CN115636526A - A Method for the Transfer and Transformation of Organic Pollutants Based on Fe Redox Enhancement - Google Patents

A Method for the Transfer and Transformation of Organic Pollutants Based on Fe Redox Enhancement Download PDF

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CN115636526A
CN115636526A CN202211190296.9A CN202211190296A CN115636526A CN 115636526 A CN115636526 A CN 115636526A CN 202211190296 A CN202211190296 A CN 202211190296A CN 115636526 A CN115636526 A CN 115636526A
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organic pollutants
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migration
iron
redox
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卞永荣
王紫泉
王芳
相雷雷
刘雨
赵之良
杨兴伦
谷成刚
宋洋
蒋新
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Institute of Soil Science of CAS
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Abstract

The invention discloses a method for migration and conversion of organic pollutants based on Fe redox enhancement, and belongs to the field of environmental pollution monitoring and restoration. The method comprises the steps of adding microorganisms and a carbon source into a medium containing organic pollutants and iron, and sequentially carrying out anaerobic culture and aerobic culture; the microorganism comprises Shewanella Oneidensis MR-1 Shewanella, is purchased from China center for type culture Collection, and has a collection number of CCTCC AB 2013238; the method provided by the invention regulates and controls the Fe redox process by Fe and microorganisms and providing microorganism growth conditions, so as to strengthen the migration and transformation processes of organic pollutants, and has great application potential in the fields of regulating and controlling the migration and transformation of organic pollutants in medium environments such as field soil, water and the like and controlling the diffusion of organic pollutants.

Description

一种基于Fe氧化还原强化的有机污染物迁移转化的方法A method for the migration and transformation of organic pollutants based on Fe redox enhancement

技术领域technical field

本发明涉及一种基于Fe氧化还原强化的有机污染物迁移转化的方法,属于环境污染迁移转化领域,主要用于土壤-水等多介质环境有机污染物的监测和修复。The invention relates to a method for the migration and transformation of organic pollutants based on Fe redox enhancement, which belongs to the field of environmental pollution migration and transformation, and is mainly used for monitoring and repairing organic pollutants in multi-media environments such as soil-water.

背景技术Background technique

持久性有机污染物如多环芳烃(Polycyclic aromatic hydrocarbons,PAHs)、石油烃等是土壤、沉积物、水等环境中广泛检出的污染物,主要来源于人类生产活动,包括石油化工生产、化石燃料不完全燃烧等产生的废弃物排放。环境中的持久性有机污染物具有致癌、致畸和诱变等作用,对人类健康构成潜在威胁。持久性有机污染物的迁移转化及污染监测是关系人体健康和生态系统可持续发展的重要环境问题。Persistent organic pollutants such as polycyclic aromatic hydrocarbons (PAHs) and petroleum hydrocarbons are widely detected pollutants in soil, sediment, water and other environments, mainly from human production activities, including petrochemical production, fossil Waste emissions from incomplete combustion of fuel, etc. Persistent organic pollutants in the environment have carcinogenic, teratogenic and mutagenic effects, posing a potential threat to human health. The migration and transformation of persistent organic pollutants and pollution monitoring are important environmental issues related to human health and sustainable development of ecosystems.

持久性有机污染物的迁移和转化涉及物理、化学和微生物过程,但单一的物理处理迁移转化效率低、化学氧化成本高以及微生物转化降解活性低等特点。The migration and transformation of persistent organic pollutants involves physical, chemical and microbial processes, but the single physical treatment has the characteristics of low migration and transformation efficiency, high cost of chemical oxidation, and low microbial transformation and degradation activity.

中国专利申请公开号为CN112872012A的现有技术公开了一种电化学强化过硫酸盐氧化协同去除土壤石油烃的方法。该方法在电场作用下以阴极传输方式向污染土壤注入表面活性剂,待土壤中污染物迁移富集于高级氧化填料区时,将惰性阳极取出,原位插入Fe阳极,同时根据土壤中污染物迁移情况从惰性阴极向阳极移动,而后再通电继续进行氧化降解,直至污染物降解达到要求值。该发明具有普适性,对各种类型的有机污染土壤及场地均适用,对低渗透性和贫瘠的土壤同样适用。但该方法采用电驱动方式强化污染物迁移以及化学氧化转化降解的方法,成本高、耗能高,难以适用于直接针对大面积受污染的土体的原位处理。The prior art of Chinese Patent Application Publication No. CN112872012A discloses a method for synergistically removing soil petroleum hydrocarbons through electrochemically enhanced persulfate oxidation. In this method, under the action of an electric field, the surfactant is injected into the polluted soil in the form of cathodic transport. When the pollutants in the soil are migrated and enriched in the advanced oxidation filler area, the inert anode is taken out and the Fe anode is inserted in situ. The migration situation moves from the inert cathode to the anode, and then the oxidative degradation continues until the pollutant degradation reaches the required value. The invention has universal applicability, is applicable to various types of organic polluted soils and sites, and is also applicable to low-permeability and barren soils. However, this method uses electric drive to enhance the migration of pollutants and chemical oxidation conversion and degradation, which is costly and energy-consuming, and is difficult to apply directly to in-situ treatment of large areas of polluted soil.

发明内容Contents of the invention

1.要解决的问题1. The problem to be solved

针对现有技术中存在的有机污染物迁移转化效率低、成本高、耗能大等缺点,本发明提供一种基于Fe氧化还原强化的有机污染物迁移转化的方法,通过利用微生物调控Fe的氧化还原态,使有机污染物溶出和迁移能力增加,进一步被微生物好氧培养中生成的活性氧过氧化氢H2O2和羟基自由基·OH氧化降解,从而实现有机污染物的强化迁移和转化。Aiming at the disadvantages of low migration and conversion efficiency of organic pollutants, high cost, and high energy consumption in the prior art, the present invention provides a method for the migration and conversion of organic pollutants based on Fe redox enhancement, by using microorganisms to regulate the oxidation of Fe Reduced state, which increases the dissolution and migration ability of organic pollutants, and is further oxidized and degraded by the active oxygen hydrogen peroxide H 2 O 2 and hydroxyl radical OH generated in the aerobic culture of microorganisms, thereby realizing the enhanced migration and transformation of organic pollutants .

2.技术方案2. Technical solution

一种基于Fe氧化还原强化的有机污染物迁移转化的方法,在包含有机污染物和铁的介质中加入微生物和碳源,依次进行厌氧培养、好氧培养的步骤;所述微生物包括Shewanella Oneidensis MR-1希瓦氏菌属,购于中国典型培养物保藏中心,保藏号CCTCCAB 2013238;所述包含有机污染物和铁的介质包括向含有有机污染物的介质中加入铁或含铁介质形成的介质,或向含铁介质中加入有机污染物形成的介质,或被有机污染物污染的含铁介质。所述Shewanella Oneidensis MR-1希瓦氏菌属为希瓦氏菌属兼性厌氧菌,能够厌氧还原Fe(III)为Fe(II)。A method for the migration and conversion of organic pollutants based on Fe redox enhancement, adding microorganisms and carbon sources to a medium containing organic pollutants and iron, and performing the steps of anaerobic cultivation and aerobic cultivation in sequence; the microorganisms include Shewanella Oneidensis MR-1 Shewanella genus, purchased from China Center for Type Culture Collection, preservation number CCTCCAB 2013238; the medium containing organic pollutants and iron includes adding iron or iron-containing medium to the medium containing organic pollutants. medium, or the medium formed by adding organic pollutants to the ferrous medium, or the ferrous medium polluted by organic pollutants. The Shewanella Oneidensis MR-1 is a facultative anaerobic bacterium of the genus Shewanella, which can anaerobically reduce Fe(III) to Fe(II).

优选地,所述含铁介质包括含铁土壤,自然形成或人工合成的含铁矿物,或者人工外源添加含铁化合物组成的混合体系中的一种或几种。其中,含铁矿物可以为针铁矿(铁含量一般为30-63%)、赤铁矿、纤铁矿、水铁矿、磁铁矿等。Preferably, the iron-containing medium includes one or more of iron-containing soil, naturally occurring or artificially synthesized iron-containing minerals, or a mixed system composed of artificially added iron-containing compounds. Among them, the iron-containing minerals may be goethite (generally 30-63% iron content), hematite, lepidocerite, ferrihydrite, magnetite and the like.

优选地,所述有机污染物包括多环芳烃、氯代烃、石油烃、苯系物等中的一种或多种。其中,多环芳烃包括菲、芘。Preferably, the organic pollutants include one or more of polycyclic aromatic hydrocarbons, chlorinated hydrocarbons, petroleum hydrocarbons, benzene series and the like. Among them, polycyclic aromatic hydrocarbons include phenanthrene and pyrene.

优选地,包括以下步骤:Preferably, the following steps are included:

S1采用灭菌营养肉汤培养基培养扩繁所述Shewanella Oneidensis MR-1希瓦氏菌属,随后调节细菌数量或细菌密度达到特定值;S1 uses sterilized nutrient broth medium to cultivate and multiply the Shewanella Oneidensis MR-1 Shewanella genus, and then adjust the number of bacteria or the density of bacteria to reach a specific value;

S2向含有有机污染物的介质中加入含铁化合物后,加入至灭菌无机盐培养基,随后接种步骤S1所述Shewanella Oneidensis MR-1希瓦氏菌属和碳源;或S2 adds iron-containing compounds to the medium containing organic pollutants, and then adds to the sterilized inorganic salt medium, followed by inoculating the Shewanella Oneidensis MR-1 Shewanella genus and carbon source described in step S1; or

向含铁介质中加入灭菌无机盐培养基,随后接种所述步骤S1中ShewanellaOneidensis MR-1希瓦氏菌属和碳源,之后加入有机污染物混合;或Adding a sterilized inorganic salt medium to the iron-containing medium, followed by inoculating the ShewanellaOneidensis MR-1 Shewanella genus and carbon source in the step S1, and then adding organic pollutants to mix; or

向被有机污染物污染的含铁介质中加入灭菌无机盐培养基,随后接种步骤S1所述Shewanella Oneidensis MR-1希瓦氏菌属和碳源;Adding sterilized inorganic salt medium to the iron-containing medium contaminated by organic pollutants, followed by inoculation of Shewanella Oneidensis MR-1 Shewanella genus and carbon source described in step S1;

S3厌氧培养:将所述步骤S2得到的混合体系通氮气去除氧气,密封后在厌氧条件下培养;在厌氧培养过程中,Shewanella Oneidensis MR-1希瓦氏菌属将铁还原;S3 anaerobic culture: the mixed system obtained in the step S2 is ventilated with nitrogen to remove oxygen, sealed and cultured under anaerobic conditions; during the anaerobic culture process, Shewanella Oneidensis MR-1 reduces iron;

S4好氧培养:所述步骤S3厌氧培养结束后,反应体系转为震荡的好氧条件下培养;在好氧培养过程中,Shewanella Oneidensis MR-1希瓦氏菌属产生H2O2,进一步生成·OH;·OH攻击介质表面吸附或溶解态有机污染物从而强化有机污染物降解转化;S4 aerobic culture: after the anaerobic culture in step S3, the reaction system is transformed into aerobic culture with shaking; during the aerobic culture, Shewanella Oneidensis MR-1 produces H 2 O 2 , Further generate OH; OH attacks the surface of the medium to adsorb or dissolve organic pollutants to strengthen the degradation and transformation of organic pollutants;

S5依次重复上述S3和S4厌氧培养和好氧培养步骤,循环培养;至体系中有机污染物转化降解完全;S5 repeats the steps of anaerobic culture and aerobic culture of S3 and S4 in sequence, and circulates the culture; until the conversion and degradation of organic pollutants in the system is complete;

S6厌氧培养和好氧培养过程中补充碳源。碳源根据消耗情况适当补充。S6 supplemented carbon source during anaerobic culture and aerobic culture. The carbon source is properly supplemented according to the consumption situation.

本发明方法通过Shewanella Oneidensis MR-1希瓦氏菌属在厌氧/好氧呼吸过程中调控含Fe介质还原与氧化,生成Fe(II)和过氧化氢H2O2,一方面含铁介质的还原溶解改变了介质状态,使吸附固定在介质表面或内部的有机污染物释放进入周围环境中,从而导致有机污染物的迁移活性增强;另一方面含Fe介质还原与氧化过程中生成的Fe(II)和过氧化氢H2O2能进一步发生反应生成羟基自由基·OH,·OH攻击介质表面吸附或溶解态有机污染物从而强化有机污染物降解转化。The method of the present invention uses Shewanella Oneidensis MR-1 to regulate the reduction and oxidation of the Fe-containing medium during the anaerobic/aerobic respiration process to generate Fe(II) and hydrogen peroxide H 2 O 2 . On the one hand, the iron-containing medium The reduction and dissolution of the medium changes the state of the medium, releasing the organic pollutants adsorbed and fixed on the surface or inside of the medium into the surrounding environment, which leads to the enhancement of the migration activity of the organic pollutants; on the other hand, the Fe generated during the reduction and oxidation of the Fe-containing medium (II) and hydrogen peroxide H 2 O 2 can further react to generate hydroxyl radical · OH, · OH attacks the surface of the medium to adsorb or dissolve organic pollutants, thereby strengthening the degradation and conversion of organic pollutants.

优选地,所述Shewanella Oneidensis MR-1希瓦氏菌属扩繁条件包括:好氧培养,在灭菌营养肉汤培养基中接种适量菌液,在30℃和160rpm避光条件下培养过夜;用灭菌pH7.0 0.1M磷酸盐缓冲液清洗两次,调整菌密度为OD600=1.20。Preferably, the propagation conditions of the Shewanella Oneidensis MR-1 genus include: aerobic culture, inoculating an appropriate amount of bacterial liquid in a sterilized nutrient broth medium, and cultivating overnight at 30°C and 160rpm in the dark; Wash twice with sterile pH 7.0 0.1M phosphate buffer, and adjust the bacterial density to OD 600 =1.20.

优选地,所述步骤S2~S4反应体系含铁介质或被有机污染物污染的含铁介质与无机盐培养基固液质量比为1:(20~100),Shewanella Oneidensis MR-1希瓦氏菌属接种稀释后OD600不小于0.05。Preferably, the solid-to-liquid mass ratio of the iron-containing medium or the iron-containing medium contaminated by organic pollutants to the inorganic salt medium in the reaction system of steps S2 to S4 is 1: (20 to 100), Shewanella Oneidensis MR-1 The OD 600 of the genus after inoculation and dilution is not less than 0.05.

优选地,所述步骤S3中厌氧培养通氮气时间不少于15min,已达到完全去除体系中氧的目的;厌氧培养时间不少于24h,以充分还原生成Fe(II)。Preferably, in the step S3, the anaerobic culture is passed through nitrogen for no less than 15 minutes to achieve the purpose of completely removing oxygen in the system; the anaerobic culture time is no less than 24 hours to fully reduce and generate Fe(II).

优选地,所述步骤S4中好氧培养时间为3~8h。好氧培养生成活性氧过氧化氢H2O2和羟基自由基·OH。Preferably, the aerobic cultivation time in the step S4 is 3-8 hours. Aerobic culture generates reactive oxygen species hydrogen peroxide H 2 O 2 and hydroxyl radical · OH.

优选地,所述步骤S5中循环培养总次数不少于3次。Preferably, the total number of cycle culture in step S5 is not less than 3 times.

优选地,所述步骤S2中碳源选自乳酸盐、柠檬酸盐、丙酮酸盐等中的一种或几种;浓度为10~500mM。Preferably, the carbon source in the step S2 is selected from one or more of lactate, citrate, pyruvate, etc.; the concentration is 10-500 mM.

3.有益效果3. Beneficial effect

相比于现有技术,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:

(1)本发明中,针对有机污染物,尤其是多环芳烃,采用Shewanella OneidensisMR-1希瓦氏菌属与铁协同依次进行循环多次的厌氧培养(还原过程)、好氧培养(氧化过程)步骤,能够在铁氧化还原条件下Fe(III)/Fe(II)循环生成,同时,Shewanella OneidensisMR-1希瓦氏菌属在好氧条件下生成H2O2,上述的厌氧与好氧过程对有机污染物的迁移转化具有重大的影响;Fe(II)和H2O2之间的相互作用可以产生·OH等活性氧使有机污染物被高效氧化;Fe是地壳中第四大元素,Fe在土壤和水体介质中含量丰富,其氧化还原循环与多种生物地球化学过程有关,在污染物迁移转化过程中具有重要作用;在土壤-地下水氧化还原波动环境中,微生物与含铁矿物的相互作用对活性氧生成有显著影响。(1) In the present invention, for organic pollutants, especially polycyclic aromatic hydrocarbons, adopt Shewanella OneidensisMR-1 Shewanella genus and iron synergy to carry out anaerobic culture (reduction process) and aerobic culture (oxidation process) that cycle repeatedly successively process) step, which can generate Fe(III)/Fe(II) cycle under iron redox conditions. At the same time, Shewanella OneidensisMR-1 Shewanella can generate H 2 O 2 under aerobic conditions. The above-mentioned anaerobic and The aerobic process has a significant impact on the migration and transformation of organic pollutants; the interaction between Fe(II) and H 2 O 2 can generate active oxygen such as OH to efficiently oxidize organic pollutants; Fe is the fourth The large element, Fe, is rich in soil and water media, and its redox cycle is related to a variety of biogeochemical processes, and plays an important role in the migration and transformation of pollutants; in the environment of soil-groundwater redox fluctuations, microorganisms and Iron-mineral interactions have a significant effect on ROS generation.

(2)针对被有机污染物污染的含铁介质如含铁矿物,本发明通过利用ShewanellaOneidensis MR-1希瓦氏菌属调控含铁矿物中铁的还原和氧化,改变矿物状态,使有机污染物随着含铁矿物等介质的还原溶解而释放,进一步被活性氧氧化降解转化,实现了强化有机污染物迁移转化的目的;含铁矿物的氧化还原过程对有机污染物迁移转化具有突出的效果,这可能是由于含铁矿物是有机污染物的吸附固定介质,通过自身价态变化来调控有机污染物的吸附和溶解状态,从而影响和改变有机污染物的迁移活性;含铁矿物能够刺激和促进微生物生长代谢,促进有机污染物的迁移和转化。(2) For iron-containing media polluted by organic pollutants such as iron-containing minerals, the present invention regulates the reduction and oxidation of iron in iron-containing minerals by utilizing ShewanellaOneidensis MR-1 Shewanella, changes the mineral state, and makes organic pollution The substances are released with the reduction and dissolution of iron-containing minerals and other media, and are further oxidized and degraded by active oxygen, which realizes the purpose of strengthening the migration and transformation of organic pollutants; the oxidation-reduction process of iron-containing minerals has outstanding effects on the migration and transformation of organic pollutants. This may be due to the fact that iron-containing minerals are the adsorption and fixation medium of organic pollutants, and regulate the adsorption and dissolution state of organic pollutants through their own valence changes, thereby affecting and changing the migration activity of organic pollutants; It can stimulate and promote the growth and metabolism of microorganisms, and promote the migration and transformation of organic pollutants.

附图说明Description of drawings

图1为本发明实施例1中厌氧/好氧循环下Shewanella Oneidensis MR-1希瓦氏菌属调控含Fe矿物氧化还原强化多环芳烃菲和芘迁移转化特征:a,c:含Fe针铁矿体系菲和芘的转化;b,d:不含Fe高岭石对照体系菲和芘的转化;Fig. 1 shows the characteristics of the migration and transformation of polycyclic aromatic hydrocarbons phenanthrene and pyrene under the anaerobic/aerobic cycle of Shewanella Oneidensis MR-1 under the regulation of Fe-containing minerals by Shewanella Oneidensis MR-1 in Example 1 of the present invention: a, c: Fe-containing needles Transformation of phenanthrene and pyrene in iron ore system; b, d: Transformation of phenanthrene and pyrene in kaolinite control system without Fe;

图2为本发明实施例2中厌氧/好氧循环厌氧培养结束时含Fe针铁矿体系生成Fe(II)的浓度;Fig. 2 is the concentration that the Fe goethite system generates Fe(II) when the anaerobic/aerobic cycle anaerobic culture finishes in the embodiment of the present invention 2;

图3为本发明实施例2中厌氧/好氧循环好氧培养结束时H2O2的浓度变化特征:a:含Fe针铁矿体系;b:不含Fe高岭石对照体系;Figure 3 is the characteristics of the concentration change of H2O2 at the end of anaerobic/aerobic cycle aerobic culture in Example 2 of the present invention: a: Fe-containing goethite system; b: Fe-free kaolinite control system;

图4为本发明实施例2中第4次厌氧/好氧循环好氧培养结束时生成·OH的浓度特征,a:含Fe针铁矿体系;b:不含Fe高岭石对照体系。Figure 4 is the concentration characteristics of OH generated at the end of the fourth anaerobic/aerobic cycle aerobic culture in Example 2 of the present invention, a: Fe-containing goethite system; b: Fe-free kaolinite control system.

具体实施方式Detailed ways

除非另有定义,本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同;本文所使用的术语“和/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by those skilled in the technical field of the present invention; the term "and/or" used herein includes one or more related listed Any and all combinations of items.

实施例中未注明具体条件者,按照常规条件或制造商建议的条件进行。所用试剂或仪器未注明生产厂商者,均为可以通过市售购买获得的常规产品。Those who do not indicate the specific conditions in the examples are carried out according to the conventional conditions or the conditions suggested by the manufacturer. The reagents or instruments used were not indicated by the manufacturer, and they were all conventional products that could be purchased from the market.

浓度、量和其他数值数据可以在本文中以范围格式呈现。应当理解,这样的范围格式仅是为了方便和简洁而使用,并且应当灵活地解释为不仅包括明确叙述为范围极限的数值,而且还包括涵盖在所述范围内的所有单独的数值或子范围,就如同每个数值和子范围都被明确叙述一样。例如,约1至约4.5的数值范围应当被解释为不仅包括明确叙述的1至约4.5的极限值,而且还包括单独的数字(诸如2、3、4)和子范围(诸如1至3、2至4等)。相同的原理适用于仅叙述一个数值的范围,诸如“小于约4.5”,应当将其解释为包括所有上述的值和范围。此外,无论所描述的范围或特征的广度如何,都应当适用这种解释。Concentrations, amounts, and other numerical data may be presented herein in a range format. It should be understood that such range format is used for convenience and brevity only, and should be construed flexibly to include not only the numbers expressly recited as the limits of the range, but also to encompass all individual values or subranges within said range, It is as if each value and subrange were expressly recited. For example, a numerical range of about 1 to about 4.5 should be interpreted to include not only the expressly recited limit of 1 to about 4.5, but also include individual numbers (such as 2, 3, 4) and subranges (such as 1 to 3, 2 to 4 etc.). The same principle applies to ranges reciting only one numerical value, such as "less than about 4.5", which should be construed to include all such values and ranges. Moreover, such an interpretation should apply regardless of the breadth of the range or features described.

以下结合附图和实例对本发明的具体实施作进一步说明,但本发明的实施和保护不限于此。需指出的是,以下若有未特别详细说明之过程,均是本领域技术人员可参照现有技术实现或理解的。所用试剂或仪器未注明生产厂商者,视为可以通过市售购买得到的常规产品。The specific implementation of the present invention will be further described below in conjunction with the accompanying drawings and examples, but the implementation and protection of the present invention are not limited thereto. It should be pointed out that, if there are any processes in the following that are not specifically described in detail, those skilled in the art can realize or understand with reference to the prior art. The reagents or instruments used were not indicated by the manufacturer, and they were regarded as conventional products that can be purchased from the market.

作为举例,以下实施例中采用针铁矿为含Fe矿物介质、高岭石为不含Fe矿物介质,选择多环芳烃中的菲和芘作为代表性有机污染物,以及Shewanella Oneidensis MR-1希瓦氏菌属进行实验。所述菌株是Fe还原菌,购自中国典型培养物保藏中心,保藏号CCTCCAB2013238,为革兰氏阴性菌。As an example, in the following examples, goethite is used as Fe-containing mineral medium, kaolinite is Fe-free mineral medium, phenanthrene and pyrene in polycyclic aromatic hydrocarbons are selected as representative organic pollutants, and Shewanella Oneidensis MR-1 Greek Varella spp. for experiments. The strain is an Fe-reducing bacterium, purchased from the China Center for Type Culture Collection with the preservation number CCTCCAB2013238, and is a Gram-negative bacterium.

实施例1Example 1

一、多环芳烃污染矿物介质的制备1. Preparation of PAH Contaminated Mineral Media

使多环芳烃与矿物混合,包括以下步骤,具体为:Mixing polycyclic aromatic hydrocarbons with minerals includes the following steps, specifically:

分别称取10g矿物(针铁矿,铁含量约为60%;高岭石,不含铁)于100mL玻璃烧杯中,加入10mL丙酮配置的菲和芘混合液,轻轻摇匀,然后静置于通风橱中,待丙酮完全挥发,制得菲和芘污染的矿物。污染矿物中菲和芘的含量分别为:Weigh 10g of minerals (goethite, iron content about 60%; kaolinite, iron-free) into a 100mL glass beaker, add 10mL of acetone-prepared phenanthrene and pyrene mixture, shake gently, and then let stand In a fume hood, wait until the acetone is completely volatilized to obtain minerals contaminated with phenanthrene and pyrene. The contents of phenanthrene and pyrene in polluted minerals are respectively:

针铁矿:菲,346±25μg g-1;芘,328±11μg g-1;∑PAHs,674±27μg g-1Goethite: phenanthrene, 346±25 μg g -1 ; pyrene, 328±11 μg g -1 ; ΣPAHs, 674±27 μg g -1 .

高岭石:菲,258±31μg g-1;芘,238±17μg g-1;∑PAHs,495±36μg g-1Kaolinite: phenanthrene, 258±31 μg g -1 ; pyrene, 238±17 μg g -1 ; ΣPAHs, 495±36 μg g -1 .

矿物研磨过60目筛后保存于棕色玻璃试剂瓶中。Minerals were ground and passed through a 60-mesh sieve and stored in brown glass reagent bottles.

二、菌株的培养扩繁2. Cultivation and propagation of strains

菌株活化和扩繁,菌株为Shewanella Oneidensis MR-1希瓦氏菌属,购买于中国典型培养物保藏中心,保藏号CCTCC AB 2013238。该菌为典型的金属还原菌,能够还原Fe(III)生成Fe(II)。活化和扩繁包括如下步骤,具体为:Activation and propagation of the strain, the strain is Shewanella Oneidensis MR-1 Shewanella genus, purchased from China Center for Type Culture Collection, preservation number CCTCC AB 2013238. The bacteria is a typical metal-reducing bacteria, which can reduce Fe(III) to Fe(II). Activation and multiplication include the following steps, specifically:

将保存于-80℃甘油中的降解菌(Shewanella Oneidensis MR-1希瓦氏菌属)解冻,接种于灭菌的营养肉汤培养基中,接种比例为每100mL培养基接种0.2mL保藏液,随后于30℃,160rpm好氧避光培养过夜,待菌株生长至对数期,取出,转移至灭菌离心管中5000rpm离心收集下层菌体,然后采用灭菌磷酸盐缓冲液(pH7.0)清液2次,重新悬浮后调节细菌密度使得OD600=1.20。Thaw the degrading bacteria (Shewanella Oneidensis MR-1 Shewanella spp.) stored in glycerol at -80°C, inoculate them in sterilized nutrient broth medium, the inoculation ratio is 0.2mL of preservation solution per 100mL of medium, Then culture overnight at 30°C, 160rpm aerobic and dark. After the strain grows to the logarithmic phase, take it out, transfer it to a sterilized centrifuge tube at 5000rpm and centrifuge to collect the lower layer of bacteria, and then use sterilized phosphate buffer (pH7.0) The supernatant was used twice, and after resuspension, the bacterial density was adjusted so that OD 600 =1.20.

三、微生物调控含Fe介质还原氧化强化多环芳烃菲和芘的迁移转化3. Microorganisms regulate the reduction and oxidation of Fe-containing media to enhance the migration and transformation of polycyclic aromatic hydrocarbons phenanthrene and pyrene

微生物调控的含Fe介质的还原和氧化强化多环芳烃菲和芘的迁移转化,包括如下步骤,具体为:The reduction and oxidation of Fe-containing media regulated by microorganisms enhance the migration and transformation of polycyclic aromatic hydrocarbons phenanthrene and pyrene, including the following steps, specifically:

MR-1+碳源组:分别称取0.6g两种污染矿物于50mL玻璃离心管,加入28mL灭菌无机盐培养基,随后接种2mL准备好的Shewanella Oneidensis MR-1希瓦氏菌属菌液(OD600=1.20),加入0.12mL 60%乳酸盐作为碳源(最终浓度为20mM)。本实验中固液比为1:50(1:20~1:100均可),接种后使细菌密度OD600不小于0.05。MR-1+carbon source group: Weigh 0.6g of the two contaminated minerals into a 50mL glass centrifuge tube, add 28mL of sterilized inorganic salt medium, and then inoculate 2mL of the prepared Shewanella Oneidensis MR-1 Shewanella bacterium solution (OD 600 =1.20), 0.12 mL of 60% lactate was added as a carbon source (final concentration 20 mM). In this experiment, the solid-to-liquid ratio was 1:50 (1:20 to 1:100 is acceptable), and the bacterial density OD 600 was not less than 0.05 after inoculation.

MR-1组:同时设置接种菌株但不加乳酸盐碳源的处理(对照组1,MR-1),以确定Shewanella Oneidensis MR-1希瓦氏菌属是否能以PAHs为唯一碳源进行生长代谢。MR-1 group: At the same time, set the inoculated strain but no lactate carbon source treatment (control group 1, MR-1), to determine whether Shewanella Oneidensis MR-1 Shewanella can use PAHs as the sole carbon source growth metabolism.

CK组:实验还设置了不接种Shewanella Oneidensis MR-1希瓦氏菌属的处理(对照组2,CK),以此排除矿物体系PAHs的非生物调控降解。CK group: The experiment also set up the treatment of not inoculating Shewanella Oneidensis MR-1 Shewanella spp. (control group 2, CK) to exclude the non-biologically regulated degradation of PAHs in the mineral system.

上述实验体系先通入N2 15min以除去溶液中的氧气,随后放置于28℃静置厌氧培养40h,随后在震荡条件下好氧培养8h,以此为一个厌氧/好氧培养循环。The above-mentioned experimental system was fed with N 2 for 15 minutes to remove oxygen in the solution, then placed at 28°C for static anaerobic culture for 40 hours, and then aerobic cultured for 8 hours under shaking conditions, which was an anaerobic/aerobic culture cycle.

本实验过程中厌氧/好氧培养循环4次。During this experiment, the anaerobic/aerobic culture cycle was repeated 4 times.

在每个厌氧/好氧培养阶段结束时吸取样品液测定菲和芘的浓度,分析菲和芘的迁移转化特征。样品液采用有机溶剂提取,高效液相色谱(HPLC)法测定提取液中剩余菲和芘的含量,绘制菲和芘的转化动力学曲线(图1),并计算菲和芘转化率。结果显示,经过4个厌氧/好氧循环培养(192h)后,针铁矿体系中MR-1+碳源处理观测到60%的菲和48.6%的芘被降解转化(图1a,c)。尽管对照处理菲和芘也有一定降解,但MR-1+碳源处理菲和芘转化率有显著提高,但只接种MR-1处理菲和芘降解转化与对照没有差异。在高岭石体系中,MR-1+碳源处理观测到38.1%的菲和37.2%的芘被降解转化(图1b,d),MR-1+碳源处理、MR-1处理与对照处理相比,PAHs转化没有明显差异,甚至低于对照组2处理(图1b)。以上结果揭示菌株MR-1并不能以PAHs为唯一碳源转化PAHs,也不能与乳酸盐共代谢转化PAHs。只有在Fe和碳源共同存在下菌株MR-1才能调控含Fe矿物介质好氧/厌氧循环条件下PAHs的强化迁移转化。At the end of each anaerobic/aerobic culture stage, the sample solution was drawn to measure the concentration of phenanthrene and pyrene, and the migration and transformation characteristics of phenanthrene and pyrene were analyzed. The sample liquid was extracted with an organic solvent, and the content of remaining phenanthrene and pyrene in the extract was determined by high performance liquid chromatography (HPLC), and the conversion kinetics curve of phenanthrene and pyrene (Fig. 1) was drawn, and the conversion rate of phenanthrene and pyrene was calculated. The results showed that after 4 anaerobic/aerobic cycle cultivation (192h), 60% of phenanthrene and 48.6% of pyrene were observed to be degraded and transformed in the goethite system with MR-1+ carbon source (Figure 1a,c) . Although phenanthrene and pyrene were also degraded in the control treatment, the conversion rate of phenanthrene and pyrene was significantly increased in the MR-1+ carbon source treatment, but there was no difference in the degradation and conversion of phenanthrene and pyrene in the MR-1 treatment alone compared with the control. In the kaolinite system, 38.1% of phenanthrene and 37.2% of pyrene were observed to be degraded and converted by MR-1+ carbon source treatment (Fig. 1b, d), MR-1+ carbon source treatment, MR-1 treatment and control treatment In contrast, there was no significant difference in PAHs transformation, even lower than that of control group 2 treatment (Fig. 1b). The above results revealed that the strain MR-1 could not use PAHs as the sole carbon source to convert PAHs, nor could it co-metabolize PAHs with lactate. Only under the coexistence of Fe and carbon source can the strain MR-1 regulate the enhanced migration and transformation of PAHs under aerobic/anaerobic cycle conditions in Fe-containing mineral media.

实施例2Example 2

(一)微生物调控含Fe矿物介质Fe还原活性(1) Microbial regulation of Fe reduction activity in Fe-containing mineral media

微生物调控含Fe矿物介质Fe还原活性的研究,包括如下步骤,具体为:The research on the reduction activity of Fe-containing mineral media by microorganisms, including the following steps, specifically:

采用实施例1的方法构建微生物-矿物(Shewanella Oneidensis MR-1+碳源-矿物)迁移转化多环芳烃的厌氧/好氧培养体系中,于每个厌氧培养阶段结束时吸取样品液测定Fe(II)含量,分析Fe还原活性。采用菲咯嗪测定厌氧培养结束时体系中Fe(II)的生成浓度。Fe(II)与菲咯嗪形成红色络合物,在562nm下具有最大吸收峰。吸取0.5mL样品液于2mL离心管中,加入0.5mL 2mM菲咯嗪溶液,反应5min后定容到1.5mL,随后在6000r/min离心5min,上清液中Fe(II)采用紫外可见分光光度计在562nm波长下比色测定,摩尔吸光系数为27900M-1cm-1。结果显示(图2),在无Shewanella Oneidensis MR-1和碳源添加的针铁矿体系(对照组2)中,基本没有检测到Fe(II);而接种MR-1的处理(MR-1和MR-1+碳源)均观测到Fe(II)的生成,Fe(II)浓度为0.6~9.0μM。证明了在厌氧培养条件下,针铁矿能被菌株MR-1还原溶解生成为Fe(II)。Adopt the method of Example 1 to construct the anaerobic/aerobic culture system of microorganism-mineral (Shewanella Oneidensis MR-1+carbon source-mineral) migration conversion polycyclic aromatic hydrocarbons, draw sample liquid and measure at the end of each anaerobic culture stage Fe(II) content, analysis of Fe reduction activity. The concentration of Fe(II) in the system at the end of anaerobic culture was determined by phenanthrozine. Fe(II) forms a red complex with phenanthroxine, which has a maximum absorption peak at 562nm. Draw 0.5mL of sample solution into a 2mL centrifuge tube, add 0.5mL of 2mM phenanthrozine solution, react for 5min and then make it to 1.5mL, then centrifuge at 6000r/min for 5min, and the Fe(II) in the supernatant is measured by UV-Vis spectrophotometry It is measured colorimetrically at a wavelength of 562nm, and the molar absorptivity is 27900M -1 cm -1 . The results show (Fig. 2), in the goethite system (control group 2) without Shewanella Oneidensis MR-1 and carbon source addition, basically no Fe(II) was detected; while the treatment of inoculated MR-1 (MR-1 and MR-1+carbon source) were observed to form Fe(II), and the concentration of Fe(II) was 0.6-9.0μM. It was proved that under anaerobic culture conditions, goethite could be reductively dissolved into Fe(II) by the strain MR-1.

(二)微生物调控含Fe矿物介质氧化活性物质生成(2) Microorganisms regulate the generation of active substances in the oxidation of Fe-containing mineral media

微生物调控含Fe矿物介质氧化活性物质生成的研究,包括如下步骤,具体为:The research on microbial regulation of the formation of oxidative active substances in Fe-containing mineral media includes the following steps, specifically:

采用实施例1的方法构建微生物-矿物(Shewanella Oneidensis MR-1+碳源-矿物)迁移转化多环芳烃的厌氧/好氧培养体系中,于每个好氧培养阶段结束时吸取样品液测定过氧化氢H2O2含量,在最后一个好氧培养阶段结束时吸取样品分析羟基自由基·OH含量。具体方法如下:Using the method of Example 1 to construct an anaerobic/aerobic culture system in which microorganisms-minerals (Shewanella Oneidensis MR-1+carbon source-minerals) migrate and convert polycyclic aromatic hydrocarbons, draw sample liquid for determination at the end of each aerobic culture stage Hydrogen peroxide H 2 O 2 content, a sample was drawn at the end of the last aerobic incubation period to analyze the hydroxyl radical · OH content. The specific method is as follows:

(1)过氧化氢H2O2含量测定:具体过程为:采用辣根过氧化物酶法测定体系中生成的H2O2。吸取样品液0.5mL加入2mL离心管,加入0.1mL 1mg/mL辣根过氧化物酶,然后加入0.5mL 10mM ABTS溶液,反应5min,随后定容到1.5mL,混合液在6000r/min下离心5min。H2O2在辣根过氧化物酶的催化下氧化ABTS生成绿色的ABTS·+。样品离心后,上清液中的ABTS·+在415nm处用比色法测定,摩尔吸光度为34000M-1cm-1。H2O2与ABTS·+与的化学计量比2,将ABTS·+浓度除以系数2即得到溶液中生成的H2O2的浓度。结果显示(图3):在好氧培养阶段,针铁矿和高岭石体系均能检测到H2O2的生成。在CK处理以及MR-1处理下,仅检测到极少量的H2O2生成(<0.3μM),揭示在无菌或接菌但不外加碳源的情况下,H2O2活性氧的累积生成量极低,也反应微生物活性很小。在MR-1+碳源的处理中,两种矿物体系均能生成较高浓度的H2O2,且都在第2个好氧阶段培养后累计浓度达到最高(~40μM),在第3和4阶段H2O2生成浓度急剧下降(~0.64μM),推测其原因是添加的碳源乳酸盐浓度较低(20mM),在两个厌氧/好氧循环培养后(96h)碳源耗尽,导致后续培养过程中好氧呼吸活性降低进而H2O2产量下降。(1) Determination of hydrogen peroxide H 2 O 2 content: the specific process is: use the horseradish peroxidase method to measure the H 2 O 2 generated in the system. Draw 0.5mL of the sample solution into a 2mL centrifuge tube, add 0.1mL of 1mg/mL horseradish peroxidase, then add 0.5mL of 10mM ABTS solution, react for 5min, then dilute to 1.5mL, and centrifuge the mixture at 6000r/min for 5min . H 2 O 2 oxidizes ABTS under the catalysis of horseradish peroxidase to produce green ABTS ·+ . After the sample was centrifuged, ABTS ·+ in the supernatant was measured by colorimetry at 415nm, and the molar absorbance was 34000M -1 cm -1 . The stoichiometric ratio of H 2 O 2 to ABTS ·+ is 2, and the concentration of ABTS ·+ is divided by the coefficient 2 to obtain the concentration of H 2 O 2 generated in the solution. The results show (Fig. 3): During the aerobic culture stage, the generation of H 2 O 2 can be detected in both goethite and kaolinite systems. Under CK treatment and MR-1 treatment, only a very small amount of H 2 O 2 generation (<0.3 μM) was detected, revealing that in the case of aseptic or inoculation but no external carbon source, the generation of H 2 O 2 reactive oxygen species The cumulative production is extremely low, which also reflects little microbial activity. In the treatment of MR-1+ carbon source, the two mineral systems can generate higher concentration of H 2 O 2 , and the cumulative concentration reached the highest (~40μM) after the second aerobic stage culture, and in the third and 4 stage H 2 O 2 production concentration decreased sharply (~0.64μM), presumably because of the low concentration of added carbon source lactate (20mM), after two anaerobic/aerobic cycle culture (96h) carbon The depletion of the source leads to the reduction of aerobic respiration activity and the decrease of H 2 O 2 production in the subsequent cultivation process.

(2)羟基自由基·OH含量测定:具体过程为:采用香豆素作为探针测定体系中好氧培养结束时生成的·OH的浓度。将0.5mL样品液与0.5mL 2mM的香豆素混合,好氧培养2h,培养结束时加入0.5mL甲醇终止反应。随后混合液在6000r/min下离心5min,上清液过0.22μm滤膜后采用HPLC-荧光检测系统测定氧化产物7-羟基香豆素。7-羟基香豆素浓度通过0.005~1μM标准曲线计算,此方法检出限为0.0032μM。生成的·OH浓度通过7-羟基香豆素浓度除以系数14.5%计算而得。结果显示(图4):在所有处理中均检测到·OH,其含量在0.008μM~0.54μM之间。对照处理中·OH的生成揭示了矿物体系污染物可能存在非生物转化。而本研究结果中CK处理中菲和芘浓度的降低证实矿物体系PAHs的非生物转化降解。在微生物处理中,只接种MR-1的处理·OH生成量最低,甚至小于对照处理。这是因为菌株MR-1在没有额外碳源的情况下,微生物好氧呼吸活性很低,与前文中Fe(II)和H2O2生成活性低结果一致,造成MR-1不能调控·OH生成,并且影响非生物因素·OH的生成。在有碳源的情况下,MR-1调控生成大量的·OH,这与厌氧呼吸还原生成Fe(II)和好氧呼吸生成H2O2有关,二者反应生成·OH,从而转化矿物体系菲和芘等有机污染物。(2) Determination of hydroxyl radical · OH content: the specific process is: use coumarin as a probe to measure the concentration of · OH generated at the end of aerobic culture in the system. Mix 0.5mL sample liquid with 0.5mL 2mM coumarin, incubate aerobically for 2h, and add 0.5mL methanol at the end of the culture to terminate the reaction. Then the mixture was centrifuged at 6000r/min for 5min, and the supernatant was passed through a 0.22μm filter membrane, and the oxidized product 7-hydroxycoumarin was determined by HPLC-fluorescence detection system. The concentration of 7-hydroxycoumarin was calculated by the standard curve of 0.005-1 μM, and the detection limit of this method was 0.0032 μM. The resulting · OH concentration was calculated by dividing the 7-hydroxycoumarin concentration by a factor of 14.5%. The results showed ( FIG. 4 ): · OH was detected in all treatments, and its content was between 0.008 μM and 0.54 μM. The formation of · OH in the control treatment revealed the possible abiotic transformation of mineral system pollutants. However, the decrease of phenanthrene and pyrene concentration in CK treatment in this study confirmed the abiotic transformation degradation of PAHs in mineral system. Among the microbial treatments, the treatment only inoculated with MR-1 produced the lowest · OH production, even less than that of the control treatment. This is because the microbial aerobic respiration activity of the strain MR-1 is very low in the absence of additional carbon sources, which is consistent with the previous results of low Fe(II) and H 2 O 2 production activities, resulting in the inability of MR-1 to regulate OH Formation, and affect the formation of abiotic factors · OH. In the presence of carbon sources, MR-1 regulates the generation of a large amount of OH, which is related to the reduction of anaerobic respiration to Fe(II) and the generation of H 2 O 2 in aerobic respiration, and the two react to form OH, thereby transforming minerals System phenanthrene and pyrene and other organic pollutants.

以上结果表明微生物调控Fe(III)/Fe(II)还原与氧化过程能够导致含Fe矿物介质的还原溶解并释放有机污染物,在随后的好氧培养过程中受到活性氧H2O2·OH攻击而转化降解,从而实现对有机污染物的强化迁移转化。实验表明基于Fe的氧化还原过程在土壤-水等环境介质中有机污染物迁移转化过程和污染分布具有重要影响,在场地有机污染控制方面具有较好的应用潜力。The above results indicated that microbial regulation of the Fe(III)/Fe(II) reduction and oxidation process could lead to the reductive dissolution of Fe-containing mineral media and the release of organic pollutants, which were stimulated by reactive oxygen species H 2 O 2 and · OH attack to transform and degrade, so as to realize the enhanced migration and transformation of organic pollutants. Experiments show that the redox process based on Fe has an important impact on the migration and transformation process and pollution distribution of organic pollutants in environmental media such as soil-water, and has good application potential in the control of organic pollution on site.

以上实施例仅为本发明较优的实施方式,仅用于解释本发明,而非限制本发明,本领域技术人员在未脱离本发明精神实质下所作的改变、替换、修饰等均应属于本发明的保护范围。The above examples are only preferred implementations of the present invention, and are only used to explain the present invention, rather than limit the present invention. Changes, replacements, modifications, etc. made by those skilled in the art without departing from the spirit of the present invention shall belong to the present invention. protection scope of the invention.

Claims (10)

1.一种基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,在包含有机污染物和铁的介质中加入微生物和碳源,依次进行厌氧培养、好氧培养的步骤;所述微生物包括Shewanella Oneidensis MR-1希瓦氏菌属,购于中国典型培养物保藏中心,保藏号CCTCC AB 2013238;所述包含有机污染物和铁的介质包括向含有有机污染物的介质中加入铁或含铁介质形成的介质,或向含铁介质中加入含有机污染物形成的介质,或被有机污染物污染的含铁介质。1. A method for the migration and conversion of organic pollutants based on Fe redox enhancement, characterized in that, adding microorganisms and carbon sources to the medium containing organic pollutants and iron, followed by the steps of anaerobic cultivation and aerobic cultivation; The microorganisms include Shewanella Oneidensis MR-1 Shewanella genus, purchased from the China Center for Type Culture Collection, preservation number CCTCC AB 2013238; the medium containing organic pollutants and iron includes adding to the medium containing organic pollutants The medium formed by iron or ferrous medium, or the medium formed by adding organic pollutants to the ferrous medium, or the ferrous medium polluted by organic pollutants. 2.根据权利要求1所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,所述含铁介质包括含铁土壤,自然形成或人工合成的含铁矿物,或者人工外源添加含铁化合物组成的混合体系中的一种或几种。2. The method for the migration and conversion of organic pollutants based on Fe redox enhancement according to claim 1, wherein the iron-containing medium includes iron-containing soil, naturally formed or artificially synthesized iron-containing minerals, or artificial One or more of the mixed systems composed of external sources of iron-containing compounds. 3.根据权利要求2所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,所述有机污染物包括多环芳烃、氯代烃、石油烃、苯系物等中的一种或多种。3. the method for the migration and conversion of organic pollutants based on Fe redox strengthening according to claim 2, is characterized in that, described organic pollutants comprise polycyclic aromatic hydrocarbons, chlorinated hydrocarbons, petroleum hydrocarbons, benzene series etc. one or more. 4.根据权利要求1所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,包括以下步骤:4. the method for the migration and conversion of organic pollutants based on Fe redox strengthening according to claim 1, is characterized in that, comprises the following steps: S1采用灭菌营养肉汤培养基培养扩繁所述Shewanella Oneidensis MR-1希瓦氏菌属,随后调节细菌数量或细菌密度达到特定值;S1 uses sterilized nutrient broth medium to cultivate and multiply the Shewanella Oneidensis MR-1 Shewanella genus, and then adjust the number of bacteria or the density of bacteria to reach a specific value; S2向含有有机污染物的介质中加入含铁化合物后,加入至灭菌无机盐培养基,随后接种步骤S1所述Shewanella Oneidensis MR-1希瓦氏菌属和碳源;或S2 adds iron-containing compounds to the medium containing organic pollutants, and then adds to the sterilized inorganic salt medium, followed by inoculating the Shewanella Oneidensis MR-1 Shewanella genus and carbon source described in step S1; or 向含铁介质中加入灭菌无机盐培养基,随后接种所述步骤S1中ShewanellaOneidensis MR-1希瓦氏菌属和碳源,之后加入有机污染物混合;或Adding a sterilized inorganic salt medium to the iron-containing medium, followed by inoculating the ShewanellaOneidensis MR-1 Shewanella genus and carbon source in the step S1, and then adding organic pollutants to mix; or 向被有机污染物污染的含铁介质中加入灭菌无机盐培养基,随后接种步骤S1所述Shewanella Oneidensis MR-1希瓦氏菌属和碳源;Adding sterilized inorganic salt medium to the iron-containing medium contaminated by organic pollutants, followed by inoculation of Shewanella Oneidensis MR-1 Shewanella genus and carbon source described in step S1; S3厌氧培养:将所述步骤S2得到的混合体系通氮气去除氧气,密封后在厌氧条件下培养;S3 anaerobic culture: the mixed system obtained in the step S2 is ventilated with nitrogen to remove oxygen, and cultured under anaerobic conditions after sealing; S4好氧培养:所述步骤S3厌氧培养结束后,反应体系转为震荡的好氧条件下培养;S4 aerobic culture: after the anaerobic culture in step S3 is completed, the reaction system is converted to culture under aerobic conditions of vibration; S5依次重复上述S3和S4厌氧培养和好氧培养步骤,循环培养;S5 repeats the above-mentioned steps of S3 and S4 anaerobic cultivation and aerobic cultivation successively, and circulates cultivation; S6厌氧培养和好氧培养过程中补充碳源。S6 supplemented carbon source during anaerobic culture and aerobic culture. 5.根据权利要求4所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,所述Shewanella Oneidensis MR-1希瓦氏菌属扩繁条件包括:好氧培养,在灭菌营养肉汤培养基中接种适量菌液,在30℃和160rpm避光条件下培养过夜;用灭菌pH7.0 0.1M磷酸盐缓冲液清洗两次,调整菌密度为OD600=1.20。5. the method for the migration and conversion of organic pollutants based on Fe redox strengthening according to claim 4, is characterized in that, described Shewanella Oneidensis MR-1 Shewanella propagation condition comprises: aerobic culture, after killing Inoculate an appropriate amount of bacterial solution into the bacterial nutrient broth medium, and culture overnight at 30°C and 160 rpm in the dark; wash twice with sterilized pH 7.0 0.1M phosphate buffer, and adjust the bacterial density to OD 600 =1.20. 6.根据权利要求4所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,所述步骤S2-S4反应体系含铁介质或被有机污染物污染的含铁介质与无机盐培养基固液质量比为1:(20~100),Shewanella Oneidensis MR-1希瓦氏菌属接种稀释后OD600不小于0.05。6. The method for the migration and conversion of organic pollutants based on Fe redox enhancement according to claim 4, characterized in that, the step S2-S4 reaction system contains iron-containing medium or the iron-containing medium polluted by organic pollutants and inorganic The solid-to-liquid mass ratio of the salt medium is 1: (20-100), and the OD 600 after inoculation and dilution of Shewanella Oneidensis MR-1 is not less than 0.05. 7.根据权利要求4所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于,所述步骤S3中厌氧培养通氮气时间不少于15min,厌氧培养时间不少于24h。7. The method for the migration and transformation of organic pollutants based on Fe redox enhancement according to claim 4, characterized in that, in the step S3, the nitrogen gas flow time for anaerobic cultivation is not less than 15min, and the anaerobic cultivation time is not less than 24h. 8.根据权利要求4所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于所述步骤S4中好氧培养时间为3~8h。8. The method for the migration and transformation of organic pollutants based on Fe redox enhancement according to claim 4, characterized in that the aerobic cultivation time in the step S4 is 3-8 hours. 9.根据权利要求4~8中任意一项所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于所述步骤S5中循环培养总次数不少于3次。9 . The method for the migration and transformation of organic pollutants based on Fe redox enhancement according to any one of claims 4 to 8 , characterized in that the total number of cycle cultures in the step S5 is not less than 3 times. 10.根据权利要求4所述的基于Fe氧化还原强化的有机污染物迁移转化的方法,其特征在于所述步骤S2中碳源选自乳酸盐、柠檬酸盐、丙酮酸盐中的一种或几种;浓度为10~500mM。10. The method for the migration and transformation of organic pollutants based on Fe redox enhancement according to claim 4, characterized in that in the step S2, the carbon source is selected from one of lactate, citrate, and pyruvate Or several; the concentration is 10-500mM.
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