[go: up one dir, main page]

CN113979532B - A galvanic battery-type constructed wetland system with phosphorus recovery - Google Patents

A galvanic battery-type constructed wetland system with phosphorus recovery Download PDF

Info

Publication number
CN113979532B
CN113979532B CN202111265655.8A CN202111265655A CN113979532B CN 113979532 B CN113979532 B CN 113979532B CN 202111265655 A CN202111265655 A CN 202111265655A CN 113979532 B CN113979532 B CN 113979532B
Authority
CN
China
Prior art keywords
electrode
magnesium
phosphorus recovery
phosphorus
inner sleeve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202111265655.8A
Other languages
Chinese (zh)
Other versions
CN113979532A (en
Inventor
胡振
金凤林
王玉茹
张建
徐丹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong University
Original Assignee
Shandong University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shandong University filed Critical Shandong University
Priority to CN202111265655.8A priority Critical patent/CN113979532B/en
Publication of CN113979532A publication Critical patent/CN113979532A/en
Application granted granted Critical
Publication of CN113979532B publication Critical patent/CN113979532B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/105Phosphorus compounds

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Electrochemistry (AREA)
  • Biotechnology (AREA)
  • Botany (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

本发明公开了一种具有磷回收作用的原电池型人工湿地系统,属于污水资源化利用领域,其技术方案为:采用潜流人工湿地系统,包括基质层,基质层内设有至少一个原电池系统,所述原电池系统以镁电极为负极,以惰性电极为正极,镁电极和惰性电极通过导线连接;所述惰性电极插入基质层,镁电极插入基质层中的磷回收装置内,通过氧化反应使磷在镁电极上富集。本发明在人工湿地系统中耦合镁负极原电池系统,镁负极设于磷回收装置中,通过镁负极发生氧化反应使磷在镁负极附近富集,从而实现磷的高效回收。

Figure 202111265655

The invention discloses a galvanic battery-type constructed wetland system with phosphorus recovery function, which belongs to the field of sewage resource utilization. , the primary battery system uses the magnesium electrode as the negative electrode and the inert electrode as the positive electrode, and the magnesium electrode and the inert electrode are connected by wires; the inert electrode is inserted into the matrix layer, and the magnesium electrode is inserted into the phosphorus recovery device in the matrix layer, and the oxidation reaction is carried out through the oxidation reaction. Phosphorus is enriched on the magnesium electrode. The invention couples a magnesium negative electrode primary battery system in a constructed wetland system, the magnesium negative electrode is arranged in a phosphorus recovery device, and phosphorus is enriched near the magnesium negative electrode through the oxidation reaction of the magnesium negative electrode, thereby realizing the efficient recovery of phosphorus.

Figure 202111265655

Description

一种具有磷回收作用的原电池型人工湿地系统A galvanic battery-type constructed wetland system with phosphorus recovery

技术领域technical field

本发明涉及污水资源化利用领域,具体涉及一种具有磷回收作用的原电池型人工湿地系统。The invention relates to the field of sewage resource utilization, in particular to a galvanic battery type constructed wetland system with phosphorus recovery function.

背景技术Background technique

在水处理过程中回收磷资源,实现资源回收利用,能够有效缓解磷矿资源匮乏的问题。Recovering phosphorus resources in the process of water treatment and realizing resource recycling can effectively alleviate the problem of shortage of phosphate rock resources.

人工湿地利用植物、基质、微生物的综合生态作用实现污水的有效净化,具有基建投资省、运行费用低、生态景观优美等优点,它在发展中地区流域水污染治理、再生水回用及生态修复等领域具有突出的应用优势。与碳氮污染物可在微生物的作用下最终转化为气态物质离开湿地系统不同,人工湿地主要通过质的吸附作用、沉淀作用将水体中的磷截留蓄积在系统内部。但是,一旦接近或达到填料的吸附容量,将会导致人工湿地除磷效率的大幅下降,甚至发生磷释放现象。此外,磷在湿地中分布分散,无法实现磷的高效回收。Constructed wetlands use the comprehensive ecological effects of plants, substrates and microorganisms to achieve effective purification of sewage. It has the advantages of low investment in infrastructure, low operating costs, and beautiful ecological landscapes. It is used in water pollution control, recycled water reuse and ecological restoration in developing regions. The field has outstanding application advantages. Unlike carbon and nitrogen pollutants, which can be finally converted into gaseous substances and leave the wetland system under the action of microorganisms, constructed wetlands mainly intercept and accumulate phosphorus in the water body through mass adsorption and precipitation. However, once the adsorption capacity of the filler is approached or reached, the phosphorus removal efficiency of the constructed wetland will be greatly reduced, and even phosphorus release will occur. In addition, phosphorus is distributed and dispersed in wetlands, and efficient phosphorus recovery cannot be achieved.

另外,在污水处理过程中,可将磷转化为磷酸铁、磷酸铝、磷酸镁铵和羟基磷灰石等磷酸盐沉淀物,从而实现磷的回收。其中,基于利用氢氧化钠和镁盐等化学试剂投加进行的镁回收磷技术,所得到的的产品磷含量高;但是,化学试剂投加法的成本高,操作复杂,不便进行大规模的应用。In addition, in the process of sewage treatment, phosphorus can be converted into phosphate precipitates such as iron phosphate, aluminum phosphate, magnesium ammonium phosphate and hydroxyapatite, so as to realize the recovery of phosphorus. Wherein, based on the magnesium recovery phosphorus technology that utilizes the addition of chemical reagents such as sodium hydroxide and magnesium salts, the obtained product has a high phosphorus content; however, the chemical reagent addition method has high cost, complicated operation, and is inconvenient for large-scale application. .

发明内容SUMMARY OF THE INVENTION

针对现有技术存在的不足,本发明的目的是提供一种具有磷回收作用的原电池型人工湿地系统,在人工湿地系统中耦合镁负极原电池系统,镁负极设于磷回收装置中,通过镁负极发生氧化反应使磷在镁负极附近富集,从而实现磷的高效回收。In view of the deficiencies in the prior art, the purpose of the present invention is to provide a galvanic battery-type constructed wetland system with phosphorus recovery function. The oxidation reaction of the magnesium anode causes phosphorus to be enriched near the magnesium anode, so as to realize the efficient recovery of phosphorus.

为了实现上述目的,本发明是通过如下的技术方案来实现:In order to achieve the above object, the present invention is realized by the following technical solutions:

本发明的实施例提供了一种具有磷回收作用的原电池型人工湿地系统,采用潜流人工湿地系统,包括基质层,基质层内设有至少一个原电池系统,所述原电池系统以镁电极为负极,以惰性电极为正极,镁电极和惰性电极通过导线连接;The embodiment of the present invention provides a galvanic battery-type constructed wetland system with phosphorus recovery function, using a submerged flow constructed wetland system, including a matrix layer, and at least one galvanic battery system is arranged in the matrix layer, and the galvanic battery system uses magnesium electrodes. It is the negative electrode, the inert electrode is the positive electrode, and the magnesium electrode and the inert electrode are connected by wires;

所述惰性电极插入基质层,镁电极插入基质层中的磷回收装置内,通过氧化反应使磷在镁电极上富集。The inert electrode is inserted into the matrix layer, the magnesium electrode is inserted into the phosphorus recovery device in the matrix layer, and phosphorus is enriched on the magnesium electrode through oxidation reaction.

作为进一步的实现方式,所述磷回收装置包括套设在一起的内套筒和外套筒,内套筒和外套筒的底部封闭;内套筒中填充有基质层。As a further implementation manner, the phosphorus recovery device includes an inner sleeve and an outer sleeve sleeved together, the bottoms of the inner sleeve and the outer sleeve are closed; the inner sleeve is filled with a matrix layer.

作为进一步的实现方式,所述镁电极插入内套筒中的基质层中,惰性电极和镁电极均不完全插入基质层中。As a further implementation, the magnesium electrode is inserted into the matrix layer in the inner sleeve, and neither the inert electrode nor the magnesium electrode is completely inserted into the matrix layer.

作为进一步的实现方式,所述镁电极与惰性电极的间隔小于等于电极在基质层浸没长度,并大于等于电极浸没长度的1/2;As a further implementation manner, the interval between the magnesium electrode and the inert electrode is less than or equal to the immersion length of the electrode in the matrix layer, and greater than or equal to 1/2 of the immersion length of the electrode;

所述内套筒高度大于镁电极浸没高度。The height of the inner sleeve is greater than the immersion height of the magnesium electrode.

作为进一步的实现方式,所述内套筒和外套筒的侧壁均开有若干通孔,外套筒和内套筒之间形成容纳空间。As a further implementation manner, a plurality of through holes are opened on the side walls of the inner sleeve and the outer sleeve, and an accommodation space is formed between the outer sleeve and the inner sleeve.

作为进一步的实现方式,原电池系统为多个时,任意两个原电池系统的间隔大于电极浸没长度。As a further implementation manner, when there are multiple primary battery systems, the interval between any two primary battery systems is greater than the electrode immersion length.

作为进一步的实现方式,所述镁电极和惰性电极之间连接有电流表。As a further implementation manner, an ammeter is connected between the magnesium electrode and the inert electrode.

作为进一步的实现方式,所述惰性电极为石墨电极。As a further implementation manner, the inert electrode is a graphite electrode.

作为进一步的实现方式,所述基质层一侧设有进水系统,另一侧设有出水系统。As a further implementation, one side of the substrate layer is provided with a water inlet system, and the other side is provided with a water outlet system.

作为进一步的实现方式,所述进水系统采用间歇流。As a further implementation manner, the water inlet system adopts intermittent flow.

本发明的有益效果如下:The beneficial effects of the present invention are as follows:

(1)本发明在人工湿地系统中耦合镁负极原电池系统,镁电极发生氧化反应,释放出镁离子,与向镁电极移动的磷酸根离子结合生成磷酸镁铵等磷酸盐沉淀,使磷在镁电极附近富集,能够有效去除并回收磷资源,解决现有人工湿地技术所存在的吸附饱和以及磷资源回收困难的问题,实现磷资源的可持续。(1) The present invention couples a magnesium negative electrode primary battery system in a constructed wetland system, and the magnesium electrode undergoes an oxidation reaction to release magnesium ions, which combine with phosphate ions that move toward the magnesium electrode to generate phosphate precipitations such as magnesium ammonium phosphate, so that phosphorus in the The enrichment near the magnesium electrode can effectively remove and recover phosphorus resources, solve the problems of adsorption saturation and difficult phosphorus resource recovery in the existing constructed wetland technology, and realize the sustainability of phosphorus resources.

(2)本发明的人工湿地系统中设置一个或多个原电池系统,在实现磷回收的同时产生电能,实现能源再利用,降低污水处理能耗,增加人工湿地处理污水的广泛性和环保性。(2) One or more primary battery systems are arranged in the constructed wetland system of the present invention, which can generate electricity while realizing phosphorus recovery, realize energy reuse, reduce energy consumption for sewage treatment, and increase the extensiveness and environmental protection of constructed wetlands for sewage treatment. .

(3)本发明的磷回收装置包括套设在一起的内套筒和外套筒,镁电极放于内套筒中,将内套筒内填入人工湿地填料,内套筒和外套筒之间无填料填充,减少提升内套筒过程中的阻力。(3) The phosphorus recovery device of the present invention includes an inner sleeve and an outer sleeve that are sleeved together, the magnesium electrode is placed in the inner sleeve, the inner sleeve is filled with artificial wetland filler, the inner sleeve and the outer sleeve are There is no filler filling in between, reducing the resistance in the process of lifting the inner sleeve.

(4)本发明设置进水系统和排水系统,使得输出人工湿地基质内的水体形成循环,通过磷回收装置对污水内磷进行富集沉淀回收,进水系统输出的水体采用间歇流,以保证人工湿地为静水系统,水不流动,从而保证磷酸根阴离子向镁负极的自由扩散。(4) The present invention is provided with a water inlet system and a drainage system, so that the water body in the output constructed wetland matrix forms a cycle, and the phosphorus in the sewage is enriched, precipitated and recovered by the phosphorus recovery device, and the water body output by the water inlet system adopts intermittent flow to ensure The constructed wetland is a hydrostatic system, and the water does not flow, so as to ensure the free diffusion of phosphate anions to the magnesium negative electrode.

附图说明Description of drawings

构成本发明的一部分的说明书附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。The accompanying drawings forming a part of the present invention are used to provide further understanding of the present invention, and the exemplary embodiments of the present invention and their descriptions are used to explain the present invention, and do not constitute an improper limitation of the present invention.

图1是本发明根据一个或多个实施方式的结构示意图;1 is a schematic structural diagram of the present invention according to one or more embodiments;

图2是本发明根据一个或多个实施方式的磷回收装置结构示意图;2 is a schematic structural diagram of a phosphorus recovery device according to one or more embodiments of the present invention;

其中,1、湿地植物,2、进水口,3、镁电极,4、磷回收装置,5、基质层,6、电流表,7、石墨电极,8、出水口,9、内套筒,10、外套筒,11、容纳空间,12、垫层。Among them, 1. Wetland plants, 2. Water inlet, 3. Magnesium electrode, 4. Phosphorus recovery device, 5. Substrate layer, 6. Ammeter, 7. Graphite electrode, 8. Water outlet, 9. Inner sleeve, 10. Outer sleeve, 11, accommodating space, 12, cushion.

具体实施方式Detailed ways

实施例一:Example 1:

本实施例提供了一种具有磷回收作用的原电池型人工湿地系统,采用潜流人工湿地系统,在人工湿地系统中耦合镁负极原电池系统,镁负极发生氧化反应,释放出镁离子,与向镁负极移动的磷酸根离子作用生成难溶沉淀,使磷在镁负极附近富集,从而实现磷的高效回收。This embodiment provides a galvanic battery-type constructed wetland system with phosphorus recovery. A submerged constructed wetland system is used, and a magnesium anode galvanic battery system is coupled to the constructed wetland system. The magnesium anode undergoes an oxidation reaction to release magnesium ions, which are combined with The action of phosphate ions moved by the magnesium negative electrode generates insoluble precipitates, which enriches phosphorus near the magnesium negative electrode, thereby realizing the efficient recovery of phosphorus.

具体的,如图1所示,本实施例的人工湿地系统包括基质层5、湿地植物1、原电池系统、磷回收装置4、进水系统和出水系统,原电池系统在基质层5中设置一个或多个,任意两个原电池系统的间隔大于电极浸没长度,以避免原电池系统之间彼此影响。Specifically, as shown in FIG. 1 , the constructed wetland system of this embodiment includes a matrix layer 5 , wetland plants 1 , a primary battery system, a phosphorus recovery device 4 , a water inlet system and a water outlet system, and the primary battery system is set in the matrix layer 5 . One or more, the interval between any two galvanic cell systems is greater than the electrode immersion length, so as to avoid mutual influence between the galvanic cell systems.

所述基质层5的材料为砾石、火山岩、陶粒等非导电材料。The material of the matrix layer 5 is non-conductive materials such as gravel, volcanic rock, and ceramsite.

本实施例的人工湿地系统还布置有湿地植物1,所述湿地植物1采用芦苇、菖蒲、香蒲和鸢尾中的任意一种或者几种的组合,以9~25株/平方米的种植密度均匀种植。The constructed wetland system of the present embodiment is further arranged with wetland plants 1, and the wetland plants 1 use any one or a combination of reeds, calamus, cattails and irises, and the planting density is uniform at a planting density of 9 to 25 plants/square meter. planting.

进一步的,所述原电池系统包括镁电极3、惰性电极,惰性电极作为正极,镁电极3作为负极,在本实施例中,惰性电极采用石墨电极7,石墨电极7垂直插入基质层5中,且不完全浸没于基质层5;镁电极3垂直插入磷回收装置4中的基质层5内,且镁电极3与石墨电极7的浸没深度相同。Further, the primary battery system includes a magnesium electrode 3, an inert electrode, the inert electrode is used as a positive electrode, and the magnesium electrode 3 is used as a negative electrode. In this embodiment, the inert electrode adopts a graphite electrode 7, and the graphite electrode 7 is vertically inserted into the matrix layer 5, And not completely immersed in the matrix layer 5; the magnesium electrode 3 is vertically inserted into the matrix layer 5 in the phosphorus recovery device 4, and the magnesium electrode 3 and the graphite electrode 7 have the same immersion depth.

在本实施例中,镁电极3与石墨电极7的浸没长度为人工湿地深度(基质层5深度)的2/3,位于基质层5外的长度5cm;镁电极3和石墨电极7的间隔小于等于电极浸没长度大于等于电极浸没长度的1/2,以保证原电池系统的电解效果。In this embodiment, the immersion length of the magnesium electrode 3 and the graphite electrode 7 is 2/3 of the depth of the constructed wetland (the depth of the matrix layer 5), and the length outside the matrix layer 5 is 5 cm; the interval between the magnesium electrode 3 and the graphite electrode 7 is less than The immersion length of the electrode is equal to or greater than 1/2 of the immersion length of the electrode to ensure the electrolysis effect of the primary battery system.

可以理解的,在其他实施例中,镁电极3与石墨电极7的浸没长度也可以适应性调整。It can be understood that, in other embodiments, the immersion lengths of the magnesium electrode 3 and the graphite electrode 7 can also be adjusted adaptively.

本实施例的镁电极4为镁含量大于等于95%的纯镁或镁合金电极板。The magnesium electrode 4 in this embodiment is a pure magnesium or magnesium alloy electrode plate with a magnesium content of 95% or more.

进一步的,镁电极3和石墨电极7位于基质层5外的一端分别连接电极夹,二者的电极夹之间连接导线,且导线上连接有电流表6,通过电流表6检测原电池系统的产生的电流。Further, one end of the magnesium electrode 3 and the graphite electrode 7 located outside the matrix layer 5 is connected to an electrode clip respectively, a wire is connected between the two electrode clips, and an ammeter 6 is connected on the wire, and the generation of the primary battery system is detected by the ammeter 6. current.

在本实施例中,导线上可串联低瓦数LED灯。In this embodiment, low-wattage LED lamps can be connected in series on the wires.

所述基质层5一侧设有进水系统,另一侧设有出水系统,进水系统包括进水口2、与进水口2连接的进水管道,出水系统包括出水口8、与出水口连接的排水管道;本实施例的进水口2安装高度高于出水口8安装高度,待处理的污水经进水系统注入基质层5内,经磷回收后的水体经排水系统排出。One side of the substrate layer 5 is provided with a water inlet system, and the other side is provided with a water outlet system. The water inlet system includes a water inlet 2 and a water inlet pipe connected with the water inlet 2. The installation height of the water inlet 2 in this embodiment is higher than the installation height of the water outlet 8, the sewage to be treated is injected into the matrix layer 5 through the water inlet system, and the water body after phosphorus recovery is discharged through the drainage system.

其中,进水采用间歇流以确保离子在系统中扩散不受流场影响。Among them, the inlet water adopts intermittent flow to ensure that the diffusion of ions in the system is not affected by the flow field.

进一步的,如图2所示,磷回收装置4包括内套筒9、外套筒10和垫层12,外套筒10,外套筒10直径大于内套筒9直径,内套筒9套设于外套筒10内,二者之间形成容纳空间11。Further, as shown in FIG. 2, the phosphorus recovery device 4 includes an inner sleeve 9, an outer sleeve 10 and a cushion layer 12, an outer sleeve 10, the diameter of the outer sleeve 10 is larger than the diameter of the inner sleeve 9, and the inner sleeve 9 sets It is arranged in the outer sleeve 10, and a accommodating space 11 is formed between the two.

外套筒10和内套筒9的底部平齐,二者通过垫层12封堵,形成顶部开口、底部闭合的结构。所述外套筒10和内套筒9侧壁均开有若干密集分布的通孔,通孔大小要求不能使人工湿地填料通过。污水经通孔渗入磷回收装置4内,容纳空间11内存有经外套筒10的通孔进入的污水。The bottoms of the outer sleeve 10 and the inner sleeve 9 are flush, and they are blocked by the cushion layer 12 to form a structure with an open top and a closed bottom. The side walls of the outer sleeve 10 and the inner sleeve 9 are provided with a number of densely distributed through holes, and the size of the through holes is required not to allow the artificial wetland filler to pass through. The sewage penetrates into the phosphorus recovery device 4 through the through holes, and the sewage entering through the through holes of the outer sleeve 10 is stored in the accommodating space 11 .

所述内套筒9内填充有基质层5,内套筒9高度大于镁电极3浸没高度,即镁电极3底端距垫层12有一定距离;所述内套筒9直径大于镁电极3直径。The inner sleeve 9 is filled with the matrix layer 5, and the height of the inner sleeve 9 is greater than the immersion height of the magnesium electrode 3, that is, the bottom end of the magnesium electrode 3 has a certain distance from the cushion layer 12; the diameter of the inner sleeve 9 is larger than that of the magnesium electrode 3 diameter.

在本实施例中,内套筒9内壁距镁电极3外壁5cm,内套筒9外壁距外套筒10内壁5cm;垫层12直径与外套筒10直径相同,高度为5cm。In this embodiment, the inner wall of the inner sleeve 9 is 5 cm away from the outer wall of the magnesium electrode 3, and the outer wall of the inner sleeve 9 is 5 cm away from the inner wall of the outer sleeve 10; the diameter of the cushion layer 12 is the same as that of the outer sleeve 10, and the height is 5 cm.

当然,在其他实施例中,内套筒9和外套筒10间距、内套筒9与镁电极3间距、垫层12高度等均可调整为其他值,具体根据人工湿地系统尺寸要求而定。Of course, in other embodiments, the distance between the inner sleeve 9 and the outer sleeve 10, the distance between the inner sleeve 9 and the magnesium electrode 3, the height of the cushion layer 12, etc. can be adjusted to other values, which are determined according to the size requirements of the constructed wetland system. .

所述外套筒10、内套筒9及垫层12为绝缘、承受载荷和抗化学反应能力强的塑料制品,如苯乙烯-丙烯睛共聚体、聚丙乙烯等。The outer sleeve 10 , the inner sleeve 9 and the cushion layer 12 are plastic products with strong insulation, load bearing and chemical resistance resistance, such as styrene-acrylonitrile copolymer, polypropylene and the like.

本实施例人工湿地系统的使用方法为:The using method of the constructed wetland system of the present embodiment is:

(1)将外套筒10埋入湿地基质层5中,其埋入深度高于镁电极3浸没长度5cm。(1) The outer sleeve 10 is embedded in the wetland matrix layer 5 , and the embedded depth is 5 cm higher than the immersion length of the magnesium electrode 3 .

(2)将垫层12放入外套筒10中,封堵外套筒10底端。(2) Put the cushion layer 12 into the outer sleeve 10 to block the bottom end of the outer sleeve 10 .

(3)将内套筒9放入垫层12中央,将内套筒9底端封堵。(3) Put the inner sleeve 9 into the center of the cushion layer 12, and seal the bottom end of the inner sleeve 9.

(4)将镁电极3放入内套筒9中央,将内套筒9中填入人工湿地填料,内套筒9和外套筒10之间无填料填充,减少提升内套筒9过程中的阻力。(4) Put the magnesium electrode 3 into the center of the inner sleeve 9, fill the inner sleeve 9 with artificial wetland filler, and no filler is filled between the inner sleeve 9 and the outer sleeve 10, which reduces the process of lifting the inner sleeve 9. resistance.

镁电极3发生氧化反应,释放出镁离子,与向镁电极移动的磷酸根离子结合生成磷酸镁铵等磷酸盐沉淀,使磷在镁电极3附近富集。The magnesium electrode 3 undergoes an oxidation reaction to release magnesium ions, which combine with the phosphate ions moving toward the magnesium electrode to form phosphate precipitation such as magnesium ammonium phosphate, so that phosphorus is enriched near the magnesium electrode 3 .

(5)电流表6显示电流为初始的15%时,将内套筒9及其中基质取出,用稀酸淋洗基质及镁电极3表面,即可实现磷的回收。(5) When the ammeter 6 shows that the current is 15% of the initial value, the inner sleeve 9 and the substrate therein are taken out, and the substrate and the surface of the magnesium electrode 3 are rinsed with dilute acid to realize the recovery of phosphorus.

本实施例是人工湿地与镁原电池技术的有机结合,在强化人工湿地除磷的基础上,改变人工湿地中磷蓄积分布,高效回收水中的磷,实现资源的回收;同时产生电能,实现能源再利用,降低污水处理能耗,增加人工湿地处理污水的广泛性和环保性。This embodiment is an organic combination of constructed wetland and magnesium primary battery technology. On the basis of strengthening phosphorus removal in constructed wetland, the distribution of phosphorus accumulation in constructed wetland is changed, phosphorus in water is efficiently recovered, and resource recovery is realized; at the same time, electricity is generated to realize energy Reuse, reduce the energy consumption of sewage treatment, and increase the extensiveness and environmental protection of sewage treatment by constructed wetlands.

以上所述仅为本申请的优选实施例而已,并不用于限制本申请,对于本领域的技术人员来说,本申请可以有各种更改和变化。凡在本申请的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本申请的保护范围之内。The above descriptions are only preferred embodiments of the present application, and are not intended to limit the present application. For those skilled in the art, the present application may have various modifications and changes. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of this application shall be included within the protection scope of this application.

Claims (9)

1. A galvanic cell type artificial wetland system with a phosphorus recovery function is characterized in that an undercurrent artificial wetland system is adopted, and the system comprises a substrate layer, wherein at least one galvanic cell system and a phosphorus recovery device are arranged in the substrate layer;
the primary battery system takes a magnesium electrode as a negative electrode and an inert electrode as a positive electrode, and the magnesium electrode is connected with the inert electrode through a lead;
the phosphorus recovery device comprises an inner sleeve and an outer sleeve which are sleeved together, and a cushion layer is arranged between the bottoms of the inner sleeve and the outer sleeve; the inner sleeve is filled with a matrix;
the inert electrode is inserted into the substrate layer, the magnesium electrode is inserted into the phosphorus recovery device in the substrate layer, and phosphorus is enriched in the phosphorus recovery device through oxidation reaction.
2. The galvanic artificial wetland system with phosphorus recovery of claim 1, wherein the magnesium electrode is inserted into the matrix layer in the inner sleeve, and neither the inert electrode nor the magnesium electrode is completely inserted into the matrix layer.
3. The galvanic artificial wetland system with phosphorus recovery function of claim 2, wherein the distance between the magnesium electrode and the inert electrode is less than or equal to the submergence length of the electrode in the substrate layer and more than or equal to 1/2 of the submergence length of the electrode;
the inner sleeve is higher than the magnesium electrode submerging height.
4. The galvanic artificial wetland system with phosphorus recovery function according to claim 1, wherein the side walls of the inner sleeve and the outer sleeve are provided with a plurality of through holes, and a containing space is formed between the outer sleeve and the inner sleeve.
5. The constructed wetland system of claim 1, wherein the distance between any two of the plurality of the galvanic cell systems is longer than the electrode immersion length.
6. The galvanic artificial wetland system with phosphorus recovery function of claim 1, wherein an ammeter is connected between the magnesium electrode and the inert electrode.
7. The galvanic artificial wetland system with phosphorus recovery function of claim 1, wherein the inert electrode is a graphite electrode.
8. The galvanic cell-type constructed wetland system with phosphorus recovery of claim 1, wherein the substrate layer is provided with a water inlet system on one side and a water outlet system on the other side.
9. The galvanic artificial wetland system with phosphorus recovery function of claim 8, wherein the water inlet system adopts intermittent flow.
CN202111265655.8A 2021-10-28 2021-10-28 A galvanic battery-type constructed wetland system with phosphorus recovery Active CN113979532B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111265655.8A CN113979532B (en) 2021-10-28 2021-10-28 A galvanic battery-type constructed wetland system with phosphorus recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111265655.8A CN113979532B (en) 2021-10-28 2021-10-28 A galvanic battery-type constructed wetland system with phosphorus recovery

Publications (2)

Publication Number Publication Date
CN113979532A CN113979532A (en) 2022-01-28
CN113979532B true CN113979532B (en) 2022-10-11

Family

ID=79743755

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111265655.8A Active CN113979532B (en) 2021-10-28 2021-10-28 A galvanic battery-type constructed wetland system with phosphorus recovery

Country Status (1)

Country Link
CN (1) CN113979532B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116135801B (en) * 2023-04-18 2023-08-08 江苏龙腾工程设计股份有限公司 A rural ecological wetland purification treatment system

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103693811A (en) * 2013-12-23 2014-04-02 中国农业大学 Movable micro electrolysis wetland sewage treatment method and system
CN104928706A (en) * 2015-06-30 2015-09-23 福建师范大学 Set for converting nitrogen and phosphorus in cultivation wastewater into magnesium ammonium phosphate on basis of seawater cell technology
CN206814494U (en) * 2017-06-07 2017-12-29 环境保护部南京环境科学研究所 A kind of removal lead, the feulcell prototype artificial swamp of zinc heavy metal
CN108249548A (en) * 2018-01-31 2018-07-06 南京大学 A kind of electrolysis modified biomass charcoal system and its application
CN109607952A (en) * 2018-12-28 2019-04-12 武汉紫光能控科技有限公司 A kind of reinforced phosphor-removing composite artificial wet land treating system
CN208948923U (en) * 2018-08-31 2019-06-07 湖北美辰环保科技有限公司 A kind of guanite method recycling reactor of array
CN111362365A (en) * 2020-01-17 2020-07-03 华中科技大学 Unpowered nitrogen and phosphorus removal primary battery and preparation method and application thereof
CN111592115A (en) * 2020-06-20 2020-08-28 中冶节能环保有限责任公司 A microbial fuel cell-constructed wetland coupling system
CN212450852U (en) * 2020-06-20 2021-02-02 中冶节能环保有限责任公司 Microbial fuel cell-constructed wetland coupling system
CN113024039A (en) * 2021-03-19 2021-06-25 南京市市政设计研究院有限责任公司 Bioelectricity-enhanced subsurface flow wetland system and pollutant treatment method
CN113023845A (en) * 2021-04-26 2021-06-25 福建师范大学 Electrochemical method for recovering low-concentration nitrogen and phosphorus in wastewater in struvite form
CN113336313A (en) * 2021-06-04 2021-09-03 重庆大学 Constructed wetland microbial fuel cell sewage treatment device

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103693811A (en) * 2013-12-23 2014-04-02 中国农业大学 Movable micro electrolysis wetland sewage treatment method and system
CN104928706A (en) * 2015-06-30 2015-09-23 福建师范大学 Set for converting nitrogen and phosphorus in cultivation wastewater into magnesium ammonium phosphate on basis of seawater cell technology
CN206814494U (en) * 2017-06-07 2017-12-29 环境保护部南京环境科学研究所 A kind of removal lead, the feulcell prototype artificial swamp of zinc heavy metal
CN108249548A (en) * 2018-01-31 2018-07-06 南京大学 A kind of electrolysis modified biomass charcoal system and its application
CN208948923U (en) * 2018-08-31 2019-06-07 湖北美辰环保科技有限公司 A kind of guanite method recycling reactor of array
CN109607952A (en) * 2018-12-28 2019-04-12 武汉紫光能控科技有限公司 A kind of reinforced phosphor-removing composite artificial wet land treating system
CN111362365A (en) * 2020-01-17 2020-07-03 华中科技大学 Unpowered nitrogen and phosphorus removal primary battery and preparation method and application thereof
CN111592115A (en) * 2020-06-20 2020-08-28 中冶节能环保有限责任公司 A microbial fuel cell-constructed wetland coupling system
CN212450852U (en) * 2020-06-20 2021-02-02 中冶节能环保有限责任公司 Microbial fuel cell-constructed wetland coupling system
CN113024039A (en) * 2021-03-19 2021-06-25 南京市市政设计研究院有限责任公司 Bioelectricity-enhanced subsurface flow wetland system and pollutant treatment method
CN113023845A (en) * 2021-04-26 2021-06-25 福建师范大学 Electrochemical method for recovering low-concentration nitrogen and phosphorus in wastewater in struvite form
CN113336313A (en) * 2021-06-04 2021-09-03 重庆大学 Constructed wetland microbial fuel cell sewage treatment device

Also Published As

Publication number Publication date
CN113979532A (en) 2022-01-28

Similar Documents

Publication Publication Date Title
CN105024089A (en) Microbial fuel cell artificial wetland device for sewage treatment and power supply to wetland
CN201713362U (en) Plate type compound electrochemical device used for recovering heavy metal in wastewater
CN104150681A (en) Reactor of microbial nitrogen and phosphorus recovery battery for water treatment
CN105217797B (en) A kind of composite vertical current artificial wetland couples the method and device of microorganism electrolysis cell strengthened denitrification
CN103820811B (en) Method for recovering elemental copper from copper-containing wastewater by using microbial fuel cell
CN110668556B (en) Visible light catalysis coupling bioelectrochemical wetland system and application thereof
CN102633320A (en) Method for treating iron-carbon microelectrode and sewage
CN103956510A (en) Microbial fuel cell with double chambers for simultaneous phosphorus and nitrogen removal
CN105399202A (en) Method for removing phosphorous based on high-efficiency promotion of spongy iron corrosion in process of nitrogen removal by denitrification
CN105502673A (en) Device for simultaneously generating electricity and purifying sewage by taking steel slag as anode
CN113979532B (en) A galvanic battery-type constructed wetland system with phosphorus recovery
CN104624628A (en) System and method for removing heavy metals by using microbial fuel cell established in soil
CN105967455A (en) Refuse leachate self-powered denitration apparatus and method
JP2004066223A (en) Electrolyte waste water treatment device, electrode used for the device and power generation device
CN201864610U (en) Folded plate type cathode strengthening electrochemical device for treating wastewater containing heavy metal
CN207391073U (en) A kind of three-dimensional electrolysis device of synchronous removal beneficiation wastewater COD and heavy metal
CN110563158A (en) Zero-valent iron-based coil spring type microbial fuel cell capable of synchronously removing nitrogen and phosphorus and working method thereof
CN102774935A (en) Method for treating hardly-degraded wastewater by ferric and cupric bimetallic particles
CN105541046B (en) It is a kind of using slag as the synchronous electrogenesis of anode and the device of sewage purification
CN203871429U (en) Simultaneous phosphorus and nitrogen removal double-chamber microbiological fuel cell
CN210764607U (en) Coil spring type microbial fuel cell for synchronous nitrogen and phosphorus removal based on zero-valent iron
CN109678254A (en) A kind of microbiological fuel cell
CN108520972A (en) An integrated iron-based decontamination and resource reuse microbial fuel cell and sewage treatment method
CN114751488B (en) Electrochemical treatment system and its application in phosphorus recovery
CN216785795U (en) Device for treating anaerobic digestion wastewater and recycling nitrogen and phosphorus resources by using magnesium-air battery

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant