JPH0741251B2 - Sewage purification device - Google Patents

Sewage purification device

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Publication number
JPH0741251B2
JPH0741251B2 JP1073086A JP1073086A JPH0741251B2 JP H0741251 B2 JPH0741251 B2 JP H0741251B2 JP 1073086 A JP1073086 A JP 1073086A JP 1073086 A JP1073086 A JP 1073086A JP H0741251 B2 JPH0741251 B2 JP H0741251B2
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JP
Japan
Prior art keywords
soil
layer
water
permeable
sewage
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
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JP1073086A
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Japanese (ja)
Other versions
JPS63240991A (en
Inventor
利之 若月
孝男 国松
修一 小村
裕治 安部
Original Assignee
利之 若月
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Priority to JP1073086A priority Critical patent/JPH0741251B2/en
Publication of JPS63240991A publication Critical patent/JPS63240991A/en
Publication of JPH0741251B2 publication Critical patent/JPH0741251B2/en
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Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔技術分野〕 本発明は、汚水特に下水や屎尿の一次,二次処理水や生
活雑排水或いは養豚場その他からの酪農廃水等を、土壌
を利用して高度に浄化する土壌浄化装置の改良に関す
る。
Description: TECHNICAL FIELD The present invention highly purifies sewage, especially sewage, primary and secondary treated water of human waste, dairy wastewater from domestic sewage, etc. or dairy wastewater from pig farms, etc., using soil. To improve the soil purification device.

〔技術的背景〕[Technical background]

土壌浄化法は、土壌動物や土壌微生物の消化・分解昨日
や土壌コロイドの持つ吸着機能を積極的に利用して汚水
を浄化するものである。従って、汚水中のSS分やBOD,CO
D分、アンモニアその他の有機物の吸着や分解除去は勿
論のこと、従来広く用いられている撒水濾床法や生活汚
泥法では除去し難い燐や窒素分の除去や脱臭も容易に行
えしかも省エネルギー省コストに優れている。
The soil purification method purifies sewage by actively utilizing the adsorption function of digestion and decomposition of soil animals and soil microorganisms yesterday and soil colloids. Therefore, SS content, BOD, CO
Not only can D components, ammonia and other organic substances be adsorbed and decomposed and removed, but also phosphorus and nitrogen, which are difficult to remove by the widely used sprinkling filter method and domestic sludge method, can be easily removed and deodorized, as well as energy saving. The cost is excellent.

しかし、従来実施されている土壌浄化法は完全に理想的
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。そこで本発明者は鋭
意研究した結果、土壌浄化装置に用いる土壌に要求され
る性質は以下の3点に要約できるとの知見を得た。
However, conventional soil purification methods 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. Therefore, as a result of earnest studies, the present inventor has found that the properties required for the soil used in the soil purifying apparatus can be summarized in the following three points.

透水性が十分高く、目詰りが起こりにくいこと。こ
れは、汚水処理能力を決定する。土地の有効利用の見地
から重要な性質である。
The water permeability is high enough that clogging is unlikely to occur. This determines the wastewater treatment capacity. It is an important property from the viewpoint of effective use of land.

活性アルミニウムや活性鉄等の燐酸を吸着できる化
合物の含量が高いこと。これは、汚水からの燐の除去能
力を決定する。
High content of compounds capable of adsorbing phosphoric acid such as activated aluminum and activated iron. This determines the ability to remove phosphorus from wastewater.

アンモニア態窒素の硝化や亜硝酸化に必要な好気的
な土壌層と、微生物による脱窒作用に必要な炭素源の供
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接触浸透
できる構造になっていること。これは、汚水中の汚濁物
質の分解浄化だけでなく、汚水中の窒素除去能力を決定
する。
The aerobic soil layer required for nitrification and nitrite of ammonia nitrogen and the carbon layer required for the denitrification by microorganisms, and the relatively anaerobic soil layer coexist, and It must have a structure that can pass through both layers at a sufficient speed and can sufficiently contact and penetrate both layers. This determines not only the decomposition and purification of pollutants in wastewater, but also the nitrogen removal capacity in wastewater.

この相矛盾する条件を共に満足させうるものとして、本
発明者は通気性及び透水性に優れた土壌層(以下「透水
・好気性土壌層」と言う)と、通気性・透水性は劣るが
活性アルミニウムや生活鉄それに炭素源に富む土壌層
(以下「難透水・嫌気性土壌層」と言う)を組み合わし
た、多段土壌層法とでもいうべき理想的な土壌浄化方法
及び装置を開発した(特願昭60−52729号)。
The inventors of the present invention are able to satisfy both of these contradictory conditions, and the soil layer having excellent air permeability and water permeability (hereinafter referred to as "water permeable / aerobic soil layer") and the air permeability / water permeability are inferior. An ideal soil remediation method and device, which should be called a multi-stage soil layer method, has been developed that combines active aluminum, daily iron, and a soil layer rich in carbon sources (hereinafter referred to as "impermeable and anaerobic soil layer") ( Japanese Patent Application No. 60-52729).

第9図に示す装置(イ)はその一例で、マサ土からなる
被覆土壌層(2)中に配設した汚水撒水管(3)の下方
に、黒ボク土壌からなる難透水・嫌気性土壌集団(ロ)
…とマサ土からなる透水・好気性土壌集団(ハ)から構
成される層と、マサ土からなる透水・好気性土壌層
(ニ)を、交互に積み重ねた浄化層(ホ)を設けたもの
である。かくすると、汚水は下方に流下する間に難透水
・嫌気性土壌集団(ロ)に十分に接触・浸透する。その
他、難透水・嫌気性土壌層と水・好気性土壌層を階段状
に積み重ねる等種々な構造のものが考えられる。透水・
好気性土壌としてはその他ゼオライト等、難透水・嫌気
性土壌としては赤土等が用いられるが、これら各土壌の
種々とその組合せ、更には積層や充填構造を種々変える
ことにより、敷地面積や被処理汚水の量,性質に応じた
浄化装置を作ることができる。
The device (a) shown in FIG. 9 is an example of such a device. Below the sewage sprinkling pipe (3) arranged in a covered soil layer (2) made of masa soil, a non-permeable and anaerobic soil made of black soil is used. Group (b)
A layer comprising a permeable / aerobic soil group (C) consisting of Masa soil and a permeable / aerobic soil layer (D) consisting of Masa soil, provided with a purification layer (E) alternately stacked. Is. In this way, the sewage sufficiently contacts and infiltrates the hardly permeable / anaerobic soil group (b) while flowing down. In addition, various structures are possible such as stacking a poorly permeable / anaerobic soil layer and a water / aerobic soil layer in steps. Water permeability
Zeolites, etc. are used as aerobic soil, and red soil, etc. are used as poorly permeable and anaerobic soils. It is possible to make a purification device according to the amount and nature of wastewater.

〔従来技術の欠点〕[Disadvantages of conventional technology]

上記した多段土壌層法による装置の特徴は、換言すれば
設計通りに施工されていなければ所期の効果を発揮し難
いと言うことである。ところが、実際の施工に際しては
第9図の如く簡単な構造のものでも一つの水平な層の中
に各土壌集団(ロ)・(ハ)がモザイク状に組み込まれ
るため、施工に極めて手間がかかる。また層の厚みや面
積を設計通りに仕上げることは実際上困難であるし、締
め固めの程度によって層の厚みや透水性も変わる。しか
も、両種の土壌が混じり合った箇所では所定の効果が生
じない。
The feature of the above-mentioned apparatus based on the multi-stage soil layer method is that, in other words, it is difficult to exert the intended effect unless it is constructed as designed. However, in the actual construction, even if it has a simple structure as shown in Fig. 9, each soil group (b) and (c) is incorporated in a mosaic pattern in one horizontal layer, so the construction is extremely troublesome. . Further, it is practically difficult to finish the layer thickness and area as designed, and the layer thickness and water permeability also change depending on the degree of compaction. Moreover, the predetermined effect does not occur in the area where the soils of both species are mixed.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記に鑑みなされたもので、設計に合わせて一
つの層或いは集団を構成するに必要な量の土壌を、予め
透水性のある容器や袋体に詰めておき、これを並べたり
積み重ねることによって容易に多段土壌層法による汚水
浄化装置を施工することが出来るようにするものであ
る。
The present invention has been made in view of the above, and the amount of soil required to form one layer or group according to the design is packed in a water-permeable container or bag in advance, and these are arranged or stacked. This makes it possible to easily construct a sewage purification device by the multi-stage soil layer method.

そして、一つの考え方としては難透水・嫌気性土壌のみ
を容器や袋体に詰め、この一種の土壌ブロックを透水・
好気性土壌層の間に介在させて浄化層を形成させるもの
である。また他の考え方としては、難透水・嫌気性土壌
のブロックと透水・好気性土壌のブロックを適宜間隔を
置いて所定の位置に敷設・積層し、空隙はそのままにす
るか或いは透水・好気性土壌を充填することにより浄化
層を形成するものである。尚、これらの容器や袋体の素
材として炭素率(C/N比)の高いものを用いると、脱窒
が良好に行なわれる。
And one way of thinking is to pack only the hardly water-permeable / anaerobic soil into a container or bag, and to put this kind of soil block into the water-permeable / anaerobic soil.
It is interposed between aerobic soil layers to form a purification layer. Another approach is to lay / stack blocks of permeable / anaerobic soil and blocks of permeable / aerobic soil at predetermined positions with appropriate intervals, leaving the voids as they are or permeable / aerobic soil. To form a purification layer. If a material having a high carbon ratio (C / N ratio) is used as the material for these containers and bags, denitrification is favorably performed.

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 will be described in detail below based on the embodiments shown in the drawings.

〔構成〕〔Constitution〕

(第1の実施例) 第1図及び第2図は、本発明に係る汚水浄化装置の一例
を示す。この汚水浄化装置(1)は、第9図に示す装置
(イ)と同じ構造で、難透水・嫌気性土壌集団(ロ)…
の代わりに、透水性の袋体(4)に難透水・嫌気性土壌
(5)を詰めた土壌ブロック(6)…を用いたものであ
る。図示の装置(1)((イ)も同じ)は実用規模のも
ので、幅75cm,長さ150cm,深さ150cmの内法寸法の鉄製の
槽(7)の中に各土壌を収めたものである。そしてその
上部は汚水撒水管(3)を配設した被覆土壌層(2)、
中央部は浄化層(8)、下部は排水層(9)となってい
る。尚、被覆土壌層(2)でも硝化その他の反応が行な
われるが、主たる反応が中央部で行なわれるので本発明
では中央部を浄化層(8)と定義する。
(First Embodiment) FIGS. 1 and 2 show an example of a sewage purification apparatus according to the present invention. This sewage purification device (1) has the same structure as the device (a) shown in FIG. 9, and has a water-impermeable / anaerobic soil group (b) ...
Instead of the above, a soil block (6) in which a water-impermeable bag (4) is filled with hardly water-permeable / anaerobic soil (5) is used. The illustrated device (1) (same as (a)) is of a practical scale, and each soil is stored in an iron tank (7) of 75 cm in width, 150 cm in length, and 150 cm in depth with an inner size. Is. And the upper part thereof is a covered soil layer (2) provided with a drainage pipe (3),
The central part is a purification layer (8) and the lower part is a drainage layer (9). Incidentally, nitrification and other reactions also take place in the coated soil layer (2), but the main reaction takes place in the central part, so the central part is defined as the purification layer (8) in the present invention.

被覆土壌層(2)は、厚さ40cm程度の透水・好気性土壌
(マサ土)からなる。汚水撒水管(3)の周囲は礫層
(10)で囲まれ、礫層(10)の上面は目詰り防止用の網
状体(11),下面は汚水拡散用の隔板(12)で囲まれて
おり、全体としてトレンチ(13)を構成している。この
隔板(12)は汚水の分散を良好にするもので、プラスチ
ックやゴムの成型品や柔軟なシートが好適に用いられ
る。また排水層(9)は厚さ15cm程度の礫層(14)から
なり、底部に有孔の排水管(15)(コルゲート管等)を
配置する。礫層(14)の上面は網状体(16)で覆われ、
その上側は厚み5cm程度の砂層(17)を介して浄化層
(8)と接している。
The covered soil layer (2) consists of permeable and aerobic soil (masa soil) with a thickness of about 40 cm. The circumference of the water sprinkling pipe (3) is surrounded by a gravel layer (10), the upper surface of the gravel layer (10) is surrounded by a mesh body (11) for preventing clogging, and the lower surface is surrounded by a partition plate (12) for diffusing sewage. And constitutes the trench (13) as a whole. The partition plate (12) improves the dispersion of sewage, and a molded product of plastic or rubber or a flexible sheet is preferably used. The drainage layer (9) is composed of a gravel layer (14) having a thickness of about 15 cm, and a drainage pipe (15) (corrugated pipe, etc.) having a hole is arranged at the bottom. The upper surface of the gravel layer (14) is covered with the mesh body (16),
The upper side is in contact with the purification layer (8) through the sand layer (17) having a thickness of about 5 cm.

一方浄化層(8)は、土壌ブロック(6)と透水・好気
性土壌(18)とから構成される。土壌ブロック(6)は
15×30(及び20)×75cmサイズのジュート製袋体(4)
に22kg(及び15kg)の黒ボク土壌を充填したもので、こ
れを10cmの間隙をおいて並べる。そしてその間隙を透水
・好気性土壌(18)としてのマサ土で埋めて一つの層を
構成し、その上に厚さ10cm程度の透水・好気性土壌(1
8)としてマサ土の層を設ける。この各層(4層と3
層)を交互に配置して全体を約90cmとする。各層の土壌
ブロック(6)は、汚水が難透水・嫌気性土壌(5)に
十分接触浸透できるように10cmずつずらして設けてい
る。尚上記の各数字は一例であり、これらに限定される
ものではない。
On the other hand, the purification layer (8) is composed of the soil block (6) and the permeable / aerobic soil (18). Soil block (6)
15 x 30 (and 20) x 75 cm size jute bag (4)
Is filled with 22 kg (and 15 kg) of black soil, which are arranged with a 10 cm gap. Then, the gap is filled with Masa soil as permeable / aerobic soil (18) to form one layer, and the permeable / aerobic soil (1
8) As a layer of masa soil. Each of these layers (4 layers and 3
Layers) are staggered to make a total of about 90 cm. The soil blocks (6) of each layer are arranged 10 cm apart so that the sewage can sufficiently contact and permeate into the impermeable and anaerobic soil (5). It should be noted that each of the above numbers is an example, and the present invention is not limited to these.

(作用) しかして、汚水撒水管(3)から礫層(10)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作用を受ける。ま
たアンモニア態窒素も硝化細菌等の作用で硝化或いは亜
硝酸化されて、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 (10) and the covered soil layer (2) from the sewage sprinkling pipe (3) is caused by the digestive decomposition action of soil organisms and the adsorption and filtration action of soil, SS minutes, BOD and COD
It is subject to aerobic decomposition and removal of organic matter and other organic substances. Ammonia nitrogen is also nitrified or nitrated by the action of nitrifying bacteria and the like, and becomes treated water (B). This is the conventional soil purification method (capillary purification method).

この処理水(B)の一部は被覆土壌層(2)の表面から
蒸散するが、大部分はトレンチ(13)下方の浄化層
(8)に重力的に浸透流下する。この際、処理水(B)
は主として透水・好気性土壌(18)の部分を通りより酸
化的条件下に置かれる(実線矢印)。
A part of the treated water (B) evaporates from the surface of the coated soil layer (2), but most of the treated water (B) gravitationally permeates into the purification layer (8) below the trench (13). At this time, treated water (B)
Is placed under more oxidative conditions mainly through the permeable and aerobic soil (18) (solid arrow).

一方、透水・好気性土壌(18)の上下及び左右には土壌
ブロック(6)…が連なっている。この土壌ブロック
(6)の外壁となるジュート製袋体(4)は、単に黒ボ
ク土壌を充填するユニットを構成しているだけでなく、
それ自体マサ土と黒ボク土壌の界面に存在する網状体で
あり、両層の接触界面であらゆる方向に水の浸透・移動
を可能にしている。この袋体(4)は巨大な細胞壁にも
譬えることができ、処理水(B)はあたかも植物組織中
を自由に動くが如く、マサ土袋体(4)黒ボク土壌
と自由に浸透・移動する(点線矢印)。尚、ジュート製
袋体(4)は炭素率(C/N比)が極めて高い(通常50以
上)ので脱窒菌の炭素源ともなり、装置の脱窒活性を高
める働きもする。
On the other hand, soil blocks (6) are connected to the top, bottom, left and right of the permeable / aerobic soil (18). The jute bag (4) which is the outer wall of the soil block (6) not only constitutes a unit for filling black soil, but also
As such, it is a reticulate body that exists at the interface between Masa soil and Kuroboku soil, and allows water to permeate and move in all directions at the contact interface between both layers. This bag (4) can be compared to a huge cell wall, and the treated water (B) freely permeates into the Masa sand bag (4) Kuroboku soil as if it freely moves through the plant tissue. Move (dotted arrow). Since the jute bag (4) has an extremely high carbon ratio (C / N ratio) (usually 50 or more), it also serves as a carbon source for denitrifying bacteria and also serves to enhance the denitrifying activity of the device.

この程度で、処理水(B)中の燐酸(正及びポリ)は土
壌ブロック(6)中の黒ボク土壌に容易に吸着固定され
る。また処理水(B)中のNO2やNO3は、同じく黒ボク土
壌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。
At this degree, the phosphoric acid (positive and poly) in the treated water (B) is easily adsorbed and fixed to the black soil in the soil block (6). Further, NO 2 and NO 3 in the treated water (B) are also converted to N 2 and N 2 O by the action of denitrifying bacteria in the black soil, and are 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(15)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 (15).

(変形例) ところで、袋体(4)は透水性を考慮して目の粗い編織
物が好ましい。また素材はジュート(麻)に限らず、稲
藁やヤシ繊維その他C/N比の高い天然繊維質のもの好適
に用いられる。もっとも、プラスチックフイルムのスプ
リットヤーン等プラスチック製品も使用可能である。但
しその場合、好ましくは炭素源を充填土壌中に混入する
とよい。
(Modification) By the way, in consideration of water permeability, the bag body (4) is preferably a knitted woven fabric having coarse mesh. Further, the material is not limited to jute (linen), and rice straw, coconut fiber, and other natural fiber having a high C / N ratio are preferably used. However, plastic products such as split yarn of plastic film can also be used. However, in that case, it is preferable to mix the carbon source into the filled soil.

難透水・嫌気性土壌(5)としては、前記した黒ボク土
壌の他、赤黄色土壌、褐色・黄褐色森林土壌或いは灰色
低地土壌等、活性アルミニウムや活性鉄が1〜2重量%
(対乾土)以上ふくまれているものならば使用できる。
場合によっては、活性アルミニウム含量を高めるため
に、充填土壌に活性アルミニウム含有資材を混合して用
いてもよい。また炭素源として、木の葉その他の動植物
体、余剰活性汚泥等炭素率(C/N比)の高い物質を混入
しておいてもよい。
As the impervious water / anaerobic soil (5), in addition to the above black soil, red-yellow soil, brown / yellow-brown forest soil or gray lowland soil, etc., active aluminum or active iron is 1 to 2% by weight.
(Available for dry soil) You can use as long as it contains the above.
In some cases, in order to increase the active aluminum content, the soil filled with the active aluminum-containing material may be mixed and used. Further, as the carbon source, leaves and other animals and plants, surplus activated sludge, and other substances having a high carbon ratio (C / N ratio) may be mixed.

一方透水・好気性土壌(18)としては、マサ土の他砂丘
未熟土、粗粒火山灰土、粗粒褐色森林土或いは粗粒褐色
低地土壌等が用いられる。更に、ゼオライトも最も好ま
しいものの一つである。
On the other hand, as the permeable and aerobic soil (18), in addition to masa soil, immature sand dune soil, coarse volcanic ash soil, coarse brown forest soil or coarse brown lowland soil is used. Further, zeolite is one of the most preferable.

この透水・好気性土壌の主要な役割は、汚水を難透水・
嫌気性土壌の層(土壌ブロック(6))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
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、砂や礫、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を
混入してもよい。
The main role of this permeable and aerobic soil is
The purpose is to allow contact, diffusion, and permeation into the anaerobic soil layer (soil block (6)) as efficiently as possible, and prevent clogging of the device to allow rapid water permeation. In addition, mainly for this permeable and aerobic soil, SS content, BOD and
Aerobic decomposition, nitrification, and deodorization of COD and other organic substances are performed. Therefore, this soil is required to have high air permeability and high water permeability (for example, saturated water permeability coefficient higher than 10 -2 to 10 -3 cm / s). In some cases, sand, gravel, tree branches of appropriate size, artificial turf, or the like, which promote water permeability, may be mixed.

尚、一般に汚水(A)中の1価のNaイオン濃度は2価の
Caイオン濃度よりも高いため、長期間汚水を浸透処理す
ると土壌コロイドはNa型となって容易に分散し、土壌浄
化装置全体の不可逆的目詰りの大きな原因となる。そこ
で、汚水撒水管(3)の周囲等に粒径数cmの石灰石を充
填したり、その前段階で汚水中にCaイオンを添加させて
おくと、汚水(A)中のCa/Na比が高くなり、土壌コロ
イドがCa型となって安定な構造を保つ。
Generally, the concentration of monovalent Na ions in sewage (A) is divalent.
Since the concentration of Ca is higher than that of Ca ions, the soil colloid becomes Na type and easily disperses when the sewage is infiltrated for a long time, which is a major cause of irreversible clogging of the entire soil purification device. Therefore, when the limestone with a particle size of several cm is filled around the waste water sprinkling pipe (3) or Ca ions are added to the waste water at the previous stage, the Ca / Na ratio in the waste water (A) becomes It becomes higher and the soil colloid becomes Ca type and maintains a stable structure.

ところで、本発明装置による浄化の程度や処理可能量
は、透水・好気性土壌(18)と土壌ブロック(6)の役
割や配置状態、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。また、より実際的な装置の大きさ
特に巾と長さは、汚水の処理量,装置の構造,敷地面積
等により決まるが、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。槽(7)は底面を省略してもよく、またその素材
は他コンクリート,プラスチック,その他粘土や木材等
透水請求項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。
By the way, the degree of purification and the treatable amount by the device of the present invention vary depending on the roles and arrangement states of the permeable / aerobic soil (18) and the soil block (6), and also the type of soil used and the components contained therein. 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. Also, the more practical size of the equipment, especially the width and length, is determined by the amount of sewage treated, the structure of the equipment, the site area, etc., but the maximum width is 3 m and the length is about 20 m. It suffices if a large number of such devices are arranged in parallel. The bottom of the tank (7) may be omitted, and other materials such as concrete, plastic, clay, wood, etc. having a low water permeability claim may be used, and sometimes masonry or bedrock may be used.

(他の実施例) 第3図及び第4図に示す汚水浄化装置(1A)は、前記例
のものよりも小さい袋体(4)(8×25×75cmサイズ)
に10kgの黒ボク土壌を充填した土壌ブロック(6K)…を
約2cmの間隙をあけて並べた層(6層)と、同じく13kg
の赤色土壌を充填した土壌ブロック(6R)…を並べた層
(2層)を、上下2cmの間隙をあけて積層したものであ
る。赤色土壌は黒ボク土壌の代用品であり、この割合を
変えてもよく、いずれか一方のみにしてもよい。尚、偶
数段目の土壌ブロックは1/2ずつずらすため両端に黒ボ
ク土壌或いは赤色土壌を詰めている。
(Other Embodiments) The wastewater purifying apparatus (1A) shown in FIGS. 3 and 4 is a bag body (4) smaller than that of the above example (8 × 25 × 75 cm size).
A soil block (6K) filled with 10 kg of black soil (6 layers) with a gap of about 2 cm, and 13 kg
This is a layer (2 layers) in which soil blocks (6R) filled with red soil are lined up with a gap of 2 cm above and below. Red soil is a substitute for black soil, and this ratio may be changed or only one of them may be used. In addition, since the soil blocks in the even-numbered stages are shifted by 1/2, both ends are filled with black soil or red soil.

上記各間隙には、透水・好気性土壌(18)として粒径が
1〜3mmのゼオライト(クリノプチオライト)粒子が充
填されている。ゼオライト粒子は、本装置では目詰りを
防止し、処理水(B)の浸透・流下を助ける通水路の役
割をもっている。そして、使用するゼオライトの粒径や
ゼオライト層の厚みを変えることにより、処理水(B)
の透水性を制御できる。また、ゼオライトはアンモニウ
ムイオン保持能が大きいので、装置内における窒素の滞
留時間を長くする効果を持つ。更に、ゼオライトの大き
なCECは硝化に伴う処理水(B)のpH低下に対する緩衝
作用を持っており、装置内における微生物活動を保護す
る。またそれ自身が各微生物の住処となる。ゼオライト
はモルデナイト型のものでもよい。
Zeolite (clinoptiolite) particles having a particle diameter of 1 to 3 mm are filled in the gaps as the water-permeable / aerobic soil (18). In this device, the zeolite particles have a role of a water passage that prevents clogging and helps the permeation / flow of the treated water (B). Then, the treated water (B) is changed by changing the particle size of the zeolite used and the thickness of the zeolite layer.
The water permeability of the can be controlled. Further, since zeolite has a large ammonium ion retaining ability, it has an effect of prolonging the residence time of nitrogen in the apparatus. Further, the large CEC of zeolite has a buffering action against the pH drop of the treated water (B) due to nitrification, and protects the microbial activity in the device. In addition, it becomes a home for each microorganism. The zeolite may be of the mordenite type.

本装置(1A)では、第4図に示す如くあたかもジュート
製袋体(4)とゼオライトが黒ボク土壌(赤色土壌)を
二重に被覆した状態となっており、これらが有機的に作
用して、汚水中の有機性汚濁物質(BOD,COD,SS)の分解
作用だけでなく、燐や窒素分の浄化にも極めて優れた能
力を発揮する。尚、図中実線矢印は透水・好気性土壌
(18)中での処理水(B)の流れ、点線矢印は難透水・
嫌気性土壌(5)中での処理水(B)の流れを示す。
In this device (1A), as shown in Fig. 4, the jute bag (4) and the zeolite are in a state in which the black soil (red soil) is double-coated, and these act organically. In addition to its ability to decompose organic pollutants (BOD, COD, SS) in wastewater, it also has an extremely excellent ability to purify phosphorus and nitrogen. In the figure, the solid arrow indicates the flow of treated water (B) in the permeable / aerobic soil (18), and the dotted arrow indicates the impervious water.
The flow of the treated water (B) in anaerobic soil (5) is shown.

次に第5図に示す汚水浄化装置(1B)は、袋体(4)に
代えて透水性のある容器(19)を用いた例を示す。この
容器(19)は、第6図に示す如く底面(20)に透孔(2
1)…を多数設け、且つ上面を開口したトレー状の木箱
である。尚、ツマ面(22)の上部と両側方に夫々寸法a
とbの出っ張りを設け、多数積み重ねた場合間隙ができ
るようになっている。また透孔(21)…を大きくし、土
壌脱落防止用の網状体で塞ぐようにしてもよい。
Next, the sewage purification apparatus (1B) shown in FIG. 5 shows an example in which a water-permeable container (19) is used instead of the bag body (4). This container (19) has a through hole (2) on the bottom surface (20) as shown in FIG.
1) A tray-like wooden box with a large number of ... In addition, the dimension a on the upper side and both sides of the tab surface (22)
Protrusions b and b are provided so that a gap can be formed when a large number are stacked. Further, the through holes (21) may be enlarged and closed with a net-like body for preventing soil from falling off.

そしてこの容器(19)に、黒ボク土壌及び赤色土壌を充
填して難透水・嫌気性土壌ブロック(23K)・(23R)と
し、ゼオライト粒子を充填して透水・好気性土壌ブロッ
ク(23Z)とし、これらを図の如く敷き詰め積層して浄
化層(8)としたものである。そして、各土壌ブロック
(23)…間には上下方向にacm,長さ方向にbcmの間隙(2
4)ができ、この間隙(24)が処理水(B)や浄化水
(C)の通路となり且つ好気的雰囲気を与える。
And, this container (19) is filled with black soil and red soil to make a hardly permeable / anaerobic soil block (23K) / (23R), and it is filled with zeolite particles to make a permeable / aerobic soil block (23Z). The purification layer (8) is obtained by laying and stacking these as shown in the figure. And, between each soil block (23)…, a gap of acm in the vertical direction and bcm in the longitudinal direction (2
4) is formed, and the gap (24) serves as a passage for the treated water (B) and purified water (C) and gives an aerobic atmosphere.

本装置(1B)における黒ボク土壌(赤色土壌)の役割
は、前記装置(1A)と同じである。ただ本例では、ゼオ
ライトも土壌ブロック化されている点が異なる。従っ
て、全ての土壌がユニット化できるので工事の省力化,
規格化に役立つとともに、各土壌ブロック(23)間の間
隙を調整することにより汚水の流れを簡単に制御できる
特徴を有する。更に、炭素率の大きい木箱はジュート性
袋体(4)と同様にそれ自身が脱窒菌の炭素源となり、
効率的な窒素浄化能を実現する。
The role of the black soil (red soil) in this device (1B) is the same as that in the device (1A). However, in this example, the zeolite is also soil-blocked. Therefore, since all soil can be unitized, labor saving in construction,
It is useful for standardization and has a feature that the flow of sewage can be easily controlled by adjusting the gap between each soil block (23). In addition, the wooden box with a high carbon rate is itself a carbon source for denitrifying bacteria, similar to the jute bag (4).
Achieves efficient nitrogen purification capacity.

容器(19)は、木箱の他段ボール箱等微生物的な分解を
受けて炭素源を供給するものであれば何でもよい。容器
の形状や透孔の数,形状,位置も適宜選定すればよい。
なお、容器としてプラスチックの多孔性成型物も利用で
きる。但しその場合には充填土壌中に炭素源を別途混入
しておくことが好ましい。本装置(1B)の変形例として
は、ゼオライトの代わりにマサ土等他の透水・好気性土
壌(18)を用いること、間隙(24)を大きくしてここに
透水・好気性土壌(18)を充填すること等が考えられ
る。更に、図は省略するが袋体(4)に土壌を充填した
ものを上下間隙をあけて縦横に架設したパイプ等で支え
るようにして浄化層(4)を形成することも考えられ
る。
The container (19) may be a wooden box, a corrugated box, or any other source that supplies a carbon source by being subjected to microbial decomposition. The shape of the container and the number, shape and position of the through holes may be appropriately selected.
In addition, a plastic porous molding can be used as the container. However, in that case, it is preferable to separately mix a carbon source in the filled soil. As a modified example of this device (1B), other permeable / aerobic soil (18) such as masa soil is used in place of zeolite, and the gap (24) is enlarged to have permeable / aerobic soil (18) here. It is conceivable to fill the Further, although not shown, it is also possible to form the purification layer (4) by supporting a bag (4) filled with soil with a pipe or the like installed vertically and horizontally with a vertical gap.

以上は、汚水供給源として被覆土壌層(2)中に汚水撒
水管(3)を配設したものについて述べたが、本発明は
第8図の如く汚水槽(25)の場合にも当然に用いられ
る。この場合、汚水槽(25)の開口部周縁及びその下方
に上記した如き浄化層(8)を展開させるとよい。また
汚水撒水管(3)を用いる場合でもその側方や上方に浄
化層(8)を配置してもよい。
The above has described the case where the waste water sprinkling pipe (3) is arranged in the covered soil layer (2) as a waste water supply source, but the present invention is naturally applicable to the waste water tank (25) as shown in FIG. Used. In this case, the purification layer (8) as described above may be spread around and around the opening of the dirty water tank (25). Further, even when using the sewage sprinkling pipe (3), the purification layer (8) may be arranged on the side or the upper side thereof.

尚、汚水供給の方式や浄化層(4)の上方部分の構造等
はその他種々考えられるが、要は処理水(B)を効率浴
浄化層(4)に供給するものであれば良い。或いは、浄
化層(4)自体にマサ土の層を多くし、ここで硝化反応
も行わせるようにすることも考えられる。
Although there are various other conceivable methods of supplying the sewage and the structure of the upper portion of the purification layer (4), the point is that the treated water (B) is supplied to the efficiency bath purification layer (4). Alternatively, it is conceivable to increase the layer of masa soil in the purification layer (4) itself so that the nitrification reaction also takes place there.

(従来の土壌浄化装置との比較) 次に、本発明装置と従来の単なる多段土壌層法により装
置による汚水浄化能を比較した結果を表1に示す。
(Comparison with Conventional Soil Purifying Device) Next, Table 1 shows the results of comparing the sewage purification performance of the device of the present invention with the conventional simple multi-stage soil layer method.

尚、表中本発明装置(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、実施例3が第5図に示す構造のものである。また従
来の多段式装置(比較例)は第9図に示す構造のもので
ある。これら各装置に用いたマサ土及び黒ボク土壌中の
活性アルミニウム及び活性鉄の含量(乾土重量基準)
は、夫々0.1と0.3%,5.6と0.6%であった。
In the table, the device of the present invention (embodiment) means that the embodiment 1 has the structure shown in FIG. 1, the embodiment 2 has the structure shown in FIG. 3, and the embodiment 3 has the structure shown in FIG. belongs to. A conventional multistage device (comparative example) has a structure shown in FIG. Content of active aluminum and active iron in Masa soil and Kuroboku soil used for each of these devices (based on dry soil weight)
Were 0.1 and 0.3%, 5.6 and 0.6%, respectively.

比較例装置も、多段土壌層構造を有し表から判るように
高度の浄化能を有するが、実施例の装置は何れも実用上
十分な処理可能容量(l/m2・日)を有し、且つ浄化能も
比較例と同等かそれ以上の能力を示している。特に実施
例2に示すものは窒素浄化能が極めて高く、その他BOD
等の浄化能も高く優れたものと言うことができる。
The comparative device also has a multi-stage soil layer structure and has a high degree of purification as can be seen from the table, but all the devices of the examples have a practically sufficient treatable capacity (l / m 2 · day). Moreover, the purifying ability is equal to or higher than that of the comparative example. In particular, the one shown in Example 2 has an extremely high nitrogen purifying ability, and other BOD
It can be said that it has excellent purifying ability and is excellent.

一方、略同様な構造である第1図の装置(実施例1)と
第9図に示す多段式の従来装置(比較例)を施工するに
要する時間は、夫々約2日と4日であり、本発明装置の
場合効率が約2倍以上も向上する。この差は大型化した
実際の装置ではより大きくなり、構造が複雑な場合その
差はより開く。また、本発明の場合容易に設計通りのも
のが施工でき、期待通りの効果を発揮する。
On the other hand, the time required for constructing the apparatus of FIG. 1 (Example 1) and the conventional multi-stage apparatus (Comparative Example) shown in FIG. 9 having substantially the same structure is about 2 days and 4 days, respectively. In the case of the device of the present invention, the efficiency is improved about twice or more. This difference becomes larger in a large-scale actual device, and the difference becomes larger when the structure is complicated. Further, in the case of the present invention, the work as designed can be easily performed, and the expected effect is exhibited.

〔効果〕 以上詳述したように、本発明は難透水・嫌気性土壌と透
水・好気性土壌の層或いは集団を積層した多段土壌層法
による汚水浄化装置を施工するに際し、難透水・嫌気性
土壌更には透水・好気性土壌の一定量を透水性に優れた
袋体或いは容器に充填して一種のブロック化し、この土
壌ブロックを敷設・集積するものである。
[Effect] As described in detail above, the present invention is difficult to permeable to water and anaerobic when constructing a sewage purification device by a multi-stage soil layer method in which layers or groups of hardly permeable / anaerobic soil and permeable / aerobic soil are laminated A certain amount of soil or water-permeable / aerobic soil is filled in a bag or container having excellent water permeability to form a kind of block, and this soil block is laid and accumulated.

従って本発明によれば、構造の複雑な多段土壌層式の汚
水浄化装置が設計通り正確に作れ、その機能を十分発揮
せしめることができるとともに規格化ができて施工に手
間がかからず施工コストの低減化が図れる。また、土壌
ブロックを作る袋体や容器に炭素率の高いものを用いる
と、脱窒反応が顕著に行なわれる等、経済的・技術的な
面で種々な利点を有するものである。
Therefore, according to the present invention, a multi-stage soil layer type sewage purification device having a complicated structure can be accurately manufactured as designed, and its function can be fully exerted and standardization can be performed without labor and construction cost. Can be reduced. Further, if a bag or a container for forming a soil block having a high carbon content is used, it has various advantages in economic and technical aspects such as a remarkable denitrification reaction.

【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、第3図は他の実施例を示
す縦断面図、第4図は第3図の部分拡大図、第5図は更
に他の例を示す汚水浄化装置の縦断面図、第6図は第5
図の装置に用いる透水性容器の斜視図、第7図は第5図
の部分拡大図、第8図は汚水供給源が異なる他の例を示
す汚水浄化装置の縦断面図、第9図は従来例を示す縦断
面図である。 1・1A・1B……汚水浄化装置 2……被覆土壌層 3……汚水撒水管 4……袋体 5……難透水・嫌気性土壌 6・6K・6R……土壌ブロック 8……浄化層 9……排水層 13……トレンチ 15……排水管 18……透水・好気性土壌 19……容器 23K.23R.23Z……土壌ブロック 24……間隙 25……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, FIG. 2 is a transverse sectional view showing the same, FIG. 3 is a longitudinal sectional view showing another embodiment, and FIG. FIG. 5 is a partially enlarged view, FIG. 5 is a vertical cross-sectional view of a sewage purification device showing still another example, and FIG.
FIG. 7 is a perspective view of a water-permeable container used in the apparatus of FIG. 7, FIG. 7 is a partially enlarged view of FIG. 5, FIG. 8 is a vertical cross-sectional view of a wastewater purification apparatus showing another example in which wastewater supply sources are different, It is a longitudinal cross-sectional view showing a conventional example. 1.1A ・ 1B …… Sewage purification device 2 …… Coated soil layer 3 …… Sewage sprinkling pipe 4 …… Bag 5 …… Impermeable water / anaerobic soil 6.6K ・ 6R …… Soil block 8 …… Purification layer 9 …… Drainage layer 13 …… Trench 15 …… Drain pipe 18 …… Permeable / aerobic soil 19 …… Container 23K.23R.23Z …… Soil block 24 …… Gap 25 …… Sewage tank A …… Sewage B… … Treated water C… Purified water

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】通気性及び透水性は劣るが活性アルミニウ
ム乃至活性鉄に富む土壌を透水性のある容器や袋体に詰
めたものを、間に通気性及び透水性に優れた土壌層を介
して積み重ねた浄化層を備えたことを特徴とする汚水浄
化装置。
1. A container or a bag having water permeability, which is poor in air permeability and water permeability but is rich in activated aluminum or iron, is filled with a soil layer having excellent air permeability and water permeability. A sewage purification device characterized by having a purification layer that has been stacked.
【請求項2】炭素率の高い素材で作られた容器或いは袋
体を用いるものである特許請求の範囲第1項記載の汚水
浄化装置。
2. The sewage purification device according to claim 1, which uses a container or a bag made of a material having a high carbon rate.
【請求項3】通気性及び透水性に優れた土壌を詰めた透
水性の容器や袋体と、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に富む土壌を詰めた透水性の容器
や袋体を、周囲に空隙を設けた状態で層状、段階状に積
み重ねた浄化層を備えたことを特徴とする汚水浄化装
置。
3. A water-permeable container or bag filled with soil having excellent air permeability and water permeability, and a water-permeable container filled with soil having poor air permeability and water permeability but rich in active aluminum or iron. A sewage purification device comprising a purification layer in which a bag body is stacked in layers and in a stepwise manner with a space provided around the bag body.
【請求項4】周囲の空隙に、通気性及び透水性に優れた
土壌を充填してなる特許請求の範囲第3項記載の汚水浄
化装置。
4. The sewage purification device according to claim 3, wherein the surrounding voids are filled with soil having excellent air permeability and water permeability.
【請求項5】炭素率の高い素材で作られた容器或いは袋
体を用いるものである特許請求の範囲第3項記載の汚水
浄化装置。
5. The sewage purification device according to claim 3, which uses a container or a bag made of a material having a high carbon rate.
JP1073086A 1986-01-20 1986-01-20 Sewage purification device Expired - Lifetime JPH0741251B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1073086A JPH0741251B2 (en) 1986-01-20 1986-01-20 Sewage purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1073086A JPH0741251B2 (en) 1986-01-20 1986-01-20 Sewage purification device

Publications (2)

Publication Number Publication Date
JPS63240991A JPS63240991A (en) 1988-10-06
JPH0741251B2 true JPH0741251B2 (en) 1995-05-10

Family

ID=11758407

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1073086A Expired - Lifetime JPH0741251B2 (en) 1986-01-20 1986-01-20 Sewage purification device

Country Status (1)

Country Link
JP (1) JPH0741251B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019181465A (en) * 2018-03-30 2019-10-24 孝洋 新井 Sewage treatment apparatus

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100804782B1 (en) 2007-01-12 2008-02-20 주식회사 네이코스엔지니어링 Sewage purification device using soil
KR101443953B1 (en) * 2008-04-16 2014-09-29 윌리엄 루카스 Bioretention system and method
KR101163061B1 (en) * 2009-11-02 2012-07-05 한국과학기술연구원 Equipment and method for water and stream purification using layered soil system
CN108689551B (en) * 2018-06-12 2023-11-24 上海交通大学 Two-section rural domestic sewage treatment system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019181465A (en) * 2018-03-30 2019-10-24 孝洋 新井 Sewage treatment apparatus

Also Published As

Publication number Publication date
JPS63240991A (en) 1988-10-06

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