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CN210993797U - A microfiltration membrane module filter bacteria and antifouling performance tester - Google Patents

A microfiltration membrane module filter bacteria and antifouling performance tester Download PDF

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CN210993797U
CN210993797U CN201921104998.4U CN201921104998U CN210993797U CN 210993797 U CN210993797 U CN 210993797U CN 201921104998 U CN201921104998 U CN 201921104998U CN 210993797 U CN210993797 U CN 210993797U
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membrane
water
filtration
membrane module
pressure
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刘轲
王栋
程盼
郭启浩
范明
鲁振坦
李沐芳
张泉城
王雯雯
曹永清
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Shandong Taipeng Environmental Protection Material Co ltd
Wuhan Textile University
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Wuhan Textile University
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Abstract

The utility model provides a micro-filtration membrane component filter bacterium and anti-fouling performance tester, belonging to the testing technical field, comprising a filter membrane filter element filtering system and a microorganism detection system, wherein the filter membrane filter element filtering system comprises a water inlet system, a filtering system, a back washing system, a pressure testing system and a flux testing system; the microorganism detection system comprises a bacteria detector and a cell counter, wherein the bacteria detector and the cell counter are used for filtering and sterilizing in a cross-flow filtering mode, the transmembrane pressure difference is monitored in real time after filtering and sterilizing, whether a membrane assembly is polluted by microorganisms or not is evaluated, and backwashing operation is carried out.

Description

一种微滤膜组件滤菌抗污性能测试仪A microfiltration membrane module filter bacteria and antifouling performance tester

技术领域technical field

本技术属于测试技术领域,具体涉及一种微滤膜组件滤菌抗污性能测试仪。The technology belongs to the technical field of testing, and in particular relates to a microfiltration membrane component filter bacteria and antifouling performance tester.

背景技术Background technique

微滤膜是一种多孔且表面均匀的薄膜,微滤膜以静压差作为动力,通过微滤膜筛分作用对物质进行分离;采用微滤膜分离技术能够去除气相或液相物质中的胶体、细菌及固体,从而可实现对混合物的净化。微滤膜能够将微生物或微生物尺寸的杂质进行全部拦截,保证未有微生物透过膜材进入下游处理工艺中;同时,拦截的微生物或杂质等污染物能够通过错流方式去除,而不粘附在微滤膜表面,实现重复使用和寿命延长。但是,目前市场上的微滤膜过滤设备无法实现充分的滤菌除菌处理和即时检测水中微生物是否存在,传统方法检测水样是否存在细菌需要将终端水样在培养基中培养,观察是否存在菌落生长,耗时费力。此外,对微滤膜抗污染性能的测试还未有相关仪器设备及测试方法。The microfiltration membrane is a porous and uniform surface film. The microfiltration membrane uses the static pressure difference as the driving force to separate the substances through the sieving effect of the microfiltration membrane; the microfiltration membrane separation technology can remove the gas phase or liquid phase substances. Colloids, bacteria and solids, thus enabling decontamination of mixtures. The microfiltration membrane can intercept all microorganisms or impurities of the size of microorganisms to ensure that no microorganisms pass through the membrane material and enter the downstream processing process; at the same time, the intercepted microorganisms or impurities and other pollutants can be removed by cross-flow without adhesion. On the surface of the microfiltration membrane, repeated use and extended life are achieved. However, the current microfiltration membrane filtration equipment on the market cannot achieve sufficient filtration and sterilization treatment and real-time detection of the existence of microorganisms in the water. The traditional method to detect the existence of bacteria in the water sample requires culturing the terminal water sample in the culture medium to observe whether the existence of bacteria exists. Colony growth is time-consuming and labor-intensive. In addition, there are no relevant equipment and test methods for the test of the anti-fouling performance of microfiltration membranes.

中国专利公开号CN201464116U,公开了平片式滤膜元件真空检测器,其虽然可以有效地检测平板过滤膜元件膜的密封性和多个平片式滤膜元件的滤膜性能的均一性,但是单纯地检测这些参数是无法保证平板过滤膜元件膜的质量,这主要是因为影响平板过滤膜元件的质量的主要因素是滤膜的水通量和抗污染性。Chinese Patent Publication No. CN201464116U discloses a flat-plate filter element vacuum detector, although it can effectively detect the tightness of the flat-plate filter element membrane and the uniformity of the filter performance of multiple flat-plate filter elements, but Simply testing these parameters cannot guarantee the quality of the flat filter membrane element, mainly because the main factors affecting the quality of the flat filter membrane element are the water flux and anti-fouling of the filter membrane.

中国专利公开号CN201310589128.1,公开了用于平板过滤膜元件的检测装置,该实用新型通过用于容纳所述平板过滤膜元件的模拟流体箱:能够以固定压力循环平板过滤膜元件与模拟流体箱之间的流体的循环装置:用于检测循环装置循环的流体的流量的计量件。根据本实用新型的用于平板过滤膜元件的检测装置,能够有效地检测平板过滤膜元件的水通量和抗污染性,从而确保平板过滤膜元件的质量,虽然该实用新型可以有效地检测平板过滤膜元件的水通量和抗污染性,但是其不足之处在于无法即时检测水中微生物。Chinese Patent Publication No. CN201310589128.1, discloses a detection device for flat filter membrane elements, the utility model uses a simulated fluid box for accommodating the flat filter membrane elements: the flat filter membrane element and the simulated fluid can be circulated at a fixed pressure Circulation device of fluid between tanks: a metering piece for detecting the flow rate of the fluid circulated by the circulation device. The detection device for flat filter membrane elements according to the present invention can effectively detect the water flux and anti-pollution property of the flat filter membrane elements, thereby ensuring the quality of the flat filter membrane elements, although the utility model can effectively detect the flat plate filter elements The water flux and anti-fouling performance of the filtration membrane element, but its disadvantage is that it cannot detect microorganisms in water instantly.

因此,亟需研发一款能够同时评估微滤膜滤除细菌性能及可冲洗重复使用性能的检测设备。Therefore, there is an urgent need to develop a testing device that can simultaneously evaluate the performance of microfiltration membranes in removing bacteria and being able to be washed and reused.

实用新型内容Utility model content

为了解决上述技术问题,本实用新型提供了一种微滤膜组件滤菌抗污性能测试仪,通过错流过滤方式进行过滤除菌,采用实时监控跨膜压差大小,评估出膜组件是否被微生物污染进行反冲洗操作,细菌检测仪和细胞计数仪与过滤后的水样进行连接,能够即时检测通过膜组件过滤后的水样是否含微生物。In order to solve the above-mentioned technical problems, the utility model provides a microfiltration membrane module filter bacteria and antifouling performance tester, which is filtered and sterilized by cross-flow filtration, and uses real-time monitoring of the transmembrane pressure difference to evaluate whether the membrane module is damaged or not. Microbial contamination is backwashed, and the bacteria detector and cell counter are connected to the filtered water sample, which can instantly detect whether the water sample filtered through the membrane module contains microorganisms.

一种微滤膜组件滤菌抗污性能测试仪,包括滤膜滤芯过滤系统和微生物检测系统,所述滤膜滤芯过滤系统包括进水系统、过滤系统、反冲洗系统、压力测试系统和通量测试系统;所述微生物检测系统包括细菌检测仪,细胞计数仪;需过滤水经进水系统通过管道进入过滤系统后,采用错流过滤方式冲刷过滤组件进行过滤,过滤完成后净水进入反冲洗系统进行反冲洗,污水回流至进水系统中进行再次过滤。A microfiltration membrane component filtration bacteria and antifouling performance tester, including a membrane filter element filtration system and a microorganism detection system, the filter membrane filter element filtration system includes a water inlet system, a filtration system, a backwash system, a pressure test system and a flux Test system; the microorganism detection system includes a bacteria detector and a cell counter; after the water to be filtered enters the filtration system through the pipeline through the water inlet system, the filter element is washed by cross-flow filtration for filtration, and after the filtration is completed, the purified water enters the backwash The system is backwashed, and the sewage is returned to the influent system for re-filtration.

进一步,所述进水系统包括进水箱、水泵和设置在水泵前端的进水阀,进水箱与水泵通过管道连接,通过调节进水阀控制进水量流量。Further, the water inlet system includes a water inlet tank, a water pump, and a water inlet valve arranged at the front end of the water pump. The water inlet tank and the water pump are connected by pipelines, and the water inlet flow rate is controlled by adjusting the water inlet valve.

进一步,所述过滤系统包括浸没池和设置在浸没池中的膜组件,膜组件内腔位于膜组件内,当需过滤水进入膜组件内腔后,通过错流过滤方式,形成垂直方向的两个力,垂直于膜组件表面的力使水分子通过膜组件进行过滤,平行于膜组件表面的力,把膜组件表面的颗粒带走,减少膜组件的污染。Further, the filtration system includes an immersion tank and a membrane module arranged in the immersion tank, and the inner cavity of the membrane module is located in the membrane module. The force perpendicular to the surface of the membrane module makes the water molecules filter through the membrane module, and the force parallel to the surface of the membrane module takes away the particles on the surface of the membrane module and reduces the pollution of the membrane module.

进一步,所述膜组件中含有过滤膜片或者滤芯,其中所述过滤膜片为孔径为0.10μm-0.22μm微滤膜。Further, the membrane module contains a filter membrane or a filter element, wherein the filter membrane is a microfiltration membrane with a pore size of 0.10 μm-0.22 μm.

由于过滤膜为微滤膜和超滤膜,孔径较小,在压力的驱动下,能够截留悬浮物、细菌、部分病毒及大尺寸胶体。Because the filtration membrane is a microfiltration membrane and an ultrafiltration membrane, the pore size is small, and under the drive of pressure, it can retain suspended solids, bacteria, some viruses and large-sized colloids.

进一步,所所述压力测试系统通过带有气源的氮气瓶和设置在氮气瓶气瓶口的减压阀和压力罐组成,调节压力罐中的气阀调节压力,并进行压力的读取。Further, the pressure test system is composed of a nitrogen cylinder with a gas source, a pressure reducing valve and a pressure tank arranged at the gas cylinder mouth of the nitrogen cylinder, and the gas valve in the pressure tank is adjusted to adjust the pressure and read the pressure.

进一步,所述通量测试系统测试步骤为:通过压力测试仪提供恒定压力,水样在压力驱动下通过过滤系统中膜组件内腔后,在膜组件的过滤作用后,此时记录过滤膜的水通量,同时通过反冲洗系统中的出水阀以及水箱装置,记录流出水的通量,通过比较膜通量过滤前后的变化,分析膜污染情况,判断是否需要对膜组件进行反冲洗操作;所述压力测试仪提供恒定压力范围为0.5bar-1bar。Further, the testing steps of the flux testing system are as follows: a constant pressure is provided by a pressure tester, after the water sample passes through the inner cavity of the membrane module in the filtration system under the pressure drive, and after the filtration of the membrane module, the filter membrane is recorded at this time. At the same time, through the water outlet valve and water tank device in the backwash system, the flux of the effluent water is recorded, and by comparing the changes of the membrane flux before and after filtration, the membrane fouling situation is analyzed, and the membrane module needs to be backwashed. The pressure tester provides a constant pressure range of 0.5 bar-1 bar.

当跨膜压差较大时,容易造成水流摇曳力增大,导致小分子有机物更容易形成膜孔堵塞,阻碍后续有机物通过膜孔,进而容易引起膜污染,因此为了减少膜孔堵塞,提高浸没池中过滤组件的过滤性能,跨膜压差的范围为0.5bar-1bar。When the transmembrane pressure difference is large, it is easy to cause the swaying force of the water flow to increase, which makes it easier for small molecular organics to form membrane pores and block the subsequent organic substances from passing through the membrane pores, thereby easily causing membrane fouling. The filtration performance of the filter element in the pool, the range of the transmembrane pressure difference is 0.5bar-1bar.

进一步,所述反冲洗操作的指示条件为:当水样通过过滤系统的跨膜压差大于1bar时,则进行反冲洗操作。Further, the indication condition of the backwashing operation is: when the transmembrane pressure difference of the water sample passing through the filtration system is greater than 1 bar, the backwashing operation is performed.

进一步,所述反冲洗操作的流程为采用水箱内的过滤水,反冲洗系统中的反冲泵和反冲阀打开,将水箱内的过滤水通过水管对膜组件进行反冲洗。Further, the process of the backwash operation is to use the filtered water in the water tank, open the backwash pump and the backwash valve in the backwash system, and backwash the membrane module with the filtered water in the water tank through the water pipe.

进一步,所述反冲洗系统采用逆流反洗、松弛法进行反冲洗,其中逆流反洗时间为20-30s,松弛时间为10-15min,反冲洗通量的强度为过滤通量强度的1.5-2倍。Further, the backwashing system adopts countercurrent backwashing and relaxation method for backwashing, wherein the countercurrent backwashing time is 20-30s, the relaxation time is 10-15min, and the intensity of the backwashing flux is 1.5-2% of the filtration flux intensity. times.

进一步,所述微生物检测系统包括细菌检测仪和细胞计数仪,细菌检测仪和细胞计数仪分别与过滤后的水样进行连接,能够即时检测通过膜组件过滤后的水样是否含微生物。Further, the microorganism detection system includes a bacteria detector and a cell counter, and the bacteria detector and the cell counter are respectively connected with the filtered water sample, and can instantly detect whether the water sample filtered through the membrane module contains microorganisms.

其中,所述微生物检测系统中细胞计数仪(11)采用的荧光法快速检验法,所述荧光法快速检验法的采用的是ATP发光原理,ATP发光原理为:腺嘌呤核苷三磷酸简称ATP,是所有生命活动的能量载体,活细菌中ATP会维持在一定范围内,当细菌死亡后ATP会在短时间内被细胞内酶所分解,不会对活体微生物的测量产生影响,检测样品中ATP含量可以间接反应活细菌数量。ATP生物发光法是荧光素酶在镁离子条件下催化荧光素与ATP反应形成荧光素-AMP的复合物,该复合体被氧分子氧化,导致荧光素产生电激发而发光,放出二氧化碳和水,发光强度与ATP浓度呈线性关系,从而检测活菌的数量。Wherein, the fluorescence rapid detection method adopted by the cell counter (11) in the microorganism detection system, the fluorescence rapid detection method adopts the ATP luminescence principle, and the ATP luminescence principle is: adenosine triphosphate is abbreviated as ATP , is the energy carrier of all life activities. ATP in live bacteria will be maintained within a certain range. When bacteria die, ATP will be decomposed by intracellular enzymes in a short time, which will not affect the measurement of living microorganisms. ATP content can indirectly reflect the number of viable bacteria. The ATP bioluminescence method is that luciferase catalyzes the reaction of luciferin and ATP under the condition of magnesium ions to form a complex of luciferin-AMP, which is oxidized by oxygen molecules, causing luciferin to generate electrical excitation and emit light, releasing carbon dioxide and water, The luminescence intensity is linearly related to the ATP concentration to detect the number of viable bacteria.

本实用新型的工作原理为:打开进水阀,使进水箱中的待过滤水经水泵通过管道进入膜组件内腔,进入到膜组件内腔中的待过滤水在膜组件中进行错流过滤,错流过滤中形成垂直方向的两个力,垂直于膜组件表面的力使水分子通过膜组件进行过滤,平行于膜组件表面的力,把膜组件表面的颗粒带走,减少膜组件的污染;错流过滤后的净水进入到浸水池通过管道流入反冲洗系统中,通过调节反冲洗系统中出水阀和抽吸泵使过滤后的净水进入到水箱,经反冲泵调节反冲阀使净水进入浸没池后流经膜组件内腔内进行反冲洗,错流过滤后的污水经过滤膜组件内腔通过调节回流阀经管道回到进水箱中进行再次过滤。The working principle of the utility model is as follows: open the water inlet valve, so that the water to be filtered in the water inlet tank enters the inner cavity of the membrane module through the pipeline through the water pump, and the water to be filtered entering the inner cavity of the membrane module is cross-flowed in the membrane module Filtration, two forces in the vertical direction are formed in cross-flow filtration. The force perpendicular to the surface of the membrane module enables water molecules to filter through the membrane module, and the force parallel to the surface of the membrane module takes away the particles on the surface of the membrane module and reduces the number of membrane modules. The clean water after cross-flow filtration enters the immersion tank and flows into the backwash system through the pipeline. By adjusting the water outlet valve and suction pump in the backwash system, the filtered clean water enters the water tank, and the backwash pump adjusts the backwash system. The flush valve makes the clean water flow into the immersion tank and flows through the inner cavity of the membrane module for backwashing. The sewage after cross-flow filtration passes through the inner cavity of the filter membrane module through the regulating return valve and returns to the water inlet tank through the pipeline for re-filtration.

有益效果beneficial effect

(1)本实用新型中膜组件中含有微滤膜片,由于过滤膜为孔径较小的微滤膜在压力的驱动下,能够截留悬浮物、细菌、部分病毒及大尺寸胶体,达到较好的过滤效果。(1) The membrane assembly of the present utility model contains a microfiltration membrane. Because the filter membrane is a microfiltration membrane with a smaller pore size, under the drive of pressure, it can retain suspended solids, bacteria, some viruses and large-sized colloids, and achieve better filter effect.

(2)本实用新型在过滤测试系统中通过采取恒压模式过滤装置,在恒定压力驱动下,通过比较膜通量的变化,分析膜组件污染的情况,达到实时监控膜组件污染的目的。(2) The utility model adopts the constant pressure mode filter device in the filtration test system, and under the constant pressure drive, by comparing the change of membrane flux, the pollution of the membrane module is analyzed, and the purpose of monitoring the pollution of the membrane module in real time is achieved.

(3)在本实用新型中,通过采用实时监控跨膜压差大小,来控制反清洗操作,相较于定时反冲洗操作而言,通过监控跨膜压差大小,来控制反清洗操作,可以减少高强度的反冲洗频次对过滤网膜以及滤芯的损害,延长过滤网膜以及滤芯的使用寿命,减少电能以及水量的使用,节约能源,且能够避免膜污染后由于定时反冲洗操作清洗不及时,造成膜孔堵塞,进而影响过滤膜池的过滤性能。(3) In the present utility model, the backwashing operation is controlled by monitoring the size of the transmembrane pressure difference in real time. Compared with the timed backwashing operation, the backwashing operation is controlled by monitoring the size of the transmembrane pressure difference. It can reduce the damage to the filter membrane and the filter element caused by the frequency of high-intensity backwashing, prolong the service life of the filter mesh membrane and the filter element, reduce the use of electric energy and water, save energy, and avoid untimely cleaning due to regular backwashing operation after membrane pollution. , resulting in blockage of the membrane pores, which in turn affects the filtration performance of the filtration membrane pool.

(4)本实用新型采用错流过滤的方式进行,错流过滤中形成垂直方向的两个力,垂直于膜组件表面的力使水分子通过膜组件进行过滤,平行于膜组件表面的力,把膜组件表面的颗粒带走,减少膜组件的污染。(4) The utility model adopts the method of cross-flow filtration, and two forces in the vertical direction are formed in the cross-flow filtration, the force perpendicular to the surface of the membrane module makes the water molecules filter through the membrane module, and the force parallel to the surface of the membrane module, Take away the particles on the surface of the membrane module to reduce the pollution of the membrane module.

(5)本实用新型中细胞计数仪采用的ATP生物发光法,灵敏度高,检测速度快,准确性较高。(5) The ATP bioluminescence method adopted in the cell counter of the present invention has high sensitivity, fast detection speed and high accuracy.

附图说明Description of drawings

图1为本实用新型微滤膜组件滤菌抗污性能测试仪装置的示意图;Fig. 1 is the schematic diagram of the utility model microfiltration membrane assembly filtration bacteria and antifouling performance tester device;

图中:1、氮气瓶;2、减压阀;3、压力罐;4、浸没池;5、膜组件;6、出水阀;7、反冲阀;8、反冲泵;9、水箱;10、抽吸泵;11、细胞计数仪;12、细菌检测仪;13、进水阀;14、水泵;15、膜组件内腔;16、进水箱;17、回流阀。In the figure: 1. Nitrogen bottle; 2. Pressure reducing valve; 3. Pressure tank; 4. Immersion tank; 5. Membrane module; 6. Water outlet valve; 7. Backflushing valve; 8. Backflushing pump; 9. Water tank; 10. Suction pump; 11. Cell counter; 12. Bacteria detector; 13. Water inlet valve; 14. Water pump; 15. Inner cavity of membrane module; 16. Water inlet tank; 17. Return valve.

具体实施方式Detailed ways

以下将结合附图对本实用新型各实施例的技术方案进行清楚、完整的描述,显然,所描述的实施例仅仅是本实用新型的一部分实施例,而不是全部的实施例;基于本实用新型的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所得到的所有其它实施例,都属于本实用新型所保护的范围。The technical solutions of the various embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments; Embodiments, all other embodiments obtained by those of ordinary skill in the art without creative work, all belong to the scope of protection of the present invention.

实施例1Example 1

一种微滤膜组件滤菌抗污性能测试仪,包括滤膜滤芯过滤系统和微生物检测系统,所述滤膜滤芯过滤系统包括进水系统、过滤系统、反冲洗系统、压力测试系统和通量测试系统;所述微生物检测系统包括细菌检测仪12,细胞计数仪11;需过滤水经进水系统通过管道进入过滤系统后,采用错流过滤方式冲刷过滤组件进行过滤,过滤完成后净水进入反冲洗系统进行反冲洗,污水回流至进水系统中进行再次过滤。A microfiltration membrane component filtration bacteria and antifouling performance tester, including a membrane filter element filtration system and a microorganism detection system, the filter membrane filter element filtration system includes a water inlet system, a filtration system, a backwash system, a pressure test system and a flux Test system; the microorganism detection system includes a bacteria detector 12 and a cell counter 11; after the water to be filtered enters the filtration system through the pipeline through the water inlet system, the filter component is washed by cross-flow filtration for filtration, and after the filtration is completed, the purified water enters The backwashing system is used for backwashing, and the sewage is returned to the water inlet system for re-filtration.

进一步,所述进水系统包括进水箱16、水泵14和设置在水泵14前端的进水阀13,进水箱16与水泵14通过管道连接,通过调节进水阀13控制进水量流量。Further, the water inlet system includes a water inlet tank 16 , a water pump 14 and a water inlet valve 13 arranged at the front end of the water pump 14 .

进一步,所述过滤系统包括浸没池4和设置在浸没池4中的膜组件5,膜组件内腔15位于膜组件5内,当需过滤水进入膜组件内腔15后,通过错流过滤方式,形成垂直方向的两个力,垂直于膜组件5表面的力使水分子通过膜组件5进行过滤,平行于膜组件5表面的力,把膜组件5表面的颗粒带走,减少膜组件5的污染。Further, the filtration system includes an immersion tank 4 and a membrane module 5 arranged in the immersion tank 4. The inner cavity 15 of the membrane module is located in the membrane module 5. When the water to be filtered enters the inner cavity 15 of the membrane module, it is filtered by cross-flow. , forming two forces in the vertical direction, the force perpendicular to the surface of the membrane module 5 makes water molecules filter through the membrane module 5, and the force parallel to the surface of the membrane module 5 takes away the particles on the surface of the membrane module 5, reducing the membrane module 5. pollution.

进一步,所述膜组件5中含有过滤膜片或者滤芯,其中所述过滤膜片为孔径为0.10μm-0.22μm微滤膜。Further, the membrane module 5 contains a filter membrane or a filter element, wherein the filter membrane is a microfiltration membrane with a pore size of 0.10 μm-0.22 μm.

进一步,所所述压力测试系统通过带有气源的氮气瓶和设置在氮气瓶气瓶口的减压阀和压力罐组成,调节压力罐中的气阀调节压力,并进行压力的读取。Further, the pressure test system is composed of a nitrogen cylinder with a gas source, a pressure reducing valve and a pressure tank arranged at the gas cylinder mouth of the nitrogen cylinder, and the gas valve in the pressure tank is adjusted to adjust the pressure and read the pressure.

进一步,所述通量测试系统测试步骤为:通过压力测试仪提供恒定压力,水样在压力驱动下通过过滤系统中膜组件内腔15后,在膜组件5的过滤作用后,此时记录过滤膜的水通量,同时通过反冲洗系统中的出水阀6以及水箱9装置,记录流出水的通量,通过比较膜通量过滤前后的变化,分析膜污染情况,判断是否需要对膜组件进行反冲洗操作;所述压力测试仪提供恒定压力范围为0.5bar-1bar。Further, the testing steps of the flux testing system are as follows: a constant pressure is provided by a pressure tester, and after the water sample passes through the inner cavity 15 of the membrane module in the filtration system under the pressure drive, after the filtration of the membrane module 5, the filtration is recorded at this time. The water flux of the membrane is recorded through the water outlet valve 6 and the water tank 9 device in the backwash system, and the flux of the effluent water is recorded. Backwash operation; the pressure tester provides a constant pressure range of 0.5bar-1bar.

进一步,所述反冲洗操作的指示条件为:当水样通过过滤系统的跨膜压差大于1bar时,则进行反冲洗操作。Further, the indication condition of the backwashing operation is: when the transmembrane pressure difference of the water sample passing through the filtration system is greater than 1 bar, the backwashing operation is performed.

进一步,所述反冲洗操作的流程为采用水箱9内的过滤水,反冲洗系统中的反冲泵8和反冲阀7打开,将水箱9内的过滤水通过水管对膜组件5进行反冲洗。Further, the process of the backwash operation is to use the filtered water in the water tank 9, open the backwash pump 8 and the backwash valve 7 in the backwash system, and backwash the membrane module 5 with the filtered water in the water tank 9 through the water pipe. .

进一步,所述反冲洗系统采用逆流反洗、松弛法进行反冲洗,其中逆流反洗时间为20-30s,松弛时间为10-15min,反冲洗通量的强度为过滤通量强度的1.5-2倍。Further, the backwashing system adopts countercurrent backwashing and relaxation method for backwashing, wherein the countercurrent backwashing time is 20-30s, the relaxation time is 10-15min, and the intensity of the backwashing flux is 1.5-2% of the filtration flux intensity. times.

进一步,所述微生物检测系统包括细菌检测仪12和细胞计数仪11,细菌检测仪12和细胞计数仪11分别与过滤后的水样进行连接,能够即时检测通过膜组件过滤后的水样是否含微生物。Further, the microorganism detection system includes a bacteria detector 12 and a cell counter 11. The bacteria detector 12 and the cell counter 11 are respectively connected to the filtered water sample, and can instantly detect whether the water sample filtered through the membrane module contains microorganism.

实施例2-3Example 2-3

实施例2-3提供了一种微滤膜组件滤菌抗污性能测试仪,与实施例1相比,不同之处在于,除上述区别外,改变过滤膜片孔径大小,其他操作均相同,此处不再赘述,具体参数如表1所示,通过配制细菌溶液,进行微滤膜组件滤菌抗污性能测试仪的性能分析,其中细菌溶液的配制步骤为:Embodiment 2-3 provides a microfiltration membrane assembly filter bacteria and antifouling performance tester, compared with embodiment 1, the difference is that, except for the above differences, changing the pore size of the filter membrane, other operations are the same, The specific parameters are shown in Table 1. By preparing the bacterial solution, the performance analysis of the microfiltration membrane module filter bacteria and antifouling performance tester is carried out, and the preparation steps of the bacterial solution are as follows:

(1)将复苏液倒入装有冻干金黄色葡萄球菌菌株的冷冻管中,轻轻振荡,使冻干菌株溶解呈悬浮状。用酒精灯灼烧接种环至红色,冷却后沾取菌液并轻轻地划在斜面培养基上,在恒温培养箱中恒温37℃培养24h。取出后,用接种环取一个完整的菌落,放入装有100ml灭菌液体培养基的锥形瓶中,37℃,200r/min下振荡培养24h,即可得到金黄色葡萄球菌菌液。用紫外测定其悬浮液浓度,保证其活菌数达到109CFU/ml。(1) Pour the recovery solution into a freezing tube containing freeze-dried Staphylococcus aureus strains, and shake gently to dissolve the freeze-dried strains into suspension. Burn the inoculation ring with an alcohol lamp until it turns red, and after cooling, dip the bacterial solution and gently scratch it on the slant medium, and incubate it in a constant temperature incubator at a constant temperature of 37 °C for 24 hours. After taking it out, use an inoculation loop to take a complete colony, put it into a conical flask containing 100 ml of sterile liquid medium, and shake it for 24 hours at 37° C. and 200 r/min to obtain Staphylococcus aureus bacterial liquid. The concentration of the suspension was determined by UV light to ensure that the viable bacterial count reached 10 9 CFU/ml.

(2)取1ml109CFU的细菌培养液,稀释到1000ml无菌生理盐水中,搅拌混合均匀配置成106CFU的细菌悬浮液。(2) Take 1 ml of 10 9 CFU of bacterial culture solution, dilute it into 1000 ml of sterile physiological saline, stir and mix evenly to prepare a bacterial suspension of 10 6 CFU.

将配置好的细菌悬浮液作为待过滤水源进行测试。The prepared bacterial suspension was tested as the water source to be filtered.

表1:Table 1:

Figure BDA0002130916160000081
Figure BDA0002130916160000081

由实施例1-3可以看出,过滤膜片孔径大小在0.10μm-0.22μm范围内,在对模拟过滤水源进行性能测试时,金黄色葡萄球菌菌落数为0,说明过滤膜片孔径大小在0.10μm-0.22μm范围内时具有较优的过滤效果。It can be seen from Examples 1-3 that the pore size of the filter membrane is in the range of 0.10 μm to 0.22 μm. When the simulated filtered water source is tested for performance, the number of Staphylococcus aureus colonies is 0, indicating that the pore size of the filter membrane is between It has better filtering effect in the range of 0.10μm-0.22μm.

实施例4-6Examples 4-6

实施例4-6提供了一种微滤膜组件滤菌抗污性能测试仪,与实施例1相比,不同之处在于,改变压力测试仪中压力大小,除上述区别外,其他操作均相同,此处不再赘述,具体参数如下表2所示。通过配制细菌溶液,进行微滤膜组件滤菌抗污性能测试仪的性能分析,其中细菌溶液的配制步骤为:Embodiments 4-6 provide a microfiltration membrane module filtration bacteria and antifouling performance tester. Compared with embodiment 1, the difference is that the pressure in the pressure tester is changed. Except for the above differences, other operations are the same , which will not be repeated here, and the specific parameters are shown in Table 2 below. By preparing the bacterial solution, the performance analysis of the microfiltration membrane component filtration and antifouling performance tester is carried out, wherein the preparation steps of the bacterial solution are:

(1)将复苏液倒入装有冻干金黄色葡萄球菌菌株的冷冻管中,轻轻振荡,使冻干菌株溶解呈悬浮状。用酒精灯灼烧接种环至红色,冷却后沾取菌液并轻轻地划在斜面培养基上,在恒温培养箱中恒温37℃培养24h。取出后,用接种环取一个完整的菌落,放入装有100ml灭菌液体培养基的锥形瓶中,37℃,200r/min下振荡培养24h,即可得到金黄色葡萄球菌菌液。用紫外测定其悬浮液浓度,保证其活菌数达到109CFU/ml。(1) Pour the recovery solution into a freezing tube containing freeze-dried Staphylococcus aureus strains, and shake gently to dissolve the freeze-dried strains into suspension. Burn the inoculation ring with an alcohol lamp until it turns red, and after cooling, dip the bacterial solution and gently scratch it on the slant medium, and incubate it in a constant temperature incubator at a constant temperature of 37 °C for 24 hours. After taking it out, use an inoculation loop to take a complete colony, put it into a conical flask containing 100 ml of sterile liquid medium, and shake it for 24 hours at 37° C. and 200 r/min to obtain Staphylococcus aureus bacterial liquid. The concentration of the suspension was determined by UV light to ensure that the viable bacterial count reached 10 9 CFU/ml.

(2)取1ml109CFU的细菌培养液,稀释到1000ml无菌生理盐水中,搅拌混合均匀配置成106CFU的细菌悬浮液。(2) Take 1 ml of 10 9 CFU of bacterial culture solution, dilute it into 1000 ml of sterile physiological saline, stir and mix evenly to prepare a bacterial suspension of 10 6 CFU.

将配置好的细菌悬浮液作为待过滤水源进行测试。The prepared bacterial suspension was tested as the water source to be filtered.

表2:Table 2:

Figure BDA0002130916160000091
Figure BDA0002130916160000091

由实施例4-6可以看出,压力测试仪中压力大小范围为0.5-1bar时,在对模拟过滤水源进行性能测试时,金黄色葡萄球菌菌落数为0,说明压力测试仪提供恒定压力0.5-1bar时,过滤组件的过滤性能较优,不容易堵塞过滤组件,过滤效果较优。It can be seen from Examples 4-6 that when the pressure range in the pressure tester is 0.5-1 bar, when the simulated filtered water source is tested for performance, the number of Staphylococcus aureus colonies is 0, indicating that the pressure tester provides a constant pressure of 0.5 At -1bar, the filtering performance of the filter element is better, it is not easy to block the filter element, and the filtering effect is better.

实施例7-15Examples 7-15

实施例7-15提供了一种微滤膜组件滤菌抗污性能测试仪,与实施例1相比,不同之处在于,改变逆流反洗时间,松弛时间,反冲洗通量的强度,除上述区别外,其他操作均相同,此处不再赘述,具体参数如下表3所示。通过配制细菌溶液,进行微滤膜组件滤菌抗污性能测试仪的性能分析,其中细菌溶液的配制步骤为:Embodiments 7-15 provide a microfiltration membrane module filtration bacteria and antifouling performance tester. Compared with Embodiment 1, the difference is that the countercurrent backwashing time, relaxation time, and backwashing flux strength are changed, except Except for the above differences, other operations are the same, which will not be repeated here. The specific parameters are shown in Table 3 below. By preparing the bacterial solution, the performance analysis of the microfiltration membrane component filtration and antifouling performance tester is carried out, wherein the preparation steps of the bacterial solution are:

(1)将复苏液倒入装有冻干大肠杆菌菌株的冷冻管中,轻轻振荡,使冻干菌株溶解呈悬浮状。用酒精灯灼烧接种环至红色,冷却后沾取菌液并轻轻地划在斜面培养基上,在恒温培养箱中恒温37℃培养24h。取出后,用接种环取一个完整的菌落,放入装有100ml灭菌液体培养基的锥形瓶中,37℃,200r/min下振荡培养24h,即可得到金黄色葡萄球菌菌液。用紫外测定其悬浮液浓度,保证其活菌数达到109CFU/ml。(1) Pour the recovery solution into a freezing tube containing freeze-dried Escherichia coli strains, and shake gently to dissolve the freeze-dried strains into suspension. Burn the inoculation ring with an alcohol lamp until it turns red, and after cooling, dip the bacterial solution and gently scratch it on the slant medium, and incubate it in a constant temperature incubator at a constant temperature of 37 °C for 24 hours. After taking it out, use an inoculation loop to take a complete colony, put it into a conical flask containing 100 ml of sterile liquid medium, and shake it for 24 hours at 37° C. and 200 r/min to obtain Staphylococcus aureus bacterial liquid. The concentration of the suspension was determined by UV light to ensure that the viable bacterial count reached 10 9 CFU/ml.

(2)取1ml109CFU的细菌培养液,稀释到1000ml无菌生理盐水中,搅拌混合均匀配置成106CFU的细菌悬浮液。(2) Take 1 ml of 10 9 CFU of bacterial culture solution, dilute it into 1000 ml of sterile physiological saline, stir and mix evenly to prepare a bacterial suspension of 10 6 CFU.

将配置好的细菌悬浮液作为待过滤水源进行测试。The prepared bacterial suspension was tested as the water source to be filtered.

表3:table 3:

Figure BDA0002130916160000101
Figure BDA0002130916160000101

由实施例7-15可以看出,当逆流反洗时间为20-30s,松弛时间为10-15min,反冲洗通量的强度为过滤通量强度的1.5-2倍时,在对模拟过滤水源进行性能测试时,大肠杆菌菌落数为0,说明在此反冲洗条件下,有助于减少对膜组件的反冲洗次数,减少对膜组件的损耗,提高膜组件的过滤性能。It can be seen from Examples 7-15 that when the countercurrent backwash time is 20-30s, the relaxation time is 10-15min, and the backwash flux intensity is 1.5-2 times the filtration flux intensity, the simulated filtered water source is During the performance test, the number of E. coli colonies was 0, indicating that under this backwashing condition, it was helpful to reduce the number of backwashing of the membrane module, reduce the loss of the membrane module, and improve the filtration performance of the membrane module.

以上所述,仅为本实用新型较佳的具体实施方式,但本实用新型的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本实用新型揭露的技术范围内,根据本实用新型的技术方案及其实用新型构思加以等同替换或改变,都应涵盖在本实用新型的保护范围之内。The above description is only a preferred embodiment of the present invention, but the protection scope of the present invention is not limited to this. Equivalent replacement or modification of the new technical solution and its utility model concept shall be included within the protection scope of the present utility model.

Claims (3)

1. The utility model provides a micro-filtration membrane subassembly strains fungus anti-soil capability test appearance, includes filter membrane filter core filtration system and microorganism detecting system, its characterized in that: the filter membrane filter element filtering system comprises a water inlet system, a filtering system, a back washing system, a pressure testing system and a flux testing system;
the microorganism detection system comprises a bacteria detector (12) and a cell counter (11); the water inlet system comprises a water inlet tank (16), a water pump (14) and a water inlet valve (13) arranged at the front end of the water pump (14), the water inlet tank (16) is connected with the water pump (14) through a pipeline, and the flow of water inflow is controlled by adjusting the water inlet valve (13); the filtering system comprises an immersion tank (4) and a membrane module (5) arranged in the immersion tank (4), and an inner cavity (15) of the membrane module is positioned in the membrane module (5); the microorganism detection system comprises a bacterium detector (12) and a cell counter (11) which are arranged on two sides of the inner cavity (15) of the membrane component, wherein the bacterium detector (12) and the cell counter (11) are respectively connected with a filtered water sample, and can immediately detect whether the water sample filtered by the membrane component (5) contains microorganisms.
2. The microfiltration membrane assembly bacterial filtration and anti-fouling performance tester according to claim 1, wherein: the membrane component (5) contains a filtering membrane or a filter element, wherein the filtering membrane is a microfiltration membrane with the pore diameter of 0.10-0.22 μm.
3. The microfiltration membrane assembly bacterial filtration and anti-fouling performance tester according to claim 1, wherein: the pressure testing system is composed of a nitrogen cylinder (1) with an air source, a pressure reducing valve (2) arranged at the air bottle opening of the nitrogen cylinder (1) and a pressure tank (3), and is used for adjusting the pressure of an air valve in the pressure tank (3) and reading the pressure.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112760215A (en) * 2020-12-25 2021-05-07 山东省医疗器械产品质量检验中心 Tester and testing method for dry microbial barrier of breathable packaging material
CN113176236A (en) * 2021-04-02 2021-07-27 深圳技术大学 Large-scale visual membrane pollution in-situ online monitoring system suitable for membrane filtration
CN114088505A (en) * 2021-11-18 2022-02-25 光大水务科技发展(南京)有限公司 Pretreatment device system of water treatment water quality detection instrument and working method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112760215A (en) * 2020-12-25 2021-05-07 山东省医疗器械产品质量检验中心 Tester and testing method for dry microbial barrier of breathable packaging material
CN113176236A (en) * 2021-04-02 2021-07-27 深圳技术大学 Large-scale visual membrane pollution in-situ online monitoring system suitable for membrane filtration
CN114088505A (en) * 2021-11-18 2022-02-25 光大水务科技发展(南京)有限公司 Pretreatment device system of water treatment water quality detection instrument and working method thereof

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