JPS6211596A - Treatment of waste water by microbe and apparatus therefor - Google Patents

Treatment of waste water by microbe and apparatus therefor

Info

Publication number
JPS6211596A
JPS6211596A JP60150986A JP15098685A JPS6211596A JP S6211596 A JPS6211596 A JP S6211596A JP 60150986 A JP60150986 A JP 60150986A JP 15098685 A JP15098685 A JP 15098685A JP S6211596 A JPS6211596 A JP S6211596A
Authority
JP
Japan
Prior art keywords
wastewater
column
microorganisms
waste water
bacteria
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
JP60150986A
Other languages
Japanese (ja)
Other versions
JPH0226558B2 (en
Inventor
Shiyunichi Kumaoka
隈岡 俊一
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.)
FUIRUTON INTERNATL KK
Original Assignee
FUIRUTON INTERNATL 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 FUIRUTON INTERNATL KK filed Critical FUIRUTON INTERNATL KK
Priority to JP60150986A priority Critical patent/JPS6211596A/en
Publication of JPS6211596A publication Critical patent/JPS6211596A/en
Publication of JPH0226558B2 publication Critical patent/JPH0226558B2/ja
Granted 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

PURPOSE:To removed COD even in oil-contg. waste water by immobilizing microbes on a ceramic granular material packed in a column, mixing the ceramic granular material with a carbonized material and passing waste water through the column. CONSTITUTION:Microbes capable of treating pollutants in waste water flowing in a column such as org. material digesting bacteria exemplified by methane bacteria and bacilli and inorg. material accumulating independent nutrient bacteria such as nitrification bacteria and iron oxidizing bacteria are immobilized on a porous ceramic granular material packed in a column and obtained by adding a pore forming material to the essential component of clay and baking the mixture, the ceramic granular material and a carbonized material (e.g., activated carbon) are mixed and the waste water is passed through the column. Consequently, the COD in oil-contg. waste water which has not been removed by the conventional method can be removed for a long period.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、担体粒子に定着させた微生物による廃水処理
に係り、更に詳しくはセラミックス粒状物に定着させた
微生物によって各種産業および生活雑廃水等のCOD等
を高効率で除去できるようにした廃水処理方法およびそ
の装置に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to wastewater treatment using microorganisms fixed on carrier particles, and more specifically, the treatment of wastewater from various industries and household wastewater, etc. using microorganisms fixed on ceramic granules. The present invention relates to a wastewater treatment method and apparatus that can remove COD, etc. with high efficiency.

(従来の技術) 従来から、活性炭や砂などの担体粒子に微生物膜を付着
させ流動層を形成させて廃水を生物化学的に処理しよう
とする流動層水処理法は広く知られている。
(Prior Art) Fluidized bed water treatment methods have been widely known in which wastewater is biochemically treated by attaching a microbial film to carrier particles such as activated carbon or sand to form a fluidized bed.

例えば、特公昭59−45439号公報には、微生物を
付着させた粒状媒体の流動床で生物化学的にBOD除去
などを行なう用廃水の生物処理方法が開示され、更に、
該処理方法において、運転初期の微生物の集殖期間中に
先ず前記用廃水を一定期間下向流にて通水し、微生物の
媒体表面への付着を容易にし、微生物の付着、集殖によ
り正常機能に復帰したのちに、上向流に通水して微生物
の付着した粒状媒体を流動化させることが提示されてい
る。
For example, Japanese Patent Publication No. 59-45439 discloses a biological treatment method for wastewater in which BOD is removed biochemically in a fluidized bed of granular media to which microorganisms are attached.
In this treatment method, the wastewater is first passed in a downward flow for a certain period of time during the microbial cultivation period at the initial stage of operation to facilitate the attachment of the microorganisms to the medium surface, and normalization is achieved by the attachment and cultivation of the microorganisms. After returning to function, it has been proposed to pass water in an upward flow to fluidize the granular media with attached microorganisms.

(発明が解決しようとする問題点) ところが、このような従来の方法においては、前記微生
物を付着させる粒状媒体が砂、ゼオライト、コークス、
活性炭等の材料からなるものであるので、前記微生物を
定着させるための有効な表面積が小さく、従って生物化
学的に廃水中のitのBOD除去、硝化、脱窒素などを
行なうことはできても、例えば、該微生物の増殖等に必
要な酸素移動を阻害する機械油や界面活性剤等を含有す
る用廃水を対象にその浄化作用を実施させることは困難
であり、特に、無機系汚濁物質の分解等に起因するCO
D指示数、すなわち、該廃水におけるCOD除去作用を
行わせることは無理なものとなっている。
(Problems to be Solved by the Invention) However, in such conventional methods, the granular medium to which the microorganisms are attached is made of sand, zeolite, coke,
Since it is made of a material such as activated carbon, the effective surface area for the microorganisms to colonize is small, and therefore, although it is possible to biochemically remove BOD, nitrification, denitrification, etc. of IT in wastewater, For example, it is difficult to purify commercial wastewater that contains machine oil, surfactants, etc. that inhibit the oxygen transfer necessary for the growth of microorganisms, and in particular, it is difficult to perform purification on industrial wastewater that contains mechanical oil and surfactants that inhibit the oxygen transfer necessary for the growth of microorganisms. CO caused by
It is impossible to perform the COD removal action in the wastewater according to the number D indicated.

(問題点を解決するための手段) 本発明は、前述した従来の問題点を解決するとともに、
従来不可能とされていた微生物にょる含油系廃水中のC
ODの除去をも実現させた新しい廃水処理法並びにその
装置を提供することを目的としてなされたものである。
(Means for solving the problems) The present invention solves the above-mentioned conventional problems, and
C in oil-containing wastewater caused by microorganisms, which was previously thought to be impossible.
The purpose of this work is to provide a new wastewater treatment method and equipment that also realizes the removal of OD.

すなわち、その内容を実施例に対応する図面(フローシ
ート)に基づいて説明すると、例えば−次処理された廃
水を収容する廃水処理槽1内に連設した送給管2により
適宜流量を調整しながら、該廃水を送給するとともに、
一定量の廃水を受け入れる大きさを有するカラム5内の
媒体、すなわち、粘土を主成分とし、これに気孔形成用
材料を添加して焼成してなるポーラス状セラミックス粒
状物に、少なくとも前記カラム内に流入、される廃水中
の汚濁物質を処理するための微生物、例えばメタン菌、
桿状菌等の有機物消化菌と、硝化細菌、鉄酸化細菌等の
無機物M積独立栄養細菌を定着させるとともに、このセ
ラミックス粒状物に活性炭などの炭化物を混合させてな
る充てん剤6に前記廃水を流量させて処理する方法とそ
の装置をもってなる手段にある。
That is, to explain the contents based on the drawings (flow sheets) corresponding to the embodiments, for example, the flow rate is adjusted as appropriate using a feed pipe 2 connected to a waste water treatment tank 1 that accommodates treated waste water. While delivering the wastewater,
The medium in the column 5 having a size to receive a certain amount of wastewater, that is, the porous ceramic granules made by adding a pore-forming material to the clay as a main component and firing the medium, at least in the column. Microorganisms for treating pollutants in inflowing wastewater, such as methane bacteria,
Organic matter-digesting bacteria such as rod-shaped bacteria and inorganic matter M-autotrophic bacteria such as nitrifying bacteria and iron-oxidizing bacteria are colonized, and the wastewater is fed at a flow rate to a filler 6 made by mixing the ceramic granules with a carbonized material such as activated carbon. There is a method and a device for processing it.

(作 用) まず、廃水処理槽1内の廃水、例えば、含油系廃水等を
ポンプPで槽1外へ送給管2を通して送給するとともに
、開放状態としたバルブ3を介してフローメータ4内に
注入させ、その送給流量を検知し、前記バルブ3によっ
て流量調整を行ない過剰量を返送管2aを通しコンプレ
ッサーCにより前記処理槽1内に返送させる。
(Function) First, wastewater in the wastewater treatment tank 1, for example, oil-containing wastewater, is sent to the outside of the tank 1 through the feed pipe 2 using the pump P, and the flow meter 4 is fed through the valve 3 which is in an open state. The flow rate is detected, the flow rate is adjusted by the valve 3, and the excess amount is returned to the processing tank 1 by the compressor C through the return pipe 2a.

更に、前記フローメータ4に延設した送給管2を通して
適正量の廃水を外通給管2と連通するカラム5へ移入さ
せる。
Further, an appropriate amount of wastewater is transferred through the feed pipe 2 extending from the flow meter 4 to the column 5 communicating with the external feed pipe 2.

なお、このカラム5内には廃水中の無機系汚濁物質を除
去させるための前記無機物蓄積独立栄養細ぼと、有機物
系汚濁物質を除去させるための有機物消化菌とからなる
微生物を定着させたセラミックス粒状物と、主として廃
水中の懸濁物質等を吸着除去させる作用を行なう炭化物
とが混合され、前記カラム5内に流入される廃水に対し
て浄化作用お行なう。
In addition, in this column 5, there is a ceramic colonized with microorganisms consisting of the above-mentioned inorganic accumulation autotrophic cells for removing inorganic pollutants in wastewater and organic matter digesting bacteria for removing organic pollutants. The granules are mixed with charcoal, which mainly acts to adsorb and remove suspended matter in the wastewater, and purify the wastewater flowing into the column 5.

この浄化作用は前記廃水と接しても容易に変形成は粉末
化しない硬度を有し、しかも前記微生物を定着させるの
に必要な有効表面積が、例えばカラム5内ニ1r+?充
てんした場合、600,000 mと極めて広大な前記
セラミックス粒状物に定着させた微生物の作用と炭化物
との相乗作用により実施されるので、従来にない酸素移
動と栄養物質の移動が持続されるようになり、これから
前記微生物の培養と、その同化作用が長続きすることに
よって、前記界面活性剤等を含む廃水中のCODの除去
作用が行なわれるのである。
This purifying action has a hardness that does not easily deform or turn into powder even when it comes into contact with the wastewater, and the effective surface area necessary for colonizing the microorganisms is, for example, 1r+? When it is filled, it is carried out by the synergistic action of the microorganisms colonized in the ceramic granules, which are extremely vast at 600,000 m, and the carbide, so that the unprecedented movement of oxygen and nutrients is sustained. From now on, by culturing the microorganisms and continuing their assimilation action, the removal action of COD in the wastewater containing the surfactant etc. is carried out.

ちなみに、COD指示数は、大部分廃水中の無機物の分
解等に起因するものであるが、有機物の分解等に起因す
るBOD指示数の中にもCOD指示数が解集合し、存在
することがら、本発明においては、前記広大な表面積を
もつセラミックス粒状物6を微生物培養の培地とすると
ともに、この解集合部分を利用して無機系、有機系の汚
濁物質を浄化する微生物を共存繁殖させ、廃水中の無機
物或は有機物の分解等に基因するCOD等の除去作用を
、前記微生物等により広範囲に行なうものである。
By the way, the COD indication number is mostly caused by the decomposition of inorganic substances in wastewater, but it is also possible that the COD indication number is disaggregated and exists in the BOD indication number caused by the decomposition of organic substances. In the present invention, the ceramic granules 6 having a large surface area are used as a culture medium for microorganisms, and the disaggregated parts are used to co-propagate microorganisms that purify inorganic and organic pollutants. The microorganisms and the like perform a wide-ranging action to remove COD and the like caused by the decomposition of inorganic or organic substances in wastewater.

(実施例) 以下、図面として示した実施例に基づいて本発明に係る
装置を具体的に説明する。
(Example) Hereinafter, an apparatus according to the present invention will be specifically described based on an example shown in the drawings.

図中1は廃水処理槽で、その内部或は槽1外辺にポンプ
Pを設置している。そして、ポンプPには、槽1外に突
設させる長さの送給管2を連結、連通させてなる。該送
給管2は、更に、廃水処理槽1内から送給される廃水W
の流量を調節するフローメータ4の入口側に位置するバ
ルブ3と連通し、該バルブ3を介してフローメータ4に
前記廃水Wを送給する。なお、過剰に送給された廃水は
、返送管2aを通してコンプレッサーCの駆動により廃
水処理槽1内に返送させるようにしている。
In the figure, 1 is a wastewater treatment tank, and a pump P is installed inside the tank or on the outside of the tank 1. The pump P is connected and communicated with a feed pipe 2 having a length that projects outside the tank 1. The feed pipe 2 further includes waste water W fed from inside the waste water treatment tank 1.
It communicates with a valve 3 located on the inlet side of a flow meter 4 that adjusts the flow rate of the waste water W, and supplies the waste water W to the flow meter 4 through the valve 3. Incidentally, the excess wastewater is returned to the wastewater treatment tank 1 by driving the compressor C through the return pipe 2a.

次に、前記フローメータ4の他側から延設した送給管2
は、内部に粘土を主成分とし、これに気孔形成用材料を
添加して焼成してなるポーラス状セラミックス粒状物と
、このセラミックス粒状物に付着された少なくとも流入
される廃水中の汚濁物質を処理できる量の微生物と、こ
のセラミックス粒状物と混合される炭化物とからなる充
てん物6を充てんしたカラム5の上部開口側に連通して
なる。
Next, a feed pipe 2 extending from the other side of the flow meter 4 is
is a porous ceramic granular material whose main component is clay, with the addition of a pore-forming material and fired, and a method for treating pollutants attached to the ceramic granular material, at least in inflowing wastewater. The column 5 is connected to the upper opening side of a column 5 filled with a packing material 6 consisting of as much microorganism as possible and a carbide mixed with the ceramic particles.

すなわち、このカラム5内のセラミックス粒状物は、前
述のように、特殊なポーラス形状からなり、その表面積
は広大なものであるので、該装置運転初期時における該
セラミックス表面上への前記有機物消化菌或は無機物蓄
積独立栄養細菌等の微生物の培養は、好適に、且つ、多
面的に行なえるとともに、該無機系並びに有機系の両菌
頚と共存させた状態で集殖定着させ得るものとなる。
That is, as mentioned above, the ceramic particles in the column 5 have a special porous shape and have a large surface area, so that the organic matter-digesting bacteria may be absorbed onto the ceramic surface at the initial stage of operation of the apparatus. Alternatively, microorganisms such as inorganic-accumulating autotrophic bacteria can be cultured suitably and multifaceted, and can be colonized in coexistence with both the inorganic and organic microorganisms. .

又、この微生物類は、前記セラミックス粒状物と混合さ
れる活性炭等の炭化物表面にも定着し、該微生物の同化
作用等により流入される廃水の浄化を行なうが、前記の
ように該炭化物は、例えば、凝集沈澱等の第1次処理後
の廃水中のSSや残溜油分等の吸着作用を行なわせるこ
とを主体とさせるものであり、この観点から前記カラム
5内の充てん物6は、セラミックス粒状物50〜80重
量%、炭化物20〜50重量%とじてブレンド、或は不
活性ガス中で焼成させながら両者を混合し、該混合物に
前記微生物を定着させれば本発明の目的に適うものとな
る。又、図中7は、前記廃水Wを浄化後、再利用先に送
給するための再生水処理管である。
In addition, these microorganisms also settle on the surface of charcoal such as activated carbon that is mixed with the ceramic granules, and purify the incoming wastewater through the assimilation action of the microorganisms, but as mentioned above, the charcoal For example, the main purpose is to adsorb SS, residual oil, etc. in wastewater after primary treatment such as coagulation and sedimentation, and from this point of view, the filler 6 in the column 5 is made of ceramics. The purpose of the present invention can be achieved by blending 50 to 80% by weight of granules and 20 to 50% by weight of carbides, or by mixing both while firing in an inert gas, and allowing the microorganisms to colonize the mixture. becomes. Moreover, 7 in the figure is a recycled water treatment pipe for sending the waste water W to a reuse destination after purification.

なお、前記した本発明に係る装置は、図示したように、
処理槽1、フローメータ4、カラム5を各々単体として
組立てたものでもよいが、廃水量に対応して複数個連設
し、或はカラム5のみを複数個とするなど、適宜その配
置を変更することも可能である。
Note that the device according to the present invention described above, as shown in the figure,
The treatment tank 1, flow meter 4, and column 5 may each be assembled as a single unit, but depending on the amount of wastewater, the arrangement may be changed as appropriate, such as by arranging a plurality of them in a row or by using only a plurality of columns 5. It is also possible to do so.

次に、前述した本発明に係る装置を用いて、被処理廃水
Wを高度処理した実例を記載する。
Next, an example in which wastewater W to be treated is highly treated using the apparatus according to the present invention described above will be described.

すなわち、自動車工場から排出された被処理廃水W1〜
W4を各々図示しない第1次廃水処理槽に収容後、適量
の有機系或は無機系の凝集剤を添加することにより該廃
水中の無機或は有機系物質を大略沈降させる。
That is, wastewater to be treated W1~ discharged from an automobile factory
After each W4 is placed in a first wastewater treatment tank (not shown), an appropriate amount of an organic or inorganic flocculant is added to substantially precipitate the inorganic or organic substances in the wastewater.

そして、該沈降物は槽外に排出し、乾燥ケーキとして成
形処理するとともに、残溜廃水は2次処理するための廃
水処理槽、例えば、図示したような廃水処理槽1内に各
々貯留させる。
Then, the sediment is discharged outside the tank and formed into a dry cake, and the remaining wastewater is stored in a wastewater treatment tank for secondary treatment, for example, the wastewater treatment tank 1 as shown.

このようにして採量した廃水W1〜W4を対象に、該各
廃水中のCO0% S S、 N −hexaneの除
去操作を行なった。
The wastewaters W1 to W4 thus collected were subjected to an operation for removing CO0% SS and N-hexane from each of the wastewaters.

表 1 (原廃水) (単位ppm) 具体的に説明すると、供試廃水W1〜W4を各々、ポン
プPの駆動により送給管2を介して送給するとともに、
フローメータ4並びにバルブ3にてその流量を調整し、
更に送給管2にて前記光てん物6をその内部に充てんし
てなる筒口径60φmm、高さ1300mmのカラム5
内に各々0.71 /mmの速度で送入させ、充てん物
6に定着させた微生物等により浄化作用を行なわせ、処
理後の廃水をカラム5に連設した再生水処理管7を通し
て河川や他の供給路に排出させるものである。
Table 1 (Raw wastewater) (Unit: ppm) To explain specifically, each of the sample wastewaters W1 to W4 was fed through the feed pipe 2 by driving the pump P, and
Adjust the flow rate with flow meter 4 and valve 3,
Furthermore, a column 5 having a diameter of 60 φ mm and a height of 1300 mm is filled with the optical fiber 6 in the feed pipe 2.
The treated wastewater is fed into the columns at a rate of 0.71 mm/mm, and the microorganisms fixed on the filler 6 perform a purifying action, and the treated wastewater is passed through the reclaimed water treatment pipe 7 connected to the column 5 and sent to rivers and other places. is discharged into the supply channel.

表2として示す処理値は、前記表1でしめしす廃水W1
〜W4を前述の処理工程で処理した後の結果を示すもの
であって、この結果からもわかるンうに、従来の微生物
による処理方法では不可能であった廃水中のCOD 、
 S S % N  hexaneの除去作用が実現さ
れていることが認められている。
The treatment values shown in Table 2 are as shown in Table 1 above.
This shows the results after treating ~W4 with the above-mentioned treatment process, and as can be seen from this result, COD in wastewater, which was impossible with conventional microbial treatment methods,
It has been recognized that the removal action of S S % N hexane has been achieved.

表 2(処理後) (単位ppm) 続いて、他の実施例を記載する。Table 2 (after processing) (Unit: ppm) Next, other examples will be described.

IC基盤工場における金属シリカ棒切断工程から排出さ
れるノニオン界面活性剤、油脂石鹸2種及びPを含有す
る廃水W5を前記同様第1次処理後、筒口径100 φ
mm、高さ1300mmOカラム5にフローメータ4に
て2.01 /mmの流速で該廃水W5を送入させ、前
記工程順に処理し、該処理水を再生水処理管7を通して
逆浸透圧(RO)プラントへ供給し、再利用に供した。
Wastewater W5 containing a nonionic surfactant, two types of oil and fat soaps, and P discharged from the metal silica rod cutting process at an IC substrate factory was treated as described above, and then treated with a cylinder diameter of 100 φ.
The waste water W5 is fed into an O column 5 with a height of 1300 mm and a flow meter 4 at a flow rate of 2.01/mm, treated in the order of steps described above, and the treated water is passed through a reclaimed water treatment pipe 7 to reverse osmosis (RO). It was supplied to the plant for reuse.

表3はこの実施例の結果を示すものである。Table 3 shows the results of this example.

表3 (単位ρpm) なお、前述した本発明に係る充てん物6に定着させた微
生物、例えば、前記無機物蓄積独立栄養細菌又は有機物
硝化菌は、繰返し送入される廃水W等に含有するCOD
源等となる汚濁物質を、その細胞内に取込み蓄積するが
、次第に該菌体の同化作用等に伴って不活性化し、それ
自体が汚泥物となって充てん物6中に混在するようにな
るので、該充てん物6と混合した活性炭等の炭化物に吸
着しているSS等とともに反応系外に排出することにな
る。
Table 3 (unit: ρpm) Note that the microorganisms colonized in the filling material 6 according to the present invention described above, for example, the inorganic matter accumulating autotrophic bacteria or the organic matter nitrifying bacteria, are used to reduce the COD contained in repeatedly fed wastewater W, etc.
The pollutants that serve as sources are taken into the cells and accumulated, but they gradually become inactivated due to the assimilation of the microbial cells, and the pollutants themselves become sludge and are mixed in the filling material 6. Therefore, it is discharged to the outside of the reaction system together with SS and the like adsorbed on the carbide such as activated carbon mixed with the filling material 6.

このような微生物の破過点において、洗浄された前記セ
ラミックス粒状物は、前記有機物硝化菌  ・や無機物
蓄積独立栄養細菌を再度培養、繁殖させる培地として利
用される。
At the breakthrough point of such microorganisms, the washed ceramic granules are used as a medium for culturing and propagating the organic matter nitrifying bacteria and inorganic matter accumulating autotrophic bacteria again.

(発明の効果) 以上のように、本発明に係る微生物による廃水処理方法
およびその装置は、カラム内に、粘土を主成分とし、こ
れに気孔形成用材料を添加して焼成してなるポーラス状
のセラミックス粒状物と炭化物とを混合して微生物繁殖
用の培地とするとともに、該培地に有機物硝化菌と、無
機物蓄積独立栄養細菌とを定着させて、各種廃水を処理
するようにしているから、広大な表面積をもつセラミッ
クス粒状物上の微生物は、その繁殖に必要な酸素の供給
と栄養物質を付加されながら、従来法では不可能とされ
ていた前記廃水中のCOD等の除去作用を長期間行なう
ものとなる。
(Effects of the Invention) As described above, the method and apparatus for treating wastewater using microorganisms according to the present invention provide a column with a porous structure formed by adding clay as a main component, adding a pore-forming material to the column, and firing the clay. Ceramic granules and carbide are mixed to form a medium for microbial propagation, and the medium is colonized with organic matter nitrifying bacteria and inorganic matter accumulating autotrophic bacteria to treat various wastewaters. The microorganisms on the ceramic granules, which have a vast surface area, are supplied with the oxygen and nutrients necessary for their reproduction, and are able to remove COD, etc. from the wastewater for a long period of time, which was considered impossible with conventional methods. It becomes something that you do.

従って、その処理後の再生水は、COD値が10ppm
以下でないと使用不可とされる逆浸透圧(RO)プラン
ト等にも利用できるなど、用途も広くその効果は顕著な
ものがある。
Therefore, the recycled water after the treatment has a COD value of 10 ppm.
It can be used in reverse osmosis (RO) plants, etc., which would otherwise be unusable, and has a wide range of uses, and its effects are remarkable.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は、本発明に係る実施例を示す装置とその系統説明
図である。 l・・・廃水処理槽、  2・・・送給管、3・・・バ
ルブ、     4・・・フローメータ、5・・・カラ
ム、     6・・・充てん物、7・・・再生水処理
管、 C・・・コンプレッサー、P・・・ポンプ。
The drawings are an explanatory diagram of an apparatus and its system showing an embodiment of the present invention. l...Wastewater treatment tank, 2...Feeding pipe, 3...Valve, 4...Flow meter, 5...Column, 6...Filling material, 7...Recycled water treatment pipe, C...Compressor, P...Pump.

Claims (4)

【特許請求の範囲】[Claims] (1)カラム内に充てんされた粘土を主成分とし、これ
に気孔形成用材料を添加して焼成してなるポーラス状の
セラミックス粒状物に、少なくとも該カラム内に流入さ
れる廃水中の汚濁物質を処理できる微生物を定着させる
とともに、このセラミックス粒状物と炭化物とを混合し
た後、該カラム内に廃水を流入させることを特徴とする
微生物による廃水処理方法。
(1) The porous ceramic granules, which are mainly composed of clay and are made by adding pore-forming materials and firing, are filled in a column and contain at least pollutants in the wastewater flowing into the column. 1. A method for treating wastewater using microorganisms, which comprises colonizing microorganisms capable of treating charcoal, mixing the ceramic granules and charcoal, and then flowing wastewater into the column.
(2)前記炭化物が活性炭であることを特徴とする特許
請求の範囲第1項記載の微生物による廃水処理方法。
(2) The method for treating wastewater using microorganisms according to claim 1, wherein the carbonized material is activated carbon.
(3)前記微生物が有機物消化菌と、無機物蓄積独立栄
養細菌との共存体であることを特徴とする特許請求の範
囲第1項記載の微生物による廃水処理方法。
(3) The method for wastewater treatment using microorganisms according to claim 1, wherein the microorganisms are coexisting organisms of organic matter-digesting bacteria and inorganic matter-accumulating autotrophic bacteria.
(4)一定量の廃水を受け入れる大きさを有するカラム
と、前記カラム内部に充てんされた粘土を主成分とし、
これに気孔形成用材料を添加して焼成してなるポーラス
状セラミックス粒状物と、 前記セラミックス粒状物に定着された少なくとも前記カ
ラム内に流入される廃水中の汚濁物質を処理できる微生
物と、 前記セラミックス粒状物と混合される炭化物と、からな
る微生物による廃水処理装置。
(4) A column having a size that accepts a certain amount of wastewater, and a clay filled inside the column as the main components,
porous ceramic granules obtained by adding a pore-forming material to the porous ceramic granules and firing them; microorganisms that are fixed to the ceramic granules and capable of treating pollutants in at least wastewater flowing into the column; and the ceramics. Wastewater treatment equipment using microorganisms consisting of carbonized material mixed with granular material.
JP60150986A 1985-07-09 1985-07-09 Treatment of waste water by microbe and apparatus therefor Granted JPS6211596A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60150986A JPS6211596A (en) 1985-07-09 1985-07-09 Treatment of waste water by microbe and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60150986A JPS6211596A (en) 1985-07-09 1985-07-09 Treatment of waste water by microbe and apparatus therefor

Publications (2)

Publication Number Publication Date
JPS6211596A true JPS6211596A (en) 1987-01-20
JPH0226558B2 JPH0226558B2 (en) 1990-06-11

Family

ID=15508785

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60150986A Granted JPS6211596A (en) 1985-07-09 1985-07-09 Treatment of waste water by microbe and apparatus therefor

Country Status (1)

Country Link
JP (1) JPS6211596A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58131342A (en) * 1982-01-30 1983-08-05 Mitsubishi Motors Corp Engine speed controlling apparatus
JPH01151997A (en) * 1987-12-09 1989-06-14 Ebara Infilco Co Ltd Circulating purification apparatus for water tank
JPH01151998A (en) * 1987-12-08 1989-06-14 Nippon Steel Corp Method for purifying water using ceramics
JPH0290997A (en) * 1988-09-27 1990-03-30 Toppan Shoji Kk Waste water purification process
JPH03232587A (en) * 1990-06-15 1991-10-16 Yondenko Corp Small-sized treating septic tank
JPH03245815A (en) * 1990-02-23 1991-11-01 Kubota Corp Biological deodorizing apparatus using ceramic carrier for immobilizing bacteria and waste water treatment apparatus
JPH0459096A (en) * 1990-06-22 1992-02-25 Suido Kiko Kk Method for immobilizing ammonia oxidative bacterium due to composite carrier

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0469057U (en) * 1990-10-29 1992-06-18

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54146459A (en) * 1978-05-09 1979-11-15 Kiyuushiyuu Kankiyou Kanri Kiy Method of purifying secondary treatment water
JPS5584591A (en) * 1978-12-21 1980-06-25 Kubota Ltd Waste water treatment apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54146459A (en) * 1978-05-09 1979-11-15 Kiyuushiyuu Kankiyou Kanri Kiy Method of purifying secondary treatment water
JPS5584591A (en) * 1978-12-21 1980-06-25 Kubota Ltd Waste water treatment apparatus

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58131342A (en) * 1982-01-30 1983-08-05 Mitsubishi Motors Corp Engine speed controlling apparatus
JPH0232460B2 (en) * 1982-01-30 1990-07-20 Mitsubishi Motors Corp
JPH01151998A (en) * 1987-12-08 1989-06-14 Nippon Steel Corp Method for purifying water using ceramics
JPH01151997A (en) * 1987-12-09 1989-06-14 Ebara Infilco Co Ltd Circulating purification apparatus for water tank
JPH0290997A (en) * 1988-09-27 1990-03-30 Toppan Shoji Kk Waste water purification process
JPH0423597B2 (en) * 1988-09-27 1992-04-22 Totsupan Shoji Kk
JPH03245815A (en) * 1990-02-23 1991-11-01 Kubota Corp Biological deodorizing apparatus using ceramic carrier for immobilizing bacteria and waste water treatment apparatus
JPH03232587A (en) * 1990-06-15 1991-10-16 Yondenko Corp Small-sized treating septic tank
JPH0459096A (en) * 1990-06-22 1992-02-25 Suido Kiko Kk Method for immobilizing ammonia oxidative bacterium due to composite carrier

Also Published As

Publication number Publication date
JPH0226558B2 (en) 1990-06-11

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