[go: up one dir, main page]

CN104261628A - Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process - Google Patents

Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process Download PDF

Info

Publication number
CN104261628A
CN104261628A CN201410527709.7A CN201410527709A CN104261628A CN 104261628 A CN104261628 A CN 104261628A CN 201410527709 A CN201410527709 A CN 201410527709A CN 104261628 A CN104261628 A CN 104261628A
Authority
CN
China
Prior art keywords
aerobic
membrane
film
electricity
organic wastewater
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.)
Pending
Application number
CN201410527709.7A
Other languages
Chinese (zh)
Inventor
曹占平
张景丽
王晶
张明慧
李松松
武静明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tiangong University
Original Assignee
Tianjin Polytechnic University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tianjin Polytechnic University filed Critical Tianjin Polytechnic University
Priority to CN201410527709.7A priority Critical patent/CN104261628A/en
Publication of CN104261628A publication Critical patent/CN104261628A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • 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
    • C02F3/005Combined electrochemical biological processes
    • 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
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1278Provisions for mixing or aeration of the mixed liquor
    • 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
    • C02F3/28Anaerobic digestion processes
    • C02F3/2853Anaerobic digestion processes using anaerobic membrane bioreactors

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

该本发明涉及一种膜电生物耦合工艺处理难降解有机废水的方法,本发明的特征在于:膜电生物耦合工艺分为厌氧和好氧两个区,阴极板放置在厌氧区中,过滤膜和阳极板都放置在好氧区中,膜的平均孔径在0.1~0.4μm之间,膜过滤采用负压抽吸出水。本发明采用电辅助强化微生物还原和氧化降解难生物降解废水并耦合膜过滤技术而开发的,实现了厌氧微生物和好氧微生物的完全分离,并采用膜过滤出水,简化工艺流程。该方法可使难降解有机废水的CODCr去除在90%以上,色度去除在95%以上,电生物的强化降解使污水处理效果好,膜污染得到了较好的控制。膜出水提高了固液分离的效率,出水水质稳定。The present invention relates to a method for treating refractory organic wastewater by a membrane electrobiological coupling process. The feature of the present invention is that the membrane electrobiological coupling process is divided into anaerobic and aerobic areas, and the cathode plate is placed in the anaerobic area. Both the filter membrane and the anode plate are placed in the aerobic zone, the average pore size of the membrane is between 0.1 and 0.4 μm, and the membrane filter adopts negative pressure suction to discharge water. The invention is developed by using electric-assisted enhanced microbial reduction and oxidative degradation of refractory biodegradable wastewater and coupled with membrane filtration technology, which realizes the complete separation of anaerobic microorganisms and aerobic microorganisms, and uses membranes to filter water, simplifying the process flow. The method can remove more than 90% of COD Cr and more than 95% of chroma in refractory organic wastewater. The enhanced degradation of electrobiology makes the sewage treatment effect better, and the membrane fouling is well controlled. Membrane effluent improves the efficiency of solid-liquid separation, and the effluent quality is stable.

Description

一种膜电生物耦合工艺处理难降解有机废水的方法A method for the treatment of refractory organic wastewater by a membrane electrobiological coupling process

技术领域technical field

本发明涉及一种膜电生物耦合工艺处理难生物降解有机废水的方法,该方法主要是采用电辅助微生物(电生物)强化难降解有机废水还原和氧化降解过程并耦合膜过滤技术而开发的,属于环境保护领域,The invention relates to a method for treating refractory organic wastewater by a membrane-electrobiological coupling process. The method is mainly developed by using electric-assisted microorganisms (electrobiology) to strengthen the reduction and oxidative degradation process of refractory organic wastewater and coupling membrane filtration technology. In the field of environmental protection,

背景技术Background technique

随着社会工业的发展,水环境中难降解有机物的处理是环境治理中的难点,针对含难降解有机物的工业废水日渐多样化且生化处理难度加大的趋势,特别是医药废水、印染废水、化工及燃料废水等,废水成分复杂、色度大、生物毒性大。常规的生物处理效果差,出水悬浮物含量高。电辅助作为一种强化微生物处理的手段,特别是电辅助阴极提供微生物还原降解所需的电子供体,可极大地提高生物的还原降解效率。此外,电辅助作为一种生物刺激因素,使生物体产生一系列的电场生化效应,也进一步提高了微生物的降解效率。电生物体系的核心是形成电辅助与微生物新陈代谢的多相耦合过程,以提高难生物降解有机废水的处理效率。With the development of social industry, the treatment of refractory organic matter in the water environment is a difficult point in environmental governance. In view of the increasing diversification of industrial wastewater containing refractory organic matter and the increasing difficulty of biochemical treatment, especially medical wastewater, printing and dyeing wastewater, Chemical and fuel wastewater, etc. The wastewater has complex components, large chroma, and high biological toxicity. The effect of conventional biological treatment is poor, and the content of suspended solids in the effluent is high. As a means to strengthen the treatment of microorganisms, electrical assistance, especially the electro-assisted cathode to provide electron donors required for microbial reductive degradation, can greatly improve the reductive degradation efficiency of organisms. In addition, electrical assistance, as a biostimulant, causes organisms to produce a series of electric field biochemical effects, which further improves the degradation efficiency of microorganisms. The core of the electrobiological system is to form a multiphase coupling process of electrical assistance and microbial metabolism to improve the treatment efficiency of refractory biodegradable organic wastewater.

膜过滤是一种高效分离的过程,广泛应用于水处理领域,如MBR污水处理工艺、污水回用的CMF工艺等。难降解有机废水因其水质特性影响污泥微生物的泥水分离,造成生物处理后的出水悬浮物含量高,即影响出水水质又影响生物降解系统的污泥微生物的富集。因此将电生物和膜过滤进行耦合,组成膜电生物耦合工艺处理难降解有机废水具有广泛的应用前景。Membrane filtration is a high-efficiency separation process widely used in the field of water treatment, such as MBR sewage treatment process, CMF process for sewage reuse, etc. Refractory organic wastewater affects the sludge-water separation of sludge microorganisms due to its water quality characteristics, resulting in a high content of suspended solids in the effluent after biological treatment, which affects both effluent water quality and the enrichment of sludge microorganisms in the biodegradation system. Therefore, the coupling of electrobiology and membrane filtration to form a membrane electrobiology coupling process for the treatment of refractory organic wastewater has broad application prospects.

发明内容Contents of the invention

本发明的目的在于将电生物和膜过滤结合起来,提高膜电生物工艺在难降解有机污染物方面协同强化降解效率。提供一种在电催化下利用微生物高效、稳定降解难降解有机废水,并通过膜过滤出水的新方法。The purpose of the invention is to combine electrobiology and membrane filtration to improve synergistically enhanced degradation efficiency of membrane electrobiology process in respect of refractory organic pollutants. A new method for efficiently and stably degrading refractory organic wastewater by using microorganisms under electrocatalysis and filtering the water through membranes is provided.

本发明的特征在于:电生物体系分为厌氧和好氧两个区域,阴极板放置在厌氧区中,阴极板采用具有储电子和缓慢释电子功能的钯极板、镀钯极板或石墨极板,该区仅进行搅拌,不曝气;阳极板放在好氧区,过滤膜也放在好氧区,在该区曝气供氧并吹扫膜面。耦合工艺的厌氧区处于厌氧的状态,在电辅助供电子的情况下,厌氧微生物利用电辅助提供的电子还原降解有机污染物,而后废水溢流进入好氧区,在好氧区进行生物好氧处理和阳极氧化处理后,经负压抽吸膜过滤出水。过滤膜的外径在5.0~15mm之间,内径在2~12mm之间,膜的平均孔径在0.1~0.4μm之间。电生物体系可充分发挥微生物和电辅助的强化作用,且微生物可在厌氧和好氧条件下保持各自的最佳降解环境。电辅助电极的电压为0.2~3V,总水力停留时间在20~50h,耦合工艺的厌氧与好氧区的水力停留时间比为1∶1~5∶1。厌氧区域的搅拌强度为2~8w/m3,好氧区域曝气的气水比为5~10∶1。The present invention is characterized in that: the electrobiological system is divided into anaerobic and aerobic areas, the cathode plate is placed in the anaerobic area, and the cathode plate adopts a palladium plate, a palladium plated plate or a The graphite plate is only stirred without aeration; the anode plate is placed in the aerobic area, and the filter membrane is also placed in the aerobic area, where aeration is used to supply oxygen and purge the membrane surface. The anaerobic zone of the coupling process is in an anaerobic state. In the case of electric assist electron supply, anaerobic microorganisms use the electrons provided by electric assist to reduce and degrade organic pollutants, and then the wastewater overflows into the aerobic zone, where the After biological aerobic treatment and anodic oxidation treatment, the water is filtered through negative pressure suction membrane. The outer diameter of the filter membrane is between 5.0-15 mm, the inner diameter is between 2-12 mm, and the average pore diameter of the membrane is between 0.1-0.4 μm. The electrobiological system can give full play to the strengthening effect of microorganisms and electric assistance, and microorganisms can maintain their respective optimal degradation environments under anaerobic and aerobic conditions. The voltage of the electric auxiliary electrode is 0.2-3V, the total hydraulic retention time is 20-50h, and the hydraulic retention time ratio of the anaerobic and aerobic zones of the coupling process is 1:1-5:1. The stirring intensity in the anaerobic zone is 2-8w/m 3 , and the gas-water ratio of aeration in the aerobic zone is 5-10:1.

本发明的优点在于:充分发挥了电生物和膜过滤耦合的优点,简化了工艺流程。该方法可使难降解有机废水的CODCr去除在90%以上,色度去除在95%以上,电生物提高了污水处理效果,膜污染得到了较好的控制。膜出水提高了固液分离的效率,出水水质稳定。The invention has the advantages of fully exerting the coupling advantages of electrobiology and membrane filtration, and simplifying the technological process. The method can remove more than 90% of COD Cr and more than 95% of chroma in refractory organic wastewater, the electrobiology improves the sewage treatment effect, and the membrane fouling is well controlled. Membrane effluent improves the efficiency of solid-liquid separation, and the effluent quality is stable.

附图说明Description of drawings

图1:膜电生物耦合工艺处理难降解有机废水的流程示意图Figure 1: Schematic diagram of the membrane electrobiological coupling process for the treatment of refractory organic wastewater

1.进水 2.搅拌器 3.阴极板 4.厌氧区 5.厌氧混合液溢流 6.厌氧沉淀区 7.厌氧出水1. Water inlet 2. Stirrer 3. Cathode plate 4. Anaerobic zone 5. Anaerobic mixture overflow 6. Anaerobic sedimentation zone 7. Anaerobic effluent

8.阳极板 9.膜抽吸出水 10.阳极区 11.真空泵 12.曝气系统 13.直流电源8. Anode plate 9. Membrane suction water 10. Anode area 11. Vacuum pump 12. Aeration system 13. DC power supply

具体实施方式Detailed ways

实施例1:Example 1:

采用膜电生物耦合工艺处理焦化化工有机废水,处理水量15m3/h。该有机废水含有苯酚、氰、氯酚、煤焦油等有机物,CODCr含量在1500~3000mg/L之间。焦化化工有机废水在反应器中停留时间为20h,厌氧区域和好氧区域水力停留时间均为10h,厌氧区域的微生物浓度在3000~5000mg/L之间,好氧区域的微生物浓度在2000~4000mg/L之间。厌氧区域搅拌功率为150W,好氧区的曝气的气水比为8∶1,阴极板采用钛基镀钯的网状平板极板,阳极采用石墨极板,直流电源所施加的电压为1.2V。Coking chemical organic wastewater is treated by membrane electrobiological coupling process, and the treated water volume is 15m 3 /h. The organic waste water contains phenol, cyanide, chlorophenol, coal tar and other organic matter, and the COD Cr content is between 1500 and 3000 mg/L. The residence time of coking chemical organic wastewater in the reactor is 20h, the hydraulic retention time in the anaerobic zone and the aerobic zone are both 10h, the microbial concentration in the anaerobic zone is between 3000-5000mg/L, and the microbial concentration in the aerobic zone is 2000 ~4000mg/L. The stirring power in the anaerobic zone is 150W, the gas-water ratio of aeration in the aerobic zone is 8:1, the cathode plate is made of titanium-based palladium-plated mesh flat plate, the anode is made of graphite plate, and the voltage applied by the DC power supply is 1.2V.

经调试稳定运行后,膜出水水质如下:酚<0.5mg/L,氰<0.2mg/L,COD<90mg/L,在调试及近一年的运行中膜通量几乎没有衰减,污水处理效果好,膜污染得到了较好的控制。该发明为难降解有机废水的高效降解提供了新的方法和思路。After commissioning and stable operation, the water quality of membrane effluent is as follows: phenol < 0.5mg/L, cyanide < 0.2mg/L, COD < 90mg/L. During commissioning and nearly one year of operation, the membrane flux has almost no attenuation, and the sewage treatment effect Well, membrane fouling is well under control. The invention provides a new method and idea for the efficient degradation of refractory organic wastewater.

实施例2:Example 2:

印染废水处理站的污水含分散蓝离子型染料,色度为300~500倍,CODCr为300~500mg/L,SS为130mg/L,处理水量为200m3/d,BOD/COD为0.25,生化性较差。原处理工艺采用混凝沉淀-微生物厌氧降解-微生物好氧降解的流程,出水CODCr的浓度在100~150mg/L,出水色度高,不满足环保排放要求。为提高去除效果采用该发明的电生物膜过滤耦合工艺进行改造,在厌氧反应器中安装圆桶型网状钛基镀钯阴极板,在好氧池中安装网状钢极板作为阳极,稳流直流电压提供1.5V的电压。极板安装完成后,经过一个月的运行调试,开始进行正常运行,在处理废水流量、水质不变,水力停留时间也不变的情况下进行了水质检测,检测出水水质为:出水CODCr浓度在30~50mg/L,去除率在92%以上,色度在10~15倍。改造后,废水的处理效率较原工艺提高了近30%,而处理运行费用仅增加5%,膜污染得到了较好的控制,膜通量基本保持稳定。满足了环保的需要和改造要求,且运行稳定。The sewage from the printing and dyeing wastewater treatment station contains disperse blue ionic dyes, the chroma is 300-500 times, the COD Cr is 300-500mg/L, the SS is 130mg/L, the treated water volume is 200m 3 /d, and the BOD/COD is 0.25. Biochemically poor. The original treatment process adopts the process of coagulation sedimentation-microbial anaerobic degradation-microbial aerobic degradation. The concentration of COD Cr in the effluent is 100-150mg/L, and the chroma of the effluent is high, which does not meet the environmental protection discharge requirements. In order to improve the removal effect, the electric biofilm filtration coupling process of the invention is used for transformation. A drum-shaped mesh titanium-based palladium-plated cathode plate is installed in the anaerobic reactor, and a mesh steel plate is installed as an anode in the aerobic tank. The regulated DC voltage provides a voltage of 1.5V. After the installation of the pole plate was completed, after a month of operation and commissioning, the normal operation began. The water quality test was carried out under the condition that the treated wastewater flow rate, water quality and hydraulic retention time were not changed. The detected water quality was: effluent COD Cr concentration At 30-50 mg/L, the removal rate is above 92%, and the chroma is 10-15 times. After the transformation, the wastewater treatment efficiency increased by nearly 30% compared with the original process, while the treatment operation cost only increased by 5%, the membrane fouling was well controlled, and the membrane flux remained basically stable. It meets the needs of environmental protection and transformation requirements, and runs stably.

从实施例1和实施例2得出:采用本发明的一种膜电生物耦合工艺处理难降解有机废水的方法,对难生物降解废水的处理效果稳定,在处理效果上较传统的微生物方法有较大的提升,同时处理效率的提高也使膜污染得到了较好的控制,该发明可对现有的生物处理工艺进行提升改造以提高处理效率。Draw from embodiment 1 and embodiment 2: adopt a kind of method of membrane electrobiological coupling process of the present invention to process refractory organic waste water, the processing effect to refractory biodegradable waste water is stable, compares traditional microbial method on processing effect. Larger improvement, and the improvement of treatment efficiency also makes membrane fouling better controlled. This invention can upgrade and transform the existing biological treatment process to improve treatment efficiency.

本发明提出的一种膜电生物耦合工艺处理难降解有机废水的方法,已通过实施例进行了描述,相关技术人员明显能在不脱离本发明的内容、精神和范围内对本文所述的内容进行改动或适当变更与组合,来实现本发明。特别需要指出的是,所有相类似的替换和改动对本领域技术人员来说是显而易见的,他们都被视为包括在本发明的精神、范围和内容中。A method for treating refractory organic wastewater by a membrane electrobiological coupling process proposed by the present invention has been described through the examples, and those skilled in the art can clearly understand the content described herein without departing from the content, spirit and scope of the present invention Changes or appropriate changes and combinations are made to realize the present invention. In particular, it should be pointed out that all similar substitutions and modifications would be obvious to those skilled in the art, and they are all considered to be included in the spirit, scope and content of the present invention.

Claims (5)

1. the method for a film electricity biological coupling art breading organic wastewater with difficult degradation thereby, it is characterized in that: film electricity biological coupling technique is divided into anaerobic and aerobic two regions, negative plate is placed in anaerobic zone, negative plate adopts palladium pole plate, plating palladium pole plate or the graphite electrode plate with the gentle slow release electric function of accumulate, this region is only stirred, not aeration, and filtering membrane and positive plate are all placed in aerobic region, film adopts negative pressure-pumping water outlet, and this aerobic zone is carried out aeration oxygen supply and purged film surface; The power acquisition D.C. regulated power supply that electricity is auxiliary, the anaerobic zone of film electricity biological coupling technique is in the state of anaerobism, anaerobion utilizes the electron reduction degradable organic pollutant of electric assisted Extraction confession, then waste water outflow enters aerobic zone, after biology aerobic process and anodic oxidation treatment are carried out in aerobic zone, through negative pressure-pumping film filtration effluent; The enhancing degradation of electricity biology makes good sewage processing effect, and fouling membrane obtains good control; Film water outlet improves the efficiency of solid-liquid separation, stable effluent quality; The external diameter of filtering membrane is between 5.0 ~ 15mm, and internal diameter is between 2 ~ 12mm, and the mean pore size of film is between 0.1 ~ 0.4 μm; Electricity living things system can give full play to the auxiliary strengthening effect of microorganism and electricity, and microorganism can keep respective the best degraded environment under anaerobism or aerobic condition; The voltage of electricity supporting electrode is 0.2 ~ 3V, and total hrt is at 20 ~ 50h, and the anaerobism of reactor is 1: 1 ~ 5: 1 with the hydraulic detention time ratio in aerobic region; The stirring intensity of anaerobic zone is 2 ~ 8w/m 3, the gas-water ratio of aerobic region aeration is 5 ~ 10: 1.
2. the method for a kind of film electricity biological coupling art breading organic wastewater with difficult degradation thereby as described in claim 1, is characterized in that in the anaerobism that the positive plate that electricity is auxiliary and negative plate are separately positioned on film electricity biological coupling technique and aerobic two different zones; Reactor total hrt is at 10 ~ 20h, and the anaerobism of reactor is 1: 1 ~ 5: 1 with the hydraulic detention time ratio in aerobic region; The stirring intensity of anaerobic zone is at 2 ~ 8w/m 3, the gas-water ratio of the aeration in aerobic region is 5 ~ 10: 1.
3. the method for a kind of film electricity biological coupling art breading organic wastewater with difficult degradation thereby as described in claim 1, it is characterized in that first organic wastewater with difficult degradation thereby enters film electricity biological coupling technique anaerobic zone after micro-reduction degraded, enter aerobic region again to degrade, finally by negative pressure-pumping film filtration effluent.
4. the method for a kind of film electricity biological coupling art breading organic wastewater with difficult degradation thereby as described in claim 1, it is characterized in that anaerobion is separated completely with aerobic microbiological, negative plate is placed on anaerobic zone, and positive plate and filtering membrane are all placed on aerobic zone, and aerobic zone aeration oxygen supply also purges film surface.
5. the method for a kind of film electricity biological coupling art breading organic wastewater with difficult degradation thereby as described in claim 1, is characterized in that the voltage between anode and cathode is: 0.2 ~ 3V.
CN201410527709.7A 2014-10-09 2014-10-09 Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process Pending CN104261628A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410527709.7A CN104261628A (en) 2014-10-09 2014-10-09 Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410527709.7A CN104261628A (en) 2014-10-09 2014-10-09 Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process

Publications (1)

Publication Number Publication Date
CN104261628A true CN104261628A (en) 2015-01-07

Family

ID=52153255

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410527709.7A Pending CN104261628A (en) 2014-10-09 2014-10-09 Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process

Country Status (1)

Country Link
CN (1) CN104261628A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104773909A (en) * 2015-03-31 2015-07-15 浙江大学 Device and process for treating printing and dyeing wastewater by combining microbial electrolysis cell and anaerobic/aerobiotic technology
CN104909514A (en) * 2015-03-09 2015-09-16 浙江大学 Integrated system for solar-driven microbial electrolysis cell strengthening treatment on rural domestic sewage
WO2017193090A1 (en) * 2016-05-06 2017-11-09 D.C Water & Sewer Authority Overcoming biofilm diffusion in water treatment
CN111977899A (en) * 2020-08-14 2020-11-24 武汉轻工大学 Treatment system and method for high-concentration refractory biodegradable organic wastewater
CN112010420A (en) * 2020-08-11 2020-12-01 盐城工学院 Electrochemical biological accelerated treatment reaction device for azo dye wastewater
CN114685012A (en) * 2022-04-27 2022-07-01 广东硕光环保科技有限公司 Fishery wastewater treatment method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104909514A (en) * 2015-03-09 2015-09-16 浙江大学 Integrated system for solar-driven microbial electrolysis cell strengthening treatment on rural domestic sewage
CN104773909A (en) * 2015-03-31 2015-07-15 浙江大学 Device and process for treating printing and dyeing wastewater by combining microbial electrolysis cell and anaerobic/aerobiotic technology
CN104773909B (en) * 2015-03-31 2016-08-24 浙江大学 Microorganism electrolysis cell is combined device and the technique processing dyeing waste water with aerobic/anaerobic
WO2017193090A1 (en) * 2016-05-06 2017-11-09 D.C Water & Sewer Authority Overcoming biofilm diffusion in water treatment
AU2017261363B2 (en) * 2016-05-06 2023-04-06 D.C Water & Sewer Authority Overcoming biofilm diffusion in water treatment
CN112010420A (en) * 2020-08-11 2020-12-01 盐城工学院 Electrochemical biological accelerated treatment reaction device for azo dye wastewater
CN111977899A (en) * 2020-08-14 2020-11-24 武汉轻工大学 Treatment system and method for high-concentration refractory biodegradable organic wastewater
CN111977899B (en) * 2020-08-14 2022-08-05 武汉轻工大学 Treatment system and method for high-concentration nonbiodegradable organic wastewater
CN114685012A (en) * 2022-04-27 2022-07-01 广东硕光环保科技有限公司 Fishery wastewater treatment method

Similar Documents

Publication Publication Date Title
CN102139979B (en) A method for treating coking wastewater by electro-Fenton-coagulation combined process
CN102583884B (en) Method for treating mixed industrial sewage in industrial park
CN104261628A (en) Method for treating degradation-resistant organic wastewater by membrane potential biological coupling process
CN103359876A (en) Harmless dimethylacetamide wastewater treatment method
CN106277555B (en) High-efficiency low-cost treatment method and system for coking wastewater
CN103395937A (en) Processing device and processing method applicable to high-ammonia-nitrogen agricultural wastewater
CN103880253B (en) A method for advanced treatment of landfill leachate and a Fenton reaction tower
CN107814458A (en) A kind of processing method of domestic waste penetrating fluid
CN102976568B (en) Fenton oxidation-aerobic granular sludge integrated device using magnetic field and processing method of device
CN104787977A (en) Continuous flow integrated electrode bio-membrane reactor and nitrate removal technology
CN208471815U (en) A kind of high-concentration sewage treatment system of AO technique and Fenton system support
CN110894125A (en) Sewage treatment process for recycling N-methyl pyrrolidone
CN201932982U (en) Combined system using micro-electrolysis-MBR (membrane bio-reactor) combined technology to treat printing and dyeing wastewater
CN201713415U (en) Dye wastewater treatment device
CN103936230B (en) The sewage water treatment method that a kind of activated sludge process and biological contact oxidation process combine
CN110642478A (en) Coupled treatment system and method for coking phenol-cyanogen wastewater by biochemical method and physicochemical method
CN113860637A (en) Method and system for treating leachate of refuse transfer station in southern region
CN102491516A (en) Method for treating wastewater difficult to be biodegraded by electric microorganism and membrane filtration coupled technology
CN102249484B (en) Shunting type dual-system sludge decrement film bioreactor and using method thereof
CN206705926U (en) A kind of efficient chemical sewage disposal device
CN115321743A (en) Method for treating garbage leachate of transfer station
CN202610073U (en) Processing apparatus of garbage percolating liquid
CN202063797U (en) High-concentration printing and dyeing wastewater treatment system
CN202400932U (en) Oil-containing wastewater treatment device
CN104229995A (en) Method for degrading degradation-resistant organic wastewater by double sludge tower-type electrical bioreactor

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20150107

WD01 Invention patent application deemed withdrawn after publication