CN109956620A - An energy-saving catalytic water treatment device with a power generation capacity of 20-87W/m2 - Google Patents

An energy-saving catalytic water treatment device with a power generation capacity of 20-87W/m2 Download PDF

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CN109956620A
CN109956620A CN201910241073.2A CN201910241073A CN109956620A CN 109956620 A CN109956620 A CN 109956620A CN 201910241073 A CN201910241073 A CN 201910241073A CN 109956620 A CN109956620 A CN 109956620A
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anode
energy
water treatment
treatment device
cathode
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CN109956620B (en
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柳丽芬
张倩
拉贝
张艺臻
郑玥石
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Dalian University of Technology
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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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • 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
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • 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
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/009Apparatus with independent power supply, e.g. solar cells, windpower or fuel cells
    • 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
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

本发明公开了一种产电20‑87W/m2的节能催化水处理装置,属于废水资源化和能源化领域。该装置包括池体、导线、负载、阴极室、曝气装置、出水溢流装置、进水泵、进水管、阳极室、碳棒和沙粒隔层。废水通过阳极室的产电微生物分解废水中的有机物并释放电子,再通过沙粒隔层过滤掉颗粒物及阳极微生物后向上渗入阴极室中,再经曝气装置进一步降解通过出水溢流装置流出,实现废水处理及废水产电。废水经过一次流过该装置,或流过多个串联的组合单元装置,实现有机质被降解、颗粒悬浮物被截留;阴极电极的负载催化剂能提高产电能力和对污染物的降解能力,有效提高出水水质;且该装置结构简单,操作方便,运行费用少。

The invention discloses an energy-saving catalytic water treatment device capable of generating 20-87 W/m 2 of electricity, belonging to the field of waste water resource utilization and energy utilization. The device includes a tank body, a wire, a load, a cathode chamber, an aeration device, an effluent overflow device, an inlet pump, a water inlet pipe, an anode chamber, a carbon rod and a sand separator. The wastewater passes through the electricity-generating microorganisms in the anode chamber to decompose the organic matter in the wastewater and release electrons, and then filter out the particles and anode microorganisms through the sand interlayer, and then infiltrate upward into the cathode chamber, and then further degrade through the aeration device and flow out through the effluent overflow device. Realize wastewater treatment and wastewater power generation. The wastewater flows through the device once, or through a plurality of combined unit devices in series, to achieve the degradation of organic matter and the retention of suspended particulate matter; the supported catalyst on the cathode electrode can improve the power generation capacity and the degradation capacity of pollutants, effectively improving the The water quality of the effluent is high; and the device is simple in structure, convenient in operation and low in operating cost.

Description

一种产电20-87W/m2的节能催化水处理装置An energy-saving catalytic water treatment device with a power generation capacity of 20-87W/m2

技术领域technical field

本发明属于废水资源化和能源化技术领域,具体涉及达到单位电极面积产电20W/m2的新型水处理装置,以活性炭颗粒和微生物作生物阳极,以基底为碳纤维布的复合电极作阴极,中间为石英砂与锰砂隔层。废水先进入装置的阳极,在生物阳极作用下,污染物浓度梯度降低,经隔层的过滤和截留作用、阴极催化作用得到进一步净化。耦合微生物产电作用和阴极催化作用如催化氧化污染物氨/COD(化学需氧量)等、还原硝态氮和氧还原作用,实现了高效水处理。The invention belongs to the technical field of waste water resource utilization and energy utilization, and in particular relates to a novel water treatment device capable of generating electricity per unit electrode area of 20 W/m 2 . In the middle is the interlayer of quartz sand and manganese sand. Wastewater first enters the anode of the device. Under the action of the biological anode, the concentration gradient of pollutants decreases, and is further purified by the filtration and interception of the interlayer and the catalytic action of the cathode. Coupling microbial electricity generation and cathodic catalysis, such as catalytic oxidation of pollutants such as ammonia/COD (chemical oxygen demand), reduction of nitrate nitrogen and oxygen reduction, realizes high-efficiency water treatment.

背景技术Background technique

生物产电技术,是近些年迅速发展起来的一种将生物法与电化学技术结合的新技术,将其应用到废水处理领域,能够在降解有机物的同时产生电能。微生物可将底物中的有机物直接转化成CO2、H2O等小分子无机物,并将其中的化学能转化为电能,不排放污染物,是一种清洁能源。阳极微生物能够将有机物氧化,并将氧化过程中释放出来的电子转移到电极材料上,进而以电流的形式从外电路输出。微生物的生长需要厌氧或微氧环境,以保证最终电子受体是电极而不是氧气,否则电子将直接参与还原生成水。特别地,如果将有机废水作为生物阳极的底物,废水中的有机物会被微生物降解,这样便完成了有机物的氧化分解、电子流动和电位梯度的形成。从能源和环境保护的角度来看,这样一个过程实际上是实现了污染物向电能的直接转化,同时污染物又被分解,使废水不但被处理,而且“变废为宝”。但其对废水的处理效率较低,阳极出水水质一般达不到排放标准,需进一步处理,此外电能输出较小、库伦效率低等问题也有待解决。Biological power generation technology is a new technology that has developed rapidly in recent years by combining biological methods with electrochemical technology. When it is applied to the field of wastewater treatment, it can generate electricity while degrading organic matter. Microorganisms can directly convert organic substances in substrates into small molecular inorganic substances such as CO 2 and H 2 O, and convert the chemical energy into electricity without emitting pollutants, which is a kind of clean energy. Anodic microorganisms can oxidize organic matter and transfer the electrons released during the oxidation process to electrode materials, which are then output from external circuits in the form of current. The growth of microorganisms requires an anaerobic or micro-aerobic environment to ensure that the final electron acceptor is the electrode rather than oxygen, otherwise the electrons will directly participate in the reduction to produce water. In particular, if organic wastewater is used as the substrate of the bioanode, the organic matter in the wastewater will be degraded by microorganisms, thus completing the oxidative decomposition of organic matter, electron flow and formation of potential gradient. From the perspective of energy and environmental protection, such a process actually realizes the direct conversion of pollutants into electrical energy, and at the same time the pollutants are decomposed, so that the wastewater is not only treated, but also "turns waste into treasure". However, its treatment efficiency of wastewater is low, and the quality of anode effluent generally does not meet the discharge standard and needs further treatment. In addition, problems such as small power output and low Coulomb efficiency also need to be solved.

发明内容SUMMARY OF THE INVENTION

为解决上述问题,本发明提供了一种产电20-87W/m2的节能催化水处理装置,构建了一种自生电场电催化的水处理装置,本发明的技术方案为:In order to solve the above-mentioned problems, the present invention provides an energy - saving catalytic water treatment device capable of producing electricity of 20-87W/m , and a self-generated electric field electrocatalytic water treatment device is constructed. The technical scheme of the present invention is as follows:

一种产电20-87W/m2的节能催化水处理装置,包括池体1、导线2、负载3、阴极室4、曝气装置5、出水溢流装置6、进水泵7、进水管8、阳极室9、碳棒10和沙粒隔层11;An energy-saving catalytic water treatment device capable of producing 20-87W/m2 of electricity, comprising a pool body 1, a wire 2 , a load 3, a cathode chamber 4, an aeration device 5, an effluent overflow device 6, an inlet pump 7, and a water inlet pipe 8 , the anode chamber 9, the carbon rod 10 and the sand partition layer 11;

其中,沙粒隔层11位于池体1中部,沙粒隔层11将池体1分为阴极室4和阳极室9两部分;所述阳极室9位于沙粒隔层11的下方,阳极电极为碳棒10,碳棒10的一端连接导线;阳极室9用活性炭填充并负载产电微生物;所述阴极室4位于沙粒隔层11的上方,阴极电极以导电性材料为基底并负载催化剂,阴极电极的一端连接导线并接入负载3,与阳极电极碳棒10一端的导线相连,从而形成外电路;曝气装置5位于阴极室4、池体1顶部的开口处,用于向阴极室4内补充空气或氧气,进一步促进催化降解废水中的有机物;出水溢流装置6位于阴极室4、池体1上方、低于曝气装置5所在的开口处;进水泵7通过进水管8通入至阳极室9、位于池体1的下方;废水通过进水泵7从进水管8流入阳极室9,阳极室9的产电微生物分解废水中的有机物并释放电子,废水再通过沙粒隔层11过滤掉颗粒物及阳极微生物后向上渗入阴极室4中,再经曝气装置5进一步降解通过出水溢流装置6流出,从而实现废水处理及废水产电。Wherein, the sand separator 11 is located in the middle of the pool body 1, and the sand separator 11 divides the pool 1 into two parts: the cathode chamber 4 and the anode chamber 9; the anode chamber 9 is located under the sand separator 11, and the anode electrode It is a carbon rod 10, and one end of the carbon rod 10 is connected to a wire; the anode chamber 9 is filled with activated carbon and loaded with electricity-producing microorganisms; the cathode chamber 4 is located above the sand partition layer 11, and the cathode electrode is based on conductive materials and supports catalysts , one end of the cathode electrode is connected to the wire and connected to the load 3, and is connected to the wire of one end of the anode electrode carbon rod 10, thereby forming an external circuit; the aeration device 5 is located at the opening of the cathode chamber 4 and the top of the pool body 1, and is used for the cathode. Air or oxygen is supplemented in the chamber 4 to further promote the catalytic degradation of organic matter in the wastewater; the effluent overflow device 6 is located in the cathode chamber 4, above the pool body 1, below the opening where the aeration device 5 is located; the inlet pump 7 passes through the inlet pipe 8 The waste water flows into the anode chamber 9 from the water inlet pipe 8 through the inlet pump 7, and the electricity-producing microorganisms in the anode chamber 9 decompose the organic matter in the waste water and release electrons, and the waste water is separated by sand particles. The layer 11 filters out particulate matter and anode microorganisms and then infiltrates upwards into the cathode chamber 4, and is further degraded by the aeration device 5 and flows out through the effluent overflow device 6, thereby realizing wastewater treatment and wastewater power generation.

进一步地,阴极电极的基底导电性材料为碳纤维布或活性炭;阴极电极的负载催化剂为二氧化钛复合催化剂、含Fe、Mn、Zn、C、F、O元素的催化剂。Further, the base conductive material of the cathode electrode is carbon fiber cloth or activated carbon; the supported catalyst of the cathode electrode is a titanium dioxide composite catalyst, a catalyst containing Fe, Mn, Zn, C, F, and O elements.

进一步地,阳极室9活性炭的填充率为40%~95%。Further, the filling rate of the activated carbon in the anode chamber 9 is 40% to 95%.

进一步地,沙粒隔层11为石英砂、锰砂或二者的混合物。Further, the sand interlayer 11 is quartz sand, manganese sand or a mixture of the two.

进一步地,负载3为100~1000Ω的电阻。Further, the load 3 is a resistance of 100-1000Ω.

进一步地,与阳极电极碳棒10平行插入一个饱和甘汞电极作为参比电极,在碳棒10和参比电极上接入数据采集卡,实时采集阳极的电势数据;在阴极电极的导线上接入数据采集卡,实时采集电池的电势数据。Further, a saturated calomel electrode is inserted in parallel with the anode electrode carbon rod 10 as a reference electrode, a data acquisition card is connected to the carbon rod 10 and the reference electrode, and the potential data of the anode is collected in real time; Enter the data acquisition card to collect the potential data of the battery in real time.

进一步地,池体1的形状为横管形、柱形、方形或多层组合结构。Further, the shape of the pool body 1 is a horizontal tube shape, a column shape, a square shape or a multi-layer composite structure.

本发明的有益效果:本发明提供了一种产电20-87W/m2的节能催化水处理装置,该装置可由多层或多个组合单元构成,整体外壳可采用水泥、PVC、玻璃钢等材料;该装置根据需要选择不同形状的池体,灵活控制水力停留时间和路径,提高对废水中有机物的降解和转化;廉价砂层代替质子交换膜,既降低了成本,又对废水起到过滤作用,截留大颗粒物质和阳极微生物,有利于提高出水水质;阴极电极催化作用进一步提升废水处理效果,同时生物阳极产电缓解了阴极的污染;且该装置结构简单,操作方便。Beneficial effects of the present invention: The present invention provides an energy-saving catalytic water treatment device capable of producing electricity of 20-87W/m 2 , the device can be composed of multiple layers or multiple combined units, and the overall shell can be made of materials such as cement, PVC, glass fiber reinforced plastic, etc. ; The device selects different shapes of pools according to the needs, flexibly controls the hydraulic retention time and path, and improves the degradation and transformation of organic matter in the wastewater; the cheap sand layer replaces the proton exchange membrane, which not only reduces the cost, but also plays a role in filtration of wastewater , intercepting large particulate matter and anode microorganisms, which is conducive to improving the quality of effluent; the catalytic action of the cathode electrode further improves the effect of wastewater treatment, and at the same time, the biological anode generates electricity to alleviate the pollution of the cathode; and the device has a simple structure and is easy to operate.

附图说明Description of drawings

图1是本发明的一种横管式水处理装置设计示意图。FIG. 1 is a schematic diagram of the design of a horizontal tube type water treatment device of the present invention.

图2是本发明的一种柱状池形水处理装置设计示意图。FIG. 2 is a schematic diagram of the design of a columnar pool-shaped water treatment device of the present invention.

图3是本发明的一种方形池水处理装置二级串联装置设计示意图。Fig. 3 is a schematic diagram of the design of a secondary series device of a square pond water treatment device of the present invention.

图4是本发明的COD脱除性能图,横坐标表示时间,单位d;纵坐标表示出水浓度和去除效率,单位mg/L和%;方块和圆点表示COD出水浓度,倒三角和菱形代表COD去除效率。Fig. 4 is the COD removal performance diagram of the present invention, the abscissa represents time, the unit d; the ordinate represents the effluent concentration and removal efficiency, the unit mg/L and %; the square and the circle point represent the COD effluent concentration, and the inverted triangle and the diamond represent COD removal efficiency.

图5是横管式水处理装置的电势图,横坐标表示时间,单位d;纵坐标表示电压,单位V;圆形和倒三角代表电池电势,正三角和菱形表示阳极电势。。Figure 5 is the potential diagram of the horizontal tube water treatment device, the abscissa represents the time, the unit d; the ordinate represents the voltage, the unit V; the circle and the inverted triangle represent the battery potential, and the positive triangle and the diamond represent the anode potential. .

图中:1池体;2导线;3负载;4阴极室;5曝气装置;6出水溢流装置;7水泵;8进水管;9阳极室;10碳棒;11沙粒隔层。In the figure: 1 tank body; 2 wires; 3 load; 4 cathode chamber; 5 aeration device; 6 water overflow device; 7 water pump; 8 water inlet pipe; 9 anode chamber; 10 carbon rod;

具体实施方式Detailed ways

以下结合技术方案和附图详细叙述本发明的具体实施方式。The specific embodiments of the present invention are described in detail below with reference to the technical solutions and the accompanying drawings.

实施例1:一种横管式水处理装置Example 1: A horizontal tube water treatment device

结合图1,本实施方式是一种横管式水处理装置,该装置是由池体1、导线2、负载3、阴极室4、曝气装置5、出水溢流装置6、进水泵7、进水管8、阳极室9、碳棒10和沙粒隔层11组成,装置设计尺寸为Ф10.5cm×0.6m,总有效体积为4L。1, this embodiment is a horizontal tube water treatment device, which is composed of a pool body 1, a lead 2, a load 3, a cathode chamber 4, an aeration device 5, an effluent overflow device 6, an inlet pump 7, The water inlet pipe 8, the anode chamber 9, the carbon rod 10 and the sand partition layer 11 are composed. The design size of the device is Ф10.5cm×0.6m, and the total effective volume is 4L.

其中,沙粒隔层11位于池体1中部,沙粒隔层11将池体1分为阴极室4和阳极室9两部分,沙粒隔层11的设计尺寸为10cm×1.3cm×0.6m;填充物为石英砂和锰砂按1:1组成的混合物,0.5-1mm,填充率为100%。Among them, the sand separator 11 is located in the middle of the pool body 1, and the sand separator 11 divides the pool 1 into two parts: the cathode chamber 4 and the anode chamber 9, and the design size of the sand separator 11 is 10cm×1.3cm×0.6m ; The filler is a mixture of quartz sand and manganese sand at 1:1, 0.5-1mm, and the filling rate is 100%.

阳极室9位于池体下部,阳极室9位于沙粒隔层11的下方,阳极电极为碳棒10,碳棒10的尺寸为Ф8mm×0.4m,碳棒10的一端连接导线;阳极室9用活性炭颗粒填充,3-5mm,填充率为40%~95%,阳极整体含有碳棒、活性炭、微生物;与阳极电极碳棒平行插入一个饱和甘汞电极作为参比电极,在碳棒10和参比电极上分别接入数据采集卡,实时采集阳极电势数据。The anode chamber 9 is located at the lower part of the tank body, the anode chamber 9 is located under the sand grain separator 11, the anode electrode is a carbon rod 10, the size of the carbon rod 10 is Ф8mm×0.4m, and one end of the carbon rod 10 is connected to a wire; the anode chamber 9 is used for Filled with activated carbon particles, 3-5mm, the filling rate is 40% to 95%, the anode as a whole contains carbon rods, activated carbon, and microorganisms; a saturated calomel electrode is inserted parallel to the anode electrode carbon rod as a reference electrode. A data acquisition card is connected to the specific electrode to collect anode potential data in real time.

阴极室4位于沙粒隔层11的上方,阴极电极以碳纤维布为基底,并负载催化剂,常用的电极催化剂有二氧化钛复合催化剂或含Fe、Mn、Zn、C、F、O等元素的催化剂;阴极电极的一端连接导线并接入500Ω电阻,与阳极电极碳棒10一端的导线相连,从而形成外电路,阴极导线也接入数据采集卡,实时采集电池电势数据;池体1上部的阴极室开口,放入曝气装置5,阴极室设置出水溢流装置6;进水泵7通过进水管8通入至阳极室9、位于池体1的下方;废水通过进水泵7从进水管8流入阳极室9,阳极室9的产电微生物分解废水中的有机物并释放电子,废水再通过沙粒隔层11过滤掉颗粒物及阳极微生物后向上渗入阴极室4中,再经曝气装置5进一步降解通过出水溢流装置6流出,从而实现废水处理及废水产电。The cathode chamber 4 is located above the sand partition layer 11, and the cathode electrode is based on carbon fiber cloth and supports a catalyst. Commonly used electrode catalysts include titanium dioxide composite catalysts or catalysts containing Fe, Mn, Zn, C, F, O and other elements; One end of the cathode electrode is connected to a wire and connected to a 500Ω resistor, and is connected to the wire at one end of the anode electrode carbon rod 10 to form an external circuit. The cathode wire is also connected to the data acquisition card to collect battery potential data in real time; the cathode chamber on the upper part of the cell body 1 The opening is put into the aeration device 5, and the cathode chamber is provided with a water overflow device 6; the inlet water pump 7 is passed into the anode chamber 9 through the water inlet pipe 8, and is located below the pool body 1; The waste water flows into the anode from the water inlet pipe 8 through the inlet water pump 7 Chamber 9, the electricity-producing microorganisms in the anode chamber 9 decompose the organic matter in the wastewater and release electrons, and the wastewater passes through the sand partition 11 to filter out particulate matter and anode microorganisms, and then penetrates upward into the cathode chamber 4, and is further degraded by the aeration device 5. The effluent overflow device 6 flows out, thereby realizing wastewater treatment and wastewater power generation.

溢流出水可以直接作为二级处理进水,串联与图1相同类型的反应器进行二级处理,二级处理能进一步净化废水,在处理高浓度废水时,可有效提高出水水质,达到排放标准。The overflow effluent can be directly used as the influent for secondary treatment, and the reactors of the same type as shown in Figure 1 are connected in series for secondary treatment. The secondary treatment can further purify the wastewater. When treating high-concentration wastewater, it can effectively improve the effluent quality and meet the discharge standards. .

图4和图5分别为该装置一级出水的COD去除性能图和产电性能图,应用不同的导电膜作阴极,COD去除率可达60%~90%,说明本装置能够实现废水处理和质能转化,即能够实现废水的资源化和能源化。Figures 4 and 5 are the COD removal performance diagram and power generation performance diagram of the primary effluent of the device, respectively. Using different conductive membranes as cathodes, the COD removal rate can reach 60% to 90%, indicating that the device can achieve wastewater treatment and The transformation of quality to energy means the resource utilization and energy utilization of wastewater can be realized.

实施例2一种柱状池形水处理装置Embodiment 2 A kind of columnar pool-shaped water treatment device

结合图2,在柱状池形水处理装置中,结合实施例1填充阳极室、多介质仓、阴极室,构成电路回路。阴极电极含有C、F、O、N、Ti金属等元素。废水经进水推流装置进入阳极室底部;多介质仓作为隔仓代替质子交换膜,废水流经的同时可以截留微生物和颗粒物;废水到达阴极后经导电膜催化作用,得到进一步净化,从溢流装置排出。系统外接负载,并连入数据采集卡。Referring to FIG. 2 , in the columnar pool-shaped water treatment device, the anode chamber, the multi-medium chamber and the cathode chamber are filled in combination with Example 1 to form a circuit loop. The cathode electrode contains C, F, O, N, Ti metals and other elements. The waste water enters the bottom of the anode chamber through the water inflow push device; the multi-media silo is used as a partition to replace the proton exchange membrane, and the waste water can retain microorganisms and particulate matter while passing through; after the waste water reaches the cathode, it is further purified by the catalysis of the conductive membrane, and the overflow flow device discharge. The system is connected to an external load and connected to a data acquisition card.

该装置在处理一种化工废水时,采用不同导电膜作阴极,COD去除率达到60~95%,TN(总氮)去除60~90%,每平米电极产电能力达到20W;光照阴极时,每平米电极产电能力达到87W。说明该装置能够实现废水的有效处理和质能转化。When the device treats a chemical wastewater, different conductive membranes are used as cathodes, the COD removal rate reaches 60-95%, the TN (total nitrogen) removal rate reaches 60-90%, and the power generation capacity per square meter of the electrode reaches 20W; when the cathode is illuminated, the The power generation capacity of the electrode per square meter reaches 87W. It shows that the device can realize the effective treatment and quality-energy conversion of wastewater.

实施例3一种二级水处理装置Embodiment 3 A kind of secondary water treatment device

结合图3,在方形池的水处理装置的单元中,阳极室和阴极室为左右结构,中间用多介质仓分隔。结合发明方案填充阳极、隔层、阴极,构成电路回路。其中,导电膜组件作为阴极,其含有F、C、N、O、Ti金属等元素。化工废水经进水流量调节装置进入左侧阳极室,经微生物作用后由隔仓进入阴极,微生物和颗粒物被截留在阳极室;阴极膜组件在曝气装置作用下进一步催化降解废水中的污染物,同时阴极耦合MBR,经膜组件过滤后出水。单级水处理装置在处理化工废水时,所得COD去除率可达60~90%。产电可达20W。Referring to FIG. 3 , in the unit of the water treatment device of the square tank, the anode chamber and the cathode chamber are left and right structures, and the middle is separated by a multi-media compartment. The anode, the separator and the cathode are filled in combination with the inventive scheme to form a circuit loop. Among them, the conductive film assembly is used as a cathode, which contains elements such as F, C, N, O, and Ti metals. The chemical wastewater enters the left anode chamber through the influent flow regulating device, and enters the cathode through the compartment after being acted by microorganisms. The microorganisms and particulate matter are trapped in the anode chamber; the cathode membrane module further catalyzes the degradation of pollutants in the wastewater under the action of the aeration device. At the same time, the cathode is coupled to the MBR, and the water is filtered through the membrane module. When the single-stage water treatment device treats chemical wastewater, the COD removal rate can reach 60-90%. The power generation can reach 20W.

单元的组合装置中布置多级、多层净化单元,废水可以同时进入每个单元的阳极,也可以先依次流经一个单元的阳极室、隔层、阴极室后,再进入另一个单元的阳极室、隔层、阴极室;这样的多级处理适合处理高浓度、难处理的废水。如图3所示的二级水处理装置,在处理一种高浓度、难处理的化工废水时,氨氮去除率在85%以上,总磷去除率稳定在90%以上,COD去除率稳定在95%以上,且产电性能良好。说明该二级水处理装置能稳定有效的进行高浓度、难处理废水的净化,实现废水资源化和能源化处理。Multi-stage and multi-layer purification units are arranged in the combined device of the unit. The waste water can enter the anode of each unit at the same time, or it can flow through the anode chamber, separator and cathode chamber of one unit in sequence, and then enter the anode of another unit. chamber, partition, cathode chamber; such multi-stage treatment is suitable for the treatment of high-concentration, difficult-to-treat wastewater. The secondary water treatment device shown in Figure 3, when treating a high-concentration and difficult-to-treat chemical wastewater, the ammonia nitrogen removal rate is above 85%, the total phosphorus removal rate is stable at more than 90%, and the COD removal rate is stable at 95% % or more, and the power generation performance is good. It shows that the secondary water treatment device can stably and effectively purify high-concentration and difficult-to-treat wastewater, and realize wastewater resource and energy treatment.

Claims (10)

1.一种产电20-87W/m2的节能催化水处理装置,其特征在于,该节能催化水处理装置包括池体(1)、导线(2)、负载(3)、阴极室(4)、曝气装置(5)、出水溢流装置(6)、进水泵(7)、进水管(8)、阳极室(9)、碳棒(10)和沙粒隔层(11);1. an energy - saving catalytic water treatment device for producing electricity 20-87W/m , wherein the energy-saving catalytic water treatment device comprises a pool body (1), a wire (2), a load (3), a cathode chamber (4) ), aeration device (5), effluent overflow device (6), inlet pump (7), inlet pipe (8), anode chamber (9), carbon rod (10) and sand partition (11); 所述沙粒隔层(11)位于池体(1)中部,沙粒隔层(11)将池体(1)分为阴极室(4)和阳极室(9)两部分;所述阳极室(9)位于沙粒隔层(11)的下方,阳极电极为碳棒(10),碳棒(10)的一端连接导线;阳极室(9)用活性炭填充并负载产电微生物;所述阴极室(4)位于沙粒隔层(11)的上方,阴极电极以导电性材料为基底并负载催化剂,阴极电极的一端连接导线并接入负载(3),与阳极电极碳棒(10)一端的导线相连,从而形成外电路;所述曝气装置(5)位于阴极室(4)、池体(1)顶部的开口处,用于向阴极室(4)内补充空气或氧气,进一步促进催化降解废水中的有机物;所述出水溢流装置(6)位于阴极室(4)、池体(1)上方、低于曝气装置(5)所在的开口处;所述进水泵(7)通过进水管(8)通入至阳极室(9)、位于池体(1)的下方;废水通过进水泵(7)从进水管(8)流入阳极室(9),阳极室(9)的产电微生物分解废水中的有机物并释放电子,废水再通过沙粒隔层(11)过滤掉颗粒物及阳极微生物后向上渗入阴极室(4)中,再经曝气装置(5)进一步降解通过出水溢流装置(6)流出,从而实现废水处理及废水产电。The sand separator (11) is located in the middle of the pool body (1), and the sand separator (11) divides the pool body (1) into two parts: a cathode chamber (4) and an anode chamber (9); the anode chamber (9) is located under the sand separator (11), the anode electrode is a carbon rod (10), and one end of the carbon rod (10) is connected to a wire; the anode chamber (9) is filled with activated carbon and loaded with electricity-producing microorganisms; the cathode The chamber (4) is located above the sand grain separator (11), the cathode electrode is based on a conductive material and supports a catalyst, one end of the cathode electrode is connected to a wire and connected to the load (3), and is connected to one end of the anode electrode carbon rod (10) The wires are connected to form an external circuit; the aeration device (5) is located at the cathode chamber (4) and the opening at the top of the pool (1), and is used to supplement air or oxygen into the cathode chamber (4), further promoting The organic matter in the wastewater is catalytically degraded; the effluent overflow device (6) is located above the cathode chamber (4), the pool body (1), and is lower than the opening where the aeration device (5) is located; the inlet water pump (7) The water inlet pipe (8) leads to the anode chamber (9), which is located below the pool body (1); the waste water flows into the anode chamber (9) from the water inlet pipe (8) through the inlet water pump (7). The electricity-generating microorganisms decompose the organic matter in the wastewater and release electrons. The wastewater passes through the sand separator (11) to filter out particulate matter and anode microorganisms, and then infiltrates upwards into the cathode chamber (4), and is further degraded by the aeration device (5) to pass through the effluent. The overflow device (6) flows out, thereby realizing waste water treatment and waste water power generation. 2.根据权利要求1所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述阴极电极的基底导电性材料为碳纤维布或活性炭;阴极电极的负载催化剂为二氧化钛复合催化剂、含Fe、Mn、Zn、C、F、O元素的催化剂。 2. The energy-saving catalytic water treatment device of producing electricity 20-87W/m according to claim 1, wherein the base conductive material of the cathode electrode is carbon fiber cloth or activated carbon; the supported catalyst of the cathode electrode is titanium dioxide Composite catalyst, catalyst containing Fe, Mn, Zn, C, F, O elements. 3.根据权利要求1或2所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述阳极室(9)活性炭的填充率为40%~95%。3. The energy-saving catalytic water treatment device capable of generating 20-87W/m2 of electricity according to claim 1 or 2 , wherein the filling rate of the activated carbon in the anode chamber (9) is 40%-95%. 4.根据权利要求1或2所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述沙粒隔层(11)为石英砂、锰砂或二者的混合物。4. The energy-saving catalytic water treatment device for generating electricity 20-87W/m according to claim 1 or 2 , wherein the sand grain barrier (11) is quartz sand, manganese sand or a mixture of the two . 5.根据权利要求3所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述沙粒隔层(11)为石英砂、锰砂或二者的混合物。5. The energy-saving catalytic water treatment device for generating electricity of 20-87 W/m 2 according to claim 3, characterized in that, the sand interlayer (11) is quartz sand, manganese sand or a mixture of the two. 6.根据权利要求1、2或5任一所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述负载(3)为100~1000Ω的电阻。6 . The energy-saving catalytic water treatment device capable of generating electricity of 20-87 W/m 2 according to any one of claims 1, 2 or 5, wherein the load (3) is a resistance of 100-1000Ω. 7.根据权利要求1、2或5任一所述的产电20-87W/m2的节能催化水处理装置,其特征在于,与阳极电极碳棒(10)平行插入一个饱和甘汞电极作为参比电极,在碳棒(10)和参比电极上接入数据采集卡,实时采集阳极的电势数据;在阴极电极的导线上接入数据采集卡,实时采集电池的电势数据。7. The energy-saving catalytic water treatment device of generating electricity 20-87W/m according to any one of claims 1, 2 or 5, wherein a saturated calomel electrode is inserted in parallel with the anode electrode carbon rod (10) as a For the reference electrode, a data acquisition card is connected to the carbon rod (10) and the reference electrode to collect the potential data of the anode in real time; the data acquisition card is connected to the wire of the cathode electrode to collect the potential data of the battery in real time. 8.根据权利要求6所述的产电20-87W/m2的节能催化水处理装置,其特征在于,与阳极电极碳棒(10)平行插入一个饱和甘汞电极作为参比电极,在碳棒(10)和参比电极上接入数据采集卡,实时采集阳极的电势数据;在阴极电极的导线上接入数据采集卡,实时采集电池的电势数据。8. The energy - saving catalytic water treatment device of generating electricity 20-87W/m according to claim 6, wherein a saturated calomel electrode is inserted in parallel with the anode electrode carbon rod (10) as a reference electrode, and the carbon A data acquisition card is connected to the rod (10) and the reference electrode to collect the potential data of the anode in real time; the data acquisition card is connected to the wire of the cathode electrode to collect the potential data of the battery in real time. 9.根据权利要求1、2、5或8任一所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述池体(1)的形状为横管形、柱形、方形或多层组合结构。9. The energy-saving catalytic water treatment device for generating electricity 20-87W/m according to any one of claims 1, 2 , 5 or 8, wherein the pond body (1) is in the shape of a horizontal tube, Column, square or multi-layer composite structure. 10.根据权利要求7所述的产电20-87W/m2的节能催化水处理装置,其特征在于,所述池体(1)的形状为横管形、柱形、方形或多层组合结构。10. The energy - saving catalytic water treatment device for generating electricity of 20-87W/m according to claim 7, wherein the shape of the pool body (1) is a horizontal tube, a column, a square or a multi-layer combination structure.
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