JPS6051595A - Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus - Google Patents

Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus

Info

Publication number
JPS6051595A
JPS6051595A JP16115083A JP16115083A JPS6051595A JP S6051595 A JPS6051595 A JP S6051595A JP 16115083 A JP16115083 A JP 16115083A JP 16115083 A JP16115083 A JP 16115083A JP S6051595 A JPS6051595 A JP S6051595A
Authority
JP
Japan
Prior art keywords
tank
sewage
sludge
soil
layer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16115083A
Other languages
Japanese (ja)
Inventor
Tadashi Niimi
新見 正
Masaaki Niimi
新見 正彰
Masanori Niimi
新見 正則
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 JP16115083A priority Critical patent/JPS6051595A/en
Publication of JPS6051595A publication Critical patent/JPS6051595A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16NLUBRICATING
    • F16N21/00Conduits; Junctions; Fittings for lubrication apertures

Abstract

PURPOSE:To perfectly treat excessive sludge, by a relatively simple and small sewage treating apparatus wherein excessive sludge adhered to the pebble layer on a perforated plate is released by forcibly feeding air from an air diffusion pipe provided to the bottom part of a sewage treating tank and decomposed in an aqueous system filter material layer provided the upper part of the tank wall. CONSTITUTION:Sewage is supplied into a sewage treating tank 1 so as to bring the variable surface of sewage to the highest level with respect to excessive sludge adhered to pebbles 3 and, at the same time, air is sent to an air diffusion pipe 6 in an amount of several times as compared with a usual amount to generate a water stream in the tank 1 and the excessive sludge adhered to the pebbles 3 is forcibly released. As a result, a liquid mixture of released sludge and sewage filling the tank 1 is sent into an aqueous system filter material 9 under pressure by a pump P2 through a conduit T and a ceramic pipe 9 provided to the upper part of the tank 1. In this case, moisture is recirculated into the tank 1 from the recessed part of a mountain shaped net 4 and sludge holding a proper amount of moisture remaining in the filter material 9 is subjected to biological decomposition (soil animals, soil microorganisms and plant roots).

Description

【発明の詳細な説明】 本発明は、汚水処理装置から発生する余剰汚泥の分解処
理方法と装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for decomposing excess sludge generated from a sewage treatment apparatus.

従来、汚水の生物処理装置から発生する余剰汚泥は、固
液分離、脱水、乾燥、焼却されるか汚水処理装置の系外
に搬出されて処理又は処分される。
Conventionally, surplus sludge generated from biological wastewater treatment equipment is subjected to solid-liquid separation, dewatering, drying, and incineration, or is carried out of the system of the wastewater treatment equipment for treatment or disposal.

汚水処理装置が小規模になるほど汚泥の処理場内での処
理、処分は困難であるので系外に運搬されるのであるが
、生物処理では水分が多い為に非常に運搬量が多くなり
、汚水処理よりも′、汚泥処理の方が維持管理が困難と
なる場合があった。このための対策として、汚水処理装
置自体で余剰汚泥の発生量を減量し、自己分解させる」
二法が本願発明者により開発されているが(特公昭55
−26929゜同5G−23672,同57−4691
9)、これらの工法は、余剰汚泥を処理するための装置
を別途に必要とし、敷地面積、建設費が増大し、また汚
水供給量が少ない処理装置においては礫に汚泥が付着し
て残るという欠点があった。
The smaller the sewage treatment equipment, the more difficult it is to process and dispose of sludge within the treatment plant, so the sludge is transported outside the system.However, in biological treatment, the amount of sludge transported is extremely large due to the high water content. In some cases, sludge treatment was more difficult to maintain and manage. As a countermeasure for this, the amount of surplus sludge generated by the sewage treatment equipment itself is reduced and self-decomposed."
Two methods have been developed by the inventor of the present application (Japanese Patent Publication No. 55
-26929゜5G-23672, 57-4691
9) These methods require separate equipment to treat excess sludge, increasing the site area and construction costs, and in treatment equipment with a small amount of sewage supply, sludge remains attached to the gravel. There were drawbacks.

本発明は、上記欠点を解消するためになされたもので、
その目的とするところは、比較的簡易なかつ小規模な汚
水処理装置で、汚水処理の維持管理作業と組合せるのみ
で余剰汚泥を完全に処理したり、液肥として利用する方
法および装置を提供することにある。
The present invention has been made to solve the above-mentioned drawbacks.
The purpose is to provide a method and device that can completely treat surplus sludge or use it as liquid fertilizer by simply combining it with sewage treatment maintenance and management work using a relatively simple and small-scale sewage treatment device. It is in.

すなわち本発明は、汚水処理槽に汚水を導入腰該処理槽
内の下部に配設した多孔板上に礫JF’lを設け、該礫
層な被覆する通気性土壌との間にアミを介在させて構成
した水位変動層に汚水面を」二下動せしめ、上記通気性
土壌より汚水の一部を外部」二環中に浸潤排出せしめる
汚水処理方法において、槽の底部に散気管を設け、礫に
イ」着した余剰汚泥を散気管からの強制送気によって剥
離させ、その剥離汚泥を槽壁上部に設けた木質系濾材層
内で分解することを特徴とする土壌被覆型汚水処理装置
と組合せた余剰汚泥の分解処理力法である。
That is, the present invention introduces sewage into a sewage treatment tank, provides gravel on a perforated plate placed at the bottom of the treatment tank, and interposes sand between the gravel layer and the covering permeable soil. In a sewage treatment method in which the sewage surface is moved downward in a water level variable layer constructed by a water level change layer, and a part of the sewage is infiltrated and discharged from the permeable soil to the outside into the two rings, an aeration pipe is provided at the bottom of the tank, A soil-covered sewage treatment device characterized in that excess sludge adhering to gravel is separated by forced air from an aeration pipe, and the separated sludge is decomposed in a wood-based filter layer provided on the upper part of the tank wall. This is a combined method for decomposing and treating excess sludge.

また、凹型汚水処理槽内の下部に多孔板を配設して、処
理槽底面との開に汚水流下槽を形成し、上記多孔板上に
礫層を設け、該礫層の上部にアミを介して通気性土壌を
被覆して構成した汚水処理装置において、槽の底部に散
気管を設け、槽壁上部に透水性を有する管体を延設し、
該管体の周囲に通気性土壌と連続して木質系濾材を設置
し、前記散気管に強制送気を行なうことによって礫に付
着した余剰汚泥を剥離させ、この余剰汚泥と汚水の混合
水を管体内に供給するように構成したことを特徴とする
土壌被覆型汚水処理装置と組合せた余剰汚泥の分解装置
である。
In addition, a perforated plate is placed at the bottom of the concave sewage treatment tank to form a sewage flow tank at the bottom of the treatment tank, a gravel layer is provided on the perforated plate, and a layer of sand is placed on the top of the gravel layer. In a sewage treatment device constructed by covering permeable soil through a tank, an aeration pipe is provided at the bottom of the tank, and a permeable pipe body is installed at the top of the tank wall,
A wood-based filter medium is installed around the pipe body in a continuous manner with the permeable soil, and excess sludge adhering to the gravel is peeled off by forcing air into the aeration pipe, and the mixed water of this excess sludge and sewage is This is a surplus sludge decomposition device combined with a soil-covered sewage treatment device, characterized in that the surplus sludge is supplied into a pipe.

生物処理装置で発生する余剰汚泥には通常2種類がある
が、第1次処理装置(最初沈澱槽)での余剰汚泥はトイ
レットペーパーや砂を含み水分量も若干低く97%前後
であり、第2次処理装置での余剰汚泥は活性汚泥法と接
触バッキ法では若干黒磯化率が異なるがそれでも水分量
は99%1)u後である。この2種類の余剰汚泥は装置
の大小によって異なるが維持管理作業は前者は年数間、
後者は年4回から48回程度に定められている。本発明
は余剰汚泥の処理に特別な労力や技術を必要とせず上述
の定められた維持管理作業毎に単に手動あるいは自動で
汚水ポンプか汚泥ポンプを動かすだけで余剰汚泥の処理
又は液肥として利用することができる。
There are usually two types of surplus sludge generated in biological treatment equipment, but the surplus sludge in the primary treatment equipment (initial settling tank) contains toilet paper and sand and has a slightly lower moisture content, around 97%. Although the surplus sludge in the secondary treatment equipment has a slightly different black rock formation rate between the activated sludge method and the contact bacterium method, the moisture content is still 99%. These two types of surplus sludge differ depending on the size of the equipment, but the former requires maintenance work for several years.
The latter is scheduled to occur between 4 and 48 times a year. The present invention does not require special labor or technology to process surplus sludge, and can be used as liquid fertilizer by simply operating the sewage pump or sludge pump manually or automatically for each of the above-mentioned maintenance operations. be able to.

次に本発明の実施例について図面を参照しながら説明す
る。第1図は、土壌被覆型接触循環バッキ槽の直上の通
気性土壌内に余剰汚泥分解装置を組合せた装置の平面図
、12図はこの装置の一部断面図である。
Next, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a plan view of a device in which an excess sludge decomposition device is combined in permeable soil directly above a soil-covered contact circulation bagging tank, and FIG. 12 is a partial sectional view of this device.

第1図において汚水は汚水導入管へから汚水マスBを介
して汚水処理槽1に供給される。2は汚水が土壌に通し
るための孔を有する多孔板又はロスドル、3は礫1合成
樹脂、空缶等の接触波相、4は山形状アミである。汚水
面5は、汚水供給電を変化させ水位変動させるようにす
る。6は処理槽1の底部に設けた散気管であり空気ボン
ブト1が接続されている。7は被覆土壌で通常槽の内外
が30〜50cm連続した構造を与えである。
In FIG. 1, sewage is supplied to a sewage treatment tank 1 from a sewage inlet pipe via a sewage mass B. In FIG. 2 is a perforated plate or rosdol having holes for sewage to pass through the soil; 3 is gravel 1; contact wave phase such as synthetic resin or an empty can; 4 is a mountain-shaped mesh. The water level of the wastewater level 5 is varied by changing the electricity supplied to the wastewater. Reference numeral 6 denotes an aeration pipe provided at the bottom of the processing tank 1, to which the air bomb 1 is connected. 7 is covered soil, which usually has a continuous structure of 30 to 50 cm inside and outside the tank.

以上は従来の汚水処理装置の構造であるか、本発明は通
気性土壌層7を50〜80cmとなるよう設計し、処理
槽の側壁上部の両側に間隙をあけて陶管8を設け、その
周囲に木質系濾材9を適当量充填し、更にこの木質系波
相9の周囲をアミ4′で覆い、該濾材9中に周囲の土壌
が混入しないようにする。散気管6は、上方に強制的に
空気を供給できるものを用いる。木質系波相9は、チッ
プ。
The above is the structure of a conventional sewage treatment device, but the present invention is designed so that the permeable soil layer 7 is 50 to 80 cm thick, and ceramic tubes 8 are provided with gaps on both sides of the upper side wall of the treatment tank. An appropriate amount of wood filter material 9 is filled around the filter material 9, and the surrounding area of the wood material corrugated layer 9 is covered with net 4' to prevent surrounding soil from being mixed into the filter material 9. The diffuser pipe 6 is one that can forcefully supply air upward. Woody wave phase 9 is a chip.

木質廃材の破砕物、オガクズ、枝、モミガラ、泥炭。Crushed wood waste, sawdust, branches, rice husk, peat.

それら等の混合物で汚泥のC/N比が低い為に土壌中の
生物活性を維持するようC/N比を高める目的も併せ持
つ。同様の目的達成のため、通気土壌7中にムギワラ、
イナワラ、ホティアオイ、モミ〃う破砕品を混入してい
る。土壌中のC/N比の目安は常時10〜15の範囲と
なるよう、炭素源が不足する場合は数年に1同地表面か
ら補給する。
Since the C/N ratio of sludge is low with a mixture of these, it also has the purpose of increasing the C/N ratio to maintain biological activity in the soil. To achieve the same purpose, wheat straw was added to the aerated soil 7.
Contains crushed products such as rice straw, water hyacinth, and fir. The standard C/N ratio in the soil is always in the range of 10 to 15, and if there is a shortage of carbon sources, replenish from the ground surface once every few years.

次に本発明の作用について説明する。処理槽内に汚水を
供給することにより装置内で発生する余剰汚泥が礫3に
イ」着する。汚水処理槽内で汚水面の水位変動を行なう
と、礫層内は湿気があるので乾燥、又カム化することが
なく、従って汚泥は礫に付着残存するようなことはない
。しかし小規模な処理装置においては、汚水供給量か多
くない場合があり常に礫層内に湿気を保つことがでδず
、礫に汚泥が付着し乾燥する場合がある。そこで汚水変
動面の最高位になるように処理4“jlIに汚水を供給
し、散気管6に通常の数倍の送気を行なうことによって
処理槽内に水流を発生さぜ礫3に(=1着している余剰
汚泥を強制的に剥離させる。その結果剥離汚泥と汚水と
の混合液が処理槽内を)1シ」たす。
Next, the operation of the present invention will be explained. Excess sludge generated within the device by supplying sewage into the treatment tank lands on the gravel 3. When the water level of the sewage surface is changed in the sewage treatment tank, the gravel layer is moist, so it does not dry out or form a scum, so sludge does not remain attached to the gravel. However, in small-scale treatment equipment, the amount of sewage supplied may not be large enough to keep moisture in the gravel layer at all times, and sludge may adhere to the gravel and dry out. Therefore, sewage is supplied to the treatment 4 "jlI so that the sewage fluctuation surface is at the highest level, and several times the normal amount of air is supplied to the aeration pipe 6, thereby generating a water flow in the treatment tank and discharging the gravel 3 (= The remaining excess sludge is forcibly peeled off. As a result, a mixed solution of the peeled sludge and sewage fills the treatment tank.

この混合液を汚泥輸送ポンプP2の作動により導管Tを
介して処理槽上部の陶管9に通じて木質系濾材内に供給
する。この場合水分は山形状アミ4の凹部から槽内に還
流し、木質系波相9内には適量の水分を保有した汚泥の
みが残留し生物分解(土壌動物、土壌微生物、植物根)
を受けるのである。
This mixed liquid is supplied into the wood-based filter medium through the conduit T through the ceramic tube 9 in the upper part of the treatment tank by the operation of the sludge transport pump P2. In this case, water flows back into the tank from the concave part of the mountain-shaped ridge 4, and only sludge with an appropriate amount of moisture remains in the woody wave 9 and is biodegraded (soil animals, soil microorganisms, plant roots).
You receive it.

さらに陶管8の末端を最初沈澱槽に返送する構造として
置けば脱窒にも役立ちのである。また本実施例において
1i−空つぎした陶管を使用したがこれに限定するもの
でなく、例えば陶管に多数の透水孔を設けたものを接続
する好、管体内部から礫層に汚泥汚水が透水するような
構造であればよい。
Furthermore, if the end of the ceramic tube 8 is initially returned to the settling tank, it will also be useful for denitrification. In addition, although a 1i-empty ceramic pipe was used in this example, it is not limited to this. For example, it is preferable to connect a ceramic pipe with a large number of permeable holes. Any structure that allows water to pass through is sufficient.

本発明が通常のドレンチェ法と異なる点は、汚泥分解装
置が15日とか数箇月に1回という間欠使用されること
と、通気性土壌中で下層から散気管6によって強制通気
されている為に生物の活性が非常に高い土壌層を描成し
、その結果汚泥の分解が促進される点である。
The difference between the present invention and the normal drench method is that the sludge decomposition equipment is used intermittently, once every 15 days or every few months, and because forced aeration is carried out from the lower layer in the permeable soil using an aeration pipe 6. This method creates a soil layer with extremely high biological activity, which promotes the decomposition of sludge.

第3図は本発明の池の実施例を示し、土壌被覆型装置外
の通気性土壌と連続した土壌内に余剰汚泥分解装置を組
合せた装置の断面図である。この装置は最初沈澱槽の余
剰汚泥処理装置用であるが、装置の簡略化が必要である
場合は、アミ4′、陶管8.木質系波相9を省略しても
よい−。処η11槽1の側壁に沿って合成4に1脂等で
できた不透水槽10を延設する。具体的設計に関しては
、不透水槽10の高さは1回の余剰汚泥の注入量で定め
ればよい。不透水槽10の上方に粗砂11を敷藁する。
FIG. 3 shows an embodiment of the pond of the present invention, and is a cross-sectional view of a device in which an excess sludge decomposition device is combined in soil that is continuous with permeable soil outside the soil-covered device. This device is initially used for treating excess sludge in a settling tank, but if it is necessary to simplify the device, use the following methods: The wood wave phase 9 may be omitted. A water-impermeable tank 10 made of a synthetic resin or the like is extended along the side wall of the treatment tank 1. Regarding the specific design, the height of the impermeable tank 10 may be determined by the amount of surplus sludge injected at one time. Coarse sand 11 is spread over the impermeable tank 10.

この粗砂11は余剰汚泥と一部にポンプ揚水された水分
が濾別されて、処理4qlJ内に還流させるよう10c
IIl程度敷設すればよい。12は5〕と同様の濾材で
あり、粗砂11の上方、陶管13の周囲に設置する。陶
管13は透水性を有するように(11Y成されており、
汚泥輸送ポンプによって汚水が供給される。陶管のかわ
りに半裁の孔あき塩ビ管を用いてもよい。濾材12の上
方は山形状アミ14を介して通気性土壌15と通じてい
る。通気性土壌15の全体の沫さは60cm前後であり
−に部30<:+^は外部土壌と連続した構造が原則で
あるが、連続し Jていない場合も実施可能である。尚
、陶管13の末端を最初沈澱槽流入口に還流させる構造
とすると、脱窒にも役立つのは第1図の実施例と同しで
ある。また、汚泥分解装置は年数回供給するのであるが
、ミミズの自然発生を待たず適当量供給すると好ましい
This coarse sand 11 is heated to 10c so that excess sludge and some water pumped up are filtered out and returned to the treatment 4qlJ.
It is sufficient to install about IIl. 12 is a filter medium similar to 5], and is installed above the coarse sand 11 and around the ceramic tube 13. The ceramic tube 13 is made of 11Y so as to have water permeability.
Sewage is supplied by a sludge transport pump. Half-cut perforated PVC pipes may be used instead of ceramic pipes. The upper part of the filter medium 12 communicates with the permeable soil 15 via the mountain-shaped mesh 14. The overall permeability of the permeable soil 15 is around 60 cm, and the structure in which the permeable soil 15 is continuous with the external soil is a general rule, but it is also possible to implement the structure in which the permeable soil 15 is not continuous. It should be noted that if the end of the ceramic tube 13 is constructed to initially flow back to the inlet of the settling tank, it will also be useful for denitrification, as in the embodiment shown in FIG. In addition, although the sludge decomposition equipment is supplied several times a year, it is preferable to supply an appropriate amount without waiting for the natural generation of earthworms.

第4図は本発明の別の実施例であり、汚泥を液肥利用す
るために汚泥分解装置を処理槽と接触させていない。こ
の場合粗砂を必要としない点で第2図の実施97と相異
する。装置全体の深さは60em程度でる。不透水4a
16は標準的には高さ20〜30 am、 [1」50
 coo程度が好ましい。
FIG. 4 shows another embodiment of the present invention, in which the sludge decomposition device is not brought into contact with the treatment tank in order to utilize the sludge as liquid fertilizer. This case differs from embodiment 97 of FIG. 2 in that coarse sand is not required. The depth of the entire device is about 60 em. Impermeable 4a
16 is typically 20-30 am high, [1''50
It is preferable that it is around coo.

本発明は以上のように、たえず汚泥分解装置を活用する
のでなく数箇月に1回という間欠に使用するように構成
したので、犬規俣で複雑な装置でなくとも余剰汚泥を十
分に分解でき、汚水処理槽の処理能力が向上するのであ
る。また農緑地の利用形態によっては、濾材に散気の余
剰気体が注入される方式を組合せておくと効率がよくな
る。
As described above, the present invention is configured so that the sludge decomposition device is used intermittently, once every few months, rather than constantly, so excess sludge can be sufficiently decomposed in Inukimata without a complicated device. , the processing capacity of the sewage treatment tank will be improved. Also, depending on the type of use of agricultural and green space, efficiency may be improved by combining a method in which surplus gas for aeration is injected into the filter medium.

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

第1図は本発明の実施例の平面図、第2図はt51図の
装置の一部断面図、153図は本発明の池の実施例を示
す断面図、第4図は本発明の別の実施例を示す断面図で
ある。 1・・・処理槽、2・・・多孔板、3・・・礫、4・・
・アミ、6・・・散気管、7・・・通気性土壌、訃・・
陶管、9・・・木質系濾材、P2・・・汚泥輸送ポンプ
。 特許出願人 新 見 正 外2名 代理人弁理士 鈴 木 征 四 部 第1図 第肇鴇可
FIG. 1 is a plan view of an embodiment of the present invention, FIG. 2 is a partial sectional view of the device shown in FIG. FIG. 1... Treatment tank, 2... Perforated plate, 3... Gravel, 4...
・Ami, 6...Aeration pipe, 7...Aerated soil, Graves...
Ceramic pipe, 9...wood filter material, P2...sludge transport pump. Patent Applicant Niimi Seiji and two other Patent Attorneys Masaru Suzuki Part 4 Figure 1 Toka Hajime

Claims (2)

【特許請求の範囲】[Claims] (1)汚水処理槽に汚水を導入し、該処理槽内の下部に
配設した多孔板上に礫層を設け、該礫層を被覆する通気
性土壌との間にアミを介在させて構成した水位変動層に
汚水面を上下動せしめ、」二記通気性土壌より汚水の一
部を外部土壌中に浸潤排出せしめる汚水処理方法におい
て、槽の底部に散気管を設け、礫に付着した余剰汚泥を
散気管からの強制送気によって剥離させ、その剥離汚泥
を槽壁上部に設けた木質系濾材層内で分解することを特
徴とする土壌被覆型汚水処理装置と組合せた余剰汚泥の
分解処理方法。
(1) Sewage is introduced into a sewage treatment tank, a gravel layer is provided on a perforated plate placed at the bottom of the treatment tank, and a layer is interposed between the gravel layer and the permeable soil covering it. In the sewage treatment method, a part of the sewage is infiltrated and discharged from the permeable soil into the external soil by moving the sewage surface up and down in a water level fluctuation layer. A decomposition treatment of surplus sludge combined with a soil-covered sewage treatment device characterized by exfoliating sludge by forced air supply from an aeration pipe and decomposing the exfoliated sludge in a wood-based filter layer provided on the upper part of a tank wall. Method.
(2)凹型汚水処理槽内の下部に多孔板を配設して、処
理槽底面との間に汚水流下槽を形成し、上記多孔板上に
礫層を設け、該礫層の上部にアミを介して通気性土壌を
被覆して構成した汚水処理装置において、槽の底部に散
気管を設け、槽壁上部に透水性を有する管体を延設し、
該管体の周囲に通気性土壌と連終して木質系濾材を設置
し、前記散気管に強制送気を行なうことによって礫に付
着した。 余剰汚泥を剥離させ、この余剰汚泥と汚水の混合水を管
体内に供給するように構成したことを特徴とする土壌被
覆型汚水処理装置と組合せた余剰汚泥の分解装置。
(2) A perforated plate is placed at the bottom of the concave sewage treatment tank to form a sewage flow tank between it and the bottom of the treatment tank, a gravel layer is provided on the perforated plate, and a gravel layer is placed above the gravel layer. In a sewage treatment device constructed by covering permeable soil through a tank, an aeration pipe is provided at the bottom of the tank, and a permeable pipe body is installed at the top of the tank wall,
A wood-based filter medium was installed around the pipe body in continuous contact with the permeable soil, and air was forced to flow through the aeration pipe to cause it to adhere to the gravel. A surplus sludge decomposition device combined with a soil-covered sewage treatment device, characterized in that the surplus sludge is peeled off and a mixed water of the surplus sludge and sewage is supplied into a pipe body.
JP16115083A 1983-09-01 1983-09-01 Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus Pending JPS6051595A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16115083A JPS6051595A (en) 1983-09-01 1983-09-01 Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16115083A JPS6051595A (en) 1983-09-01 1983-09-01 Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus

Publications (1)

Publication Number Publication Date
JPS6051595A true JPS6051595A (en) 1985-03-23

Family

ID=15729540

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16115083A Pending JPS6051595A (en) 1983-09-01 1983-09-01 Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus

Country Status (1)

Country Link
JP (1) JPS6051595A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5526920A (en) * 1978-08-15 1980-02-26 Tokyo Shibaura Electric Co Ultrasonic eave diagnosis device
JPS5623672A (en) * 1979-08-01 1981-03-06 Hitachi Ltd Method of controlling air conditioner
JPS5746919A (en) * 1980-09-03 1982-03-17 Kyosei Seiyaku Kk Remedy for radioinflammation and cushing's ulcer

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5526920A (en) * 1978-08-15 1980-02-26 Tokyo Shibaura Electric Co Ultrasonic eave diagnosis device
JPS5623672A (en) * 1979-08-01 1981-03-06 Hitachi Ltd Method of controlling air conditioner
JPS5746919A (en) * 1980-09-03 1982-03-17 Kyosei Seiyaku Kk Remedy for radioinflammation and cushing's ulcer

Similar Documents

Publication Publication Date Title
US4209388A (en) Method and apparatus for treating sewage
US5707513A (en) Wastewater treatment method and apparatus
JPH0394893A (en) Waste water disposal system
US5980739A (en) Wastewater treatment method and apparatus
US6153094A (en) Wastewater treatment method and apparatus
US2795542A (en) Disposal of septic tank effluent and the like
US4050907A (en) Organic waste treating and conversion system
EP0836585B1 (en) Treatment system for treating waste water
CN106688900A (en) Circulating system with integrated ecological cultivation, planting and liquid manure treatment
CN106430581A (en) Aeration type downward-flow constructed wetland wastewater treatment system
CN205856282U (en) A kind of feces disposal equipment
CN108975625A (en) A kind of artificial wet land system with recovery of nitrogen and phosphorus effect
JPS6051595A (en) Excessive sludge decomposition treatment method and apparatus combined with soil covering type sewage treating apparatus
GB2140402A (en) Plant for processing organic material
CN207792820U (en) A kind of two-stage artificial wet land treating system
CN205676333U (en) A kind of system utilizing artificial wetland treatment slaughterhouse sewage
KR20010022136A (en) Improvements to mechanical composting
CA2096175C (en) Wastewater treatment method and apparatus
JPH02157096A (en) Fixed bed type bioreactor
CN207792972U (en) Artificial wetland treatment device
JP3076024B2 (en) Water purification device using inclined soil tank and water purification method using the same
JP4370699B2 (en) Wastewater treatment equipment
CN213285808U (en) Livestock and poultry breeding industry waste water high efficiency processing apparatus
KR102587711B1 (en) Slurry liquid fertilizer production and circulation system of livestock excrement with effect reducing odor, and Method for treating excrement of livestock using the same
CN109368933A (en) Adjustable type artificial wet land system