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CN111675312A - A pilot-scale experimental device for a column MBR system - Google Patents

A pilot-scale experimental device for a column MBR system Download PDF

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CN111675312A
CN111675312A CN202010667698.8A CN202010667698A CN111675312A CN 111675312 A CN111675312 A CN 111675312A CN 202010667698 A CN202010667698 A CN 202010667698A CN 111675312 A CN111675312 A CN 111675312A
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tank
water
membrane
mbr
water tank
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张佳乐
林振锋
虞晓春
王红专
刘春玲
陈浩
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Suzhou Sujing New Materials In Environmental Protection Co ltd
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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
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • 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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • 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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  • Biodiversity & Conservation Biology (AREA)
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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本发明公开一种柱式MBR系统中试实验装置,用于测试MBR膜的过滤性能,其包括膜池水箱、原水箱、产水箱、反洗组件、污泥回流泵和曝气组件,由于本发明设置了连接产水箱和原水箱的回流管道,产水箱中净水可以回流至原水箱,再通过原水箱进入膜池水箱,使得膜池水箱内的原水能够保持浓度不变,以模拟MBR膜的实际过滤情况。曝气组件除了能够清洁MBR膜,还能够充分将原水中的沉淀搅匀,给予MBR膜一个稳定的测试环境。

Figure 202010667698

The invention discloses a pilot-scale experimental device for a column MBR system, which is used for testing the filtration performance of an MBR membrane. The invention sets up a return pipe connecting the production water tank and the original water tank, and the purified water in the water production tank can return to the original water tank, and then enter the membrane tank water tank through the original water tank, so that the raw water in the membrane tank water tank can keep the concentration unchanged, so as to simulate the MBR membrane. the actual filtering situation. In addition to cleaning the MBR membrane, the aeration module can also fully stir the sediment in the raw water, giving the MBR membrane a stable test environment.

Figure 202010667698

Description

一种柱式MBR系统中试实验装置A pilot-scale experimental device for a column MBR system

技术领域technical field

本发明涉及水处理领域,特别是一种柱式MBR系统中试实验装置。The invention relates to the field of water treatment, in particular to a pilot-scale experimental device of a column-type MBR system.

背景技术Background technique

膜生物反应器Membrane Bio-Reactor (简称MBR),是一种由膜分离单元与生物处理单元相结合的水处理技术。目前这种水处理技术正在被越来越广泛使用。Membrane Bio-Reactor (MBR for short) is a water treatment technology that combines a membrane separation unit with a biological treatment unit. At present, this water treatment technology is being used more and more widely.

但是,一些采用新配方生产的MBR膜产品,出厂未对其进行细致的参数测试,在后期项目投入使用过程中,由于前期数据收集不充分,膜产品对不同水质的适应性有较大的不同,及易造成组件通量的衰减,对后续的操作运行产生影响,从而造成水质不达标的问题。However, some MBR membrane products produced with new formulas have not undergone detailed parameter testing before leaving the factory. In the process of putting into use in the later project, due to insufficient data collection in the early stage, the adaptability of membrane products to different water quality is quite different. , and it is easy to cause the attenuation of the component flux, which will affect the subsequent operation and operation, resulting in the problem of substandard water quality.

目前的测试装置需要在污水产生地建造占地面积大的试验设备,针对具体的污水进行试验,建造和运行成本居高不下,不利于推广普及,具有诸多不足之处。The current testing device needs to build a large area of test equipment in the place where the sewage is generated, and conduct tests for specific sewage. The construction and operation costs remain high, which is not conducive to popularization and has many shortcomings.

因此,目前需要一种能够克服上述问题的柱式MBR系统中试实验装置。Therefore, there is currently a need for a pilot-scale experimental device for a column-type MBR system that can overcome the above-mentioned problems.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种能够采用少量污水进行试验并且方便的柱式MBR系统中试实验装置。The purpose of the present invention is to provide a pilot-scale experimental device for a column MBR system that can be tested with a small amount of sewage and is convenient.

为达到上述目的,本发明采用的技术方案是:一种柱式MBR系统中试实验装置,用于测试MBR膜的过滤性能,其包括膜池水箱、原水箱、产水箱、反洗组件、污泥回流泵和曝气组件,所述膜池水箱内设置有滤膜组件,所述膜池水箱上具有连接所述原水箱的原水入口、连接所述产水箱的产水出口、连接所述曝气组件的曝气口和连接污泥回流泵的污泥回流口,所述产水出口和所述产水箱之间设置有自吸泵,所述产水箱上设置有连接原水箱的回流管道,所述产水出口设置有检测压力和流量的检测组件。In order to achieve the above object, the technical scheme adopted in the present invention is: a pilot-scale experimental device of a column MBR system for testing the filtration performance of the MBR membrane, which includes a membrane tank water tank, a raw water tank, a water production tank, a backwash component, a sewage A mud return pump and an aeration assembly, the membrane tank water tank is provided with a filter membrane assembly, and the membrane tank water tank has a raw water inlet connected to the raw water tank, a produced water outlet connected to the water production tank, and a water outlet connected to the aeration tank. The aeration port of the air component and the sludge return port connected to the sludge return pump, a self-priming pump is arranged between the water production outlet and the water production tank, and the water production tank is provided with a return pipe connected to the original water tank, The produced water outlet is provided with a detection component for detecting pressure and flow.

优选地,所述实验装置还包括连接所述检测组件的报警装置,当检测组件的检测到的压力和流量达到或超过设定数值时报警装置发出提示信息。Preferably, the experimental device further includes an alarm device connected to the detection component, and the alarm device sends out a prompt message when the detected pressure and flow of the detection component reach or exceed a set value.

优选地,所述实验装置其还包括支架,所述膜池水箱、所述产水箱、所述反洗组件和所述曝气组件均设置在所述支架上,所述原水箱可拆卸设置在所述支架的侧部。Preferably, the experimental device further includes a bracket, the membrane tank water tank, the water production tank, the backwash component and the aeration component are all arranged on the bracket, and the raw water tank is detachably arranged on the the side of the bracket.

进一步优选地,所述产水箱设置在所述支架的上部。Further preferably, the water production tank is arranged on the upper part of the bracket.

优选地,所述膜池水箱、所述产水箱、所述反洗组件和所述曝气组件与管道的连接方式均为可拆卸连接。Preferably, the connection modes of the membrane tank water tank, the production water tank, the backwashing component and the aeration component and the pipeline are all detachable connections.

优选地,所述滤膜组件包括与所述产水箱固定连接的管道架和与所述管道架可拆卸连接的MBR膜架,所述MBR膜架上固定设置有所述MBR膜。Preferably, the filter membrane assembly includes a pipe frame fixedly connected to the water production tank and an MBR membrane frame detachably connected to the pipe frame, and the MBR membrane is fixed on the MBR membrane frame.

进一步优选地,所述产水箱的侧壁设置有滑动轨道,所述MBR膜架滑动设置在所述滑动轨道上。Further preferably, the side wall of the water production tank is provided with a sliding track, and the MBR film frame is slidably arranged on the sliding track.

优选地,所述反洗组件包括反洗泵和加药装置,所述反洗泵的入口和出口分别连接所述产水箱和所述产水出口。Preferably, the backwashing assembly includes a backwashing pump and a dosing device, and the inlet and the outlet of the backwashing pump are respectively connected to the produced water tank and the produced water outlet.

由于上述技术方案运用,本发明与现有技术相比具有下列优点:Due to the application of the above-mentioned technical solutions, the present invention has the following advantages compared with the prior art:

由于本发明设置了连接产水箱和原水箱的回流管道,产水箱中净水可以回流至原水箱,再通过原水箱进入膜池水箱,使得膜池水箱内的原水能够保持浓度不变,以模拟MBR膜的实际过滤情况。曝气组件除了能够清洁MBR膜,还能够充分将原水中的沉淀搅匀,给予MBR膜一个稳定的测试环境。由此,本发明的实验装置无需大量的原水即可对MBR膜的性能进行长时间的测试,只需要将少量原水运送到测试地点既可完成长时间的MBR膜测试,无需到原水地建造成本昂贵的试验装置。Since the present invention is provided with a return pipeline connecting the production water tank and the original water tank, the purified water in the produced water tank can return to the original water tank, and then enter the membrane tank water tank through the original water tank, so that the raw water in the membrane tank water tank can keep the concentration unchanged, so as to simulate Actual filtration of MBR membranes. In addition to cleaning the MBR membrane, the aeration component can fully stir the sediment in the raw water, giving the MBR membrane a stable test environment. Therefore, the experimental device of the present invention can perform a long-term test on the performance of the MBR membrane without a large amount of raw water, and only need to transport a small amount of raw water to the test site to complete the long-term MBR membrane test, without the need to go to the raw water site to build the cost. Expensive test setup.

本发明的实验装置通过支架支撑,结构较小,也可以根据需要运送至原水地,对MBR膜的性能进行测试。The experimental device of the present invention is supported by a bracket, has a small structure, and can also be transported to a raw water site as required to test the performance of the MBR membrane.

本发明的实验装置的管道架和MBR膜架可拆卸连接,能够在保证密封性能的前提下用于测试不同的MBR膜,并且更换MBR膜相传统试验装置更为简单高效。The pipe frame and the MBR film frame of the experimental device of the invention can be detachably connected, which can be used to test different MBR films on the premise of ensuring the sealing performance, and the replacement of the MBR film is simpler and more efficient than the traditional experimental device.

附图说明Description of drawings

附图1为本发明的原理示意图。1 is a schematic diagram of the principle of the present invention.

以上附图中:1、膜池水箱;11、原水入口;12、产水出口;13、曝气口;14、污泥回流口;2、原水箱;3、产水箱;4、曝气组件;5、污泥回流泵;6、自吸泵;7、回流管道;81、反洗泵;82、酸加药桶;83、酸计量泵;84、碱加药桶;85、碱计量泵。In the above drawings: 1. Membrane tank water tank; 11. Raw water inlet; 12. Produced water outlet; 13. Aeration port; 14. Sludge return port; 2. Raw water tank; 3. Production water tank; 4. Aeration assembly ;5, sludge return pump; 6, self-priming pump; 7, return pipeline; 81, backwash pump; 82, acid dosing barrel; 83, acid metering pump; 84, alkali dosing barrel; 85, alkali metering pump .

具体实施方式Detailed ways

下面结合附图所示的实施例对本发明作进一步描述:The present invention will be further described below in conjunction with the embodiments shown in the accompanying drawings:

参见附图1所示,一种柱式MBR系统中试实验装置,用于测试MBR膜的过滤性能,其包括膜池水箱1、原水箱2、产水箱3、反洗组件和曝气组件4,膜池水箱1内设置有滤膜组件(图中未表示),膜池水箱1上具有连接原水箱2的原水入口11、连接产水箱3的产水出口12、连接曝气组件4的曝气口13和连接污泥回流泵5的污泥回流口14,产水出口12和产水箱3之间设置有自吸泵6,产水箱3上设置有连接原水箱2的回流管道7,产水出口12设置有检测压力和流量的检测组件(图中未表示)。Referring to Figure 1, a pilot-scale experimental device for a column MBR system is used to test the filtration performance of MBR membranes, which includes a membrane tank water tank 1, a raw water tank 2, a production water tank 3, a backwash component and an aeration component 4 The membrane tank 1 is provided with a membrane filter assembly (not shown in the figure). The air port 13 and the sludge return port 14 connected to the sludge return pump 5, the self-priming pump 6 is arranged between the produced water outlet 12 and the water production tank 3, and the water production tank 3 is provided with a return pipe 7 connected to the original water tank 2, The water outlet 12 is provided with a detection component (not shown in the figure) for detecting pressure and flow.

反洗组件包括反洗泵81、酸加药桶82、酸计量泵83、碱加药桶84和碱计量泵85,反洗泵81的入口和出口分别连接产水箱3和产水出口12,反洗组件根据设定对滤膜组件进行反洗,以模拟实际使用情况下的反洗步骤。The backwash assembly includes a backwash pump 81, an acid dosing barrel 82, an acid metering pump 83, an alkali dosing barrel 84 and an alkali metering pump 85. The inlet and outlet of the backwash pump 81 are respectively connected to the water production tank 3 and the water production outlet 12, The backwash module backwashes the membrane module according to the settings to simulate the backwash steps in actual use.

本实施例工作时,将需要测试的MBR膜安装至膜池水箱1,将对应的原水加入原水箱2,原水从原水箱2流入膜池水箱1,启动自吸泵6和曝气组件4,自吸泵6为产水出口12提供负压,膜池水箱1内的原水通过滤膜组件过滤后的净水通过自吸泵6后进入产水箱3,曝气组件4在膜池水箱1的底部通入气体,气体上浮产生的抖动用于清洁滤膜组件,产水箱3中的净水通过回流管道7重新进入原水箱2,再进入膜池水箱1,使得膜池水箱内的原水的浓度保持不变,如果膜池水箱1中的原水浓度变化过大,可以采用污泥回流泵5用于抽取膜池水箱1中的部分污泥,以保持浓度。当检测组件检测到产水出口12的运行负压≥0.04Mpa时,或者产水通量衰减率超过20%时,则说明MBR膜发生污堵,进水水质不适合该膜组件稳定运行,本实施例的检测数值为跟据MBR膜类型和原水水质决定,在其他实施例中,可以跟据需要进行调整。When the present embodiment works, the MBR membrane to be tested is installed in the membrane tank water tank 1, the corresponding raw water is added to the original water tank 2, the raw water flows into the membrane tank water tank 1 from the original water tank 2, and the self-priming pump 6 and the aeration assembly 4 are activated, The self-priming pump 6 provides negative pressure for the outlet 12 of the produced water. The raw water in the membrane tank 1 passes through the filter membrane module and the purified water passes through the self-priming pump 6 and then enters the water production tank 3. The aeration module 4 is placed in the membrane tank 1. Gas is introduced into the bottom, and the vibration generated by the gas floating is used to clean the filter membrane module. The purified water in the water production tank 3 re-enters the raw water tank 2 through the return pipe 7, and then enters the membrane tank water tank 1, so that the concentration of the raw water in the membrane tank water tank is increased. Remaining unchanged, if the concentration of raw water in the membrane tank 1 changes too much, the sludge return pump 5 can be used to extract part of the sludge in the membrane tank 1 to maintain the concentration. When the detection module detects that the operating negative pressure of the permeate outlet 12 is greater than or equal to 0.04Mpa, or the permeate flux decay rate exceeds 20%, it means that the MBR membrane is fouled and the influent water quality is not suitable for the stable operation of the membrane module. The detection value of the embodiment is determined according to the type of the MBR membrane and the quality of the raw water. In other embodiments, it can be adjusted as needed.

由于本实施例设置了连接产水箱3和原水箱2的回流管道7,产水箱3中净水可以回流至原水箱2,再通过原水箱2进入膜池水箱1,使得膜池水箱1内的原水能够保持浓度不变,以模拟MBR膜的实际过滤情况。曝气组件4除了能够清洁MBR膜,还能够充分将原水中的沉淀搅匀,给予MBR膜一个稳定的测试环境。由此,本实施例的实验装置无需大量的原水即可对MBR膜的性能进行长时间的测试,只需要将少量原水运送到测试地点既可完成长时间的MBR膜测试,无需到原水地建造成本昂贵的试验装置,能够大幅度降低MBR膜测试的成本。Since the present embodiment is provided with a return pipeline 7 connecting the produced water tank 3 and the raw water tank 2, the purified water in the produced water tank 3 can return to the raw water tank 2, and then enter the membrane tank water tank 1 through the raw water tank 2, so that the water in the membrane tank water tank 1 The raw water can keep the concentration constant to simulate the actual filtration of the MBR membrane. In addition to cleaning the MBR membrane, the aeration module 4 can also fully stir the sediment in the raw water to give the MBR membrane a stable test environment. Therefore, the experimental device of this embodiment can test the performance of the MBR membrane for a long time without a large amount of raw water. It only needs to transport a small amount of raw water to the test site to complete the long-term MBR membrane test, and there is no need to construct the raw water site. The expensive test device can greatly reduce the cost of MBR film testing.

为了方便操作,实验装置还包括连接检测组件的报警装置,当检测组件的检测到的压力和流量达到或超过设定数值时报警装置发出提示信息。报警装置可以根据需要采用合适的设备,本实施例中采用PLC电路作为报警装置。In order to facilitate the operation, the experimental device also includes an alarm device connected to the detection component. When the detected pressure and flow of the detection component reach or exceed the set value, the alarm device will issue a prompt message. The alarm device can use appropriate equipment as required, and in this embodiment, a PLC circuit is used as the alarm device.

实验装置其还包括支架(图中未表示),膜池水箱1、产水箱3、反洗组件和曝气组件4均设置在支架上,原水箱2可拆卸设置在支架的侧部。并且,产水箱3设置在支架的上部,产水箱3中的水流可以通过重力进入原水箱2体中,并且可以跟据产水速度调节进入原水箱2的水流速度,以保证膜池水箱1内的原水浓度。本实施例的实验装置通过支架支撑,整体结构较小,以方便运输,在需要时候可以跟据需要运送至原水地,对MBR膜的性能进行测试。The experimental device also includes a bracket (not shown in the figure), the membrane tank water tank 1, the production water tank 3, the backwash component and the aeration component 4 are all arranged on the bracket, and the raw water tank 2 is detachably arranged on the side of the bracket. Moreover, the water production tank 3 is arranged on the upper part of the bracket, the water flow in the water production tank 3 can enter the raw water tank 2 by gravity, and the water flow speed into the raw water tank 2 can be adjusted according to the water production speed to ensure that the membrane tank 1 is in the water tank 1. raw water concentration. The experimental device of this embodiment is supported by a bracket, and the overall structure is small to facilitate transportation. When necessary, it can be transported to the original water site to test the performance of the MBR membrane.

本实施例中,膜池水箱1、产水箱3、反洗组件和曝气组件4与管道的连接方式均为可拆卸连接。由于本实施的装置为实验装置,容易发生故障,可拆卸的连接方式能够方便更换和维修。In this embodiment, the membrane tank water tank 1, the water production tank 3, the backwash component and the aeration component 4 are all connected in a detachable manner to the pipeline. Since the device in this embodiment is an experimental device, it is prone to failure, and the detachable connection mode can facilitate replacement and maintenance.

本实施例中,滤膜组件包括与产水箱3固定连接的管道架和与管道架可拆卸连接的MBR膜架,MBR膜架上固定设置有MBR膜,由于,只需要提前将MBR膜固定在不同的MBR膜架上,既可方便不同MBR膜的测试。In this embodiment, the filter membrane assembly includes a pipe frame fixedly connected to the water production tank 3 and an MBR membrane frame detachably connected to the pipe frame. The MBR membrane frame is fixedly provided with an MBR membrane, because it is only necessary to fix the MBR membrane in advance. On different MBR membrane holders, it is convenient to test different MBR membranes.

本发明的实验装置的管道架和MBR膜架可拆卸连接,能够在保证密封性能的前提下用于测试不同的MBR膜,并且产水箱3的侧壁设置有滑动轨道,MBR膜架滑动设置在滑动轨道上,能够方便MBR膜架的安装。The pipe frame and the MBR film frame of the experimental device of the present invention are detachably connected, which can be used to test different MBR films on the premise of ensuring the sealing performance, and the side wall of the water production tank 3 is provided with a sliding track, and the MBR film frame is slidably arranged on the On the sliding track, it is convenient to install the MBR film frame.

上述实施例只为说明本发明的技术构思及特点,其目的在于让熟悉此项技术的人士能够了解本发明的内容并据以实施,并不能以此限制本发明的保护范围。凡根据本发明精神实质所作的等效变化或修饰,都应涵盖在本发明的保护范围之内。The above-mentioned embodiments are only intended to illustrate the technical concept and characteristics of the present invention, and the purpose thereof is to enable those who are familiar with the art to understand the content of the present invention and implement them accordingly, and cannot limit the protection scope of the present invention. All equivalent changes or modifications made according to the spirit of the present invention should be included within the protection scope of the present invention.

Claims (8)

1. The utility model provides a pilot scale experimental apparatus of column type MBR system for the filtering quality of test MBR membrane, it includes membrane cisterna water tank, former water tank, produces the water tank, backwash subassembly, mud backwash pump and aeration subassembly, be provided with the filter membrane subassembly in the membrane cisterna water tank, have on the membrane cisterna water tank and connect the raw water entry of former water tank, connect produce the water outlet of water tank, connect the aeration mouth of aeration subassembly and the mud backward flow mouth of connecting mud backwash pump, produce the water outlet with produce and be provided with self priming pump, its characterized in that between the water tank: the water production tank is provided with a return pipeline connected with the original water tank, and the water production outlet is provided with a detection assembly for detecting pressure and flow.
2. The pilot plant experimental facility of the column MBR system of claim 1, wherein: the experimental device also comprises an alarm device connected with the detection assembly, and the alarm device sends prompt information when the detected pressure and flow of the detection assembly reach or exceed set values.
3. The pilot plant experimental facility of the column MBR system of claim 1, wherein: the experimental device further comprises a support, the membrane pool water tank, the water production tank, the backwashing component and the aeration component are all arranged on the support, and the raw water tank is detachably arranged on the side portion of the support.
4. The pilot plant experimental facility of the column MBR system of claim 3, wherein: the water production tank is arranged at the upper part of the bracket.
5. The pilot plant experimental facility of the column MBR system of claim 1, wherein: the membrane tank, the water production tank, the backwashing component and the aeration component are detachably connected with the pipeline.
6. The pilot plant experimental facility of the column MBR system of claim 1, wherein: the filter membrane component comprises a pipeline frame fixedly connected with the water production tank and an MBR membrane frame detachably connected with the pipeline frame, and the MBR membrane frame is fixedly provided with the MBR membrane.
7. The pilot plant experimental facility of the column MBR system of claim 6, wherein: the side wall of the water production tank is provided with a sliding rail, and the MBR membrane frame is arranged on the sliding rail in a sliding manner.
8. The pilot plant experimental facility of the column MBR system of claim 1, wherein: the backwashing component comprises a backwashing pump and a dosing device, and an inlet and an outlet of the backwashing pump are respectively connected with the water production tank and the water production outlet.
CN202010667698.8A 2020-07-13 2020-07-13 A pilot-scale experimental device for a column MBR system Pending CN111675312A (en)

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