CN203768095U - Device for in-situ remediation of polluted groundwater by using microbial electrolysis cell process - Google Patents
Device for in-situ remediation of polluted groundwater by using microbial electrolysis cell process Download PDFInfo
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Abstract
Description
技术领域 technical field
本实用新型属于地下水处理技术领域,具体涉及利用微生物电解池技术原位修复受污染地下水并同时获得氢能或回收金属的装置。 The utility model belongs to the technical field of groundwater treatment, in particular to a device for in-situ repairing of polluted groundwater using microbial electrolytic cell technology and simultaneously obtaining hydrogen energy or recovering metals.
背景技术 Background technique
地下水作为人类宝贵的淡水资源,随着现代社会工业化进程的不断发展,出现了不同程度的污染问题。从上个世纪60年代开始,地下水污染逐渐加剧,于是地下水的修复技术也随之发展起来。地下水污染修复技术包括异位修复、原位修复和监测自然衰减技术。异位修复技术是将受污染的地下水抽出至地表再进行处理的技术。该技术在短期内处理量大、处理效率较高,但长期应用普遍存在着拖尾、反弹等现象,最终降低了处理效率,增加处理成本。监测自然衰减技术是充分依靠自然净化能力的修复技术,需要的修复时间很长。加之地下水中污染物的种类日益增多,除有机物外,还包括重金属、无机盐和放射性元素等,于是地下水污染原位修复技术便以其修复彻底、处理污染物的种类多、时间相对较短、成本相对低廉等优势在地下水污染修复领域崭露头角。其中原位生物修复技术是指在基本不破坏土体和地下水自然环境条件下,对受污染的对象不做搬运或运输,而是在原场所里,通过生物(特别是微生物)的作用去除地下水中污染物的方法。原位生物修复技术具有速度快、干扰小、效率高、成本低及反应条件温和等显著优点,已成为地下水污染原位修复的重要技术。但原位生物修复技术也存在着一些局限。例如,受污染地下水能够被微生物原位修复的关键是保持相应微生物的高活性,才能使得地下水的污染物能够被高效的去除。 As a precious fresh water resource for human beings, groundwater has been polluted to varying degrees with the continuous development of industrialization in modern society. Since the 1960s, groundwater pollution has gradually increased, so groundwater restoration technology has also been developed. Groundwater pollution remediation technologies include ex-situ remediation, in-situ remediation and monitoring natural attenuation technologies. Ex-situ remediation technology is a technology that pumps contaminated groundwater to the surface for treatment. This technology has a large processing capacity and high processing efficiency in a short period of time, but long-term application generally has phenomena such as tailing and rebound, which ultimately reduces processing efficiency and increases processing costs. Monitoring natural attenuation technology is a restoration technology that fully relies on natural purification capabilities, and requires a long restoration time. In addition, the types of pollutants in groundwater are increasing day by day. In addition to organic matter, they also include heavy metals, inorganic salts and radioactive elements. Therefore, the in-situ remediation technology for groundwater pollution is characterized by thorough restoration, many types of pollutants, and relatively short time. Advantages such as relatively low cost have emerged in the field of groundwater pollution remediation. Among them, the in-situ bioremediation technology refers to the removal of groundwater through the action of organisms (especially microorganisms) in the original place without carrying or transporting the contaminated objects under the condition of basically not destroying the natural environment of the soil and groundwater. method of contamination. The in-situ bioremediation technology has significant advantages such as fast speed, less interference, high efficiency, low cost and mild reaction conditions, and has become an important technology for in-situ remediation of groundwater pollution. However, in situ bioremediation technology also has some limitations. For example, the key to in-situ remediation of contaminated groundwater by microorganisms is to maintain the high activity of corresponding microorganisms, so that the pollutants in groundwater can be efficiently removed.
近年来,微生物燃料电池(Microbial Fuel Cell,MFC)技术正成为新概念废水处理技术之一,其在对废水处理的同时可以获得电能。MFC技术以被用于原位修复受污染地下水(CN 102659237 A)。该方法利用阳极室的微生物将地下水中的还原性污染分解代谢去除,并利用阴极室将地下水中的氧化性污染物还原去除,同时获得电能。此外,该方法将阴极电极置于与大气相通的阴极室中,以克服向地下水中添加电子受体的实施难度,但是该方法中电子受体(空气中的氧气)是通过扩散的方式进入阴极室,电子受体供应速度慢,且该电子受体在水中的溶解度低,同时在阴极电极表面易形成生物膜,从而降低了阴极反应效率,进而降低了污染物的去除效率。此外,该方法无法对还原电位较低的Pb2+、Ni2+、氯代烃及五价铀(U(V))等污染物进行去除。 In recent years, microbial fuel cell (Microbial Fuel Cell, MFC) technology is becoming one of the new concept wastewater treatment technologies, which can obtain electricity while treating wastewater. MFC technology has been used to remediate contaminated groundwater in situ (CN 102659237 A). The method utilizes the microorganisms in the anode chamber to catabolize and remove the reductive pollution in the groundwater, and uses the cathode chamber to reduce and remove the oxidative pollutants in the groundwater, and simultaneously obtains electric energy. In addition, this method places the cathode electrode in the cathode chamber open to the atmosphere to overcome the implementation difficulty of adding electron acceptors to groundwater, but in this method the electron acceptor (oxygen in the air) enters the cathode by diffusion The supply speed of the electron acceptor is slow, and the solubility of the electron acceptor in water is low. At the same time, biofilm is easy to form on the surface of the cathode electrode, which reduces the efficiency of the cathode reaction and the removal efficiency of pollutants. In addition, this method cannot remove pollutants such as Pb 2+ , Ni 2+ , chlorinated hydrocarbons and pentavalent uranium (U(V)) with low reduction potential.
微生物电解池(Microbial Electrolysis Cell,MEC)是近年迅速发展起来的一种融合了污水处理和产生能源的新技术,可以在对污水进行生物处理的同时获得不同形式的能源,作为污水处理的新工艺,引起了国内外的广泛关注。在MEC中无需提供电子受体(O2),从而可以避免MFC原位修复地下水污染物需向地下水中添加电子受体的问题。此外,在MFC中无法去除的一些还原电位较低的Pb2+、Ni2+、氯代烃及U(V)等污染物,可以在MEC的阴极被去除。 Microbial Electrolysis Cell (MEC) is a new technology developed rapidly in recent years that combines sewage treatment and energy generation. It can obtain different forms of energy while biologically treating sewage, and is used as a new process for sewage treatment. , has aroused widespread attention at home and abroad. There is no need to provide electron acceptors (O 2 ) in MEC, which can avoid the problem that MFC needs to add electron acceptors to groundwater for in-situ remediation of groundwater pollutants. In addition, some pollutants such as Pb 2+ , Ni 2+ , chlorinated hydrocarbons and U(V) with low reduction potential that cannot be removed in MFC can be removed in the cathode of MEC.
发明内容 Contents of the invention
本实用新型提供一种利用微生物电解池技术原位修复受污染地下水的装置,以避免传统原位修复受污染地下水及利用微生物燃料电池技术原位修复受污染地下水需向地下水中添加电子受体的问题,同时可以去除利用微生物燃料电池技术原位修复受污染地下水方法中无法去除的一些还原电位较低的Pb2+、Ni2+、氯代烃及U(V)等污染物。 The utility model provides a device for in-situ repairing of polluted groundwater using microbial electrolytic cell technology, so as to avoid the traditional in-situ repairing of polluted groundwater and the use of microbial fuel cell technology for in-situ repairing of polluted groundwater requiring adding electron acceptors to the groundwater At the same time, it can remove some pollutants such as Pb 2+ , Ni 2+ , chlorinated hydrocarbons and U(V) with low reduction potential that cannot be removed in the method of in-situ remediation of contaminated groundwater using microbial fuel cell technology.
为解决上述问题,本实用新型采用如下技术方案: In order to solve the above problems, the utility model adopts the following technical solutions:
本实用新型利用微生物电解池技术原位修复受污染地下水的装置,其特征在于:在受污染地下水中设置密封的阳极室和密封的阴极室,阳极室和阴极室的室壁均开有小孔;阳极室和阴极室内分别放置阳极电极和阴极电极;将稳压电源的高电位端和低电位端分别连接阳极电极和阴极电极;使受污染地下水通过阳极室和阴极室室壁的小孔流经阳极室和阴极室内的阳极电极和阴极电极,污水中的还原性有机污染物作为附着在阳极电极表面的产电微生物的代谢底物而被降解去除,同时在电辅助下,阳极电极表面产电微生物代谢有机污染物产生的H+和电子迁移到阴极室,并在阴极电极表面结合产生H2。此外,地下水中的氧化还原电位较低的一些氧化性污染物在阴极电极表面被还原而去除。 The utility model utilizes microbial electrolytic cell technology to restore polluted groundwater in situ, and is characterized in that a sealed anode chamber and a sealed cathode chamber are arranged in the polluted groundwater, and the chamber walls of the anode chamber and the cathode chamber are all provided with small holes ; Place the anode electrode and the cathode electrode in the anode chamber and the cathode chamber respectively; connect the high potential end and the low potential end of the regulated power supply to the anode electrode and the cathode electrode respectively; make the polluted groundwater flow through the small holes in the walls of the anode chamber and the cathode chamber Through the anode electrode and cathode electrode in the anode chamber and cathode chamber, the reducing organic pollutants in the sewage are degraded and removed as the metabolic substrate of the electrogenic microorganisms attached to the surface of the anode electrode. The H + and electrons generated by the electro-microbial metabolism of organic pollutants migrate to the cathode chamber and combine on the surface of the cathode electrode to produce H 2 . In addition, some oxidative pollutants with low redox potential in groundwater are reduced and removed on the surface of the cathode electrode.
所述阳极电极材料为碳布、石墨毡、网状玻璃碳、石墨或碳纤维刷。 The anode electrode material is carbon cloth, graphite felt, mesh glassy carbon, graphite or carbon fiber brush.
所述阴极电极材料为Pt修饰的碳布、石墨毡、石墨或碳纤维刷,或者是铅和铜。 The cathode electrode material is Pt modified carbon cloth, graphite felt, graphite or carbon fiber brush, or lead and copper.
所述的阳极电极表面产电微生物的富集是通过向已建好的阳极室注入厌氧活性污泥和去除氧气培养基混合物,通过一段时间的运行微生物电解池产生的电流最大、且稳定,为阳极电极表面充分附着了产电微生物。 The enrichment of the electricity-producing microorganisms on the surface of the anode electrode is by injecting the anaerobic activated sludge and the oxygen-removing culture medium mixture into the built anode chamber, and the current generated by the microbial electrolytic cell through a period of operation is maximum and stable, Electrode-producing microorganisms are fully attached to the surface of the anode electrode.
所述的阴极电极的电位控制为-0.5V~-2.0 V,所述的稳压电源的直流输出电压为-2.0V~2.0V。 The potential of the cathode electrode is controlled to be -0.5V~-2.0V, and the DC output voltage of the stabilized power supply is -2.0V~2.0V.
可采用本实用新型装置原位修复的污染物包括在阳极室中的还原性污染物苯酚所述的和/或苯,在阴极室中的氧化还原电位较低的氧化性污染物硝基苯类化合物污染和/或氯代烃污染和/或U(V)污染和/或Pb2+污染和/或Ni2+污染和/或低浓度Cu2+污染。 The pollutants that can be repaired in situ by the device of the utility model include reducing pollutants such as phenol and/or benzene in the anode chamber, and oxidative pollutants such as nitrobenzenes that have a lower redox potential in the cathode chamber Compound pollution and/or chlorinated hydrocarbon pollution and/or U(V) pollution and/or Pb 2+ pollution and/or Ni 2+ pollution and/or low concentration Cu 2+ pollution.
对于修复还原性污染物苯酚和/或苯污染的地下水,使受污染地下水先流经阳极室;对于修复氧化性污染物硝基苯类化合物和/或氯代烃和/或U(V)和/或Pb2+和/或Ni2+和/或低浓度Cu2+污染的地下水,使受污染地下水先流经阴极室;对于被还原性污染物和氧化性污染物同时污染的地下水,将阳极室和阴极室同时设置在垂直于受污染地下水流向的同一截面上,并使污染的地下水首先流经阴极室,然后再流经阳极室。 For remediation of groundwater polluted by reducing pollutants phenol and/or benzene, the contaminated groundwater first flows through the anode chamber; for remediation of oxidative pollutants nitrobenzene compounds and/or chlorinated hydrocarbons and/or U(V) and /or Pb 2+ and/or Ni 2+ and/or low-concentration Cu 2+ polluted groundwater, make the polluted groundwater flow through the cathode chamber first; for the groundwater polluted by reducing pollutants and oxidizing pollutants simultaneously, the The anode chamber and the cathode chamber are arranged on the same section perpendicular to the flow direction of the polluted groundwater, and the polluted groundwater first flows through the cathode chamber, and then flows through the anode chamber.
附图说明 Description of drawings
图1为本实用新型实施例1的微生物电解池阳极去除还原性污染物的结构示意图。 Fig. 1 is a schematic diagram of the structure of the anode of the microbial electrolytic cell in Example 1 of the present invention for removing reducing pollutants.
图2为本实用新型实施例2的微生物电解池阴极去除氧化还原电位较低的CHCl3氧化性污染物的结构示意图。 Fig. 2 is the structural representation of removing CHCl 3 oxidative pollutants with a lower redox potential by the cathode of the microbial electrolytic cell in Example 2 of the utility model.
具体实施方式 Detailed ways
以下通过具体实施例,结合附图对本实用新型做进一步详细说明。 The utility model will be described in further detail below through specific embodiments in conjunction with the accompanying drawings.
实施例1:Example 1:
图1为本实用新型实施例1的微生物电解池阳极去除还原性污染物的结构示意图。本实施例是利用微生物电解池技术原位修复受苯酚污染地下水,具体按以下顺序和步骤进行操作: Fig. 1 is a schematic diagram of the structure of the anode of the microbial electrolytic cell in Example 1 of the present invention for removing reducing pollutants. In this embodiment, the microbial electrolytic cell technology is used to restore the groundwater polluted by phenol in situ, and the specific operations are carried out in the following order and steps:
(1)在受污染地下水区域的地面下原位构建微生物电解池 (1) In-situ construction of microbial electrolysis cells under the ground in contaminated groundwater areas
首先在受污染地下水区域的地面钻两个相距一定距离的圆柱形的洞,将底端密封、管壁开孔的两根聚氯乙烯管分别放入到圆柱形洞中构成阳极室1和阴极室6;将碳纤维刷阳极电极2放入到聚氯乙烯管构成的阳极室1中,阳极电极2通过密封盖3上的孔、经导线4与稳压电源5的高电位相连;将碳纤维刷阴极电极7放入到聚氯乙烯管构成的阴极室6中,阴极电极7通过密封盖8上的孔、经导线9与稳压电源5的低电位相连;在阳极室2的上端设计有进样管10,在阴极室6的上端设计有气体收集管11。 Firstly, two cylindrical holes with a certain distance are drilled on the ground of the polluted groundwater area, and two polyvinyl chloride pipes with sealed bottoms and perforated pipe walls are respectively put into the cylindrical holes to form the anode chamber 1 and the cathode Chamber 6; put the carbon fiber brush anode electrode 2 into the anode chamber 1 formed by the polyvinyl chloride tube, and the anode electrode 2 is connected to the high potential of the stabilized power supply 5 through the hole on the sealing cover 3; the carbon fiber brush Cathode electrode 7 is put into the cathode chamber 6 that polyvinyl chloride tube constitutes, and cathode electrode 7 is connected with the low potential of stabilized voltage power supply 5 through the hole on sealing cover 8; The sample tube 10 is provided with a gas collection tube 11 at the upper end of the cathode chamber 6 .
(2)阳极电极表面产电微生物的富集 (2) Enrichment of electrogenic microorganisms on the surface of the anode electrode
以污水处理厂的厌氧活性污泥为接种物,人工配制的模拟废水为培养基,纯氮气除氧气后按2:9(v/v)的比例通过进样管10接种到微生物电解池的阳极室1富集阳极产电微生物。微生物电解池为批次操作,每次实验结束后按上述比例加入接种物与培养基的混合液。稳压电源的电压固定为-0.9V,定期对微生物电解池的电流数据进行采样,待微生物电解池的电流最大且稳定后,认为在阳极电极1的表面充分附着了产电微生物。 The anaerobic activated sludge from the sewage treatment plant is used as the inoculum, the artificially prepared simulated wastewater is used as the culture medium, and the pure nitrogen is inoculated into the microbial electrolysis cell through the sampling tube 10 at a ratio of 2:9 (v/v) after deoxygenation. The anode compartment 1 is enriched with anode electrogenic microorganisms. The microbial electrolysis cell is operated in batches, and the mixture of inoculum and medium is added according to the above ratio after each experiment. The voltage of the stabilized power supply is fixed at -0.9V, and the current data of the microbial electrolytic cell is regularly sampled. After the current of the microbial electrolytic cell is maximum and stable, it is considered that the surface of the anode electrode 1 is fully adhered to the electrogenic microorganisms.
表1 模拟人工废水基液组成及含量 Table 1 Composition and content of simulated artificial wastewater base fluid
表2 微量元素溶液组成及含量 Table 2 Composition and content of trace element solution
(3)苯酚污染地下水的原位修复 (3) In-situ remediation of phenol-contaminated groundwater
待阳极电极2的表面充分富集了产电微生物,此时微生物电解池可用于原位修复苯酚污染的地下水。让苯酚污染的地下水依次流经微生物电解池的阳极室1和阴极室6,同时稳压电源5的电压固定为-0.9 V。阳极电极2表面附着的产电微生物代谢地下水中污染物苯酚产生CO2、H+及电子,从而去除污染物,产生的H+和电子迁移到阴极室6,在电辅助下H+和电子在阴极电极7表面结合生成H2,具体化学反应方程式如下: When the surface of the anode electrode 2 is fully enriched with electricity-producing microorganisms, the microbial electrolytic cell can be used for in-situ remediation of phenol-contaminated groundwater. Let the phenol-contaminated groundwater flow through the anode chamber 1 and cathode chamber 6 of the microbial electrolysis cell in sequence, while the voltage of the stabilized power supply 5 is fixed at -0.9 V. The electrogenic microorganisms attached to the surface of the anode electrode 2 metabolize the pollutant phenol in the groundwater to produce CO 2 , H + and electrons, thereby removing the pollutants, and the generated H + and electrons migrate to the cathode chamber 6, where the H + and electrons are assisted by electricity. The surface of the cathode electrode 7 combines to generate H 2 , and the specific chemical reaction equation is as follows:
阳极电极 Anode electrode
阴极电极 cathode electrode
而所产生的H2经气体收集管11收集。 And the produced H 2 is collected through the gas collection pipe 11.
实施例2:Example 2:
图2为本实用新型实施例2的微生物电解池阴极去除氧化还原电位较低的三氯甲烷污染物的结构示意图。本实施例是利用微生物电解池技术原位修复受三氯甲烷污染的地下水,具体按以下顺序和步骤进行操作: Fig. 2 is a structural schematic diagram of removing chloroform pollutants with low redox potential by the cathode of the microbial electrolytic cell in Example 2 of the present invention. The present embodiment utilizes microbial electrolytic cell technology to in situ remediate groundwater polluted by chloroform, and specifically operates in the following order and steps:
(1)在受污染地下水区域的地面下原位构建微生物电解池 (1) In-situ construction of microbial electrolysis cells under the ground in contaminated groundwater areas
首先在受污染地下水区域的地面钻两个相距一定距离的圆柱形的洞,将底端密封、管壁开孔的两根聚氯乙烯管分别放入到圆柱形洞中构成阳极室1和阴极室6;将碳纤维刷阳极电极2放入到聚氯乙烯管构成的阳极室1中,阳极电极2通过密封盖3上的孔、经导线4与稳压电源5的高电位相连;将铜阴极电极7放入到聚氯乙烯管构成的阴极室6中,阴极电极7通过密封盖8上的孔、经导线9与稳压电源5的低电位相连;在阳极室2的上端设计有进样管10,在阴极室6的上端设计有气体收集管11。 Firstly, two cylindrical holes with a certain distance are drilled on the ground of the polluted groundwater area, and two polyvinyl chloride pipes with sealed bottoms and perforated pipe walls are respectively put into the cylindrical holes to form the anode chamber 1 and the cathode Chamber 6; put the carbon fiber brush anode electrode 2 into the anode chamber 1 formed by the polyvinyl chloride tube, the anode electrode 2 is connected to the high potential of the stabilized voltage power supply 5 through the hole on the sealing cover 3; the copper cathode The electrode 7 is put into the cathode chamber 6 formed by the polyvinyl chloride tube, and the cathode electrode 7 is connected to the low potential of the stabilized power supply 5 through the hole on the sealing cover 8 and the lead wire 9; The tube 10 is designed with a gas collection tube 11 at the upper end of the cathode chamber 6 .
(2)阳极电极表面产电微生物的富集 (2) Enrichment of electrogenic microorganisms on the surface of the anode electrode
阳极电极表面产电微生物的富集同实例1中的阳极电极表面产电微生物的富集。 The enrichment of electrogenic microorganisms on the surface of the anode electrode is the same as the enrichment of electrogenic microorganisms on the surface of the anode electrode in Example 1.
(3)三氯甲烷污染地下水的原位修复 (3) In-situ remediation of chloroform-contaminated groundwater
待阳极电极2的表面充分富集了产电微生物,此时微生物电解池可用于原位修复三氯甲烷污染的地下水。通过进样管10向阳极室1中连续或间断添加人工模拟废水以提供电子供体。让三氯甲烷污染的地下水依次流经微生物电解池的阴极室6和阳极室1,同时稳压电源5的电压固定为-0.9 V。阳极电极2表面附着的产电微生物代谢人工模拟废水中的有机物产生CO2、H+及电子,产生的H+和电子迁移到阴极室6,在电辅助下三氯甲烷、H+和电子在阴极电极7表面发生反应,具体化学反应方程式如下: After the surface of the anode electrode 2 is fully enriched with electricity-producing microorganisms, the microbial electrolytic cell can be used for in-situ remediation of chloroform-contaminated groundwater. Artificial simulated waste water is continuously or intermittently added into the anode chamber 1 through the sampling tube 10 to provide electron donors. Let the chloroform-contaminated groundwater flow through the cathode chamber 6 and the anode chamber 1 of the microbial electrolysis cell in sequence, while the voltage of the stabilized power supply 5 is fixed at -0.9 V. The electrogenic microorganisms attached to the surface of the anode electrode 2 metabolize the organic matter in artificially simulated wastewater to generate CO 2 , H + and electrons, and the generated H + and electrons migrate to the cathode chamber 6, and chloroform, H + and electrons are in the A reaction occurs on the surface of the cathode electrode 7, and the specific chemical reaction equation is as follows:
阳极电极 Anode electrode
阴极电极 cathode electrode
最后应说明的是:显然,上述实施例仅仅是为清楚地说明本实用新型所作的举例,而并非对实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引申出的显而易见的变化或变动仍处于本实用新型的保护范围之中。 Finally, it should be noted that obviously, the above-mentioned embodiments are only examples for clearly illustrating the utility model, rather than limiting the implementation manner. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. And the obvious changes or changes derived therefrom are still within the protection scope of the present utility model.
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