CN2682069Y - Automatic control membrane biological reactor - Google Patents
Automatic control membrane biological reactor Download PDFInfo
- Publication number
- CN2682069Y CN2682069Y CNU2004200261427U CN200420026142U CN2682069Y CN 2682069 Y CN2682069 Y CN 2682069Y CN U2004200261427 U CNU2004200261427 U CN U2004200261427U CN 200420026142 U CN200420026142 U CN 200420026142U CN 2682069 Y CN2682069 Y CN 2682069Y
- Authority
- CN
- China
- Prior art keywords
- membrane
- sides
- membrane module
- reactor
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 84
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000003814 drug Substances 0.000 claims abstract description 13
- 238000005273 aeration Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 21
- 238000004140 cleaning Methods 0.000 claims description 9
- 239000012459 cleaning agent Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims 2
- 238000009285 membrane fouling Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 12
- 230000004907 flux Effects 0.000 abstract description 8
- 238000005406 washing Methods 0.000 abstract description 7
- 239000002351 wastewater Substances 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 5
- 238000005452 bending Methods 0.000 abstract description 4
- 229940079593 drug Drugs 0.000 abstract description 4
- 239000010840 domestic wastewater Substances 0.000 abstract description 3
- 230000008859 change Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 description 6
- 230000008021 deposition Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000004677 Nylon Substances 0.000 description 4
- 229920001778 nylon Polymers 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型公开了一种自控式膜生物反应器,它主要由反应器箱体、膜组件、进水装置、出水装置、曝气装置、膜污染控制装置和自动在线药洗装置组成。该反应器在运行过程中,由膜污染控制装置驱动膜丝作往复弯曲运动,使膜丝过滤表面在被处理的水中产生运动,以减少膜污染,并根据水通量的变化判断膜污染程度,自动执行在线药洗程序,去除膜污染。本实用新型操作程序简化,出水水质良好,达到国家规定的杂用水回用标准,可广泛用于对生活废水、餐饮废水和食品工业废水的处理,特别适用于土地资源紧缺、对污水处理要求高的地区使用。
The utility model discloses a self-control membrane bioreactor, which is mainly composed of a reactor box body, a membrane module, a water inlet device, a water outlet device, an aeration device, a membrane pollution control device and an automatic online medicine washing device. During the operation of the reactor, the membrane filament is driven by the membrane pollution control device to make a reciprocating bending movement, so that the filter surface of the membrane filament moves in the treated water to reduce membrane fouling, and the degree of membrane fouling can be judged according to the change of water flux , Automatically execute the online drug washing program to remove membrane pollution. The utility model has simplified operation procedures, good effluent quality, and meets the miscellaneous water reuse standard stipulated by the state. It can be widely used in the treatment of domestic wastewater, catering wastewater and food industry wastewater, and is especially suitable for land resources in short supply and high requirements for sewage treatment. used in the region.
Description
一、技术领域1. Technical field
本实用新型涉及一种污水处理中的膜生物反应器,特别是一种自控式膜生物反应器。The utility model relates to a membrane bioreactor in sewage treatment, in particular to a self-control membrane bioreactor.
二、背景技术2. Background technology
膜生物反应器,由于其具有占地面积小、容积负荷高、出水水质好等诸多优点,而被广泛应用于污水处理领域中。但在目前开发的各类膜生物反应器中,膜的污染和堵塞问题一直没有得到很好的解决。中国专利02205775.7公开了一种“一体式膜生物反应器”,它是由箱体、膜组件、进出水管、导流装置、曝气装置等组成。该反应器分为活性污泥反应区和膜分离区,在活性污泥反应区内设曝气装置,通过曝气产生的膜面错流对膜污染进行过程控制,污染逐步恶化直至造成反应器不能正常运行后,则采用化学药剂浸泡法使膜通量恢复。这种方法在实际应用中存在的问题是:1、需要较高的气水比来提高膜面流速,以减缓膜面污染物的沉积和吸附,而在利用加大曝气强度来提高气水比的过程中,要经过两次能量转换,其能量损失较大,利用率低;2、单位膜面积通量低。该反应器单位膜面积通量一般只有5~10L/m2·h(0.03Mpa下)。因气液流冲洗效率低,能耗大,膜污染难以有效去除,所以,单位膜面积处理水量小,造成膜费用增大。3、膜化学浸泡操作繁复,费工费时,且影响反应器的连续运行,同时造成二次污染,因此工业应用难以实现。Membrane bioreactors are widely used in the field of sewage treatment because of their advantages such as small footprint, high volume load, and good effluent quality. However, in all kinds of membrane bioreactors currently developed, the problems of membrane fouling and clogging have not been well resolved. Chinese patent 02205775.7 discloses an "integrated membrane bioreactor", which is composed of a box body, membrane modules, water inlet and outlet pipes, diversion devices, aeration devices and the like. The reactor is divided into an activated sludge reaction area and a membrane separation area. An aeration device is installed in the activated sludge reaction area, and the process of membrane fouling is controlled by the cross-flow of the membrane surface generated by aeration. The pollution gradually deteriorates until the reactor After the normal operation is not possible, the chemical agent soaking method is used to restore the membrane flux. The problems in the practical application of this method are: 1. A higher air-water ratio is required to increase the flow rate on the membrane surface to slow down the deposition and adsorption of pollutants on the membrane surface. In the process of comparison, two energy conversions are required, and the energy loss is large and the utilization rate is low; 2. The flux per unit membrane area is low. The flux per unit membrane area of the reactor is generally only 5-10L/m 2 ·h (under 0.03Mpa). Due to the low efficiency of gas-liquid flushing, high energy consumption, and difficulty in effectively removing membrane fouling, the amount of treated water per unit membrane area is small, resulting in increased membrane costs. 3. The membrane chemical soaking operation is complicated, labor-intensive and time-consuming, and affects the continuous operation of the reactor and causes secondary pollution, so industrial application is difficult to realize.
三、发明内容3. Contents of the invention
本实用新型的目的在于提供一种能较好地减缓和消除膜污染,同时又能在膜污染严重时对其进行实时在线处理,且运行操作程序简化的自控式膜生物反应器。The purpose of the utility model is to provide a self-control membrane bioreactor that can better slow down and eliminate membrane fouling, and at the same time, when the membrane fouling is serious, it can be processed on-line in real time, and the operation procedure is simplified.
本实用新型的目的是通过以下技术方案来实现的。一种自控式膜生物反应器,它包括反应器箱体、膜组件、进水装置、出水装置以及曝气装置,膜组件由膜丝和集水管构成,它位于反应器箱体内,曝气装置中的曝气管位于反应器箱体内膜组件的下方,其特征是它还包括一个膜污染控制装置和自动在线药洗装置,膜污染控制装置由挡板、支架和电机驱动装置组成,支架位于反应器箱体内膜组件的两边,电机驱动装置位于支架的顶部,挡板位于膜组件中膜丝的中部,挡板两边设置有可在支架上横向运动的上下支撑板,上支撑板开有条形槽,支架两边设有对称的定滑轮,并开有用于支撑挡板上下支撑板的孔,挡板两边还设有连接环,两根驱动绳的一端分别固定在挡板两边的连接环上,另一端通过支架两边的定滑轮、并穿过挡板上支撑板上的条形槽与电机驱动装置连接;自动在线药洗装置主要由控制箱、液位传感器、清洗剂储槽、加药泵、单向阀和两个电动阀组成。液位传感器设置在反应器箱体内膜组件的上方,液位传感器的输出与控制箱输入端相接,清洗药剂储槽的出液口通过加药泵和单向阀与膜组件的集水管相连,该集水管出水处设置有电动阀,清洗药剂储槽的入液口通过另一个电动阀与膜组件的另一端集水管相连,加药泵、两个电动阀、以及进水装置中的进水泵和出水阀均由控制箱控制。上述膜污染控制装置中电机驱动装置是由电机、左右转盘组成,左右转盘由电机带动旋转,其边缘分别设有用于连接驱动绳的转轴。The purpose of this utility model is achieved through the following technical solutions. A self-controlled membrane bioreactor, which includes a reactor box, a membrane module, a water inlet device, a water outlet device, and an aeration device. The membrane module is composed of a membrane wire and a water collection pipe. The aeration pipe in the reactor is located below the membrane module in the reactor box, and it is characterized in that it also includes a membrane pollution control device and an automatic online medicine washing device. The membrane pollution control device is composed of a baffle, a bracket and a motor drive device. The bracket Located on both sides of the membrane module in the reactor box, the motor drive device is located on the top of the bracket, the baffle is located in the middle of the membrane filament in the membrane module, and the upper and lower support plates that can move laterally on the bracket are arranged on both sides of the baffle, and the upper support plate is opened. There are strip grooves, symmetrical fixed pulleys on both sides of the bracket, and holes for supporting the upper and lower support plates of the baffle, and connecting rings on both sides of the baffle. The other end is connected to the motor drive device through the fixed pulleys on both sides of the bracket and through the strip groove on the support plate on the baffle; the automatic online medicine washing device is mainly composed of a control box, a liquid level sensor, a cleaning agent storage tank, It consists of a dosing pump, a one-way valve and two electric valves. The liquid level sensor is set above the membrane assembly in the reactor box, the output of the liquid level sensor is connected to the input end of the control box, and the liquid outlet of the cleaning agent storage tank passes through the dosing pump and the one-way valve to the water collection pipe of the membrane assembly An electric valve is installed at the water outlet of the water collection pipe, and the liquid inlet of the cleaning agent storage tank is connected with the water collection pipe at the other end of the membrane module through another electric valve. The dosing pump, two electric valves, and the water inlet device Both the water inlet pump and the water outlet valve are controlled by the control box. The motor driving device in the above-mentioned membrane pollution control device is composed of a motor and a left and right turntable. The left and right turntables are rotated by the motor, and the edges of the left and right turntables are respectively provided with rotating shafts for connecting the driving ropes.
本实用新型的工作原理是:当反应器运行的整个过程中,膜污染控制装置同时处于工作状态,其电机驱动装置通过驱动绳带动挡板使膜丝在水中作往复弯曲运动,它一方面可以使膜丝间空隙始终处于闭合交替变化的状态,造成膜丝表面较为强烈的紊流;另一方面由于膜组件不同部位膜丝形变的差异,在膜丝之间产生一定的相互摩擦,破坏了沉积层形成所需的条件;此外膜丝弯曲对已形成的沉积层的拉伸作用,造成沉积层破裂、脱落,从而减缓了污染的形成速度。该方法使装置消耗的能量除克服装置运行中的摩擦阻力外,几乎全部作用于膜丝和膜表面附近的混合料液,提高了能耗的利用率和膜污染的去除效率。自动在线药洗装置是通过设置在反应器箱体内的液位传感器控制,进水流量由液体流量计控制为设定值,随膜污染的增加,膜保持通量所需的液位升高,超过最高限位时,由控制箱控制自动关闭进水泵和出水阀,执行在线药洗程序,开启加药泵使清洗药液循环通过膜内腔,去除膜内壁有机污染层,同时通过膜孔的渗透作用,清洗药液渗透至外表面,去除外表面的有机污染层,从而达到清除污染的目的。The working principle of the utility model is: when the whole process of the reactor is running, the membrane pollution control device is in the working state at the same time, and its motor drive device drives the baffle plate through the driving rope to make the membrane wire do reciprocating bending movement in the water. On the one hand, it can The gap between the membrane filaments is always in a state of closed and alternating changes, resulting in a relatively strong turbulent flow on the surface of the membrane filaments; The conditions required for the formation of the deposition layer; in addition, the stretching effect of the bending of the membrane filament on the formed deposition layer causes the deposition layer to break and fall off, thus slowing down the formation of pollution. In this method, besides overcoming the frictional resistance during the operation of the device, almost all of the energy consumed by the device acts on the mixed material liquid near the membrane filament and the membrane surface, which improves the utilization rate of energy consumption and the removal efficiency of membrane fouling. The automatic online medicine washing device is controlled by a liquid level sensor installed in the reactor tank, and the influent flow rate is controlled by a liquid flow meter to a set value. With the increase of membrane fouling, the liquid level required for the membrane to maintain flux increases. When the upper limit is exceeded, the control box will automatically shut down the water inlet pump and the water outlet valve, execute the online drug washing program, turn on the drug dosing pump to circulate the cleaning drug solution through the inner cavity of the membrane, remove the organic pollution layer on the inner wall of the membrane, and at the same time pass through the membrane pores. Osmosis, the cleaning liquid penetrates to the outer surface, removes the organic pollution layer on the outer surface, so as to achieve the purpose of decontamination.
本实用新型与现有技术相比其有益效果是:1、将膜组件与污染控制装置连接,由电机驱动膜丝作往复弯曲运动,使膜丝过滤表面在被处理的水中产生运动,以减少膜污染;2、系统采用自动控制的在线药洗技术,根据水通量的变化判断膜污染程度,自动执行在线药洗程序,去除膜污染,实现了过程的自动控制,同时简化了膜污染清洗的操作程序;3、运行方式易实现,在膜的机械强度允许的范围内,膜丝往复运动的幅度和频率可以方便的调节;4、自动在线药洗使膜污染的化学清洗在反应器内完成,所用药剂本身就可以用于水的杀菌消毒,且用量与化学浸泡法相比较小,不会产生二次污染;5、本实用新型将污染层控制装置与在线清洗系统有效结合,简化了实际操作,使膜通量保持在良好的水平。本实用新型出水水质良好,达到国家规定的杂用水回用标准,可广泛用于对生活废水、餐饮废水和食品工业废水的处理,特别适用于土地资源紧缺、对污水处理要求高的地区使用。Compared with the prior art, the utility model has the beneficial effects as follows: 1. The membrane module is connected with the pollution control device, and the motor drives the membrane wire to perform reciprocating bending motion, so that the membrane wire filter surface moves in the treated water to reduce pollution. Membrane fouling; 2. The system adopts automatic control online chemical washing technology, judges the membrane fouling degree according to the change of water flux, automatically executes the online chemical washing program, removes membrane fouling, realizes automatic control of the process, and simplifies membrane fouling cleaning at the
四、附图说明4. Description of drawings
图1是根据本实用新型所述自控式膜生物反应器的整体结构示意图。Fig. 1 is a schematic diagram of the overall structure of the self-control membrane bioreactor according to the utility model.
图2、图3是本实用新型中的膜污染控制装置结构示意图和立体图。Fig. 2 and Fig. 3 are structural schematic diagrams and perspective views of the membrane fouling control device in the utility model.
图4是本实用新型中的自动在线药洗装置结构示意图。Fig. 4 is a structural schematic diagram of the automatic online medicine washing device in the utility model.
五、具体实施方式5. Specific implementation
下面结合附图对本实用新型的具体结构作进一步详细说明。Below in conjunction with accompanying drawing, the concrete structure of the present utility model is described in further detail.
参见图1,根据本实用新型所述的自控式膜生物反应器,它主要由反应器箱体、膜组件、进水装置、出水装置、曝气装置、膜污染控制装置和自动在线药洗装置组成,膜组件位于反应器箱体13内。参见图2、图3,膜污染控制装置由挡板12、支架23、驱动绳25、定滑轮21以及电机9、左转盘7、右转盘8组成的驱动装置构成,挡板12中部为环形,它固定在膜组件中的膜丝的中部,挡板12两边各有上下两块支撑板28,上支撑板上开有条形槽30;支架23为长方形框架,框架两边各开有两个孔29,挡板的支撑板28从该孔29中穿出,支架23的两边框架上还设有四个定滑轮21,其中两个固定在框架的上边缘,另两个固定在两孔29之间的框架上,驱动绳25为两根尼龙绳,两根尼龙绳25的一端分别与左右转盘7、8边缘的转轴26a、26b相接,另一端分别沿滑轮21a、21b、穿过挡板上支撑板的条型槽30,再经滑轮21c、21d后穿过支架23两边的框架板与固定于挡板左右侧的连接环27相接。另外,为了使挡板12在做往复运动时滑动自如,在支架23两边用于支撑挡板12上下支撑板的孔29处均设置有滑轮22。自动清洗装置由控制箱1、清洗剂储槽3、加药泵15、单向阀5、电动阀4、电动阀10、液位传感器6组成,其位置结构参见图4。Referring to Fig. 1, according to the self-controlled membrane bioreactor described in the utility model, it mainly consists of a reactor box, a membrane module, a water inlet device, a water outlet device, an aeration device, a membrane pollution control device and an automatic online medicine washing device Composition, the membrane module is located in the reactor box 13. Referring to Fig. 2 and Fig. 3, the membrane pollution control device is composed of a driving device consisting of a
本实用新型所述自控式膜生物反应器在运行时,进水通过进水泵2提升,流量由一个阀门20和液体流量计19控制,采用恒定流量的方法,出水液位差通过出水流量与进水流量的平衡自动调节。由气泵18进行曝气,曝气管16位于膜组件正下方,曝气量通过气体流量计17测定并调节。在反应器运行的整个过程中,污染控制装置始终处于工作状态,电机9带动转盘7、8旋转,与转盘上转轴26连接固定的尼龙绳25通过转盘7、8的旋转牵引挡板12作往复运动。使膜丝在挡板12的作用下作横向弯曲运动,阻止膜面沉积层的形成。When the self-controlled membrane bioreactor described in the utility model is in operation, the inlet water is lifted by the inlet pump 2, and the flow rate is controlled by a valve 20 and a liquid flow meter 19. The method of constant flow rate is adopted, and the outlet water level difference is determined by the difference between the outlet water flow rate and the inlet water flow rate. The balance of water flow is automatically adjusted. The aeration is carried out by the air pump 18, the aeration pipe 16 is located directly under the membrane module, and the aeration volume is measured and adjusted by the gas flow meter 17. During the whole process of the reactor operation, the pollution control device is always in the working state, the motor 9 drives the turntable 7, 8 to rotate, and the
反应器运行过程中,电动阀10和出水阀14开启,电动阀4关闭,净化出水通过出水阀14流出。随膜污染的增加,出水流量下降,由于进水流量大于出水流量,反应器内液位上升。当污染达到一定程度后,液面触动液位传感器6,控制箱1内自控电路关闭进水泵2、出水阀14和电动阀10,开启电动阀4、加药泵15,使清洗药剂循环通过膜丝内腔,实现在线污染治理,从而恢复膜通量。清洗完毕后重新关闭电动阀4,开启进水泵2、出水阀14和电动阀10,恢复装置的正常运行。During the operation of the reactor, the
本实用新型自控式膜生物反应器处理生活废水、餐饮废水和食品工业废水,出水水质良好,可达到国家规定的杂用水回用标准。同时生物降解效率高、能耗低,自控程度高、膜组件操作维护方便,使用寿命长,并且占地面积小,安装方便,特别适用于土地资源紧缺、对污水处理要求高的地区使用。The self-controlled membrane bioreactor of the utility model treats domestic waste water, catering waste water and food industry waste water, and the effluent water quality is good, which can reach the miscellaneous water reuse standard stipulated by the state. At the same time, it has high biodegradation efficiency, low energy consumption, high degree of self-control, convenient operation and maintenance of membrane modules, long service life, small footprint, and easy installation. It is especially suitable for use in areas with scarce land resources and high requirements for sewage treatment.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2004200261427U CN2682069Y (en) | 2004-04-09 | 2004-04-09 | Automatic control membrane biological reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2004200261427U CN2682069Y (en) | 2004-04-09 | 2004-04-09 | Automatic control membrane biological reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2682069Y true CN2682069Y (en) | 2005-03-02 |
Family
ID=34607140
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2004200261427U Expired - Fee Related CN2682069Y (en) | 2004-04-09 | 2004-04-09 | Automatic control membrane biological reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2682069Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100375648C (en) * | 2005-11-11 | 2008-03-19 | 清华大学 | On-line chemical cleaning method for membrane-bioreactor |
| CN103288206A (en) * | 2013-06-24 | 2013-09-11 | 金华市洁能环保科技有限公司 | A curtain-style membrane sewage cleaning system |
| CN104192998A (en) * | 2014-09-23 | 2014-12-10 | 吕晓龙 | Immersed membrane separation device and running method thereof |
| CN105129974A (en) * | 2015-08-31 | 2015-12-09 | 北京神州瑞霖环保科技有限公司 | Reciprocating rotary type membrane bioreactor |
| CN117326745A (en) * | 2023-10-30 | 2024-01-02 | 南京理工大学 | Municipal tail water sterilization device and process based on functional membrane filtration technology |
| CN117466431A (en) * | 2023-10-17 | 2024-01-30 | 天津市水利工程集团有限公司 | Intelligent modularized rural domestic sewage membrane method integrated treatment device and method |
-
2004
- 2004-04-09 CN CNU2004200261427U patent/CN2682069Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100375648C (en) * | 2005-11-11 | 2008-03-19 | 清华大学 | On-line chemical cleaning method for membrane-bioreactor |
| CN103288206A (en) * | 2013-06-24 | 2013-09-11 | 金华市洁能环保科技有限公司 | A curtain-style membrane sewage cleaning system |
| CN104192998A (en) * | 2014-09-23 | 2014-12-10 | 吕晓龙 | Immersed membrane separation device and running method thereof |
| CN105129974A (en) * | 2015-08-31 | 2015-12-09 | 北京神州瑞霖环保科技有限公司 | Reciprocating rotary type membrane bioreactor |
| CN117466431A (en) * | 2023-10-17 | 2024-01-30 | 天津市水利工程集团有限公司 | Intelligent modularized rural domestic sewage membrane method integrated treatment device and method |
| CN117326745A (en) * | 2023-10-30 | 2024-01-02 | 南京理工大学 | Municipal tail water sterilization device and process based on functional membrane filtration technology |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103708606B (en) | A kind of pulse energy saving formula MBR method and apparatus | |
| CN110104766A (en) | A kind of sewage water treatment method of pneumatic type biological rotary cage equipment and high-efficiency biological denitrification | |
| CN105198177B (en) | Integrated sewage treating apparatus | |
| CN108069524B (en) | In-situ ecological water activating device | |
| CN204675957U (en) | Integrated sewage treating apparatus | |
| CN207608464U (en) | The device of inversion A AO+MBR integrated sewage disposals | |
| CN116177737A (en) | Method for rapidly culturing aerobic granular sludge and enhancing denitrification | |
| CN2682069Y (en) | Automatic control membrane biological reactor | |
| CN206408055U (en) | Aeration type sewage treatment device | |
| CN1648071A (en) | Split membrane bioreactor | |
| CN113845271B (en) | Resource water purifying device for treating rural domestic sewage and application method thereof | |
| CN207713491U (en) | A kind of microbial augmentation device | |
| CN101830607A (en) | Alternate two-stage aerobic membrane bioreactor | |
| CN118307157A (en) | Livestock and poultry manure sewage aerobic treatment system | |
| CN216687606U (en) | Biological treatment device for dairy waste water | |
| CN115650411A (en) | Unpowered backflow composite biological rotary drum type sewage treatment device | |
| CN212403632U (en) | Device for promoting aerobic floc sludge to be rapidly granulated by utilizing moving magnetic field | |
| CN202279728U (en) | Membrane bioreactor and activated sludge combined sewage treatment device | |
| CN212770323U (en) | A tank type sewage biological deep purification device | |
| CN211470944U (en) | Vertical flow type hydrolysis acidification reactor | |
| CN114620903A (en) | Sewage treatment station conveying system based on Roots blower drive | |
| CN208200663U (en) | Circulating biological embrane method sewage disposal system | |
| CN209226765U (en) | A kind of starch wastewater treatment device | |
| CN223823464U (en) | A wastewater treatment device | |
| CN1789167A (en) | Integrated tubular dynamic membrane bioreactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20050302 |
