JPH09308892A - Biological purification of waste water and waste water treatment apparatus - Google Patents

Biological purification of waste water and waste water treatment apparatus

Info

Publication number
JPH09308892A
JPH09308892A JP15009196A JP15009196A JPH09308892A JP H09308892 A JPH09308892 A JP H09308892A JP 15009196 A JP15009196 A JP 15009196A JP 15009196 A JP15009196 A JP 15009196A JP H09308892 A JPH09308892 A JP H09308892A
Authority
JP
Japan
Prior art keywords
tank
carrier
tanks
treated
aerobic decomposition
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP15009196A
Other languages
Japanese (ja)
Other versions
JP3457125B2 (en
Inventor
Kiyohide Idogawa
清秀 伊戸川
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.)
CLEAN TEC KK
Original Assignee
CLEAN TEC KK
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 CLEAN TEC KK filed Critical CLEAN TEC KK
Priority to JP15009196A priority Critical patent/JP3457125B2/en
Publication of JPH09308892A publication Critical patent/JPH09308892A/en
Application granted granted Critical
Publication of JP3457125B2 publication Critical patent/JP3457125B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste water purifying method and a waste water treatment apparatus not almost generating the abrasion of a floatable carrier in an aerobic decomposition tank and facilitating the culture of bacteria on the carrier and having large aerobic decomposition capacity. SOLUTION: An aerobic decomposition tank 1 is laterally partitioned into two tanks by a partition wall 2 and a reticulated material 3 preventing the passage of a carrier is horizontally provided to the respective tanks in a single stage or a multistage fashion to demarcate the respective tanks into a plurality of chambers in an up and down direction. The respective chambers are loosely packed with the floatable carrier. Air diffusing and distributing device 5 are provided to the bottom parts of the respective tanks. An opening part 13 is provided to the lower part of the partition wall 2 of the tank communicating with the sedimentation tank 16 of the partitioned aerobic decomposition tank 1 and the front tank adjacent thereto. The transfer pipe 9 returning a part of water to be treated to the front tank by a circulating pump 6 is provided to the tank communicating with the sedimentation tank 16.

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、各種食品材料の調
理ゴミ等の厨芥含有排水、油等を含む排水等を浄化する
排水の生物学的浄化方法及び排水処理装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater biological purification method and wastewater treatment apparatus for purifying wastewater containing garbage such as cooking waste of various food materials, wastewater containing oil and the like.

【0002】[0002]

【従来の技術】従来、排水を浄化するには好気分解槽に
浮上性担体を浸漬し、これに微生物を付着させ、槽内で
被処理水と共に浮上性担体を回流させると共に、好気分
解槽内の底部より空気を送り、有機物を分解する流動床
によっている。
2. Description of the Related Art Conventionally, in order to purify waste water, a buoyant carrier is immersed in an aerobic decomposition tank, microorganisms are allowed to adhere to the tank, and the buoyant carrier is circulated together with the water to be treated in the tank and aerobically decomposed. It uses a fluidized bed that sends air from the bottom of the tank to decompose organic substances.

【0003】[0003]

【発明が解決しようとする課題】従来の流動床で排水を
浄化する場合は、被処理水と共に浮上性担体を回流する
ために大きな動力を必要とすると共に、回流時に浮上性
担体は好気分解槽のコンクリート槽壁に摺擦され摩耗が
激しく、耐久性に欠ける問題があった。又、浮上性担体
の投入初期は微生物の増殖がなく、負荷が小さいため比
重が軽く、水面近くに浮上し旋回が起きないので、浮上
性担体に微生物を予め付着させる馴養のための培養槽を
必要とした。又、好気分解槽内の浮上性担体の投入量も
好気分解槽容積の30%が限度で、それ以上になると回
流しないので、好気分解能力も限定されていた。
When purifying wastewater in a conventional fluidized bed, a large amount of power is required to circulate the flotation carrier together with the water to be treated, and the flotation carrier is aerobically decomposed during circulation. There was a problem in that it was rubbed against the concrete tank wall of the tank and abraded severely, resulting in poor durability. In addition, since the growth of microorganisms does not occur at the initial stage of loading the buoyant carrier, the specific gravity is light because the load is small, and it does not swirl because it floats near the surface of the water, so a culture tank for acclimatization to pre-attach the microorganisms to the buoyant carrier is provided. Needed. Further, the amount of the floatable carrier to be charged in the aerobic decomposition tank is limited to 30% of the aerobic decomposition tank volume, and if it exceeds the limit, the aerobic decomposition capacity is limited because it is not circulated.

【0004】そして、浮上性担体は培養される微生物が
回流や空気流により剥離し易く、かつ浮上性担体はポリ
エステル系の軟質ポリウレタンフォームを使用している
ため加水分解を受け易く、耐久性がないという欠点を有
していた。
The buoyant carrier is liable to be exfoliated by microorganisms to be cultivated due to circulation or air flow, and since the buoyant carrier uses a polyester-based flexible polyurethane foam, it is easily hydrolyzed and has no durability. It had a drawback.

【0005】上記点より本発明は、浮上性担体を有する
微生物固定化担体の摩耗が殆どないと共に、浮上性を有
する微生物固定化担体への微生物の培養も容易で、好気
分解能力も大きな排水の生物学的浄化方法及び排水処理
装置を提供しようとするものである。
From the above point of view, the present invention shows that the microorganism-immobilized carrier having the floatable carrier hardly wears, the microorganism can be easily cultured on the microorganism-immobilized carrier having the floating property, and the aerobic decomposition ability is large. The biological purification method and the wastewater treatment device of the present invention are provided.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
本発明方法は、液化分解処理工程、好気処理工程及び沈
澱処理工程等複数の工程より成る排水処理方法に於い
て、好気分解槽を横方向に仕切り、仕切られた各槽に担
体の通過を阻止する網状体を単段又は多段に水平に横設
して、各槽内を上下方向に数室に区画し、各室に浮上性
を有する微生物固定化担体を緩やかに装入充填し、仕切
られた好気分解槽の沈澱槽に連絡する槽内の被処理水は
上向流で担体層内を通過させ、この槽に隣接する前部の
槽内の被処理水は下向流で担体層内を通過させると共
に、各槽の底部より散気を行い、被処理水を浄化し、前
記沈澱槽に連絡する槽より被処理水の一部を前部の槽へ
返送し、浄化処理を繰り返すことにより有機不純物を含
有する排水を生物学的に浄化することを特徴とするもの
である。
In order to solve the above problems, the method of the present invention is an aerobic decomposition tank comprising a plurality of steps such as a liquefaction decomposition step, an aerobic treatment step and a precipitation treatment step. Is horizontally partitioned, and a mesh-like body that blocks the passage of carriers is horizontally installed horizontally in a single or multi-stage in each partitioned tank, and each tank is divided into several chambers in the vertical direction and floated in each chamber. The carrier for immobilizing microorganisms that has the property of slowly adsorbing and filling, and communicating with the settling tank of the partitioned aerobic decomposition tank The water to be treated in the tank is passed upward through the carrier layer and adjacent to this tank. The water to be treated in the front tank passes through the carrier layer in a downward flow, and air is diffused from the bottom of each tank to purify the water to be treated and to be treated from the tank which communicates with the settling tank. By returning part of the water to the front tank and repeating the purification process, wastewater containing organic impurities can be treated biologically. It is characterized in that the purifying.

【0007】又、本発明方法は、好気分解槽を横方向に
三槽以上に仕切り、沈澱槽に連絡する槽を除き最前部の
槽より後続の槽へ順次被処理水を上方より下向流で各室
の担体層を通過させると共に、沈澱槽に連絡する槽は下
方より上向流で各室の担体層を通過させることを特徴と
するものである。
Further, in the method of the present invention, the aerobic decomposition tank is laterally partitioned into three or more tanks, and the treated water is sequentially directed downward from the foremost tank to the succeeding tank except the tank communicating with the precipitation tank. The carrier layer of each chamber is passed by a flow, and the tank communicating with the precipitation tank is passed through the carrier layer of each chamber in an upward flow from below.

【0008】又、本発明装置は、嫌気分解槽、好気分解
槽、沈澱槽等の複数の処理槽を設け、これ等の処理槽に
被処理水を順次移流して排水の浄化を行う排水処理装置
に於いて、好気分解槽が横方向に仕切られると共に、仕
切られた各槽内は単段又は多段に水平に横設された担体
の通過を阻止する網状体で上下方向に数室に区画され、
各室内に浮上性を有する微生物固定化担体が緩やかに充
填されると共に、各槽の底部に散気分配装置が設置さ
れ、仕切られた好気分解槽の沈澱槽に連絡する槽と、こ
の槽に隣接する前部の槽との仕切り壁の下部に開口部が
設けられると共に、前記沈澱槽に連絡する槽に被処理水
の一部を前部の槽へ返送する移送手段が設けられている
ことを特徴とするものである。
Further, the apparatus of the present invention is provided with a plurality of treatment tanks such as an anaerobic decomposition tank, an aerobic decomposition tank, and a precipitation tank, and the treated water is sequentially transferred to these treatment tanks to purify the wastewater. In the treatment equipment, the aerobic decomposition tank is horizontally partitioned, and each of the partitioned tanks is a single or multi-tiered horizontally-arranged mesh-like body that prevents the passage of carriers. Is divided into
Each chamber was gently filled with a microbial immobilization carrier having buoyancy, and an aeration distribution device was installed at the bottom of each tank, and a tank that communicates with the settling tank of the partitioned aerobic decomposition tank and this tank An opening is provided in the lower part of the partition wall between the front tank and the front tank, and a transfer means for returning a portion of the treated water to the front tank is provided in the tank communicating with the precipitation tank. It is characterized by that.

【0009】又、本発明装置は、好気分解槽を横方向に
三槽以上に仕切り、沈澱槽に連絡する槽を除き最前部の
槽より後続の槽へ順次被処理水が上方より下向流で各室
の担体層内を通過されるよう、前部の槽の底部より後部
の槽の上部へ連絡する流路が前部の槽と後部の槽の仕切
り壁に形成され、沈澱槽に連絡する槽の仕切り壁の下部
に連通部が設けられていることを特徴とするものであ
る。
Further, in the apparatus of the present invention, the aerobic decomposition tank is laterally partitioned into three or more tanks, and the treated water is sequentially directed downward from the top tank to the succeeding tank except the tank communicating with the precipitation tank. A flow path that connects the bottom of the front tank to the top of the rear tank is formed in the partition walls of the front tank and the rear tank so that it can be passed through the carrier layer of each chamber by the flow. A communication part is provided below the partition wall of the tank to be connected.

【0010】よって、本発明方法及び装置は、微生物固
定化担体(以下、担体と称する)は網状体で上下を区画
された室内に緩やかに装入充填されるため浮揚状態にあ
り、周囲に微細気泡が付着して浮き上がっても各室は担
体の通過を阻止する網状体で区画されているため、各室
に担体層が形成される。
Therefore, according to the method and apparatus of the present invention, since the microorganism-immobilized carrier (hereinafter referred to as carrier) is gently charged and filled in the chamber divided into upper and lower parts by the mesh-like body, it is in a floating state, and the fine particles are surrounded. Even if air bubbles adhere and float up, each chamber is defined by a net-like body that prevents passage of the carrier, so that a carrier layer is formed in each chamber.

【0011】そして、担体に微生物が増殖されると、比
重が増し沈下しようとするが、各槽の底部からの散気に
よる空気流により浮揚すると共に、仕切られた好気分解
槽の沈澱槽に連絡する槽を除いた各槽の上方からは被処
理水が下向流で担体層を通過するので、殆ど移動するこ
となく上方で浮揚状態にあり、被処理水のみが担体間を
通過する。
When the microorganisms grow on the carrier, the specific gravity increases and the particles tend to sink. However, they are levitated by the air flow from the bottom of each tank due to the air diffusion, and the microorganisms grow in the settling tank of the partitioned aerobic decomposition tank. Since the water to be treated passes through the carrier layer in a downward flow from the upper side of each tank except the connecting tank, it is in a floating state above without moving, and only the water to be treated passes between the carriers.

【0012】又、好気分解槽が二槽以上に仕切られ、か
つ各槽が上下方向に数室に区画されているため、被処理
水は複数回担体層を通過すると共に、沈澱槽に連絡する
槽より被処理水の一部を二槽の場合は前部の槽、三槽以
上の場合は最前部の槽へ返送し浄化処理を繰り返すこと
により効率よく浄化される。
Further, since the aerobic decomposition tank is divided into two or more tanks and each tank is divided into several chambers in the vertical direction, the water to be treated passes through the carrier layer a plurality of times and communicates with the precipitation tank. In case of two tanks, a part of the water to be treated is returned to the front tank, and in the case of three or more tanks, it is returned to the front tank and the purification treatment is repeated, whereby the water is efficiently purified.

【0013】又、網状体は槽の上方からの被処理水の下
向流及び槽底部よりの空気流により目詰りが防止され
る。被処理水は沈澱槽に連絡する槽を除いた各槽総て上
方から下向流となるため、各槽同様の作用を有する。
尚、好気分解槽の沈澱槽に連絡する槽は浮上性の担体充
填層に対し上向流に被処理水を通過させるが、上下方向
に数段の網状体で担体層を分割することにより、下部の
散気による空気は充填担体を流動化するため、微細粒子
の捕捉力は低下するが生物による酸化分解力は向上す
る。
The mesh is prevented from clogging by the downward flow of the water to be treated from above the tank and the air flow from the bottom of the tank. Since the water to be treated flows downward from all the tanks except the tank connected to the settling tank, it has the same action as each tank.
In addition, the tank communicating with the settling tank of the aerobic decomposition tank passes the water to be treated in an upward flow with respect to the floatable carrier-packed layer, but by dividing the carrier layer by several stages of meshes in the vertical direction Since air due to air diffusion in the lower part fluidizes the packed carrier, the capturing power of fine particles is reduced but the oxidative decomposition power by organisms is improved.

【0014】又、本発明方法及び装置に使用される担体
の特徴は、微生物固定化担体は主原料であるポリオール
の高分子鎖がエーテル結合から成る軟質ポリウレタンフ
ォームで、内面および外面の気孔が互いに連通した一辺
の大きさが10〜30mmのサイコロ形の粒状物である
ものである。
The carrier used in the method and apparatus of the present invention is characterized in that the carrier for immobilizing microorganisms is a flexible polyurethane foam in which the polymer chain of the polyol, which is the main raw material, is composed of ether bonds, and the pores on the inner and outer surfaces are mutually It is a dice-shaped granular material having a size of one side that communicates with each other of 10 to 30 mm.

【0015】よって、本発明担体はエーテル系の軟質ポ
リウレタンフォームを使用しているため加水分解を受け
難く、耐久性も十分である。そして、内面および外面の
気孔が互いに連通しているので、微生物は担体の表面だ
けでなく内部に入り込むため培養が容易であると共に、
被処理水や空気流によって微生物が剥離せず、担体の内
部で被処理水を浄化する。
Therefore, since the carrier of the present invention uses the flexible polyurethane foam of ether type, it is hard to be hydrolyzed and has sufficient durability. And, since the pores on the inner surface and the outer surface are in communication with each other, the microorganisms can be easily cultured because they enter not only the surface of the carrier but also the inside thereof.
Microorganisms are not separated by the water to be treated or the air flow, and the water to be treated is purified inside the carrier.

【0016】[0016]

【発明の実施の形態】以下、本発明の一実施の形態を図
面に基づき説明する。図1は本発明方法および装置の一
実施の形態を示し好気分解槽が二槽に仕切られた場合
の、図2は同上の好気分解槽が三槽に仕切られた場合の
断面図、図3は同上の一部平面図、図4は同上の作用を
示す部分拡大断面図である。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. 1 shows an embodiment of the method and apparatus of the present invention, and FIG. 2 is a sectional view when the aerobic decomposition tank is divided into two tanks, and FIG. 2 is a sectional view when the aerobic decomposition tank is divided into three tanks. FIG. 3 is a partial plan view of the above, and FIG. 4 is a partial enlarged sectional view showing the operation of the above.

【0017】而して、図中1は好気分解槽であり、図1
では仕切り壁2により二槽に仕切られている。図2では
三槽となっているが、横方向に三槽以上に仕切ることも
できる。各槽内は上方部、下方部およびその間に二箇所
水平に網状体3が横設されて、上部室1Aと中央室1B
及び下部室1Cに区画されている。図面では三室に区画
されているが、それ以外単段又は多段の室に区画するこ
ともできる。
1 is an aerobic decomposition tank.
Then, it is divided into two tanks by the partition wall 2. In FIG. 2, it is divided into three tanks, but it is also possible to laterally partition into three or more tanks. Inside each tank, a net 3 is horizontally installed in two parts, an upper part, a lower part and between them, and an upper chamber 1A and a central chamber 1B are provided.
And the lower chamber 1C. Although it is divided into three chambers in the drawing, it may be divided into a single-stage or multi-stage chamber.

【0018】上部室1Aと中央室1B、及び下部室1C
内には、被処理水中に含まれる有機不純物を好気分解す
る好気性微生物が担持された浮上性を有する担体4が緩
やかに多数充填されている。前記網状体3の網目は担体
4の通過を阻止する大きさに形成されており、担体4は
室内より出ることはない。
Upper chamber 1A, central chamber 1B, and lower chamber 1C
A large number of floatable carriers 4 carrying aerobic microorganisms that aerobically decompose organic impurities contained in the water to be treated are gently filled therein. The mesh of the mesh body 3 is formed in a size that prevents the carrier 4 from passing therethrough, and the carrier 4 does not come out of the room.

【0018】担体4は主原料であるポリオールの高分子
鎖がエーテル結合から成る軟質ポリウレタンフォーム
で、内面および外面の気孔が互いに連通した一辺の大き
さが10〜30mmのサイコロ形の粒状物であり、密度
16〜70kg/m3、比重0.016〜0.07、
0.5〜1.0mmの気孔が互いに連通している。各槽
に充填される担体の充填率は、各槽容積の30〜80%
の容積分に相応する量である。
The carrier 4 is a soft polyurethane foam in which the polymer chain of the polyol, which is the main raw material, is composed of ether bonds, and is a dice-shaped granular material having pores on the inner and outer surfaces communicating with each other and having a side of 10 to 30 mm. , Density 16 to 70 kg / m 3 , specific gravity 0.016 to 0.07,
Pores of 0.5 to 1.0 mm communicate with each other. The filling rate of the carrier filled in each tank is 30 to 80% of the volume of each tank.
It is an amount corresponding to the volume of.

【0019】5は好気分解槽1の仕切られた各槽の底部
に設けた散気分配装置であり、好気分解槽1外に設けた
ポンプより供給管6を経て、空気又は純粋な酸素が各槽
内に供給される。7は排水供給管であり、排水供給管7
は前工程の嫌気分解槽(図示せず)で処理された排水を
二槽に仕切られた好気分解槽では前部の槽内上方に導入
し、三槽以上に仕切られた好気分解槽では最前部の槽内
に導入する。8は仕切られた好気分解槽1の沈澱槽16
に連絡する槽に設けた循環ポンプであり、沈澱槽16に
連絡する槽内の被処理水の一部を二槽の場合は前部の槽
へ、又三槽以上の場合は最前部の槽内の上部へ返送する
移送管9と連結している。
Reference numeral 5 denotes an air diffuser provided at the bottom of each of the partitioned aerobic decomposition tanks 1. Air or pure oxygen is supplied from a pump provided outside the aerobic decomposition tank 1 through a supply pipe 6. Is supplied to each tank. 7 is a drainage supply pipe, and the drainage supply pipe 7
In the aerobic decomposition tank divided into two tanks, the wastewater treated in the anaerobic decomposition tank (not shown) in the previous process is introduced above the inside of the front tank, and the aerobic decomposition tank divided into three or more tanks. Then, it is introduced into the front tank. 8 is a settling tank 16 of the aerobic decomposition tank 1 partitioned
Is a circulation pump provided in the tank that communicates with the settling tank 16, and if a part of the water to be treated in the tank that communicates with the settling tank 16 is two tanks, to the front tank, and if there are three or more tanks, the front tank It is connected to a transfer pipe 9 for returning to the upper part inside.

【0020】10は三槽以上の場合沈澱槽16に連絡す
る槽に隣接する前部の槽及びこの槽より前方の槽の仕切
り壁2に形成された四方を壁で仕切られた被処理水の流
路であり、流路10は下部に前部の槽の底部に通じる連
通孔11が設けられ、上部は後続の槽の上部に開口12
している垂直に上方へ延長した煙突状に形成されてい
る。13は沈澱槽16に連絡する槽とこの槽に隣接する
前部の槽との仕切り壁2の下部に設けた開口部であり、
前部の槽の被処理水が開口部13より流入し上向流とな
る。14は排気管、15は仕切られた好気分解槽1の沈
澱槽16に連絡する槽より沈澱槽16へ被処理水を導入
する移流管、17は沈澱槽16の被処理水排出管、18
は沈澱槽16の底部に設けた汚泥排出管である。
In the case of three or more tanks, the water to be treated is divided into four parts by the front wall adjacent to the tank connected to the settling tank 16 and the partition wall 2 of the tank in front of this tank. The flow channel 10 is provided with a communication hole 11 in the lower portion, which communicates with the bottom of the front tank, and an upper portion with an opening 12 in the upper portion of the subsequent tank.
It is shaped like a chimney that extends vertically upward. Reference numeral 13 denotes an opening provided in the lower part of the partition wall 2 between the tank communicating with the precipitation tank 16 and the front tank adjacent to this tank,
The water to be treated in the front tank flows in through the opening 13 and becomes an upward flow. Reference numeral 14 is an exhaust pipe, 15 is an advection pipe for introducing treated water into the precipitation tank 16 from a tank connected to the settling tank 16 of the aerobic decomposition tank 1, and 17 is a treated water discharge tube of the precipitation tank 16.
Is a sludge discharge pipe provided at the bottom of the settling tank 16.

【0021】次に、被処理水の浄化方法を図につき説明
する。好気分解槽1が二槽に仕切られた場合は排水供給
管7より好気分解槽1の前部の槽内の上方に又、好気分
解槽1が三槽以上に仕切られた場合は最前部の槽内の上
方に夫々導入された被処理水は、下向流Aで槽内の上部
室1A内の担体4層より中央室1B及び下部室1C内の
担体4層を通過するが、担体4には好気性微生物が担持
され、これにより好気分解を受ける。担体4は被処理水
の下向流Aと下方よりの空気流Bにより浮揚状態にあ
り、移動はしない。
Next, a method for purifying water to be treated will be described with reference to the drawings. When the aerobic decomposition tank 1 is partitioned into two tanks, when the aerobic decomposition tank 1 is partitioned into three tanks or more above the drainage supply pipe 7 in the front of the aerobic decomposition tank 1. The water to be treated introduced into the upper part of the tank in the uppermost part passes through the four layers of the carrier in the central chamber 1B and the lower chamber 1C from the four layers of the carrier in the upper chamber 1A in the tank in the downward flow A. The carrier 4 carries aerobic microorganisms, which undergo aerobic decomposition. The carrier 4 is in a floating state due to the downward flow A of the water to be treated and the air flow B from below, and does not move.

【0022】そして、好気分解を受けた被処理水は、二
槽に仕切られた場合は仕切り壁2の下部に設けた開口部
13より沈澱槽16に連絡する槽へ流入され、又三槽以
上に仕切られた場合は槽の底部の連通孔11より流路1
0を通り、開口12部より後続の槽の上方へ導入され、
再び下向流Aで担体4層により好気分解を受け、沈澱槽
16に連絡する槽とこの槽に隣接する前部の槽との仕切
り壁2の底部の開口部13より沈澱槽16に隣接する槽
内に上向流Cで流入され、この槽内の被処理水の一部は
更に二槽に仕切られた場合は前部の槽の上部へ又、三槽
以上に仕切られた場合は最前部の槽へ夫々移送管9によ
り返送され、繰り返し好気分解を受け、沈澱槽16に連
絡する槽より移流管15で沈澱槽16へ移流される。
When the water to be treated that has undergone aerobic decomposition is divided into two tanks, it flows into the tank communicating with the settling tank 16 through the opening 13 provided in the lower portion of the partition wall 2, and also three tanks. When it is divided into the above, the flow path 1 is made through the communication hole 11 at the bottom of the tank.
It is introduced through 0 through the opening 12 to the upper part of the following tank,
Again, in the downward flow A, the carrier 4 layers aerobically decomposed, adjoining the precipitation tank 16 through the opening 13 at the bottom of the partition wall 2 between the tank communicating with the precipitation tank 16 and the front tank adjacent to this tank. In the case where a part of the water to be treated in this tank is divided into two tanks by an upward flow C, the upper part of the tank is divided into two tanks. It is returned to the frontmost tank by the transfer pipe 9, repeatedly aerobically decomposed, and transferred to the precipitation tank 16 by the advection pipe 15 from the tank communicating with the precipitation tank 16.

【0023】[0023]

【発明の効果】本発明によれば、担体は上方からの被処
理水による下向流と下部からの空気流とにより移動する
ことなく、浮揚状態で被処理水のみが担体間を通過する
ため、担体を回流するものに比較して動力が少なくて済
むと共に、回流による担体の摩耗がなく、耐久性を有す
る。又、担体を回流しないので好気分解槽1への初期の
投入に際し、微生物の増殖がなくても馴養の必要がない
と共に、担体の投入量も好気分解槽容積の30〜80%
の容積分に相応する量となり、好気分解能力が格段に向
上できる。そして被処理水は担体層を繰り返し通過する
ため、効率よく浄化を受ける。又、被処理水は沈澱槽に
連絡する槽を除いて槽の上方より下向流で導入されるた
め、総ての槽内で同様の条件で浄化される。尚、三槽以
上に仕切られた場合流路を設けたことは清掃時に便利な
利点を有する。又、浮上性の担体充填層に対し上向流に
被処理水を通過させると充填層にて微細粒子を捕捉し、
1〜2日間程度で充填層が目詰まりする欠点があった
が、上下方向に数段の網状体で充填層を分割することに
より下部の散気による空気は充填担体を流動化するため
微細粒子の捕捉力は低下するが生物による酸化分解力は
向上する。又、担体はエーテル系の軟質ポリウレタンフ
ォームを使用しているため、加水分解を受け難く耐久性
も十分有すると共に、内面及び外面の気孔が互いに連通
しているので、微生物は担体の内部に入り込むため培養
が容易で、被処理水や空気流によって微生物が剥離しな
い等有用な発明である。
According to the present invention, the carrier does not move due to the downward flow of the treated water from above and the air flow from the lower side, and only the treated water passes between the carriers in the floating state. In addition, it requires less power than a carrier that circulates, and has durability without wear of the carrier due to circulation. Further, since the carrier is not circulated, it is not necessary to acclimate at the time of initial charging to the aerobic decomposition tank 1 even if there is no growth of microorganisms, and the amount of the carrier charged is 30 to 80% of the aerobic decomposition tank volume.
The amount is equivalent to the volume of, and the aerobic decomposition ability can be significantly improved. Since the water to be treated repeatedly passes through the carrier layer, it is efficiently purified. Further, since the water to be treated is introduced in a downward flow from above the tank except for the tank communicating with the settling tank, it is purified under the same conditions in all the tanks. It should be noted that the provision of the flow path when it is partitioned into three or more tanks has an advantage that it is convenient for cleaning. Also, when the water to be treated is passed in an upward flow with respect to the floatable carrier packed bed, fine particles are captured in the packed bed,
Although there was a drawback that the packed bed was clogged in about 1 to 2 days, by dividing the packed bed by several stages of meshes in the vertical direction, air due to air diffusion in the lower part fluidized the packed carrier and thus fine particles were obtained. The ability to capture oxidase is reduced, but the ability to be decomposed by living organisms is improved. In addition, since the carrier uses an ether type flexible polyurethane foam, it is hard to undergo hydrolysis and has sufficient durability, and since the pores on the inner and outer surfaces are in communication with each other, microorganisms enter the carrier. It is a useful invention because it is easily cultivated and microorganisms are not separated by the water to be treated or the air flow.

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

【図1】本発明による装置の一実施の形態を示し、好気
分解槽が二槽に仕切られた場合の断面図である。
FIG. 1 is a cross-sectional view showing an embodiment of an apparatus according to the present invention, in which an aerobic decomposition tank is divided into two tanks.

【図2】本発明による装置の一実施の形態を示し、好気
分解槽が三槽に仕切られた場合の断面図である。
FIG. 2 is a cross-sectional view showing an embodiment of the apparatus according to the present invention, in which the aerobic decomposition tank is divided into three tanks.

【図3】本発明による装置の一実施の形態を示し、好気
分解槽が三槽に仕切られた場合の一部平面図である。
FIG. 3 is a partial plan view showing an embodiment of the apparatus according to the present invention, in which the aerobic decomposition tank is divided into three tanks.

【図4】本発明による装置の作用を示す部分拡大断面図
である。
FIG. 4 is a partially enlarged sectional view showing the operation of the device according to the present invention.

【符号の説明】[Explanation of symbols]

1 好気分解槽 1A 好気分解槽の上部室 1B 好気分解槽の中央室 1C 好気分解槽の下部室 2 仕切り壁 3 網状体 4 微生物固定化担体 5 散気分配装置 6 供給管 7 排水供給管 8 循環ポンプ 9 移送管 10 流路 11 連通孔 12 開口 13 開口部 14 排気管 15 移流管 16 沈澱槽 17 被処理水排出管 18 汚泥排出管 A 被処理水の下向流 B 空気流 C 上向流 1 Aerobic decomposition tank 1A Upper chamber of aerobic decomposition tank 1B Central chamber of aerobic decomposition tank 1C Lower chamber of aerobic decomposition tank 2 Partition wall 3 Reticulate body 4 Microorganism immobilization carrier 5 Aeration distribution device 6 Supply pipe 7 Drainage Supply pipe 8 Circulation pump 9 Transfer pipe 10 Flow path 11 Communication hole 12 Opening 13 Opening 14 Exhaust pipe 15 Advection pipe 16 Settling tank 17 Treated water discharge pipe 18 Sludge discharge pipe A Downflow of treated water B Air flow C Upward flow

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 液化分解処理工程、好気処理工程及び沈
澱処理工程等複数の工程より成る排水処理方法に於い
て、好気分解槽を横方向に仕切り、仕切られた各槽に担
体の通過を阻止する網状体を単段又は多段に水平に横設
して、各槽内を上下方向に数室に区画し、各室に浮上性
を有する微生物固定化担体を緩やかに装入充填し、仕切
られた好気分解槽の沈澱槽に連絡する槽内の被処理水は
上向流で担体層内を通過させ、この槽に隣接する前部の
槽内の被処理水は下向流で担体層内を通過させると共
に、各槽の底部より散気を行い、被処理水を浄化し、前
記沈澱槽に連絡する槽より被処理水の一部を前部の槽へ
返送し、浄化処理を繰り返すことにより有機不純物を含
有する排水を生物学的に浄化することを特徴とする排水
の生物学的浄化方法。
1. In a wastewater treatment method comprising a plurality of steps such as a liquefaction decomposition treatment step, an aerobic treatment step and a precipitation treatment step, an aerobic decomposition tank is laterally partitioned, and a carrier is passed through each partitioned tank. Horizontally installed in a single or multi-stage horizontally to prevent the, each chamber is divided into several chambers in the vertical direction, each chamber is gently charged and filled with a microbial immobilization carrier having levitation properties, The treated water in the tank connected to the settling tank of the partitioned aerobic decomposition tank passes through the carrier layer in an upward flow, and the treated water in the front tank adjacent to this tank flows in a downward flow. While passing through the carrier layer, air is diffused from the bottom of each tank to purify the water to be treated, and a portion of the water to be treated is returned from the tank that connects to the settling tank to the front tank for purification treatment. A biological purification method for wastewater, characterized in that the wastewater containing organic impurities is biologically purified by repeating.
【請求項2】 好気分解槽を横方向に三槽以上に仕切
り、沈澱槽に連絡する槽を除き最前部の槽より後続の槽
へ順次被処理水を上方より下向流で各室の担体層を通過
させると共に、沈澱槽に連絡する槽は下方より上向流で
各室の担体層を通過させることを特徴とする請求項1記
載の排水の生物学的浄化方法。
2. The aerobic decomposition tank is laterally partitioned into three or more tanks, except for the tank communicating with the settling tank, from the frontmost tank to the succeeding tank, the treated water is sequentially flowed downward from above. 2. The method for biologically purifying wastewater according to claim 1, wherein the carrier layer is passed through, and the tank communicating with the precipitation tank is passed through the carrier layer in each chamber in an upward flow from below.
【請求項3】 微生物固定化担体は、主原料であるポリ
オールの高分子鎖がエーテル結合から成る軟質ポリウレ
タンフォームで、内面及び外面の気孔が互いに連通した
一辺の大きさが10〜30mmのサイコロ形の粒状物で
ある請求項1又は2記載の排水の生物学的浄化方法。
3. The microorganism-immobilized carrier is a flexible polyurethane foam in which a polymer chain of a polyol, which is a main raw material, has an ether bond, and has a size of 10 to 30 mm on one side in which pores on the inner surface and the outer surface communicate with each other. The method for biologically purifying wastewater according to claim 1 or 2, which is a granular substance of.
【請求項4】 嫌気分解槽、好気分解槽、沈澱槽等の複
数の処理槽を設け、これ等の処理槽に被処理水を順次移
流して排水の浄化を行う排水処理装置に於いて、好気分
解槽が横方向に仕切られると共に、仕切られた各槽内は
単段又は多段に水平に横設された担体の通過を阻止する
網状体で上下方向に数室に区画され、各室内に浮上性を
有する微生物固定化担体が緩やかに充填されると共に、
各槽の底部に散気分配装置が設置され、仕切られた好気
分解槽の沈澱槽に連絡する槽と、この槽に隣接する前部
の槽との仕切り壁の下部に開口部が設けられると共に、
前記沈澱槽に連絡する槽に被処理水の一部を前部の槽へ
返送する移送手段が設けられていることを特徴とする排
水処理装置。
4. A wastewater treatment apparatus for cleaning wastewater by providing a plurality of treatment tanks such as an anaerobic decomposition tank, an aerobic decomposition tank, and a precipitation tank, and sequentially advancing the water to be treated to these treatment tanks to purify the wastewater. The aerobic decomposition tank is horizontally partitioned, and each of the partitioned tanks is vertically divided into several chambers by a mesh-like body that prevents the passage of carriers horizontally laid in a single stage or multiple stages. The microorganism-immobilized carrier having buoyancy is gently filled into the room, and
An air diffuser is installed at the bottom of each tank, and an opening is provided at the bottom of the partition wall between the tank that communicates with the settling tank of the aerobic decomposition tank that is partitioned and the front tank that is adjacent to this tank. With
A wastewater treatment device, characterized in that a transfer means for returning part of the water to be treated to the front tank is provided in a tank communicating with the settling tank.
【請求項5】 好気分解槽を横方向に三槽以上に仕切
り、沈澱槽に連絡する槽を除き最前部の槽より後続の槽
へ順次被処理水が上方より下向流で各室の担体層内を通
過されるよう、前部の槽の底部より後部の槽の上部へ連
絡する流路が前部の槽と後部の槽の仕切り壁に形成さ
れ、沈澱槽に連絡する槽の仕切り壁の下部に連通部が設
けられていることを特徴とする請求項4記載の排水処理
装置。
5. The aerobic decomposition tank is laterally partitioned into three or more tanks, and the treated water is sequentially flowed downward from the frontmost tank to the subsequent tank except the tank communicating with the precipitation tank. A flow path that connects the bottom of the front tank to the top of the rear tank is formed in the partition walls of the front and rear tanks so that it can pass through the carrier layer. The wastewater treatment equipment according to claim 4, wherein a communication portion is provided at a lower portion of the wall.
【請求項6】 微生物固定化担体は、主原料であるポリ
オールの高分子鎖がエーテル結合から成る軟質ポリウレ
タンフォームで、内面及び外面の気孔が互いに連通した
一辺の大きさが10〜30mmのサイコロ形の粒状物で
ある請求項4又は5記載の排水処理装置。
6. The microorganism-immobilized carrier is a flexible polyurethane foam in which a polymer chain of a polyol, which is a main raw material, has an ether bond, and a dice shape in which pores on an inner surface and an outer surface communicate with each other and a side of which is 10 to 30 mm. The wastewater treatment device according to claim 4 or 5, which is a granular material.
JP15009196A 1996-05-20 1996-05-20 Wastewater biological purification method and wastewater treatment device Expired - Lifetime JP3457125B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15009196A JP3457125B2 (en) 1996-05-20 1996-05-20 Wastewater biological purification method and wastewater treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15009196A JP3457125B2 (en) 1996-05-20 1996-05-20 Wastewater biological purification method and wastewater treatment device

Publications (2)

Publication Number Publication Date
JPH09308892A true JPH09308892A (en) 1997-12-02
JP3457125B2 JP3457125B2 (en) 2003-10-14

Family

ID=15489323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15009196A Expired - Lifetime JP3457125B2 (en) 1996-05-20 1996-05-20 Wastewater biological purification method and wastewater treatment device

Country Status (1)

Country Link
JP (1) JP3457125B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002113482A (en) * 2000-10-10 2002-04-16 Clean Tec Kk Wastewater treatment apparatus and contact material used therein
JP2019529094A (en) * 2016-05-16 2019-10-17 バン ダン チュオン Sewage treatment equipment and drainage stormwater intake type sewage collection system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002113482A (en) * 2000-10-10 2002-04-16 Clean Tec Kk Wastewater treatment apparatus and contact material used therein
JP2019529094A (en) * 2016-05-16 2019-10-17 バン ダン チュオン Sewage treatment equipment and drainage stormwater intake type sewage collection system

Also Published As

Publication number Publication date
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