JPH07115022B2 - Sewage purification method and device - Google Patents

Sewage purification method and device

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Publication number
JPH07115022B2
JPH07115022B2 JP60052729A JP5272985A JPH07115022B2 JP H07115022 B2 JPH07115022 B2 JP H07115022B2 JP 60052729 A JP60052729 A JP 60052729A JP 5272985 A JP5272985 A JP 5272985A JP H07115022 B2 JPH07115022 B2 JP H07115022B2
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JP
Japan
Prior art keywords
soil
sewage
layer
soil layer
permeable
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Japanese (ja)
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JPS61212386A (en
Inventor
利之 若月
孝男 国松
修一 小村
裕治 安部
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利之 若月
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Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野及び従来技術〕 本発明は、汚水性に下水や屎尿の一次,二次処理水や生
活雑排水を、土壌を利用して更に高度に浄化する土壌浄
化法及び土壌浄化原理を利用した汚水浄化装置の改良に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application and prior art] The present invention further purifies sewage, primary and secondary treated water of sewage, and domestic wastewater to sewage to a higher degree using soil. The present invention relates to improvement of a sewage purification device using a soil purification method and a soil purification principle.

理想的な汚水浄化方法は、汚水中のSS分,BOD及びCOD
分,アンモニアその他の有機物を吸着や分解除去したり
脱臭するだけでなく、窒素分や燐の除去を質,量ともに
効率的に実行し、且つ十分な耐用年数(例えば10年以
上)を有するものであると言うことができる。然るに、
従来から我国で広く行われている撒水濾床法や活性汚泥
法は、大量のエネルギーを消費する上に悪臭成分や燐,
窒素分の除去に対しては殆ど無力である。
The ideal sewage purification method is SS content, BOD and COD in sewage.
Not only adsorbing, decomposing and removing organic matter such as ammonia, ammonia and deodorizing, but also efficiently removing nitrogen and phosphorus in quality and quantity, and having a sufficient service life (for example, 10 years or more) Can be said to be. However,
The sprinkling filter method and the activated sludge method, which have been widely used in Japan, consume a large amount of energy and also produce odorous components, phosphorus, and
Almost ineffective in removing nitrogen.

そこで最近、脱臭や燐,窒素分の除去を効率的に行う土
壌浄化法が脚光を浴びてきている。これは、土壌動物や
土壌微生物の消化・分解機能や土壌コロイドの持つ吸着
機能を積極的に利用するもので、省エネルギー省コスト
に優れたものである。しかし、現在実施されている土壌
処理法は完全に理想的なものとは言い難い。これは、理
想的な汚水浄化方法であるために土壌に要求される諸条
件が相矛盾しているにも拘わらず、それらの諸条件につ
いて十分な考察や検討がなされていないことに起因す
る。
Therefore, recently, a soil purification method that efficiently removes deodorant and phosphorus and nitrogen components has been in the spotlight. It actively utilizes the digestion / decomposition function of soil animals and soil microorganisms and the adsorption function of soil colloid, and is excellent in energy saving and cost saving. However, the soil treatment methods currently in use are not completely ideal. This is because although the various conditions required for soil are inconsistent as it is an ideal sewage purification method, those conditions have not been sufficiently considered or examined.

〔従来技術の問題点〕[Problems of conventional technology]

即ち土壌浄化法において、SS分,BOD及びCOD分,アンモ
ニアその他の有機物の分解除去や脱臭或いは硝化を効率
的に行なうためには、通気性のよい土壌中で好気的生物
活性を高めながら処理を行なう必要がある。この目的に
は、マサ土のように粗粒で通気性のよい土壌が向くが、
マサ土では窒素分の除去は勿論、長期的に見れば燐の除
去も効率的に行なうことは困難である。
That is, in the soil purification method, in order to efficiently decompose and remove SS components, BOD and COD components, ammonia and other organic substances, and deodorize or nitrify, treat them while enhancing aerobic biological activity in well-ventilated soil. Need to do. For this purpose, coarse-grained and well-ventilated soil like Masa soil is suitable,
In Masa soil, it is difficult to remove nitrogen as well as phosphorus efficiently in the long term.

まず、燐(正燐酸及びポリ燐酸)の除去を行なうために
は、土壌中に活性アルミニウム(場合によっては活性
鉄)が十分な量存在することが不可欠であるが、マサ土
にはこれらの成分が極めて少ない。通常、乾土重量当た
りにして0.1%以下である。(ここでは、土壌中の成分
のうち、0.15M蓚酸ナトリウム−蓚酸混液(pH3.5)に可
溶性のアルミニウム及び鉄を、夫々活性アルミニウム及
び活性鉄と定義する。)従って、従来のマサ土等を主体
とする浄化装置では1〜2年以内に燐の除去能力が半減
するのが普通である。
First, in order to remove phosphorus (orthophosphoric acid and polyphosphoric acid), it is indispensable that active aluminum (in some cases, active iron) is present in the soil. Is extremely small. Usually, it is 0.1% or less per dry soil weight. (Here, of the components in the soil, aluminum and iron soluble in 0.15M sodium oxalate-oxalic acid mixture (pH 3.5) are defined as active aluminum and active iron, respectively.) It is usual that the purifying device, which is the main constituent, halves the ability to remove phosphorus within 1-2 years.

一方、活性アルミニウム含量の高い土壌は、腐植質或い
は非腐植質の火山灰土壌,褐色或いは黄褐色森林土壌,
赤黄色土壌,灰色或いは褐色低地土壌等であるが、これ
らは一般に粘土含量が高く、通気性及び透水性に劣る。
従って、これらは細粒質で浄化装置内に充填した場合目
詰りが起き易く、汚水負荷量を大きく出来ないという致
命的な欠点を有する。
On the other hand, soils with high active aluminum content are humic or non-humic volcanic ash soils, brown or tan forest soils,
Red-yellow soils, gray or brown lowland soils, etc., which generally have a high clay content and are inferior in air permeability and water permeability.
Therefore, these have a fatal defect that when they are filled with fine particles in a purification device, they are apt to be clogged and the sewage load cannot be increased.

次に窒素分の除去の為には、好気的条件下でアンモニア
態窒素の硝化或いは亜硝酸化、次いで十分な炭素源の存
在と相対的な嫌気条件下で、微生物による脱窒反応(N2
やN2Oの生成と揮散)が行なわれる必要がある。このた
めには、好気的な土壌と嫌気的な土壌が共存する必要が
ある。
Next, in order to remove the nitrogen content, nitrification or nitration of ammonia nitrogen under aerobic conditions, followed by denitrification reaction (N 2
And N 2 O generation and volatilization). For this purpose, aerobic and anaerobic soils must coexist.

以上の考察から分かるように、汚水浄化装置内の土壌の
具備すべき性質は以下の3点に要約できる。
As can be seen from the above consideration, the properties that the soil in the wastewater purification device should have can be summarized into the following three points.

透水性が十分高いこと。土地の有効利用の見地から
考えて、汚水の1日当たりの処理能力が100〜200l/m2
上必要である。
Permeability is high enough. From the viewpoint of effective use of land, the daily treatment capacity of sewage is required to be 100 to 200 l / m 2 or more.

燐の除去能力が高いこと。200l/m2・日の負荷量と
して、全燐濃度の平均が5mg/l,除去率95%以上で10年の
耐用年数とすると、活性アルミニウムの量は、活性アル
ミニウムと燐の吸着比が1:1で燐の吸着効率を25%とし
て、15kg/m2以上必要である。従って、充填土壌の仮比
重を0.8g/cm3,土壌層の厚みを1.5mとすれば、活性アル
ミニウムの含量が1.25%以上の土壌を使用すれば良いこ
とになる。我国に広く分布する黒ボク土壌は、通常この
条件を満足している。
High phosphorus removal capacity. Assuming that the average load of total phosphorus concentration is 5 mg / l and the removal rate is 95% or more and the service life is 10 years with a loading of 200 l / m 2 / day, the amount of active aluminum is 1 When the adsorption efficiency of phosphorus is 25% at 1: 1, 15 kg / m 2 or more is required. Therefore, if the provisional specific gravity of the filled soil is 0.8 g / cm 3 and the thickness of the soil layer is 1.5 m, it is sufficient to use soil with an active aluminum content of 1.25% or more. Kuroboku soil widely distributed in Japan usually satisfies this condition.

透水・好気的土壌層と、脱窒に必要な有機物の供給
が可能でしかも相対的に嫌気的な土壌層が共存し、汚水
は両層を十分な速さで通過し、且つ両層に十分に接触・
浸透できる構造になっていること。
A permeable / aerobic soil layer and a relatively anaerobic soil layer capable of supplying organic substances necessary for denitrification coexist, and sewage passes through both layers at a sufficient speed, and Full contact
Must have a structure that can penetrate.

前記した理想的な汚水処理方法は、この相矛盾する3つ
の条件が共に満足されてこそ可能となる。
The ideal sewage treatment method described above can be realized only when these three contradictory conditions are satisfied.

しかし従来の土壌浄化法では、装置内に充填する土壌の
浄化能力に全面的に依存しているにもかかわらず、土の
種類,性質,構造或いは土壌層構造についての十分な検
討・研究が行われておらず、精々通気性土壌の必要性が
述べられている程度である。
However, in the conventional soil purification method, although it depends entirely on the purification ability of the soil filled in the equipment, sufficient examination and research on the soil type, properties, structure, or soil layer structure are performed. It has not been mentioned, and the need for air-permeable soil is stated at best.

〔問題を解決する手段、実施例〕[Means for Solving Problems, Examples]

そこで本発明者は、現在の土壌浄化法を更に理想的なも
のにするべく鋭意研究した結果、前記した土壌それ自体
についての考察を行い、本発明を完成させたものであ
る。
Therefore, the present inventor has completed the present invention by studying the soil itself as a result of earnest research to make the present soil purification method more ideal.

そして本発明は、性質の極めて異なる2種類の土壌、即
ち通気性及び透水性に優れた土壌(以下「透水・好気性
土壌」とする)と、通気性及び透水性は劣るが活性アル
ミニウム乃至活性鉄及び炭素源に富む土壌(以下「難透
水・嫌気性土壌」とする)を、夫々層状,階段状等に組
合せることにより、汚水の浄化に必要な相互に矛盾する
諸条件を満足させるもので、多段土壌層法とでも言うべ
きものである。以下、本発明を図面に示す実施例に基づ
いて詳細に説明する。
The present invention provides two types of soils having extremely different properties, that is, a soil excellent in air permeability and water permeability (hereinafter referred to as "water permeable / aerobic soil"), and an aluminum or active substance which is inferior in air permeability and water permeability. Soil that is rich in iron and carbon sources (hereinafter referred to as "impermeable and anaerobic soil") is combined in layers, steps, etc. to satisfy mutually contradictory conditions necessary for purification of sewage. Therefore, it should be called the multi-stage soil layer method. Hereinafter, the present invention will be described in detail based on embodiments shown in the drawings.

(構造) 第1図及び第2図は、本発明に係る汚水浄化装置(1)
の一例を示す。この汚水浄化装置(1)は、被覆土壌層
(2)中に配設した汚水撒水管(3)の下方に、透水・
好気性土壌層(4)・・・と難透水・嫌気性土壌層
(5)・・・を層状,階段状に充填したものである。
尚、図では、同種の土壌層が1/2ずつずれて重なり合
い、且つ他種の土壌層と連なって1つの層を形成したも
のが5段積みになっている。また被覆土壌層(2)は、
マサ土等の通気性土壌からなり、芝生等を植えることが
できる。汚水撒水管(3)の周囲は礫層(6)で囲ま
れ、礫層(6)の上面は目詰り防止用の網状体(7),
下面は汚水拡散用の隔板(8)で囲まれており、全体と
してトレンチ(9)を構成している。この隔板(8)
は、プラスチック成型品でもよいし、プラスチックやゴ
ムの柔軟なシートを用いてもよい。また最下層には、礫
層(10)に囲まれた有孔の排水管(11)(コルゲート管
等)が配設され、該礫層(10)の上面には網状体(12)
が設けられている。
(Structure) FIGS. 1 and 2 show a wastewater purifying apparatus (1) according to the present invention.
An example is shown. This sewage purification device (1) is provided with a permeable / water-permeable device under a sewage sprinkling pipe (3) arranged in a covered soil layer (2).
An aerobic soil layer (4) ... and a poorly permeable / anaerobic soil layer (5) ... are packed in layers and steps.
In the figure, the soil layers of the same type are overlapped with each other with a shift of 1/2, and one soil layer is formed in succession with the soil layers of other types to form a stack of five layers. The covered soil layer (2) is
It is made of breathable soil such as masa soil and can be used to plant lawns. The perimeter of the dirty water sprinkling pipe (3) is surrounded by a gravel layer (6), and the upper surface of the gravel layer (6) is a mesh body (7) for preventing clogging,
The lower surface is surrounded by a partition plate (8) for diffusing sewage, and constitutes a trench (9) as a whole. This partition (8)
May be a plastic molded product, or a flexible sheet of plastic or rubber may be used. In addition, a perforated drainage pipe (11) (corrugated pipe, etc.) surrounded by the gravel layer (10) is disposed in the lowermost layer, and a net-like body (12) is provided on the upper surface of the gravel layer (10).
Is provided.

そしてこれら全体が、コンクリート等不透水性素材から
なる槽(13)内に納められている。尚、槽(13)は周囲
だけのものでもよく、コンクリートやプラスチックの他
に、粘土,木材等透水性の低い素材も用いられ、時には
石積みや岩盤等も利用できる。また汚水撒水管(3)
は、目詰りや冬期の浄化能力の低下を考慮して、2組配
置している。
Then, all of them are housed in a tank (13) made of impermeable material such as concrete. It should be noted that the tank (13) may be only the surrounding area, and in addition to concrete and plastic, materials having low water permeability such as clay and wood are also used, and sometimes masonry or bedrock can be used. In addition, the sewage pipe (3)
In consideration of clogging and deterioration of purification capacity in winter, two sets are arranged.

具体的な装置としては、例えば被覆土壌層(2)を50c
m、各土壌層(4)・(5)の厚みを20cmとし(土壌層
全体で約1.5m)、周囲を厚み5〜10cm程度のコンクリー
ト槽(13)で囲んで処理済みの汚水を集水できるように
する。槽(13)の大きさは、汚水の処理量にもよるが例
えば最大で巾3m長さ20m程度とし、より大量の処理のた
めには、このような装置を多数並列すればよい。尚、有
機物の分解を助けるためにミミズ等の小動物を槽内で飼
うようにしてもよい。
As a concrete device, for example, the coated soil layer (2) is 50c.
m, each soil layer (4) / (5) has a thickness of 20 cm (total soil layer is about 1.5 m), surrounded by a concrete tank (13) with a thickness of about 5-10 cm to collect treated sewage. It can be so. Although the size of the tank (13) depends on the amount of wastewater treated, for example, the maximum width is about 3 m and the length is about 20 m, and a large number of such devices may be arranged in parallel. It should be noted that small animals such as earthworms may be kept in the tank in order to help the decomposition of organic substances.

次に、本発明において透水・好気性土壌層(4)を構成
する土壌とは、粗粒で粘土含量が10%以下,シルト含量
35%以下のもので、土性分類は砂土、壌質砂土、砂壌土
或いはこれらより粗い土壌を言う。マサ土、砂丘未熟
土、粗粒火山灰土、粗粒褐色森林土或いは粗粒褐色低地
土壌等が概ね透水・好気性土壌として適当である。
Next, in the present invention, the soil constituting the water-permeable / aerobic soil layer (4) means coarse grains with a clay content of 10% or less and a silt content.
The soil classification is sand soil, loamy sand soil, sandy loam soil, or coarser soil than these, which is less than 35%. Masa soil, immature dune soil, coarse-grained volcanic ash soil, coarse-grained brown forest soil or coarse-grained brown lowland soil is generally suitable as a permeable / aerobic soil.

この透水・好気性土壌の主要な役割は、汚水を難透水・
嫌気性土壌層(5)になるべく効率的に接触,拡散,浸
透できるようにするとともに、装置の目詰りを防止して
速やかに透水させることである。また、この透水・好気
性土壌を中心として、SS分,BOD及びCOD分その他の有機
物の好気的分解や硝化,脱臭等が行なわれる。従って、
この土壌には通気性及び透水性が大きいこと(例えば、
飽和透水性係数が10-2〜10-3cm/sよりも大)が要求され
る。場合によっては、粒径が0.2〜2.0mm程の砂、2mm〜
数cm程度までの粒径を持つ礫をこの透水・好気性土壌層
(4)に用いることができる。更に、その一部特に下部
等では、適当な大きさの木の枝や人工芝等、透水性を促
進させるものであれば何でも用いられる。
The main role of this permeable and aerobic soil is
The purpose is to allow the anaerobic soil layer (5) to contact, diffuse, and permeate as efficiently as possible, prevent clogging of the device, and allow water to permeate quickly. In addition, aerobic decomposition, nitrification, deodorization, etc. of SS, BOD, COD, and other organic substances are performed around this permeable and aerobic soil. Therefore,
The soil is highly breathable and water permeable (eg
Saturated hydraulic conductivity of 10 -2 to 10 -3 cm / s is required). Depending on the case, sand with a particle size of 0.2-2.0 mm, 2 mm-
Gravel with a particle size of up to several cm can be used for this permeable and aerobic soil layer (4). Further, in a part thereof, especially in the lower part thereof, any material such as a tree branch or an artificial grass having an appropriate size may be used as long as it promotes water permeability.

一方、難透水・嫌気性土壌層(5)を構成する土壌は、
粘土及び腐植の含量が合計20%以上(腐植含量が3〜5
%以上が望ましい)で、且つ活性アルミニウムがAlとし
て少なくとも対乾土2〜3重量%以上より好ましくは5
重量%以上のものであることが望ましい。比較的細粒の
黒ボク土壌(腐植質の火山灰土壌)、褐色或いは黄褐色
森林土壌の表層、灰色低地土壌等が難透水・嫌気性土壌
として適切である。難透水・嫌気性土壌の飽和透水係数
は、自然の土壌構造の破壊を考慮した再充填土壌とし
て、透水・好気性土壌の10分の1以下で、略10-3〜10-4
cm/s以下である。尚、活性アルミニウム含量が少ない難
透水・嫌気性土壌の場合は使用量を多くすればよい。例
えば、Alとして2〜3重量%の場合は5重量%の場合の
1.7〜2.5倍程度の難透水・嫌気性土壌が必要となる。こ
れは、使用する土壌層の段数を増やすとか、一層内の難
透水・嫌気性土壌の割合を増やすことで簡単に実現でき
る。また炭素源として、木の葉その他の動植物体、余剰
活性汚泥等C/N比の高い物質を混入しておいてもよい。
On the other hand, the soil that constitutes the impervious and anaerobic soil layer (5) is
The total content of clay and humus is 20% or more (humus content is 3-5
% Or more), and active aluminum as Al is at least 2 to 3% by weight or more with respect to dry soil, more preferably 5% or more.
It is desirable that the content be at least wt%. Relatively fine-grained black soil (humic volcanic ash soil), surface layers of brown or tan forest soil, gray lowland soil, etc. are suitable as poorly permeable and anaerobic soils. The saturated hydraulic conductivity of refractory and anaerobic soils is less than one-tenth that of permeable and aerobic soils as refilling soil considering the destruction of natural soil structure, and is about 10 -3 to 10 -4.
It is below cm / s. It should be noted that in the case of hardly water-permeable / anaerobic soil with a low content of active aluminum, the amount used may be increased. For example, if the Al content is 2 to 3% by weight, the Al content is 5% by weight.
1.7 to 2.5 times more difficult to permeate and anaerobic soil is required. This can be easily achieved by increasing the number of steps in the soil layer used or by increasing the proportion of hardly permeable / anaerobic soil in each layer. Further, as a carbon source, a substance having a high C / N ratio such as leaves and other plants and animals, and surplus activated sludge may be mixed.

(作用) しかして、汚水撒水管(3)から礫層(6)や被覆土壌
層(2)中に浸透した汚水(A)は、土壌生物の消化分
解作用や土の吸着や濾過作用により、SS分,BOD及びCOD
分その他の有機物の好気的分解や除去が行なわれる。ま
たアンモニア態窒素も硝化細菌の作用で硝化されて、処
理水(B)となる。これが、従来の土壌浄化法(毛管浄
化法)である。
(Action) Then, the sewage (A) that permeates the gravel layer (6) and the covered soil layer (2) from the sewage sprinkling pipe (3) is subjected to the digestive decomposition action of soil organisms and the adsorption and filtration action of soil, SS minutes, BOD and COD
Aerobic decomposition and removal of organic matter and other organic matter. Ammonia nitrogen is also nitrified by the action of nitrifying bacteria and becomes treated water (B). This is the conventional soil purification method (capillary purification method).

そしてこの処理水(B)の一部は、被覆土壌層(2)の
表面から蒸発散する。他の一部は、トレンチ(9)の下
方に配置された両土壌層(4)・(5)間を重力的に浸
透流下する。透水・好気性土壌層(4)は、通気性,透
水性の高い土壌よりなるため、処理水(B)は主として
透水・好気性土壌層(4)を通り(実線矢印)、より酸
化的条件下に置かれる。
And a part of this treated water (B) evaporates from the surface of the covered soil layer (2). The other part gravitationally flows down between the soil layers (4) and (5) arranged below the trench (9). Since the permeable / aerobic soil layer (4) is composed of highly permeable and permeable soil, the treated water (B) mainly passes through the permeable / aerobic soil layer (4) (solid arrow), and has more oxidative conditions. Placed below.

透水・好気性土壌層(4)の上下及び左右には、難透水
・嫌気性土壌層(5)が連なっている。従って、透水・
好気性土壌層(4)中を流れる処理水(B)は難透水・
嫌気性土壌層(5)に接触したり一部浸透拡散し(点線
矢印)、処理水(B)中の燐酸(正及びポリ)は、難透
水・嫌気性土壌層(5)中に容易に吸着固定される。一
方、処理水(B)中のNO2やNO3は同じく嫌気的で炭素源
に富む難透水・嫌気性土壌層(5)中で、脱窒菌の作用
によりN2やN2Oに変化し、脱窒される。尚、各種重金属
も吸着除去される。
A non-permeable and anaerobic soil layer (5) is connected above and below and to the left and right of the permeable and aerobic soil layer (4). Therefore, water permeability
The treated water (B) flowing through the aerobic soil layer (4) is not permeable to water.
The phosphoric acid (positive and poly) in the treated water (B) easily contacts the anaerobic soil layer (5) and partially penetrates (dashed arrow) to easily penetrate into the poorly permeable and anaerobic soil layer (5). It is fixed by adsorption. On the other hand, NO 2 and NO 3 in the treated water (B) are changed to N 2 and N 2 O by the action of denitrifying bacteria in the same anaerobic and carbon source-rich impermeable / anaerobic soil layer (5). , Denitrified. Various heavy metals are also adsorbed and removed.

かくして、SS分,BOD及びCOD分その他の有機物に加えて
窒素分や燐が略完全に除去された浄化水(C)が、排水
管(11)を通って装置外に排出される。
Thus, the purified water (C) from which SS, BOD, COD, and other organic substances, as well as nitrogen and phosphorus are almost completely removed, is discharged out of the apparatus through the drain pipe (11).

ところで、本発明装置(1)による浄化の程度や処理可
能量は、透水・好気性土壌層(4)と難透水・嫌気性土
壌層(5)の割合や配置状態、更には夫々用いる土壌の
種類や含有成分等により変化する。従って、汚水の量や
質及び目的とする浄化水の質等により最適な土壌層の組
合せを夫々具体的に決定するとよい。
By the way, the degree of purification and the treatable amount by the device (1) of the present invention are determined by the ratio and arrangement state of the permeable / aerobic soil layer (4) and the hardly permeable / anaerobic soil layer (5), and further of the soil used respectively. It changes depending on the type and contained components. Therefore, it is advisable to concretely determine the optimum combination of soil layers depending on the quantity and quality of wastewater and the desired quality of purified water.

例えば、透水・好気性土壌層(4)と難透水・嫌気性土
壌層(5)の好ましい比率は、汚水中の燐酸(正及びポ
リ)濃度によって異なる。実験結果によると、全燐とし
て10ppm含まれる汚水を200l/m2というような高負荷・高
速処理を目的とする場合は、難透水・嫌気性土壌の活性
アルミニウム含量が10%以上のときは難透水・嫌気性土
壌層(5)と透水・好気性土壌層(4)の比が概略1対
1である。活性アルミニウムの含量が5〜10%の時は2
対1、3〜5%のときは4対1程度である。
For example, the preferable ratio of the permeable / aerobic soil layer (4) to the hardly permeable / anaerobic soil layer (5) depends on the phosphoric acid (positive and poly) concentration in the sewage. According to the experimental results, when aiming at high load and high speed treatment of 200 l / m 2 of sewage containing 10 ppm of total phosphorus, it is difficult to obtain when the active aluminum content of the permeable and anaerobic soil is 10% or more. The ratio of permeable / anaerobic soil layer (5) to permeable / aerobic soil layer (4) is approximately 1: 1. 2 when the active aluminum content is 5-10%
When the ratio is 1 to 3 and 5%, it is about 4 to 1.

汚水中の燐酸(正及びポリ)濃度が5ppm,処理量が100l/
m2程度であれば、活性アルミニウムの濃度は上述の数値
の4分の1程度でも良いことになる。
Concentration of phosphoric acid (positive and poly) in wastewater is 5ppm, throughput is 100l /
If it is about m 2 , the concentration of active aluminum may be about 1/4 of the above value.

両土壌層の使用量の比率は、第1図の構造のものの場
合、各土壌層(4)・(5)の長さの割合に比例する。
或いは、第3図の如く土壌層(4)・(5)の連なった
ものの間に更に他の透水・好気性土壌層(14)を介挿す
るなど、第1図のものとは異なった構造のものとし、夫
々の土壌層(4)・(5)・(14)の割合を変えて両者
の比率を種々調整することも出来る。
In the case of the structure shown in FIG. 1, the ratio of the amount of use of both soil layers is proportional to the ratio of the length of each soil layer (4) / (5).
Alternatively, as shown in Fig. 3, another permeable / aerobic soil layer (14) is inserted between the soil layers (4) and (5) connected to each other, which is a different structure from that of Fig. 1. It is also possible to change the ratio of each soil layer (4), (5), (14) to variously adjust the ratio of both.

また、第1図における勾配θや、第1図,第3図におけ
る各土壌層の積み重ね段数や厚み等により、透水性更に
は浄化率が変化する。特に第3図の如く、処理水(B)
が難透水・嫌気性土壌層(5)により良く接するような
構造の場合、浄化率は向上する。
Further, the water permeability and the purification rate change depending on the gradient θ in FIG. 1 and the number of stacked layers and the thickness of each soil layer in FIGS. 1 and 3. Especially as shown in Fig. 3, treated water (B)
In the case where the structure has a structure that is better in contact with the poorly permeable / anaerobic soil layer (5), the purification rate is improved.

尚、第3図に示す具体的装置としては、透水・好気性土
壌層(4)と難透水・嫌気性土壌層(5)を夫々15cm程
度の厚みとし、使用量比を1対2とし、また両層(4)
・(5)間に5cm厚程度の透水・好気性土壌層(14)を
介挿したものが考えられる。その他の構造は第1図に示
すものと略同様にする。
As a concrete device shown in FIG. 3, the permeable / aerobic soil layer (4) and the hardly permeable / anaerobic soil layer (5) each have a thickness of about 15 cm, and the usage ratio is 1: 2, Both layers (4)
・ It is considered that a 5 cm thick permeable / aerobic soil layer (14) is inserted between (5). Other structures are substantially the same as those shown in FIG.

一般に、浄化水(C)の質よりも処理液量を重視した大
量処理の場合は、第1図の如き構造をとるとか、透水・
好気性土壌層(4)の割合を大きくして透水性を高めれ
ばよい。逆に、浄化水(C)の質を重視する場合は、第
3図の如く処理水(B)が難透水・嫌気性土壌層(5)
に接し易い構造とするか、難透水・嫌気性土壌層(5)
の割合を高くして透水性を低くすればよい。
Generally, in the case of a large amount of treatment in which the amount of treated liquid is more important than the quality of purified water (C), the structure shown in FIG.
The water permeability may be increased by increasing the ratio of the aerobic soil layer (4). On the contrary, when the quality of the purified water (C) is emphasized, the treated water (B) is the impervious and anaerobic soil layer (5) as shown in FIG.
A structure that makes it easy to come into contact with water, or a poorly permeable / anaerobic soil layer (5)
The water permeability may be lowered by increasing the ratio of.

このように本発明の汚水浄化装置は、汚水・好気性土壌
層(4)と難透水・嫌気性土壌層(5)を組合せて汚水
を処理する多段土壌層法の原理に基づくもので、各層
(4)・(5)の比や積層構造・積層段数を変化させる
ことにより、処理可能量と浄化水の質が任意に制御でき
ることが大きな特徴である。
As described above, the sewage purification apparatus of the present invention is based on the principle of the multi-stage soil layer method of treating sewage by combining the sewage / aerobic soil layer (4) and the hardly permeable / anaerobic soil layer (5). A major feature is that the treatable amount and the quality of purified water can be arbitrarily controlled by changing the ratio of (4) and (5), the laminated structure, and the number of laminated layers.

(比較例) 次に、本発明方法と従来法による土壌式浄化装置の汚水
浄化能を比較した結果を表1に示す。
(Comparative Example) Next, Table 1 shows the results of comparing the sewage purification capacities of the soil purification apparatus according to the method of the present invention and the conventional method.

尚本発明方法による装置(実施例)とは、実施例1が第
1図に示す構造のもの、実施例2が第3図に示す構造の
ものである。また従来方法による装置(比較例)とは、
トレンチの構造は本発明装置と同様であるがトレンチ下
部の充填土壌が多段土壌構造を持たず、マサ土のみ(比
較例1)及び黒ボクのみ(比較例2)のもので、実施例
と同じ厚さ(1m)に充填されている装置によるものであ
る。
The apparatus according to the method of the present invention (embodiment) has a structure shown in FIG. 1 for the first embodiment and a structure shown in FIG. 3 for the second embodiment. In addition, the device by the conventional method (comparative example) is
The structure of the trench is the same as that of the device of the present invention, but the filling soil in the lower part of the trench does not have a multi-stage soil structure, only the Masa soil (Comparative Example 1) and only Kuroboku (Comparative Example 2), the same as the Example. This is due to the device being filled to a thickness (1 m).

そして、ここで用いた透水・好気性土壌としてのマサ土
の活性アルミニウム及び活性鉄の含量は、夫々0.1及び
0.3%(乾土重量基準)、難透水・嫌気性土壌としての
黒ボクの活性アルミニウム及び活性鉄の含量は夫々5.6
%及び0.6%(乾土重量基準)であった。またトレンチ
下部の 土壌の仮比重は、比較例1のマサ土が1.5、比較例2の
黒ボクが0.8であるのに対し、実施例1,2とも夫々1.2で
あった。
And, the active aluminum and active iron contents of the Masa soil as the permeable and aerobic soil used here are 0.1 and
0.3% (dry soil weight basis), the content of activated aluminum and activated iron of Kuroboku as permeable soil / anaerobic soil is 5.6, respectively.
% And 0.6% (dry soil weight basis). Also at the bottom of the trench The temporary specific gravity of the soil was 1.5 for the masa soil of Comparative Example 1 and 0.8 for black pearl of Comparative Example 2, whereas it was 1.2 for both Examples 1 and 2.

この表から、比較例1では汚水処理可能量は大きいが浄
化水の質は格段に落ちることがわかる。また比較例2で
は目詰りを起こし易くて処理可能量が小さく、燐の除去
能力は高いが、脱窒は殆ど期待できない。これに対し実
施例(本発明装置)は1,2とも実用上十分な処理可能量
であり、しかも脱窒,燐の除去とも従来装置よりも優れ
ており、本発明装置が汚水処理可能量及び質的処理能力
の点で極めて優れていることがわかる。
From this table, it can be seen that in Comparative Example 1, the amount of wastewater that can be treated is large, but the quality of purified water is significantly reduced. Further, in Comparative Example 2, clogging is likely to occur, the treatable amount is small, and the phosphorus removal capability is high, but denitrification can hardly be expected. On the other hand, the embodiment (the device of the present invention) has a practically sufficient treatment amount for both 1 and 2, and is superior to the conventional device in denitrification and phosphorus removal. It can be seen that it is extremely excellent in terms of qualitative processing capacity.

(他の実施例) 以上は、透水・好気性土壌層(4)と難透水・嫌気性土
壌層(5)を、被覆土壌層(2)中に配設されている汚
水撒水管(3)の下方に配置したものについて説明した
が、本発明装置はこのような構造のものに限らない。
Other Examples The above is the sewage sprinkling pipe (3) in which the permeable / aerobic soil layer (4) and the hardly permeable / anaerobic soil layer (5) are arranged in the covered soil layer (2). However, the device of the present invention is not limited to such a structure.

例えば、透水・好気性土壌層(4)と難透水・嫌気性土
壌層(5)は第4図の如く汚水撒水管(3)の側方や上
方に配置されてもよい。この場合、汚水撒水管(3)か
らの汚水の浸透を妨げないように、透水・好気性土壌層
(4)の間に難透水・嫌気性土壌層(5)を点在させる
ようにするとよい。
For example, the water-permeable / aerobic soil layer (4) and the hardly water-permeable / anaerobic soil layer (5) may be arranged beside or above the waste water sprinkling pipe (3) as shown in FIG. In this case, it is advisable to intersperse the hardly permeable and anaerobic soil layers (5) between the permeable and aerobic soil layers (4) so as not to prevent the permeation of the sewage from the sewage sprinkling pipes (3). .

或いは、第5図のように汚水撒水管(3)の上方に別途
多孔の排水管(15)を設け、汚水撒水管(3)と排水管
(15)の間及びその周囲を含めて、透水・好気性土壌層
(4)と難透水・嫌気性土壌層(5)を配置するように
してもよい。これは、風呂排水や洗濯排水等が一度に排
出されて一次的に汚水量が多くなるような場合、汚水を
被覆土壌層(2)に逆浸透させて排水管(15)から排出
させるようにしたもので、逆浸透中に処理水を難透水・
嫌気性土壌層(5)で浄化させるものである。
Alternatively, as shown in FIG. 5, a separate perforated drainage pipe (15) is provided above the wastewater sprinkling pipe (3), and the permeated water is included between and around the wastewater sprinkling pipe (3) and the drainage pipe (15). -The aerobic soil layer (4) and the hardly permeable / anaerobic soil layer (5) may be arranged. This is because when the wastewater from the bath or laundry is discharged at one time and the amount of sewage increases temporarily, the sewage is reversely permeated into the covered soil layer (2) and discharged from the drain pipe (15). It is difficult to permeate treated water during reverse osmosis.
It is to be purified by the anaerobic soil layer (5).

また、汚水の供給源は汚水撒水管(3)に限らず、例え
ば第6図の如く地中に設けた汚水槽(16)でもよい。そ
して、この汚水槽(16)の開口部から周囲に透水・好気
性土壌槽(4)と難透水・嫌気性土壌槽(5)を設け
て、処理水(B)を浄化水(C)とすることもできる。
Further, the source of the sewage is not limited to the sewage spouting pipe (3), but may be a sewage tank (16) provided in the ground as shown in FIG. 6, for example. Then, a permeable / aerobic soil tank (4) and a hardly permeable / anaerobic soil tank (5) are provided around the opening of the sewage tank (16) to treat the treated water (B) as purified water (C). You can also do it.

第4図〜第6図においては槽(13)及び排水管(11)は
図示を省略したが、第1図の場合と同様これらを設けて
集水式としてもよく、またこれらを略して地下浸透式に
してもよい。勿論第1図及び第3図に示す装置でも槽
(13)を省略して地下浸透式としてもよい。地下浸透式
とする場合、各土壌槽(4)・(5)を広くするなど汚
水が難透水・嫌気性土壌層に接し易いような構造とす
る。或いは、第1図における槽(13)の代わりに(特に
周囲を)黒ボク等の難透水・嫌気性土壌で囲ってもよ
い。
Although the tank (13) and the drainage pipe (11) are not shown in FIGS. 4 to 6, they may be provided with a water collecting type by providing them similarly to the case of FIG. Permeation type may be used. Of course, even in the apparatus shown in FIGS. 1 and 3, the tank (13) may be omitted and an underground infiltration type may be used. In the case of the underground infiltration type, the soil tanks (4) and (5) should be widened so that sewage can easily come into contact with the poorly permeable and anaerobic soil layers. Alternatively, instead of the tank (13) shown in FIG. 1, (particularly around), it may be surrounded by a non-permeable and anaerobic soil such as black bokeh.

尚、透水・好気性土壌や難透水・嫌気性土壌層は、第1
図及び第3図の場合を含めて夫々ある塊として配置すれ
ばよく、必ずしも層状のものに限るわけではないが、処
理効率及び設計・施工の面から見て層状のものが最も良
い。
The permeable / aerobic soil and the hardly permeable / anaerobic soil layer are the first
As shown in FIG. 3 and FIG. 3, it may be arranged as a certain lump, and is not necessarily limited to the layered one, but the layered one is the best from the viewpoint of treatment efficiency and design / construction.

〔効果〕 以上詳述したように、本発明方法は、有孔汚水撒水管等
の汚水供給源から周囲の土壌層中に浸透させた汚水を、
汚水中に含まれるSS分,BOD或いはCOD分,アンモニアそ
の他の有機物を通気性及び透水性に優れた土壌層中で好
気的分解や硝化作用を加えつつ流下或いは逆浸透させ、
その途中に於いて通気性や透水性に劣るが活性アルミニ
ウムや活性鉄及び炭素源に富む土壌層に接触,拡散,浸
透させて燐の吸着と脱窒を行わせるものである。
[Effect] As described in detail above, the method of the present invention, the sewage permeated into the surrounding soil layer from a sewage supply source such as a perforated sewage pipe,
SS, BOD or COD contained in wastewater, ammonia and other organic substances are allowed to flow down or reverse osmosis while adding aerobic decomposition and nitrification in a soil layer with excellent air permeability and water permeability.
During this process, it adsorbs and denitrifies phosphorus by contacting, diffusing, and permeating a soil layer rich in activated aluminum, activated iron, and carbon source, which has poor air permeability and water permeability.

従って本発明方法によれば、汚水の脱臭や汚濁有機物の
分解除去のみならず、従来の土壌浄化法では困難乃至不
可能であった全燐や全窒素分の除去が質・量ともに効率
的に行うことが可能となる。特に、土壌中の活性アルミ
ニウムの含量がある基準値以上の場合、通常の生活雑排
水や屎尿の一次,二次処理水等であれば十年以上にわた
って高い燐除去能を保持することができる。
Therefore, according to the method of the present invention, not only deodorization of sewage and decomposition and removal of polluted organic matter, but also removal of total phosphorus and total nitrogen, which were difficult or impossible by conventional soil purification methods, are efficiently performed in both quality and quantity. It becomes possible to do. In particular, when the content of active aluminum in the soil is higher than a certain standard value, high phosphorus removal ability can be maintained for 10 years or longer with ordinary domestic wastewater or treated primary sewage or secondary effluent.

また本発明装置は、汚水撒水管や汚水槽の開口部が配設
されている被覆土壌層自体、或いは被覆土壌層の側方や
特に下方に、汚水・好気性土壌層と難透水・嫌気性土壌
層を層状,階段状に配置したものである。従って、構築
するのに高度な技術もいらず、処理操作も簡単で省エネ
ルギー,省コストなものである。しかも、透水・好気性
土壌層と難透水・嫌気性土壌層の比率や積層構造を工夫
することにより、汚水の処理可能量や浄化水の質を自在
に制御できる等多くの利点を有している。
Further, the device of the present invention is provided with a sewage / aerobic soil layer and a non-permeable / anaerobic sewage / aerobic soil layer itself or on the side or particularly below the coated soil layer in which the opening of the sewage spouting pipe or the sewage tank is arranged. The soil layers are arranged in layers and steps. Therefore, it requires no advanced technology for construction, and the processing operation is simple, energy saving and cost saving. Moreover, by devising the ratio of the permeable / aerobic soil layer to the difficultly permeable / anaerobic soil layer and the layered structure, there are many advantages such as the controllable amount of sewage and the quality of purified water. There is.

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

第1図は本発明に係る汚水浄化装置の一例を示す縦断面
図、第2図は同じく横断面図である。第3図乃至第6図
は夫々異なる他の例を示し、第3図及び第6図は縦断面
図、第4図及び第5図は横断面図である。 1……汚水浄化装置 2……被覆土壌層 3……汚水撒水管 4・14……透水・好気性土壌層 5……難透水・嫌気性土壌層 6・10……礫層 7・12……網状体 8……隔板 9……トレンチ 11・15……排水管 13……槽 16……汚水槽 A……汚水 B……処理水 C……浄化水
FIG. 1 is a longitudinal sectional view showing an example of the wastewater purifying apparatus according to the present invention, and FIG. 2 is a transverse sectional view of the same. FIGS. 3 to 6 show other different examples, FIGS. 3 and 6 are longitudinal sectional views, and FIGS. 4 and 5 are transverse sectional views. 1 …… Sewage purification device 2 …… Coated soil layer 3 …… Sewage sprinkling pipe 4 ・ 14 …… Permeable / aerobic soil layer 5 …… Slightly permeable / anaerobic soil layer 6 ・ 10 …… Gravel layer 7 ・ 12 ... … Mesh 8 …… Separator 9 …… Trench 11 ・ 15 …… Drainage pipe 13 …… Tank 16 …… Sewage tank A …… Sewage B …… Treated water C …… Purified water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 安部 裕治 島根県八束郡八束町二子896 (56)参考文献 特開 昭57−194090(JP,A) 特公 昭59−31400(JP,B2) 特公 昭57−54194(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yuji Abe 896 Futako, Yatsuka-cho, Yatsuka-gun, Shimane Prefecture (56) Reference JP-A-57-194090 (JP, A) JP-B 59-31400 (JP, B2) JP Kosho 57-54194 (JP, B2)

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】汚水供給源から周囲の土壌層中に浸透させ
た汚水を、汚水中に含まれるSS分,BOD及びCOD分,アン
モニアその他の有機物を砂土、壌質砂土、砂壌土或いは
これらより粗い土壌からなる通気性及び透水性に優れた
土壌層中で好気的分解や硝化作用を加えつつ流下或いは
逆浸透させ、その途中に於いて通気性や透水性に劣るが
活性アルミニウムや活性鉄及び炭素源に富む土壌層であ
って上記透水・好気性土壌層と層状,階段状に組み合わ
せて設けた黒ボク土壌、褐色或いは黄褐色森林土壌の表
層、或いは灰色低地土壌からなる土壌層に接触,拡散,
浸透させて、汚水中の燐の吸着除去と脱窒を行わせるこ
とを特徴とする汚水の浄化方法。
1. The sewage infiltrated into the surrounding soil layer from the sewage supply source is used as SS, BOD and COD, and ammonia and other organic substances contained in the sewage as sand soil, loamy sand, sandy loam, or these. In a soil layer consisting of coarser soil with excellent air permeability and water permeability, it is made to flow down or reverse osmosis while adding aerobic decomposition and nitrifying action. A soil layer rich in iron and carbon sources, which is a combination of the above-mentioned permeable / aerobic soil layer in a layered or stepwise manner, on the surface of a black or brown forest soil, or a soil layer consisting of a gray lowland soil. Contact, diffusion,
A method for purifying sewage, which is characterized by adsorbing and removing phosphorus in sewage and performing denitrification after permeation.
【請求項2】汚水の処理可能量及び処理の程度を、汚水
が通過する両土壌層の配置,段数或いは量的割合を変え
ることにより任意に設定できるものである特許請求の範
囲第1項記載の汚水の浄化方法。
2. The method according to claim 1, wherein the treatable amount of sewage and the degree of treatment can be arbitrarily set by changing the arrangement, the number of stages or the quantitative ratio of both soil layers through which the sewage passes. How to purify sewage in Japan.
【請求項3】周囲を不透水性素材で囲み、浄化水を下部
に集水するものである特許請求の範囲第1項又は第2項
記載の汚水の浄化方法。
3. The method for purifying sewage according to claim 1 or 2, wherein the periphery is surrounded by an impermeable material and purified water is collected in the lower part.
【請求項4】有孔汚水撒水管或いは汚水槽開口部が位置
する被覆土壌層の少なくとも下方の一部に、砂土、壌質
砂土、砂壌土或いはこれらより粗い土壌からなる通気性
及び透水性に優れた土壌層と、黒ボク土壌、褐色或いは
黄褐色森林土壌の表層、或いは灰色低地土壌からなる通
気性及び透水性は劣るが活性アルミニウム乃至活性鉄及
び炭素源に富む土壌層を、層状,段階状に多段に配置し
たことを特徴とする汚水の浄化装置。
4. Permeability and water permeability of sandy soil, loamy sandy soil, sandy loam soil, or coarser soil in at least a part of the lower part of the covered soil layer where the perforated drainage pipe or the opening of the wastewater tank is located. Excellent soil layer, black my soil, surface layer of brown or tan forest soil, or gray lowland soil with poor permeability and water permeability, but a layer of soil rich in active aluminum or active iron and carbon source, layered, A sewage purification device characterized by being arranged in stages in multiple stages.
【請求項5】最下層に礫層で囲まれた排水管を配設し、
周囲及び底面を不透水性素材で囲んでなる特許請求の範
囲第4項記載の汚水の浄化装置。
5. A drainage pipe surrounded by a gravel layer is provided at the lowermost layer,
The sewage purification device according to claim 4, wherein the periphery and the bottom surface are surrounded by an impermeable material.
JP60052729A 1985-03-16 1985-03-16 Sewage purification method and device Expired - Fee Related JPH07115022B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60052729A JPH07115022B2 (en) 1985-03-16 1985-03-16 Sewage purification method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60052729A JPH07115022B2 (en) 1985-03-16 1985-03-16 Sewage purification method and device

Publications (2)

Publication Number Publication Date
JPS61212386A JPS61212386A (en) 1986-09-20
JPH07115022B2 true JPH07115022B2 (en) 1995-12-13

Family

ID=12923011

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH07115022B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63171696A (en) * 1986-12-30 1988-07-15 Bandou Gijutsu Kogyo Kk Lake and marsh purifying boat
JP2835394B2 (en) * 1988-10-26 1998-12-14 カナツ技建工業株式会社 Sewage purification method and apparatus
KR101163061B1 (en) * 2009-11-02 2012-07-05 한국과학기술연구원 Equipment and method for water and stream purification using layered soil system
CN108059304B (en) * 2017-12-24 2021-04-02 苏州市海魄洁净环境工程有限公司 Constant temperature water supply device
CN112390462A (en) * 2020-11-02 2021-02-23 广西金妙松环保工程有限公司 Multilayer medium filler for efficient dephosphorization and denitrification and preparation method thereof
CN114230103B (en) * 2021-12-23 2023-04-07 西南交通大学 Rural distributed domestic sewage treatment device based on multistage soil infiltration system
CN114524589B (en) * 2022-03-04 2023-10-10 贵州中化新能源开发有限公司 Ecological low-energy-consumption efficient laminated infiltration sewage treatment system and method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0046628A3 (en) * 1980-08-18 1982-05-26 Gulf Research & Development Company Process for the preparation of nickel ylides containing directly sulfonated ylide ligands
JPS58216782A (en) * 1982-06-09 1983-12-16 Koji Niwayama Evaporation and diffusion device
JPS5931400A (en) * 1982-08-16 1984-02-20 川崎重工業株式会社 Tunnel excavator

Also Published As

Publication number Publication date
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