CN103848539A - Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell - Google Patents
Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell Download PDFInfo
- Publication number
- CN103848539A CN103848539A CN201310732550.8A CN201310732550A CN103848539A CN 103848539 A CN103848539 A CN 103848539A CN 201310732550 A CN201310732550 A CN 201310732550A CN 103848539 A CN103848539 A CN 103848539A
- Authority
- CN
- China
- Prior art keywords
- mfc
- mbr
- fuel cell
- water
- wastewater treatment
- 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
Links
Images
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本发明提供一种耦合微生物燃料电池低能耗膜生物反应器的有机废水处理装置,属于有机废水资源化技术领域。本发明目的是要解决微生物燃料电池(MFC)出水水质差、膜生物反应器(MBR)能耗高且膜污染严重的问题,本发明装置由池体、MFC阳极、导流板构成阳极室,为厌氧反应区,由导流板、MBR膜组件(兼MFC阴极)、曝气管构成阴极室,为好氧反应区,导流板区则为缺氧反应区;同时采用折流板替代普通MFC中的质子交换膜,系统脱氮效果好,构建成本低,与传统MBR系统相比,本发明装置吨废水处理能耗降低30%~70%,出水水质符合我国城镇污水处理厂污染物排放标准(GB18918—2002)中的一级A标准。
The invention provides an organic wastewater treatment device coupled with a low-energy consumption membrane bioreactor of a microbial fuel cell, and belongs to the technical field of organic wastewater recycling. The purpose of the present invention is to solve the problems of poor water quality of microbial fuel cell (MFC), high energy consumption of membrane bioreactor (MBR) and serious membrane pollution. It is an anaerobic reaction zone, and the cathode chamber is composed of deflectors, MBR membrane modules (and MFC cathodes), and aeration tubes. It is an aerobic reaction zone, and the deflector zone is an anoxic reaction zone; The proton exchange membrane in ordinary MFC has good denitrification effect and low construction cost. Compared with the traditional MBR system, the energy consumption per ton of wastewater treatment of the device of the present invention is reduced by 30% to 70%, and the effluent quality meets the pollutants of urban sewage treatment plants in China. Class A standard in the emission standard (GB18918-2002).
Description
技术领域technical field
一种耦合微生物燃料电池低能耗膜生物反应器的有机废水处理装置,属于有机废水处理技术领域。The invention relates to an organic wastewater treatment device coupled with a low-energy consumption membrane bioreactor of a microbial fuel cell, belonging to the technical field of organic wastewater treatment.
背景技术Background technique
近年来,作为废水物理与生物处理技术的优势组合,以剩余污泥产量低和高效脱氮见长、以污水资源化(或回用)和无害化为最终目标的膜生物反应器(Membrane Bioreactor,MBR)技术已在污水处理领域得到广泛的应用。据统计,我国投入运行或在建的MBR污水处理工程已超过300项,其中,万吨级MBR系统近10套。然而,国内外实践表明,运行成本和膜污染始终是制约MBR稳定运行的主要障碍。就其运行成本而言,传统市政污水处理厂平均电耗为0.3kWh/m3污水,但MBR处理污水的能耗高达0.5~1.0kWh/m3污水。另一方面,无论采用何种膜污染预防措施,一旦膜与污泥混合液接触,膜污染即开始。因此,寻找低能耗、能有效解决MBR膜污染问题的污水处理方法十分必要。In recent years, as an advantageous combination of wastewater physical and biological treatment technologies, the Membrane Bioreactor (Membrane Bioreactor) is known for its low yield of excess sludge and high-efficiency denitrification, and its ultimate goal is to turn sewage into a resource (or reuse) and make it harmless. , MBR) technology has been widely used in the field of sewage treatment. According to statistics, there are more than 300 MBR sewage treatment projects put into operation or under construction in my country, among which nearly 10 sets of MBR systems of 10,000-ton level. However, domestic and foreign practices have shown that operating costs and membrane fouling are always the main obstacles restricting the stable operation of MBR. In terms of its operating cost, the average power consumption of traditional municipal sewage treatment plants is 0.3kWh/ m3 sewage, but the energy consumption of MBR sewage treatment is as high as 0.5-1.0kWh/ m3 sewage. On the other hand, no matter what kind of membrane fouling prevention measures are adopted, once the membrane comes into contact with the sludge mixture, membrane fouling begins. Therefore, it is necessary to find a sewage treatment method that has low energy consumption and can effectively solve the problem of MBR membrane fouling.
微生物燃料电池(Microbial Fuel Cell,MFC)是一项通过阳极产电生物膜降解污水中有机物并产生可持续电能的新技术。像所有燃料电池一样,MFC发电不是将燃料(废水或废弃物中的有机物)燃烧,而是在厌氧条件下从燃料分子剥取电子(即微生物呼吸作用产生的电子),并将其通过预定途径(电极和外电路)传递到氧,将原本用于氧化磷酸化生物合成ATP的能量转化为电,其中微生物是生化反应的催化剂,MFC的产电过程通过阳极有机物(电子供体)的氧化和阴极氧气(电子受体)的还原实现。然而,作为厌氧生物处理技术之一,MFC难以获得优良的出水水质,若与硝化过程、序批式反应器、生物转盘、生物接触氧化等工艺结合、或将MFC置于活性污泥法的曝气池中,可改善MFC出水水质,但上述过程均无法有效去除系统出水中的悬浮物,出水难以回用或排放。Microbial Fuel Cell (MFC) is a new technology that degrades organic matter in sewage and generates sustainable electricity through anode-generated biofilm. Like all fuel cells, MFC power generation does not burn fuel (organic matter in wastewater or waste), but strips electrons (that is, electrons produced by microbial respiration) from fuel molecules under anaerobic conditions and passes them through predetermined The pathway (electrode and external circuit) is transferred to oxygen, which converts the energy originally used for oxidative phosphorylation biosynthesis of ATP into electricity, where microorganisms are catalysts for biochemical reactions, and the electricity production process of MFC is through the oxidation of organic matter (electron donor) at the anode and the reduction of cathode oxygen (electron acceptor) is achieved. However, as one of the anaerobic biological treatment technologies, MFC is difficult to obtain excellent effluent quality. If it is combined with nitrification process, sequencing batch reactor, biological turntable, biological contact oxidation, etc. In the aeration tank, the water quality of the MFC effluent can be improved, but the above-mentioned processes cannot effectively remove the suspended solids in the effluent of the system, and the effluent is difficult to reuse or discharge.
本发明以生活污水或有机工业废水为处理对象,将MFC与MBR有机地结合在一起,构成一种新的有机废水处理装置,该装置利用MFC产生的电能补偿MBR电能消耗,并使作为MFC阴极的MBR膜表面带负电,产生静电斥力,有效降低膜污染,降低运行成本,同时MBR保证了本装置具有良好的出水水质。The present invention takes domestic sewage or organic industrial wastewater as the processing object, and organically combines MFC and MBR to form a new organic wastewater treatment device. The surface of the MBR membrane is negatively charged to generate electrostatic repulsion, which effectively reduces membrane pollution and reduces operating costs. At the same time, MBR ensures that the device has good effluent water quality.
发明内容Contents of the invention
本发明的目的在于提供一种能耗低、出水水质优良的生活污水或有机工业废水的处理装置。The object of the present invention is to provide a treatment device for domestic sewage or organic industrial wastewater with low energy consumption and excellent effluent quality.
本发明的装置由以下部件构成:Device of the present invention is made of following parts:
池体(1)、MFC阳极(2)、进水管(3)、给水泵(4)、密封塞(16)、折流板(8)、MBR膜组件(9)、曝气管(10)、电极/水管固定塞(13)、出水管(11)、出水泵(12)、负载(14)、导线(15)、阀门(5)、污泥泵(6)、污泥管(7)组成;由3~7块折流板(8)形成折流板区,将整个废水处理装置分成MFC阳极室和MBR;进水管(3)经给水泵(4)与位于MFC阳极室底部的进水口相连;出水管(11)经出水泵(12)与导电聚合物膜组件(9)的出水口连通;MFC阳极(2)和导电聚合物膜组件(9)由导线(15)与负载(14)相连;污泥泵(6)、阀门(5)经污泥管(7)与阳极室、折流板区和MBR反应室底部连通,构成污泥回流和排出系统。Pool body (1), MFC anode (2), water inlet pipe (3), feed water pump (4), sealing plug (16), baffle plate (8), MBR membrane module (9), aeration pipe (10) , electrode/water pipe fixing plug (13), outlet pipe (11), outlet pump (12), load (14), wire (15), valve (5), sludge pump (6), sludge pipe (7) It consists of 3 to 7 baffles (8) forming a baffle area, which divides the entire wastewater treatment device into an MFC anode chamber and an MBR; the water inlet pipe (3) connects to the inlet at the bottom of the MFC anode chamber through a feed pump (4) The water outlet is connected; the water outlet pipe (11) is communicated with the water outlet of the conductive polymer membrane module (9) through the water outlet pump (12); the MFC anode (2) and the conductive polymer membrane module (9) are connected by the wire (15) and the load ( 14) are connected; the sludge pump (6), valve (5) communicates with the anode chamber, the baffle area and the bottom of the MBR reaction chamber through the sludge pipe (7), forming a sludge return and discharge system.
MFC阳极(2)材料为碳毡、碳布、石墨及其改性修饰材料,MBR的膜组件(9)兼做MFC阴极,材料为导电聚合物修饰的不锈钢网、无纺布、碳毡、碳布。The MFC anode (2) is made of carbon felt, carbon cloth, graphite and its modified materials, and the MBR membrane module (9) is also used as the MFC cathode, and the material is stainless steel mesh modified by conductive polymer, non-woven fabric, carbon felt, carbon cloth.
本发明的优点Advantages of the invention
1.污水中包括葡萄糖在内的大部分有机物在MFC阳极(2)发生氧化反应,产生的电子经由MFC阳极(2)、导线(15)和负载(14)传递到阴极,产生的电能用于补偿MBR的电能消耗,可有效降低运行成本。1. Most of the organic matter in the sewage, including glucose, undergoes an oxidation reaction at the MFC anode (2), and the generated electrons are transferred to the cathode through the MFC anode (2), the wire (15) and the load (14), and the generated electric energy is used for Compensating the power consumption of the MBR can effectively reduce the operating cost.
2.MFC阳极(2)氧化产生的质子随水流穿越折流板到达MBR,与电子和氧气结合生成水,消除了普通MFC阳极易酸化、反馈抑制产电微生物活性的问题,阳极氧化后的极少量剩余有机物也随水流穿越折流板到达阴极好氧区,进一步好氧矿化去除。2. The protons produced by the oxidation of the MFC anode (2) pass through the baffles with the water flow to reach the MBR, and combine with electrons and oxygen to form water, which eliminates the problems of easy acidification of ordinary MFC anodes and feedback inhibition of the activity of electricity-producing microorganisms. A very small amount of remaining organic matter also passes through the baffle plate with the water flow to reach the cathode aerobic zone, and is further removed by aerobic mineralization.
3.由导电聚合物膜组件(9)、曝气管(10)、电极/水管固定塞(13)、出水管(11)和池体(1)组成的MBR可兼做MFC阴极室,为好氧区,MBR膜组件(9)兼做MFC阴极,其材料为导电聚合物修饰的不锈钢网、无纺布、碳毡、碳布,在传递电子的同时可为MBR膜表面与膜面污染物间提供静电斥力,有效缓解膜污染。3. The MBR composed of conductive polymer membrane module (9), aeration pipe (10), electrode/water pipe fixing plug (13), outlet pipe (11) and pool body (1) can also be used as MFC cathode chamber, for In the aerobic area, the MBR membrane module (9) is also used as the MFC cathode, and its material is stainless steel mesh, non-woven fabric, carbon felt, and carbon cloth modified by conductive polymers, which can pollute the surface of the MBR membrane and the membrane surface while transmitting electrons. Electrostatic repulsion is provided between objects to effectively alleviate membrane fouling.
4.由3~7块折流板(8)和池体(1)构成的弓形折流板区为缺氧区,保证了阳极室的厌氧和MBR的好氧状态,由于此缺氧区的存在,使得硝化和反硝化反应得以发生,系统脱氮效果好,同时折流板还用于拦截厌氧区的污泥,防止污泥流入MBR,影响出水水质,另外还是阳极产生的质子随水流到好氧区阴极的通道;通过隔板数量和隔板在池体中的位置,可以调整各部分的水力停留时间,以满足不同水质的处理要求。4. The bow-shaped baffle area composed of 3 to 7 baffles (8) and the pool body (1) is an anoxic area, which ensures the anaerobic state of the anode chamber and the aerobic state of the MBR. Due to this anoxic area The existence of nitrification and denitrification reactions can occur, and the denitrification effect of the system is good. At the same time, the baffles are also used to intercept the sludge in the anaerobic zone, preventing the sludge from flowing into the MBR and affecting the quality of the effluent water. In addition, the protons produced by the anode are The channel for water to flow to the cathode in the aerobic zone; through the number of partitions and the position of the partitions in the pool body, the hydraulic retention time of each part can be adjusted to meet the treatment requirements of different water quality.
5.该装置结构简单,操作管理方便,采用折流板替代普通MFC中的质子交换膜,大大降低了系统构建成本。5. The device has a simple structure and is easy to operate and manage. Baffles are used to replace the proton exchange membrane in ordinary MFC, which greatly reduces the system construction cost.
6.与传统MBR系统相比,吨污水处理能耗降低30%~70%,系统的COD和氨氮去除率均为70.0%~99.8%,出水水质符合行业回用标准。6. Compared with the traditional MBR system, the energy consumption per ton of sewage treatment is reduced by 30% to 70%, the COD and ammonia nitrogen removal rates of the system are both 70.0% to 99.8%, and the effluent water quality meets the industry reuse standard.
附图说明Description of drawings
附图为本发明装置示意图。Accompanying drawing is the device diagram of the present invention.
具体实施方式Detailed ways
实施例1:MFC阳极(2)采用碳毡,导流板(8)采用3块交叉布置,MBR膜组件(9)兼MFC阴极采用石墨烯、聚偏氟乙烯1∶2混合修饰无纺布。系统进水水质如下:COD浓度为500mg/L,氨氮20mg/L,pH值为7;MFC阳极室的HRT为8h;折流板区HRT为10h,溶解氧浓度为0.2mg/L;MBR单元的HRT为6h,溶解氧浓度为4.0mg/L;温度为25℃。Example 1: MFC anode (2) adopts carbon felt, deflector (8) adopts 3 pieces of cross arrangement, MBR membrane module (9) and MFC cathode adopt graphene, polyvinylidene fluoride 1: 2 mixed modification non-woven fabric . The water quality of the system is as follows: COD concentration is 500mg/L, ammonia nitrogen is 20mg/L, and the pH value is 7; the HRT of the MFC anode chamber is 8h; the HRT of the baffle area is 10h, and the dissolved oxygen concentration is 0.2mg/L; the MBR unit The HRT is 6h, the dissolved oxygen concentration is 4.0mg/L; the temperature is 25°C.
实施例2:MFC阳极(2)采用碳布,导流板(8)采用5块交叉布置,MBR膜组件(9)兼MFC阴极采用聚苯胺修饰不锈钢网。系统进水水质如下:COD浓度为1000mg/L,氨氮50mg/L,pH值为8;MFC阳极室的HRT为10h;折流板区HRT为12h,溶解氧浓度为0.5mg/L;MBR单元的HRT为8h,溶解氧浓度为2.0mg/L;温度为30℃。Example 2: The MFC anode (2) is made of carbon cloth, the deflector (8) is arranged in five intersections, and the MBR membrane module (9) and the MFC cathode are made of polyaniline-modified stainless steel mesh. The water quality of the system feed water is as follows: COD concentration is 1000mg/L, ammonia nitrogen is 50mg/L, and the pH value is 8; the HRT of the MFC anode chamber is 10h; the HRT of the baffle area is 12h, and the dissolved oxygen concentration is 0.5mg/L; the MBR unit The HRT is 8h, the dissolved oxygen concentration is 2.0mg/L; the temperature is 30℃.
实施例3:MFC阳极(2)采用石墨,导流板(8)采用7块交叉布置,MBR膜组件(9)兼MFC阴极采用石墨烯修饰碳布。系统进水水质如下:COD浓度为10000mg/L,氨氮2000mg/L,pH值为9;MFC阳极室的HRT为22h;折流板区HRT为18h,溶解氧浓度为0.1mg/L;MBR单元的HRT为12h,溶解氧浓度为6.0mg/L;温度为35℃。Example 3: The MFC anode (2) is made of graphite, the deflector (8) is arranged in 7 intersections, and the MBR membrane module (9) and the MFC cathode are made of graphene-modified carbon cloth. The water quality of the system inlet water is as follows: COD concentration is 10000mg/L, ammonia nitrogen is 2000mg/L, and the pH value is 9; the HRT of the MFC anode chamber is 22h; the HRT of the baffle area is 18h, and the dissolved oxygen concentration is 0.1mg/L; the MBR unit The HRT is 12h, the dissolved oxygen concentration is 6.0mg/L; the temperature is 35°C.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310732550.8A CN103848539A (en) | 2013-12-26 | 2013-12-26 | Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310732550.8A CN103848539A (en) | 2013-12-26 | 2013-12-26 | Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103848539A true CN103848539A (en) | 2014-06-11 |
Family
ID=50856715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310732550.8A Pending CN103848539A (en) | 2013-12-26 | 2013-12-26 | Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103848539A (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104148371A (en) * | 2014-07-25 | 2014-11-19 | 中国环境科学研究院 | Organic garbage treatment-energy regeneration combined device and organic garbage treatment method |
| CN104538659A (en) * | 2014-12-26 | 2015-04-22 | 吴云 | Microbial fuel cell by taking conducting film aerating bio-film reactor as cathode |
| CN104843862A (en) * | 2014-12-31 | 2015-08-19 | 广东省微生物研究所 | Process for intensifying anaerobic degradation and transformation of azo dyes based on breath of microbial electrode |
| CN104944697A (en) * | 2015-06-12 | 2015-09-30 | 浙江大学 | Microbial electrolysis cell-Fenton combined treatment device and process for treating furniture production wastewater |
| CN107098459A (en) * | 2017-03-10 | 2017-08-29 | 广东工业大学 | A kind of electrochemical appliance and processing method for handling ammonia nitrogen in high density organic wastewater |
| CN107352648A (en) * | 2017-09-11 | 2017-11-17 | 上海海事大学 | New up flow type MFC MBR coupled systems under a kind of anaerobic condition |
| CN107840456A (en) * | 2017-12-12 | 2018-03-27 | 广州市清逸水处理科技有限公司 | A kind of internal electric field stimulates integral type film biological reactor |
| CN108002527A (en) * | 2017-12-15 | 2018-05-08 | 天津工业大学 | A kind of new membrane bioreactor-microbiological fuel cell coupled system |
| CN108083454A (en) * | 2018-01-11 | 2018-05-29 | 广西师范大学 | A kind of device that Industrial Wastewater Treatment denitrogenation production capacity is carried out based on DAMO |
| CN108128899A (en) * | 2018-02-07 | 2018-06-08 | 山西大学 | A kind of EGSB-MFC coupled systems and its biodegrading process for being used to handle coking wastewater difficult to degrade |
| CN109516543A (en) * | 2018-12-14 | 2019-03-26 | 中北大学 | Two-chamber continuous flow MFC/MBR integrated coking wastewater treatment device and method |
| CN111498980A (en) * | 2020-04-24 | 2020-08-07 | 东南大学 | Membrane pollution prevention MFC-AnMBR coupling device |
| CN111747530A (en) * | 2020-08-04 | 2020-10-09 | 清华大学 | Microbial electrochemical coupled membrane bioreactor system and sewage treatment method |
| CN112939198A (en) * | 2021-03-31 | 2021-06-11 | 天津城建大学 | Integrated double-chamber coupling system for enhancing micro-pollutant degradation and gas production performance |
| CN114314808A (en) * | 2021-12-16 | 2022-04-12 | 济南大学 | Microbial fuel cell coupled completely autotrophic dynamic membrane reactor denitrification device and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101673837A (en) * | 2009-09-22 | 2010-03-17 | 北京大学深圳研究生院 | Microbial fuel cells system and method for processing microbial wastewater and generating electric energy |
| CN101924228A (en) * | 2010-08-25 | 2010-12-22 | 天津理工大学 | A kind of microbial fuel cell and its method for treating aniline wastewater |
| CN101941759A (en) * | 2010-08-16 | 2011-01-12 | 大连理工大学 | Method for improving pollution resistance and flux of membrane by using weak electric field |
| CN102616918A (en) * | 2012-03-23 | 2012-08-01 | 大连理工大学 | Membrane bioreactor (MBR)/microbial fuel cell (MFC) directly-coupled reactor and wastewater treatment method |
| CN102701543A (en) * | 2012-06-28 | 2012-10-03 | 天津工业大学 | Water treatment device combining microbial fuel cells with membrane technology |
| CN103241895A (en) * | 2013-04-28 | 2013-08-14 | 哈尔滨工业大学 | Membrane biological electrochemical reactor device with high-quality effluent and low membrane pollution |
-
2013
- 2013-12-26 CN CN201310732550.8A patent/CN103848539A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101673837A (en) * | 2009-09-22 | 2010-03-17 | 北京大学深圳研究生院 | Microbial fuel cells system and method for processing microbial wastewater and generating electric energy |
| CN101941759A (en) * | 2010-08-16 | 2011-01-12 | 大连理工大学 | Method for improving pollution resistance and flux of membrane by using weak electric field |
| CN101924228A (en) * | 2010-08-25 | 2010-12-22 | 天津理工大学 | A kind of microbial fuel cell and its method for treating aniline wastewater |
| CN102616918A (en) * | 2012-03-23 | 2012-08-01 | 大连理工大学 | Membrane bioreactor (MBR)/microbial fuel cell (MFC) directly-coupled reactor and wastewater treatment method |
| CN102701543A (en) * | 2012-06-28 | 2012-10-03 | 天津工业大学 | Water treatment device combining microbial fuel cells with membrane technology |
| CN103241895A (en) * | 2013-04-28 | 2013-08-14 | 哈尔滨工业大学 | Membrane biological electrochemical reactor device with high-quality effluent and low membrane pollution |
Cited By (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104148371B (en) * | 2014-07-25 | 2016-10-19 | 中国环境科学研究院 | Organic waste treatment-energy regeneration combined device and organic waste treatment method |
| CN104148371A (en) * | 2014-07-25 | 2014-11-19 | 中国环境科学研究院 | Organic garbage treatment-energy regeneration combined device and organic garbage treatment method |
| CN104538659A (en) * | 2014-12-26 | 2015-04-22 | 吴云 | Microbial fuel cell by taking conducting film aerating bio-film reactor as cathode |
| CN104538659B (en) * | 2014-12-26 | 2017-09-26 | 吴云 | A kind of microbiological fuel cell using conductive membrane aeration biomembrane reactor as negative electrode |
| CN104843862A (en) * | 2014-12-31 | 2015-08-19 | 广东省微生物研究所 | Process for intensifying anaerobic degradation and transformation of azo dyes based on breath of microbial electrode |
| CN104944697A (en) * | 2015-06-12 | 2015-09-30 | 浙江大学 | Microbial electrolysis cell-Fenton combined treatment device and process for treating furniture production wastewater |
| CN107098459B (en) * | 2017-03-10 | 2020-08-11 | 广东工业大学 | Electrochemical device and treatment method for treating high-concentration ammonia nitrogen organic wastewater |
| CN107098459A (en) * | 2017-03-10 | 2017-08-29 | 广东工业大学 | A kind of electrochemical appliance and processing method for handling ammonia nitrogen in high density organic wastewater |
| CN107352648B (en) * | 2017-09-11 | 2020-09-29 | 上海海事大学 | Novel up-flow MFC-MBR coupled system under anaerobic condition |
| CN107352648A (en) * | 2017-09-11 | 2017-11-17 | 上海海事大学 | New up flow type MFC MBR coupled systems under a kind of anaerobic condition |
| CN107840456B (en) * | 2017-12-12 | 2023-11-24 | 广州市清逸环保科技有限公司 | An integrated membrane bioreactor stimulated by an internal electric field |
| CN107840456A (en) * | 2017-12-12 | 2018-03-27 | 广州市清逸水处理科技有限公司 | A kind of internal electric field stimulates integral type film biological reactor |
| CN108002527A (en) * | 2017-12-15 | 2018-05-08 | 天津工业大学 | A kind of new membrane bioreactor-microbiological fuel cell coupled system |
| CN108083454A (en) * | 2018-01-11 | 2018-05-29 | 广西师范大学 | A kind of device that Industrial Wastewater Treatment denitrogenation production capacity is carried out based on DAMO |
| CN108128899A (en) * | 2018-02-07 | 2018-06-08 | 山西大学 | A kind of EGSB-MFC coupled systems and its biodegrading process for being used to handle coking wastewater difficult to degrade |
| CN109516543A (en) * | 2018-12-14 | 2019-03-26 | 中北大学 | Two-chamber continuous flow MFC/MBR integrated coking wastewater treatment device and method |
| CN114477421A (en) * | 2018-12-14 | 2022-05-13 | 中北大学 | Double-chamber continuous flow integrated coking wastewater treatment device and method |
| CN111498980A (en) * | 2020-04-24 | 2020-08-07 | 东南大学 | Membrane pollution prevention MFC-AnMBR coupling device |
| CN111747530A (en) * | 2020-08-04 | 2020-10-09 | 清华大学 | Microbial electrochemical coupled membrane bioreactor system and sewage treatment method |
| CN111747530B (en) * | 2020-08-04 | 2023-08-25 | 清华大学 | Microbial electrochemical coupling membrane bioreactor system and sewage treatment method |
| CN112939198A (en) * | 2021-03-31 | 2021-06-11 | 天津城建大学 | Integrated double-chamber coupling system for enhancing micro-pollutant degradation and gas production performance |
| CN114314808A (en) * | 2021-12-16 | 2022-04-12 | 济南大学 | Microbial fuel cell coupled completely autotrophic dynamic membrane reactor denitrification device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103848539A (en) | Organic wastewater treatment device coupled with low-energy-consumption membrane biological reactor of microbial fuel cell | |
| CN104478073B (en) | A kind of device utilizing ABR-bio electricity Fenton coupling technique to process difficult for biological degradation industrial wastewater | |
| CN113149343B (en) | Electrochemical nitrogen and phosphorus removal device and method | |
| CN105481208B (en) | A kind of high-efficiency sewage treatment process and device based on electron stream orientation regulation and control | |
| CN104600345B (en) | Continuous-flow anaerobic biological cathode microbial fuel cell | |
| CN108946941B (en) | A Low Energy Consumption Microbial-Electrochemical Sewage Treatment System | |
| CN105217797B (en) | A kind of composite vertical current artificial wetland couples the method and device of microorganism electrolysis cell strengthened denitrification | |
| CN110104874A (en) | A kind of continuous flow wetland type microbiological fuel cell reactor sewage-treatment plant | |
| CN110818190B (en) | Multi-electrode electrocoagulation-anaerobic microorganism electroplating comprehensive wastewater treatment device and method and heavy metal recovery method | |
| CN102110835A (en) | Microbe fuel cell device for enhanced nitrogen removal in AAO sewage treatment technology | |
| Das et al. | A sustainable approach for the production of green energy with the holistic treatment of wastewater through microbial electrochemical technologies: a review | |
| CN109970187A (en) | A device and method for adding biomass carbon particles to strengthen UASB process performance | |
| CN105355950A (en) | Large-scale biological negative electrode microbial fuel cell stack apparatus | |
| CN102502946A (en) | Method for treating chemical wastewater by utilizing three-dimensional electrode-biological membrane process | |
| CN110668556B (en) | Visible light catalysis coupling bioelectrochemical wetland system and application thereof | |
| CN109912145B (en) | Aerobic granular sludge power generation device | |
| CN107381811B (en) | Microbial dual-source electrochemical sewage reactor and method for treating low C/N urban sewage | |
| CN116253475B (en) | An electro-Fenton sewage treatment system and its application | |
| CN103865957B (en) | A kind of method combining hydrogen-producing acetogens and product electricity bacterium enhanced biological hydrogen manufacturing usefulness | |
| CN104628134A (en) | Up-flow electrochemical biofilm reactor | |
| CN208008545U (en) | A kind of EGSB-MFC coupled systems of processing coking wastewater difficult to degrade | |
| CN110127840A (en) | Sewage Treatment Based on Aerobic Granular Sludge Bed Reactor Cathode Microbial Fuel Cell | |
| CN103739161A (en) | Low-energy-consumption degradation-resistant organic wastewater recycling method | |
| CN103739070A (en) | Low-energy-consumption municipal wastewater recycling method | |
| CN208716927U (en) | The integrated apparatus of advanced oxidation processing waste water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140611 |