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JP3836682B2 - Wastewater purification system - Google Patents
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JP3836682B2 - Wastewater purification system - Google Patents

Wastewater purification system Download PDF

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Publication number
JP3836682B2
JP3836682B2 JP2001031554A JP2001031554A JP3836682B2 JP 3836682 B2 JP3836682 B2 JP 3836682B2 JP 2001031554 A JP2001031554 A JP 2001031554A JP 2001031554 A JP2001031554 A JP 2001031554A JP 3836682 B2 JP3836682 B2 JP 3836682B2
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Prior art keywords
water
tank
fine particles
waste water
purification system
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JP2002233888A (en
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利洋 高橋
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青木電器工業株式会社
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Priority to KR10-2002-0006403A priority patent/KR100433303B1/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Activated Sludge Processes (AREA)
  • Biological Treatment Of Waste Water (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、農業集落排水等の有機性排水を浄化するシステムに関する。
【0002】
【従来の技術】
特公平5−10999号公報には、この種の浄化システムと、このシステムに附随する種汚泥の簡易製造装置とが開示されている。この簡易製造装置は、外筐体と内筒体とを有し、内筒体には腐植物質を含むペレットが充填され、外筐体には浄化処理システムからの有機性排水の一部が導かれる。導かれた有機性排水は、内筒体を下から上へと通り抜けるようにして外筐体の内部を循環し、循環する間にペレットと接触し、その接触を通じて排水の浄化に役立つ土壌細菌群の増殖と代謝機能の活性化とが促進される。このような細菌群を含む有機性排水は種汚泥として取り出され、浄化システムへ返送される。浄化システムとこの簡易製造装置との間でこのように排水の一部をやりとりすることによって、浄化システムにおける細菌群を常に活性化した状態に維持することができる。
【0003】
【発明が解決しようとする課題】
前記公知のシステムにおける種汚泥の簡易製造装置では、腐植物質を含むペレットが内筒体の内部で互いに密に接触しているから、多量のペレットを使用してもペレットと排水との接触面積はそれほど増加しない。特に、簡易製造装置の運転が長期に及ぶとペレットは細粒となって内筒体に高密度で充填された状態になるから、ペレットと排水とが広い面積で接触することは一層困難になる。このような状態の内筒体は、それを外筐体から取り出して使用済みのペレットを廃棄し、新規のものを充填しなければならず、ペレットを無駄にすることが多い。そればかりではなく、内筒体の取り出しにはクレーン等の重機を使用しなければならず、ペレットを交換するたびに多大の費用と時間とが必要になる。
【0004】
この発明は、有機性排水の浄化システムにおいて、腐植物質と排水との広い面積での接触を可能にするとともに腐植物質の交換を不要にして、前記公知技術に見られるような諸問題の解消を課題にしている。
【0005】
【課題を解決するための手段】
前記課題解決のために、この発明が対象とするのは、有機性排水を土壌細菌の作用で浄化するシステムに前記排水の一部を前記システムから取り出して腐植物質と接触させ,しかる後に前記排水の一部を前記システムへ返送する工程が付随する排水浄化システムである。
【0006】
かかる排水浄化システムにおいて、この発明が特徴とするところは、次のとおりである。前記腐植物質が無機物質を含む微細粒子であって、前記微細粒子の量が0.05〜3重量%の範囲にある水との混合物の形態で前記供給手段により連続的および間欠的のいずれかの態様で供給され、前記供給手段は、前記微細粒子と水とを混合することができる攪拌機付きの混合槽と、前記混合槽へ前記微細粒子を連続的および間欠的のいずれかの態様で投入可能なホッパーと、前記微細粒子と水との混合物を前記貯水槽へ送る輸送手段とを備え、前記混合物は、前記貯水槽で処理する1日当たりの前記排水の量の0.5/1000〜5/1000を前記排水に添加して前記システムへ返送し、前記混合槽の容積が前記貯水槽の容積の0.5〜1%である。
【0007】
【発明の実施の形態】
添付の図面を参照して、この発明に係る排水浄化システムの詳細を説明すると、以下のとおりである。
【0008】
図1は、排水浄化システムの一例を示すフローチャートである。この排水浄化システムでは、図の左方から農業集落排水等の有機性排水1が調整槽2へ供給され、排水1はさらに反応槽3、分離槽4へと進み、分離槽4では浄化された排水1が分離されて処理水6となって外へ出るとともに、分離槽4における排水1の一部を必要に応じて調整槽2や反応槽3へ返送することができるというシステムを有し、このシステムには、分離槽4の排水1の一部である排水12を、必要なら分離槽4の汚泥とともに、培養槽7へ導く工程が付随している。培養槽7には、これに並置された腐植物質供給装置8から腐植物質を微細粒子の形態で含む第1混合水31(図2参照)が供給される。培養槽7からは、排水12が土壌細菌を多量に含む第2混合水32となって調整槽2や反応槽3に返送される。この第2混合水32には汚泥の含まれることがある。調整槽2は前処理槽と呼ばれることがあり、反応槽3は処理槽とかばっ気槽とか呼ばれ、分離槽4は沈殿槽と呼ばれることがある。これらの貯水槽には、当該技術分野において周知慣用のものを使用することができる。
【0009】
図2は、図1における培養槽7と供給槽8との断面図である。培養槽7には、分離槽4からの排水12と供給槽8からの第1混合水31とが供給される。培養槽7は、散気管14と第1送水管16とを有し、散気管14からの給気による好気的条件下で排水12と第1混合水31とを混合する。
【0010】
供給装置8は、給水装置20、ホッパー22、モータ23によって駆動される攪拌機24および培養槽7へつながる第2送水管26とを有し、第2送水管26には送水ポンプ27が取り付けられている。給水装置20は給水槽等であって、ここからは、培養槽7の排水12と混合して土壌細菌を増殖させるのに適した混合用の水21が連続的または間欠的に供給される。混合用の水21の一例には、図1の処理水6がある。ホッパー22には、腐植物質と無機物質を主成分とする微細粒子30が投入されており、フィーダ25を介して連続的または間欠的にこの微細粒子30が供給槽8へ送られる。水21と微細粒子30とは攪拌機24によって混合されて第1混合水31となり、ポンプ27によって培養槽7へ送られる。
【0011】
培養槽7では、散気管14の作用により第1混合水31と排水12とが微細粒子30とともに好気的条件で混合攪拌されて第2混合水32となる。第2混合水32では、かかる攪拌の下にその中に含まれる土壌細菌の増殖と代謝機能の活性化とが促進され、図1の排水1に対する浄化能力が向上する。この第2混合水32は、第1送水管16を通り調整槽2および/または反応槽3に返送される。
【0012】
かような供給装置8において、微細粒子30には、腐植物質と無機物質との混合物からなり、好ましくは50メッシュ以上の粒度を有するものが使用される。無機物質には、好ましくは鉱物粒子、より好ましくは珪酸塩を含む鉱物粒子、さらに好ましくは軽石、安山岩、流紋岩、火山ガラス、ゼオライト、グリーンタフ、珪藻土、粘土鉱物等の珪酸塩を含む鉱物粒子が使用される。微細粒子30において、無機物質は50〜90重量%を占め、腐食物質を主成分とする有機物が残余の部分を占めている。微細粒子30の使用量は、第1混合水31において0.05〜3重量%の範囲にあることが好ましい。また、第1混合水31は、培養槽7で処理する1日当たりの排水12の量の0.5/1000〜5/1000程度をポンプ27によって連続的または間欠的に排水12に添加することが好ましい。このように第1混合水31の使用量は、排水12の量に比して非常に少ないから、供給槽8の内容積は、通常であれば培養槽7の内容積の0.5〜1%で足りる。ただし、図2では供給槽8の構造を明示するために、供給槽8が培養槽7と同程度の大きさで示されている。また、培養槽7は、従来技術のうように腐植物質のペレットを充填するための容器を内蔵する必要がないから、内容積の小さいもので足りる。
【0013】
図3は、供給装置8から培養槽7への微細粒子30を含む第1混合水31の供給パターンと、培養槽7から調整槽2および/または反応槽3への第2混合水32の返送パターンとを例示する図面である。図3の(a)は、第1混合水31が培養槽7へ間欠的に供給され、その供給と供給との間において培養槽7から調整槽2および/または反応槽3へと第2混合水32が返送される。第2混合水32には、汚泥が含まれることもある。(a)の例は、第1混合水31の供給と第2混合水32の返送とが間欠的であって、一般にBOD値の高い食品関係や畜産関係の排水浄化に適している。また、図3の(b)は、第1混合水31が間欠的に供給される一方、培養槽7からは第2混合水32が連続的に返送される。(b)の例は、BOD値が比較的低い生活排水の浄化に適している。
【0014】
図4は、図1の培養槽7と供給槽8とが一体となって培養槽47を形成している場合の浄化システムの部分図である。培養槽47は、散気管14、送水管16、ホッパー22、攪拌機24を有し、分離槽4からは排水12が供給される。排水12は、汚泥を含む場合がある。ホッパー22からは、フィーダ25を介して微細粒子30が供給される。排水12と微細粒子30とは好気的条件下に混合されて、土壌細菌の増殖と代謝機能の活性化とが促進された第3混合水53となり、第1送水管16から調整槽2等へ返送される。この第1送水管16には、第3混合水53を間欠的に返送することができるように、ポンプ57が取り付けられている。この態様の培養槽47もまた、従来技術のように腐植物質のペレットを充填するための容器を内蔵する必要がない。
【0015】
排水12と腐植物質30とを混合して土壌細菌の増殖と活性化とを図る工程が附随するこの発明の排水浄化システムは、図1に例示の態様の他に、調整槽2や反応槽3、分離槽4のいずれかが複数の槽からなる態様、調整槽2と反応槽3とが一体化している態様、調整槽2や反応槽3、分離槽4に加えてその他の目的の貯水槽を有する態様等で実施することが可能である。
【0016】
【発明の効果】
この発明に係る排水浄化システムには、排水の一部を腐植物質と接触させる工程が附随しており、その工程は、培養槽である比較的小さな貯水槽と、この貯水槽への腐植物質の供給手段と、排水の返送手段とによって形成されているから、その工程を設けることと、その工程を維持管理することとには、例えばクレーン等の重機を必要としないから費用が嵩むということがない。この工程では、腐植物質が50メッシュ以上の微細粒子の状態で使用されるから、腐植物質と排水との広い面積での接触が可能になるとともに、土壌細菌の速やかな増殖と代謝機能の活性化とが可能になる。腐植物質は、排水浄化システムを循環しながら消費されるから、従来のような腐植物質の交換が不要であり、かつ、腐植物質を無駄にすることがない。
【図面の簡単な説明】
【図1】 排水浄化システムのフローチャート。
【図2】 培養槽と腐植物質供給装置の断面図。
【図3】 培養槽の運転態様を例示する図面。
【図4】 実施態様の一例を示す培養槽の断面図。
【符号の説明】
1 排水
7 貯水槽(培養槽)
8 供給手段混合槽(腐植物質供給装置)
12 排水
16 返送手段(第1送水管)
22 供給手段(ホッパー)
24 攪拌機
26 輸送手段(第2送水管)
30 微細粒子
31 混合物(第1混合水)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a system for purifying organic wastewater such as agricultural settlement wastewater.
[0002]
[Prior art]
Japanese Examined Patent Publication No. 5-10999 discloses a purification system of this kind and a simple production apparatus for seed sludge attached to this system. This simple manufacturing apparatus has an outer casing and an inner cylinder, the inner cylinder is filled with pellets containing humic substances, and a part of the organic waste water from the purification system is introduced into the outer casing. It is burned. The guided organic wastewater circulates inside the outer casing as it passes from the bottom to the top of the inner cylinder, contacts the pellets during circulation, and the soil bacteria that help purify the wastewater through the contact Growth and activation of metabolic function are promoted. Organic wastewater containing such bacteria is taken out as seed sludge and returned to the purification system. By exchanging a part of the waste water between the purification system and the simplified manufacturing apparatus in this way, the bacteria group in the purification system can always be maintained in an activated state.
[0003]
[Problems to be solved by the invention]
In the simple seed sludge production apparatus in the known system, since the pellets containing humic substances are in close contact with each other inside the inner cylinder, the contact area between the pellet and the drainage is large even if a large amount of pellets are used. Does not increase so much. In particular, when the operation of the simple manufacturing apparatus is extended for a long period, the pellets become fine particles and are filled in the inner cylinder body at a high density, so that it becomes more difficult for the pellets and the drainage to contact in a wide area. . The inner cylinder in such a state must be taken out of the outer casing, discarded used pellets and filled with new ones, and the pellets are often wasted. In addition, a heavy machine such as a crane must be used to take out the inner cylinder, and a great deal of cost and time are required each time the pellets are replaced.
[0004]
The present invention provides an organic wastewater purification system that enables contact between humic substances and wastewater over a wide area and eliminates the need for exchange of humic substances, thereby solving various problems such as those found in the above-mentioned known technology. It is an issue.
[0005]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention is directed to a system for purifying organic wastewater by the action of soil bacteria, taking a part of the wastewater from the system and bringing it into contact with humic substances, and then the wastewater. Is a wastewater purification system accompanied by a step of returning a part of the system to the system.
[0006]
In this waste water purification system, the present invention is characterized as follows. The humic substance is fine particles containing an inorganic substance, and the amount of the fine particles is in the form of a mixture with water in the range of 0.05 to 3% by weight , either continuously or intermittently by the supply means The supply means is a mixing tank with a stirrer capable of mixing the fine particles and water, and the fine particles are charged into the mixing tank either continuously or intermittently. A possible hopper and transport means for sending the mixture of fine particles and water to the reservoir, the mixture being 0.5 / 1000-5 of the amount of the wastewater per day to be treated in the reservoir / 1000 is added to the waste water and returned to the system, and the volume of the mixing tank is 0.5-1% of the volume of the water tank.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
The details of the waste water purification system according to the present invention will be described with reference to the accompanying drawings.
[0008]
FIG. 1 is a flowchart showing an example of a wastewater purification system. In this waste water purification system, organic waste water 1 such as agricultural settlement waste water is supplied to the adjustment tank 2 from the left side of the figure, and the waste water 1 further proceeds to the reaction tank 3 and the separation tank 4 and purified in the separation tank 4. The waste water 1 is separated and goes out as treated water 6 and has a system that can return part of the waste water 1 in the separation tank 4 to the adjustment tank 2 and the reaction tank 3 as necessary. This system is accompanied by a step of leading the waste water 12 which is a part of the waste water 1 of the separation tank 4 to the culture tank 7 together with the sludge of the separation tank 4 if necessary. The culture tank 7 is supplied with a first mixed water 31 (see FIG. 2) containing humic substances in the form of fine particles from a humic substance supply device 8 juxtaposed thereto. From the culture tank 7, the drainage 12 becomes the second mixed water 32 containing a large amount of soil bacteria and is returned to the adjustment tank 2 and the reaction tank 3. The second mixed water 32 may contain sludge. The adjustment tank 2 may be referred to as a pretreatment tank, the reaction tank 3 may be referred to as a treatment tank or an aeration tank, and the separation tank 4 may be referred to as a precipitation tank. As these water tanks, those commonly used in the art can be used.
[0009]
FIG. 2 is a cross-sectional view of the culture tank 7 and the supply tank 8 in FIG. The culture tank 7 is supplied with the waste water 12 from the separation tank 4 and the first mixed water 31 from the supply tank 8. The culture tank 7 has a diffuser pipe 14 and a first water supply pipe 16, and mixes the waste water 12 and the first mixed water 31 under aerobic conditions by supplying air from the diffuser pipe 14.
[0010]
The supply device 8 has a water supply device 20, a hopper 22, a stirrer 24 driven by a motor 23, and a second water supply pipe 26 connected to the culture tank 7. A water supply pump 27 is attached to the second water supply pipe 26. Yes. The water supply device 20 is a water supply tank or the like, and from here, water 21 for mixing suitable for mixing with the waste water 12 of the culture tank 7 to grow soil bacteria is supplied continuously or intermittently. An example of the mixing water 21 is the treated water 6 of FIG. Fine particles 30 mainly composed of humic substances and inorganic substances are introduced into the hopper 22, and the fine particles 30 are sent to the supply tank 8 continuously or intermittently via the feeder 25. The water 21 and the fine particles 30 are mixed by the stirrer 24 to become the first mixed water 31 and sent to the culture tank 7 by the pump 27.
[0011]
In the culture tank 7, the first mixed water 31 and the drainage 12 are mixed and agitated under the aerobic condition together with the fine particles 30 by the action of the air diffuser 14 to become the second mixed water 32. In the second mixed water 32, the growth of soil bacteria contained therein and the activation of the metabolic function are promoted under such agitation, and the purification capacity for the waste water 1 in FIG. 1 is improved. The second mixed water 32 is returned to the adjustment tank 2 and / or the reaction tank 3 through the first water supply pipe 16.
[0012]
In such a supply apparatus 8, the fine particles 30 are made of a mixture of humic substances and inorganic substances, and preferably have a particle size of 50 mesh or more. The inorganic substance is preferably a mineral particle, more preferably a mineral particle containing silicate, more preferably a mineral containing a silicate such as pumice, andesite, rhyolite, volcanic glass, zeolite, green tough, diatomaceous earth, clay mineral, etc. Particles are used. In the fine particles 30, the inorganic substance occupies 50 to 90% by weight, and the organic substance mainly composed of the corrosive substance occupies the remaining part. The amount of the fine particles 30 used is preferably in the range of 0.05 to 3% by weight in the first mixed water 31. In addition, the first mixed water 31 may be added to the waste water 12 continuously or intermittently by the pump 27 about 0.5 / 1000 to 5/1000 of the amount of the daily waste water 12 to be treated in the culture tank 7. preferable. Thus, since the usage-amount of the 1st mixing water 31 is very small compared with the quantity of the waste_water | drain 12, the internal volume of the supply tank 8 is 0.5-1 of the internal volume of the culture tank 7, if normal. % Is enough. However, in FIG. 2, the supply tank 8 is shown in the same size as the culture tank 7 in order to clearly show the structure of the supply tank 8. Further, the culture tank 7 does not need to contain a container for filling humic pellets as in the prior art, so a small internal volume is sufficient.
[0013]
FIG. 3 shows the supply pattern of the first mixed water 31 containing fine particles 30 from the supply device 8 to the culture tank 7 and the return of the second mixed water 32 from the culture tank 7 to the adjustment tank 2 and / or the reaction tank 3. It is drawing which illustrates a pattern. In FIG. 3A, the first mixed water 31 is intermittently supplied to the culture tank 7, and the second mixing is performed from the culture tank 7 to the adjustment tank 2 and / or the reaction tank 3 between the supply. Water 32 is returned. The second mixed water 32 may contain sludge. In the example of (a), the supply of the first mixed water 31 and the return of the second mixed water 32 are intermittent, and it is generally suitable for food-related or livestock-related wastewater purification with a high BOD value. In FIG. 3B, the first mixed water 31 is intermittently supplied, while the second mixed water 32 is continuously returned from the culture tank 7. The example of (b) is suitable for purification of domestic wastewater having a relatively low BOD value.
[0014]
FIG. 4 is a partial view of the purification system when the culture tank 7 and the supply tank 8 of FIG. 1 are integrated to form a culture tank 47. The culture tank 47 includes a diffuser pipe 14, a water supply pipe 16, a hopper 22, and a stirrer 24, and drainage 12 is supplied from the separation tank 4. The drainage 12 may contain sludge. Fine particles 30 are supplied from the hopper 22 through the feeder 25. The waste water 12 and the fine particles 30 are mixed under an aerobic condition to become the third mixed water 53 in which the growth of soil bacteria and the activation of the metabolic function are promoted. From the first water pipe 16 to the adjusting tank 2 and the like Will be returned to. A pump 57 is attached to the first water supply pipe 16 so that the third mixed water 53 can be returned intermittently. The culture tank 47 of this embodiment also does not need to contain a container for filling humic pellets as in the prior art.
[0015]
The waste water purification system according to the present invention, which is accompanied by a step of mixing the waste water 12 and the humic substance 30 to promote the growth and activation of soil bacteria, is not limited to the embodiment illustrated in FIG. A mode in which any one of the separation tanks 4 is composed of a plurality of tanks, a mode in which the adjustment tank 2 and the reaction tank 3 are integrated, a water tank for other purposes in addition to the adjustment tank 2, the reaction tank 3, and the separation tank 4 It is possible to implement in the aspect etc. which have.
[0016]
【The invention's effect】
The wastewater purification system according to the present invention is accompanied by a step of bringing a part of the wastewater into contact with the humic substance, and the step includes a relatively small water tank as a culture tank and the humic substance in the water tank. Since it is formed by the supply means and the return means for drainage, providing the process and maintaining the process does not require heavy equipment such as a crane, for example. Absent. In this process, since the humic substance is used in the form of fine particles of 50 mesh or more, it is possible to contact the humic substance and the wastewater over a wide area, and the soil bacteria can rapidly grow and activate the metabolic function. And become possible. Since the humic substance is consumed while circulating through the waste water purification system, it is not necessary to replace the humic substance as in the prior art, and the humic substance is not wasted.
[Brief description of the drawings]
FIG. 1 is a flowchart of a wastewater purification system.
FIG. 2 is a cross-sectional view of a culture tank and a humic substance supply apparatus.
FIG. 3 is a diagram illustrating an operation mode of a culture tank.
FIG. 4 is a cross-sectional view of a culture tank showing an example of an embodiment.
[Explanation of symbols]
1 Drainage 7 Water storage tank (culture tank)
8 Supply means mixing tank (humic substance supply device)
12 Drainage 16 Return means (first water pipe)
22 Supply means (hopper)
24 Stirrer 26 Transport means (second water pipe)
30 Fine particles 31 Mixture (first mixed water)

Claims (6)

有機性排水を土壌細菌の作用で浄化するシステムに前記排水の一部を前記システムから取り出して腐植物質と接触させ、しかる後に前記排水の一部を前記システムへ返送する工程が付随する排水浄化システムにおいて、
前記工程が前記システムから取り出された前記排水の一部を流入させる貯水槽と、前記貯水槽への前記腐植物質の供給手段と、前記貯水槽の前記排水を前記システムへ返送する手段とからなり、
前記腐植物質が無機物質を含む微細粒子であって、前記微細粒子の量が0.05〜3重量%の範囲にある水との混合物の形態で前記供給手段により連続的および間欠的のいずれかの態様で供給され、
前記供給手段は、前記微細粒子と水とを混合することができる攪拌機付きの混合槽と、前記混合槽へ前記微細粒子を連続的および間欠的のいずれかの態様で投入可能なホッパーと、前記微細粒子と水との混合物を前記貯水槽へ送る輸送手段とを備え、前記混合物は、前記貯水槽で処理する1日当たりの前記排水の量の0.5/1000〜5/1000を前記排水に添加して前記システムへ返送し、
前記混合槽の容積が前記貯水槽の容積の0.5〜1%であることを特徴とする前記排水浄化システム。
A system for purifying organic wastewater by the action of soil bacteria, wherein a part of the wastewater is taken out of the system and brought into contact with humic substances, and then a part of the wastewater is returned to the system. In
The process comprises a water storage tank into which a part of the waste water taken out from the system flows, a supply means for the humic substance to the water storage tank, and a means for returning the waste water from the water storage tank to the system. ,
The humic substance is fine particles containing an inorganic substance, and the amount of the fine particles is in the form of a mixture with water in the range of 0.05 to 3% by weight , either continuously or intermittently by the supply means Supplied in the form of
The supply means includes a mixing tank equipped with a stirrer capable of mixing the fine particles and water, a hopper capable of charging the fine particles continuously or intermittently into the mixing tank, Transportation means for sending a mixture of fine particles and water to the water tank, and the mixture uses 0.5 / 1000 to 5/1000 of the amount of the waste water per day to be treated in the water tank as the waste water. Add and return to the system,
The said waste water purification system characterized by the volume of the said mixing tank being 0.5 to 1% of the volume of the said water storage tank.
前記貯水槽が前記排水浄化システムにおける培養槽である請求項1に記載の排水浄化システム。  The waste water purification system according to claim 1, wherein the water storage tank is a culture tank in the waste water purification system. 前記微細粒子における前記無機物質の含有量が50〜90重量%である請求項1または2に記載の排水浄化システム。  The wastewater purification system according to claim 1 or 2, wherein the content of the inorganic substance in the fine particles is 50 to 90% by weight. 前記無機物質に珪酸塩化合物が含まれる請求項1〜3のいずれかに記載の排水浄化システム。  The drainage purification system according to any one of claims 1 to 3, wherein the inorganic substance includes a silicate compound. 前記珪酸塩化合物が軽石、安山岩、流紋岩、火山ガラス、ゼオライト、グリーンタフ、珪藻土、粘土鉱物のいずれかである請求項4記載の排水浄化システム。  The drainage purification system according to claim 4, wherein the silicate compound is any one of pumice, andesite, rhyolite, volcanic glass, zeolite, green tough, diatomaceous earth, and clay mineral. 前記微細粒子が50メッシュ以上のものである請求項1〜5のいずれかに記載の排水浄化システム。  The waste water purification system according to any one of claims 1 to 5, wherein the fine particles are 50 mesh or more.
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