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JPH11300379A - Biological treating device - Google Patents

Biological treating device

Info

Publication number
JPH11300379A
JPH11300379A JP12307298A JP12307298A JPH11300379A JP H11300379 A JPH11300379 A JP H11300379A JP 12307298 A JP12307298 A JP 12307298A JP 12307298 A JP12307298 A JP 12307298A JP H11300379 A JPH11300379 A JP H11300379A
Authority
JP
Japan
Prior art keywords
carrier
water
biological treatment
treated
specific gravity
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.)
Pending
Application number
JP12307298A
Other languages
Japanese (ja)
Inventor
Souetsu Kitamura
総謁 北村
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.)
Inax Corp
Original Assignee
Inax Corp
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 Inax Corp filed Critical Inax Corp
Priority to JP12307298A priority Critical patent/JPH11300379A/en
Publication of JPH11300379A publication Critical patent/JPH11300379A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the defective cleaning of a carrier in the biological treating device for aerobically purifying the water to be treated by the use of a flowable carrier carrying a microorganism. SOLUTION: A carrier T to be placed in a biological treating tank 2 is formed with a material having a specific gravity equal to or slightly lower than that of water and free of the open cells communicating with the inside. All the surface openings are communicated with any of the other surface openings, and the inside dimensions are so set that the bubbles are not caught with plural wings arranged regularly. Since the air is not held in the carrier, the apparent sp.gr. is not changed, and the carrier exhibits stabilized flowability. As the wings are furnished, the flowability is increased, and agitation is ensured.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生活排水や屎尿下
水等を、微生物の活性により浄化処理する生物的処理装
置の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a biological treatment apparatus for purifying domestic wastewater and human wastewater by the activity of microorganisms.

【0002】[0002]

【従来の技術】生活排水や屎尿下水等を微生物の分解・
同化作用を利用して浄化処理する生物的処理装置は従来
広く用いられており、様々なタイプのものが提案されて
いる。特開平6−23065号公報に、このような処理
装置の一例が記載されており、これは、微生物を担持さ
せる担体を、例えばポリウレタンフォームを用いて、水
と同程度の比重を有する立体網目構造を持つものに形成
した点を特色とする。同処理装置で浄化処理を実行する
に際しては、微生物を担持する前記担体が収納された処
理槽内へ下方部から散気管等で空気を供給することによ
り、担体に浮力を与えて浮上させ、この状態を維持した
まま被処理水を処理槽の上方から供給して担体の間を下
向きに通過させる。被処理水が担体間を通過する間に、
担体に担持される微生物によって有機物が分解又は同化
処理を受け、被処理水の浄化がなされる。
[Prior Art] Decomposition of microorganisms into domestic wastewater and human wastewater
BACKGROUND ART Biological treatment apparatuses for purifying by utilizing assimilation have been widely used, and various types of biological treatment apparatuses have been proposed. JP-A-6-23065 describes an example of such a processing apparatus. This processing apparatus uses a three-dimensional network structure having a specific gravity similar to that of water using, for example, a polyurethane foam as a carrier for supporting microorganisms. The point formed in the thing with is featured. When performing the purification treatment in the same processing apparatus, by supplying air from the lower part by a diffuser tube or the like into the processing tank in which the carrier carrying the microorganisms is stored, the carrier is given buoyancy and floated. While maintaining the state, the water to be treated is supplied from above the treatment tank and passed downward between the carriers. While the water to be treated passes between the carriers,
The organic matter is decomposed or assimilated by the microorganisms carried on the carrier, and the water to be treated is purified.

【0003】前述の処理装置において、処理能力の低下
を防ぐため、所要の時期に担体を洗浄する。担体の洗浄
処理を実行する場合、定常運転時の5〜10倍量の空気
を供給して、処理槽内に激しい気液混合流を発生させ
る。担体は処理槽内に固定されているわけではなく浮遊
状態で存在するから、気液混合流により撹拌され、その
結果、担体間に捕捉されていたSS等の固形分や増殖微
生物のフロック等が脱落し除去される。
In the above-described processing apparatus, the carrier is washed at a required time in order to prevent a reduction in processing capacity. When the carrier cleaning process is performed, air is supplied in an amount 5 to 10 times that of the normal operation to generate a strong gas-liquid mixed flow in the processing tank. Since the carrier is not fixed in the treatment tank but exists in a floating state, the carrier is stirred by a gas-liquid mixed flow, and as a result, solids such as SS and flocs of growing microorganisms trapped between the carriers are removed. Dropped and removed.

【0004】[0004]

【発明が解決しようとする課題】前記従来の生物的処理
装置は、微生物を担持する担体として、立体網目構造を
有するものを使用している。そのため、処理工程時又は
洗浄工程時に供給される空気が網目構造内に捕らえら
れ、担体内から容易には抜け出せなくなる場合がある。
空気を内部に保持する担体は、見かけ比重が減少して浮
力が増大するので、流動性の低下をきたす。また、空気
保有量の多寡に応じて担体の見かけ比重にばらつきが生
ずるので、担体の流動性が不均一になる。このような現
象の結果、効果的な洗浄が阻害され、洗浄不良を招くと
いう問題を発生させる。
The conventional biological treatment apparatus uses a carrier having a three-dimensional network structure as a carrier for supporting microorganisms. For this reason, air supplied during the processing step or the cleaning step may be trapped in the network structure and may not easily escape from the carrier.
The carrier holding air therein has a reduced apparent specific gravity and an increased buoyancy, resulting in a decrease in fluidity. Further, since the apparent specific gravity of the carrier varies depending on the amount of air holding, the fluidity of the carrier becomes uneven. As a result of such a phenomenon, there occurs a problem that effective cleaning is hindered and cleaning failure occurs.

【0005】[0005]

【課題を解決するための手段】本発明は、微生物を担持
させた流動可能な多数の担体により、被処理水を好気的
条件下で浄化処理する生物的処理装置における前記従来
の問題点を解決する手段を提供するものである。本発明
が採用する前記問題点の解決手段の特徴とするところ
は、前記担体を、比重が水と同等か又はわずかに小さ
く、且つ、内部へ通ずる連続気孔を持たない材料で形成
することにある。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems in a biological treatment apparatus for purifying treated water under aerobic conditions by using a large number of flowable carriers carrying microorganisms. It provides a means to solve. The feature of the means for solving the problems adopted by the present invention is that the carrier is formed of a material having a specific gravity equal to or slightly smaller than that of water, and having no continuous pores leading to the inside. .

【0006】さらに前記担体は、比重が水と同等か又は
わずかに小さく且つ内部へ通ずる連続気孔を持たない材
料で形成され、規則的に配置された複数の羽根体を備
え、全ての表面開口部が他のいずれかの表面開口部に連
通するように構成され、内部空間の内法寸法が気泡を捕
捉しない大きさに設定されたものとしてもよい。
Further, the carrier is formed of a material having a specific gravity equal to or slightly lower than that of water and having no continuous pores communicating with the inside, and has a plurality of regularly arranged vanes, and all surface openings are provided. May be configured to communicate with any of the other surface openings, and the internal dimension of the internal space may be set to a size that does not trap air bubbles.

【0007】微生物を担持させる担体を、比重が水と同
等か又はわずかに小さい材料で形成することにより、当
該担体は被処理水中で浮上状態に維持される。但し、比
重を水と同等か又はわずかに小さい程度としたから、多
量の空気を送給する洗浄工程時において、当該担体は必
要十分な流動性を示すことができる。また、当該担体の
形成材料を、内部へ通ずる連続気孔を持たないものとし
たから、内部に空気を取り込んで保持することがない。
それ故、担体の見かけ比重が変動するおそれがなくなる
ので、担体の流動性が均一に保たれ、良好な洗浄効果が
得られる。
[0007] By forming the carrier for supporting microorganisms from a material having a specific gravity equal to or slightly smaller than that of water, the carrier is maintained in a floating state in the water to be treated. However, since the specific gravity is set to be equal to or slightly smaller than that of water, the carrier can exhibit necessary and sufficient fluidity in the washing step of feeding a large amount of air. In addition, since the material for forming the carrier does not have continuous pores communicating with the inside, air is not taken in and held inside.
Therefore, there is no possibility that the apparent specific gravity of the carrier fluctuates, so that the fluidity of the carrier is kept uniform and a good washing effect is obtained.

【0008】なお、担体の構造を、規則的に配置された
複数の羽根体を備え、全ての表面開口部が他のいずれか
の表面開口部と連通するように構成すると共に、内部空
間の内法寸法を気泡を捕捉しない大きさに設定したもの
については、次のような機能を発揮する。まず、規則的
に配置された複数の羽根体を備えることによって、洗浄
工程時において多量の空気供給により発生する気液混合
流の作用を受けやすくなるから、担体の流動性が増し、
撹拌が確実となる。全ての表面開口部が他のいずれかの
表面開口部と連通するように構成したことによって、水
や空気が担体内を通過できるようになるから、処理工程
時にあっては被処理水と担体の微生物との接触効率が高
くなり、洗浄工程時にあっては気液混合流が担体内部に
溜まったSSや余剰フロックを除去しやすくなる。さら
に内部空間の内法寸法を気泡を捕捉しない大きさに設定
することによって、担体内に空気が保持されることがな
くなるから、担体が見かけ比重の変動をきたすおそれが
ない。
The carrier has a structure in which a plurality of blades are regularly arranged, and all the surface openings communicate with any other surface openings. When the normal size is set to a size that does not capture bubbles, the following functions are exhibited. First, by providing a plurality of regularly arranged blades, it becomes easier to receive the action of the gas-liquid mixed flow generated by a large amount of air supply during the cleaning process, so the fluidity of the carrier increases,
Stirring is assured. Since all the surface openings are configured to communicate with any other surface openings, water and air can pass through the carrier. The efficiency of contact with microorganisms is increased, and during the washing step, the gas-liquid mixed flow can easily remove SS and excess flocs accumulated inside the carrier. Further, by setting the inner dimension of the internal space to a size that does not trap air bubbles, air is no longer retained in the carrier, so that there is no possibility that the carrier will fluctuate in apparent specific gravity.

【0009】ところで、前記の羽根体を備える担体を使
用する場合、大小の担体を混在させて用いてもよく、ま
た比重が水と同等か又はわずかに小さい材料で形成され
た羽根体を持たない担体を混在させてもよい。羽根体を
備える担体は流動エネルギーを受けやすいから、羽根体
を持たない担体が適当量混在していても、洗浄工程時に
確実な撹拌状態を現出させることが可能である。
In the case where a carrier having the above-mentioned blade body is used, large and small carriers may be used in combination, and there is no blade body made of a material having a specific gravity equal to or slightly smaller than that of water. Carriers may be mixed. Since the carrier having the blade body is liable to receive the flow energy, even if the carrier without the blade body is mixed in an appropriate amount, it is possible to cause a reliable stirring state to appear during the washing step.

【0010】なお、前記担体が収納される処理槽におけ
る被処理水の貯留水位よりやや下方の位置に、担体の通
過を阻止する押さえ部材を設けてもよい。押さえ部材に
よって、担体全部が被処理水中に浸漬されるので、被処
理水と不接触の部分が生じない。また被処理水の水面領
域には固形物が溜まり易いが、押さえ部材で担体を水面
下に保持するので、担体と固形物との接触を避けること
ができる。
[0010] A holding member for preventing passage of the carrier may be provided at a position slightly below the storage level of the water to be treated in the treatment tank in which the carrier is stored. Since the entire carrier is immersed in the water to be treated by the pressing member, there is no portion that is not in contact with the water to be treated. Further, although solids tend to accumulate in the water surface area of the water to be treated, the carrier is held below the water surface by the pressing member, so that contact between the carrier and the solids can be avoided.

【0011】[0011]

【発明の実施の形態】〔第1の実施形態〕図1及び図2
に、本発明に係る生物的処理装置1の一例を示す。この
処理装置1は、被処理水を微生物の生物化学的活性によ
り浄化処理する生物処理槽2と、生物処理槽2で浄化処
理して得られた処理水を一時貯留する処理水分離槽3と
を一体的に連設して構成したものである。生物処理槽2
は、微生物を担持させる担体Tが多数収納され、下方部
に曝気手段4が配設されている。曝気手段4は、2基の
ブロワー5,6と、それぞれに接続した散気管7,8と
からなり、通常の浄化処理工程時には一方のブロワー5
及び散気管7のみ使用し、洗浄工程時には、もう一方の
洗浄用ブロワー6及び散気管8を使用するか、又は、両
方のブロワー5,6及び散気管7,8を用いることによ
り、空気の供給量を増大させる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS First Embodiment FIGS. 1 and 2
FIG. 1 shows an example of the biological treatment device 1 according to the present invention. The treatment apparatus 1 includes a biological treatment tank 2 for purifying treated water by the biochemical activity of microorganisms, a treated water separation tank 3 for temporarily storing treated water obtained by purifying treatment water in the biological treatment tank 2, Are integrally connected to each other. Biological treatment tank 2
Has a large number of carriers T for carrying microorganisms, and an aeration unit 4 is provided below. The aeration means 4 is composed of two blowers 5, 6 and diffuser tubes 7, 8 connected to the two blowers, respectively.
In the cleaning process, only the air blower 7 and the other air blower 6 and the air diffuser 8 are used, or both the blowers 5 and 6 and the air diffusers 7 and 8 are used to supply air. Increase volume.

【0012】処理水分離槽3は、生物処理槽2と底部付
近で連通部9を通じて連絡し、流入した処理水は上部か
ら外部へ流出するようになされている。処理水中に混入
しているわずかな固形分は、分離槽3内に貯留されてい
る間に沈降する。底部に溜まった沈殿物は、適宜の排出
手段20により抜き出して、別途設けられる固形物貯留
槽へ移送するか、または生物処理槽2の上流に設けられ
ている嫌気処理槽等へ循環返送される。なお必要に応
じ、沈殿物を排出手段20付近へ案内するための傾斜面
構造Nを、分離槽3の底部に設けてもよい。
The treated water separation tank 3 communicates with the biological treatment tank 2 near the bottom through a communication portion 9 so that the inflowed treated water flows out from the top to the outside. A small amount of solids mixed in the treated water settles while being stored in the separation tank 3. The sediment accumulated at the bottom is extracted by an appropriate discharging means 20 and transferred to a separately provided solid storage tank, or is circulated and returned to an anaerobic treatment tank provided upstream of the biological treatment tank 2. . If necessary, an inclined surface structure N for guiding the sediment to the vicinity of the discharge means 20 may be provided at the bottom of the separation tank 3.

【0013】生物処理槽2の担体Tが分離槽3へ移行す
るのを防止するため、図1(a)では、生物処理槽2内
における散気管7よりやや上方の位置に、担体分離板1
0が設けられる。あるいは、散気管7,8より、やや下
方の位置に設けてもよい。担体分離板10は、例えば多
孔板や網体などから成り、水や空気等の流体は容易に通
過できるが、担体Tは通過させないように構成されてい
る。なお、担体分離板10を設ける位置は、図1(b)
のように、生物処理槽2と分離槽3との境界に位置する
連通部9であってもよい。
In order to prevent the carrier T in the biological treatment tank 2 from migrating to the separation tank 3, in FIG. 1A, the carrier separation plate 1 is located at a position slightly above the air diffuser 7 in the biological treatment tank 2.
0 is provided. Alternatively, it may be provided at a position slightly lower than the air diffusers 7 and 8. The carrier separation plate 10 is made of, for example, a perforated plate or a mesh body, and is configured such that a fluid such as water or air can easily pass through, but does not allow the carrier T to pass. The position where the carrier separation plate 10 is provided is shown in FIG.
The communication part 9 located at the boundary between the biological treatment tank 2 and the separation tank 3 may be used.

【0014】生物処理槽2に収納され微生物を担持させ
る担体Tは、例えばポリプロピレンやポリエチレンなど
の合成樹脂で製作され、その比重が水の比重と同等か又
はわずかに小さい程度(具体的には0.800〜0.9
99の範囲)に設定される。生物処理槽2に供給される
被処理水の比重は、通常、水よりも若干大きいと考えら
れるので、担体の比重を水の比重以下とすることによ
り、担体を生物処理槽2内で浮上させることができる。
しかも、水の比重と同等か又はわずかに小さい程度に設
定してあるから、担体重量に対する浮力の比率が過大に
なって流動性を失うおそれがなく、担体は程よく水面下
になじむ。また当該担体は、内部へ通ずる連続気孔を持
たない材質で形成するから、空気が内部に取り込まれて
保持されることがなく、それ故、見かけ比重の変動を招
くおそれがない。
The carrier T accommodated in the biological treatment tank 2 and supporting microorganisms is made of, for example, a synthetic resin such as polypropylene or polyethylene, and has a specific gravity equal to or slightly smaller than that of water (specifically, 0). .800-0.9
99 range). Since the specific gravity of the water to be treated supplied to the biological treatment tank 2 is usually considered to be slightly larger than that of water, the carrier is floated in the biological treatment tank 2 by setting the specific gravity of the carrier to the specific gravity of water or less. be able to.
Further, since the specific gravity is set to be equal to or slightly smaller than the specific gravity of water, there is no possibility that the ratio of buoyancy to the weight of the carrier becomes excessively large and the fluidity is not lost, and the carrier fits under the water surface moderately. Further, since the carrier is formed of a material having no continuous pores leading to the inside, air is not taken in and held inside, and therefore, there is no possibility of causing a change in apparent specific gravity.

【0015】担体Tの具体的な形状は、特に限定される
ものではないが、内部に気泡を保持するおそれがなく、
また隣接する担体どうしが分かち難く噛み合うことの無
いものとすることが望ましい。図3に例示する担体T
は、8枚の同形の羽根体Hを中心軸Pから等角度(45
度)で放射状に配置して構成したものであって、平面形
状及び正面形状はほぼ正八角形を呈し、全体形状は多面
体を呈する。羽根体Hの高さ方向中央位置には、隣接す
る羽根体H,Hどうしを連結する細幅の連結部材Jが設
けられる。図4の担体Tは、前記図3の担体Tにおける
中心軸Pを、中空の円筒軸Qに変更したものである。ま
た図5の担体Tは、中心部へ3個のリング体Rを同軸的
に配し、これらリング体Rの周囲に羽根体Hを放射状に
配置したものである。さらに図6に示す担体Tは、中心
部に配したリング体Rの周りに4分の1円形の羽根体H
を配して全体形状をほぼ球体に成すと共に、環状の連結
部材Jの上側と下側とで、羽根体位置が異なるように成
した。すなわち、上側の各羽根体H(u)に対し、下側
の各羽根体H(d)が、隣接する羽根体H,Hが成す角
度(30度)の半分だけ位置がずれるように構成されて
いる。
The specific shape of the carrier T is not particularly limited, but there is no possibility of retaining air bubbles therein,
It is also desirable that adjacent carriers are difficult to share and do not mesh with each other. The carrier T illustrated in FIG.
Means that eight identical blades H are equiangular (45
Degrees), and the plane shape and the front shape are almost regular octagons, and the whole shape is a polyhedron. At the center of the blade body H in the height direction, a narrow connecting member J for connecting adjacent blade bodies H, H is provided. The carrier T of FIG. 4 is obtained by changing the center axis P of the carrier T of FIG. 3 to a hollow cylindrical axis Q. The carrier T shown in FIG. 5 has three ring members R arranged coaxially at the center, and wing members H arranged radially around these ring members R. Further, the carrier T shown in FIG. 6 has a quarter circular blade body H around a ring body R arranged at the center.
And the entire shape is substantially spherical, and the upper and lower sides of the annular connecting member J have different blade positions. In other words, the lower blades H (d) are configured such that the lower blades H (d) are displaced from the upper blades H (u) by half the angle (30 degrees) formed by the adjacent blades H, H. ing.

【0016】図3乃至図6に例示する如き羽根体Hを備
えた担体Tは、次のような特質を持つ。まず、複数の羽
根体Hを備えることにより、水や空気の流動エネルギー
を受けやすくなるから、流動性が向上する。また比表面
積が増大するから、担体T一個当たりの微生物保持量が
多くなり、被処理水の処理能力が高まる。連結部材J
は、羽根体Hの変形を防いで強度を高めると共に、担体
Tどうしが羽根体Hの部分で噛み合うのを阻止する役割
を果たす。羽根体Hや連結部材J等で囲まれる担体Tの
内部空間Sは、いずれも少なくとも2方が開口する開空
間に形成されている。すなわち、任意の開口部K(図
中、網かけで示す)はいずれか他の開口部Kに連通する
よう構成されているから、水や空気が担体T内を容易に
流通することができ、被処理水と担体Tに担持させた微
生物との接触効率が良好である。さらに、担体Tの内部
空間の内法寸法が、気泡を捕捉しないような大きさに設
定されているから、気泡を内部に保持して見かけ比重を
変動させる、というおそれがない。
The carrier T provided with the blade body H as illustrated in FIGS. 3 to 6 has the following characteristics. First, by providing a plurality of blades H, it becomes easier to receive the flow energy of water or air, so that the flowability is improved. Further, since the specific surface area increases, the amount of microorganisms retained per carrier T increases, and the treatment capacity of the water to be treated increases. Connecting member J
Plays a role in preventing deformation of the blade body H to increase the strength and preventing the carriers T from meshing with each other at the portion of the blade body H. The inner space S of the carrier T surrounded by the blade body H, the connecting member J, and the like is formed as an open space in which at least two sides are open. That is, since any opening K (shown by hatching in the figure) is configured to communicate with any other opening K, water or air can easily flow through the carrier T, The contact efficiency between the water to be treated and the microorganisms carried on the carrier T is good. Furthermore, since the internal dimension of the internal space of the carrier T is set to a size that does not trap air bubbles, there is no danger that the air bubbles will be held inside and the apparent specific gravity will fluctuate.

【0017】担体Tが前記特質を発揮するには、以下に
述べるような条件を満たすことが望ましい。まず、担体
Tの大きさは直径5〜50mmの範囲とする。直径が5
mm未満であると、内部空間が狭くなって気泡を保持し
やすくなる。直径が50mmを越えると、比表面積が小
さくなるので、単位体積当たりの微生物保持量や被処理
水との接触量が少なくなり、処理効率が低下する。そこ
で、担体Tの好ましい直径の値は前記範囲とする。微生
物の担持量を確保すると共に流動エネルギーを受けやす
くするため、羽根体Hの総表面積は、当該担体Tを中実
体であると仮定したときの表面積の3分の1以上となる
ようにする。担体Tの内部空間Sを水や空気が流通でき
且つ内部空間Sに気泡が捕捉されないようにするための
条件は、各開口部Kの開口面積を4mm2 以上とすると
共に、直径1mmの球が、内部空間Sを構成する3面以
上と同時に接することなく当該内部空間S内を移動でき
るように内法寸法を設定することである。
In order for the carrier T to exhibit the above characteristics, it is desirable that the following conditions are satisfied. First, the size of the carrier T is in a range of 5 to 50 mm in diameter. 5 in diameter
If it is less than mm, the internal space is narrowed and air bubbles are easily held. When the diameter exceeds 50 mm, the specific surface area becomes small, so that the amount of microorganisms retained per unit volume and the amount of contact with the water to be treated decrease, and the treatment efficiency decreases. Therefore, the preferable value of the diameter of the carrier T is set in the above range. In order to secure the amount of microorganisms to be carried and to easily receive the flow energy, the total surface area of the blade body H is set to be one third or more of the surface area when the carrier T is assumed to be a solid body. Conditions for allowing water and air to flow through the internal space S of the carrier T and preventing air bubbles from being trapped in the internal space S are as follows: the opening area of each opening K is 4 mm 2 or more, and a sphere having a diameter of 1 mm Is to set the inner dimension so that the inner space S can move in the inner space S without simultaneously touching three or more surfaces constituting the inner space S.

【0018】前述の如く構成された生物的処理装置1に
おける被処理水の浄化処理は、次の如く実行される。生
物処理槽2における担体分離板10より上方の上流領域
が有効処理空間となされ、ここに担体Tが収納される。
担体Tの充填率は、担体Tの流動性を確保するため、通
常は、有効処理空間の約50〜85%とされる。生物処
理槽2に担体Tを収納し、被処理水を供給すると、担体
Tはその比重が被処理水よりもわずかに小さいから浮力
を受けて浮上し、図1(a)に示す如く生物処理槽2の
上方領域に生物濾過層Fを形成する。好気的処理を行う
ため、曝気手段4の一方の散気管7から槽2内へ空気を
送り込む。その供給量は、生物濾過層Fを形成している
担体Tが流動しない程度に調節され、例えば有効処理空
間1m3当たり0.1〜10.0m3 /時の割合とす
る。この状態において、上方部から生物処理槽2内へ被
処理水を少しずつ送給すると、被処理水が担体Tの間隙
を縫って下方へ流動する間に、被処理水中に含まれる有
機物が担体T表面に担持されている微生物によって分解
又は同化され、その結果、被処理水の浄化が進行する。
浄化処理を受けて得られる処理水は、生物処理槽2の底
部から連通部9を通って分離槽3へ移行する。処理水中
に含まれるわずかな固形物は分離槽3で沈降分離され、
上澄み液だけが外部へ排出される。分離槽3の底部に溜
まった沈殿物は、適宜の排出手段20により引き抜いて
排除する。
The treatment of the water to be treated in the biological treatment apparatus 1 constructed as described above is executed as follows. The upstream area above the carrier separation plate 10 in the biological treatment tank 2 is an effective treatment space, and the carrier T is stored therein.
The filling rate of the carrier T is usually about 50 to 85% of the effective processing space in order to secure the fluidity of the carrier T. When the carrier T is stored in the biological treatment tank 2 and the water to be treated is supplied, the carrier T receives buoyancy because the specific gravity of the carrier T is slightly smaller than the water to be treated, and floats. As shown in FIG. The biological filtration layer F is formed in the upper region of the tank 2. In order to perform aerobic treatment, air is sent into the tank 2 from one of the air diffusers 7 of the aeration means 4. The supply amount is adjusted so that the carrier T forming the biological filtration layer F does not flow, and is set to, for example, a rate of 0.1 to 10.0 m 3 / hour per 1 m 3 of the effective treatment space. In this state, when the water to be treated is fed little by little into the biological treatment tank 2 from the upper part, while the water to be treated flows downward through the gap of the carrier T, the organic substances contained in the water to be treated are removed from the carrier. Decomposed or assimilated by microorganisms carried on the T surface, and as a result, purification of the water to be treated proceeds.
The treated water obtained by the purification treatment is transferred from the bottom of the biological treatment tank 2 to the separation tank 3 through the communication part 9. Slight solids contained in the treated water are settled and separated in the separation tank 3,
Only the supernatant is drained out. The sediment accumulated at the bottom of the separation tank 3 is pulled out and removed by an appropriate discharging means 20.

【0019】続いて、当該生物的処理装置1における洗
浄工程を説明する。担体Tの洗浄を実行するには、図2
に示すように、曝気手段4の2つの散気管7,8両方か
ら、又は洗浄用の散気管8から、生物処理槽2内へ定常
運転時の約1.1〜10倍量(例えば、有効処理空間1
3 当たり1〜30m3 /時)の空気を供給する。この
とき、被処理水の供給は停止させても続行させてもよ
い。生物濾過層Fと担体分離板10との間には適当な距
離を持たせてあるから、大量の空気が供給されることに
より、生物処理槽2内に激しい気液混合流が生じ、生物
濾過層Fを形成している担体Tが分散して流動する。本
実施形態の担体Tは複数の羽根体を備えているので、気
液混合流の流動エネルギーを受けやすく、依って流動能
力に優れている。しかも担体Tは、内部に空気を保持す
ることのない構造となっているから見かけ比重の変動が
なく、それ故、一様な流動状態を得ることが可能であ
る。担体Tの流動の結果、担体T間に捕捉されていたS
S等の固形分や、有機物の分解・同化に伴って増殖した
微生物の余剰フロックが脱落する。脱落した固形物は沈
殿させ、排出手段20により排除する。
Next, the cleaning step in the biological treatment apparatus 1 will be described. To carry out the washing of the carrier T, FIG.
As shown in (1), about 1.1 to 10 times the amount during normal operation (for example, effective) from both the two air diffusers 7 and 8 of the aeration means 4 or from the air diffuser 8 for washing into the biological treatment tank 2 Processing space 1
m supplies air 3 per 1-30 m 3 / h). At this time, the supply of the water to be treated may be stopped or continued. Since an appropriate distance is provided between the biological filtration layer F and the carrier separation plate 10, a large amount of air is supplied, so that a violent gas-liquid mixed flow is generated in the biological treatment tank 2 and the biological filtration The carrier T forming the layer F is dispersed and flows. Since the carrier T of the present embodiment has a plurality of blades, it is easy to receive the flow energy of the gas-liquid mixed flow, and therefore has excellent flowability. Moreover, since the carrier T has a structure that does not hold air inside, there is no change in apparent specific gravity, and therefore, it is possible to obtain a uniform flow state. As a result of the flow of the carrier T, S trapped between the carriers T
Solids such as S and surplus flocs of microorganisms that have grown due to the decomposition and assimilation of organic substances fall off. The solids that have fallen out are settled out and eliminated by the discharge means 20.

【0020】〔第2の実施形態〕担体Tを連続気泡を持
たない材質を用いて製作することにより、空気の保持に
よる見かけ比重の変動のおそれがなくなるので、担体T
を羽根体を持たないものとしても、洗浄工程時における
流動性を確保することが可能である。図7は、そのよう
な担体Tを例示するものであって、同図(a)に示す円
筒状、同図(b)の隅部や稜部に面取を施したサイコロ
状、同図(c)の突起を有する短柱状のほか、図示は省
略するが、球状,ドーナツ状(トーラス状),六角柱
状,円筒外周面に凸起や軸方向のリブを形成したものな
どが考えられる。本実施形態の場合、担体Tの大きさは
2〜25mm程度とするのが好ましい。
[Second Embodiment] By manufacturing the carrier T using a material having no open cells, there is no fear that the apparent specific gravity fluctuates due to the retention of air.
It is possible to ensure the fluidity during the washing step even if the blade does not have a blade body. FIG. 7 exemplifies such a carrier T, and has a cylindrical shape shown in FIG. 7A, a dice shape having chamfered corners and ridges in FIG. In addition to the short column shape having the protrusion c), a spherical shape, a donut shape (a torus shape), a hexagonal column shape, a protrusion having a projection on the outer peripheral surface of the cylinder, or a rib in the axial direction are conceivable. In the case of the present embodiment, the size of the carrier T is preferably about 2 to 25 mm.

【0021】〔第3の実施形態〕図8は、本発明に係る
生物的処理装置1の異なる態様を示すものであって、生
物処理槽2と沈殿槽12とを、連通管11で接続して構
成したものである。前記第1の実施形態では、生物処理
槽2と処理水分離槽3とが底部で直接的に連通している
ため、分離槽3は生物処理槽2における流動状態の影響
を受け易かった。本実施形態では、連通管11を介して
生物処理槽2と沈殿槽12とを接続したので、沈殿槽1
2は生物処理槽2における流動状態の影響を受けること
がない。依って、生物処理槽2から移送される処理水中
に含まれるわずかな固形物の沈降分離を、安定して行う
ことができる。
[Third Embodiment] FIG. 8 shows a different embodiment of the biological treatment apparatus 1 according to the present invention. The biological treatment tank 2 and the sedimentation tank 12 are connected by a communication pipe 11. It is configured. In the first embodiment, since the biological treatment tank 2 and the treated water separation tank 3 are directly in communication at the bottom, the separation tank 3 was easily affected by the flow state in the biological treatment tank 2. In the present embodiment, since the biological treatment tank 2 and the sedimentation tank 12 are connected via the communication pipe 11, the sedimentation tank 1
2 is not affected by the flow state in the biological treatment tank 2. Accordingly, sedimentation and separation of a small amount of solids contained in the treated water transferred from the biological treatment tank 2 can be stably performed.

【0022】なお、処理水から沈降分離させた沈殿物S
を引き抜き排除するための排出手段21は、沈殿槽12
に設けるだけで十分ではあるが、生物処理槽2にも、洗
浄工程によって担体Tから脱落する固形物を抜き取るた
めの排除手段22を設けることを妨げない。
The sediment S separated from the treated water by sedimentation
The discharging means 21 for extracting and removing the
Is sufficient, but it does not prevent the biological treatment tank 2 from being provided with the elimination means 22 for extracting solids falling off from the carrier T in the washing step.

【0023】〔第4の実施形態〕本発明は、図9に示す
ような、担体Tを流動させながら好気的処理を行う生物
処理装置1に適用することも可能である。担体流動式の
生物処理槽2は、曝気装置4からやや多めの空気を被処
理水中へ送り込んで、担体Tを緩やかな流動状態に保ち
つつ、浄化処理工程を行うものである。前述した複数の
羽根体Hを備える担体Tは、このような担体流動式の生
物処理槽2に適用した場合にも、好適な結果を得ること
ができる。なお、本実施形態の場合、担体Tの充填率は
5〜85%程度に設定される。
[Fourth Embodiment] The present invention can be applied to a biological treatment apparatus 1 for performing aerobic treatment while flowing a carrier T as shown in FIG. The carrier flow type biological treatment tank 2 performs a purification treatment step by sending a little more air from the aeration device 4 into the water to be treated and keeping the carrier T in a gentle fluidized state. The carrier T provided with the plurality of blades H described above can also obtain suitable results even when applied to such a carrier flow type biological treatment tank 2. In the present embodiment, the filling rate of the carrier T is set to about 5 to 85%.

【0024】〔第5の実施形態〕図10に示すように、
生物処理槽2における被処理水の貯留水位Lよりも若干
下側の位置に、網体・多孔板等よりなり、担体Tは通過
させないが空気・水等の流体は容易に通過できる担体押
さえ部材40を配設してもよい。担体押さえ部材40を
設けることにより、担体Tの全部が被処理水中に浸漬さ
れるので、被処理水との接触が効率的になる。また、生
物処理槽2の水面近くに溜まる固形物と担体Tとが接触
するのを避けられるから、固形物付着による担体Tの流
動性低下を免れることができる。
[Fifth Embodiment] As shown in FIG.
At a position slightly below the storage water level L of the water to be treated in the biological treatment tank 2, a carrier holding member made of a mesh body, a perforated plate, or the like, which does not allow the carrier T to pass but can easily pass a fluid such as air or water. Forty may be provided. By providing the carrier pressing member 40, all of the carrier T is immersed in the water to be treated, so that the contact with the water to be treated becomes efficient. Further, since it is possible to avoid contact between the carrier T and the solid matter accumulated near the water surface of the biological treatment tank 2, it is possible to avoid a decrease in the fluidity of the carrier T due to the adhesion of the solid matter.

【0025】〔第6の実施形態〕本発明に係る生物的処
理装置1に使用する担体Tは、1種類に限られるもので
はなく、異なる2種類又は数種類を混合して使用するこ
とも妨げない。例えば羽根体Hを備える担体T1 (図3
〜6参照)の異なる大きさのものを2種類以上併用して
もよい。あるいは図11に示すように、羽根体を備える
担体T1 とこれより小径の羽根体を持たない担体T
2 (図7参照)とを混合して生物処理槽2に収納せしめ
ることができる。この場合、羽根体Hを備える担体T1
は流動エネルギーを受けやすいから、羽根体を持たない
担体T2 を一定量混合しても、担体全体を槽内で確実に
流動させることができる。羽根体を備える担体T1 に対
する羽根体を持たない担体T2 の混合割合は、T2 /T
1 =0.05〜1.0程度の範囲となるように設定され
る。
[Sixth Embodiment] The carrier T used in the biological treatment apparatus 1 according to the present invention is not limited to one type, and it does not prevent the use of a mixture of two or more different types. . For example, the carrier T 1 provided with the blade body H (FIG. 3)
-6) may be used in combination of two or more. Alternatively, as shown in FIG. 11, a carrier T 1 having a blade body and a carrier T having no blade body having a smaller diameter.
2 (see FIG. 7) can be mixed and stored in the biological treatment tank 2. In this case, the carrier T 1 provided with the blade body H
Can is because prone to flow energy, even if a certain amount mixed carrier T 2 without a sail body, to reliably flow the entire carrier in a bath. The mixing ratio of the carrier T 2 having no blade to the carrier T 1 having the blade is T 2 / T
1 is set to be in the range of about 0.05 to 1.0.

【0026】〔第7の実施形態〕本発明に係る生物的処
理装置1を用いて、図12に例示するような排水処理シ
ステムを構築することができる。同図の排水処理システ
ムは、被処理水(原水)を嫌気的に処理する第1の嫌気
処理槽13及び第2の嫌気処理槽14に続けて、前記第
1の実施形態に説明する好気的処理を行う生物処理槽2
及び処理水分離槽3を連設して構成したものである。第
1嫌気処理槽13で、被処理水(原水)中の固形物を分
離し、分離し切れなかった固形物を第2嫌気処理槽14
で分離・分解する。しかるのち、生物処理槽2におい
て、担体Tに担持させた微生物の活性により、被処理水
中の有機物を好気的に処理して浄化する。得られた処理
水は隣接する分離槽3へ移送され、上澄み液だけを分離
排出する。
Seventh Embodiment A wastewater treatment system as illustrated in FIG. 12 can be constructed using the biological treatment apparatus 1 according to the present invention. The wastewater treatment system shown in the figure is aerobic treatment described in the first embodiment following the first anaerobic treatment tank 13 and the second anaerobic treatment tank 14 for anaerobically treating the water to be treated (raw water). Biological treatment tank 2 for chemical treatment
And a treated water separation tank 3 connected in series. In the first anaerobic treatment tank 13, solids in the water to be treated (raw water) are separated, and the solids that cannot be separated are removed from the second anaerobic treatment tank 14.
To separate and disassemble. Thereafter, in the biological treatment tank 2, the organic matter in the water to be treated is aerobically treated and purified by the activity of the microorganisms carried on the carrier T. The obtained treated water is transferred to the adjacent separation tank 3, and only the supernatant liquid is separated and discharged.

【0027】なお本実施形態の排水処理システムは、処
理水分離槽3で処理水中から沈降分離した固形物を外部
へ排除するための排出路30を、前記第1嫌気処理槽1
3に接続して循環流路を形成するものとした。従って、
分離槽3で生じた沈殿物や、生物処理槽2において洗浄
工程の結果発生する固形物は、上記排出路30を通じ
て、第1嫌気処理槽13へ返送される。
In the wastewater treatment system of the present embodiment, the discharge path 30 for removing solids settled and separated from the treated water in the treated water separation tank 3 to the outside is provided in the first anaerobic treatment tank 1.
3 to form a circulation channel. Therefore,
The sediment generated in the separation tank 3 and the solid matter generated as a result of the washing step in the biological treatment tank 2 are returned to the first anaerobic treatment tank 13 through the discharge path 30.

【0028】なお本発明の実施形態は前述のものに限定
されるのではなく、実施の状況に即して適宜の応用・変
更を施すことを妨げない。
The embodiment of the present invention is not limited to the above-described embodiment, and does not hinder appropriate application and modification in accordance with the state of implementation.

【0029】[0029]

【発明の効果】本発明は、好気的処理を行う生物的処理
装置において、微生物を担持させる流動可能な担体を、
内部に連続気孔を持たない材料で形成したことにより、
当該担体が空気を内部に取り込んで見かけ比重の変動を
きたすことがなくなるので、担体の流動性が安定化す
る。また、担体を複数の羽根体を備え、内部に空気を保
持することのないものとすることにより、流動エネルギ
ーを受けやすくなり、その結果、担体の流動性が向上す
る。従って、生物処理装置における担体の洗浄工程を効
果的に実行することが可能となり、洗浄不良の問題が解
消される。
According to the present invention, in a biological treatment apparatus for performing aerobic treatment, a flowable carrier for carrying microorganisms is provided.
By using a material that does not have continuous pores inside,
Since the carrier does not take in air to cause a change in apparent specific gravity, the fluidity of the carrier is stabilized. Further, by providing the carrier with a plurality of blades and keeping no air inside, the carrier is more likely to receive flow energy, and as a result, the fluidity of the carrier is improved. Therefore, the carrier cleaning step in the biological treatment apparatus can be effectively performed, and the problem of poor cleaning is eliminated.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の第1の実施形態に関するものであっ
て、図(a)は浄化処理工程時における生物的処理装置
の断面図、図(b)は生物的処理装置の別態様を示す要
部の断面図である。
FIG. 1 relates to a first embodiment of the present invention, in which FIG. 1 (a) is a cross-sectional view of a biological treatment apparatus in a purification treatment step, and FIG. 1 (b) shows another aspect of the biological treatment apparatus. It is sectional drawing of a principal part.

【図2】 本発明の第1の実施形態に関するものであっ
て、洗浄工程時における生物的処理装置の断面図であ
る。
FIG. 2 relates to the first embodiment of the present invention and is a cross-sectional view of the biological treatment apparatus during a cleaning step.

【図3】 本発明に係る生物的処理装置に用いる担体の
1例を示すものであって、図(a)は平面図、図(b)
は正面図、図(c)は正面断面図である。
FIG. 3 shows an example of a carrier used in the biological treatment apparatus according to the present invention, wherein FIG. 3 (a) is a plan view and FIG.
Is a front view, and FIG.

【図4】 本発明に係る生物的処理装置に用いる担体の
1例を示すものであって、図(a)は平面図、図(b)
は正面図、図(c)は正面断面図である。
FIG. 4 shows an example of a carrier used in the biological treatment apparatus according to the present invention, wherein FIG. 4 (a) is a plan view and FIG.
Is a front view, and FIG.

【図5】 本発明に係る生物的処理装置に用いる担体の
1例を示すものであって、図(a)は平面図、図(b)
は正面図、図(c)は正面断面図である。
FIG. 5 shows an example of a carrier used in the biological treatment apparatus according to the present invention, wherein FIG. 5 (a) is a plan view and FIG.
Is a front view, and FIG.

【図6】 本発明に係る生物的処理装置に用いる担体の
1例を示すものであって、図(a)は平面図、図(b)
は正面図、図(c)は底面図である。
FIG. 6 shows an example of a carrier used in the biological treatment apparatus according to the present invention, wherein FIG. 6 (a) is a plan view and FIG.
Is a front view, and FIG.

【図7】 本発明の第2の実施形態に係るものであっ
て、担体の他の例を示す斜視図である。
FIG. 7 is a perspective view according to a second embodiment of the present invention, showing another example of the carrier.

【図8】 本発明の第3の実施形態に係る生物的処理装
置の断面図である。
FIG. 8 is a sectional view of a biological treatment apparatus according to a third embodiment of the present invention.

【図9】 本発明の第4の実施形態に係る生物的処理装
置の断面図である。
FIG. 9 is a sectional view of a biological treatment apparatus according to a fourth embodiment of the present invention.

【図10】 本発明の第5の実施形態に係る生物的処理
装置の断面図である。
FIG. 10 is a sectional view of a biological treatment apparatus according to a fifth embodiment of the present invention.

【図11】 本発明の第6の実施形態に係る生物的処理
装置の断面図である。
FIG. 11 is a sectional view of a biological treatment apparatus according to a sixth embodiment of the present invention.

【図12】 本発明の第7の実施形態に関するものであ
って、本発明に係る生物的処理装置を利用して構築した
排水処理システムの一例を示す断面図である。
FIG. 12 relates to a seventh embodiment of the present invention, and is a cross-sectional view showing an example of a wastewater treatment system constructed using the biological treatment device according to the present invention.

【符号の説明】[Explanation of symbols]

1…生物的処理装置 2…生物処理槽 3…処理水分離
槽 4…曝気手段 5,6…ブロワー 7,8…散気管
9…連通部 10…担体分離板 11…連通管12…
沈殿槽 20…排出手段 40…担体押さえ部材 F…
生物濾過層 H…羽根体 J…連結部材 K…開口部
L…被処理水の貯留水位 N…傾斜面部材P…中心軸
Q…円筒軸 R…リング体 S…内部空間 T…担体
DESCRIPTION OF SYMBOLS 1 ... Biological treatment apparatus 2 ... Biological treatment tank 3 ... Treated water separation tank 4 ... Aeration means 5, 6 ... Blower 7, 8 ... Aeration tube 9 ... Communication part 10 ... Carrier separation plate 11 ... Communication tube 12 ...
Sedimentation tank 20 ... Discharge means 40 ... Carrier holding member F ...
Biological filtration layer H: feather body J: connecting member K: opening
L: Storage water level of treated water N: Inclined surface member P: Central axis
Q: Cylindrical shaft R: Ring body S: Internal space T: Carrier

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 微生物を担持させた流動可能な多数の担
体により、被処理水を好気的条件下で浄化処理する装置
において、前記担体は、比重が水と同等か又はわずかに
小さく且つ内部へ通ずる連続気孔を持たない材料で形成
されていることを特徴とする生物的処理装置。
1. An apparatus for purifying water to be treated under aerobic conditions with a large number of flowable carriers carrying microorganisms, wherein the carrier has a specific gravity equal to or slightly smaller than that of water, and A biological treatment apparatus characterized by being formed of a material that does not have continuous pores leading to water.
【請求項2】 微生物を担持させた流動可能な多数の担
体により、被処理水を好気的条件下で浄化処理する装置
において、前記担体は、比重が水と同等か又はわずかに
小さく且つ内部へ通ずる連続気孔を持たない材料で形成
され、規則的に配置された複数の羽根体を備え、全ての
表面開口部が他のいずれかの表面開口部と連通するよう
に構成され、内部空間の内法寸法が気泡を捕捉しない大
きさに設定されていることを特徴とする生物的処理装
置。
2. An apparatus for purifying water to be treated under aerobic conditions with a large number of flowable carriers carrying microorganisms, wherein the carrier has a specific gravity equal to or slightly smaller than that of water, and It is formed of a material that does not have continuous pores leading to the air, comprises a plurality of regularly arranged vanes, and is configured such that all surface openings communicate with any other surface openings, A biological treatment apparatus characterized in that the inner dimension is set to a size that does not trap air bubbles.
【請求項3】 大きさの異なる担体を混在させた請求項
2に記載の生物的処理装置。
3. The biological treatment apparatus according to claim 2, wherein carriers having different sizes are mixed.
【請求項4】 比重が水と同等か又はわずかに小さい材
料で形成され、羽根体を持たない担体を混在させた請求
項2に記載の生物的処理装置。
4. The biological treatment apparatus according to claim 2, wherein a carrier made of a material having a specific gravity equal to or slightly smaller than that of water and having no blade body is mixed.
【請求項5】 前記担体が収納される処理槽における被
処理水の貯留水位よりやや下方の位置に、担体の通過を
阻止する押さえ部材を設けた請求項1乃至4のいずれか
に記載の生物的処理装置。
5. The living organism according to claim 1, wherein a holding member for preventing passage of the carrier is provided at a position slightly below the storage level of the water to be treated in the treatment tank in which the carrier is stored. Processing equipment.
JP12307298A 1998-02-19 1998-05-06 Biological treating device Pending JPH11300379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12307298A JPH11300379A (en) 1998-02-19 1998-05-06 Biological treating device

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP3707898 1998-02-19
JP10-37078 1998-02-19
JP12307298A JPH11300379A (en) 1998-02-19 1998-05-06 Biological treating device

Publications (1)

Publication Number Publication Date
JPH11300379A true JPH11300379A (en) 1999-11-02

Family

ID=26376180

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12307298A Pending JPH11300379A (en) 1998-02-19 1998-05-06 Biological treating device

Country Status (1)

Country Link
JP (1) JPH11300379A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Water treatment equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Water treatment equipment

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