CN201098608Y - Integrated membrane filter and its filtration system - Google Patents
Integrated membrane filter and its filtration system Download PDFInfo
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- CN201098608Y CN201098608Y CNU2007200967994U CN200720096799U CN201098608Y CN 201098608 Y CN201098608 Y CN 201098608Y CN U2007200967994 U CNU2007200967994 U CN U2007200967994U CN 200720096799 U CN200720096799 U CN 200720096799U CN 201098608 Y CN201098608 Y CN 201098608Y
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- 239000012528 membrane Substances 0.000 title claims abstract description 127
- 238000001914 filtration Methods 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 75
- 238000004519 manufacturing process Methods 0.000 claims abstract description 28
- 239000012510 hollow fiber Substances 0.000 claims abstract description 20
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims description 7
- 239000002033 PVDF binder Substances 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 229920000573 polyethylene Polymers 0.000 claims description 5
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 3
- -1 polyethylene Polymers 0.000 claims description 3
- 239000004800 polyvinyl chloride Substances 0.000 claims description 3
- 238000011045 prefiltration Methods 0.000 claims description 3
- 238000005728 strengthening Methods 0.000 claims description 3
- 239000004695 Polyether sulfone Substances 0.000 claims 1
- 229920006393 polyether sulfone Polymers 0.000 claims 1
- 229920000915 polyvinyl chloride Polymers 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 7
- 238000004065 wastewater treatment Methods 0.000 abstract description 6
- 238000011001 backwashing Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000000746 purification Methods 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 2
- 238000001223 reverse osmosis Methods 0.000 abstract description 2
- 239000013535 sea water Substances 0.000 abstract description 2
- 238000010612 desalination reaction Methods 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000008213 purified water Substances 0.000 abstract 1
- 230000004907 flux Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000003670 easy-to-clean Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
-
- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
用于废水处理的一体式膜过滤器及过滤系统。原水经预处理后进入一体式膜过滤器,包括浸入式中空纤维膜组件、上孔板,下孔板,进水管,产水管及进气管等。膜组件为柱状或帘式不含外壳的膜组件,其下部通过裙座、下孔板固定安装于膜过滤器的槽体或池子内,净化水通过抽吸水泵抽吸出水。本实用新型省掉了许多复杂的管路系统,整体设备占地面积小,结构简单,设备中设置了自动反冲洗装置、曝气装置、清洗装置、使得设备不仅具有高效处理的性能,还具有膜自动维护清洗功能。该系统过滤性能稳定,单位水处理能耗低,减小单位水处理费用,提高了该技术在水处理行业应用中的经济实用性。本实用新型可用于水净化,废水处理,海水淡化及反渗透预处理等领域。
Integrated membrane filters and filtration systems for wastewater treatment. The raw water enters the integrated membrane filter after pretreatment, including the submerged hollow fiber membrane module, the upper orifice plate, the lower orifice plate, the water inlet pipe, the water production pipe and the air inlet pipe, etc. The membrane module is a columnar or curtain-type membrane module without a shell, and its lower part is fixedly installed in the tank or pool of the membrane filter through the skirt seat and the lower orifice plate, and the purified water is sucked out by the suction pump. The utility model saves many complex pipeline systems, the overall equipment occupies a small area, and has a simple structure. The equipment is equipped with an automatic backwashing device, an aeration device, and a cleaning device, so that the equipment not only has the performance of efficient processing, but also has Membrane automatic maintenance cleaning function. The system has stable filtration performance, low energy consumption per unit of water treatment, reduces unit water treatment costs, and improves the economical practicability of this technology in the water treatment industry. The utility model can be used in the fields of water purification, waste water treatment, seawater desalination, reverse osmosis pretreatment and the like.
Description
【技术领域】 【Technical field】
本实用新型属于水处理行业的水净化与废水处理技术领域。特别涉及一种用于水处理的一体式膜过滤器及其过滤系统。The utility model belongs to the technical field of water purification and waste water treatment in the water treatment industry. In particular, it relates to an integrated membrane filter for water treatment and a filtering system thereof.
【背景技术】 【Background technique】
随着社会经济的高速发展,全球性水资源匾乏问题日益突出,迫切需要实用而有效的水处理新技术与新装备,本实用新型一体式膜过滤器是基于膜分离技术而产生的用于水净化与废水深度处理的新技术与新设备,该实用新型技术具有污染物去除效率高、出水水质好等特点,具有良好的发展前景。With the rapid development of social economy, the problem of lack of global water resources has become increasingly prominent, and there is an urgent need for practical and effective water treatment new technologies and new equipment. The utility model integrated membrane filter is based on membrane separation technology and is used for New technology and new equipment for water purification and advanced wastewater treatment. This utility model technology has the characteristics of high pollutant removal efficiency and good effluent quality, and has a good development prospect.
目前用于废水处理的膜生物反应器其缺点是所需膜面积大、膜片间连接管路多、占地面积大、整个膜组件的管理不方便,并且在处理污水后一段时间,整个膜组件设备变得沉重,不易进行清洗,其出水指标难以达到各项出水相应的水质标准。The disadvantages of membrane bioreactors currently used for wastewater treatment are that the required membrane area is large, there are many connecting pipelines between the membranes, the floor area is large, and the management of the entire membrane module is inconvenient, and after a period of time after sewage treatment, the entire membrane The component equipment becomes heavy and difficult to clean, and its effluent indicators are difficult to meet the corresponding water quality standards for each effluent.
【发明内容】 【Content of invention】
本实用新型的目的是解决现有技术存在的上述不足,提供一种一体式膜过滤器以及由该一体式膜过滤器构成的过滤系统。The purpose of the utility model is to solve the above-mentioned deficiencies in the prior art, and provide an integrated membrane filter and a filtration system composed of the integrated membrane filter.
该一体式膜过滤器能克服上述缺陷,使其占地面积少,体积小,管路少,结构简单、清洗方便、更换及增设容易、膜组件工作寿命长。采用连续或间歇曝气,间歇出水,在线自动清洗的方式来减小膜的污染,各项出水指标稳定合格,运行稳定,减小操作成本。The one-piece membrane filter can overcome the above-mentioned defects, so that it occupies less land, is small in size, has few pipelines, simple in structure, easy to clean, easy to replace and add, and has a long working life of the membrane components. Continuous or intermittent aeration, intermittent water discharge, and online automatic cleaning are used to reduce membrane pollution. The water discharge indicators are stable and qualified, the operation is stable, and the operating cost is reduced.
本实用新型提供的一体式膜过滤器,包括槽体或池子及一组中空纤维膜组件,中空纤维膜组件通过槽体或池子底部安装的下孔板及其上的裙座固定安装在槽体或池子内,槽体或池子的上部同时安装有用于加强固定中空纤维膜组件的上孔板;一体式膜过滤器的进水管和进气管均由槽体或池子的上部引进,进气管由上部引进至膜组件底部的曝气管,曝气管由一根总管分为两个支管通入膜过滤器的槽体或池子底部,并绕成环形均匀分布于膜组件的下方均匀曝气;产水管路布置于膜组件的上方。The integrated membrane filter provided by the utility model includes a tank body or a pond and a group of hollow fiber membrane modules, and the hollow fiber membrane module is fixedly installed in the tank body through the lower orifice plate installed at the bottom of the tank body or the pond and the skirt seat on it Or in the pool, the upper part of the tank or the pool is equipped with an upper orifice plate for strengthening and fixing the hollow fiber membrane module; the water inlet pipe and the air inlet pipe of the integrated membrane filter are introduced from the upper part of the tank or the pool, and the air intake pipe is introduced from the upper part The aeration pipe introduced to the bottom of the membrane module, the aeration pipe is divided into two branch pipes by a main pipe, leading to the bottom of the tank or pool of the membrane filter, and evenly distributed under the membrane module in a ring shape to aerate evenly; The water pipeline is arranged above the membrane module.
所述的中空纤维膜组件为柱状或帘式不含外壳的膜组件。所用膜形式为外压式中空纤维膜;膜材质为亲水性聚醚砜(PES)、聚偏氟乙烯(PVDF)、聚氯乙烯(PVC)、或聚乙烯(PE)中的一种。优选采用亲水性且膜孔径分布窄的膜生物反应器专用膜材料,膜的孔径为0.01~0.45微米。The hollow fiber membrane module is a columnar or curtain-type membrane module without a shell. The membrane used is an external pressure hollow fiber membrane; the membrane material is one of hydrophilic polyethersulfone (PES), polyvinylidene fluoride (PVDF), polyvinyl chloride (PVC), or polyethylene (PE). It is preferred to use a special membrane material for membrane bioreactors that is hydrophilic and has a narrow membrane pore size distribution, and the pore size of the membrane is 0.01-0.45 microns.
所述的下孔板上开有用于固定膜组件的固定孔,和用于使膜组件能够充分曝气的导流孔,固定孔与导流孔相间设置,且固定孔孔径大于导流孔孔径。The lower orifice plate is provided with fixing holes for fixing the membrane module, and diversion holes for fully aerating the membrane module, the fixing holes and the diversion holes are arranged alternately, and the diameter of the fixing holes is larger than the diameter of the diversion holes .
本实用新型同时提供了一种由上述一体式膜过滤器构成的过滤系统,即,上述一体式膜过滤器的进水管分别经过进水阀门和前级过滤器接来水;进气管经过气动阀门连接鼓风机;产水管路经过产水阀门连接产水用抽吸水泵,再经过管路送入产水箱。The utility model also provides a filtration system composed of the above-mentioned integrated membrane filter, that is, the water inlet pipe of the above-mentioned integrated membrane filter receives water through the water inlet valve and the pre-filter respectively; the air inlet pipe passes through the pneumatic valve Connect the blower; the production water pipeline is connected to the suction pump for production water through the production water valve, and then sent to the production water tank through the pipeline.
在产水阀门之前的产水管路上与产水箱之间同时安装由反洗水泵及反洗管路阀门构成的反冲洗回路。A backwash circuit composed of a backwash water pump and a backwash pipeline valve is installed between the product water pipeline before the water production valve and the product water tank.
本实用新型的优点和积极效果:Advantage and positive effect of the utility model:
膜过滤器为一体式,将中空纤维膜安装在膜过滤器内,压力驱动靠抽吸水泵,省掉了许多复杂的管路系统,整体设备占地面积小,外观精巧,节约大量连接管件,设备中设置了自动反冲洗装置、曝气装置、清洗装置、使得设备不仅具有高效处理的性能,还具有膜自动维护清洗功能。膜组件采用中空纤维膜制成,膜组件的工作寿命长,膜通量能维持稳定,本实用新型整套系统也更加便于工作人员的操作与管理。结构简单,清洗、更换及增设方便。本实用新型可用于水净化,废水处理,海水净化以及反渗透预处理等领域。The membrane filter is integrated, the hollow fiber membrane is installed in the membrane filter, and the pressure is driven by the suction pump, which saves many complicated piping systems, the overall equipment occupies a small area, the appearance is exquisite, and a large number of connecting pipes are saved. The equipment is equipped with automatic backwashing device, aeration device and cleaning device, so that the equipment not only has the performance of efficient treatment, but also has the function of automatic membrane maintenance and cleaning. The membrane module is made of hollow fiber membrane, the working life of the membrane module is long, and the membrane flux can be kept stable. The whole system of the utility model is also more convenient for the operation and management of the staff. Simple structure, easy to clean, replace and add. The utility model can be used in the fields of water purification, waste water treatment, seawater purification, reverse osmosis pretreatment and the like.
【附图说明】 【Description of drawings】
图1是一体式膜过滤器构成的过滤系统总体结构示意图,Figure 1 is a schematic diagram of the overall structure of a filtration system composed of an integrated membrane filter,
图2是一体式膜过滤器正视图,Figure 2 is a front view of the integrated membrane filter,
图3是一体式膜过滤器俯视图,Figure 3 is a top view of the integrated membrane filter,
图4是一体式膜过滤器剖面图,Figure 4 is a sectional view of an integrated membrane filter,
图5是一体式膜过滤器孔板图。Fig. 5 is a diagram of an orifice plate of an integrated membrane filter.
其中,1中空纤维膜组件、2裙座、3下孔板、4中间孔板、5上孔板、6进气管、7进水管、8产水管、9抽吸水泵、10鼓风机、11反洗水泵、12溢流孔、13仪表孔、14、排污口、15槽体(也可以是池子)、16产水箱、17叠片过滤器。Among them, 1 hollow fiber membrane module, 2 skirt, 3 lower orifice plate, 4 middle orifice plate, 5 upper orifice plate, 6 inlet pipe, 7 water inlet pipe, 8 water production pipe, 9 suction pump, 10 blower, 11 backwash Water pump, 12 overflow holes, 13 instrument holes, 14, sewage outlet, 15 tank body (also can be pool), 16 water production tanks, 17 laminated filters.
【具体实施方式】 【Detailed ways】
实施例1一体式膜过滤器Embodiment 1 integrated membrane filter
如图2至5所示,该一体式膜过滤器,包括槽体15(也可以是池子),一组中空纤维膜组件1通过槽体15底部安装的下孔板3及其上的裙座2固定安装在槽体15内,膜组件之间保持距离便于拆卸更换。槽体的上部和中部同时安装有用于加强固定中空纤维膜组件的上孔板5和中间孔板4;进水管7和进气管6均由槽体的上部引进,进气管由上部引进至膜组件1底部的曝气管,曝气管由一根总管分为两个支管通入膜过滤器的槽体底部,并绕成环形均匀分布于膜组件的下方均匀曝气,曝气可以是连续或间歇的方式进行。曝气量控制在气水比为0.5~10∶1。产水管路8布置于膜组件1的上方。As shown in Figures 2 to 5, this integrated membrane filter includes a tank body 15 (also can be a pond), a group of hollow fiber membrane modules 1 are installed through the
中空纤维膜组件为柱状或帘式不含外壳的膜组件。所用膜形式为外压式中空纤维膜;膜材质为亲水性聚醚砜(PES)、聚偏氟乙烯(PVDF)、聚氯乙烯(PVC)、或聚乙烯(PE)中的一种。优选采用亲水性且膜孔径分布窄的膜生物反应器专用膜材料,膜的孔径为0.01~0.45微米。The hollow fiber membrane module is a columnar or curtain-type membrane module without a shell. The membrane used is an external pressure hollow fiber membrane; the membrane material is one of hydrophilic polyethersulfone (PES), polyvinylidene fluoride (PVDF), polyvinyl chloride (PVC), or polyethylene (PE). It is preferred to use a special membrane material for membrane bioreactors that is hydrophilic and has a narrow membrane pore size distribution, and the pore size of the membrane is 0.01-0.45 microns.
如图5所示,下孔板上开有用于固定膜组件1的固定孔,和用于使膜组件能够充分曝气的导流孔,下孔板开孔均匀,固定孔孔径大于导流孔孔径,且固定孔与导流孔相间设置,使膜组件能够充分曝气。As shown in Figure 5, the lower orifice plate is provided with fixing holes for fixing the membrane module 1 and diversion holes for fully aerating the membrane module. The pore size, and the fixed holes and diversion holes are arranged alternately, so that the membrane module can be fully aerated.
中间孔板和上孔板对膜组件固定进行了加强,防止膜组件上部不稳定而发生上浮,管路之间不稳定变形导致管路漏水的问题。The middle orifice plate and the upper orifice plate strengthen the fixation of the membrane module to prevent the upper part of the membrane module from being unstable and floating, and the unstable deformation between the pipelines leads to the problem of pipeline leakage.
实施例2一体式膜过滤器构成的过滤系统Example 2 Filtration system composed of integrated membrane filter
如图1所示,本实用新型同时提供了一种由上述一体式膜过滤器构成的过滤系统,即,上述一体式膜过滤器的进水管7分别经过进水阀门DF1和前级过滤器(叠片过滤器17)接来水;进气管6经过气动阀门QF1连接鼓风机10;产水管路8经过产水阀门DF2连接产水用抽吸水泵9,再经过管路送入产水箱16。As shown in Figure 1, the utility model simultaneously provides a kind of filter system that is made of above-mentioned integrated membrane filter, namely, the
在产水阀门之前的产水管路8上与产水箱16之间同时安装由反洗水泵11及反洗管路阀门构成的反冲洗回路。A backwash circuit composed of a
本实用新型的工作过程是:The working process of the present utility model is:
(1)膜过滤器操作前准备工作:向一体式膜过滤器内注水直到溢流后,开启鼓风,膜过滤器均匀的鼓气,鼓气量大约每支膜组件0.2-1m3/h左右即可以。鼓风10min后,停止进水和鼓风,将膜过滤器内的水排净,再次进水冲洗膜器,冲洗干净。(1) Preparations before operation of the membrane filter: pour water into the integrated membrane filter until it overflows, then turn on the blower, and the membrane filter will blow air evenly, and the blowing volume is about 0.2-1m 3 /h for each membrane module That's it. After blowing for 10 minutes, stop water intake and blowing, drain the water in the membrane filter, and then rinse the membrane filter with water again, and rinse it clean.
(2)过滤操作:一体式膜过滤器相关设备、仪表等的单机调试后,膜过滤器再次进水并开启鼓风,开始正常过滤(产水),膜过滤器产水过程中注意观察相关设备、仪表运转正常。具体操作为:先开启产水阀门DF2,将产水流量定为额定值的1/3,然后再开启抽吸水泵,与此同时自动进水阀门DF1、气动阀门QFI、鼓风机仍然保持打开。开机运行时确认产水手动调节阀门V2处在产水流量额定值的1/3的状态,待产水渐渐稳定后,调节系统的压力慢慢上升,直至达到所要求的设计产水量要求。要注意观察相关设备、仪表是否正常。(2) Filtration operation: After the stand-alone debugging of the integrated membrane filter related equipment, instruments, etc., the membrane filter is fed with water again and the blast is turned on to start normal filtration (water production). During the water production process of the membrane filter, pay attention to the related Equipment and instruments are operating normally. The specific operation is: first open the water production valve DF2, set the production water flow rate to 1/3 of the rated value, and then turn on the suction pump, while the automatic water inlet valve DF1, the pneumatic valve QFI, and the blower remain open. When starting up and running, confirm that the water production manual adjustment valve V2 is in the state of 1/3 of the rated water production flow rate. After the production water gradually stabilizes, the pressure of the regulating system will rise slowly until the required design water production volume is reached. Pay attention to observe whether the relevant equipment and instruments are normal.
(3)反洗操作:反冲洗过程分为两组分别进行,反洗水泵利用产水对膜组件设备进行反冲洗。依次将抽吸水泵,产水阀门DF2关闭后,开启自动反洗阀门DF3、反洗手动调节阀V3,确认反洗手动调节阀门V3处在反洗流量额定值的1/3状态,反洗渐渐稳定后缓慢调节反洗手动调节阀V3,让反洗的压力逐渐上升到0.1MPa左右,反洗过程时的水通量为正常产水水量的2-3倍。(3) Backwashing operation: The backwashing process is divided into two groups, and the backwashing pump uses the produced water to backwash the membrane module equipment. Turn off the suction pump and production water valve DF2 in sequence, then open the automatic backwash valve DF3 and the backwash manual control valve V3, and confirm that the backwash manual control valve V3 is in the state of 1/3 of the backwash flow rate, and the backwash gradually After stabilization, slowly adjust the backwash manual control valve V3, so that the backwash pressure gradually rises to about 0.1MPa, and the water flux during the backwash process is 2-3 times the normal water production.
本实用新型提供的一体式膜过滤器及过滤系统,克服了现有技术占地面积大,不易清洗,膜通量衰减等问题,具有占地面积小,连续曝气,间歇出水的特点。该过滤系统以在线清洗的方式来减小膜的污染,维持稳定的膜通量,减少水处理制水成本,节约能源。The integrated membrane filter and filtration system provided by the utility model overcomes the problems of the prior art such as large occupied area, difficult cleaning, membrane flux attenuation, etc., and has the characteristics of small occupied area, continuous aeration, and intermittent water discharge. The filtration system uses online cleaning to reduce membrane pollution, maintain stable membrane flux, reduce water treatment costs, and save energy.
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Cited By (2)
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CN107321187A (en) * | 2017-07-04 | 2017-11-07 | 中山市创思泰新材料科技股份有限公司 | A kind of sour wastewater treatment equipment of use membrane technology |
CN109179888A (en) * | 2018-09-30 | 2019-01-11 | 浙江工商大学 | The wastewater treatment equipment and technique of integrated ozone coupling membrane bioreactor |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107321187A (en) * | 2017-07-04 | 2017-11-07 | 中山市创思泰新材料科技股份有限公司 | A kind of sour wastewater treatment equipment of use membrane technology |
CN109179888A (en) * | 2018-09-30 | 2019-01-11 | 浙江工商大学 | The wastewater treatment equipment and technique of integrated ozone coupling membrane bioreactor |
CN109179888B (en) * | 2018-09-30 | 2021-10-22 | 浙江工商大学 | Wastewater treatment device and process for integrated ozone-coupled membrane bioreactor |
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