JP2584763B2 - Immersion filter bed method for cleaning biological treatment equipment - Google Patents

Immersion filter bed method for cleaning biological treatment equipment

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Publication number
JP2584763B2
JP2584763B2 JP62062750A JP6275087A JP2584763B2 JP 2584763 B2 JP2584763 B2 JP 2584763B2 JP 62062750 A JP62062750 A JP 62062750A JP 6275087 A JP6275087 A JP 6275087A JP 2584763 B2 JP2584763 B2 JP 2584763B2
Authority
JP
Japan
Prior art keywords
water
filler
cleaning
treated
washing
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.)
Expired - Fee Related
Application number
JP62062750A
Other languages
Japanese (ja)
Other versions
JPS63232892A (en
Inventor
雅博 川端
武夫 吉田
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.)
Organo Corp
Original Assignee
Organo Corp
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Filing date
Publication date
Application filed by Organo Corp filed Critical Organo Corp
Priority to JP62062750A priority Critical patent/JP2584763B2/en
Publication of JPS63232892A publication Critical patent/JPS63232892A/en
Application granted granted Critical
Publication of JP2584763B2 publication Critical patent/JP2584763B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、有機物及び/又は窒素成分を含む被処理水
を生物学的に処理する浸漬濾床法生物学的処理装置の洗
浄方法に関するものである。
Description: TECHNICAL FIELD The present invention relates to a method for cleaning a biological treatment apparatus using a immersion filter bed method for biologically treating water to be treated containing an organic substance and / or a nitrogen component. It is.

<従来の技術> 従来から廃水等の被処理水中に含まれる有機物(BOD
又はCOD)の除去、あるいは窒素成分(NH4−N、NO3
Nなど)の硝化又は脱窒を行う生物学的処理装置の一つ
として運転管理が容易で任意の除去率が得られる浸漬濾
床法処理装置(以下、浸漬濾床装置という)が広く使用
されている。当該浸漬濾床装置は砂利、砕石、ラシヒリ
ング、網状体等からなる充填材層の上部又は下部から有
機物及び/又は窒素成分を含む被処理水を流入し、前記
充填材層に着生した微生物(好気性微生物又は嫌気性微
生物)の働きによって被処理水中の有機物を生物学的に
分解除去したり、あるいは窒素成分を生物学的に硝化又
は脱窒したりするもので、いわゆる遊離式の生物処理装
置に比べて槽内の微生物濃度を相当程度高く出来、従っ
て有機物あるいは窒素成分の高負荷処理が可能であると
いう特長を有している。
<Conventional technology> Conventionally, organic substances (BOD) contained in treated water such as wastewater
Or removal of COD), or nitrogen components (NH 4 -N, NO 3 -
As a biological treatment apparatus for performing nitrification or denitrification of N, etc., a immersion filter bed treatment apparatus (hereinafter referred to as an immersion filter bed apparatus) that is easily operated and can obtain an arbitrary removal rate is widely used. ing. The immersion filter bed apparatus flows in the water to be treated containing an organic substance and / or a nitrogen component from the upper or lower part of a filler layer composed of gravel, crushed stone, Raschig rings, a net-like body, and the like, and microorganisms that have formed on the filler layer ( Aerobic microorganisms or anaerobic microorganisms) to biologically decompose and remove organic matter in the water to be treated or to biologically nitrify or denitrify nitrogen components, so-called free biological treatment Compared to the apparatus, the concentration of microorganisms in the tank can be considerably increased, and therefore, it has the feature that high-load treatment of organic substances or nitrogen components is possible.

しかしながら、このような浸漬濾床装置においては、
被処理水の処理を継続すると微生物の肥大化、被処理水
中の懸濁物質の堆積等により充填材層が目詰まりを起こ
し、所定の通水量が確保出来なくなったり、好気性微生
物処理の場合は微生物の嫌気化が起こったりして処理水
質が悪化することとなるので定期的に充填材層の下部か
ら洗浄水及び/又は洗浄気体を流入して充填材層の目詰
まりを解消する、いわゆる洗浄操作を行っている。
However, in such a submerged filter bed apparatus,
If the treatment of the treated water is continued, the filler layer will be clogged due to the enlargement of microorganisms and the accumulation of suspended solids in the treated water, and it will not be possible to secure a predetermined water flow rate. So-called washing, in which washing water and / or washing gas flows periodically from the lower part of the filler layer to eliminate clogging of the filler layer, since the anaerobicization of microorganisms and the quality of treated water deteriorates. You are performing an operation.

<発明が解決しようとする問題点> このような浸漬濾床装置における充填材層の洗浄に際
し、洗浄効果を高めようとすれば、洗浄時に充填材層を
円滑に流動化させ、充填材を互いに離隔させることが必
要であるが、従来の浸漬濾床装置においては充填材とし
て天然砂利又は砕石等、比重の大きなもので、かつ少し
でも目詰まりを起こしにくくするために径の大きな(10
〜30mm程度)充填材が使用される場合がほとんどである
から、充填材層を流動化させるために相当大きな流速の
水及び/又は空気が必要であり、そのため大きな動力を
必要とするという問題点があるとともに、往々にしてそ
の洗浄効果が不充分となる欠点を有していた。更に、こ
のように大きな流速の水及び/又は空気を用いて洗浄を
行った場合には、充填材表面に着生している微生物の過
剰剥離が生じ、洗浄直後の通水処理における処理水質が
一時的に悪化するという問題点もある。
<Problems to be Solved by the Invention> When cleaning the filler layer in such a immersed filter bed apparatus, if the cleaning effect is to be enhanced, the filler layer is fluidized smoothly during cleaning, and the fillers are mutually separated. It is necessary to separate them. However, in the conventional immersion filter apparatus, natural fillers such as natural gravel or crushed stone are used as fillers, and large fillers are used to prevent clogging.
In most cases, a filler is used, so that a relatively large flow rate of water and / or air is required to fluidize the filler layer, and thus a large power is required. And the disadvantage that the cleaning effect is often insufficient. Further, when washing is performed using water and / or air having such a large flow rate, excessive separation of microorganisms that have formed on the surface of the filler occurs, and the treated water quality in the water passage treatment immediately after washing is reduced. There is also the problem that it worsens temporarily.

本発明は、従来の浸漬濾床装置におけるかかる問題点
を解決するもので、充填材層が目詰まりを起こした場合
の洗浄に要する動力を少なくすることが出来るととも
に、洗浄直後の通水処理における一時的な処理水質の悪
化を極力防ぎ、処理水質を安定化させることが出来る浸
漬濾床装置の洗浄方法を提供することを目的とするもの
である。
The present invention solves such a problem in a conventional immersion filter bed apparatus, and can reduce the power required for cleaning when the filler layer is clogged, and can reduce the power required for water passing treatment immediately after cleaning. It is an object of the present invention to provide a method for cleaning a submerged filter bed apparatus that can prevent temporary deterioration of treated water quality as much as possible and stabilize treated water quality.

<問題点を解決するための手段> 本発明は、好気性微生物又は嫌気性微生物をその表面
に着生させた充填材を槽内に充填して充填材槽を形成
し、前記充填材として、被処理水中で浮上して浮上充填
材層を形成する比重が0.9以上,1.0未満のものと、被処
理水中で沈降して沈降充填材層を形成する比重が1.0以
上,1.1以下のものとの2種類の粒状物を、両充填材層の
間に洗浄時の充填材流動化のための空所を形成するよう
に充填し、当該充填材層に被処理水を流入して被処理水
を生物学的に処理する浸漬濾床法生物学的処理装置にお
いて、微生物の肥大化が激しく目詰りの頻度が高い一方
の充填材層だけを流動化させる部分洗浄と、両充填材層
ともに目詰りを起した場合に充填材層全体を流動化させ
る全体洗浄とを選択して行うことを特徴とするものであ
る。
<Means for solving the problems> The present invention forms a filler tank by filling a tank with an aerobic microorganism or an anaerobic microorganism grown on its surface to form a filler tank, and as the filler, The specific gravity of floating above the treated water to form a floating filler layer is 0.9 or more and less than 1.0, and the specific gravity of sedimenting in the treated water to form a settling filler layer is 1.0 or more and 1.1 or less. The two kinds of particulate matter are filled so as to form a space between the two filler layers for fluidizing the filler during washing, and the water to be treated flows into the filler layer to remove the water to be treated. In biological treatment equipment using a immersion filter bed method for biological treatment, microbial enlargement is severe and clogging is frequently caused.Partial washing to fluidize only one filler layer, and both filler layers are clogged. And selecting the whole cleaning to fluidize the entire filler layer in the event of occurrence of A.

以下に本発明の実施態様の一例を図面を用いて詳細に
説明する。
Hereinafter, an example of an embodiment of the present invention will be described in detail with reference to the drawings.

図面は、好気性微生物を用いた浸漬濾床装置であっ
て、被処理水を充填材層内に上向流で流過させる構成と
した装置に本発明を適用した例を示す縦断面説明図であ
り、断面が円形又は矩形の槽1の下部に多数の開口又は
スリットを有する床板2を設けるとともに槽1の上部に
多数のスリットを有するコレクター(集水機構)3を複
数本付設し、当該床板2と当該コレクター3との間の槽
1内に充填材4を充填する。当該充填材4は、被処理水
中で浮上しかつ比重が0.9以上、1.0未満のものと、被処
理水中で沈みかつ比重1.0以上、1.1以下のものとの2種
類の粒状物を混合したもので、槽1内水中では図面を示
す如く、水中で浮上する充填材4Aからなる浮上充填材層
5及び水中で沈降する充填材4Bからなる沈降充填材層6
を形成する。また、両充填材層5及び6の間には、洗浄
を行った際に充填材4が円滑に流動出来る程度の空所7
を設けておく。なお、以下の説明では、浮上充填材層
5、沈降充填材層6、及び当該空所7の全体をまとめて
充填層部8という。又、床板2の下部に原水管9及び洗
浄水管10に連通する多数の穴を穿った散水管11、及び空
気管12に連通する多数の穴を穿った散気管13をそれぞれ
多数本埋設し、更にコレクター3には出口管14を接続す
る。
The drawing is an immersion filter bed apparatus using aerobic microorganisms, and is a longitudinal sectional explanatory view showing an example in which the present invention is applied to an apparatus configured to allow water to be treated to flow upward in a filler layer. A floor plate 2 having a large number of openings or slits is provided below a tank 1 having a circular or rectangular cross section, and a plurality of collectors (water collecting mechanisms) 3 having a large number of slits are provided above the tank 1. The filling material 4 is filled in the tank 1 between the floor plate 2 and the collector 3. The filler 4 is a mixture of two types of particulates, which float in the water to be treated and have a specific gravity of 0.9 or more and less than 1.0, and those which sink in the water to be treated and have a specific gravity of 1.0 or more and 1.1 or less. As shown in the drawing, a floating filler layer 5 composed of a filler 4A floating in water and a settling filler layer 6 composed of a filler 4B settling in water as shown in the drawing.
To form In addition, a space 7 between the two filler layers 5 and 6 is provided such that the filler 4 can flow smoothly when washing is performed.
Is provided. In the following description, the entirety of the floating filler layer 5, the settling filler layer 6, and the empty space 7 will be collectively referred to as a packed layer portion 8. In addition, a plurality of water diffusion pipes 11 having a large number of holes communicating with the raw water pipe 9 and the washing water pipe 10 and a large number of air diffusion pipes 13 having a large number of holes communicating with the air pipe 12 are buried under the floor plate 2, respectively. Further, an outlet pipe 14 is connected to the collector 3.

本発明に使用する充填材4には、例えば天然石を粉砕
したものを比重を調整して造粒、焼成した多孔性の人工
石あるいは比重を調整して造粒、焼成した粒状の煉瓦等
で、粒径が15〜30mm程度のものを使用するのが望まし
い。当該充填材4の形状は粒状物であれば他は特に限定
しないが、充填材4相互間の適度の空隙率の保持、洗浄
時における充填材4の円滑な流動を行うためにはほぼ球
形であることが望ましく、かつ目詰まりを少なくするた
めに、その表面が滑面状で凹凸部がないものが望まし
い。
The filler 4 used in the present invention is, for example, a granulated and baked porous artificial stone or a granulated brick that has been granulated and baked by adjusting the specific gravity of natural stone or granulated by calcining natural stone, It is desirable to use one having a particle size of about 15 to 30 mm. The shape of the filler 4 is not particularly limited as long as it is a granular material. However, in order to maintain an appropriate porosity between the fillers 4 and to perform a smooth flow of the filler 4 during washing, the shape of the filler 4 is substantially spherical. In order to reduce clogging, it is desirable that the surface has a smooth surface and no irregularities.

<作用> 図面に示した浸漬濾床装置により、例えば有機物ある
いはNH4−Nを含む被処理水を処理するには、原水管9
を介して散水管11の穴より被処理水を流入して被処理水
を充填層部8内に上向流で流過させるとともに、空気管
12を介して散気管13の穴より空気を流入する。このよう
にすると沈降充填材層5及び浮上充填材層6に着生した
好気性微生物の働きにより、被処理水中の有機物の生物
学的酸化分解あるいはNH4−Nの生物学的硝化を行うこ
とが出来、処理水をコレクター3スリットから集水して
出口管14より得ることが出来る。なお、コレクタ−3に
代えて、多数の開口を有する押さえ板(例えば金網)を
槽1内に横設するとともに当該押さえ板の上方に出口管
14を設けた構造としてもよい。
<Effect> In order to treat the water to be treated containing, for example, organic substances or NH 4 —N by the immersion filter bed apparatus shown in the drawing, the raw water pipe 9
The water to be treated flows through the hole of the water sprinkling pipe 11 through the through hole, and the water to be treated flows through the packed bed portion 8 in an upward flow, and the air pipe
Air flows in from the hole of the air diffuser 13 through 12. In this manner, the biological oxidation and decomposition of organic substances in the water to be treated or the biological nitrification of NH 4 —N are performed by the action of the aerobic microorganisms that have settled on the settling filler layer 5 and the floating filler layer 6. The treated water is collected from the slit of the collector 3 and can be obtained from the outlet pipe 14. Note that, instead of the collector-3, a holding plate (for example, a wire mesh) having a large number of openings is horizontally provided in the tank 1 and an outlet pipe is provided above the holding plate.
14 may be provided.

このような処理を続行するうちに、好気性微生物の肥
大化及び被処理水中のSSの若干の堆積により充填層部8
が目詰まりを起こすので、定期的に洗浄を行うが、本発
明においては洗浄を、比較的ゆるやかな洗浄条件で行う
充填層部8の部分的な洗浄(以下通常洗浄という)と、
比較的激しい洗浄条件で行う充填層部8全体の洗浄(以
下特別洗浄という)との2種類の方法で実施し、両洗浄
方法を組み合わせることによって充填層部8の目詰まり
を効果的に解消するとともに洗浄後の通水処理における
処理水質の一時的な悪化を極力防止することが出来る。
While such treatment is continued, the packed bed portion 8 is enlarged due to the enlargement of aerobic microorganisms and the slight accumulation of SS in the water to be treated.
Are clogged, so that they are periodically cleaned. In the present invention, the cleaning is performed by partially cleaning the packed bed portion 8 under relatively mild cleaning conditions (hereinafter referred to as normal cleaning),
Clogging of the packed bed portion 8 is effectively eliminated by performing two types of washing with the entire packed bed portion 8 (hereinafter referred to as special washing) performed under relatively intense washing conditions. At the same time, it is possible to prevent temporary deterioration of the treated water quality in the water passing treatment after the washing as much as possible.

すなわち、浸漬濾床装置における微生物の肥大化は、
被処理水が流入する側の充填材層、図面においては槽1
下部に形成されている沈降充填材層6内で激しく、一
方、流出側、図面においては槽1上部の浮上充填材層5
内では肥大化の速度が遅いという特性がある。従って、
通常の洗浄においては前記通水処理を中断した後、洗浄
水管10を介して散水管11より洗浄水を通常処理時の通水
量の3〜6倍程度の流量で充填層部8内に流入し、一
方、散気管13からは空気を空気管12を介して通常処理時
の通気量のまま流入して5〜20分間洗浄を行い、この時
には槽1内下部の、微生物の肥大化が顕著な沈降充填材
層6の洗浄を主として行う。これが前述の通常洗浄であ
る。この際、沈降充填材層6を形成している充填材4B
は、前述の如くその比重が1.0以上、1.1以下で、槽1内
の水の比重に近く、洗浄水及び空気の上昇粒により容易
に浮上し、充填材4Bは互いに離隔して沈降充填材層6は
ゆるやかな流動を起こす。当該流動による充填材4B相互
の軽度の衝突によって充填材4Bの表面に着生した余剰の
好気性微生物を剥離させることが出来、剥離した微生物
は沈降充填材層6の上方に追い出され、当該充填材層6
の目詰まりは大部分解消する。更に、剥離した微生物は
当該空気と洗浄水との混合流によって細かく破砕されて
槽1内を上昇し、浮上充填材層5に達するか、当該充填
材層5を形成している充填材4Aは前述の如く、その粒径
が15〜30mm程度と比較的大きなものを使用するので、剥
離した微生物は一部当該充填材層5に捕捉されるもの
の、大部分は当該充填材層5の間隙を通過してコレクタ
ー3に達し、出口管14を経て系外に排出される。従っ
て、当該洗浄により浮上充填材層5が急激に目詰まりす
るようなことはない。
That is, the enlargement of the microorganisms in the immersion filter bed device,
Filler layer on the side where the water to be treated flows in, tank 1 in the drawing
Violently in the settling filler layer 6 formed in the lower part, while on the outflow side, in the drawing, the floating filler layer 5 in the upper part of the tank 1
Inside, there is a characteristic that the rate of enlargement is slow. Therefore,
In the normal cleaning, after the water supply process is interrupted, the cleaning water flows from the sprinkling pipe 11 through the cleaning water pipe 10 into the packed bed portion 8 at a flow rate of about 3 to 6 times the flow rate in the normal processing. On the other hand, air is introduced from the air diffuser 13 through the air pipe 12 at the same flow rate as during normal processing, and washing is performed for 5 to 20 minutes. At this time, the enlargement of microorganisms in the lower part of the tank 1 is remarkable. The settling filler layer 6 is mainly washed. This is the aforementioned normal cleaning. At this time, the filler 4B forming the settling filler layer 6
As described above, the specific gravity is 1.0 or more and 1.1 or less, close to the specific gravity of the water in the tank 1, easily floated by the rising particles of the washing water and the air, and the filler 4B is separated from the sedimentary filler layer. 6 causes a gentle flow. Excessive aerobic microorganisms that have settled on the surface of the filler 4B due to slight collision between the fillers 4B due to the flow can be separated, and the separated microorganisms are expelled above the settled filler layer 6, and Material layer 6
Most of the clogging is eliminated. Furthermore, the separated microorganisms are finely crushed by the mixed flow of the air and the washing water and rise in the tank 1, and reach the floating filler layer 5 or the filler 4A forming the filler layer 5 As described above, since a relatively large particle having a particle size of about 15 to 30 mm is used, the exfoliated microorganisms are partially captured by the filler layer 5, but most of the microorganisms pass through the gap of the filler layer 5. After passing through, it reaches the collector 3 and is discharged out of the system via the outlet pipe 14. Therefore, the floating filler layer 5 does not suddenly become clogged by the washing.

この際、浮上充填材層5を形成している、被処理水中
で浮上する充填材4Aはその浮力によってほとんど流動す
ることがなく、当該充填材4Aに着生している微生物はほ
とんど剥離しない。従って、充填材層全体を流動化させ
て洗浄を行う従来の浸漬濾床装置に比べて洗浄後の槽内
微生物保有量を高く維持することが出来、よって洗浄直
後の通水処理における処理水質の一時的な悪化を防ぐこ
とが出来る。
At this time, the filler 4A that floats in the water to be treated and forms the floating filler layer 5 hardly flows due to its buoyancy, and the microorganisms that have settled on the filler 4A hardly peel off. Therefore, compared to the conventional immersion filter apparatus in which the entire filler layer is fluidized and washed, the amount of microorganisms in the tank after washing can be maintained higher, and thus the quality of the treated water in the water treatment immediately after washing can be maintained. Temporary deterioration can be prevented.

上述のような通常洗浄を定期的に行うことにより、微
生物の肥大化の激しい、従って目詰まりを起こし易い沈
降充填材層6の目詰まりを解消することが出来るが、こ
のような洗浄を定期的に繰り返すうちに、槽1内の上部
に形成した浮上充填材層5内でも微生物の肥大化が進行
し、また、前記通常洗浄によって剥離した微生物の一部
が浮上充填材層5内で捕捉されることにより、遂には浮
上充填材層5も目詰まりを起こすこととなる。従ってこ
の場合には、充填層部8全体を流動化させる洗浄方法、
すなわち、前述の特別洗浄を行う。当該特別洗浄は、以
下のような方法で行うのが最も効果的である。すなわ
ち、通水処理を中断した後、先ず空気管12を介して散気
管13より洗浄空気のみを通常処理時の3〜6倍程度の流
量で3〜15分間流入し、当該洗浄空気の上昇流により、
槽1内に沈降している充填材4Bを互いに離隔せしめると
ともに沈降充填材層6を流動化させるが、この時、本発
明においては当該洗浄空気の上昇流によって浮上充填材
層5をも流動化させることが出来る。というのは、当該
洗浄空気の上昇流がもたらすエアリフト効果によって槽
1内に循環流が生じ、浮上充填材層5に下向きの流れが
作用することとなり、一方、浮上充填材層5を形成して
いる充填材4Aは、被処理水中で浮上するものではあって
も、その比重が0.9以上、1.0未満のもので、槽1内の水
の比重に近く、浮力がそれほど大きくないので、前記下
向きの流れによって、浮上充填材層5を容易に流動化さ
せることが出来る。なお、当該充填材4Aの比重を0.9未
満としたのでは、浮力が大き過ぎてエリアソフト効果に
よって流動化させることが難しくなり、好ましくない。
By performing the regular cleaning as described above at regular intervals, it is possible to eliminate clogging of the settling filler layer 6 in which the microbial growth is intense and, therefore, clogging is likely to occur. During the repetition of the above, the microbial enlargement progresses also in the floating filler layer 5 formed in the upper part of the tank 1, and a part of the microorganisms separated by the normal washing is captured in the floating filler layer 5. As a result, the floating filler layer 5 will eventually be clogged. Therefore, in this case, a cleaning method for fluidizing the entire packed bed portion 8,
That is, the above-described special cleaning is performed. The special cleaning is most effectively performed by the following method. That is, after the water supply process is interrupted, first, only the cleaning air flows from the air diffuser 13 through the air pipe 12 at a flow rate about 3 to 6 times that of the normal processing for 3 to 15 minutes, and the rising flow of the cleaning air is increased. By
The fillers 4B settled in the tank 1 are separated from each other and the settled filler layer 6 is fluidized. At this time, in the present invention, the floating filler layer 5 is also fluidized by the rising flow of the cleaning air. Can be done. That is, a circulating flow is generated in the tank 1 by an air lift effect caused by the rising flow of the cleaning air, and a downward flow acts on the floating filler layer 5, while forming the floating filler layer 5 The filling material 4A, which floats in the water to be treated, has a specific gravity of 0.9 or more and less than 1.0, is close to the specific gravity of water in the tank 1, and has not so large buoyancy. By the flow, the floating filler layer 5 can be easily fluidized. If the specific gravity of the filler 4A is less than 0.9, the buoyancy is too large and it is difficult to fluidize by the area soft effect, which is not preferable.

前記洗浄空気のみの洗浄により、両充填材層5及び6
を流動化させるとともに充填材4を互いに衝突せしめ、
充填材4間に堆積した若干のSSを浮遊状態にするととも
に充填材4の表面に着生した余剰の好気性微生物を剥離
する。次いで洗浄空気を流入させたまま、あるいは洗浄
空気の流入を一旦停止した後、再び散気管13より洗浄空
気を流入し、同時に洗浄水を洗浄水管10を介して散水管
11より通常処理時の3〜6倍程度の流量で流入し、洗浄
空気と洗浄水との同時流入による洗浄を5〜20分間行っ
て当該混合流体の上昇流によって前記洗浄空気のみの場
合と同じような作用を生ぜしめるとともに、浮遊状態と
したSS及び剥離した微生物を洗浄水の流入によって充填
層部8から追い出し、コレクター3を介して出口管14よ
り系外に排出する。以上のように、当該特別洗浄におい
ては、はじめに洗浄空気単独の洗浄工程、次いで洗浄空
気及び洗浄水併用の洗浄工程を設けることにより、充填
材4間に堆積した若干のSSの浮遊化、充填材4の表面か
らの余剰の好気性微生物の剥離、充填層部8からのSS及
び好気性微生物の追い出しを効果的に行うことが出来、
また洗浄空気単独の洗浄工程を設けることにより、洗浄
水の大幅な節減を行うことが出来る。なお、当該特別洗
浄においては、洗浄空気単独の洗浄を行う前に、予め槽
1内の水を、槽1の下部に付設した水抜き管(図示せ
ず)により引き抜いて、その水位を沈降充填材層6の上
面よりやや下の位置まで下降させ、その後散水管11より
洗浄水を流入して槽1内の水位を再びコレクター3の位
置まで上昇させ、しかる後に洗浄空気単独の洗浄を行う
ようにすると、より一層効果的な洗浄が行える。という
のは、槽1内の水位の上下動に追随して浮上充填材層5
も空所7に相当する距離だけ上下動し、この間に浮上充
填材層5がほぐれて、当該層5を形成している充填材4A
を互いに離隔させることが出来るからである。
By cleaning only the cleaning air, both the filler layers 5 and 6 are removed.
And cause the fillers 4 to collide with each other,
Some of the SS deposited between the fillers 4 is floated, and excess aerobic microorganisms that have settled on the surface of the fillers 4 are peeled off. Next, with the washing air flowing in or after stopping the inflow of the washing air, the washing air flows again from the air diffuser 13, and at the same time, the washing water is sprayed through the washing water pipe 10.
11 flows at a flow rate of about 3 to 6 times that of the normal processing, and the cleaning by simultaneous inflow of the cleaning air and the cleaning water is performed for 5 to 20 minutes, and the rising flow of the mixed fluid is the same as the case of only the cleaning air. In addition to the above action, the suspended SS and the separated microorganisms are expelled from the packed bed portion 8 by the inflow of the washing water, and are discharged from the outlet pipe 14 through the collector 3 to the outside of the system. As described above, in the special cleaning, by first providing a cleaning step using only the cleaning air, and then providing a cleaning step using the cleaning air and the cleaning water together, some of the SS deposited between the fillers 4 is floated, 4. Exfoliation of surplus aerobic microorganisms from the surface of No. 4 and elimination of SS and aerobic microorganisms from the packed bed portion 8 can be performed effectively.
Further, by providing the cleaning step using only the cleaning air, it is possible to significantly reduce the cleaning water. In addition, in the special washing, before washing with the washing air alone, the water in the tank 1 is drawn in advance by a drain pipe (not shown) attached to the lower part of the tank 1, and the water level is settled and filled. The water level is lowered to a position slightly lower than the upper surface of the material layer 6, and then the washing water flows in from the sprinkling pipe 11 to raise the water level in the tank 1 again to the position of the collector 3, and then the washing air alone is washed. In this case, more effective cleaning can be performed. That is, the floating filler layer 5 follows the vertical movement of the water level in the tank 1.
Also moves up and down by a distance corresponding to the space 7, during which the floating filler layer 5 is loosened, and the filler 4A forming the layer 5
Can be separated from each other.

特別洗浄においては、充填層部8全体を流動化させて
洗浄するので、前述の如く充填材4表面に着生した好気
性微生物の過剰剥離が生じる恐れがあり、従って当該洗
浄直後の通水処理において一時的に処理水質が悪化する
場合もあるが、本発明においては、通常は洗浄直後の処
理水質の悪化が少ない前述の通常洗浄を実施し、これを
数回繰り返した後に、前記特別洗浄を一度行うようにす
ればよく、従って毎回当該特別洗浄と同様な強力な洗浄
を必要とする従来の浸漬濾床装置に比べて、処理水質を
飛躍的に安定させることが出来、かつ洗浄に要するエネ
ルギーを従来より低下させることが出来る。
In the special cleaning, since the entire packed bed portion 8 is fluidized and washed, the aerobic microorganisms settled on the surface of the filler 4 may be excessively peeled off as described above. Although the treated water quality may be temporarily deteriorated in the present invention, in the present invention, the above-mentioned normal cleaning is usually performed with little deterioration of the treated water quality immediately after the cleaning, and after repeating this several times, the special cleaning is performed. It is only necessary to perform once, so that the quality of treated water can be remarkably stabilized, and the energy required for cleaning can be greatly improved as compared with the conventional immersion filter apparatus requiring the same strong cleaning as the special cleaning every time. Can be reduced than before.

本発明において使用する充填材4は、被処理水中で浮
上しかつ比重が0.9以上、1.0未満のもの(充填材4A)
と、被処理水中で沈降しかつ比重が1.0以上、1.1以下の
もの(充填材4B)とを混合したもので、被処理水中で浮
上するものであってもその比重が0.9未満のものは、前
述の如く浮力が大き過ぎて洗浄時に流動化させることが
難しく、又、沈降するものであっても比重が1.1を超え
るものは重過ぎてやはり流動化させるのに大きな動力を
必要とするので好ましくない。なお、混合するそれぞれ
の充填材4A、4Bは上記条件を満たすものであればいかな
るものでもよく、単一比重のものであっても、一定の比
重幅をもったものであってもどちらでもよい。
Filler 4 used in the present invention floats in the water to be treated and has a specific gravity of 0.9 or more and less than 1.0 (filler 4A)
And those that settle in the water to be treated and have a specific gravity of 1.0 or more and 1.1 or less (filler 4B), and even those that float in the water to be treated and have a specific gravity of less than 0.9, As described above, the buoyancy is too large to fluidize at the time of washing, and even if it settles, those having a specific gravity of more than 1.1 are too heavy and also require large power to fluidize. Absent. The respective fillers 4A and 4B to be mixed may be any as long as the above conditions are satisfied, and may be a single specific gravity, or may have a specific specific width. .

又、被処理水中で浮上する充填材4Aと、被処理水中で
沈降する充填材4Bとの混合割合は、被処理水中で浮上す
るものが30〜70%、被処理水中で沈降するものが70〜30
%となるように混合するのがよく、望ましくはそれぞれ
の充填材を半々に混合して充填するのがよい。このよう
な混合割合とすることにより、充填材層の効果的な洗浄
が行え、かつ、洗浄直後の通水処理における処理水質の
一時的な悪化を極力少なくできる浸漬濾床装置を得るこ
とが出来る。
In addition, the mixing ratio of the filler 4A floating in the water to be treated and the filler 4B sinking in the water to be treated is 30 to 70% of those floating in the water to be treated, and 70% of those floating in the water to be treated. ~ 30
%, And preferably each filler is mixed in half and filled. By using such a mixing ratio, it is possible to obtain an immersion filter bed device capable of effectively cleaning the filler layer and reducing the temporary deterioration of the treated water quality in the water passing treatment immediately after the cleaning as much as possible. .

上述の実施態様においては被処理水を充填材層内に上
向流で流過させる構成としたが、本発明は被処理水を下
向流で流過させる構成とすることも可能である。
In the above-described embodiment, the configuration is such that the water to be treated flows through the filler layer in the upward flow, but the present invention may be configured to flow the water to be treated in the downward flow.

以上、好気性微生物を用いた浸漬濾床装置に本発明を
適用した一例を説明したが、嫌気性微生物を用いた浸漬
濾床装置、例えば嫌気性醗酵装置に本発明を適用した場
合も、槽1の上部を密閉して発生するガスを集め、その
集めたガスを空気の代わりに散気管13の穴より流入する
以外は好気性微生物を用いた浸漬濾床装置と同じである
ので、詳細な説明は省略する。
As described above, an example in which the present invention is applied to a immersion filter bed apparatus using an aerobic microorganism has been described.However, even when the present invention is applied to an immersion filter bed apparatus using an anaerobic microorganism, for example, an anaerobic fermentation apparatus, a tank is used. The gas generated by closing the upper part of 1 is collected, and the collected gas flows in through the hole of the air diffuser 13 instead of air. Description is omitted.

<効果> 以上説明した如く、本発明においては浸漬濾床装置の
充填材として、被処理水中で浮上しかつ比重が0.9以
上、1.0未満のものと、被処理水中で沈降しかつ比重が
1.0以上、1.1以下のものとの、いずれも槽内の水の比重
に近い2種類の粒状物を混合した充填材を使用するの
で、洗浄において、充填材を流動化させるための水ある
いは空気の流量が少なくてよく省エネルギー的である。
更に、当該充填材は槽内において浮上充填材層と沈降充
填材層とを別個に形成するので、通常の洗浄においては
被処理水が流入する側の、微生物の肥大化が激しく目詰
まりの頻度が高い一方の充填材層のみを選択的に流動化
させて洗浄することが出来、当該洗浄を繰り返して両充
填材層ともに目詰まりを起こした場合にのみ、充填材層
全体を流動化させる洗浄を行えばよいので、洗浄毎に充
填材層全体を強力に洗浄しなければならない従来装置に
比べて着生微生物が過剰に剥離する度合が少なく、槽内
の微生物保有量を高く維持することが出来、従って、洗
浄直後の通水処理における処理水質の一時的な悪化を極
力防止し、処理水質を飛躍的に安定化させることが出来
る。
<Effects> As described above, in the present invention, as a filler of the immersion filter bed device, a material that floats in the water to be treated and has a specific gravity of 0.9 or more and less than 1.0, and a material that sediments in the water to be treated and has a specific gravity of 0.9 or less.
1.0 or more and 1.1 or less, both of which use a filler mixture of two types of particulate matter close to the specific gravity of the water in the tank, so in cleaning, water or air for fluidizing the filler is used. Low flow rate and energy saving.
Furthermore, since the filler forms a floating filler layer and a sedimentary filler layer separately in the tank, in normal cleaning, microorganisms are greatly enlarged on the side to which the water to be treated flows, and the frequency of clogging is severe. Cleaning can be performed by selectively fluidizing only one of the filler layers, and only when the cleaning is repeated and both filler layers are clogged. Therefore, it is possible to maintain a high level of microorganisms in the tank, because the degree of exfoliation of epiphytic microorganisms is less than that of conventional equipment, in which the entire filler layer must be strongly washed every time washing is performed. Therefore, it is possible to prevent the temporary deterioration of the treated water quality in the water passing treatment immediately after washing as much as possible, and to stabilize the treated water quality dramatically.

<実施例> 以下に、本発明の効果をより明確とするために実施例
を説明する。
<Examples> Examples will be described below to clarify the effects of the present invention.

粒径15〜30mmでほぼ球形の人工石からなる、比重0.95
の粒状物と比重1.05の粒状物とを半々に混合した混合粒
状物を充填材とし、その実質充填層高(図面において空
所7を除いた、充填材のみの層高)を3.4mとした図面に
示したような浸漬濾床装置A(本発明例)と、粒径15〜
30mm、比重1.5の人工石を充填材とし、その充填材層高
を3.4mとした浸漬濾床装置B(従来例)とを使用し、そ
れぞれ以下のような条件で洗浄を定期的に行いながら食
品加工廃水の好気性処理を継続して行い、定常状態にお
ける両装置のCOD除去性能を比較した。
Made of almost spherical artificial stone with a particle size of 15 to 30 mm, specific gravity 0.95
And a granular material having a specific gravity of 1.05 mixed in halves was used as a filler, and the actual packed bed height (layer height of the filler alone excluding the void 7 in the drawing) was 3.4 m. A immersion filter bed apparatus A (example of the present invention) as shown in the drawing, with a particle size of 15 to
Using artificial stone with 30 mm and specific gravity of 1.5 as filler, and using a dipping filter bed apparatus B (conventional example) with a filler layer height of 3.4 m, while periodically performing cleaning under the following conditions, respectively. The aerobic treatment of food processing wastewater was continuously performed, and the COD removal performance of both devices in a steady state was compared.

洗浄条件 (1)浸漬濾床装置A(本発明例) 通常洗浄:1日1回、20分間 特別洗浄:10日に1回(洗浄空気単独の工程:10分間、洗
浄空気、洗浄水併用の工程:20分間) (2)浸漬濾床装置B(従来例) 前記特別洗浄と同じ洗浄を1日1回 その結果、本発明例である浸漬濾床装置Aにおいて
は、特別洗浄直後の通水処理においては処理性能の低下
が見られたが(COD除去率50〜60%)、その他はCOD除去
率70〜80%の性能が安定して得られ、かつ、充填材層の
目詰まりは充分に解消されていた。これに対し、浸漬濾
床装置Bにおいては、通常処理時のCOD除去率が60〜70
%であったのに対し、洗浄直後の通水においてはCOD除
去率が毎回40〜50%に低下したと同時に、洗浄時の目詰
まり解消がやや不充分であったために、充填材層は常に
多少閉塞傾向にあり、そのため通常処理時のCOD除去能
力自体も前記の如く本発明例に比べて低下している。
Washing conditions (1) Immersion filter bed device A (Example of the present invention) Normal washing: once a day for 20 minutes Special washing: once a day (process of washing air alone: 10 minutes, washing air and washing water combined use) (Step: 20 minutes) (2) Immersion filter bed apparatus B (conventional example) The same washing as the above-mentioned special washing is performed once a day. As a result, in the immersion filter bed apparatus A which is an example of the present invention, water is passed immediately after the special washing. Degradation of processing performance was observed in the processing (COD removal rate of 50-60%), but in other cases, the performance of COD removal rate of 70-80% was obtained stably, and the clogging of the filler layer was sufficient Had been resolved. On the other hand, in the immersion filter bed apparatus B, the COD removal rate during the normal treatment is 60-70.
%, While the COD removal rate dropped to 40 to 50% every time when water was passed immediately after washing, and at the same time the clogging during washing was somewhat inadequate. There is a tendency to be somewhat clogged, so that the COD removal ability itself during normal processing is also lower than that of the present invention as described above.

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

図面は好気性微生物を用いた浸漬濾床装置に本発明を適
用した一例を示す縦断面説明図である。 1……槽、2……床板 3……コレクター、4……充填材 5……浮上充填材層、6……沈降充填材層 7……空所、8……充填層部 9……原水管、10……洗浄水管 11……散水管、12……空気管 13……散気管、14……出口管
The drawing is an explanatory longitudinal sectional view showing an example in which the present invention is applied to a immersion filter bed device using an aerobic microorganism. DESCRIPTION OF SYMBOLS 1 ... Tank, 2 ... Floor plate 3 ... Collector, 4 ... Filler 5 ... Floating filler layer, 6 ... Settling filler layer 7 ... Vacancy, 8 ... Filling layer part 9 ... Original Water pipe, 10 ... Cleaning water pipe 11 ... Sprinkling pipe, 12 ... Air pipe 13 ... Diffusion pipe, 14 ... Outlet pipe

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】微生物はその表面に着生させた充填材を槽
内に充填して充填材層を形成し、前記充填材として、被
処理水中で浮上して浮上充填材層を形成する比重が0.9
以上,1.0未満のものと、被処理水中で沈降して沈降充填
材層を形成する比重が1.0以上,1.1以下のものとの2種
類の粒状物を、両充填材層の間に洗浄時の充填材流動化
のための空所を形成するように充填し、当該充填材層に
被処理水を流入して被処理水を生物学的に処理する浸漬
濾床法生物学的処理装置において、主に微生物の肥大化
が激しく目詰りの頻度が高い一方の充填材層を流動化さ
せる部分的洗浄と、両充填材層ともに目詰りを起した場
合に充填材層全体を流動化させる全体洗浄とを選択して
行うことを特徴とする浸漬濾床法生物学的処理装置の洗
浄方法。
A microorganism fills a tank with a filler that has settled on its surface to form a filler layer, and as the filler, a specific gravity for floating in the water to be treated to form a floating filler layer. Is 0.9
Above, less than 1.0, and two types of particulate matter, the specific gravity of which is settled in the treated water to form a settling filler layer is 1.0 or more, 1.1 or less, between the two filler layers when washing Filling to form a space for fluidization of the filler, in the immersion filter bed biological treatment apparatus for biologically treating the water to be treated by flowing the water to be treated into the filler layer, Partial washing to fluidize one of the packing layers, mainly due to microbial enlargement and high frequency of clogging, and total washing to fluidize the entire packing layer when both packing layers are clogged And a method for cleaning a biological treatment apparatus using a immersion filter bed method.
JP62062750A 1987-03-19 1987-03-19 Immersion filter bed method for cleaning biological treatment equipment Expired - Fee Related JP2584763B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62062750A JP2584763B2 (en) 1987-03-19 1987-03-19 Immersion filter bed method for cleaning biological treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62062750A JP2584763B2 (en) 1987-03-19 1987-03-19 Immersion filter bed method for cleaning biological treatment equipment

Publications (2)

Publication Number Publication Date
JPS63232892A JPS63232892A (en) 1988-09-28
JP2584763B2 true JP2584763B2 (en) 1997-02-26

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