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CN112028378A - Integrated treatment system for semiconductor industrial wastewater - Google Patents

Integrated treatment system for semiconductor industrial wastewater Download PDF

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CN112028378A
CN112028378A CN201910480304.5A CN201910480304A CN112028378A CN 112028378 A CN112028378 A CN 112028378A CN 201910480304 A CN201910480304 A CN 201910480304A CN 112028378 A CN112028378 A CN 112028378A
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mbr
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林超
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Weitai Technology Wuxi Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/346Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from semiconductor processing, e.g. waste water from polishing of wafers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes

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  • Engineering & Computer Science (AREA)
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  • Water Treatment By Sorption (AREA)

Abstract

本发明公开了一种用于半导体工业废水一体化处理系统,包括废水收集池,MBR膜处理单元、活性炭过滤单元、MF处理单元,所述废水收集池通过管道依次与MBR膜处理单元、活性炭过滤单元、MF处理单元连接,储水池,各部分通过管道连接,构成了一体化处理系统,处理的半导体废水主要是有机废水,其净化后的水主要用于厂区内冷却塔、废气洗涤塔和绿化用水,此一体化处理系统不仅能够节约大量水资源,而且降低环境污染,解决半导体工业废水循环再利用问题,实现废水资源化。

Figure 201910480304

The invention discloses an integrated treatment system for semiconductor industry wastewater, comprising a wastewater collection tank, an MBR membrane treatment unit, an activated carbon filter unit, and an MF treatment unit. The unit and the MF treatment unit are connected, and the water storage tank is connected by pipes to form an integrated treatment system. The treated semiconductor wastewater is mainly organic wastewater, and the purified water is mainly used for cooling towers, waste gas washing towers and greening in the factory area. This integrated treatment system can not only save a lot of water resources, but also reduce environmental pollution, solve the problem of recycling and reuse of wastewater in the semiconductor industry, and realize the recycling of wastewater.

Figure 201910480304

Description

一种用于半导体工业废水一体化处理系统An integrated treatment system for semiconductor industry wastewater

技术领域technical field

本发明属于工业再生水处理领域,尤其涉及一种用于半导体工业废水一体化处理系统。The invention belongs to the field of industrial regeneration water treatment, and in particular relates to an integrated treatment system for semiconductor industrial wastewater.

背景技术Background technique

半导体行业是一个高能耗行业,在半导体生产制造过程中,会产生大量工业废水。随着水和其他资源日渐短缺以及环境污染治理日益迫切的情况下,工业废水的发展趋势是:把水和污染物作为有用资源回收利用和实行闭路循环。膜分离技术可以完美的达到以上标准,随着水处理技术的发展,该工艺开始逐渐在水处理的环节中得到应用。The semiconductor industry is a high energy consumption industry, and a large amount of industrial waste water will be generated during the semiconductor manufacturing process. With the increasing shortage of water and other resources and the increasing urgency of environmental pollution control, the development trend of industrial wastewater is to recycle water and pollutants as useful resources and implement closed-circuit circulation. Membrane separation technology can perfectly meet the above standards. With the development of water treatment technology, this process has gradually been applied in water treatment.

在污水处理,水资源再利用领域,MBR又称膜生物反应器(Membrane Bio-Reactor),是一种由活性污泥法与膜分离技术相结合的新型水处理技术。In the field of sewage treatment and water resource reuse, MBR, also known as Membrane Bio-Reactor, is a new type of water treatment technology that combines activated sludge process and membrane separation technology.

在申请号为:CN201820915919.7,申请日为:20180613名称为:一种对流式MBR废水处理设备的专利中,公开了一种对流式MBR废水处理设备,包括MBR池、MBR膜片和风机,所述MBR池的内部下侧连接有第一连接块,且第一连接块的上方卡合连接有MBR膜连接块,所述MBR池的右下侧设置有第四阀门,且第四阀门通过双通水管与MBR池相连接,所述风机通过双通水管与MBR膜连接块相连接,且风机的左侧设置有第一阀门,并且第一阀门位于MBR池的右侧,所述MBR膜片的上下两侧均设置与MBR膜连接块。该对流式MBR废水处理设备。The application number is: CN201820915919.7, the application date is: 20180613, and the title is: A convective MBR wastewater treatment equipment patent, discloses a convective MBR wastewater treatment equipment, including MBR pool, MBR diaphragm and fan, The inner lower side of the MBR pool is connected with a first connection block, and the top of the first connection block is connected with an MBR membrane connection block, and the lower right side of the MBR pool is provided with a fourth valve, and the fourth valve passes through The double-pass water pipe is connected to the MBR pool, the fan is connected to the MBR membrane connecting block through the double-pass water pipe, and the left side of the fan is provided with a first valve, and the first valve is located on the right side of the MBR pool, the MBR membrane The upper and lower sides of the sheet are provided with blocks connected to the MBR film. The convective MBR wastewater treatment equipment.

在申请号为:CN201620520752.5,申请日为:20160601名称为:一种水处理设备的专利中公开了一种水处理设备,所述水处理设备至少包括网格滤池、高级氧化单元、生物活性炭吸附池以及MF过滤单元,所述第一臭氧接触池与所述生物活性炭吸附池并列通过滤后水箱连接至预网格滤池,所述第二臭氧接触池单元双向连接所述生物活性炭吸附池;所述生物活性炭吸附池连接MF过滤单元,所述MF过滤单元连接MF产水箱;所述网格滤池分别连接进水提升泵、PFS/PFM加药装置、废水收集箱、废水提升泵、滤后水箱、滤后水提升泵以及反洗泵;所述高级氧化单元包括第一臭氧接触池和第二臭氧接触池。本发明在节能降耗保护环境方面具有重大意义。The application number is: CN201620520752.5, the application date is: 20160601 The patent titled: A water treatment equipment discloses a water treatment equipment, the water treatment equipment at least includes a grid filter, an advanced oxidation unit, a biological Activated carbon adsorption tank and MF filter unit, the first ozone contact tank and the biological activated carbon adsorption tank are connected in parallel to the pre-grid filter tank through the filtered water tank, and the second ozone contact tank unit is bidirectionally connected to the biological activated carbon adsorption tank The biological activated carbon adsorption tank is connected to the MF filter unit, and the MF filter unit is connected to the MF water production tank; , filtered water tank, filtered water lift pump and backwash pump; the advanced oxidation unit includes a first ozone contact pool and a second ozone contact pool. The invention has great significance in saving energy, reducing consumption and protecting the environment.

发明内容SUMMARY OF THE INVENTION

本发明所解决的技术问题在于提供一种用于半导体工业废水一体化处理系统。The technical problem solved by the present invention is to provide an integrated treatment system for semiconductor industry wastewater.

本发明的的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:

一种用于半导体工业废水一体化处理系统,包括废水收集池,MBR膜处理单元、活性炭过滤单元、MF处理单元,所述废水收集池通过管道依次与MBR膜处理单元、活性炭过滤单元、MF处理单元连接,储水池;An integrated treatment system for semiconductor industry wastewater, comprising a wastewater collection tank, an MBR membrane treatment unit, an activated carbon filter unit, and an MF treatment unit. unit connection, reservoir;

所述MBR膜处理单元包括pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,MBR产水池,所述pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,MBR产水池依次通过管道连接,所述MBR一体化装置设有MBR膜组件、生物反应器、鼓风机,所述MBR膜组件设置在生物反应器内部;The MBR membrane treatment unit includes a pH adjustment tank, an anaerobic tank, an anoxic tank, an aerobic tank, an MBR integrated device, an MBR water production tank, the pH adjustment tank, the anaerobic tank, the anoxic tank, the aerobic tank, MBR integrated device, MBR water production pools are sequentially connected through pipelines, the MBR integrated device is provided with an MBR membrane module, a bioreactor, and a blower, and the MBR membrane module is arranged inside the bioreactor;

所述活性炭过滤单元包括活性炭过滤器,所述活性炭过滤器为内装填粗石英砂垫层及活性炭的压力容器,The activated carbon filter unit includes an activated carbon filter, and the activated carbon filter is a pressure vessel filled with a coarse quartz sand cushion and activated carbon,

所述MF处理单元包括滤芯,所述滤芯包括微滤膜、内外导流层、滤芯端盖、壳体及中心杆。The MF processing unit includes a filter element, and the filter element includes a microfiltration membrane, an inner and outer diversion layer, an end cover of the filter element, a casing and a center rod.

优选的,所述MBR一体化装置包括活性污泥系统、所述活性污泥系统设置在MBR膜组件之前,所述废水经过好氧池通过管道进入活性污泥系统。Preferably, the MBR integrated device includes an activated sludge system, the activated sludge system is arranged before the MBR membrane module, and the waste water enters the activated sludge system through a pipeline through an aerobic tank.

更优选的,所述MBR储水池与MBR产水池之间设有抽吸泵。More preferably, a suction pump is provided between the MBR water storage tank and the MBR water production tank.

更优选的,所述MBR膜组件孔径为0.01μm-0.03μm。More preferably, the pore size of the MBR membrane module is 0.01 μm-0.03 μm.

更优选的,所述MBR膜处理单元还包括污泥回流系统和反洗泵,所述污泥回流系统设置在MBR一体化装置内,所述反洗泵设置在污泥回流系统内。More preferably, the MBR membrane treatment unit further includes a sludge return system and a backwash pump, the sludge return system is arranged in the MBR integrated device, and the backwash pump is arranged in the sludge return system.

优选的,所述活性炭过滤器的外壳为不锈钢或者玻璃钢。Preferably, the shell of the activated carbon filter is stainless steel or glass fiber reinforced plastic.

优选的,所述MF处理单元的微滤膜为有机高分子膜。Preferably, the microfiltration membrane of the MF processing unit is an organic polymer membrane.

本发明的有益效果:Beneficial effects of the present invention:

此系统废水收集池,MBR膜处理单元、活性炭过滤单元、MF处理单元的设置使得此系统不仅能够有效的去除半导体工业废水的污染物质,而且能够实现废水循环再利用,不仅能够节约大量水资源,而且降低环境污染。The system wastewater collection tank, MBR membrane treatment unit, activated carbon filter unit, and MF treatment unit are set up, so that this system can not only effectively remove the pollutants from the semiconductor industry wastewater, but also realize the recycling of wastewater, which can not only save a lot of water resources, And reduce environmental pollution.

附图说明Description of drawings

图1为一种用于半导体工业废水一体化处理系统的结构示意图。FIG. 1 is a schematic structural diagram of an integrated treatment system for wastewater in the semiconductor industry.

具体实施方式Detailed ways

结合附图所示,本发明的技术方案作进一步的描述:As shown in conjunction with the accompanying drawings, the technical scheme of the present invention is further described:

一种用于半导体工业废水一体化处理系统,包括废水收集池,MBR膜处理单元、活性炭过滤单元、MF处理单元,所述废水收集池通过管道依次与MBR膜处理单元、活性炭过滤单元、MF处理单元连接,储水池;An integrated treatment system for semiconductor industry wastewater, comprising a wastewater collection tank, an MBR membrane treatment unit, an activated carbon filter unit, and an MF treatment unit. unit connection, reservoir;

所述MBR膜处理单元包括pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,MBR产水池,所述pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,MBR产水池依次通过管道连接,所述MBR一体化装置设有MBR膜组件、生物反应器、鼓风机,所述MBR膜组件设置在生物反应器内部;The MBR membrane treatment unit includes a pH adjustment tank, an anaerobic tank, an anoxic tank, an aerobic tank, an MBR integrated device, an MBR water production tank, the pH adjustment tank, the anaerobic tank, the anoxic tank, the aerobic tank, MBR integrated device, MBR water production pools are sequentially connected through pipelines, the MBR integrated device is provided with an MBR membrane module, a bioreactor, and a blower, and the MBR membrane module is arranged inside the bioreactor;

所述活性炭过滤单元包括活性炭过滤器,所述活性炭过滤器为内装填粗石英砂垫层及活性炭的压力容器,The activated carbon filter unit includes an activated carbon filter, and the activated carbon filter is a pressure vessel filled with a coarse quartz sand cushion and activated carbon,

所述MF处理单元包括滤芯,所述滤芯包括微滤膜、内外导流层、滤芯端盖、壳体及中心杆。The MF processing unit includes a filter element, and the filter element includes a microfiltration membrane, an inner and outer diversion layer, an end cover of the filter element, a casing and a center rod.

本实施例中,优选的,所述MBR一体化装置包括活性污泥系统、所述活性污泥系统设置在MBR膜组件之前,所述废水经过好氧池通过管道进入活性污泥系统。In this embodiment, preferably, the MBR integrated device includes an activated sludge system, the activated sludge system is arranged before the MBR membrane module, and the waste water enters the activated sludge system through a pipeline through an aerobic tank.

本实施例中,优选的,所述MBR储水池与MBR产水池之间设有抽吸泵。In this embodiment, preferably, a suction pump is provided between the MBR water storage tank and the MBR water production tank.

本实施例中,优选的,所述MBR膜组件孔径为0.01μm-0.03μm。In this embodiment, preferably, the pore size of the MBR membrane module is 0.01 μm-0.03 μm.

本实施例中,优选的,所述MBR膜处理单元还包括污泥回流系统和反洗泵,所述污泥回流系统设置在MBR一体化装置内,所述反洗泵设置在污泥回流系统内。In this embodiment, preferably, the MBR membrane treatment unit further includes a sludge return system and a backwash pump, the sludge return system is arranged in the MBR integrated device, and the backwash pump is arranged in the sludge return system Inside.

本实施例中,优选的,所述活性炭过滤器的外壳为不锈钢或者玻璃钢。In this embodiment, preferably, the shell of the activated carbon filter is stainless steel or glass fiber reinforced plastic.

本实施例中,优选的,所述MF处理单元的微滤膜为有机高分子膜。In this embodiment, preferably, the microfiltration membrane of the MF processing unit is an organic polymer membrane.

所述的MBR膜处理单元包括pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,产水池。半导体工业废水首先排入废水收集池,依次进入pH调节池,厌氧池和缺氧池和好氧池,经过活性污泥系统的前端生化处理,再进入MBR一体化装置内,其中MBR一体化装置设有活性污泥系统和生物反应器以及鼓风机、抽吸泵、污泥回流系统、反洗泵,其中MBR膜组件置于生物反应器内部。The MBR membrane treatment unit includes a pH adjustment tank, an anaerobic tank, an anoxic tank, an aerobic tank, an MBR integrated device, and a water production tank. The wastewater from the semiconductor industry is firstly discharged into the wastewater collection tank, and then enters the pH adjustment tank, the anaerobic tank, the anoxic tank and the aerobic tank in turn. After the front-end biochemical treatment of the activated sludge system, it enters the MBR integrated device. The device is provided with an activated sludge system and a bioreactor, as well as a blower, a suction pump, a sludge return system, and a backwash pump, wherein the MBR membrane module is placed inside the bioreactor.

其中MBR工艺属于一体式结构,膜组件置于生物反应器内部,进水进入膜-生物反应器,其中的大部分污染物已经被混合液中的活性污泥去除,采用鼓风机持续曝气,在负压作用下经过MBR膜过滤出水。经过抽吸泵进入MBR产水池。出水进入MBR产水池,然后经过泵进入活性炭过滤装置,利用活性炭较强的吸附性能深度处理此废水,然后出水进入微滤过滤器,最终出水主要用于厂区内冷却塔、废气洗涤塔和绿化灌溉等用水。Among them, the MBR process is an integrated structure. The membrane module is placed inside the bioreactor, and the influent water enters the membrane-bioreactor. Most of the pollutants in it have been removed by the activated sludge in the mixed solution. The blower is used for continuous aeration. Under the action of negative pressure, the water is filtered through the MBR membrane. It enters the MBR production pool through the suction pump. The effluent enters the MBR water production tank, and then enters the activated carbon filter device through the pump, and uses the strong adsorption performance of activated carbon to further treat the wastewater, and then the effluent enters the microfiltration filter. The final effluent is mainly used for cooling towers, waste gas washing towers and green irrigation in the plant Wait for water.

所述的活性炭过滤单元是以活性炭过滤器为主,是一种内装填粗石英砂垫层及优质活性炭的压力容器,外壳一般为不锈钢或者玻璃钢,活性炭过滤器用来过滤水中的游离物、微生物、部分重金属离子,并能有效降低水的色度。The activated carbon filter unit is mainly activated carbon filter, which is a pressure vessel filled with coarse quartz sand cushion and high-quality activated carbon. The shell is generally stainless steel or glass fiber reinforced plastic. Part of heavy metal ions, and can effectively reduce the color of water.

活性炭过滤器主要利用含碳量高、分子量大、比表面积大的活性炭有机絮凝体对水中杂质进行物理吸附,达到水质要求,当水流通过活性炭的孔隙时,各种悬浮颗粒、有机物等在范德华力的作用下被吸附在活性炭孔隙中;同时,吸附于活性炭表面的氯(次氯酸)在炭表面发生化学反应,被还原成氯离子,从而有效地去除了氯,确保出水余氯量小于0.1ppm。用颗粒活性炭进一步去除MBR膜反应器出水中的残存的余氯、有机物、悬浮物的杂质,为后续的MF处理提供良好条件。The activated carbon filter mainly uses activated carbon organic flocs with high carbon content, large molecular weight and large specific surface area to physically adsorb impurities in the water to meet the water quality requirements. When the water flows through the pores of the activated carbon, various suspended particles, organic matter, etc. At the same time, the chlorine (hypochlorous acid) adsorbed on the surface of the activated carbon undergoes a chemical reaction on the surface of the activated carbon and is reduced to chloride ions, thereby effectively removing the chlorine and ensuring that the residual chlorine in the effluent is less than 0.1 ppm. Granular activated carbon is used to further remove residual chlorine, organic matter, and suspended matter impurities in the effluent of the MBR membrane reactor, providing good conditions for subsequent MF treatment.

活性炭吸附原理是在其颗粒表面形成一层平衡的表面浓度,再把有机物质吸附到活性炭颗粒内,使用初期的吸附效果很高。但时间一长,活性炭的吸附能力会不同程度地减弱,吸附效果也随之下降。装填的活性炭性能差异可以达到不同的处理效果,主要去除水中的有机物、色度、余氯、部分重金属离子、洗涤剂、细菌和病毒等;其中活性炭过滤器出水的含量也要定期检测,当余氯>0.1mg/l时,说明已经吸附饱和,切不可将出水送入微滤过滤器处理装置,必须及时更换活性炭。The principle of activated carbon adsorption is to form a layer of balanced surface concentration on the surface of the particles, and then adsorb organic substances into the activated carbon particles, and the adsorption effect at the initial stage of use is very high. But over time, the adsorption capacity of activated carbon will be weakened to varying degrees, and the adsorption effect will also decrease. The difference in the performance of the activated carbon loaded can achieve different treatment effects, mainly to remove organic matter, chromaticity, residual chlorine, some heavy metal ions, detergents, bacteria and viruses in the water; among them, the content of the activated carbon filter effluent should also be regularly detected. When chlorine is greater than 0.1mg/l, it means that the adsorption has been saturated, and the effluent must not be sent to the microfiltration filter treatment device, and the activated carbon must be replaced in time.

废水经活性炭过滤后水质得到进一步的净化,再用泵抽入精密过滤器微滤处理单元,微滤操作简单,通水量大,工作压力低,制水率高;微滤又称微孔过滤,它属于精密过滤,截留溶液中的砂砾、淤泥、黏土等颗粒和贾第虫、隐孢子虫、藻类和一些细菌等,而大量溶剂、小分子及少量大分子溶质都能透过膜的分离过程。After the wastewater is filtered by activated carbon, the water quality is further purified, and then pumped into the microfiltration treatment unit of the precision filter. The microfiltration operation is simple, the water flow is large, the working pressure is low, and the water production rate is high; It belongs to precision filtration, which traps grit, silt, clay and other particles in the solution and Giardia, Cryptosporidium, algae and some bacteria, etc., while a large amount of solvent, small molecules and a small amount of macromolecular solutes can pass through the separation process of the membrane .

所述的MF处理单元是把微滤设备与一些配套设备有机结合起来,组装成一个独立的微滤系统,其中包括微滤膜、内外导流层、滤芯端盖、壳体及中心杆等又可组成滤芯。决定膜分离效果的是膜的物理结构,形状和大孔的小。根据微粒在微滤过程中的截留位置,可分为3种截留机制:筛分、吸附及架桥。废水经活性炭过滤后水质得到进一步的净化,再用泵抽入精密过滤器微滤处理单元,微滤操作简单,通水量大,工作压力低,制水率高;微滤又称微孔过滤,它属于精密过滤,截留溶液中的砂砾、淤泥、黏土等颗粒和贾第虫、隐孢子虫、藻类和一些细菌等,而大量溶剂、小分子及少量大分子溶质都能透过膜的分离过程。The MF processing unit is an organic combination of microfiltration equipment and some supporting equipment to assemble an independent microfiltration system, which includes microfiltration membrane, inner and outer diversion layers, filter element end caps, shell and center rod, etc. Can form a filter element. What determines the separation effect of the membrane is the physical structure, shape and size of the macropores of the membrane. According to the retention position of particles in the microfiltration process, it can be divided into 3 retention mechanisms: sieving, adsorption and bridging. After the wastewater is filtered by activated carbon, the water quality is further purified, and then pumped into the microfiltration treatment unit of the precision filter. The microfiltration operation is simple, the water flow is large, the working pressure is low, and the water production rate is high; It belongs to precision filtration, which traps grit, silt, clay and other particles in the solution and Giardia, Cryptosporidium, algae and some bacteria, etc., while a large amount of solvent, small molecules and a small amount of macromolecular solutes can pass through the separation process of the membrane .

经过微滤处理后的半导体工业废水主要用于厂区内冷却塔、废气洗涤塔和绿化灌溉用水。The semiconductor industry wastewater after microfiltration treatment is mainly used for cooling towers, waste gas washing towers and green irrigation water in the factory area.

其中,有机废水主要水质指标:pH为5.5-8.5,COD为500-1000mg/l,NH3-N为50-100mg/l,SS为10-100mg/l,;经组合工艺处理后出水指标pH为6.5-7.5、COD为10-30mg/l、NH3-N为0.1-1mg/l,主要污染物去除率可达到95%以上、SS去除率为100%,出水水质达到《城市污水再生利用工水质》,出水水质好且稳定。Among them, the main water quality indicators of organic wastewater: pH is 5.5-8.5, COD is 500-1000mg/l, NH3-N is 50-100mg/l, SS is 10-100mg/l,; after the combined process treatment, the effluent index pH is 6.5-7.5, COD is 10-30mg/l, NH 3 -N is 0.1-1mg/l, the removal rate of main pollutants can reach more than 95%, the removal rate of SS is 100%, and the effluent quality meets the requirements of "Urban Sewage Recycling and Utilization Engineering". Water Quality", the effluent quality is good and stable.

MBR处理单元依次包括:pH调节池、厌氧池、缺氧池、好氧池、MBR一体化装置,MBR膜组件孔径为0.01μm-0.03μm;MBR膜生物反应器是生物处理技术与膜分离技术相结合的一种新技术,取代了传统工艺中的二沉池,它可以高效地进行固液分离,得到直接使用的稳定中水。又可在生物池内维持高浓度的微生物量,工艺剩余污泥少,极有效地去除氨氮,出水悬浮物和浊度接近于零,出水中细菌和病毒被大幅度去除,能耗低,占地面积小。The MBR treatment unit sequentially includes: pH adjustment tank, anaerobic tank, anoxic tank, aerobic tank, and MBR integrated device. The pore size of the MBR membrane module is 0.01 μm-0.03 μm; the MBR membrane bioreactor is a biological treatment technology and membrane separation. A new technology combined with technology, which replaces the secondary sedimentation tank in the traditional process, it can efficiently carry out solid-liquid separation and obtain stable reclaimed water for direct use. It can also maintain a high concentration of microorganisms in the biological pool, with less residual sludge in the process, extremely effective removal of ammonia nitrogen, effluent suspended solids and turbidity close to zero, bacteria and viruses in effluent water are largely removed, low energy consumption, land occupation Small area.

MF处理单元选用微孔滤膜为过滤介质,以物理截留的方式去除水中一定大小的杂质颗粒。在压力驱动下,溶液中水、有机低分子、无机离子等尺寸小的物质可通过纤维壁上的微孔到达膜的另一侧,溶液中菌体、胶体、颗粒物、有机大分子等大尺寸物质则不能透过纤维壁而被截留,从而达到筛分溶液中不同组分的目的。该过程为常温操作,无相态变化,不产生二次污染。The MF treatment unit selects the microporous membrane as the filter medium, and removes the impurity particles of a certain size in the water by means of physical interception. Driven by pressure, small-sized substances such as water, low organic molecules, and inorganic ions in the solution can pass through the micropores on the fiber wall to reach the other side of the membrane. Substances cannot pass through the fiber wall and are retained, so as to achieve the purpose of sieving different components in the solution. The process is operated at room temperature, with no phase change and no secondary pollution.

最后应说明的是:Finally, it should be noted that:

本领域技术人员可以参考本文内容,实施该方法,实现其应用,特别需要指出的是,所有类似的替换和改动对本领域技术人员来说是显而易见的,它们都被视为包括在本发明内。本发明的方法及应用己经通过较佳的实施例进行了描述,相关人员明显能在不脱离本发明内容、精神和范围内对本文制各方法和应用进行改动或适当变更与组合,来实现和应用本发明技术。Those skilled in the art can refer to the content herein, implement the method, and realize its application. It should be particularly pointed out that all similar replacements and modifications are obvious to those skilled in the art, and they are all considered to be included in the present invention. The method and application of the present invention have been described through preferred embodiments, and it is obvious that relevant persons can make changes or appropriate changes and combinations to the methods and applications of the present invention without departing from the content, spirit and scope of the present invention. and application of the technology of the present invention.

以上实施例仅用以说明而非限制本发明的技术方案,尽管参照上述实施例对本发明进行了详细说明,本领域的普通技术人员应当理解:依然可以对本发明进行修改或者等同替换,而不脱离本发明的精神和范围,而所附权利要求意在涵盖落入本发明精神和范围中的这些修改或者等同替换。The above embodiments are only used to illustrate rather than limit the technical solutions of the present invention. Although the present invention has been described in detail with reference to the above embodiments, those of ordinary skill in the art should understand that the present invention can still be modified or equivalently replaced without departing from the The spirit and scope of the invention and the appended claims are intended to cover such modifications or equivalents as fall within the spirit and scope of the invention.

Claims (7)

1. The utility model provides a be used for semiconductor industrial waste water integration processing system which characterized in that:
the device comprises a wastewater collection tank, an MBR membrane treatment unit, an active carbon filtration unit and an MF treatment unit, wherein the wastewater collection tank is sequentially connected with the MBR membrane treatment unit, the active carbon filtration unit and the MF treatment unit through pipelines, and a water storage tank;
the MBR membrane treatment unit comprises a pH adjusting tank, an anaerobic tank, an anoxic tank, an aerobic tank, an MBR integrated device and an MBR water production tank, wherein the pH adjusting tank, the anaerobic tank, the anoxic tank, the aerobic tank and the MBR integrated device are sequentially connected through a pipeline;
the active carbon filtering unit comprises an active carbon filter, the active carbon filter is a pressure container filled with a coarse quartz sand cushion layer and active carbon,
the MF treatment unit comprises a filter element, wherein the filter element comprises a microfiltration membrane, an inner flow guide layer, an outer flow guide layer, a filter element end cover, a shell and a center rod.
2. The integrated semiconductor industrial wastewater treatment system according to claim 1, wherein: the MBR integrated device comprises an activated sludge system, wherein the activated sludge system is arranged in front of an MBR membrane module, and the wastewater enters the activated sludge system through a pipeline through an aerobic tank.
3. The integrated semiconductor industrial wastewater treatment system according to claim 2, wherein: and a suction pump is arranged between the MBR water storage tank and the MBR water production tank.
4. The integrated semiconductor industrial wastewater treatment system according to claim 3, wherein: the aperture of the MBR membrane module is 0.01-0.03 μm.
5. The integrated semiconductor industrial wastewater treatment system according to claim 4, wherein: the MBR membrane treatment unit further comprises a sludge backflow system and a backwashing pump, the sludge backflow system is arranged in the MBR integrated device, and the backwashing pump is arranged in the sludge backflow system.
6. The integrated semiconductor industrial wastewater treatment system according to claim 1, wherein: the shell of the activated carbon filter is made of stainless steel or glass fiber reinforced plastic.
7. The integrated semiconductor industrial wastewater treatment system according to claim 1, wherein: and the microfiltration membrane of the MF treatment unit is an organic polymer membrane.
CN201910480304.5A 2019-06-04 2019-06-04 Integrated treatment system for semiconductor industrial wastewater Pending CN112028378A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103796957A (en) * 2011-10-13 2014-05-14 栗田工业株式会社 Organic sewage collection processing device and collection processing method
CN210313900U (en) * 2019-06-04 2020-04-14 伟泰科技(无锡)有限公司 Integrated treatment system for semiconductor industrial wastewater

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103796957A (en) * 2011-10-13 2014-05-14 栗田工业株式会社 Organic sewage collection processing device and collection processing method
CN210313900U (en) * 2019-06-04 2020-04-14 伟泰科技(无锡)有限公司 Integrated treatment system for semiconductor industrial wastewater

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
王浩;王学华;王国梁;高超;秦毅;: "反硝化-水解酸化-厌氧-缺氧-MBR工艺处理氮磷废水", 水处理技术, vol. 40, no. 01, 25 January 2014 (2014-01-25), pages 132 - 134 *
肖燕;陈彤;胡永健;韩永萍;林亚凯;王晓琳;: "面向半导体废水回用处理的MBR-RO组合工艺可行性", 水处理技术, vol. 39, no. 02, 10 February 2013 (2013-02-10), pages 102 - 106 *

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