JP2003340464A - Apparatus for purifying waste water - Google Patents

Apparatus for purifying waste water

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Publication number
JP2003340464A
JP2003340464A JP2002148498A JP2002148498A JP2003340464A JP 2003340464 A JP2003340464 A JP 2003340464A JP 2002148498 A JP2002148498 A JP 2002148498A JP 2002148498 A JP2002148498 A JP 2002148498A JP 2003340464 A JP2003340464 A JP 2003340464A
Authority
JP
Japan
Prior art keywords
water
sludge
waste water
wastewater
discharging
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002148498A
Other languages
Japanese (ja)
Inventor
Norihide Saho
典英 佐保
Yuko Okada
祐子 岡田
Noriyo Nishijima
規世 西嶋
Katsuhiko Asano
克彦 浅野
Rei Okawa
令 大川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2002148498A priority Critical patent/JP2003340464A/en
Publication of JP2003340464A publication Critical patent/JP2003340464A/en
Pending legal-status Critical Current

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  • Sanitary Device For Flush Toilet (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a waste water purifying apparatus in which sewage from a building or a multiple-family dwelling, domestic waste water, industrial waste water, or the like, is purified effectively at a low cost so that the purified water is used as regenerated water and the recovered sludge is used effectively at a low cost as manure for farming land and the generation of gaseous carbon dioxide is restrained. <P>SOLUTION: Waste water is purified by separating/removing large organic matter having ≥0.5 mm particle size in the waste water by using a screen having about 0.5-1.0 mm mesh, adding a flocculant such as ferric polysulfate and aluminum polychloride to the organic matterremoved waste water to flocculate tainting particles into flocks and removing the flocks by precipitating them, filtering them by using another screen having about several tens μm mesh or adding another flocculant, magnetic powder and a macromolecular flocculant to the flock-containing waste water to transform them into magnetic flocks and separating the magnetic flocks magnetically. At this step, the tainting sludge having ≥0.1 μm particle size is removed and the dissolved phosphorus is also removed by transforming it into iron phosphate chemically. A decomposing unit is combined with this waste water purifying apparatus for decomposing at ≤200°C the sludge recovered at this step, namely, when the filtration, the flocculation and the magnetic separation are performed. <P>COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、生活空間周りの緑
地への散水水源や道路冷却水源とする地域分散型の排水
浄化装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an area-dispersed wastewater purification device which serves as a watering source for a green space around a living space or a road cooling water source.

【0002】[0002]

【従来の技術】現状の都市生活地域の下水の浄化システ
ムとしては、生活地域のトイレ排水や台所からの排水を
含む下水を、下水配管で集め下水処理場にて一括的に浄
化処理するシステムが採用されている。しかし、このシ
ステムでは、下水配管が長尺となり、下水配管を移動す
る間に最初有機物サイズが100μm以上が大半であっ
た下水は、配管中の微生物で分解され、下水中の有機物
サイズが0.1μm以下の粒子となり、処理場における
凝集沈殿処理による有機物除去効率が低下したり、微生
物処理時間が増加し処理場が大型化したり、微小粒子を
吸着させるための大型の活性炭吸着槽が必要となりと頻
繁に活性炭を新品と取り替える必要があり、設備コスト
や運転コストが上昇する。
2. Description of the Related Art As a current sewage purification system for urban living areas, there is a system that collects sewage including toilet drainage and kitchen drainage in living areas through sewer pipes and collectively purifies the sewage at a sewage treatment plant. Has been adopted. However, in this system, the sewage pipe becomes long, and the sewage whose organic matter size was 100 μm or more for the first time while moving through the sewage pipe was decomposed by microorganisms in the pipe and the organic matter size in the sewage was 0. Particles of 1 μm or less will reduce the efficiency of organic matter removal by coagulation-sedimentation treatment at the treatment plant, increase the treatment time of microorganisms and increase the size of the treatment plant, and require a large activated carbon adsorption tank for adsorbing fine particles. It is necessary to frequently replace the activated carbon with a new one, which increases equipment costs and operating costs.

【0003】また、下水処理場で下水から中水を製造し
これを再び下水を発生するビルに地下の送水管で送水
し、ビル周りの緑地用資源や水洗トイレの洗浄水として
ビルで使用する場合も、地下の送水管の敷設、メンテナ
ンス費用が必要であり、安価な中水を利用できない。
[0003] In addition, in the sewage treatment plant, middle water is produced from the sewage, and this is again sent to a building that generates sewage by an underground water pipe, and is used in the building as a green space resource around the building and as flush water for flush toilets. In this case, too, underground water pipes need to be laid and maintained, and inexpensive middle water cannot be used.

【0004】このため、かかる都市生活地域の浄化シス
テムの効率向上を図るべく、従来からいろいろ提案がな
されている。地域分散型浄化システムとしては、特開平
10−118043号公報のようにビル内で消費される
上水が元となる下水を、同ビル下部の空間において、バ
クテリア等の微生物で下水中の有機物を分解処理して汚
泥を低減し、かつ、活性炭やオゾン酸化で高度浄化処理
し、下水から中水と上水を製造し、中水はトイレ等の洗
浄水として再使用し、上水は飲料用として再利用する浄
化システムがある。
Therefore, various proposals have been made in the past in order to improve the efficiency of such a purification system for urban living areas. As a locally dispersed purification system, sewage derived from clean water consumed in a building as disclosed in Japanese Patent Laid-Open No. 10-118043, and organic matter in the sewage due to microorganisms such as bacteria in a space below the building. Sludge is reduced to reduce sludge, and advanced purification treatment with activated carbon and ozone oxidation is performed to produce gray water and tap water from the sewage, and the tap water is reused as wash water for toilets, etc. There is a purification system for reuse.

【0005】一般的には、トイレ排水等の有機物を多く
含む排水では、バクテリア等の微生物で下水中の有機物
を分解処理して汚泥を低減させる浄化方法が採用されて
いる。下水汚泥をコンポストとして再利用する社会シス
テムが一般的でない現状では、有機物を生物分解処理し
下水汚泥をできるだけ低減して、汚泥処理費用を低減す
る方法が有効である。
In general, for wastewater containing a large amount of organic matter such as toilet wastewater, a purification method of decomposing organic matter in sewage with microorganisms such as bacteria to reduce sludge is adopted. In the current situation where social systems that reuse sewage sludge as compost are not common, it is effective to reduce sludge treatment costs by biodegrading organic matter to reduce sewage sludge as much as possible.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上述し
た従来の処理方法では、バクテリアが有機物の炭素を炭
酸ガスに変えて大気中に放出することを前提としてお
り、地球温暖化防止の観点からは、大量の炭酸ガスを環
境に放出する問題が生じている。また、有機物や有機物
中に固定されている不溶解性の窒素を、微生物が分解し
粒子径が0.1μm以下の溶解性有機物や、アンモニア
や硝酸イオン等の溶解性窒素に変えてしまう。これによ
って、0.1μm以下の溶解性有機物のフミン酸や溶解
性窒素を処理するために、活性炭やオゾン等を大量に消
費する高度処理が必要となり、運転コストが高価なオゾ
ン酸化や活性炭吸着によるフミン酸の酸化、吸着処理
や、大型処理槽が必要となる処理時間が長くかかる嫌気
性硝化菌による溶解性窒素分解工程が必要となり、設備
コストや運転コストが増加する問題がある。
However, in the above-mentioned conventional treatment method, it is premised that the bacteria convert carbon of the organic matter into carbon dioxide gas and release it into the atmosphere. From the viewpoint of preventing global warming, The problem of releasing large amounts of carbon dioxide into the environment has arisen. In addition, organic matter or insoluble nitrogen fixed in the organic matter is decomposed by microorganisms to be dissolved organic matter having a particle diameter of 0.1 μm or less, or soluble nitrogen such as ammonia or nitrate ions. Due to this, in order to treat humic acid and soluble nitrogen of soluble organic substances of 0.1 μm or less, advanced treatment that consumes a large amount of activated carbon, ozone, etc. is required, and ozone oxidation and activated carbon adsorption, which are expensive to operate, are required. There is a problem that humic acid is oxidized and adsorbed, and a large-scale treatment tank is required, and a soluble nitrogen decomposing step by anaerobic nitrifying bacteria that requires a long time is required, resulting in increase in equipment cost and operation cost.

【0007】また、近年、都市ビル群の空間平面では、
緑地が少なく夏場には前記空間の気温が上昇するヒート
アイランド現象が発生しており、ビル屋上等に緑地を生
成することが前記空間の気温防止の有効であるが、緑地
の育成・維持のための水源は雨水や上水や中水を使用す
ることが一般的である。しかし、雨水は毎日や数日ごと
に確保するのは困難であり、上水や中水を使用すると散
水コストが高くなる問題がある。
[0007] In recent years, in the space plane of city buildings,
The heat island phenomenon that the temperature of the space rises in the summer when there is little green space, and it is effective to prevent the temperature of the space by creating a green space on the roof of a building, etc. The water source is generally rainwater, clean water, or clean water. However, it is difficult to secure rainwater every day or every few days, and there is a problem that the cost of watering increases when using clean water or medium water.

【0008】また、近年、食料品を加工する工場廃水や
病院排水には、多量の有機物が含まれており、この排水
をバクテリア等の微生物で下水中の有機物を分解処理し
て汚泥を低減し、かつ、活性炭やオゾン酸化で高度浄化
処理して河川や海洋に放水しており、処理コストが高く
なる問題がある。
[0008] In recent years, a large amount of organic matter is contained in factory wastewater and hospital wastewater that process food products, and this wastewater is decomposed with microorganisms such as bacteria to decompose organic matter in sewage to reduce sludge. In addition, it is highly purified by activated carbon or ozone oxidation and discharged to rivers and oceans, which causes a problem of high treatment cost.

【0009】また、従来浄化装置から回収された有機汚
泥は長時間かけて微生物でコンポスト化する方法が提供
されているが、肥料化に長時間必要であることから、外
設の肥料化工場やプラント施設まで輸送し肥料化処理す
ることが一般であるが、回収汚泥の運搬費用に多額を要
し、処理費用が高額となっていた。また、前記肥料化工
場やプラント施設まで輸送するあいだ、輸送定量になる
まで未輸送で保管する必要があり、このとき回収汚泥か
ら悪臭が発生し、居住空間に悪臭がもれたり、また、も
れを防ぐために悪臭を処理する装置が必要であった。
Further, although a method of composting organic sludge collected from a conventional purification device with microorganisms for a long time is provided, it is necessary for a long time for fertilization, so that it is necessary to use an external fertilizer factory or Generally, it is transported to a plant facility for fertilizer treatment, but the transportation cost of the recovered sludge is large and the treatment cost is high. In addition, during transportation to the fertilizer plant or plant facility, it is necessary to store the transportation until it reaches a fixed amount, and at this time, a bad odor is generated from the collected sludge, and a bad odor is generated in the living space, and also In order to prevent this, a device for treating the bad smell was required.

【0010】本発明の目的は、ビルやマンション等の多
数の人間が居住し、下水や生活廃水および工場廃水等を
低コストでかつ良好に浄化し、下水や生活廃水を再生水
として再利用することができる浄化装置を提供すること
にある。また、回収汚泥を低コストでかつ良好に肥料化
し、農耕地用肥料として汚泥を再利用することができる
浄化装置を提供することにある。
An object of the present invention is to allow a large number of people such as buildings and condominiums to live, to purify sewage, domestic wastewater, industrial wastewater, etc. at low cost and to reuse the sewage and domestic wastewater as recycled water. It is to provide a purifying device capable of Another object of the present invention is to provide a purification device that can convert recovered sludge into a good fertilizer at low cost and reuse the sludge as fertilizer for agricultural land.

【0011】[0011]

【課題を解決するための手段】上記目的は、リン等を含
む汚濁水を一時保留する排水保留手段と、排水を前記排
水保留手段に収集する排水収集手段と、前記排水を浄化
処理する浄化手段と、前記浄化処理で発生する汚泥を排
水から分離排出する汚泥分離排出手段と、前記浄化処理
で発生する浄化水を排出する手段とを有する排水浄化装
置において、前記浄化手段を凝集剤を注入して汚濁粒子
やリン等を含有するフロックを形成し、このフロックを
分離する凝集分離手段で前記フロックを汚泥として分離
排出することにより達成される。
[Means for Solving the Problems] The above-mentioned objects are as follows: wastewater holding means for temporarily holding polluted water containing phosphorus, etc., wastewater collecting means for collecting wastewater in the wastewater holding means, and purification means for purifying the wastewater. And a sludge separating and discharging means for separating and discharging sludge generated in the purification treatment from wastewater, and a means for discharging purified water generated in the purification treatment, in which the purifying means is injected with a coagulant. This is accomplished by forming flocs containing pollutant particles, phosphorus, etc., and separating and discharging the flocs as sludge by a flocculating separation means for separating the flocs.

【0012】また、上記目的は、前記汚濁水を無薬注処
理で濾過する無薬注濾過手段と、凝集剤を注入して汚濁
粒子やリン等を含有するフロックを形成し、前記フロッ
クを分離する凝集分離手段で構成することにより達成さ
れる。
[0012] Further, the above-mentioned object is to form a floc containing pollutant particles and phosphorus by injecting a flocculant by injecting a flocculant by separating the floc by means of a non-medicated filtration means for filtering the contaminated water by a non-medicated treatment. It is achieved by the aggregating and separating means.

【0013】また、上記目的は、前記汚濁水を無薬注処
理で濾過する無薬注濾過手段と、凝集剤、磁性物質を注
入して汚濁粒子やリン等を含有する磁性フロックを形成
し、前記磁性フロックを分離する凝集分離手段で前記磁
性フロックを汚泥として磁気分離収集するこにより達成
される。
Further, the above-mentioned object is to form a magnetic floc containing pollutant particles, phosphorus, etc. by injecting a flocculant and a magnetic substance by means of a non-medicated filtration means for filtering the polluted water in a non-medicated treatment. This is achieved by magnetically separating and collecting the magnetic flocs as sludge by a flocculation separation means for separating the magnetic flocs.

【0014】また、上記目的は、前記浄化処理で発生す
る浄化水を排出する手段に、植物への給水手段を有する
ことにより達成される。
Further, the above object can be achieved by providing a water supply means for plants as a means for discharging the purified water generated in the purification treatment.

【0015】また、上記目的は、前記浄化処理で発生す
る浄化水を排出する手段に、土地を冷却もしくは加温す
る給水手段を有することにより達成される。
Further, the above object can be achieved by providing a means for discharging purified water generated in the purification treatment with a water supply means for cooling or heating the land.

【0016】また、上記目的は、前記排水収集手段に料
理残渣を細かく破砕し排水する破砕排出手段を有するこ
とにより達成される。
Further, the above object can be achieved by providing the waste water collecting means with a crushing discharging means for crushing the cooking residue finely and discharging it.

【0017】また、上記目的は、前記汚泥回収手段に、
回収した汚泥を乾燥し、200℃以下で熱処理し汚泥含
水率を低減する汚泥乾燥手段を有することにより達成さ
れる。
Further, the above object is to provide the sludge collecting means as follows.
This is achieved by having sludge drying means for drying the recovered sludge and heat-treating it at 200 ° C. or lower to reduce the sludge water content.

【0018】また、上記目的は、前記浄化手段を、前記
汚濁水を無薬注処理で物理的濾過する無薬注濾過手段
と、磁性物質を生成する凝集剤を注入して汚濁粒子やリ
ン等を含有する磁性フロックを形成し、前記磁性フロッ
クを汚泥として磁気分離収集することにより達成され
る。
Further, the above-mentioned object is that the purification means is a non-chemical-injection filtering means for physically filtering the polluted water by a non-chemical-injection treatment, and a flocculating particle or phosphorus by injecting a flocculant which produces a magnetic substance. Is formed by forming a magnetic floc containing the above, and magnetically separating and collecting the magnetic floc as sludge.

【0019】また、上記目的は、前記浄化処理で発生す
る浄化水を排出する手段に、水洗トイレの洗浄水として
使用する給水手段を有することにより達成される。
Further, the above object can be achieved by providing a means for discharging purified water generated in the purification treatment with a water supply means used as flush water for a flush toilet.

【0020】また、上記目的は、前記浄化処理で発生す
る浄化水を排出する手段に、前記居住空間内や産業生産
場の建屋の一部を冷却するための給水手段を有すること
により達成される。
Further, the above object can be achieved by providing the means for discharging the purified water generated in the purification treatment with a water supply means for cooling a part of the building of the industrial space or the living space. .

【0021】[0021]

【発明の実施の形態】さて、本発明は、ビルやマンショ
ン等の多数の人間が居住する建造物の敷地内などに設置
された生活廃水の排水処理装置や、工場などでは工場廃
水の排水処理施設が敷地内などに設置されている。この
下水や生活廃水や工場廃水等の初期処理段階において
は、物理的な濾過処理や凝集処理等の非生物処理による
水処理を行うことにより、まず目開き0.5mm〜1.
0mm程度の網を使用し、0.5mm以上の粒子径の大
きな有機物等を濾過分離除去する。例えば、トイレで使
用された紙のくずや、台所から排出されるディスポーザ
で細かく切断、破砕した残野菜や残料理等の荒めの粒子
等を廃水中から除去するものである。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is a wastewater treatment apparatus for domestic wastewater installed in a site of a building where many people live such as buildings and condominiums. Facilities are installed on the premises. In the initial treatment stage of sewage, domestic wastewater, factory wastewater, etc., water is first treated by abiotic treatment such as physical filtration or coagulation treatment, so that the opening is 0.5 mm to 1.
Using a net of about 0 mm, organic substances having a large particle size of 0.5 mm or more are separated by filtration. For example, it is used to remove waste paper from waste water, scraps of paper used in the toilet, residual vegetables crushed by a disposer discharged from the kitchen, and crushed into pieces.

【0022】次に、濾過後の廃水にポリ硫酸第2鉄やポ
リ塩化アルミニュウム等の凝集剤を加えて廃水中の汚濁
粒子をフロック化して沈殿分離やまず目開き数十μm程
度の網を使用した濾過分離したり、凝集剤とともに磁性
粉や高分子凝集剤を追加添付して汚濁粒子を磁性フロッ
ク化して磁気分離したりして、廃水を浄化する。ここ
で、0.1μm以上粒子径を有する汚濁物や、溶解性リ
ンを燐酸鉄に化学変化させて除去することができる。例
えば、この浄化工程で排水中のSS(汚濁浮遊粒子)、BO
D(生物的酸素要求量)、COD(化学酸素要求量)、窒
素、リンの90%以上を除去する。
Next, a coagulant such as ferric polysulfate or polyaluminium chloride is added to the waste water after filtration to flocculate the polluted particles in the waste water to separate them by sedimentation or use a net with an opening of several tens of μm. The wastewater is purified by filtering and separating, or by additionally attaching magnetic powder or polymer coagulant together with the coagulant to magnetically separate polluted particles into magnetic flocs for magnetic separation. Here, contaminants having a particle size of 0.1 μm or more and soluble phosphorus can be chemically changed to iron phosphate and removed. For example, in this purification process, SS (polluted suspended particles) and BO in the wastewater
Removes 90% or more of D (biological oxygen demand), COD (chemical oxygen demand), nitrogen and phosphorus.

【0023】また、濾過および凝集分離、凝集磁気分離
で回収した汚泥を、200℃以下の温度で分解処理する
装置を組み合わせて構成するものであって、汚泥を運搬
することなく、汚泥は居住空間内や工場内およびその近
傍において、この工程で脱水され、有機物が数時間の熱
分解により乾燥し、悪臭等の原因となる物質は揮発す
る。揮発したガスは燃焼や触媒酸化処理等により無臭化
され、熱分解、乾燥した汚泥はすべて有機肥料材として
有効再利用できるようにしたものである。
The sludge collected by filtration, coagulation separation, and coagulation magnetic separation is combined with a device for decomposing the sludge at a temperature of 200 ° C. or less, and the sludge is transported in a living space without being transported. Inside the plant, in the plant, and in the vicinity thereof, dehydration is performed in this step, the organic matter is dried by thermal decomposition for several hours, and a substance causing an offensive odor is volatilized. The volatilized gas is deodorized by combustion, catalytic oxidation, etc., and the pyrolyzed and dried sludge can be effectively reused as an organic fertilizer material.

【0024】以下、本発明の一実施例を図1および図2
により説明する。図1は、本発明の下水排水浄化システ
ムを備えたビルの概略断面図である。図1において、例
えばビル1のトイレ2や、給湯室の流し台3からの排水
が排水管4で各階の排水が集められ、例えばビルの地階
5の空間に設置された浄化装置6内に流入する。浄化装
置6で浄化された処理水は、用水揚水管7からビル内の
トイレ洗浄用の用水や、屋上緑地等への供給水として用
水槽8に揚水、貯蔵される。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
Will be described. FIG. 1 is a schematic cross-sectional view of a building equipped with the sewage drainage purification system of the present invention. In FIG. 1, for example, the drainage from the toilet 2 of the building 1 or the sink 3 of the hot water supply room is collected by the drainage pipe 4 and flows into the purifying device 6 installed in the space of the basement 5 of the building, for example. . The treated water purified by the purifying device 6 is pumped and stored in the water tank 8 from the water pumping pipe 7 as water for cleaning the toilet in the building and as water supplied to the rooftop green space and the like.

【0025】この揚水の途中にビル壁を冷却もしくは加
温するチューブ式のビル壁熱交換器9を設ける場合もあ
る。用水槽8には、用水供給管10を通じてトイレ2の
洗浄水の一部に使用され、また用水供給管11、流量調
整弁12を通じて緑地槽13内の土壌14に分配管15
で水分を所定の時間的間隔で供給され、草木16を育成
する。トイレ2の一部や給湯室の流し台3には、水道等
の外部からの上水を上水配管17で受け入れ、上水供給
管18でビル内に供給する。
A tube-type building wall heat exchanger 9 for cooling or heating the building wall may be provided in the middle of this pumped water. In the water tank 8, a part of the wash water for the toilet 2 is used through the water supply pipe 10, and the distribution pipe 15 is connected to the soil 14 in the green space tank 13 through the water supply pipe 11 and the flow rate adjusting valve 12.
The water is supplied at predetermined time intervals, and the plants 16 are grown. Part of the toilet 2 and the sink 3 of the hot water supply room receive tap water from the outside through a tap water pipe 17 and supply it into the building through a tap water supply pipe 18.

【0026】また、用水槽8には、用水供給管10およ
び19、流量調整弁20、分配管21を通じて、地面3
0に配置した緑地槽22内の土壌23に水分を所定の時
間間隔で供給し、草木24を育成する。
Further, the water tank 8 is connected to the ground 3 through the water supply pipes 10 and 19, the flow rate adjusting valve 20, and the distribution pipe 21.
Water is supplied to the soil 23 in the green tract tank 22 arranged at 0 at a predetermined time interval to grow the plants 24.

【0027】また、用水槽8には、用水供給管10、1
9および25、流量調整弁26、分配管27を通じて、
車両28等が走行する透水性の舗装道路29内に水分を
所定の時間間隔で供給し、舗装道路29内に水が浸透
し、夏場にはさらに蒸発することにより舗装道路29を
夏場は冷却し、冬場は加温するようになっている。
Further, in the water tank 8, water supply pipes 10, 1 are provided.
9 and 25, the flow rate adjusting valve 26, the distribution pipe 27,
Moisture is supplied at a predetermined time interval into the permeable paved road 29 on which the vehicle 28 or the like travels, water permeates into the paved road 29, and further evaporates in the summer, thereby cooling the paved road 29 in the summer. , It is designed to be heated in winter.

【0028】図2は、本発明の下水排水浄化システムを
説明する構成図である。図2において、被処理水である
下水を、排水管4から貯水槽31に保留し、貯水槽31
から、導管32、大きなゴミを取るためのフィルタ33
を通してポンプ34で下水貯槽35に貯留される。貯留
された下水36に導管38を通じて、薬剤供給装置37
から、四酸酸化鉄等の磁性粉とpH調整剤、ポリ塩化ア
ルミニウムや塩化鉄や硫酸第二鉄等の水溶液等のアルミ
ニュウムイオンや鉄イオンを提供する凝集剤や高分子補
強剤等を加えられる。このような薬剤が加えられた下水
36は撹絆槽39内でモータ40により回転駆動される
攪拌翼41で撹絆され、数百ミクロンメートル〜数ミリ
メートル程度の大きさの磁性フロックを含む前処理水4
2が生成される。
FIG. 2 is a block diagram for explaining the sewage drainage purification system of the present invention. In FIG. 2, sewage, which is water to be treated, is reserved from the drain pipe 4 in the water storage tank 31,
, Conduit 32, filter 33 for removing large dust
Through the pump 34 to be stored in the sewage storage tank 35. A medicine supply device 37 is provided through the conduit 38 to the stored sewage 36.
, Magnetic powders such as iron tetraoxide and pH adjusters, flocculants and polymeric reinforcing agents that provide aluminum ions and iron ions such as aqueous solutions of polyaluminum chloride, iron chloride and ferric sulfate can be added. . The sewage 36 to which such a chemical has been added is agitated by an agitating blade 41 which is rotationally driven by a motor 40 in an agitating tank 39, and a pretreatment including magnetic flocs having a size of several hundreds of micrometers to several millimeters. Water 4
2 is generated.

【0029】このように生成した前処理水42を矢印A
で示すように導管43を通じて、濾過分離装置44に通
水する。濾過分離装置44では、紙面時計回りに回転
し、目開き数十μmの回転型の網45により、前処理水
42中の磁性フロックが濾過される。濾過分離で浄化さ
れた処理水は、導管46を通じて脱臭装置47に送水さ
れ、オゾン酸化、紫外線殺菌処理等を施し、無臭で雑菌
の無い水に処理される。
The pretreated water 42 produced in this way is indicated by an arrow A.
Water is passed through the conduit 43 to the filtration / separation device 44 as shown in FIG. In the filtration / separation device 44, the magnetic flocs in the pretreated water 42 are filtered by a rotation type net 45 that rotates clockwise in the plane of the drawing and has an opening of several tens of μm. The treated water purified by filtration and separation is sent to the deodorizing device 47 through the conduit 46, subjected to ozone oxidation, ultraviolet sterilization treatment, etc., and treated to be odorless and free of germs.

【0030】この水は、用水揚水管7からからビル内の
トイレ洗浄用の用水や、屋上緑地等への供給水として図
1に示した用水槽8に揚水、貯蔵される。濾過水処理水
の一部は、導管46から取水されポンプ(図示せず)で
加圧された後、配管48を通じて散水管49に導かれ
る。回転型の網45の外表面に濾過された磁性フロック
は、散水管49からのシャワー水50で網内部から洗浄
され、洗い流された後、静止固定された磁石51の磁気
力で磁石側に引き寄せられ、紙面に対し反時計回りに回
転する非磁性材料の回転円筒体52の表面に付着し、前
処理水43の水面上に輸送され、余分な水分切を行い、
静止しているかき取り板53でかき取られて回収され、
汚泥槽54に落下し貯留される。
This water is pumped and stored in the water tank 8 shown in FIG. 1 as water for cleaning the toilet in the building from the water pumping pipe 7 and water supplied to the rooftop green space and the like. A part of the filtered water treated water is taken from the conduit 46, pressurized by a pump (not shown), and then guided to the sprinkling pipe 49 through the pipe 48. The magnetic flocs filtered on the outer surface of the rotary net 45 are washed from the inside of the net with shower water 50 from the water sprinkling pipe 49, washed off, and then attracted to the magnet side by the magnetic force of the stationary magnet 51. And is attached to the surface of the rotating cylindrical body 52 made of a non-magnetic material that rotates counterclockwise with respect to the paper surface, and is transported onto the surface of the pretreatment water 43 to remove excess water,
It is scraped off by a stationary scraping plate 53 and collected.
It falls into the sludge tank 54 and is stored.

【0031】回収汚泥は、配管55を通じてスラッジ槽
56に貯められ、運搬時にスラッジから水が漏れないよ
うに含水率を約85%に、またコンポスト時の有機物を
分解する微生物の活性化を図るように含水率を約75%
にするように運搬前、コンポスト処理前にスラッジの含
水率を、遠心分離機やベルトプレス機等の脱水手段57
によって更に濃縮される。回収汚泥はトラックで処分場
や焼却場に運搬したり、後段に堆肥化槽58を設け、ス
ラッジを堆肥化槽58に流路59を通じて移送し、コン
ポスト化したりする。尚、堆肥化した後、堆肥を粉状に
破砕し肥料中の磁性粉や生成磁性物質を他の磁石磁気分
離装置で回収して再利用しても良い。
The recovered sludge is stored in a sludge tank 56 through a pipe 55, and has a water content of about 85% so that water does not leak from the sludge during transportation and activates microorganisms that decompose organic matter during composting. With a moisture content of about 75%
As described above, the water content of the sludge before transportation and before the composting process is determined by the dewatering means 57 such as a centrifuge or a belt press.
Is further concentrated by. The recovered sludge is transported to a disposal site or an incinerator by a truck, or a composting tank 58 is provided in the latter stage, and sludge is transferred to the composting tank 58 through a flow path 59 to be composted. In addition, after composting, the compost may be crushed into a powder form, and the magnetic powder or the generated magnetic substance in the fertilizer may be recovered by another magnet magnetic separation device and reused.

【0032】図3は、他の実施例を示す洗浄装置の構成
図である。図3において、回収汚泥を配管55の通じて
スラッジ槽56に貯め、汚泥液化装置60で温度約200
℃以下の温度で加熱・加圧して凝集剤の凝集機能を無く
して汚泥を液化する。その後、磁気分離装置61で大気
圧に戻し、ここで蒸気や匂い成分は揮発し、これらは配
管62を通って燃焼器63で高温燃焼され匂いが脱臭さ
れる。その排ガスは大気に放出される。磁気分離装置6
1で、汚泥中の磁性粉等の磁性物資を除去し、その後、
乾燥加熱装置64で温度180℃以下で乾燥、粉砕処理
され、糞や料理残渣等の有機物は乾燥されると数ミリの
大きさに砕けるが、料理残渣中のラップ等のビニール類
の残渣は強度があるので粉砕されずに大きいサイズのま
ま残る。その後、金網等の濾過装置や振動式の振るい装
置で構成した容器等分別装置65で肥料化した加熱乾燥
汚泥とビニール類の残渣を分別し、ビニール類の残渣は
焼却処分かプラスチックリサイクル原料として使用し、
加熱乾燥汚泥を肥料として再利用する。
FIG. 3 is a block diagram of a cleaning apparatus showing another embodiment. In FIG. 3, the recovered sludge is stored in a sludge tank 56 through a pipe 55, and a sludge liquefaction device 60 is used to store a temperature of about 200
The sludge is liquefied by heating and pressurizing at a temperature of ℃ or less to eliminate the coagulation function of the coagulant. After that, the pressure is returned to the atmospheric pressure by the magnetic separation device 61, where vapor and odor components are volatilized, and these are burned at a high temperature in the combustor 63 through the pipe 62 to deodorize the odor. The exhaust gas is released to the atmosphere. Magnetic separation device 6
In 1, remove magnetic substances such as magnetic powder in sludge, and then
It is dried and pulverized at a temperature of 180 ° C or less in a drying and heating device 64, and organic matter such as feces and cooking residues are crushed to a size of several millimeters when dried, but vinyl residues such as wrap in cooking residues are strong Since it is there, it remains in a large size without being crushed. After that, the heat-dried sludge fertilized with the container separation device 65 composed of a filtering device such as a wire mesh or a vibrating screen device and vinyl residue are separated, and the vinyl residue is incinerated or used as a plastic recycling material. Then
Reuse the heat-dried sludge as fertilizer.

【0033】本実施例によれば、ビル内の下水や廃水は
同ビル内や同敷地内の近傍の場所に設置された浄化装置
により、下水発生以後短時間内に濾過分離、凝集濾過分
離や凝集磁気分離することにより、下水中の汚濁粒子や
溶解性のリンの大部分を除去できるので、生物処理工程
を含まずとも、凝集剤投入から数分間の処理工程で終了
する凝集濾過分離や凝集磁気分離工程のみで、河川放流
水質基準を十分満たす水質までにすることができる。
According to this embodiment, the sewage and wastewater in the building are filtered and coagulated within a short time after the generation of sewage by a purifying device installed in the building or in the vicinity of the site. Coagulation Magnetic separation can remove most of pollutant particles and soluble phosphorus in sewage.Therefore, even if biological treatment step is not included, coagulation filtration separation or coagulation is completed within a few minutes from the coagulant input. It is possible to obtain water quality that fully meets the river discharge water quality standard only by the magnetic separation process.

【0034】すなわち、バクテリア等で有機物がサイズ
がが0.1μm以下の微細物に分解される前の下水発生
以後短時間内に、凝集剤を使用して汚濁粒子を除去でき
るので、分離後には微細な粒子物がほとんど無く、非常
に高い資質の処理水をえることができる。したがって、
その処理水は脱臭、殺菌処理を施すだけで、トイレの洗
浄水として再使用したり、ビル壁の冷却やビルの屋上や
近傍地面の草木への散水用の用水として使用したり、ビ
ル近傍の道路の、夏場の冷却や冬場の加温等の用水とし
て使用できる。
That is, since a flocculant can be used to remove the pollutant particles within a short time after the generation of sewage before the organic substances are decomposed into fine particles having a size of 0.1 μm or less by bacteria or the like, after separation, Almost no fine particles are present, and treated water of very high quality can be obtained. Therefore,
By simply deodorizing and sterilizing the treated water, it can be reused as toilet wash water, water for cooling building walls, watering plants on the roof of the building or nearby ground, and water near the building. It can be used as water for cooling roads in summer and heating in winter.

【0035】したがって、生物処理工程を含まないので
処理時間が短く、浄化装置が小型ですみ、狭い場所に設
置でき装置および設置コストを低減することができるの
で、ビルやマンション等の多数の人間が居住し、下水や
生活廃水および工場廃水等を低コストでかつ良好に浄化
し、下水や生活廃水を再生水として再利用することがで
きる浄化装置を提供できる。
Therefore, since the biological treatment process is not included, the treatment time is short, the purification device is small, and the device and the installation cost can be reduced in a narrow space, so that many people such as buildings and condominiums can use it. It is possible to provide a purification device that can live and purify sewage, domestic wastewater, factory wastewater, and the like at low cost and satisfactorily, and reuse the sewage and domestic wastewater as recycled water.

【0036】また、回収汚泥はその住居空間から排出さ
れる成分を把握できるので、工業製品製造工程排水等に
混入する可能性がある有害重金属等は混入していないこ
とも確認できる。すなわち、一般的にビルやマンション
やホテル等から排出される下水には有害物が混入してい
ない場合が大半であり、これらの有害物を除去する費用
は発生せず、回収汚泥は有機肥料として低コストでかつ
良好に肥料化し、農耕地用肥料として汚泥を再利用する
ことができる。
Further, since the components of the recovered sludge discharged from the living space can be ascertained, it can be confirmed that harmful heavy metals, which may possibly be mixed in the wastewater of the industrial product manufacturing process, are not mixed. That is, in general, sewage discharged from buildings, condominiums, hotels, etc. does not contain harmful substances in most cases, and there is no cost to remove these harmful substances. The sludge can be reused as fertilizer for agricultural land at low cost and with good fertilization.

【0037】図4も本発明の他の実施例を説明する浄化
装置の構成図である。図4は、ビルやマンションやホテ
ル等で、野菜や料理残渣をディスポーザで機械的に細か
く切断した有機物等が生活廃水とともにそれぞれの居住
空間内の排水に混在する場合の浄化装置の構成を示すも
のである。図4において、排水中に混在したディスポー
ザで切断された有機物の大きさは数ミリである。排水管
4で供給される各階の排水は、目開きが.5〜1mm程度
である回転ドラム状第一濾過装置61の網60の内側に
導入され、網60で物理的に濾過される。濾過された第
一処理水62は網60の外側に排出され、処理槽63に
貯留される。ディスポーザで切断された野菜や料理残渣
は、野菜砕片のサイズが0.5mm未満の細かい有機物
が多く含まれる。これらの有機物は前記第一濾過装置6
1では濾過できず、第一処理水62中に混入する。前記
第一濾過装置61で濾過網を通過した第一処理水62
は、浄化装置の排水管72に導かれ、凝集剤を使用して
前記0.5mm未満の細かい有機物を凝集して濾過分離
する。これは、前記した処理法と同一である。
FIG. 4 is also a block diagram of a purifying device for explaining another embodiment of the present invention. Fig. 4 shows the configuration of a purification device in buildings, condominiums, hotels, etc., where vegetables and food residues are mechanically finely cut with a disposer and organic substances and the like are mixed with domestic wastewater in the drainage of each living space. Is. In FIG. 4, the size of the organic matter cut by the disposer mixed in the waste water is several millimeters. The drainage water of each floor supplied by the drainage pipe 4 is introduced into the inside of the net 60 of the rotary drum first filtration device 61 having an opening of about 0.5 to 1 mm and physically filtered by the net 60. The filtered first treated water 62 is discharged to the outside of the net 60 and stored in the treatment tank 63. The vegetables and food residues cut by the disposer contain a large amount of fine organic matter having a vegetable fragment size of less than 0.5 mm. These organic substances are used in the first filtration device 6
No. 1 cannot be filtered and is mixed in the first treated water 62. The first treated water 62 that has passed through the filtration net in the first filtration device 61
Is guided to the drainage pipe 72 of the purifying device, and the fine organic matter of less than 0.5 mm is aggregated and separated by filtration using a coagulant. This is the same as the processing method described above.

【0038】回転式濾過膜45を通過した処理水の一部
を配管46から配管64で取水し、ホンプ65で加圧し
たのち配管66に導き、前記第一濾過装置61の回転す
る濾過網60の洗浄水68としてノズル67に供給して
使用できるので、前記濾過網60の洗浄水として高価な
上水を使用しなくても良く、運転コストを低減できる効
果がある。
A portion of the treated water that has passed through the rotary filtration membrane 45 is taken from the pipe 46 through the pipe 64, pressurized by the horn 65 and then introduced into the pipe 66, and the rotary filtration net 60 of the first filtration device 61 is rotated. Since the cleaning water 68 can be supplied to the nozzle 67 for use, it is not necessary to use expensive clean water as the cleaning water for the filtration net 60, and the operating cost can be reduced.

【0039】前記第一濾過装置61の洗浄水68と濾過
物は、洗浄受け樋69に落下し、その後傾斜型のスリッ
ト状の開口部を有する傾斜樋70を移動しながら、水が
切られ含水率が低減された残渣汚泥となり、スクリュー
フィーダ(図示せず)等で機械的に配管71に送られ
る。切られた水は傾斜樋70のスリット部から回転網6
0の内側に落下する。配管71中の汚泥は、配管71を
通じてスラッジ槽56に搬入され、有機肥料の原料とな
る。尚、前記第一濾過装置61の濾過網60の洗浄に、
圧縮空気を使用しても良い。
The washing water 68 and the filtered matter of the first filtering device 61 fall into the washing receiving trough 69, and then the water is cut off while moving the inclined trough 70 having the inclined slit-shaped opening. Residual sludge with a reduced rate is mechanically sent to the pipe 71 by a screw feeder (not shown) or the like. The cut water is fed from the slit part of the inclined gutter 70 to the rotary net 6
It falls inside 0. The sludge in the pipe 71 is carried into the sludge tank 56 through the pipe 71 and becomes a raw material for organic fertilizer. In addition, for cleaning the filter net 60 of the first filtration device 61,
Compressed air may be used.

【0040】図5も本発明の他の実施例を備えた洗浄装
置の構成図である。図5において、空気中の空気を圧縮
機72で圧縮して配管73に導き、ノズル74から噴き
つけ、空気流75で回転する濾過網60から濾過した残
渣分を剥離させ、残渣受け樋69に落下させる。本実施
例では、残渣中洗浄水の混入が防止できるので、スラッ
ジ槽56での水分量が低減でき、堆肥化時に必要な水分
の減量運転に必要な、遠心分離機やベルトプレス機等の
脱水手段57での機械的エネルギーの節約や、乾燥ヒー
ターでの熱的エネルギーの節約に効果がある。
FIG. 5 is also a block diagram of a cleaning apparatus having another embodiment of the present invention. In FIG. 5, the air in the air is compressed by the compressor 72, guided to the pipe 73, sprayed from the nozzle 74, the filtered residue is separated from the filter net 60 rotating by the air flow 75, and the residue receiving trough 69 is provided. Let it fall. In this embodiment, since the cleaning water in the residue can be prevented from being mixed, the amount of water in the sludge tank 56 can be reduced, and dehydration of a centrifugal separator, a belt press, etc., which is necessary for the operation of reducing the amount of water required for composting. It is effective in saving mechanical energy in the means 57 and thermal energy in the dry heater.

【0041】また、図5に示すように、従来のマンショ
ン等の居住空間内での生活廃水系では、トイレの排水系
Aと台所、風呂場の排水系Bは別配管地下に設置した下水
集合槽に集積されていた。このため、台所のディスポー
ザで切断された野菜や料理残渣が混入した廃水は、ビル
内の排水系Aの配管に流されるが、この配管は台所排水
量が少ないため十分に流れなく、配管内に残渣が堆積し
配管が詰まりやすくなる問題があった。しかし、排水系
AとBを統合させることにより、排水系Bはもともと人間
の排泄物を押し流す水量を確保しているので、前記残渣
が配管中に留まることが無く、配管内に残渣が堆積し配
管が詰まらない効果がある。
Further, as shown in FIG. 5, in the conventional domestic wastewater system in a living space such as an apartment, the drainage system of the toilet is used.
A, the kitchen, and the drainage system B in the bathroom were collected in a sewer collection tank installed in a separate pipe basement. For this reason, wastewater mixed with vegetables and cooking residues cut by the kitchen disposer flows into the pipe of the drainage system A in the building, but this pipe does not flow sufficiently because the kitchen drainage is small However, there was a problem that the pipes were easily accumulated and the pipes were easily clogged. However, drainage system
By integrating A and B, the drainage system B originally secures the amount of water that flushes human excrement, so the residue does not stay in the pipe, and the residue does not accumulate in the pipe and the pipe is not clogged. effective.

【0042】以上のごとく、本実施例では、料理の残渣
を居住空間内で除去回収でき、除去回収物を堆肥化でき
るので、生ごみとして居住空間の外で焼却等を行う必要
が無く、生ごみの収集や焼却に関わる経費を節減できる
効果がある。しかも、製造された肥料は、トイレ下水の
ほかに、野菜の皮の部分や、魚の骨の部分が含まれるの
で、トイレ下水汚泥から堆肥化した肥料よりもカルシュ
ウム等多くの肥料成分量を含んでおり、良質の肥料を製
造することができる。これらの肥料は、国内向けを問わ
ず海外の緑化事業向け等にも利用できる。
As described above, in the present embodiment, since the cooking residue can be removed and collected in the living space and the removed collected product can be composted, it is not necessary to incinerate it as living garbage outside the living space, This has the effect of reducing costs related to garbage collection and incineration. Moreover, since the fertilizer produced contains not only toilet sewage but also vegetable skin and fish bones, it contains more fertilizer components such as calcium than fertilizer composted from toilet sewage sludge. And can produce high quality fertilizer. These fertilizers can be used not only for domestic purposes but also for overseas greening projects.

【0043】本発明によれば、ビルやマンション、ホテ
ル及び工場等の多数の人間が居住する建築物などから発
生する下水や生活廃水、料理残さ等が混入した厨房の排
水および工場廃水等を、低コストでかつ良好に浄化し、
下水や生活廃水を再生水としてトイレの選浄水や、緑化
用散水用等に再利用することができる。
According to the present invention, sewage, domestic wastewater, kitchen wastewater, factory wastewater, etc. mixed with sewage, domestic wastewater, cooking residues, etc., generated from buildings such as buildings, condominiums, hotels and factories where many people live, Cleans well at low cost,
It is possible to reuse sewage and domestic wastewater as reclaimed water for selective cleaning of toilets and watering for greening.

【0044】また、回収汚泥を低コストでかつ良好に肥
料化し、農耕地用肥料として汚泥を再利用することがで
きる効果がある。また、下水発生域内で下水浄化処理を
行うので、既存の都市下水処理場の不可を低減でき、か
つ、排水中の有機物を肥料化し、炭素を炭酸ガスとして
大気に放出する量を低減できるので、地球温暖化の防止
につながる。
Further, there is an effect that the recovered sludge can be satisfactorily converted into fertilizer at a low cost and the sludge can be reused as a fertilizer for agricultural land. In addition, since sewage purification treatment is performed within the sewage generation area, it is possible to reduce the possibility of existing urban sewage treatment plants, and to reduce the amount of organic matter in the wastewater that is fertilized and the amount of carbon released to the atmosphere as carbon dioxide, It will help prevent global warming.

【0045】[0045]

【発明の効果】本発明によれば、ビルやマンション等の
多数の人間が居住し、下水や生活廃水および工場廃水等
を低コストでかつ良好に浄化し、下水や生活廃水を再生
水として再利用することができるとともに、回収された
汚泥を低コストでかつ良好な肥料として農耕地に利用で
きる浄化装置を提供できる。
EFFECTS OF THE INVENTION According to the present invention, a large number of people such as buildings and condominiums inhabit, sewage, domestic wastewater, factory wastewater and the like are purified at low cost and well, and sewage and domestic wastewater are reused as recycled water. In addition, it is possible to provide a purification device that can use the recovered sludge as low cost and good fertilizer in agricultural land.

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

【図1】図1は、本発明の一実施例を備えたビル内下水
排水浄化システムの構成図である。
FIG. 1 is a configuration diagram of a sewage drainage purification system in a building including an embodiment of the present invention.

【図2】図2は、本発明の他の実施例を備えた浄化装置
の構成図である。
FIG. 2 is a configuration diagram of a purifying apparatus including another embodiment of the present invention.

【図3】図3は、本発明の他の実施例を備えた浄化装置
の構成図である。
FIG. 3 is a configuration diagram of a purifying device including another embodiment of the present invention.

【図4】図4は、本発明の他の実施例を備えた浄化装置
の構成図である。
FIG. 4 is a configuration diagram of a purifying apparatus including another embodiment of the present invention.

【図5】図5は、本発明の他の実施例を備えた浄化装置
の構成図である。
FIG. 5 is a configuration diagram of a purifying apparatus including another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…ビル、2…トイレ、3…流し台4…排水管、5…地
階、6…浄化装置、8…用水槽、9…ビル壁熱交換器、
13…緑地槽、15…分配管、16…草木、29…舗装
道路、31…貯水槽、35…下水貯槽、37…薬剤供給
装置、39…撹絆槽、44…濾過分離装置、51…磁
石、52…回転円筒体、54…汚泥槽、57…脱水手
段、58…堆肥化槽、61…磁気分離装、64…乾燥加
熱装。
1 ... Building, 2 ... Toilet, 3 ... Sink 4 ... Drain pipe, 5 ... Basement, 6 ... Purification device, 8 ... Water tank, 9 ... Building wall heat exchanger,
13 ... Green tract tank, 15 ... Distribution pipe, 16 ... Plant, 29 ... Paved road, 31 ... Water tank, 35 ... Sewage storage tank, 37 ... Drug supply device, 39 ... Stirring tank, 44 ... Filtration and separation device, 51 ... Magnet , 52 ... Rotating cylinder, 54 ... Sludge tank, 57 ... Dewatering means, 58 ... Composting tank, 61 ... Magnetic separation equipment, 64 ... Dry heating equipment.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西嶋 規世 茨城県土浦市神立町502番地 株式会社日 立製作所機械研究所内 (72)発明者 浅野 克彦 茨城県日立市幸町三丁目1番1号 株式会 社日立製作所原子力事業部内 (72)発明者 大川 令 東京都国分寺市東恋ヶ窪一丁目280番地 株式会社日立製作所研究開発本部内 Fターム(参考) 2D039 DA01 4D015 BA19 BA22 BB12 CA18 DA04 DA16 DA37 DB01 EA06 EA32 EA40 FA01 FA02 FA15 FA24 4D059 AA05 AA07 BB03 BE08 BE15 BE38 BK11 BK12 CA16 CB06 CB27 EB06    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Noriyo Nishijima             502 Kintatemachi, Tsuchiura City, Ibaraki Japan             Tate Seisakusho Mechanical Research Center (72) Inventor Katsuhiko Asano             3-1-1 Sachimachi, Hitachi City, Ibaraki Prefecture Stock Association             Hitachi, Ltd. Nuclear Business Division (72) Inventor Okawa             1-280, Higashikoigakubo, Kokubunji, Tokyo             Hitachi, Ltd. Research & Development Division F-term (reference) 2D039 DA01                 4D015 BA19 BA22 BB12 CA18 DA04                       DA16 DA37 DB01 EA06 EA32                       EA40 FA01 FA02 FA15 FA24                 4D059 AA05 AA07 BB03 BE08 BE15                       BE38 BK11 BK12 CA16 CB06                       CB27 EB06

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】リン等を含む汚濁水を一時保留する排水保
留手段と、排水を前記排水保留手段に収集する排水収集
手段と、前記排水を浄化処理する浄化手段と、前記浄化
処理で発生する汚泥を排水から分離排出する汚泥分離排
出手段と、前記浄化処理で発生する浄化水を排出する手
段とを有する排水浄化装置において、前記浄化手段を凝
集剤を注入して汚濁粒子やリン等を含有するフロックを
形成し、このフロックを分離する凝集分離手段で前記フ
ロックを汚泥として分離排出することを特徴とする排水
浄化装置。
1. A wastewater holding means for temporarily holding polluted water containing phosphorus, a wastewater collecting means for collecting wastewater in the wastewater holding means, a purifying means for purifying the wastewater, and a purification treatment. In a wastewater purifying apparatus having a sludge separating and discharging means for separating and discharging sludge from wastewater, and a means for discharging purified water generated in the purification treatment, the purifying means contains a coagulant and contains pollutant particles, phosphorus, etc. A waste water purifying apparatus, characterized in that the flocs are formed, and the flocs are separated and discharged as sludge by a flocculating separation means for separating the flocs.
【請求項2】前記汚濁水を無薬注処理で濾過する無薬注
濾過手段と、凝集剤を注入して汚濁粒子やリン等を含有
するフロックを形成し、前記フロックを分離する凝集分
離手段で構成することを特徴とする請求項1記載の排水
浄化装置。
2. A non-chemical-injection filtering means for filtering the polluted water in a non-chemical-injection treatment, and an aggregating / separating means for injecting a flocculant to form flocs containing contaminant particles, phosphorus, etc., and separating the flocs. The wastewater purifying apparatus according to claim 1, wherein
【請求項3】前記汚濁水を無薬注処理で濾過する無薬注
濾過手段と、凝集剤、磁性物質を注入して汚濁粒子やリ
ン等を含有する磁性フロックを形成し、前記磁性フロッ
クを分離する凝集分離手段で前記磁性フロックを汚泥と
して磁気分離収集することを特徴とする請求項2記載の
排水浄化装置。
3. A non-chemical-injection filtering means for filtering the polluted water by a non-chemical-injection treatment, and a flocculant and a magnetic substance are injected to form magnetic flocs containing pollutant particles, phosphorus, etc. The waste water purifying apparatus according to claim 2, wherein the floc separation means for separating separates and collects the magnetic flocs as sludge.
【請求項4】前記浄化処理で発生する浄化水を排出する
手段に、植物への給水手段を有することを特徴とする請
求項1記載の排水浄化装置。
4. The waste water purification apparatus according to claim 1, wherein the means for discharging the purified water generated in the purification treatment has a means for supplying water to plants.
【請求項5】前記浄化処理で発生する浄化水を排出する
手段に、土地を冷却もしくは加温する給水手段を有する
ことを特徴とする請求項1記載の排水浄化装置。
5. The waste water purification apparatus according to claim 1, wherein the means for discharging the purified water generated in the purification treatment includes a water supply means for cooling or heating the land.
【請求項6】前記排水収集手段に料理残渣を細かく破砕
し排水する破砕排出手段を有することを特徴とする請求
項1記載の排水浄化装置。
6. The waste water purifying apparatus according to claim 1, wherein the waste water collecting means has a shredding and discharging means for finely shredding and discharging the cooking residue.
【請求項7】前記汚泥回収手段に、回収した汚泥を乾燥
し、200℃以下で熱処理し汚泥含水率を低減する汚泥
乾燥手段を有することを特徴とする請求項1記載の排水
浄化装置。
7. The waste water purification apparatus according to claim 1, wherein said sludge collecting means has sludge drying means for drying the collected sludge and heat-treating it at 200 ° C. or lower to reduce the sludge water content.
【請求項8】前記浄化手段を、前記汚濁水を無薬注処理
で物理的濾過する無薬注濾過手段と、磁性物質を生成す
る凝集剤を注入して汚濁粒子やリン等を含有する磁性フ
ロックを形成し、前記磁性フロックを汚泥として磁気分
離収集することを特徴とする請求項1記載の排水浄化装
置。
8. A non-chemical-injection filtering means for physically filtering the polluted water in a non-chemical-injection treatment, and a magnetic material containing pollutant particles or phosphorus by injecting a flocculant that produces a magnetic substance. The wastewater purifying apparatus according to claim 1, wherein flocs are formed and the magnetic flocs are magnetically separated and collected as sludge.
【請求項9】前記浄化処理で発生する浄化水を排出する
手段に、水洗トイレの洗浄水として使用する給水手段を
有することを特徴とする請求項1記載の排水浄化装置。
9. The waste water purification apparatus according to claim 1, wherein the means for discharging the purified water generated in the purification treatment includes a water supply means used as flush water for flush toilets.
【請求項10】前記浄化処理で発生する浄化水を排出す
る手段に、前記居住空間内や産業生産場の建屋の一部を
冷却するための給水手段を有することを特徴とする請求
項1記載の排水浄化装置。
10. The means for discharging purified water generated by the purification treatment includes a water supply means for cooling a part of the building in the living space or industrial production site. Wastewater purification equipment.
JP2002148498A 2002-05-23 2002-05-23 Apparatus for purifying waste water Pending JP2003340464A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2003340464A true JP2003340464A (en) 2003-12-02

Family

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Country Link
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JP2005193127A (en) * 2004-01-06 2005-07-21 Mitsubishi Rayon Co Ltd Method for withdrawing solid catalyst and reaction equipment for solid catalyst
JP2010538809A (en) * 2007-09-10 2010-12-16 ファーマフィルター ビー.ブイ. Method and system for processing different waste streams
CN103288282A (en) * 2013-06-14 2013-09-11 贵州黔鹰环卫服务有限责任公司 Kitchen wastewater treating equipment
CN108285234A (en) * 2018-03-19 2018-07-17 河南城建学院 A kind of smart home water purification device
CN108358286A (en) * 2018-05-07 2018-08-03 天津工业大学 A kind of magnetic flocculation urban rainwater processing unit and its technique
CN113772875A (en) * 2021-09-28 2021-12-10 安徽四邦环境科技有限公司 Industrial wastewater treatment equipment of safe type
CN114735838A (en) * 2022-05-20 2022-07-12 江苏电子信息职业学院 Heat pump hot water energy-saving device for recovering waste heat and waste water
KR102663184B1 (en) * 2023-07-07 2024-05-03 이병훈 Food waste disposal device

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193127A (en) * 2004-01-06 2005-07-21 Mitsubishi Rayon Co Ltd Method for withdrawing solid catalyst and reaction equipment for solid catalyst
JP2010538809A (en) * 2007-09-10 2010-12-16 ファーマフィルター ビー.ブイ. Method and system for processing different waste streams
KR101540414B1 (en) * 2007-09-10 2015-07-29 파마필터 베.브이. Method and system for treating different waste streams
CN103288282A (en) * 2013-06-14 2013-09-11 贵州黔鹰环卫服务有限责任公司 Kitchen wastewater treating equipment
CN108285234A (en) * 2018-03-19 2018-07-17 河南城建学院 A kind of smart home water purification device
CN108285234B (en) * 2018-03-19 2020-10-09 河南城建学院 Smart home water purification equipment
CN108358286A (en) * 2018-05-07 2018-08-03 天津工业大学 A kind of magnetic flocculation urban rainwater processing unit and its technique
CN113772875A (en) * 2021-09-28 2021-12-10 安徽四邦环境科技有限公司 Industrial wastewater treatment equipment of safe type
CN114735838A (en) * 2022-05-20 2022-07-12 江苏电子信息职业学院 Heat pump hot water energy-saving device for recovering waste heat and waste water
KR102663184B1 (en) * 2023-07-07 2024-05-03 이병훈 Food waste disposal device

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