不利于农村污水处理设备的长期稳定运行。Over the past 40 years of reform and opening up, our country has developed rapidly. At the same time, increasing environmental protection efforts have also improved the current situation of environmental pollution. The urban sewage treatment rate has reached more than 97%. As a large agricultural country, my country's rural sewage treatment system has developed slowly. The daily output of wastewater in rural areas is about 21 million to 24 million tons. With the implementation of the country's new rural policy, rural living standards continue to improve, and rural wastewater daily output Production is also increasing. Due to the wide geographical scope of rural areas, the dispersed population distribution, and the large differences in development conditions between villages in different regions, the water quality and quantity of domestic sewage vary greatly and fluctuate greatly over time, which has a negative impact on the sewage treatment system. Big impact. Currently, rural sewage treatment stations that have been built are mostly maintained by the village. The relatively complex sewage treatment process is not applicable in rural areas where there is a lack of professional and technical personnel. As a result, domestic rural sewage treatment facilities are commonly idle and out of operation. In addition, under the circumstances of financial constraints at the grassroots level, existing rural sewage treatment technology generally has the characteristics of high energy consumption, which is not conducive to the long-term stable operation of rural sewage treatment equipment.
目前我国农村地区的小型分散式污水处理工艺主要采用A2O、氧化沟、MBBR(移动床生物膜反应器)、生物转盘、人工湿地、浮萍塘和生态滤池等。但现有技术普遍存在曝气过剩、能耗高、运行成本高、工艺复杂、维护难度大、占地面积大以及出水水质受进水波动影响大等问题。其中MBBR是一项与农村污水处理需求较匹配的技术,其原理是将悬浮填料作为生物膜载体,按照一定比例投入好/缺氧反应器中,悬浮填料在系统内的水流、曝气和搅拌作用下形成了流化状态,填料流化过程可以与污水充分接触,微生物较易在高比表面积的填料上附着生长,从而达到较好的处理效果。相较于生物转盘工艺生物膜易脱落、处理效率低、设备构造复杂维修困难等缺点,MBBR具有容积负荷高、脱氮效果好、生物膜抗负荷冲击能力强、占地面积小、生物量大等优势,目前在城镇污水厂应用 较广泛。At present, the small-scale decentralized sewage treatment processes in rural areas of my country mainly use A2O, oxidation ditch, MBBR (moving bed biofilm reactor), biological turntable, constructed wetland, duckweed pond and ecological filter. However, the existing technology has common problems such as excessive aeration, high energy consumption, high operating costs, complex processes, difficult maintenance, large floor space, and the outlet water quality is greatly affected by fluctuations in incoming water. Among them, MBBR is a technology that is more suitable for rural sewage treatment needs. Its principle is to use suspended fillers as biofilm carriers and put them into good/anoxic reactors according to a certain proportion. The suspended fillers are used for water flow, aeration and stirring in the system. A fluidized state is formed under the action of the filler. The fluidization process of the filler can fully contact the sewage. Microorganisms are more likely to attach and grow on the filler with a high specific surface area, thereby achieving better treatment results. Compared with the shortcomings of the biological turntable process, such as easy shedding of biofilm, low processing efficiency, complex equipment structure and difficulty in maintenance, MBBR has the characteristics of high volumetric load, good denitrification effect, strong biofilm resistance to load impact, small footprint, and large biomass. and other advantages, it is currently widely used in urban sewage plants.
目前的MBBR工艺多采用过量曝气的方式来满足出水水质要求,形成了较高的曝气能耗、运行成本和曝气设备运载负荷,提高了设备故障率及维护成本,如何将MBBR技术优势在低能耗、低运行成本的条件下应用于农村生活污水的处理成为亟待解决的问题。The current MBBR process mostly uses excessive aeration to meet the effluent quality requirements, resulting in higher aeration energy consumption, operating costs and aeration equipment carrying loads, which increases equipment failure rates and maintenance costs. How to use the advantages of MBBR technology Applying it to the treatment of rural domestic sewage under the conditions of low energy consumption and low operating cost has become an urgent problem to be solved.
发明内容Contents of the invention
针对现有农村污水处理技术存在的工艺复杂、需要专业人员维护、曝气能耗高、运行成本高的问题,本发明构建了一种节能自充氧分散式生物膜污水处理装置,可以很好地解决上述背景技术中提出的问题。In view of the problems existing in the existing rural sewage treatment technology, such as complicated processes, the need for professional maintenance, high aeration energy consumption, and high operating costs, the present invention constructs an energy-saving self-oxygenating dispersed biofilm sewage treatment device, which can effectively effectively solve the problems raised in the above background technology.
为解决上述问题,本发明采用技术方案如下:In order to solve the above problems, the present invention adopts the following technical solutions:
节能自充氧分散式生物膜污水处理装置,包括一体化壳体、顶部装有盖板的反应池、安装于反应池右侧的驱动电机箱、装于电机箱内部的驱动电机、安装于驱动电机上的驱动轴、安装于电机箱外的配电箱以及安装于驱动轴上的生物转笼。Energy-saving self-oxygenating dispersed biofilm sewage treatment device, including an integrated shell, a reaction tank with a cover on the top, a drive motor box installed on the right side of the reaction tank, a drive motor installed inside the motor box, and a drive motor installed on the drive The drive shaft on the motor, the distribution box installed outside the motor box, and the biological cage installed on the drive shaft.
所述生物转笼包括网状圆柱体填料笼及左右两侧多孔底盘,圆柱笼体为不锈钢材质,开孔率70%-80%,网状孔径大小为3-8mm,左右两侧多孔底盘开孔率30%-50%,孔径大小为3-5mm。The biological cage includes a mesh cylindrical packing cage and a porous chassis on the left and right sides. The cylindrical cage is made of stainless steel with an opening rate of 70%-80%. The mesh aperture size is 3-8mm. The porous chassis on the left and right sides are open. The porosity is 30%-50%, and the pore size is 3-5mm.
所述生物转笼包括笼内填料,填料附着生物膜用于生物脱氮,填料填充率为所述反应池有效容积的40%-80%。The biological cage includes filler in the cage. The filler is attached with biofilm for biological denitrification. The filler filling rate is 40%-80% of the effective volume of the reaction tank.
进一步地,所述生物转笼内壁相对应位置设有多孔隔板,隔板长度与圆柱笼体一致,宽度为笼体直径的1/6-1/4,开孔率60%-75%,孔径大小为3-5mm,隔板与左右两侧底盘连接处设置有固定卡槽,用于固定及拆卸隔板。Further, porous partitions are provided at corresponding positions on the inner wall of the biological cage. The length of the partitions is consistent with the cylindrical cage body, the width is 1/6-1/4 of the diameter of the cage body, and the opening rate is 60%-75%. The hole diameter is 3-5mm, and fixed slots are provided at the connection between the partition and the chassis on the left and right sides for fixing and removing the partition.
进一步地,所述生物转笼四分之一为可开合笼体,开合笼体一侧安装三个不锈钢合页与转笼相连,另一侧及转笼对应位置上焊接不锈钢固定卡扣,并配备不锈钢蝶形螺栓进行固定。所述生物转笼两侧底盘设有用于固定驱动轴的方形卡扣,开孔尺寸与驱动轴厚度相对应并通过螺栓紧锁于驱动轴上,生物转笼通过驱动轴与电机连接。Furthermore, a quarter of the biological tumbling cage is an openable and closable cage. Three stainless steel hinges are installed on one side of the opening and closing cage to connect with the tumbling cage. Stainless steel fixing buckles are welded on the other side and the corresponding position of the tumbling cage. , and equipped with stainless steel butterfly bolts for fixation. The chassis on both sides of the biological cage is provided with square buckles for fixing the drive shaft. The opening size corresponds to the thickness of the drive shaft and is locked on the drive shaft through bolts. The biological cage is connected to the motor through the drive shaft.
进一步地,所述顶部装有盖板的反应池安装可开盖不锈钢合页,便于观察及开盖检修。Furthermore, the reaction tank with a cover plate on the top is equipped with a stainless steel hinge that can be opened to facilitate observation, opening and maintenance.
进一步地,所述一体化壳体上部设置有进水管、溢流出水管,下部设置有放空管及排水管槽,可根据处理进出水模式及水位要求更改进出水管的位置和数量。Furthermore, the upper part of the integrated housing is provided with a water inlet pipe and an overflow outlet pipe, and the lower part is provided with a vent pipe and a drainage pipe groove. The position and number of the inlet and outlet pipes can be changed according to the water inlet and outlet mode and water level requirements.
进一步地,所述驱动电机箱顶盖安装有不锈钢合页,便于开盖检修。Furthermore, the top cover of the drive motor box is equipped with a stainless steel hinge to facilitate opening and maintenance.
进一步地,所述驱动电机应为慢速可调速电机,并且可采用太阳能驱动以进一步节约电能,降低运行费用。Furthermore, the drive motor should be a slow speed adjustable motor and can be driven by solar energy to further save electric energy and reduce operating costs.
上述节能自充氧分散式生物膜污水处理装置的反应池及生物转笼尺寸可根据实际污水处理水量需求进行合理设计调整,生物转笼内填料可根据处理要求及建造成本采用高密度聚乙烯、聚氨酯海绵、生物球填料等不同类型填料,同时网状圆柱笼体的开孔大小应不大于填料直径或最小边长。The size of the reaction tank and biological cage of the above-mentioned energy-saving self-oxygenating dispersed biofilm sewage treatment device can be reasonably designed and adjusted according to the actual sewage treatment water volume demand. The filler in the biological cage can be made of high-density polyethylene, Polyurethane sponge, bio-ball filler and other different types of fillers. At the same time, the opening size of the mesh cylindrical cage should not be larger than the filler diameter or the minimum side length.
相较于现有技术,本发明的有益效果如下:Compared with the existing technology, the beneficial effects of the present invention are as follows:
1.本发明的节能自充氧分散式生物膜污水处理装置通过填料笼缓慢旋转过程中,笼内的多孔隔板携部分生物填料离开水面,在电机驱动下缓慢旋转过程中,多孔隔板上的生物填料跌入反应池,并在跌落过程中带入空气中的氧气,实现反应池的自充氧过程。与此同时相对位置的多孔隔板已携另一部分生物填料进入空气中,可实现持续性的自充氧过程,并且可根据实际污水处理过程对溶解氧大小的不同要求,设计不同数量、不同位置的多孔隔板卡槽,通过增减隔板数量和安装隔板于不同位置实现溶解氧的调控。1. When the energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention slowly rotates through the filler cage, the porous partitions in the cage carry part of the biological filler out of the water surface, and during the slow rotation process driven by the motor, the porous partitions on the porous partitions The biological filler falls into the reaction pool, and brings in oxygen from the air during the falling process, realizing the self-oxygenation process of the reaction pool. At the same time, the porous partition at the opposite position has brought another part of the biological filler into the air, which can achieve a continuous self-oxygenation process, and different quantities and positions can be designed according to the different requirements for the size of dissolved oxygen in the actual sewage treatment process. The porous partition card slot allows the regulation of dissolved oxygen by increasing or decreasing the number of partitions and installing partitions at different positions.
2.本发明使用的生物膜填料比表面积大、生物量大、微生物生长空间充足,具有较强的抗负荷冲击能力,能较好的适应水质水量变化较大的农村生活污水。生物转笼在缓慢旋转充氧过程中,部分填料悬浮在水面上,减少了电机的驱动阻力,进一步节约能耗,降低运行成本。2. The biofilm filler used in the present invention has a large specific surface area, large biomass, sufficient space for microbial growth, strong load impact resistance, and can better adapt to rural domestic sewage with large changes in water quality and quantity. During the slow rotation and oxygenation process of the biological cage, part of the filler is suspended on the water surface, which reduces the driving resistance of the motor, further saves energy consumption and reduces operating costs.
3.本发明的可开合生物转笼为工作人员更换填料、维护检修提供了便利,生物转笼的浸没深度可根据不同处理要求和不同处理场景进行灵活设置,设备维护难度较低,对于村内非专业人士进行简单培训即可上岗。3. The openable and closable biological turret of the present invention provides convenience for staff to replace fillers and perform maintenance and repair. The immersion depth of the biological turret can be flexibly set according to different processing requirements and different processing scenarios. The difficulty of equipment maintenance is low. For the village Non-professionals can take up the job with simple training.
4.本发明的新型自充氧分散式生物膜污水处理装置,运行操作简单、设备少、故障率低、检修方便,摒弃传统鼓风曝气设备,极大地降低了运行能耗及运行成本。4. The new self-oxygenating dispersed biofilm sewage treatment device of the present invention has simple operation, less equipment, low failure rate, and convenient maintenance. It abandons traditional blasting and aeration equipment, which greatly reduces operating energy consumption and operating costs.
5.本发明的节能自充氧分散式生物膜污水处理装置适用性场景较灵活,可与其他处理工艺及不同类型的反应器进行灵活组合,以应用于基础经济水平落后、水质水量波动大、分布较分散的农村、偏远地区以及临时搭建的活动板房,在低能耗分散式污水处理领域将具有广阔的应用前景。5. The energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention is more flexible in applicability scenarios and can be flexibly combined with other treatment processes and different types of reactors to be used in areas with backward basic economic levels, large fluctuations in water quality and quantity, Scattered rural areas, remote areas and temporarily built prefabricated houses will have broad application prospects in the field of low energy consumption decentralized sewage treatment.
附图说明Description of the drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述所需使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,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的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used to describe the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some embodiments of the present invention and are not relevant to the present invention. For those of ordinary skill in the art, other drawings can also be obtained based on these drawings without exerting creative efforts.
图1是本发明的一种节能自充氧分散式生物膜污水处理装置的结构示意图;Figure 1 is a schematic structural diagram of an energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention;
图2是生物转笼打开状态俯视图;Figure 2 is a top view of the biological cage in the open state;
图3是生物转笼左视图;Figure 3 is the left side view of the biological cage;
图4是生物转笼转动过程中自充氧运行原理图。Figure 4 is a schematic diagram of the self-oxygenation operation during the rotation of the biological cage.
附图中标号说明如下:The labels in the drawings are explained as follows:
1-一体化处理装置壳体、2-反应池体、3-生物转笼、301-可开合网状填料笼体、302-笼体合页、303-多孔隔板、304-生物膜填料、305-网状笼体、306-多孔底盘、307-驱动轴卡扣、4-进水管、5-内液位、6-驱动轴、7-开盖合页、8-透明盖板、9-不锈钢固定卡扣、901-不锈钢蝶形螺栓、10-电机箱、11-驱动电机、12-溢流出水管、13-排空管、14-排水管槽、15-配电箱。1-Integrated treatment device shell, 2-Reaction tank body, 3-Biological cage, 301-Openable mesh packing cage, 302-Cage hinge, 303-Porous partition, 304-Biofilm filler , 305-mesh cage, 306-porous chassis, 307-drive shaft buckle, 4-water inlet pipe, 5-inner liquid level, 6-drive shaft, 7-opening hinge, 8-transparent cover, 9 -Stainless steel fixed buckle, 901-stainless steel butterfly bolt, 10-motor box, 11-driving motor, 12-overflow pipe, 13-drain pipe, 14-drainage pipe trough, 15-distribution box.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明的实施例,对本发明的技术方案进行清楚、完整地描述。显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are some, but not all, of the embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
请参阅图1-4,本发明的节能自充氧分散式生物膜污水处理装置,包括一体化处理装置壳体1、污水处理反应池体2、生物转笼结构3、位于电机箱10内的驱动电机11以及电机箱10外的配电箱15。Please refer to Figures 1-4. The energy-saving self-oxygenating dispersed biofilm sewage treatment device of the present invention includes an integrated treatment device housing 1, a sewage treatment reaction tank body 2, a biological cage structure 3, and a motor box located in the motor box 10. The drive motor 11 and the distribution box 15 outside the motor box 10 are driven.
反应池体2上设置有进水管4、溢流出水管12和排空管13并设置有可开合透明盖板8了,透明盖板的设置有利于对生物转笼3进行实时观察与开盖检修。反应池体2采用易加工的矩形池体,材质一般选用碳钢防腐材料,成本较低。The reaction tank body 2 is provided with an inlet pipe 4, an overflow outlet pipe 12 and an emptying pipe 13, and is provided with an openable and closable transparent cover 8. The arrangement of the transparent cover is conducive to real-time observation and opening of the biological cage 3. Overhaul. The reaction tank body 2 adopts an easy-to-process rectangular tank body, and the material is generally carbon steel anti-corrosion material, which has low cost.
生物转笼结构3包括网状填料笼体305、生物膜填料304、多孔隔板303。The biological cage structure 3 includes a mesh filler cage 305, a biofilm filler 304, and a porous partition 303.
其中,生物转笼3左右两侧为多孔底盘306,开孔率30%,孔径大小为5mm,多孔底盘盘心位置设置有方形驱动轴卡扣307,方形卡扣的目的是使填料笼在驱动轴的驱动下随之转动。生物转笼3由中心部位的一个横向驱动轴6与驱动电机11相连接,驱动轴6的位置位于内液位5位置上方3~5cm处,可根据实际生物转笼3跌水情况进行驱动轴6位置的调整。网状填料笼体305多采用强度较大的不锈钢材质,网状圆柱体结构有利于布水均匀,开孔率80%,孔径大小为8mm,四分之一的网状填料笼体305设置为开合笼体301,开合部分通过不锈钢合页302与笼体相连接,便于填料的投加及更换,关闭状态下通过焊接在生物转笼3上的不锈钢固定卡扣9和不锈钢蝶形螺栓901进行固定。生物转笼3内壁相对位置设置有多孔隔板303,多孔隔板303通过左右两侧底盘上的固定卡槽与生物转笼3连接,并可以根据实际对跌氧程度的需求进行增减,长度通常与生物转笼3长度一致,宽度为生物转笼3直径的1/5,等间距开两排孔,开孔率65%,孔径大小为5mm。Among them, the left and right sides of the biological cage 3 are porous chassis 306, with an opening rate of 30% and a hole diameter of 5 mm. A square drive shaft buckle 307 is provided at the center of the porous chassis. The purpose of the square buckle is to make the packing cage drive The shaft rotates accordingly. The biological turret 3 is connected to the drive motor 11 by a transverse drive shaft 6 in the center. The position of the drive shaft 6 is located 3 to 5cm above the inner liquid level 5. The drive shaft can be adjusted according to the actual water drop situation of the biological turret 3. 6 position adjustment. The mesh filler cage 305 is mostly made of stainless steel with higher strength. The mesh cylindrical structure is conducive to uniform water distribution. The opening rate is 80% and the pore size is 8mm. One quarter of the mesh filler cage 305 is set to Open and close the cage body 301. The opening and closing part is connected to the cage body through a stainless steel hinge 302 to facilitate the addition and replacement of the filler. In the closed state, the stainless steel fixing buckle 9 and stainless steel butterfly bolts are welded to the biological cage 3. 901 for fixation. Porous partitions 303 are provided at relative positions on the inner wall of the biological turret 3. The porous partitions 303 are connected to the biological turret 3 through fixed slots on the left and right chassis, and can be increased or decreased according to the actual demand for the degree of oxygen drop. It is usually the same length as the biological cage 3, and the width is 1/5 of the diameter of the biological cage 3. Two rows of holes are opened at equal intervals, the opening rate is 65%, and the hole size is 5mm.
生物膜填料304为高密度聚乙烯轻质填料,生物膜填料304表面附着生物膜,填充率设置为反应池2有效容积的50%。生物膜填料304可在装置运行前进行微生物挂膜培养,也可在生物转笼3内利用活性污泥进行微生物挂膜培养。The biofilm filler 304 is a high-density polyethylene lightweight filler. The biofilm filler 304 has a biofilm attached to its surface, and the filling rate is set to 50% of the effective volume of the reaction tank 2 . The biofilm filler 304 can be used for microbial film culture before the device is operated, or activated sludge can be used in the biological cage 3 for microbial film culture.
电机箱10多采用防腐不锈钢材质,电机箱10设置有开盖不锈钢合页7。配电箱15多采用防腐不锈钢材质。The motor box 10 is mostly made of anti-corrosion stainless steel, and the motor box 10 is provided with a stainless steel hinge 7 for opening the cover. The distribution box 15 is mostly made of anti-corrosion stainless steel.
如图4所示:生物转笼3在电机11驱动下,随着驱动轴6沿顺时针方向缓慢旋转,转速为10转/分种,多孔隔板303在转出水面的过程中会将部分生物膜填料304携出水面5,转至一定高度后,被多孔隔板303携出水面的生物膜填料304携带氧气跌落至水面5,并形成跌水溶解氧,完 成自充氧过程,此时水面5以下的相对位置的多孔隔板303又将另一部分生物膜填料304携出水面5,保证自充氧过程的连续性,持续为反应池2提供充足的溶解氧。在生物转笼3缓慢旋转的过程中,部分生物膜填料304悬浮在水面5以下,一定程度上减少了电机11的驱动阻力,进一步减少电能的损耗。远离水面5的部分生物膜填料304处于缺氧状态,实现了单一反应池中好氧与缺氧反应的同步发生。As shown in Figure 4: the biological cage 3 is driven by the motor 11, and as the drive shaft 6 slowly rotates in the clockwise direction at a speed of 10 rpm, the porous partition 303 will partially rotate out of the water. The biofilm filler 304 is carried out of the water surface 5. After reaching a certain height, the biofilm filler 304 carried out of the water surface by the porous partition 303 carries oxygen and falls to the water surface 5, and forms dissolved oxygen in falling water, completing the self-oxygenation process. At this time The porous partition 303 at the opposite position below the water surface 5 brings another part of the biofilm filler 304 out of the water surface 5 to ensure the continuity of the self-oxygenation process and continue to provide sufficient dissolved oxygen for the reaction tank 2 . During the slow rotation of the biological cage 3, part of the biofilm filler 304 is suspended below the water surface 5, which reduces the driving resistance of the motor 11 to a certain extent and further reduces the loss of electrical energy. Part of the biofilm filler 304 far away from the water surface 5 is in an anoxic state, realizing the simultaneous occurrence of aerobic and anoxic reactions in a single reaction tank.
本实施例仅用电机的驱动能耗,实现了自充氧目标,平均溶解氧水平达到了8.5mg/L,减少了污水生物处理过程中消耗较多曝气能耗进行充氧这一环节,大幅降低了污水处理过程中的电能消耗和运行成本。This embodiment only uses the driving energy consumption of the motor to achieve the self-oxygenation goal, and the average dissolved oxygen level reaches 8.5 mg/L, which reduces the consumption of aeration energy for oxygenation in the biological treatment process of sewage. Significantly reduces power consumption and operating costs in the sewage treatment process.
本发明的核心技术为通过填加生物膜填料304的生物转笼3在缓慢旋转过程中,携带部分填料离开水面并跌落水中,形成跌水溶解氧,完成自充氧过程,省去了污水生物处理过程中鼓风曝气系统消耗的电能,降低了运行成本。生物膜填料304具有较大的比表面积,有利于脱氮微生物附着生长,生物膜填料304特有的结构为微生物提供了优良的生存环境,生物量大、微生物群落丰富度高,使微生物具有较强的抗冲击能力,具有一定厚度的生物膜填料304可在微观环境上形成好氧-缺氧-厌氧的氧环境变化,有助于形成同步硝化返硝化,提高脱氮效率,有效保证出水水质达标。本发明的电机11转速和生物转笼3浸没深度可根据实际需氧量和处理要求进行调整,运行操作简单,调控方式灵活,可根据实际处理要求和不同处理场景与不同工艺灵活组合,在分散式污水处理领域具有广阔前景。The core technology of the present invention is that during the slow rotation process of the biological cage 3 filled with biofilm filler 304, part of the filler leaves the water surface and falls into the water to form dissolved oxygen in the falling water, completing the self-oxygenation process and eliminating the need for sewage organisms. The power consumed by the blast aeration system during the treatment process reduces operating costs. The biofilm filler 304 has a large specific surface area, which is conducive to the attachment and growth of denitrifying microorganisms. The unique structure of the biofilm filler 304 provides an excellent living environment for microorganisms. The large biomass and high microbial community richness make the microorganisms have strong The impact resistance of biofilm filler 304 with a certain thickness can form aerobic-anoxic-anaerobic oxygen environment changes in the micro-environment, which helps to form synchronized nitrification and denitrification, improve denitrification efficiency, and effectively ensure the quality of effluent water. Meet the standards. The rotation speed of the motor 11 and the immersion depth of the biological cage 3 of the present invention can be adjusted according to the actual oxygen demand and processing requirements. The operation is simple and the control mode is flexible. It can be flexibly combined with different processes according to the actual processing requirements and different processing scenarios. The field of wastewater treatment has broad prospects.
以上所述,仅为本发明的优选实施方式,优选实施例并没有详尽叙述所有细节,本发明的保护范围并不仅局限于上述实施例,包括权利要求书中的技术特征,凡属于此发明思路下的技术方案均属于本发明的保护范围。应当指出,对于本技术领域的技术人员来说,在不脱离本发明原理的任何改进也视为本发明的保护范围。The above are only the preferred embodiments of the present invention. The preferred embodiments do not describe all the details in detail. The protection scope of the present invention is not limited to the above-mentioned embodiments, including the technical features in the claims. All belonging to this inventive idea The following technical solutions all belong to the protection scope of the present invention. It should be noted that for those skilled in the art, any modifications that do not depart from the principle of the present invention are also considered to be within the protection scope of the present invention.

Claims (5)

  1. 一种节能自充氧分散式生物膜污水处理装置,包括一体化处理装置壳体(1)、污水处理反应池体(2)、生物转笼结构(3)包括网状填料笼体(305)以及填充在其内部的生物膜填料(304)、安装于电机箱(10)内的驱动电机(11)、配电箱(15),其特征在于:An energy-saving self-oxygenating dispersed biofilm sewage treatment device, including an integrated treatment device shell (1), a sewage treatment reaction tank body (2), a biological cage structure (3) including a mesh filler cage (305) As well as the biofilm filler (304) filled inside, the drive motor (11) and the distribution box (15) installed in the motor box (10), it is characterized by:
    所述生物转笼(3)中心设置有横向驱动轴(6),横向左右两侧为盘心位置有方形驱动轴卡扣(307)的多孔底盘(306);所述网状填料笼体(305)为网状圆柱体,填充了生物膜填料(304),设置有安装了合页(302)的可开合笼体(301),开合部位通过固定卡扣(9)和蝶形螺栓(901)与笼体连接,笼体内壁设置有通过固定卡槽与笼体相连接的多孔隔板(303)。The biological cage (3) is provided with a transverse driving shaft (6) in the center, and the left and right sides of the biological cage (3) are porous chassis (306) with square driving shaft buckles (307) at the center of the disk; the mesh filler cage ( 305) is a mesh cylinder filled with biofilm filler (304), and is provided with an openable and closable cage (301) equipped with a hinge (302). The opening and closing parts are fixed with buckles (9) and butterfly bolts. (901) is connected to the cage body, and the inner wall of the cage is provided with a porous partition (303) connected to the cage body through fixed slots.
  2. 根据权利要求1所述的一种节能自充氧分散式生物膜污水处理装置,其特征在于,所述一体化处理装置壳体(1)底部设置有横向排水管槽(14),集成安装有污水处理反应池体(2)、电机箱(10)及配电箱(15)。An energy-saving self-oxygenating dispersed biofilm sewage treatment device according to claim 1, characterized in that a transverse drainage pipe groove (14) is provided at the bottom of the housing (1) of the integrated treatment device, and is integrated with a Sewage treatment reaction tank body (2), motor box (10) and distribution box (15).
  3. 根据权利要求1所述的一种节能自充氧分散式生物膜污水处理装置,其特征在于,所述污水处理反应池体(2)一侧设置有进水管(4),另一侧上端设置有溢流出水管(12)、下端设置有排空管(13),池体顶部设置有可开合盖板(8)。An energy-saving self-oxygenating dispersed biofilm sewage treatment device according to claim 1, characterized in that the sewage treatment reaction tank body (2) is provided with a water inlet pipe (4) on one side, and is provided with a water inlet pipe (4) on the upper end of the other side. There is an overflow outflow pipe (12), a drain pipe (13) at the lower end, and an openable cover plate (8) at the top of the pool body.
  4. 根据权利要求1所述的一种节能自充氧分散式生物膜污水处理装置,其特征在于,所述多孔底盘(306)开孔率30%-50%,孔径3-5mm;所述网状填料笼体(305)开孔率70%-80%,孔径3-8mm;所述多孔隔板(303)数量至少一个,宽度为填料笼体(305)直径的1/6-1/4,开孔率60%-75%,孔径3-5mm。An energy-saving self-oxygenating dispersed biofilm sewage treatment device according to claim 1, characterized in that the porous chassis (306) has an opening rate of 30%-50% and a pore diameter of 3-5mm; The opening rate of the packing cage (305) is 70%-80%, and the pore diameter is 3-8mm; the number of said porous partitions (303) is at least one, and the width is 1/6-1/4 of the diameter of the packing cage (305). The opening rate is 60%-75%, and the hole diameter is 3-5mm.
  5. 根据权利要求1所述的一种节能自充氧分散式生物膜污水处理装置,其特征在于,所述生物膜填料(304)种类可设置为高密度聚乙烯轻质填料、聚氨酯海绵填料、生物球填料。An energy-saving self-oxygenating dispersed biofilm sewage treatment device according to claim 1, characterized in that the type of biofilm filler (304) can be set to high-density polyethylene lightweight filler, polyurethane sponge filler, biofilm filler, etc. Ball filler.
PCT/CN2022/137840 2022-04-12 2022-12-09 Energy-saving self-oxygenation distributed biofilm sewage treatment apparatus WO2023197640A1 (en)

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