CN101735947A - Soil anammox bacterium gathering system simulating natural environment - Google Patents

Soil anammox bacterium gathering system simulating natural environment Download PDF

Info

Publication number
CN101735947A
CN101735947A CN200910155264A CN200910155264A CN101735947A CN 101735947 A CN101735947 A CN 101735947A CN 200910155264 A CN200910155264 A CN 200910155264A CN 200910155264 A CN200910155264 A CN 200910155264A CN 101735947 A CN101735947 A CN 101735947A
Authority
CN
China
Prior art keywords
soil
natural environment
reactor
simulating natural
peristaltic pump
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.)
Granted
Application number
CN200910155264A
Other languages
Chinese (zh)
Other versions
CN101735947B (en
Inventor
胡宝兰
沈李东
郑平
陈建伟
余燚
张吉强
陈小光
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.)
Zhejiang University ZJU
Original Assignee
Zhejiang University ZJU
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 Zhejiang University ZJU filed Critical Zhejiang University ZJU
Priority to CN 200910155264 priority Critical patent/CN101735947B/en
Publication of CN101735947A publication Critical patent/CN101735947A/en
Application granted granted Critical
Publication of CN101735947B publication Critical patent/CN101735947B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M25/00Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
    • C12M25/16Particles; Beads; Granular material; Encapsulation
    • C12M25/18Fixed or packed bed
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M33/00Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C12M33/22Settling tanks; Sedimentation by gravity

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Immunology (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

本发明公开了一种模拟自然环境的土壤厌氧氨氧化菌富集系统。它包括进水箱、蠕动泵、时控器、反应器主体、喷头、土柱、带孔圆盘、支架、排水管、沉淀区、排泥管、填料层、取泥口、圆盘圆孔、喷头圆孔,反应器主体下部设有支架,反应器主体从上到下依次设有喷头、土柱、带孔圆盘、填料层、沉淀区,反应器主体底部设有排水管、排泥管,在反应器主体放土柱的侧壁上设多个取泥口,喷头上端与蠕动泵、进水箱依次连接,蠕动泵与时控器连接。本发明的优点:1)取相应深度土层于土柱中,建立模拟自然环境的土柱,有利于土壤中厌氧氨氧化菌的富集;2)时控组件实现了反应器间歇进水;3)此富集系统完全模拟原生态,可富集土壤生态系统中的厌氧氨氧化菌。

Figure 200910155264

The invention discloses a soil anammox bacteria enrichment system simulating natural environment. It includes water inlet tank, peristaltic pump, time controller, reactor main body, nozzle, soil column, disc with holes, support, drainage pipe, sedimentation area, mud discharge pipe, packing layer, mud inlet, disc hole , Nozzle round hole, the lower part of the reactor main body is provided with brackets, the reactor main body is provided with nozzles, soil columns, discs with holes, packing layer, and sedimentation area in sequence from top to bottom, and the bottom of the reactor main body is provided with drainage pipes and sludge discharge A plurality of mud inlets are provided on the side wall of the soil column of the main body of the reactor, and the upper end of the nozzle is connected with the peristaltic pump and the water inlet tank in sequence, and the peristaltic pump is connected with the time controller. Advantages of the present invention: 1) Take the corresponding depth of soil layer in the soil column to establish a soil column simulating the natural environment, which is conducive to the enrichment of anammox bacteria in the soil; 2) The time control component realizes the intermittent water inflow of the reactor ; 3) This enrichment system completely simulates the original ecology, and can enrich the anammox bacteria in the soil ecosystem.

Figure 200910155264

Description

模拟自然环境的土壤厌氧氨氧化菌富集系统 Soil Anammox Bacteria Enrichment System Simulating Natural Environment

技术领域technical field

本发明涉及一种模拟自然环境的土壤厌氧氨氧化菌富集系统。The invention relates to a soil anammox bacteria enrichment system simulating natural environment.

背景技术Background technique

厌氧氨氧化(Anaerobic ammonia oxidation,Anammox)是指在厌氧条件下氨氮与亚硝酸氮反应,生成氮气的过程。从电子供体的角度看,厌氧氨氧化是一个氨的氧化反应,类似于硝化作用;但从电子受体的角度看,厌氧氨氧化则是一个亚硝酸盐的还原反应,类似于反硝化作用。也就是说厌氧氨氧化既可以算是硝化作用,也可以算是反硝化作用,在氮素循环中同时介入了硝化作用和反硝化作用中,改变了传统的硝化-反硝化氮循环模式。厌氧氨氧化作用的发现给微生物氮循环增加了新的内容。厌氧氨氧化最早是在人工废水处理系统中发现的,但厌氧氨氧化反应也普遍存在于自然生态系统中,如在海洋生态系统,湖泊沉积物、河口沉积物、土壤地下水处理系统等生态系统中都检测到了厌氧氨氧化活性,并被证实具有重要作用。厌氧氨氧化在全球氮素循环中所起的贡献不容忽视。Anaerobic ammonia oxidation (Anammox) is a process in which ammonia nitrogen reacts with nitrite nitrogen to generate nitrogen gas under anaerobic conditions. From the perspective of electron donor, anammox is an oxidation reaction of ammonia, similar to nitrification; but from the perspective of electron acceptor, anammox is a reduction reaction of nitrite, similar to reverse reaction. nitrification. That is to say, anaerobic ammonia oxidation can be regarded as both nitrification and denitrification. In the nitrogen cycle, both nitrification and denitrification are involved, which changes the traditional nitrification-denitrification nitrogen cycle mode. The discovery of anaerobic ammonium oxidation has added new content to the microbial nitrogen cycle. Anaerobic ammonium oxidation was first discovered in artificial wastewater treatment systems, but anaerobic ammonium oxidation reactions are also commonly found in natural ecosystems, such as in marine ecosystems, lake sediments, estuary sediments, soil groundwater treatment systems, etc. Anammox activity was detected in the system and was confirmed to play an important role. The contribution of ANAMMOX to the global nitrogen cycle cannot be ignored.

土壤氮循环是全球氮循环的一个重要组成部分。其氮素转化过程对全球氮循环具有巨大的影响。在土壤生态系统中具有缺氧和厌氧层、有氧和缺氧的交界面,从发生厌氧氨氧化的条件看,是发生厌氧氨氧化的适合环境,但对于土壤氮素循环中厌氧氨氧化的报道却很少。在海洋生态系统中,厌氧氨氧化对氮循环的贡献可达30-50%,但在土壤生态系统中,由于厌氧氨氧化反应的介入而引起的传统土壤硝化-反硝化作用氮循环模式的改变以及各个环节在土壤氮循环中所起的贡献都未见报道。因此探明土壤厌氧氨氧化过程,对于完善土壤氮素循环模式及至全球氮素循环模式都具有重要的意义。The soil nitrogen cycle is an important part of the global nitrogen cycle. Its nitrogen transformation process has a huge impact on the global nitrogen cycle. There are anoxic and anaerobic layers, aerobic and anoxic interfaces in the soil ecosystem. From the perspective of the conditions for anaerobic ammonium oxidation, it is a suitable environment for anaerobic ammonium oxidation, but it is an anaerobic environment for soil nitrogen cycle. Oxyammoxidation reports are few. In marine ecosystems, the contribution of anammox to the nitrogen cycle can reach 30-50%, but in soil ecosystems, the traditional soil nitrification-denitrification nitrogen cycle mode caused by the intervention of anammox reaction Neither the changes nor the contribution of each link in the soil nitrogen cycle have been reported. Therefore, to find out the soil anammox process is of great significance for improving the soil nitrogen cycle model and even the global nitrogen cycle model.

本发明通过模拟自然土壤生态系统,建立土壤厌氧氨氧化菌富集系统,富集土壤厌氧氨氧化菌,扩大厌氧氨氧化菌的种群范围,为深入研究厌氧氨氧化菌及其在土壤氮素循环中的贡献和进一步开发厌氧氨氧化工艺奠定良好的基础。The present invention establishes a soil anammox bacteria enrichment system by simulating a natural soil ecosystem, enriches soil anammox bacteria, and expands the population range of anammox bacteria. The contribution of soil nitrogen cycle and the further development of anammox process lay a good foundation.

发明内容Contents of the invention

本发明的目的是克服现有技术的不足,提供一种模拟自然环境的土壤厌氧氨氧化菌富集系统。The purpose of the present invention is to overcome the deficiencies of the prior art and provide a soil anammox bacteria enrichment system simulating the natural environment.

模拟自然环境的土壤厌氧氨氧化菌富集系统包括进水箱、蠕动泵、时控器、反应器主体、喷头、土柱、带孔圆盘、支架、排水管、沉淀区、排泥管、填料层、取泥口、圆盘圆孔、喷头圆孔,反应器主体下部设有支架,反应器主体内从上到下依次设有喷头、土柱、带孔圆盘、填料层、沉淀区,反应器主体底部设有排水管、排泥管,在反应器主体放土柱的侧壁上设多个取泥口,喷头上端与蠕动泵、进水箱依次连接,蠕动泵与时控器连接。The soil anammox bacteria enrichment system simulating the natural environment includes water inlet tank, peristaltic pump, time controller, reactor body, nozzle, soil column, disc with holes, bracket, drain pipe, sedimentation area, and sludge discharge pipe , packing layer, mud intake, disc hole, nozzle hole, the lower part of the reactor main body is provided with brackets, and the reactor main body is provided with nozzles, soil columns, discs with holes, packing layer, sedimentation The bottom of the main body of the reactor is provided with drainage pipes and mud discharge pipes, and multiple mud inlets are provided on the side wall of the soil column of the main body of the reactor. The upper end of the nozzle is connected with the peristaltic pump and the water inlet tank in sequence. device connection.

所述的填料层为不同大小形状的鹅卵石,粒径为10~40mm。所述的土柱与填料层的体积比为5.5~6∶1。所述的沉淀区为锥形,沉淀区与反应器主体的体积比5~6%。所述的圆盘的直径与反应器内径相同,圆盘内均匀分布孔径为3~5mm的小孔。所述的多个取泥口的间距为8~9cm。所述的时控器通过编程控制蠕动泵的定时通断电,使蠕动泵每隔3~3.2h进一次水,每次进水时间2~3min。所述的喷头的直径与反应器内径相同,喷头布满喷嘴,喷嘴直径为1~2mm。所述的反应器主体的高径比为:4~5∶1。所述的土柱为水稻田的土壤。The filler layer is pebbles of different sizes and shapes, with a particle diameter of 10-40 mm. The volume ratio of the soil column to the filler layer is 5.5-6:1. The precipitation area is conical, and the volume ratio of the precipitation area to the reactor main body is 5-6%. The diameter of the disc is the same as the inner diameter of the reactor, and small holes with a diameter of 3-5 mm are uniformly distributed in the disc. The distance between the plurality of mud-taking ports is 8-9 cm. The time controller controls the timing power-on and power-off of the peristaltic pump through programming, so that the peristaltic pump is fed with water every 3-3.2 hours, and the water-intake time is 2-3 minutes each time. The diameter of the nozzle is the same as the inner diameter of the reactor, the nozzle is covered with nozzles, and the diameter of the nozzle is 1-2 mm. The aspect ratio of the reactor main body is 4-5:1. The soil column is the soil of paddy field.

本发明与现有技术相比具有的有益效果:1)反应器主体呈柱状,取相应深度土层于反应器中,建立模拟自然环境的土柱,维持土壤原生态系统,保证了土壤菌群结构的原始存在状态,有利于土壤中厌氧氨氧化菌的富集;2)反应器填料层的设置,可有效防止反应内水流的堵塞和土壤的大量流失,具有较好的生物持留能力,并可起到支撑作用;3)土柱层和填料层间带孔的带孔隔板可有效阻隔土壤,减少土壤的流失,并使土柱层的水顺利下流;4)时控设备实现了反应器的间歇性进水,其瞬时产生较大的水压可使其连接的喷淋设备产生大量小水滴,实现了反应器内均匀布水;5)此富集系统完全模拟原生态,可富集土壤生态系统中的厌氧氨氧化菌,扩大厌氧氨氧化菌的种群范围,可为深入研究土壤厌氧氨氧化作用及其在土壤氮素循环中的贡献奠定良好的基础。Compared with the prior art, the present invention has beneficial effects: 1) The main body of the reactor is columnar, and the corresponding depth of soil layer is taken in the reactor to establish a soil column simulating the natural environment, maintain the original ecological system of the soil, and ensure the soil flora The original state of the structure is conducive to the enrichment of anammox bacteria in the soil; 2) The setting of the reactor packing layer can effectively prevent the blockage of the water flow in the reaction and the large loss of soil, and has a good biological retention capacity. And can play a supporting role; 3) The perforated partition with holes between the soil column layer and the filler layer can effectively block the soil, reduce soil loss, and make the water in the soil column layer flow down smoothly; 4) The time control equipment realizes The intermittent water inflow to the reactor can generate a large water pressure instantaneously, which can make the connected spray equipment produce a large number of small water droplets, and realize the uniform water distribution in the reactor; 5) This enrichment system completely simulates the original ecology, and can Enriching the anammox bacteria in the soil ecosystem and expanding the population range of anammox bacteria can lay a good foundation for in-depth research on soil anammox and its contribution to the soil nitrogen cycle.

附图说明Description of drawings

图1是模拟天然环境的土壤厌氧氨氧化富集系统结构示意图;Fig. 1 is a schematic diagram of the structure of the soil anammox enrichment system simulating the natural environment;

图2是本发明的带孔圆盘结构示意图;Fig. 2 is a structural schematic diagram of the disc with holes of the present invention;

图3是本发明的喷头结构示意图;Fig. 3 is a schematic diagram of the nozzle structure of the present invention;

图中:进水箱1、蠕动泵2、时控器3、反应器主体4、喷头5、土柱6、带孔圆盘7、支架8、排水管9、沉淀区10、排泥管11、填料层12、取泥口13、圆盘圆孔14、喷头圆孔15。In the figure: water inlet tank 1, peristaltic pump 2, time controller 3, reactor main body 4, nozzle 5, soil column 6, disc with holes 7, bracket 8, drain pipe 9, sedimentation area 10, mud discharge pipe 11 , Filling layer 12, get mud opening 13, disc circular hole 14, nozzle circular hole 15.

具体实施方式Detailed ways

如附图所示模拟自然环境的土壤厌氧氨氧化菌富集系统包括进水箱1、蠕动泵2、时控器3、反应器主体4、喷头5、土柱6、带孔圆盘7、支架8、排水管9、沉淀区10、排泥管11、填料层12、取泥口13、圆盘圆孔14、喷头圆孔15,反应器主体4下部设有支架8,反应器主体4内从上到下依次设有喷头5、土柱6、带孔圆盘7、填料层12、沉淀区10,反应器主体4底部设有排水管9、排泥管11,在反应器主体4放土柱6的侧壁上设多个取泥口13,喷头5上端与蠕动泵2、进水箱1依次连接,蠕动泵2与时控器3连接。As shown in the accompanying drawing, the soil anammox bacteria enrichment system simulating the natural environment includes a water inlet tank 1, a peristaltic pump 2, a time controller 3, a reactor body 4, a nozzle 5, a soil column 6, and a disc with holes 7 , support 8, drainage pipe 9, settling area 10, mud discharge pipe 11, packing layer 12, mud intake 13, disc hole 14, nozzle hole 15, the lower part of the reactor main body 4 is provided with a support 8, and the reactor main body 4 is provided with nozzle 5, soil column 6, perforated disc 7, packing layer 12, sedimentation area 10 in order from top to bottom, and the bottom of reactor main body 4 is provided with drainage pipe 9 and mud discharge pipe 11. 4. A plurality of mud intakes 13 are established on the side wall of the soil column 6. The upper end of the nozzle 5 is connected with the peristaltic pump 2 and the water inlet tank 1 in sequence, and the peristaltic pump 2 is connected with the time controller 3.

所述的填料层12为不同大小形状的鹅卵石,粒径为10~40mm。所述的土柱6与填料层12的体积比为5.5~6∶1。所述的沉淀区10为锥形,沉淀区10与反应器主体4的体积比5~6%。所述的圆盘7的直径与反应器内径相同,圆盘内均匀分布孔径为3~5mm的小孔14。所述的多个取泥口13的间距为8~9cm。所述的时控器3通过编程控制蠕动泵2的定时通断电,使蠕动泵每隔3~3.2h进一次水,每次进水时间2~3min。所述的喷头5的直径与反应器内径相同,喷头布满喷嘴15,喷嘴直径为1~2mm。所述的反应器主体4的高径比为:所述的土柱6为水稻田的土壤。The filler layer 12 is pebbles of different sizes and shapes, with a particle diameter of 10-40mm. The volume ratio of the soil column 6 to the filler layer 12 is 5.5˜6:1. The precipitation zone 10 is conical, and the volume ratio of the precipitation zone 10 to the reactor main body 4 is 5-6%. The diameter of the disc 7 is the same as the inner diameter of the reactor, and small holes 14 with a diameter of 3-5 mm are evenly distributed in the disc. The distance between the plurality of mud-taking ports 13 is 8-9 cm. The time controller 3 controls the timing power on and off of the peristaltic pump 2 through programming, so that the peristaltic pump feeds water every 3 to 3.2 hours, and the time for each water feed is 2 to 3 minutes. The diameter of the nozzle 5 is the same as the inner diameter of the reactor, and the nozzle 15 is covered with the nozzle, and the diameter of the nozzle is 1-2 mm. The aspect ratio of the reactor main body 4 is: the soil column 6 is the soil of a paddy field.

本发明反应器主体由有机玻璃制成,外形呈圆筒状。反应器主体内从上到下依次设有喷头、土柱、带孔圆盘、填料层、沉淀区。在土柱上部预留一定空间,用于暂时积存进水。土柱层填充了不同深度的土层,维持土壤原生态系统,保证土壤菌群结构的原始存在状态,有利于土壤中厌氧氨氧化菌的富集;填料层填充不同大小形状的鹅卵石,可有效防止反应内水流的堵塞和土壤的大量流失,起到过滤和支撑作用,保证了反应器具有较好的生物持留能力。反应器主体底部设有沉淀区,可以沉淀运行初期上部带出的部分土壤,防止了出水管的堵塞,沉淀区沉积的过多土壤,可从反应器底部的排泥管排出。并以天然湖水作为进水,人为向其添加适量氨氮、亚硝氮和硝氮,目的是加快土壤厌氧氨氧化菌的富集。通过时控器设置的命令控制蠕动泵实现反应器内间歇进水。进水经喷淋装置后形成大量小水滴,均匀洒布于反应器土层表面。水体在土柱中慢慢下渗,经带圆孔的圆盘后进入填料层,部分被带出的土壤可被填料所拦截,水体则继续下流,经出水管流出。整个富集系统实现了间歇运行。The main body of the reactor of the present invention is made of plexiglass and has a cylindrical shape. The main body of the reactor is sequentially provided with a nozzle, a soil column, a disc with holes, a packing layer, and a sedimentation area from top to bottom. A certain space is reserved on the upper part of the soil column for temporarily accumulating water. The soil column layer is filled with soil layers of different depths to maintain the original soil ecosystem and ensure the original state of the soil flora structure, which is conducive to the enrichment of anammox bacteria in the soil; the filler layer is filled with pebbles of different sizes and shapes, which can It effectively prevents the clogging of the water flow in the reaction and the massive loss of soil, plays the role of filtering and supporting, and ensures that the reactor has a good bioretention capacity. There is a settling area at the bottom of the main body of the reactor, which can settle part of the soil brought out from the upper part at the initial stage of operation, preventing the blockage of the outlet pipe. Excessive soil deposited in the settling area can be discharged from the sludge discharge pipe at the bottom of the reactor. The natural lake water is used as the influent, and an appropriate amount of ammonia nitrogen, nitrite nitrogen and nitrate nitrogen is artificially added to it, in order to accelerate the enrichment of soil anammox bacteria. The peristaltic pump is controlled by the command set by the time controller to realize intermittent water feeding in the reactor. After the incoming water passes through the spray device, a large number of small water droplets are formed, which are evenly distributed on the surface of the soil layer of the reactor. The water body slowly infiltrates in the soil column, and enters the filler layer after passing through the disc with round holes. Part of the soil that is brought out can be intercepted by the filler, and the water body continues to flow down and flows out through the outlet pipe. The entire enrichment system realizes intermittent operation.

Claims (10)

1. the soil anaerobic ammonoxidation bacterium concentrating system of a simulating natural environment, it is characterized in that comprising inlet chest (1), peristaltic pump (2), time controller (3), reactor body (4), shower nozzle (5), earth pillar (6), disk with holes (7), support (8), water shoot (9), settling region (10), shore pipe (11), packing layer (12), get mud mouth (13), disk circular hole (14), shower nozzle circular hole (15), reactor body (4) bottom is provided with support (8), be provided with shower nozzle (5) in the reactor body (4) from top to bottom successively, earth pillar (6), disk with holes (7), packing layer (12), settling region (10), reactor body (4) bottom is provided with water shoot (9), shore pipe (11), put at reactor body (4) on the sidewall of earth pillar (6) and establish a plurality of mud mouths (13) of getting, shower nozzle (5) upper end and peristaltic pump (2), inlet chest (1) connects successively, and peristaltic pump (2) is connected with time controller (3).
2. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1 is characterized in that described packing layer (12) is the pebbles of different size shape, and particle diameter is 10~40mm.
3. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1 is characterized in that the described earth pillar (6) and the volume ratio of packing layer (12) are 5.5~6: 1.
4. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1 is characterized in that described settling region (10) is taper, the volume ratio 5~6% of settling region (10) and reactor body (4).
5. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1 is characterized in that the diameter of described disk (7) is identical with reactor inside diameter, and the uniform distribution aperture is the aperture (14) of 3~5mm in the disk.
6. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1 is characterized in that described a plurality of spacing of getting mud mouth (13) is 8~9cm.
7. the soil anaerobic ammonoxidation bacterium concentrating system of a kind of simulating natural environment according to claim 1, it is characterized in that the timing power on/off of described time controller (3) by programming Control peristaltic pump (2), make peristaltic pump advance water one time, each flooding time 2~3min every 3~3.2h.
8. the soil anaerobic ammonia oxidation enrichment system of a kind of simulating natural environment according to claim 1 is characterized in that the diameter of described shower nozzle (5) is identical with reactor inside diameter, and shower nozzle is covered with nozzle (15), and nozzle diameter is 1~2mm.
9. the soil anaerobic ammonia oxidation enrichment system of a kind of simulating natural environment according to claim 1 is characterized in that the aspect ratio of described reactor body (4) is: 4~5: 1.
10. the soil anaerobic ammonia oxidation enrichment system of a kind of simulating natural environment according to claim 1 is characterized in that described earth pillar (6) is the soil of rice terrace.
CN 200910155264 2009-12-10 2009-12-10 Soil anammox bacterium gathering system simulating natural environment Expired - Fee Related CN101735947B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200910155264 CN101735947B (en) 2009-12-10 2009-12-10 Soil anammox bacterium gathering system simulating natural environment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200910155264 CN101735947B (en) 2009-12-10 2009-12-10 Soil anammox bacterium gathering system simulating natural environment

Publications (2)

Publication Number Publication Date
CN101735947A true CN101735947A (en) 2010-06-16
CN101735947B CN101735947B (en) 2013-02-06

Family

ID=42459978

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200910155264 Expired - Fee Related CN101735947B (en) 2009-12-10 2009-12-10 Soil anammox bacterium gathering system simulating natural environment

Country Status (1)

Country Link
CN (1) CN101735947B (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101955826A (en) * 2010-08-27 2011-01-26 浙江大学 Integrated aerobic/anaerobic safety methane biological desulfurization device
CN102267762A (en) * 2011-07-12 2011-12-07 天津城市建设学院 Intermittent water seepage type salt-alkali resistant plant-soil ecological filter bed
CN102464406A (en) * 2010-11-09 2012-05-23 中国科学院生态环境研究中心 Method for realizing biological denitrification of anaerobic ammonia oxidation by utilizing constructed wetland
CN102531177A (en) * 2010-12-13 2012-07-04 中国科学院生态环境研究中心 Method for improving nitration reaction rate of wetland system
CN107064463A (en) * 2017-04-28 2017-08-18 中国农业科学院农田灌溉研究所 Buried soil column leaching device
CN108802336A (en) * 2018-06-26 2018-11-13 青岛海洋地质研究所 It is a kind of to be used to measure wetland purification polluted by nitrogen efficiency and the stable state culture device of nitrogen cycle
CN111547866A (en) * 2020-06-11 2020-08-18 北京工业大学 Device and method for culturing and enriching anaerobic ammonium oxidation sludge

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2581440Y (en) * 2002-11-28 2003-10-22 南京龙源环保有限公司 Purifier for high turbidity waste water
CN101195803A (en) * 2007-12-25 2008-06-11 浙江大学 An anammox bacteria enrichment device
CN201222060Y (en) * 2008-06-10 2009-04-15 中国农业科学院农业资源与农业区划研究所 Apparatus for testing eluviation, migration and inversion of foreign material in soil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2581440Y (en) * 2002-11-28 2003-10-22 南京龙源环保有限公司 Purifier for high turbidity waste water
CN101195803A (en) * 2007-12-25 2008-06-11 浙江大学 An anammox bacteria enrichment device
CN201222060Y (en) * 2008-06-10 2009-04-15 中国农业科学院农业资源与农业区划研究所 Apparatus for testing eluviation, migration and inversion of foreign material in soil

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
唐崇俭: "厌氧氨氧化菌富集培养技术的研究与应用", 《化工进展》 *

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101955826A (en) * 2010-08-27 2011-01-26 浙江大学 Integrated aerobic/anaerobic safety methane biological desulfurization device
CN101955826B (en) * 2010-08-27 2013-01-30 浙江大学 Integrated aerobic/anaerobic safety methane biological desulfurization device
CN102464406A (en) * 2010-11-09 2012-05-23 中国科学院生态环境研究中心 Method for realizing biological denitrification of anaerobic ammonia oxidation by utilizing constructed wetland
CN102531177A (en) * 2010-12-13 2012-07-04 中国科学院生态环境研究中心 Method for improving nitration reaction rate of wetland system
CN102267762A (en) * 2011-07-12 2011-12-07 天津城市建设学院 Intermittent water seepage type salt-alkali resistant plant-soil ecological filter bed
CN107064463A (en) * 2017-04-28 2017-08-18 中国农业科学院农田灌溉研究所 Buried soil column leaching device
CN108802336A (en) * 2018-06-26 2018-11-13 青岛海洋地质研究所 It is a kind of to be used to measure wetland purification polluted by nitrogen efficiency and the stable state culture device of nitrogen cycle
CN108802336B (en) * 2018-06-26 2023-10-31 青岛海洋地质研究所 A steady-state cultivation device for measuring the nitrogen pollution efficiency and nitrogen cycle of wetlands
CN111547866A (en) * 2020-06-11 2020-08-18 北京工业大学 Device and method for culturing and enriching anaerobic ammonium oxidation sludge

Also Published As

Publication number Publication date
CN101735947B (en) 2013-02-06

Similar Documents

Publication Publication Date Title
CN101735947B (en) Soil anammox bacterium gathering system simulating natural environment
CN102754613B (en) An integrated circulating aquaculture system
CN101898856B (en) Subsurface flow constructed wetland system of secondary effluent from sewage treatment plant and application thereof
CN102923857A (en) Anoxic-aerobic vertical flow artificial wetland system
CN103864216B (en) Wavy subsurface flow constructed wetland landscape water body treatment system and treatment process thereof
CN103466900B (en) Method and device for deeply treating livestock and poultry breeding sewage
CN104828951A (en) Enhanced carbon-nitrogen synchronous removing system of ecological control type artificial wetland
CN101704585B (en) Progressively reduced aeration subsurface constructed wetland
CN204474503U (en) A kind of country sewage drips the ecological canal treatment system of filter
CN104986917A (en) Landscape type integrated sewage treatment system
CN203768123U (en) Wavy subsurface-flow constructed wetland landscape water body treatment system
CN104030524B (en) Seasonal aeration domestic sewage deep denitrification process and device
CN109384305A (en) A kind of tidal type biological aerated filter and sewage water treatment method
CN103663710A (en) Vertical-flow self-aeration annular artificial wetland system
CN107892446A (en) Continuum micromeehanics regulating level vertical subsurface flow wetland device
CN114477450A (en) Enhanced domestic sewage nitrogen and phosphorus removal treatment device and treatment method
CN109704468B (en) Stepped constructed wetland
CN108675443B (en) A kind of anaerobic granular sludge expanded bed reactor and start-up and operation method
CN201010585Y (en) Intermittent Constructed Wetland Sewage Treatment Reactor
CN201620166U (en) A soil anammox bacteria enrichment system simulating the natural environment
CN205838679U (en) AAO type fluidized bed integration sewage disposal device
CN105174469A (en) Integrated composite stereo constructed wetland system and sewage processing method
CN206407980U (en) A kind of good artificial wet land system of oxygen supply effect
CN202164164U (en) Sewage treatment device for removing high-concentration ammonia nitrogen
CN110981114A (en) Bury formula sewage treatment device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130206

CF01 Termination of patent right due to non-payment of annual fee