JPH0373358B2 - - Google Patents

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Publication number
JPH0373358B2
JPH0373358B2 JP8358384A JP8358384A JPH0373358B2 JP H0373358 B2 JPH0373358 B2 JP H0373358B2 JP 8358384 A JP8358384 A JP 8358384A JP 8358384 A JP8358384 A JP 8358384A JP H0373358 B2 JPH0373358 B2 JP H0373358B2
Authority
JP
Japan
Prior art keywords
wastewater
treatment
layer
wood chips
water
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 - Lifetime
Application number
JP8358384A
Other languages
Japanese (ja)
Other versions
JPS60225694A (en
Inventor
Kiichiro Sarui
Tooru Matsuoka
Hiroshige Nagata
Terubumi Saito
Minoru Takayasu
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP59083583A priority Critical patent/JPS60225694A/en
Publication of JPS60225694A publication Critical patent/JPS60225694A/en
Publication of JPH0373358B2 publication Critical patent/JPH0373358B2/ja
Granted 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】[Detailed description of the invention]

(発明の利用分野) 本発明は、主として家庭用雑排水、産業廃水、
食品加工廃水等の廃水を、木質細片を主成分とす
る処理媒質中で生物学的に処理する廃水の処理方
法、更に詳しくは、かかる処理方法において好適
に用いられる廃水の処理媒質への注加方法に関す
るものである。 (発明の背景) 近年、廃水等の醗酵、分解、消化、過処理及
び脱臭処理等に各種微生物の活性を利用する方法
が各方面で実用化されてきている。 しかし、その反面多量の汚泥が発生し、これの
適切な処理、処分が要求されている。 各種汚泥の主な化学的組成、含有量および物理
化学的特性は次表1〜3の通りである。
(Field of Application of the Invention) The present invention mainly applies to household gray water, industrial wastewater,
A wastewater treatment method in which wastewater such as food processing wastewater is biologically treated in a treatment medium containing wood chips as a main component, and more specifically, notes on the wastewater treatment medium preferably used in such a treatment method. This relates to the addition method. (Background of the Invention) In recent years, methods that utilize the activities of various microorganisms for fermentation, decomposition, digestion, overtreatment, deodorization, etc. of wastewater have been put into practical use in various fields. However, on the other hand, a large amount of sludge is generated, and appropriate treatment and disposal of this is required. The main chemical compositions, contents, and physicochemical properties of various sludges are shown in Tables 1 to 3 below.

【表】【table】

【表】【table】

【表】【table】

【表】 一般にこのような各種汚泥を適切に処分するに
は濃縮や脱水などの適用性の優劣や操作上の諸問
題ならびに最終的な処分までの経費等に多くの難
点が残されている。 そこで本発明者等が生物学的見知から、この様
な廃水について種々研究を重ねたところによると
微生物の培養基質として木質細片が極めて優れて
おり、汚泥の発生が見られないこと、更にこの木
質細片を用いた処理装置は極めて簡単な構造のも
ので長期間にわたつてほとんど保守及更新(交
換)の必要がなく安定に機能できるものであるこ
とを見出している。 汚泥廃水の微生物処理において、処理媒質層と
して当該木質細片が至適環境条件を造り出し層内
に汚泥を発生させることなく極めて効率良く廃水
を処理することの処理メカニズムは、好気性およ
び嫌気性の微生物が共存し、交互に作用して分
解、消化、醗酵等の生化学的な処理が行なわれて
いることによるものと推定され、極端な好気的或
いは嫌気的環境は汚泥の発生をまねくため避けな
ければならない。 0.2〜5mmの細片径をもつ当該木質細片がかか
る至適環境条件を造り出す因子としては以下のよ
うな事が推定される。 (イ) 比表面積200m2程の広い面積をもつている為
適度な保水性と通気性を兼ね備えている。 (ロ) 自然環境下で育成した細孔、表面構造が微生
物共存に最適である。 (ハ) 処理媒質層全体への均一な透水分散を行う
為、層内での偏流(通称水みち)が起らない。 (ニ) 処理媒質層への被処理廃水注加の過程で層内
透下廃水が層表面から適量の空気を導入する
為、層内が嫌気性的雰囲気の中で好気性微生物
が生存・活動できる環境つくり出している。し
たがつて層内の嫌気性的雰囲気が強過ぎると思
われる場合には、下層部方向から強制的に通気
することも良い。 かかる知見に基づいて、本発明者等は、木質細
片を処理媒質の主成分として微生物を好適に繁
殖・活動させるようにした廃水(汚泥)の処理方
法等につき、種々の提案を特許出願して提供して
きている。 この廃水の処理方法は、被処理廃水1容量部
を、粒度一定の木質細片を主成分とする処理媒質
層1〜10容量部に対して注加し、周囲温度で処理
することを基本的内容とするものであり、前記処
理のための装置は、代表的には、処理媒質を槽に
充填して、これに廃水を注加する形式のものとし
て構成される。なお処理媒質には通気を行なうこ
とによつて処理効果が向上される。 なお、このような微生物工学的な処理に用いら
れる前記木質細片は、その粒度、粒度分布および
木質成分組成を所望の範囲内のものとして使用さ
れるが、特に粒度は、好ましくは細片径0.5〜3
mmの範囲とすべきである。細片径が0.2mm以下で
は材等として用いる際に目詰まりを生じ易く、
また5mm以上では微生物培養質としての単位面積
当りの表面積が小さくなつて充分な処理能力を得
ることが出来ないからである。 また粒度分布0.2〜1mm:30%、1〜2mm:30
%、2〜3mm:40%とし、成分組成としてはセル
ロース60〜65%、リグニン15〜25%、ペントザン
15〜25%、水分11〜16%のものが好ましく用いら
れる。 またこの木質細片を主成分とする処理媒質は該
木質細片単独である場合の他、その一部をゼオラ
イト等の多孔性無機物に代用置換したものとして
もよいが、この場合は木質細片に対する割合を40
%以下、好ましくは25%以下とすることがよい。 ところで、前記したような処理を行なうにあた
つて、一般的な処理媒質への被処理水充填の方法
に従い、前記処理槽上部より散水もしくは通常の
注水を行なうものとすると、処理媒質である木質
細片等(以下一部を無機物とした場合を含めて木
質細片と略称する)の層上部表面付近に目詰まり
が起こり廃水の浸透速度を著しく減少させるとい
う問題があつた。 このような表面目詰りの原因は、廃水中の浮遊
物および廃水水質から順応発生する好気性の活性
汚泥等が発生するものと推定される。 又、自由表面が水没状態におかれているような
場合には、嫌気性の汚泥が発生し、これら汚泥が
自由表面上に付着、堆積し目詰りになるものと推
定される。 したがつて、前記した一般的な注加方法による
場合には、処理媒質層の表面目詰りを解消するた
めに、表面のすきとり、あるいは層のかきまぜ等
の操作が併せて必要であつた。 (発明の目的) 本発明はかかる現況に鑑みなされたもので、木
質細片の充填層に極めて効率よく、かつ微生物の
繁殖環境に適した状態を維持しながら廃水を注入
する方法を提供することを目的とする。 (発明の概要) 而して、かかる目的を達成するための本発明の
要旨とするところは、木質細片又はこれに無機多
孔粒体を混合した処理媒質層に、被処理廃水を注
加して生物学的処理を行なわせる廃水の処理方法
において、前記廃水の注加は、注加廃水が直接大
気に接することなく処理媒質内部に放出されるこ
とで行なうことを特徴とする廃水の処理方法にあ
る。 このように、廃水を直接的に大気に接触させな
いで間接的に空気を吸引し接触させる手法を用い
れば、汚泥の発生をまねくことなく、又浮遊物と
して注加された汚泥を消化してしまい、注加付近
での目詰りは起さない。このことは、処理媒質層
の上部自由表面に単に廃水を墳霧するような場合
には目詰りを生じ易いのに対し、注加廃水が直接
大気と接触しないように、筒径の2〜4倍相当の
直径範囲の表面上を蓋をかぶせるように覆をほど
こし、その覆の周囲外側から空気を層内に吸引出
来る様にしておくと、目詰りを生じにくくなる実
験結果からも裏付けられる。 ただし、実際的には、廃水の注水管を処理媒質
層の内部に差込みすることで、前記条件を満足さ
せることが通常であり、この場合において処理媒
質層内部に廃水を放出させる位置は、注水管を用
いて層の上部表面から10〜50cm以深とすることが
よく、また層の下部からは80cm程度以上の高さの
位置とされることが望ましい。これは、廃水注加
時の空気の巻き込みを考慮して、嫌気条件、好気
条件を効果的に現出させることが必要とされるこ
とからである。 前記方法に用いられる注水管の形状は、例えば
処理媒質内に差込まれる下端が開放されていて、
かつ処理媒質内の周壁部において径方向の貫通孔
が形成されている丸筒管等を使用することがで
き、貫通孔の大きさは10〜16mm程度孔間隔は40〜
60mm程度であることが好ましい。 本発明方法における注水管の配置態様は、代表
的には処理媒質層の上部表面の中央位置から垂直
下方に内部に差込まれることで行なわれるが、処
理媒質層の容量、拡がりにより複数本の注水管を
適当な間隔をもつて差込み配置するようにしても
よく、要は程水管の貫通孔から周囲に分散放出さ
れた廃水が、落下傘状のような状態で拡がりなが
ら下方に浸透するものとすればよい。 なお、本発明方法の処理対象とされる廃水と
は、主として家庭用雑排水、産業廃水、食品加工
廃水等をいうが、不溶性の無機物特に砂が多く含
まれるような場合にはこれを沈澱法等による前処
理にて除去したものとすることがよく、また好ま
しい実用的具体例としては廃水中の汚泥濃度が必
要により希釈されて1000ppm程度以下であること
が望ましい。 (発明の実施例とその効果) 以下本発明を図示する装置を用いて行なつた一
実施例に基づいて説明する。 第1図は本発明に係る廃水の注入方法の一例を
示すもので図において1は廃水導入用の注水管、
2は木質細片、3はこの木質細片を充填した処理
槽をを示す。 このような装置において、被処理廃水を注水管
1の中を通して処理槽内に入れると、廃水と木質
細片2が接触し、細片の表面に付着もしくは多孔
質部に浸透する。 また処理水が充填槽下部に移動するときに、処
理槽3の上部の大気と接触している木質細片を通
して空気が導入され、あたかも処理槽3は呼吸し
ているかのような状態を呈する。 したがつて微生物繁殖環境に適した空気の補給
作用が行なわれることになる。また注水管の埋設
部を多孔としたことにより、廃水注加の急激な流
量変動に対しても木質細片3と水の接触範囲を拡
大することで過剰水量に対しても充分対応できる
利点もある。 なお、4は廃水の導入口、5は槽3の底部に設
けられた排水管である。また第2図は注水管1の
一部特に多孔部分の形状を示すためのものであ
り、本例の注水管1は、廃水導入口4から連らな
る小径管部分から、ソケツト6を介して若干大径
を多孔管7部分に接続されるようになつており、
これらの管は合成樹脂製のものを用いることが耐
久性の面から望ましい。 なお、注水管は他の形式のものであつてもよ
く、第3図はこのような他の例として処理媒質表
面の管周囲を蓋覆8で覆つたものを示している。 本発明者等は前記第1図に示す装置を用い以下
の条件で実験を行なつた。 (実験) 使用装置 第1図に示す構造の装置において、 処理媒質 木質細片 粒径範囲 0.2〜5mm 水平断面積 1.0m2 層 高 3.0m 注水管 管 径 10cm 差込み深さ 150cm 多孔の上端位置 30cm 実験方法 BOD150、PH7の標準的な家庭用雑排水を槽上
部から筒管を介して20/分の流量で1分間注加
し、10分間休止の間欠注加操作と反復し、常温で
処理した。 以上の操作により、廃水は全て極めて迅速に消
化され、また24時間経過後において、処理槽内の
木質細片層中にはほとんど処理残渣が認められな
かつた。 処理槽からの排出液のPHは6.0、BOD値は8で
あり、処理前の廃水に比べて、BODの減少は顕
著であつた。 また、下記表4は、対象汚泥および処理条件を
変えて行なつた試験例についての結果を示してお
り、いずれもBODの充分な低減が実現された。
[Table] In general, there are many difficulties in properly disposing of these various sludges, including the applicability of thickening and dewatering, various operational problems, and the cost of final disposal. Based on biological knowledge, the present inventors have conducted various studies on such wastewater, and have found that wood chips are extremely excellent as a culture substrate for microorganisms, and no sludge is observed. It has been discovered that this processing device using wood chips has an extremely simple structure and can function stably over a long period of time with almost no need for maintenance or renewal (replacement). In the microbial treatment of sludge wastewater, the treatment mechanism is that the wood chips create optimal environmental conditions as a treatment medium layer and treat wastewater extremely efficiently without generating sludge in the layer. This is presumed to be due to the coexistence of microorganisms and their mutual interaction to carry out biochemical processes such as decomposition, digestion, and fermentation. Must be avoided. The following factors are presumed to create such optimal environmental conditions for the wood chips having a diameter of 0.2 to 5 mm. (a) It has a large specific surface area of about 200m2 , so it has appropriate water retention and breathability. (b) The pores and surface structure grown in a natural environment are optimal for the coexistence of microorganisms. (c) Uniform water permeation and dispersion throughout the treatment medium layer prevents uneven flow within the layer (commonly known as water path). (d) During the process of adding wastewater to the treatment medium layer, the wastewater that permeates through the layer introduces an appropriate amount of air from the surface of the layer, allowing aerobic microorganisms to survive and operate in an anaerobic atmosphere within the layer. We are creating an enabling environment. Therefore, if the anaerobic atmosphere in the layer is thought to be too strong, it is also a good idea to forcibly ventilate from the lower layer direction. Based on this knowledge, the present inventors have filed patent applications for various proposals regarding wastewater (sludge) treatment methods that use wood chips as the main component of the treatment medium to allow microorganisms to propagate and become active. It has been provided. This wastewater treatment method basically involves pouring 1 volume part of the wastewater to be treated into 1 to 10 volume parts of a treatment medium layer whose main component is wood chips with a constant particle size, and treating it at ambient temperature. The apparatus for the treatment is typically constructed in such a way that a treatment medium is filled in a tank and waste water is poured into the tank. Note that the treatment effect can be improved by aerating the treatment medium. The wood chips used in such microbial engineering treatments are used with their particle size, particle size distribution, and wood component composition falling within desired ranges. 0.5~3
Should be in the mm range. If the particle diameter is less than 0.2 mm, it will easily become clogged when used as a material, etc.
Moreover, if it is more than 5 mm, the surface area per unit area as microbial culture material becomes small and sufficient processing capacity cannot be obtained. Also, particle size distribution: 0.2-1mm: 30%, 1-2mm: 30%
%, 2-3mm: 40%, and the component composition is cellulose 60-65%, lignin 15-25%, pentozan.
Those containing 15 to 25% and moisture content of 11 to 16% are preferably used. In addition, the treatment medium mainly composed of wood chips may be the wood chips alone, or may be partially replaced with a porous inorganic material such as zeolite. percentage of 40
% or less, preferably 25% or less. By the way, when performing the above-mentioned treatment, if water is sprinkled or normally poured from the upper part of the treatment tank according to the general method of filling the treatment medium with water to be treated, the treatment medium, which is wood, There was a problem in that clogging occurred near the upper surface of the layer of fine particles (hereinafter referred to as wood particles, including the case where some of them were made of inorganic material), which significantly reduced the permeation rate of wastewater. The cause of such surface clogging is presumed to be the generation of suspended matter in the wastewater and aerobic activated sludge that is generated due to the quality of the wastewater. In addition, when the free surface is submerged in water, anaerobic sludge is generated, and it is assumed that this sludge adheres and accumulates on the free surface, resulting in clogging. Therefore, when using the above-mentioned general pouring method, operations such as clearing the surface or stirring the layer are also required in order to eliminate clogging of the surface of the processing medium layer. (Objective of the Invention) The present invention was made in view of the current situation, and an object of the present invention is to provide a method for injecting wastewater into a packed bed of wood chips extremely efficiently and while maintaining conditions suitable for the breeding environment of microorganisms. With the goal. (Summary of the Invention) The gist of the present invention to achieve the above object is to pour wastewater to be treated into a treatment medium layer made of wood chips or inorganic porous particles mixed therein. A method for treating wastewater in which a biological treatment is carried out using a method for treating wastewater, characterized in that the addition of the wastewater is carried out by discharging the added wastewater into a treatment medium without directly contacting the atmosphere. It is in. In this way, if we use a method in which the wastewater is not brought into direct contact with the atmosphere, but is instead brought into contact with the air by suctioning the air indirectly, sludge will not be generated, and the sludge added as suspended matter will be digested. , clogging does not occur near the injection area. This means that clogging is likely to occur if wastewater is simply poured onto the upper free surface of the treatment medium layer, but it is necessary to prevent the poured wastewater from coming into direct contact with the atmosphere. It is also supported by experimental results that clogging becomes less likely to occur if a cover is placed over the surface of the area with a diameter equivalent to twice that, and if air is sucked into the layer from the outside around the cover. However, in practice, the above conditions are usually satisfied by inserting the wastewater injection pipe into the inside of the treatment medium layer. It is preferable to use a water pipe at a depth of 10 to 50 cm or more from the upper surface of the layer, and preferably at a height of about 80 cm or more from the bottom of the layer. This is because it is necessary to effectively create anaerobic conditions and aerobic conditions by taking into consideration the entrainment of air when adding wastewater. The shape of the water injection pipe used in the method is, for example, such that the lower end inserted into the processing medium is open, and
In addition, it is possible to use a round cylindrical tube or the like in which a radial through hole is formed in the peripheral wall inside the processing medium, and the size of the through hole is 10 to 16 mm, and the hole interval is 40 to 40 mm.
It is preferably about 60 mm. The water injection pipe in the method of the present invention is typically inserted vertically downward from the center of the upper surface of the treatment medium layer, but depending on the capacity and spread of the treatment medium layer, multiple The water injection pipes may be inserted and arranged at appropriate intervals, and the point is that the wastewater discharged from the through holes of the water pipes into the surrounding area spreads out in a parachute-like manner and permeates downward. do it. The wastewater to be treated by the method of the present invention mainly refers to household gray water, industrial wastewater, food processing wastewater, etc., but if it contains a large amount of insoluble inorganic substances, especially sand, it may be treated by the precipitation method. It is preferable that the sludge be removed by pre-treatment such as the like, and as a preferred practical example, it is desirable that the sludge concentration in the wastewater is diluted as necessary to be about 1000 ppm or less. (Embodiment of the invention and its effects) The present invention will be described below based on an embodiment carried out using the illustrated apparatus. FIG. 1 shows an example of the wastewater injection method according to the present invention. In the figure, 1 is a water injection pipe for introducing wastewater;
2 indicates wood chips, and 3 indicates a treatment tank filled with the wood chips. In such an apparatus, when wastewater to be treated is introduced into the treatment tank through the water injection pipe 1, the wastewater comes into contact with the wood chips 2, and either adheres to the surface of the chips or permeates into the porous parts. Furthermore, when the treated water moves to the lower part of the filling tank, air is introduced through the wooden strips in contact with the atmosphere at the upper part of the treatment tank 3, making the treatment tank 3 appear as if it were breathing. Therefore, an air replenishment action suitable for a microbial breeding environment is performed. In addition, by making the buried part of the water injection pipe porous, it has the advantage of being able to cope with sudden changes in the flow rate of wastewater injection by expanding the contact area between the wood chips 3 and the water, which can sufficiently cope with excessive water flow. be. Note that 4 is a wastewater inlet, and 5 is a drain pipe provided at the bottom of the tank 3. Furthermore, FIG. 2 is for showing the shape of a part of the water injection pipe 1, particularly the porous part. The slightly larger diameter is connected to the 7th part of the porous pipe,
From the viewpoint of durability, it is desirable to use synthetic resin tubes for these tubes. Note that the water injection pipe may be of other types, and FIG. 3 shows another example of this type in which the periphery of the pipe on the surface of the processing medium is covered with a cover 8. The present inventors conducted experiments under the following conditions using the apparatus shown in FIG. 1. (Experiment) Apparatus used In the apparatus with the structure shown in Fig. 1, processing medium Wood particle size range 0.2 to 5 mm Horizontal cross-sectional area 1.0 m 2 layers Height 3.0 m Water injection pipe Diameter 10 cm Insertion depth 150 cm Top position of porous hole 30 cm Experimental method: Standard domestic gray water with a BOD of 150 and a pH of 7 was poured from the top of the tank through a cylinder pipe at a flow rate of 20/min for 1 minute, followed by intermittent pouring with 10-minute pauses, and treated at room temperature. . Through the above operations, all of the wastewater was digested extremely quickly, and after 24 hours, almost no treatment residue was observed in the wood debris layer in the treatment tank. The pH of the effluent from the treatment tank was 6.0, and the BOD value was 8, and the BOD value was significantly reduced compared to the wastewater before treatment. Further, Table 4 below shows the results of test examples conducted with different target sludges and treatment conditions, and in all cases, a sufficient reduction in BOD was achieved.

【表】 前記実施例に加えて家庭用雑排水、産業廃水、
食品加工排水等についてこれらの実施例と同様な
方法で処理を施した場合にも処理後の廃水は全て
廃水処理の基準を満足するものであつた。 BOD300、PH7.5の食品加工排水10m2を粒径0.2
〜5mmの木質細片を処理槽3に充填してその上部
から300/時の流量で12時間注加した。その後
注加を中断し、引き続き処理槽下部から60/時
の流量で12時間送気する操作を反復し常温で微生
物処理を行なつた。 廃水は全て極めて迅速に消化され、24時間経過
後の処理槽内の幕質細片層中にはほとんど処理残
渣が認められなかつた。処理層からの排出液のPH
は6.3であり、BOD値は10であつた。 (発明の効果) 本発明方法によれば、木質細片を主成分とする
処理媒質内への好適な廃水注加が実現され、これ
に伴なつて処理媒質内での好ましい微生物繁殖環
境が与えられるために良好な廃水処理が行なわ
れ、特に廃水の注加と適宜の通気以外には他の操
作が不要となつて、この種の廃水処理の実用化の
上での利益は極めて大なるものでがある。
[Table] In addition to the above examples, household gray water, industrial wastewater,
Even when food processing wastewater and the like were treated in the same manner as in these Examples, all of the treated wastewater satisfied the standards for wastewater treatment. BOD300, PH7.5 food processing wastewater 10m2 particle size 0.2
~5 mm of wood chips were filled into the treatment tank 3 and poured into the tank from the top at a flow rate of 300/hour for 12 hours. Thereafter, the injection was stopped, and the operation of blowing air from the bottom of the treatment tank at a flow rate of 60/hour for 12 hours was repeated to perform microbial treatment at room temperature. All of the wastewater was digested extremely quickly, and almost no treatment residue was observed in the curtain layer in the treatment tank after 24 hours. PH of the liquid discharged from the treatment layer
was 6.3, and the BOD value was 10. (Effects of the Invention) According to the method of the present invention, it is possible to suitably inject wastewater into a treatment medium containing wood chips as a main component, thereby providing a favorable microbial breeding environment within the treatment medium. The advantages of this type of wastewater treatment in practical use are extremely large, especially since no other operations are required other than the addition of wastewater and appropriate aeration. There is.

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

図面第1図は本発明方法に使用する処理媒質充
填槽を示す斜視図、第2図は廃水導入用の注水管
を示す図、第3図は注入管の型体例を示す図であ
る。
FIG. 1 is a perspective view showing a processing medium filling tank used in the method of the present invention, FIG. 2 is a view showing a water injection pipe for introducing waste water, and FIG. 3 is a view showing an example of the type of the injection pipe.

Claims (1)

【特許請求の範囲】 1 木質細片又はこれに無機多孔粒体を混合した
処理媒質層に、被処理廃水を注加して生物学的処
理を行なわせる廃水の処理方法において、前記廃
水の注加は、注加廃水が直接大気に接することな
く処理媒質内部に放出されることで行なうことを
特徴とする廃水の処理方法。 2 廃水の注加を、処理媒質内部に差込んだ注水
管を介し上部表面より10〜50cm以深で行なうこと
を特徴とする特許請求の範囲第1項に記載した廃
水の処理方法。
[Scope of Claims] 1. A wastewater treatment method in which biological treatment is performed by pouring wastewater to be treated into a treatment medium layer in which wood chips or inorganic porous particles are mixed therein. A wastewater treatment method characterized in that the added wastewater is discharged into a treatment medium without coming into direct contact with the atmosphere. 2. The method for treating wastewater according to claim 1, characterized in that the wastewater is injected at a depth of 10 to 50 cm or more from the upper surface through a water injection pipe inserted into the treatment medium.
JP59083583A 1984-04-25 1984-04-25 Treatment of waste water Granted JPS60225694A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59083583A JPS60225694A (en) 1984-04-25 1984-04-25 Treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59083583A JPS60225694A (en) 1984-04-25 1984-04-25 Treatment of waste water

Publications (2)

Publication Number Publication Date
JPS60225694A JPS60225694A (en) 1985-11-09
JPH0373358B2 true JPH0373358B2 (en) 1991-11-21

Family

ID=13806511

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59083583A Granted JPS60225694A (en) 1984-04-25 1984-04-25 Treatment of waste water

Country Status (1)

Country Link
JP (1) JPS60225694A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05269491A (en) * 1992-03-27 1993-10-19 Yasuyuki Yamato Treatment of waste water
JP2663809B2 (en) * 1992-11-09 1997-10-15 株式会社コスモクリーン Wastewater treatment equipment
JP4609582B2 (en) * 2009-01-29 2011-01-12 株式会社大林組 Groundwater purification system

Also Published As

Publication number Publication date
JPS60225694A (en) 1985-11-09

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