CN105217734A - A rotary immersion water treatment ultra-microfiltration method and device - Google Patents

A rotary immersion water treatment ultra-microfiltration method and device Download PDF

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CN105217734A
CN105217734A CN201510715512.0A CN201510715512A CN105217734A CN 105217734 A CN105217734 A CN 105217734A CN 201510715512 A CN201510715512 A CN 201510715512A CN 105217734 A CN105217734 A CN 105217734A
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membrane
water
water leg
film
filaments
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解利昕
杨继状
孙永超
徐世昌
戴海平
孙磊
柯永文
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Tianjin University
Tianjin Motimo Membrane Technology Co Ltd
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Tianjin University
Tianjin Motimo Membrane Technology Co Ltd
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Abstract

The invention relates to a rotary immersion type water treatment ultramicro-filtration method and a device, wherein two ends of hollow fiber membrane filaments are respectively cast on an upper membrane filament disc and a lower membrane filament disc, the upper membrane filament disc is connected with a water collecting tank, the lower membrane filament disc is fixed with a component chassis, cavities of the membrane filaments are communicated with cavities of the water collecting tank, the membrane filaments and the water collecting tank form a whole body to form a membrane component, the water collecting tank is connected with a hollow shaft, the hollow shaft hoists the membrane component on a bearing seat and is communicated with a negative pressure water outlet pipe, a pin gear fixed on the water collecting tank, a speed reducer, a transmission shaft and a pinion form a driving device, the membrane component can be driven to rotate positively and negatively to enable the membrane filaments to be in a motion state, the system adopts a pump or siphon mode to realize negative pressure, raw water is filtered by the membrane to discharge purified water from a negative pressure water discharge pipe, the membrane filaments and water flow generate, effectively prevents the surface of the membrane from being blocked, and prevents the filtration flow from being attenuated.

Description

一种旋转浸没式水处理超微滤方法及装置A rotary immersion water treatment ultra-microfiltration method and device

技术领域technical field

本发明属于水处理设备领域,涉及一种旋转浸没式水处理超微滤方法及装置。The invention belongs to the field of water treatment equipment, and relates to a rotary submersion ultra-microfiltration method and device for water treatment.

背景技术Background technique

水是生命之源,是经济发展、工农业生产中不可或缺的元素之一,也是人类存在的物质基础。几十年来,随着我国的改革开放,工业化的迅速发展,各种成分复杂的工业废水和生活污水经常未达标就直接进入水体,导致饮用水水源水质急剧下降,传统饮用水净化技术面临着诸多的挑战。此外,我国是一个严重缺水的国家,人均水资源占有率仅为世界平均水平的1/4,且万元GDP的耗水量远远高于国际先进水平,目前水资源短缺已严重影响我国的经济发展和社会进步。因此,开发新型高效饮用水净化技术以及水深度处理技术对于保障饮用水安全、提高水重复利用率、降低水耗、促进社会和经济可持续发展具有重要的意义。Water is the source of life, one of the indispensable elements in economic development, industrial and agricultural production, and the material basis of human existence. Over the past few decades, with the reform and opening up of our country and the rapid development of industrialization, various industrial wastewater and domestic sewage with complex components often directly enter the water body without reaching the standard, resulting in a sharp decline in the quality of drinking water sources. Traditional drinking water purification technology is facing many problems. challenge. In addition, my country is a country seriously short of water, the per capita share of water resources is only 1/4 of the world's average level, and the water consumption per 10,000 yuan of GDP is far higher than the international advanced level, the current shortage of water resources has seriously affected my country's economic development and social progress. Therefore, the development of new high-efficiency drinking water purification technology and water advanced treatment technology is of great significance to ensure drinking water safety, improve water reuse rate, reduce water consumption, and promote sustainable social and economic development.

膜技术近些年来逐渐成为饮用水净化及废(污)水深度处理领域的研究与应用的热点问题。超滤或微滤能够最有效地去除水体中的天然有机物和氯消毒副产物的前驱物,对浊度和细菌的去除率接近100%。In recent years, membrane technology has gradually become a hot issue in the research and application of drinking water purification and advanced treatment of waste (sewage) water. Ultrafiltration or microfiltration can most effectively remove the precursors of natural organic matter and chlorine disinfection by-products in water bodies, and the removal rate of turbidity and bacteria is close to 100%.

浸没式连续膜过滤系统(SMF)能除去水中大于0.03微米的颗粒。SMF利用外压式中空纤维超滤膜,通过低压气水双洗+反冲洗等运行和反洗工艺来维持系统的运行流量。过滤的流向是从中空纤维的外壁至中空的内腔。进水通过多孔的纤维壁将水中的固体截留在外壁。膜能除去大于0.03微米的颗粒,有效去除水中的微生物和悬浮物等物质。SMF单元的主要部件是SMF膜元件。SMF膜元件由数以千计微孔中空纤维膜丝和封头组成。膜组件上端封头可允许滤出水从中空纤维膜内腔流向集水管路。底部封头封堵纤维膜的出口,但允许低压工艺空气在反洗时从封头上一系列的开孔通过冲刷中空膜的外表面。Submerged continuous membrane filtration system (SMF) can remove particles larger than 0.03 microns in water. SMF uses external pressure hollow fiber ultrafiltration membranes to maintain the operating flow of the system through low-pressure air-water double washing + backwashing and backwashing processes. The flow direction of filtration is from the outer wall of the hollow fiber to the hollow lumen. The incoming water passes through the porous fiber wall and the solids in the water are trapped on the outer wall. The membrane can remove particles larger than 0.03 microns, and effectively remove microorganisms and suspended solids in water. The main component of the SMF unit is the SMF membrane element. SMF membrane elements are composed of thousands of microporous hollow fiber membranes and heads. The upper end of the membrane module can allow the filtrate water to flow from the hollow fiber membrane cavity to the water collection pipeline. The bottom head blocks the outlet of the fiber membrane, but allows low pressure process air to pass through a series of openings in the head to scour the outer surface of the hollow membrane during backwashing.

现有的浸没式连续膜过滤系统的膜和水体处于相对静止状态,在膜丝固定槽,膜内产生负压,使通过膜管内的水经过膜过滤后统一从两端的膜丝固定槽排出,这种过滤方式中的污染物积累在膜表面,使膜丝的孔道容易堵塞,降低过滤效率。The membrane and water body of the existing submerged continuous membrane filtration system are in a relatively static state. In the membrane filament fixing groove, negative pressure is generated in the membrane, so that the water passing through the membrane tube is discharged from the membrane filament fixing groove at both ends after being filtered by the membrane. Pollutants in this filtration method accumulate on the surface of the membrane, making the pores of the membrane filaments easily blocked and reducing the filtration efficiency.

专利文献CN103331101A公开一种超滤膜组件,包括承压膜管和超滤膜组,其特征在于:所述超滤膜组活动装配在所述承压膜管内,所述承压膜管包括膜管、设在膜管两端的端盖以及将膜管和端盖连接的紧固件,所述超滤膜组一端设有入水口,另一端设有出水口,所述膜管一端的端盖设有原水入口,膜管另一端的端盖设有净水出口,所述入水口与所述原水入口可拆式连接,所述出水口与所述净水出口可拆式连接。Patent document CN103331101A discloses an ultrafiltration membrane assembly, including a pressure-bearing membrane tube and an ultrafiltration membrane group, characterized in that: the ultrafiltration membrane group is movably assembled in the pressure-bearing membrane tube, and the pressure-bearing membrane tube includes a membrane tube, end caps arranged at both ends of the membrane tube and fasteners connecting the membrane tube and the end cap, one end of the ultrafiltration membrane group is provided with a water inlet, and the other end is provided with a water outlet, and the end cap at one end of the membrane tube is A raw water inlet is provided, and the end cap at the other end of the membrane tube is provided with a purified water outlet, the water inlet is detachably connected to the raw water inlet, and the water outlet is detachably connected to the purified water outlet.

CN103055700A公开一种超滤膜组件,本发明的超滤膜组件,包括超滤膜膜丝,超滤膜膜丝两端分别连接第一膜丝固定槽与第二膜丝固定槽,第一膜丝固定槽外侧连接第一堵头,第二膜丝固定槽连接第二堵头,所述第一膜丝固定槽与第二膜丝固定槽中间连接有膜丝固定管,所述超滤膜膜丝与膜丝固定管浇注为一体。与现有技术相比,本发明的一种超滤膜组件通过在两个膜丝固定槽安装膜丝固定管,膜丝固定管和膜丝浇注在一起,使得膜丝更好的固定在堵头之间,膜丝不与膜管粘连,当膜丝使用老化或是损坏,只需将浇注在一起的膜丝固定管和膜丝更换即可,从而节省成本,同时,膜丝固定管形成了过滤后液体的流通与汇集的通道及对超滤膜的支撑作用。CN103055700A discloses an ultrafiltration membrane assembly. The ultrafiltration membrane assembly of the present invention includes ultrafiltration membrane filaments, and the two ends of the ultrafiltration membrane filaments are respectively connected to the first membrane filament fixing groove and the second membrane filament fixing groove. The outer side of the wire fixing groove is connected with the first plug, the second membrane wire fixing groove is connected with the second plug, the membrane wire fixing tube is connected between the first membrane wire fixing groove and the second membrane wire fixing groove, and the ultrafiltration membrane The membrane filament and the membrane filament fixing pipe are poured into one body. Compared with the prior art, an ultrafiltration membrane module of the present invention installs the membrane fixing tubes in the two membrane fixing grooves, and the membrane fixing tubes and the membranes are poured together, so that the membranes are better fixed in the blocking Between the heads, the membrane filament does not adhere to the membrane tube. When the membrane filament is aged or damaged, it is only necessary to replace the membrane filament fixing tube and the membrane filament that are poured together, thereby saving costs. At the same time, the membrane filament fixing tube forms It provides a channel for the circulation and collection of the filtered liquid and supports the ultrafiltration membrane.

上述公开的文件不能解决上述问题,技术方案还有待继续改进。The above-mentioned disclosed documents cannot solve the above-mentioned problems, and the technical solutions still need to be continuously improved.

发明内容Contents of the invention

本发明的目的在于克服现有技术的不足之处,提供一种装置结构简单、不易堵塞、过滤效率高的旋转浸没式水处理超微滤方法及装置。The purpose of the present invention is to overcome the disadvantages of the prior art, and provide a rotary immersion water treatment ultra-microfiltration method and device with simple device structure, not easy to block, and high filtration efficiency.

本发明实现目的的工艺方案如下:The technological scheme that the present invention realizes purpose is as follows:

一种旋转浸没式水处理超微滤方法,膜组件外部不再设置膜管,使膜丝处于一种敞开的状态,直接接触流动的被过滤水体。采用驱动装置使膜组件在被处理水中进行正反旋转运动,运动中水流与膜丝发生相对运动,由于膜丝表面受到水流的冲刷力,及时将膜丝表面的污垢冲掉。A rotary immersion ultra-microfiltration method for water treatment. No membrane tube is arranged outside the membrane module, so that the membrane filaments are in an open state and directly contact the flowing filtered water. The driving device is used to make the membrane module rotate forward and backward in the treated water. During the movement, the water flow and the membrane filaments move relative to each other. The dirt on the membrane filament surface is washed away in time due to the scouring force of the water flow on the surface of the membrane filament.

一种旋转浸没式水处理超微滤装置,包括若干束膜丝、膜丝盘、组件底盘、集水槽、空心轴、轴承座以及负压排水管。每束膜丝的两端均被浇铸在上下膜丝盘上,位于下端的膜丝盘均布固定在组件底盘上,位于上端的膜丝盘密封均布固定在集水槽下表面的进水孔周围,膜丝孔与集水槽内腔相通。集水槽与空心轴法兰连接,空心轴上的卡环安装在轴承座内的轴承上,使其能承受膜组件的重量和转动。负压排水管的法兰与轴承座法兰连接,使集水槽、空心轴、负压排水管形成一条排水通道。在集水槽上安装有驱动装置部件,使膜组件可以同轴转动。A rotary submerged ultra-microfiltration device for water treatment, comprising several bundles of membrane filaments, a membrane filament disc, a component chassis, a water collection tank, a hollow shaft, a bearing seat and a negative pressure drainage pipe. Both ends of each bundle of membrane filaments are cast on the upper and lower membrane filament disks, the membrane filament disks at the lower end are uniformly fixed on the module chassis, and the membrane filament disks at the upper end are sealed and evenly distributed and fixed on the water inlet holes on the lower surface of the sump Around, the membrane silk hole communicates with the inner cavity of the sump. The water collection tank is flange-connected with the hollow shaft, and the snap ring on the hollow shaft is installed on the bearing in the bearing seat, so that it can bear the weight and rotation of the membrane module. The flange of the negative pressure drain pipe is connected to the flange of the bearing seat, so that the sump, the hollow shaft, and the negative pressure drain pipe form a drainage channel. A driving device component is installed on the sump so that the membrane module can rotate coaxially.

所述驱动装置的结构如下:在集水槽上表面外圆周固装一圈啮合销齿轮,在销齿轮的外缘固装一小齿轮,小齿轮与传动轴固装在减速机的输出轴端部。驱动装置使膜组件做正反旋转运动。The structure of the driving device is as follows: a ring of meshing pin gears is fixed on the outer circumference of the upper surface of the water collection tank, a small gear is fixed on the outer edge of the pin gear, and the pinion and the transmission shaft are fixed on the end of the output shaft of the reducer . The driving device makes the membrane assembly do forward and reverse rotation.

而且,在集水槽和组件底盘之间还均匀固装一组支撑连杆。Moreover, a group of supporting connecting rods is evenly fixed between the water collection tank and the component chassis.

本发明取得的优点和有益效果是:Advantage and beneficial effect that the present invention obtains are:

本申请提供的旋转浸没式水处理超微滤装置将膜丝一端膜丝孔封堵,另一端安装在膜丝盘内丝孔不堵,不再安装膜管,使膜丝直接处于待处理的污水或废水中,有效防止了膜管对杂质的富集作用,使膜丝孔道不易堵塞。In the rotary immersion water treatment ultra-microfiltration device provided by this application, one end of the membrane filament is blocked, and the other end is installed in the membrane filament disk without blocking the filament hole, and the membrane tube is no longer installed, so that the membrane filament is directly placed in the to-be-treated In sewage or waste water, the enrichment of impurities by the membrane tube is effectively prevented, so that the pores of the membrane filament are not easy to be blocked.

本申请提供的装置使膜组件在被处理水中进行正反旋转运动,运动中水流与膜丝发生相对运动,由于膜丝表面受到水流的冲刷力,及时将膜丝表面的污垢带走,有效防止了膜表面的堵塞,使污水过滤流量不发生衰减,提高过滤效率。The device provided by this application makes the membrane module rotate forward and backward in the water to be treated. During the movement, the water flow and the membrane filaments move relative to each other. Since the surface of the membrane filament is subjected to the scouring force of the water flow, the dirt on the surface of the membrane filament is taken away in time, effectively preventing The clogging of the membrane surface is prevented, the sewage filtration flow does not attenuate, and the filtration efficiency is improved.

附图说明Description of drawings

图1为本发明的装置示意图;其中,1—组件底盘;2—下膜丝盘;3—膜丝;4—上膜丝盘;5—集水槽;6—空心轴;7—轴承座;8—轴承;9—卡环;10—负压排水管;11—减速机;12—传动轴;13—小齿轮;14—销齿轮;15—支撑连杆。Fig. 1 is a schematic diagram of the device of the present invention; wherein, 1—component chassis; 2—lower membrane wire disc; 3—membrane wire; 4—upper membrane wire disc; 5—water collection tank; 6—hollow shaft; 7—bearing seat; 8—bearing; 9—snap ring; 10—negative pressure drain pipe; 11—reducer; 12—transmission shaft; 13—pinion gear; 14—pin gear; 15—support connecting rod.

图2为图1的A-A向剖视图。Fig. 2 is a sectional view taken along line A-A of Fig. 1 .

具体实施方式detailed description

下面通过具体实施例对本发明作进一步详述,以下实施例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。The present invention will be described in further detail below through specific examples. The following examples are only descriptive, not restrictive, and cannot limit the protection scope of the present invention.

一种旋转浸没式水处理超微滤方法,其膜组件外部不再设置膜管,使膜丝处于一种敞开的状态,直接接触流动的被过滤水体。采用驱动装置使膜组件在被处理水中进行正反旋转运动,运动中水流与膜丝发生相对摩擦,由于膜丝表面受到水流的冲刷力(切向力),及时将膜丝表面的污垢带走。A rotary immersion ultra-microfiltration method for water treatment, in which no membrane tube is arranged outside the membrane module, so that the membrane filaments are in an open state and directly contact the flowing filtered water. The driving device is used to make the membrane module rotate forward and backward in the water to be treated. During the movement, the water flow and the membrane filaments have relative friction. Because the surface of the membrane filament is subjected to the scouring force (tangential force) of the water flow, the dirt on the surface of the membrane filament is taken away in time. .

一种旋转浸没式水处理超微滤装置,包括若干束膜丝3、膜丝盘2,4、组件底盘1、集水槽5、空心轴6、轴承座7以及负压排水管10。每束膜丝的两端均被浇铸在上下膜丝盘上,位于下端的膜丝盘2(丝孔封堵)均布固定在组件底盘1上,位于上端的膜丝盘4密封均布固定在集水槽5下表面的孔周,膜丝孔与集水槽5内腔相通。集水槽5与空心轴6法兰连接,空心轴6上的卡环9安装在轴承座7内的轴承8上,使其能承受膜组件的重量和转动。负压排水管10的法兰与轴承座7法兰连接,使集水槽5、空心轴6、负压排水管10形成一条排水通道,排出净化后的水。A rotary submerged ultra-microfiltration device for water treatment, comprising several bundles of membrane filaments 3 , membrane filament discs 2 and 4 , an assembly chassis 1 , a water collection tank 5 , a hollow shaft 6 , a bearing seat 7 and a negative pressure drain pipe 10 . The two ends of each bundle of membrane filaments are cast on the upper and lower membrane filament disks, the membrane filament disk 2 (filament hole plugging) at the lower end is uniformly fixed on the module chassis 1, and the membrane filament disk 4 at the upper end is sealed and fixed evenly Around the holes on the lower surface of the sump 5 , the membrane thread holes communicate with the inner cavity of the sump 5 . The sump 5 is flange-connected with the hollow shaft 6, and the snap ring 9 on the hollow shaft 6 is installed on the bearing 8 in the bearing seat 7, so that it can bear the weight and rotation of the membrane assembly. The flange of the negative pressure drain pipe 10 is connected to the bearing block 7 flanges, so that the sump 5, the hollow shaft 6, and the negative pressure drain pipe 10 form a drainage channel to discharge purified water.

为了降低膜丝的污染效率,可以采用膜丝运动方式来实现,例如使膜组件转动,本申请推荐一种实现方式:在集水槽上表面外圆周固装一圈啮合销齿轮14,在销齿轮的外缘固装一小齿轮13,小齿轮与传动轴12固装在减速机11的输出轴端部。带电机的减速机使膜组件做正反旋转运动,使膜丝处于运动的状态来净化污水,减轻膜丝表面污染。In order to reduce the pollution efficiency of the membrane filaments, it can be realized by the movement of the membrane filaments, such as rotating the membrane module. This application recommends a realization method: a ring of meshing pin gears 14 is fixed on the outer circumference of the upper surface of the sump, and the pin gears The outer edge of the pinion gear 13 is fixed, and the pinion gear and the transmission shaft 12 are fixed on the output shaft end of the speed reducer 11. The reducer with motor makes the membrane module rotate forward and backward, so that the membrane filament is in a moving state to purify the sewage and reduce the surface pollution of the membrane filament.

为了增加上、下膜丝盘的支撑力,使膜组件成一整体,在集水槽和组件底盘之间均匀固装一组支撑连杆(图中采用的是左、中、右三个连杆)。In order to increase the supporting force of the upper and lower membrane wire discs and make the membrane module into a whole, a set of supporting connecting rods is evenly fixed between the sump and the module chassis (the left, middle and right connecting rods are used in the figure) .

本申请中旋转浸没式水处理超微滤装置的操作方法为:In this application, the operation method of the rotary immersion water treatment ultra-microfiltration device is:

将整个装置固定在污水处理池的平台上,污水水位控制在集水槽1/2厚度以下,启动电机后减速机开始工作,带动膜组件转动。采用泵抽或虹吸的方式实现负压,强制水穿过膜丝表面,进入膜丝内,向上收集至集水槽内,净化后的水通过空心轴、负压排水管被排出收集,或者进入下一级净化设备内。The whole device is fixed on the platform of the sewage treatment tank, the sewage water level is controlled below 1/2 thickness of the sump, and the reducer starts to work after starting the motor to drive the membrane module to rotate. Pumping or siphoning is used to realize negative pressure, forcing water to pass through the surface of the membrane filament, enter the membrane filament, and collect upward into the sump. The purified water is discharged and collected through the hollow shaft and negative pressure drain pipe, or enters the lower Inside the primary purification equipment.

驱动装置可控制膜组件正反旋转,集水槽外缘线速为0.5m/s~1m/s。The driving device can control the positive and negative rotation of the membrane module, and the linear speed of the outer edge of the sump is 0.5m/s~1m/s.

在膜组件的运动中,由于惯性作用,水流与膜丝之间存在速度差,使两者发生相对运动,膜丝与水流发生相对摩擦,这种水流冲刷力使膜表面附着的污垢被及时带走,有效阻止了膜的堵塞,使过滤流量不发生衰减,提高了过滤效率。During the movement of the membrane module, due to inertia, there is a speed difference between the water flow and the membrane filaments, which causes relative motion between the two, and the relative friction between the membrane filaments and the water flow. The scouring force of the water flow makes the dirt attached to the membrane surface promptly removed It effectively prevents the clogging of the membrane, prevents the filtration flow from attenuating, and improves the filtration efficiency.

Claims (4)

1. rotate an immersion water treatment ultra filtration method, it is characterized in that: membrane module outside no longer arranges housing, make film silk be in a kind of unlimited state, direct contact flow be filtered water body.Adopt drive unit to make membrane module carry out positive and negative rotation motion in processed water, current and film silk generation relative movement, because film silk surface is subject to the scouring force of current, in time the dirt on film silk surface is washed out.
2. one kind rotates immersion water treatment ultramicro filtration device, it is characterized in that: device comprises some bundle film silks, film wire tray, assembly chassis, water leg, tubular shaft, bearing support and drainage by suction pipe, the two ends of often restrainting film silk are all cast in film wire tray and lower film wire tray, be positioned at that the film wire tray of lower end is uniform to be fixed on assembly chassis, the film wire tray sealing being positioned at upper end is uniformly fixed on water leg lower surface, film silk cavity communicates with water leg inner chamber, water leg and tubular shaft Flange joint, snap ring on tubular shaft is arranged on the bearing in bearing support, weight and the rotation of membrane module can be born, the flange of drainage by suction pipe is connected with bearing block flange, make water leg, tubular shaft, drainage by suction pipe forms a drainage channel, water leg is provided with driving device component, make membrane module coaxial rotation.
3. rotation immersion water treatment ultramicro filtration device according to claim 2, it is characterized in that: the structure described water leg being provided with driving device component is: be fixedly mounted with a circle engaging pin gear at water leg upper surface excircle, a pinion(gear) is fixedly mounted with in the outer rim of pin gear, pinion(gear) and transmission shaft are packed in the output shaft end of step-down gear, and drive unit makes membrane module do positive and negative rotation motion.
4. rotation immersion water treatment ultramicro filtration device according to claim 2, is characterized in that: between water leg and assembly chassis, be fixedly mounted with one group of support link.
CN201510715512.0A 2015-10-28 2015-10-28 A rotary immersion water treatment ultra-microfiltration method and device Pending CN105217734A (en)

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107129040A (en) * 2016-02-29 2017-09-05 鞍钢股份有限公司 Method and device for prolonging service life of membrane of sequencing batch membrane bioreactor
CN107352715A (en) * 2017-08-24 2017-11-17 天津市金通正水处理技术开发有限公司 A kind of integrated type pure water device
CN107737476A (en) * 2017-10-13 2018-02-27 朱平 A kind of rotatable immersion filter
CN108722026A (en) * 2018-08-13 2018-11-02 武汉工程大学 A kind of heterogeneous separation device with sieve-board type fractal structure
CN108722095A (en) * 2018-08-13 2018-11-02 武汉工程大学 A kind of heterogeneous separation device with tubular type fractal structure
CN108946986A (en) * 2018-07-12 2018-12-07 武汉中智德远科技开发有限公司 A kind of rotation immersion water process ultramicro filtration device avoiding blocking
CN110563060A (en) * 2019-10-10 2019-12-13 博天环境集团股份有限公司 Negative-pressure submerged membrane chemical reactor and wastewater treatment method
CN111847589A (en) * 2020-07-28 2020-10-30 铜陵铜冠神虹化工有限责任公司 Sodium sulfide waste water treatment system
CN112642290A (en) * 2020-10-28 2021-04-13 苏州膜海水务科技有限公司 Non-immersed membrane separation device
CN113943048A (en) * 2021-11-30 2022-01-18 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method
CN114632420A (en) * 2022-03-15 2022-06-17 华晋瑞海科技有限公司 Concentrate stainless steel pot-type ultrafiltration system
CN116036868A (en) * 2023-03-08 2023-05-02 泰州南潇新材料科技有限公司 An ultrafiltration membrane module maintaining water flux
CN118255421A (en) * 2024-04-01 2024-06-28 江苏新宇天成环保有限公司 Wastewater treatment device adopting tubular membrane
CN120864625A (en) * 2025-09-09 2025-10-31 山东建筑大学 Membrane filtration device for in-situ purification of water body

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201882973U (en) * 2010-12-13 2011-06-29 北京朗新明环保科技有限公司南京分公司 Immersed membrane bioreactor component
CN103316591A (en) * 2013-07-10 2013-09-25 厦门市威士邦膜科技有限公司 Fan-shaped rotary film separation device
CN204619756U (en) * 2014-12-04 2015-09-09 宗秀兰 A kind of novel dynamic membrane filter system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201882973U (en) * 2010-12-13 2011-06-29 北京朗新明环保科技有限公司南京分公司 Immersed membrane bioreactor component
CN103316591A (en) * 2013-07-10 2013-09-25 厦门市威士邦膜科技有限公司 Fan-shaped rotary film separation device
CN204619756U (en) * 2014-12-04 2015-09-09 宗秀兰 A kind of novel dynamic membrane filter system

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107129040A (en) * 2016-02-29 2017-09-05 鞍钢股份有限公司 Method and device for prolonging service life of membrane of sequencing batch membrane bioreactor
CN107352715A (en) * 2017-08-24 2017-11-17 天津市金通正水处理技术开发有限公司 A kind of integrated type pure water device
CN107737476A (en) * 2017-10-13 2018-02-27 朱平 A kind of rotatable immersion filter
CN108946986B (en) * 2018-07-12 2022-04-29 大庆瑞赛克环保科技有限公司 Prevent rotatory submergence formula water treatment ultramicro filter equipment of jam
CN108946986A (en) * 2018-07-12 2018-12-07 武汉中智德远科技开发有限公司 A kind of rotation immersion water process ultramicro filtration device avoiding blocking
CN108722026A (en) * 2018-08-13 2018-11-02 武汉工程大学 A kind of heterogeneous separation device with sieve-board type fractal structure
CN108722095A (en) * 2018-08-13 2018-11-02 武汉工程大学 A kind of heterogeneous separation device with tubular type fractal structure
CN110563060A (en) * 2019-10-10 2019-12-13 博天环境集团股份有限公司 Negative-pressure submerged membrane chemical reactor and wastewater treatment method
CN111847589A (en) * 2020-07-28 2020-10-30 铜陵铜冠神虹化工有限责任公司 Sodium sulfide waste water treatment system
CN111847589B (en) * 2020-07-28 2021-06-08 铜陵铜冠神虹化工有限责任公司 Sodium sulfide waste water treatment system
CN112642290A (en) * 2020-10-28 2021-04-13 苏州膜海水务科技有限公司 Non-immersed membrane separation device
CN113943048A (en) * 2021-11-30 2022-01-18 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method
CN113943048B (en) * 2021-11-30 2023-09-05 北控水务(中国)投资有限公司 Membrane bioreactor and membrane bioreactor filtering method
CN114632420A (en) * 2022-03-15 2022-06-17 华晋瑞海科技有限公司 Concentrate stainless steel pot-type ultrafiltration system
CN116036868A (en) * 2023-03-08 2023-05-02 泰州南潇新材料科技有限公司 An ultrafiltration membrane module maintaining water flux
CN116036868B (en) * 2023-03-08 2023-10-27 泰州南潇新材料科技有限公司 An ultrafiltration membrane module that maintains water flux
CN118255421A (en) * 2024-04-01 2024-06-28 江苏新宇天成环保有限公司 Wastewater treatment device adopting tubular membrane
CN118255421B (en) * 2024-04-01 2024-10-15 江苏新宇天成环保有限公司 Wastewater treatment device adopting tubular membrane
CN120864625A (en) * 2025-09-09 2025-10-31 山东建筑大学 Membrane filtration device for in-situ purification of water body

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Application publication date: 20160106