JP4821809B2 - Microbial carrier manufacturing method and biological denitrification apparatus - Google Patents
Microbial carrier manufacturing method and biological denitrification apparatus Download PDFInfo
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- JP4821809B2 JP4821809B2 JP2008153634A JP2008153634A JP4821809B2 JP 4821809 B2 JP4821809 B2 JP 4821809B2 JP 2008153634 A JP2008153634 A JP 2008153634A JP 2008153634 A JP2008153634 A JP 2008153634A JP 4821809 B2 JP4821809 B2 JP 4821809B2
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- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 230000000813 microbial effect Effects 0.000 title description 4
- 241000894006 Bacteria Species 0.000 claims description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 22
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 14
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 10
- 230000001651 autotrophic effect Effects 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims description 6
- 244000005700 microbiome Species 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 description 17
- 238000009434 installation Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000004745 nonwoven fabric Substances 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 239000011550 stock solution Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241001453382 Nitrosomonadales Species 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000036961 partial effect Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000004748 cultured cell Anatomy 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000000802 nitrating effect Effects 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
本発明は、アンモニア性窒素と亜硝酸性窒素とを、独立栄養性脱窒菌(アナモックス菌)により窒素ガスに還元する微生物担体の製造方法並びに脱窒装置に関するものである。
The present invention relates to a method for producing a microorganism carrier and a denitrification apparatus that reduce ammonia nitrogen and nitrite nitrogen to nitrogen gas by autotrophic denitrifying bacteria (Anamox bacteria).
近年、排水処理の分野において、アンモニア性窒素と亜硝酸性窒素とを、独立栄養性脱窒菌であるアナモックス菌により窒素ガスに還元する処理が行われている。この菌を利用した窒素除去反応はアナモックス反応と呼ばれており、従来の硝化、脱窒法よりも効率の良い窒素除去を行うことができることが知られている。 In recent years, in the field of wastewater treatment, ammonia nitrogen and nitrite nitrogen have been reduced to nitrogen gas by anammox bacteria, which are autotrophic denitrifying bacteria. This nitrogen removal reaction using bacteria is called an anammox reaction, and it is known that nitrogen removal can be performed more efficiently than conventional nitrification and denitrification methods.
図5は従来のアナモックス菌を用いた窒素除去システムのフローである。アンモニア性窒素を含有する原水は、部分亜硝酸化槽に導入される。原水中のアンモニア性窒素は部分亜硝酸化槽でアンモニア酸化細菌による好気的硝化反応によって一部が亜硝酸性窒素に酸化される。次いで沈殿槽で夾雑物等を除去した後、生物脱窒槽に導入され、嫌気性条件下でアナモックス反応により窒素ガスに還元される。 FIG. 5 is a flow of a conventional nitrogen removal system using anammox bacteria. Raw water containing ammonia nitrogen is introduced into the partial nitritation tank. Ammonia nitrogen in raw water is partially oxidized to nitrite nitrogen by aerobic nitrification reaction by ammonia oxidizing bacteria in the partial nitrification tank. Next, after removing impurities and the like in the precipitation tank, it is introduced into a biological denitrification tank and reduced to nitrogen gas by an anammox reaction under anaerobic conditions.
アナモックス菌は独立栄養性であるため、有機物の供給が不要であることの経済的な利点と、菌転換率が小さく、余剰汚泥の発生も微少に抑えることができ、従来の硝化脱窒でみられるN2Oの発生がない等の環境的な利点がある。 Since anammox bacteria are autotrophic, they have the economic advantage of not requiring the supply of organic matter, the bacteria conversion rate is small, and the generation of excess sludge can be kept to a minimum. There are environmental advantages such as no generation of N 2 O.
しかし、アナモックス菌は酸素や残留有機物により阻害を受けやすく、増殖速度も低いので、槽内を高濃度化とするのに長時間が必要であり、高濃度化を維持するのが困難であった。 However, anammox bacteria are susceptible to inhibition by oxygen and residual organic matter, and the growth rate is low, so it takes a long time to increase the concentration in the tank, and it was difficult to maintain the high concentration. .
特許文献1には、アナモックス菌を網状物や不織布等に担持させた長尺状担体を反応槽内に垂設し、アナモックス反応により廃水中のアンモニアを窒素ガスに還元して除去する方法が開示されている。 Patent Document 1 discloses a method in which an elongated carrier in which anammox bacteria are supported on a net or nonwoven fabric is suspended in a reaction tank, and ammonia in wastewater is reduced to nitrogen gas and removed by an anammox reaction. Has been.
特許文献2には、硝化槽にアナモックス菌の包括固定ゲル又は自己造粒物、或いはアナモックス菌を表面に担持した担体を保持して、外周囲をアンモニア酸化細菌で覆った生物膜二重構造体を形成させ、この生物膜二重構造体によりアンモニア性窒素を窒素ガスに還元する方法が開示されている。
アナモックス菌を担持させた長尺状担体を利用する方法では、不織布形状の自由度が低いため、反応槽の大きさおよび形状に律束され、均等な設置が困難である。また、槽内にアナモックス菌を付着させた長尺状担体を投入する際に、不織布が多量の水分を保持しているため、投入時にかなりの労力を要し、担持させたアナモックス菌の剥離も発生する。さらに、アナモックス菌付着量の把握が困難であること、および投入した担体に占める菌体量が少ないことなどから、立ち上げ時の各種条件設定が困難である。アナモックス反応の際に生成される窒素ガスにより、不織布等の担体から剥離したアナモックス菌は浮上、流出するという問題がある。 In the method using the long carrier carrying the anammox bacteria, the degree of freedom of the nonwoven fabric shape is low, and therefore, the size and shape of the reaction tank are limited, and uniform installation is difficult. Also, when a long carrier with anammox bacteria attached to the tank is put in, the nonwoven fabric holds a large amount of moisture, so it takes a lot of labor at the time of loading, and peeling of the anammox bacteria carried is also carried out. appear. Furthermore, it is difficult to set various conditions at the time of start-up because the amount of anammox bacteria attached is difficult to grasp and the amount of cells in the loaded carrier is small. There is a problem that anammox bacteria separated from a carrier such as a nonwoven fabric float and flow out due to nitrogen gas generated during the anammox reaction.
アナモックス菌を高分子ゲルに包括固定したものは、アナモックス菌が担体から剥離するという課題は解決するものの、ゲル表面付近のアナモックス菌のみが脱窒処理として有効に作用するため、処理効率が低いという問題がある。また、アナモックス菌の自己造粒物を使用するものは、槽内を高濃度に維持できるが、アナモックス反応の際に生成される窒素ガスが自己造粒物を包括し、浮上させるため、処理効率が低く、また、自己造粒物の流出を防止する装置が必要である。さらに、アナモックス菌を表面に担持した担体を使用するものは、アナモックス菌付着量の把握が困難であり、アナモックス反応の際に生成される窒素ガスにより、担体から剥離したアナモックス菌の浮上、流出という問題があるため、槽内の微生物濃度管理が複雑であるという課題がある。 Incorporating and fixing anammox bacteria on a polymer gel solves the problem that anammox bacteria are detached from the carrier, but only anammox bacteria near the gel surface effectively act as denitrification treatment, so the processing efficiency is low There's a problem. In addition, those using anammox self-granulated materials can maintain a high concentration in the tank, but the nitrogen gas generated during the anammox reaction contains the self-granulated materials and floats, so the processing efficiency And a device for preventing the self-granulated product from flowing out is required. Furthermore, it is difficult to grasp the amount of anammox bacteria attached on the surface of the carrier carrying anammox bacteria, and the anammox bacteria separated from the carrier by the nitrogen gas produced during the anammox reaction Since there is a problem, there is a problem that the microbial concentration management in the tank is complicated.
一般的にアナモックス菌の槽外への流出を防止するために、出口付近にスクリーン等を設置する場合があるが、目詰まり解消、対策などのメンテナンスに手間がかかる。また、アナモックス反応の阻害要因である流入水中のSS対策として、沈殿槽および前処理槽を設置し、沈降分離除去やろ材によるろ過等でSSを除去しているが、設備が大きくなると共に、流入水の負荷変動に弱いという問題がある。 Generally, in order to prevent anammox bacteria from flowing out of the tank, there is a case where a screen or the like is installed near the outlet, but it takes time for maintenance such as clogging elimination and countermeasures. In addition, as a countermeasure against SS in the inflowing water, which is an inhibitory factor for the anammox reaction, a sedimentation tank and pretreatment tank are installed, and SS is removed by sedimentation and removal or filtration with a filter medium. There is a problem that it is vulnerable to fluctuations in water load.
本発明は上記のような従来技術に伴う問題を解決しようとするものであって、作業効率のよい微生物担体を用いて、アナモックス菌の担体からの剥離を抑え、反応槽内の濃度管理を容易とする排水の処理装置を提供することにある。 The present invention is intended to solve the problems associated with the prior art as described above, and by using a microbial carrier having a high working efficiency, it is possible to suppress the separation of anammox bacteria from the carrier and to easily manage the concentration in the reaction vessel. It is to provide a wastewater treatment apparatus.
本発明の要旨は、脱窒槽の内部に独立栄養性脱窒菌を充填し、脱窒槽に供給する原水中のアンモニア性窒素を窒素ガスとして連続的に除去する脱窒装置の微生物担持体において、培養したアナモックス菌を担持シートでろ過した後、ろ過面を内側にして円柱状に巻き回し、所定の幅で切断してロール状担持体を構成するもので、培養した菌体を容易に担体へ担持することができるので、自由度が高い担体を使用でき、槽内への設置も容易で作業効率がよい。また、担持体をロール状に巻き回しているので、アナモックス菌の担体からの剥離が極端に少ない。
The gist of the present invention is to cultivate a microorganism carrier of a denitrification apparatus in which an autotrophic denitrification bacterium is filled inside a denitrification tank and ammonia nitrogen in raw water supplied to the denitrification tank is continuously removed as nitrogen gas. After filtering the anammox bacteria with a support sheet, it is rolled into a cylindrical shape with the filtration surface inside, and cut into a predetermined width to form a roll-shaped support. Therefore, it is possible to use a carrier having a high degree of freedom, and it is easy to install in a tank and work efficiency is good. Moreover, since the carrier is wound in a roll shape, the peeling of the anammox bacteria from the carrier is extremely small.
脱窒槽の内部に独立栄養性脱窒菌を充填し、脱窒槽に供給する原水中のアンモニア性窒素を窒素ガスとして連続的に除去する生物脱窒装置において、片面にアナモックス菌を付着させて円柱状に巻き回した所定の幅のロール状担持体を脱窒槽に配設し、ロール状担持体の外周面を脱窒槽に内接させたもので、アナモックス菌の担体からの剥離が極端に少なく、担体内部に高濃度に固定化できる。また、槽内への設置も容易で作業効率がよい。 In a biological denitrification device that fills the inside of the denitrification tank with autotrophic denitrification bacteria and continuously removes ammonia nitrogen in the raw water supplied to the denitrification tank as nitrogen gas, anammox bacteria adheres to one side and forms a cylinder A roll-shaped carrier having a predetermined width wound around is disposed in a denitrification tank, and the outer peripheral surface of the roll-shaped carrier is inscribed in the denitrification tank, and there is extremely little peeling from the carrier of anammox bacteria, It can be immobilized at a high concentration inside the carrier. Moreover, installation in the tank is easy and work efficiency is good.
上記ロール状担持体を上下に通孔を有する押え板で挟持して、脱窒槽に内設しているので、設置場所のずれやロール状担持体の傾斜を防止すると共に、巻き戻りや水流による形状の崩れを防止している。 Since the roll-shaped carrier is sandwiched between press plates having through holes in the upper and lower sides and installed in the denitrification tank, it is possible to prevent displacement of the installation place and inclination of the roll-shaped carrier, as well as rewinding and water flow. Prevents shape collapse.
上記押え板で挟持したロール状担持体を所定の間隔を空けて脱窒槽に多段に配設すると、十分に脱窒処理を行われなかった原水も、後段のロール状担持体でアナモックス菌と接触し、脱窒処理が行われる。また、水流によりアナモックス菌がロール状担持体から剥離しても、次段のロール状担持体で捕捉することができ、槽内の微生物濃度が低くなることがない。 If the roll-shaped carrier sandwiched between the presser plates is arranged in multiple stages in the denitrification tank with a predetermined interval, the raw water that has not been sufficiently denitrified will come into contact with anammox bacteria on the subsequent roll-shaped carrier. Then, a denitrification process is performed. Further, even if the anammox bacteria are separated from the roll-shaped carrier by the water flow, they can be captured by the next-stage roll-shaped carrier, and the microorganism concentration in the tank is not lowered.
本発明は上記のように構成してあり、アナモックス菌の培養時に担体を使用することがなく、また、培養した菌体を容易に担体へ担持することができるので、自由度が高い担体を使用でき、槽内への設置も容易で作業効率がよい。また、担持体をロール状に巻き回しているので、アナモックス菌の担体からの剥離が極端に少なく、担体内部に高濃度に固定化できる。さらに、担持体を槽内に多段に設置してあるので、反応槽の小型化が可能であり、基質が均等にアナモックス菌に接触できると共に、槽内の高濃度化が容易に維持できるので、立ち上げ時の条件設定が容易である。 The present invention is configured as described above, and does not use a carrier during culturing of anammox bacteria, and since the cultured cells can be easily supported on the carrier, a carrier having a high degree of freedom is used. It is easy to install in the tank and the work efficiency is good. Further, since the carrier is wound in a roll shape, the anammox bacteria are hardly peeled off from the carrier, and can be immobilized at a high concentration inside the carrier. Furthermore, since the carrier is installed in multiple stages in the tank, it is possible to reduce the size of the reaction tank, the substrate can be uniformly contacted with anammox bacteria, and the high concentration in the tank can be easily maintained. It is easy to set conditions at startup.
図1は生物脱窒装置の縦断面図であって、密閉状の脱窒槽2の底部に接続した原液供給管3より原液を供給する。脱窒槽2に流入した原液は、上向流で上昇し、ロール状担持体4を挟持している下部の押え板5に到達する。押え板5の通孔5aから侵入した原水は、ロール状担持体4の繊維間を通過する間に繊維間に担持されているアナモックス菌6と接触し、アナモックス反応と呼ばれる脱窒処理が行われる。原液中のアンモニア性窒素及び亜硝酸性窒素は、アナモックス菌6により窒素ガスに還元され、脱窒槽2上部の排気管8より排出される。脱窒処理された処理液は、ロール状担持体4を挟持している上部の押え板5の通孔5aより流出し、脱窒槽2の上方に連通している処理水管7より流出される。 FIG. 1 is a longitudinal sectional view of a biological denitrification apparatus, and a stock solution is supplied from a stock solution supply pipe 3 connected to the bottom of a sealed denitrification tank 2. The stock solution that has flowed into the denitrification tank 2 rises in an upward flow and reaches the lower presser plate 5 that sandwiches the roll-shaped carrier 4. The raw water that has entered through the through holes 5a of the presser plate 5 comes into contact with the anammox bacteria 6 supported between the fibers while passing between the fibers of the roll-shaped carrier 4, and a denitrification process called an anammox reaction is performed. . Ammonia nitrogen and nitrite nitrogen in the stock solution are reduced to nitrogen gas by the anammox bacteria 6 and discharged from the exhaust pipe 8 above the denitrification tank 2. The denitrified treatment liquid flows out from the through hole 5a of the upper presser plate 5 sandwiching the roll-shaped carrier 4, and flows out from the treated water pipe 7 communicating above the denitrification tank 2.
脱窒槽2に内設されているロール状担持体4は、高さ方向に所定の間隔を設けて多段に設置してもよい。設置段数は脱窒槽の高さ/直径比や処理量、設定濃度等により適宜選択する。ロール状担持体4は多数の通孔5aをもった押え板5で上下を挟持されており、巻き戻りや水流による形状の崩れを防止している。押え板5は脱窒槽2の内壁に固定してあり、設置場所のずれやロール状担持体4の傾斜を防止している。 The roll-shaped carrier 4 provided in the denitrification tank 2 may be installed in multiple stages at predetermined intervals in the height direction. The number of installation stages is appropriately selected depending on the height / diameter ratio of the denitrification tank, the processing amount, the set concentration, and the like. The roll-shaped carrier 4 is sandwiched at the top and bottom by a pressing plate 5 having a large number of through-holes 5a to prevent the shape from being deformed by rewinding or water flow. The presser plate 5 is fixed to the inner wall of the denitrification tank 2 to prevent the displacement of the installation place and the inclination of the roll-shaped carrier 4.
図2は担持シートにアナモックス菌を担持させた斜視図であって、担持シート9は繊維又はフィラメントで構成される不織布、織布または網状物からなる。好ましくは成形性、強度に優れ、微生物の付着性がよく、適度な空隙率が確保できる不織布を用いる方がよい。 FIG. 2 is a perspective view in which anammox bacteria are supported on a support sheet, and the support sheet 9 is made of a nonwoven fabric, a woven fabric or a net-like material composed of fibers or filaments. It is preferable to use a nonwoven fabric that is excellent in moldability and strength, has good adhesion to microorganisms, and can ensure an appropriate porosity.
培養したアナモックス菌6を担持シート9の片側全面でろ過すると、担持シート9の繊維にアナモックス菌6が付着する。ろ過面を内周側とした状態で、担持シート9を円柱状に巻き回す。脱窒槽2の内径に相当する径まで巻き回した担持シート9を適度な厚みで切断して、図3に示すようにロール状担持体4としてある。ロール状担持体内4にアナモックス菌6を高密度に固定化することができ、ろ過面を内周側としてあるのでアナモックス菌6の剥離が少ない。高さ方向に適度な厚みがあるので、ロール状担持体4内のアナモックス菌6と原水は十分に接触できる。また、密に巻き回されているので、アナモックス菌6が自己造粒してグラニュール化してもロール状担持体4内に保持される。アナモックス反応の際に生成される窒素ガスは、繊維間を通過して脱窒槽2の上方へ浮上する。 When the cultured anammox bacteria 6 is filtered over the entire surface of one side of the carrier sheet 9, the anammox bacteria 6 adheres to the fibers of the carrier sheet 9. The carrier sheet 9 is wound into a columnar shape with the filtration surface set to the inner peripheral side. The carrier sheet 9 wound to a diameter corresponding to the inner diameter of the denitrification tank 2 is cut at an appropriate thickness to form a roll-shaped carrier 4 as shown in FIG. The anammox bacteria 6 can be fixed at a high density in the roll-shaped carrier 4 and the filtration surface is on the inner peripheral side, so that the anammox bacteria 6 is hardly peeled off. Since there is an appropriate thickness in the height direction, the anammox bacteria 6 in the roll-shaped carrier 4 and the raw water can sufficiently come into contact with each other. Moreover, since it is wound closely, the anammox bacteria 6 is retained in the roll-shaped carrier 4 even if it is granulated and granulated. Nitrogen gas generated during the anammox reaction passes between the fibers and rises above the denitrification tank 2.
ロール状担持体4の外周面は脱窒槽2に内接し、切断面が通水方向と直角であるので、ロール状に巻き回した中央部から外周部まで、脱窒槽2内を上昇する原水の上向流と均等に接触する。また、高さ方向に幅があるので、原水が通過する際に、アナモックス菌6との接触時間が長くなり、効率のよい脱窒処理を行うことができる。 Since the outer peripheral surface of the roll-shaped carrier 4 is inscribed in the denitrification tank 2 and the cut surface is perpendicular to the water flow direction, the raw water that rises in the denitrification tank 2 from the center portion wound in a roll shape to the outer peripheral portion. Make even contact with the upward flow. Further, since there is a width in the height direction, when the raw water passes, the contact time with the anammox bacteria 6 becomes long, and an efficient denitrification treatment can be performed.
図4は押え板の斜視図であって、ロール状担持体4を上下で挟持し、脱窒槽2の所定の位置に固定してある。薄板円板に多数の通孔5aが設けてあり、ロール状担持体4全面に均等に原水が流入できると共に、原水の通水を妨げて圧力損失が増大することがない。通孔5aの数や形状は、生物処理の妨げとなるものでなければ、特に何でもよく、格子状に構成されたものであってもよい。 FIG. 4 is a perspective view of the presser plate, in which the roll-shaped carrier 4 is sandwiched up and down and fixed at a predetermined position of the denitrification tank 2. A large number of through holes 5a are provided in the thin disk, so that the raw water can flow evenly over the entire surface of the roll-shaped carrier 4, and the pressure loss does not increase by preventing the raw water from flowing. The number and shape of the through holes 5a are not particularly limited as long as they do not hinder biological treatment, and may be configured in a lattice shape.
ロール状担持体4を高さ方向に一定間隔の隙間を設けて多段に設置すると、上流側のロール状担持体4で十分に脱窒処理を行われなかった原水は、後段のロール状担持体4でアナモックス菌6と接触し、脱窒処理が行われる。また、水流によりアナモックス菌6がロール状担持体4から剥離しても、後段のロール状担持体4で捕捉することができ、槽内の微生物濃度が低くなることがない。 When the roll-shaped carrier 4 is installed in multiple stages with gaps at regular intervals in the height direction, the raw water that has not been sufficiently denitrified by the upstream-side roll-shaped carrier 4 is converted into the subsequent roll-shaped carrier. 4 is contacted with anammox bacteria 6 and denitrification treatment is performed. Further, even if the anammox bacteria 6 is separated from the roll-shaped carrier 4 by the water flow, it can be captured by the subsequent roll-shaped carrier 4 and the microbial concentration in the tank is not lowered.
脱窒槽2に供給された原水に含まれる微細なSSや夾雑物やアナモックス反応により発生する余剰汚泥は、自重により脱窒槽2底部に堆積する。脱窒槽2の底部は夾雑物や余剰汚泥が堆積しやすいように円錐状が望ましく、槽外に排出するための排出管10が接続されている。また、ロール状担持体4を多段に設置する場合には、ロール状担持体4間の各隙間下方に排出管10a、10b・・・が接続してある。 Fine SS and impurities contained in the raw water supplied to the denitrification tank 2 and surplus sludge generated by the anammox reaction accumulate at the bottom of the denitrification tank 2 by its own weight. The bottom of the denitrification tank 2 is preferably conical so that impurities and excess sludge are easily deposited, and a discharge pipe 10 for discharging the tank to the outside of the tank is connected. When the roll-shaped carriers 4 are installed in multiple stages, discharge pipes 10a, 10b,... Are connected below the gaps between the roll-shaped carriers 4.
処理水管には処理水の一部を循環水として脱窒槽2に戻す循環配管11が接続されている。本実施例では、循環配管11の他端は原水供給管3に連結しているが、直接脱窒槽2に連結してもよく、また、循環用のポンプ12を用いて処理水を循環してもよい。 A circulating pipe 11 for returning a part of the treated water to the denitrification tank 2 as circulating water is connected to the treated water pipe. In this embodiment, the other end of the circulation pipe 11 is connected to the raw water supply pipe 3, but it may be directly connected to the denitrification tank 2, and the treated water is circulated using a circulation pump 12. Also good.
本発明に係る生物脱窒装置は、アナモックス菌が付着したロール状担持体により容易に槽内の高濃度化を維持管理できる。アナモックス菌の槽外への流出は極めて少ないため、流出を防止するために、出口付近にスクリーン等を設ける必要が無く、メンテナンスも容易である。初期および運転停止後の立ち上げ時でも、担持体の取出し、補充、再投入が容易であり、槽内での培養期間を必要としない。また、担持体を槽内に多段に設置することにより、負荷変動にも強くなると共に、装置の小型化が可能であり、大きな設置面積を必要としない。菌の取扱が容易で作業効率もよいので、脱窒処理を必要とする排水処理設備に容易に設置可能である。 The biological denitrification apparatus according to the present invention can easily maintain and increase the concentration in the tank by the roll-shaped carrier to which anammox bacteria adhere. Since the outflow of anammox bacteria to the outside of the tank is extremely small, it is not necessary to provide a screen or the like near the outlet in order to prevent the outflow, and maintenance is easy. The carrier can be easily taken out, replenished, and re-introduced at the initial stage and at the start-up after the operation is stopped, and no culture period in the tank is required. Further, by installing the carrier in multiple stages in the tank, it is strong against load fluctuations, and the apparatus can be miniaturized, and a large installation area is not required. Since it is easy to handle bacteria and has good work efficiency, it can be easily installed in wastewater treatment facilities that require denitrification.
1 生物脱窒装置
2 脱窒槽
4 ロール状担持体
5 押え板
5a 通孔
6 アナモックス菌
9 担持シート
DESCRIPTION OF SYMBOLS 1 Biological denitrification apparatus 2 Denitrification tank 4 Roll-shaped carrier 5 Holding plate 5a Through-hole 6 Anammox bacteria 9 Carrier sheet
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CN109734183B (en) * | 2019-03-11 | 2024-04-30 | 苏州科技大学 | Quick starting device for anaerobic ammoxidation in low-temperature environment |
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