JPS6034799A - Treating apparatus for filthy water derived from night soil - Google Patents

Treating apparatus for filthy water derived from night soil

Info

Publication number
JPS6034799A
JPS6034799A JP58142684A JP14268483A JPS6034799A JP S6034799 A JPS6034799 A JP S6034799A JP 58142684 A JP58142684 A JP 58142684A JP 14268483 A JP14268483 A JP 14268483A JP S6034799 A JPS6034799 A JP S6034799A
Authority
JP
Japan
Prior art keywords
treatment
dehydrator
tank
liquid
compost
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
JP58142684A
Other languages
Japanese (ja)
Inventor
Masatoshi Koseki
小関 正敏
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP58142684A priority Critical patent/JPS6034799A/en
Publication of JPS6034799A publication Critical patent/JPS6034799A/en
Pending legal-status Critical Current

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  • Treatment Of Biological Wastes In General (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To perform complete treatment of night soil and to recover useful resource effectively by providing a biological treatment means for treating liquid from a dehydrator biologically and a compost fertilizing tank, etc. for fertilizing solid from the dehydrator to compost. CONSTITUTION:Flocculated liquid from a flocculation tank 2 is fed to belt press type dehydrator 6 in the next stage in which the dehydrator is rotated with a part of two sheets of endless filter cloth 5, 5 overlapped on each other and rotated, and the flocculated liquid is poured into the dehydrator between the filter cloths and pressed at the overlapped part of the filter cloths, to perform separation of solid from liquid. The filtrate from the dehydrator 6 is conducted to a biological treating means 9 comprising an aeration tank 7 and a precipitate separation tank 8, where it is treated biologically. Since the content of SS type BOD component in the raw water for this biological treatment is small, remarkably efficient treatment is possible as compared to usual treatment using activated sludge. Biological treatment other than aerobic treatment is also possible to perform nitration-denitrification treatment, or anaerobic treatment, etc.

Description

【発明の詳細な説明】 この発明は、し尿またはし尿の他に家庭用浄化槽などの
浄化槽から発生する浄化槽汚泥などのし原糸の汚水(以
下単に「し尿」という)を処理する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for treating human waste or night soil wastewater (hereinafter simply referred to as "human waste") such as septic tank sludge generated from a septic tank such as a household septic tank.

従来、し尿処理は生物処理が主流を占めているが、希釈
水の不足、用地難、放流規制の強化などにより、新しい
し尿処理法が望まれていた。
Conventionally, biological treatment has been the mainstream for treating human waste, but new methods of treating human waste have been desired due to the lack of dilution water, land shortages, and stricter discharge regulations.

そこで本出願人は、先に、生し尿を凝集処理したのち固
液分離し、液分を活性汚泥処理等の生物処理するし尿の
処理方法を提案した。この方法は、生物処理を匝めて効
果的に行なえるなど、従来にない優れたし尿\処理方法
である。
Therefore, the present applicant has previously proposed a method for treating human waste in which human waste is subjected to flocculation treatment, solid-liquid separation is performed, and the liquid is subjected to biological treatment such as activated sludge treatment. This method is an unprecedented and excellent method for treating human waste, as it can be carried out effectively through biological treatment.

しかし、このし尿処理方法からは、脱水固形物の他に、
従来の生物処理と同様に余剰汚泥が発生するので、これ
らをも完全に処理しなければ、し尿処理全一体として、
完全に処理できたということはできない。
However, from this human waste treatment method, in addition to dehydrated solids,
As with conventional biological treatment, excess sludge is generated, so if this is not completely treated, the entire human waste treatment process will be
I cannot say that I have completely processed it.

そこで本発明は、し尿処理全体を完全に行うことを目的
とし、また、脱水固形物から賃源を有効に回収すること
を目的とする。
Therefore, an object of the present invention is to completely perform the entire human waste treatment, and also to effectively recover waste from the dehydrated solids.

し尿処理において、生し尿に凝集剤を添加し、M液分離
した際に発生する固形物の熱量は極めテ尚<、また、機
械的脱水性が優れているという特長がある。しかも、こ
の固形物は、窒素やリンの含有量が多いので、堆肥の資
材として優れた性質をもっている。
In human waste treatment, when a flocculant is added to human waste and the M liquid is separated, the amount of heat of the solid material generated is extremely low, and it also has the advantage of excellent mechanical dehydration properties. Furthermore, this solid material has a high content of nitrogen and phosphorus, so it has excellent properties as a material for compost.

また、固液分離した際の液分は、懸濁性のBODが除去
されているので、生物による分解除去が速やかに行なわ
れるという利益がある。
Furthermore, since suspended BOD has been removed from the liquid after solid-liquid separation, there is the advantage that it can be quickly decomposed and removed by living organisms.

本発明は、このような固液分離した際に得られる固形分
シ、液分の清秋を巧みに利用して、全体としてのし尿処
理を完全に行うようにしたものであって、し尿系汚水に
凝集剤を添加して凝集処理を行う凝集処理槽と、該凝集
処理槽からの凝集処理液を機械的脱水処理する脱水機と
、該脱水機からの液分を生物学的に処理するための生物
処理手段と、前記脱水処理手段からの固形分を堆肥発酵
させるための堆肥発酵槽と、前記生物処理手段から発生
する汚泥を凝集処理槽へ返送する系とを有することを特
徴とする。
The present invention skillfully utilizes the solid content and liquid content obtained during solid-liquid separation to completely process human waste as a whole. A flocculation treatment tank for performing flocculation treatment by adding a flocculant to the flocculation treatment tank, a dehydrator for mechanically dehydrating the flocculation treatment liquid from the flocculation treatment tank, and a biological treatment for the liquid from the dehydration machine. It is characterized by having a biological treatment means, a compost fermentation tank for compost fermenting the solid content from the dehydration treatment means, and a system for returning the sludge generated from the biological treatment means to the flocculation treatment tank.

以下、本発明を図示の実施例に従って説明する。Hereinafter, the present invention will be explained according to illustrated embodiments.

図は、本発明の系統図である。図においてlは、スクリ
ーンを示し、生し尿はこのスクリーン1により、夾雑物
が分離除去されて、凝集処理槽2に受け入れられる。凝
集処理槽2では、生し尿に無機凝集剤および有機凝集剤
を凝集剤添加手段3から添加し、後述する生物処理手段
からの返送汚泥も加えて攪拌混合される。そして、懸濁
物質(SS)を凝集・フロック化させる。
The figure is a system diagram of the present invention. In the figure, l indicates a screen, and impurities are separated and removed from the human waste by this screen 1, and the raw human waste is received in a coagulation treatment tank 2. In the flocculation treatment tank 2, an inorganic flocculant and an organic flocculant are added to the human waste from the flocculant addition means 3, and sludge returned from the biological treatment means to be described later is also added and mixed with stirring. Then, the suspended solids (SS) are aggregated and formed into flocs.

ここで用いられる凝集処理槽としては、攪拌器4を有す
る周知の凝集反応槽をそのまま利用することができる。
As the flocculation treatment tank used here, a well-known flocculation reaction tank having an agitator 4 can be used as is.

使用する凝集剤は、無機凝集剤と有機凝集剤を併用する
ことなく、どちらかを単独使用してもよく、要は原液の
性情に合わせて適宜選択するようにするとよい。
The flocculant to be used may be an inorganic flocculant or an organic flocculant, and either one may be used alone, and the flocculant should be appropriately selected depending on the properties of the stock solution.

無機凝集剤としては、塩化アルミニウム、ポリ塩化アル
ミニウム、硫酸アルミニウム、塩化鉄(■)、硫酸鉄(
■)、塩化コノバラス、ポリ塩化鉄、ポリ硫酸鉄などが
あり、これらの1種又は複数の使用が可能である。
Inorganic flocculants include aluminum chloride, polyaluminum chloride, aluminum sulfate, iron chloride (■), and iron sulfate (
(2), conobalous chloride, polyferric chloride, polyferric sulfate, etc., and it is possible to use one or more of these.

有機凝集剤としては、ジメチルアミンエチルメタクリレ
ートの酸塩または第四級アンモニウム塩の単独重合体、
またはアクリルアミドなどの他のモノマーとの共重合体
、ポリアクリルアミドのマンニッヒ変性物またはホフマ
ン分解物、ポリビニルイミダシリン、ポリジアルキルジ
アリルアンモニウム あるいはポリアクリルアミド、ポリアクリルアミド部分
加水分解物、ポリアクリル酸ナトリウムなどのノニオン
またはアニオン性ポリマーの1種または複数を使用する
ことができる。
As the organic flocculant, a homopolymer of dimethylamine ethyl methacrylate acid salt or quaternary ammonium salt,
or copolymers with other monomers such as acrylamide, Mannich-modified or Hofmann decomposition products of polyacrylamide, polyvinylimidacillin, polydialkyl diallylammonium or polyacrylamide, polyacrylamide partial hydrolyzate, sodium polyacrylate, etc. One or more nonionic or anionic polymers can be used.

凝集処理槽2からの凝集液は、次の無端状の二枚の戸布
5,5の一部が重なり合いながら回動し、との炉布間に
凝集液を流し込み、重なり合った部分で加圧するベルト
プレス型の脱水機6に送られて、固液分離処理が施こさ
れる。脱水機としでは、この他にデカンタ−、スクリュ
ウプレスあるいはフィルタープレスなどの公知の機械的
に脱水するものが使用可能である。しかし、ベルトプレ
ス型脱水機とフィルタープレスのように、炉布を用いて
高圧で脱水する機構のものは、被脱水物が繊維質を含ん
でいるので、脱水しやすい。したがって、ベルトプレス
型脱水機またはフィルタープレスを用いるときは、脱水
ケーキの含水率が低いために、そのケーキをそのまま堆
肥発酵できる利益がある。
The flocculating liquid from the flocculating treatment tank 2 is rotated while partially overlapping the next two endless furnace cloths 5, 5, and the flocculating liquid is poured between the furnace cloths and pressurized at the overlapping part. It is sent to a belt press type dehydrator 6 and subjected to solid-liquid separation treatment. As the dehydrator, other known mechanical dehydrators such as a decanter, screw press, or filter press can be used. However, in systems such as belt press type dehydrators and filter presses, which dehydrate at high pressure using furnace cloth, the material to be dehydrated contains fibers, so dehydration is easy. Therefore, when a belt press type dehydrator or filter press is used, since the water content of the dehydrated cake is low, there is an advantage that the cake can be composted and fermented as it is.

脱水機からの液分、すなわちFD.は、次の曝気槽7、
沈殿分離槽8からなる生物処理手段9に導ひかれ、生物
処理を受ける。この生物処理の原水は、SS性のBOD
成分が少ないため、通常の活性汚泥処理に比べて格段に
効率よく行うことができる。壕だ、生物処理として、好
気性処理の他に、生物学的に望素成分も除去可能な硝化
脱窒処理、あるいは嫌気性処理も可能であって、この場
合も従来の88を含むものと比べ、処理効率は高い。
The liquid from the dehydrator, namely FD. is the following aeration tank 7,
It is led to a biological treatment means 9 consisting of a sedimentation separation tank 8 and undergoes biological treatment. The raw water for this biological treatment is SS BOD.
Since there are fewer components, it can be carried out much more efficiently than normal activated sludge treatment. As a biological treatment, in addition to aerobic treatment, nitrification and denitrification treatment, which can biologically remove desirable components, or anaerobic treatment are also possible, and in this case, the conventional 88 is also included. Comparatively, processing efficiency is high.

生物処理手段からは、余剰汚泥が発生するので、これを
前述した凝集処理槽2に系9から返送する。したがって
、別個に汚泥処理装置を必要としない。
Excess sludge is generated from the biological treatment means, and is returned from the system 9 to the aggregation treatment tank 2 described above. Therefore, a separate sludge treatment device is not required.

沈殿分離槽8からの上澄水は、消毒処理を受けて放流さ
れる。場合によっては、濾過処理その他の三次処理を施
こしたのち放流してもよい。
The supernatant water from the sedimentation separation tank 8 is disinfected and discharged. Depending on the case, the water may be discharged after being subjected to filtration treatment or other tertiary treatment.

さて、脱水機6からの固形分は、堆肥発酵槽10に送ら
れる。この堆肥発酵槽は、縦型の槽を多段に仕切って、
多段の発酵室11を構成し、各段に堆肥原料をすき返え
す攪拌混合機12を有するとともに、各段に空気を供給
して、通気条件下に堆肥発酵させる多段発酵槽である。
Now, the solid content from the dehydrator 6 is sent to the compost fermentation tank 10. This compost fermentation tank is a vertical tank divided into multiple stages.
This is a multi-stage fermenter that has a multi-stage fermentation chamber 11, each stage has an agitation mixer 12 for re-throwing the compost raw material, and air is supplied to each stage to carry out compost fermentation under aerated conditions.

ここにおける堆肥発酵は、し尿を直接脱水して得られた
ものなので、通常のし尿処理場などから発生する余剰汚
泥を脱水して得られるケーキを原料とするものよりも熱
量が多い。したがって、堆肥発酵に際しては、十分に発
熱するので、別個に加熱手段を必要とすることなく、堆
肥発酵が可能である。
Since the compost fermentation here is obtained by directly dehydrating human waste, it has a higher calorific value than the one made from cake obtained by dehydrating surplus sludge generated from ordinary human waste processing plants. Therefore, during compost fermentation, sufficient heat is generated, so compost fermentation can be performed without requiring a separate heating means.

堆肥発酵に際し、脱水固形物の含水率が75係を越える
ような場合は、おが屑あるいは、発酵済みの堆肥などの
添加物を混入して60係程度まで水分調整するか、また
は、所望の含水率になるまでロータリーキルンなどの公
知の乾燥機を用いて水分調整してから、堆肥発酵槽に入
れると、通気が良好に維持され、堆肥発酵が効果的に行
なわれるので好ましい。特に、脱水機としてデカンタ−
を用いた場合は、このような水分調整することが重重し
い。
During compost fermentation, if the moisture content of the dehydrated solid material exceeds 75%, add additives such as sawdust or fermented compost to adjust the moisture content to about 60%, or adjust the moisture content to the desired moisture content. It is preferable to adjust the moisture content using a known dryer such as a rotary kiln until the mixture reaches 100%, and then place it in the compost fermentation tank, as this will maintain good aeration and allow effective compost fermentation. In particular, a decanter can be used as a dehydrator.
When using , it is difficult to adjust the moisture content like this.

なお、この図では省略しであるが、公知の堆肥発酵のと
きと同様に、脱水物を堆肥発酵槽10へ投入する際は、
通気が均一にゆきわたって、発酵が効果的に進行するよ
うに、固形物を小さな粒状あるいは塊状に粉砕する粉砕
手段を介在させである。
Although not shown in this figure, when introducing the dehydrated material into the compost fermentation tank 10, as in the case of known compost fermentation,
A pulverizing means for pulverizing the solids into small particles or lumps is provided so that the aeration is uniform and the fermentation proceeds effectively.

また、堆肥発酵槽の形式としては、多段発酵堆肥発酵槽
がそのまま適用できる。
Furthermore, as the type of compost fermentation tank, a multi-stage fermentation compost fermentation tank can be applied as is.

堆肥発酵槽10の下部から排出される堆肥は、ベルトコ
ンベヤーで搬出され、一定期間野積して熟成後、畑地な
どの農地に還元される。
The compost discharged from the lower part of the compost fermentation tank 10 is carried out by a belt conveyor, piled up in the open for a certain period of time, matured, and then returned to agricultural land such as a field.

この堆肥発酵槽10から得られる堆肥は、生し尿を直接
脱水して得られた固形物を原料としているため、従来の
余剰汚泥を原料とするものよりも、窒素やリン成分を多
く含み、施肥効果の優れた堆肥ということができる。
Since the compost obtained from this compost fermentation tank 10 is made from solid matter obtained by directly dehydrating raw human waste, it contains more nitrogen and phosphorus components than the conventional material made from surplus sludge, and is used as a fertilizer. It can be said to be highly effective compost.

以上のように、本発明は生し尿に凝集剤を添加して脱水
機で固液分離し、液分のみを生物処理するため、効率よ
く生物処理できるとともに、固形分を堆肥発酵させるた
めに、し尿処理全体として、処理の完全化が図れる。ま
た、施設効果の優れた堆肥が得られるため、資源の回1
1又(Vも役立つし尿処理装置である。
As described above, in the present invention, a flocculant is added to raw human waste, the solid-liquid is separated using a dehydrator, and only the liquid is subjected to biological treatment, so that it can be efficiently biologically treated, and the solid content can be fermented into compost. Overall human waste treatment can be completed. In addition, since compost with excellent facility efficiency can be obtained, the number of resource cycles is reduced.
1-pronged (V) is also a useful human waste disposal device.

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

図面は、本発明の一実施例を示す系統図でろって、2は
凝集処理槽、6は脱水機、9(末生物処理手段及び10
は堆肥発酵槽を示す。 特許出願人 栗田工業株式会社
The drawing is a system diagram showing one embodiment of the present invention, in which 2 is a flocculation treatment tank, 6 is a dehydrator, 9 is a waste biological treatment means, and 10 is a system diagram showing an embodiment of the present invention.
indicates a compost fermenter. Patent applicant Kurita Industries Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] し尿系汚水に凝集剤を添加して凝集処理を行う凝集処理
槽と、該凝集処理槽からの凝集処理液を機械的に脱水処
理する脱水機と、該脱水機からの液分を生物学的に処理
するための生物処理手段と、前記脱水処理手段からの固
形分を堆肥発酵させるための堆肥発酵槽と、前記生物処
理手段から発生する汚泥を凝集処理槽へ返送する系とを
有するし尿系汚水の処理装置。
A flocculation treatment tank that performs flocculation treatment by adding a flocculant to night soil wastewater, a dehydrator that mechanically dehydrates the flocculation treatment liquid from the flocculation treatment tank, and a biological A human waste system comprising: a biological treatment means for treating sludge; a compost fermentation tank for compost fermenting the solid content from the dehydration treatment means; and a system for returning sludge generated from the biological treatment means to a flocculation treatment tank. Sewage treatment equipment.
JP58142684A 1983-08-04 1983-08-04 Treating apparatus for filthy water derived from night soil Pending JPS6034799A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58142684A JPS6034799A (en) 1983-08-04 1983-08-04 Treating apparatus for filthy water derived from night soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58142684A JPS6034799A (en) 1983-08-04 1983-08-04 Treating apparatus for filthy water derived from night soil

Publications (1)

Publication Number Publication Date
JPS6034799A true JPS6034799A (en) 1985-02-22

Family

ID=15321115

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58142684A Pending JPS6034799A (en) 1983-08-04 1983-08-04 Treating apparatus for filthy water derived from night soil

Country Status (1)

Country Link
JP (1) JPS6034799A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0352700A (en) * 1989-07-18 1991-03-06 Ebara Infilco Co Ltd Treatment of sewage of night soil system
JPH0420708U (en) * 1990-06-11 1992-02-21
JPH06312199A (en) * 1992-08-31 1994-11-08 Gunma Hoola Kk Digestion treatment of organic concentrated sludge by combination of running type stirring machine and wooden biological agent
KR100377947B1 (en) * 2000-11-17 2003-03-29 한국과학기술연구원 Aqua-composting BNR Device and Method for Clearing Wastewater Employing the Same
JP2003095769A (en) * 2001-09-20 2003-04-03 Seihachiro Miura Method of manufacturing compost fertilizer
JP2003238278A (en) * 2002-02-12 2003-08-27 Seihachiro Miura Method of composting sewer sludge
JP2020058979A (en) * 2018-10-10 2020-04-16 日本仮設株式会社 Sludge dehydration device
CN112010511A (en) * 2020-09-09 2020-12-01 福建环球环保科技发展有限公司 Small complete equipment for treating production wastewater and treatment process thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0352700A (en) * 1989-07-18 1991-03-06 Ebara Infilco Co Ltd Treatment of sewage of night soil system
JPH0420708U (en) * 1990-06-11 1992-02-21
JPH06312199A (en) * 1992-08-31 1994-11-08 Gunma Hoola Kk Digestion treatment of organic concentrated sludge by combination of running type stirring machine and wooden biological agent
KR100377947B1 (en) * 2000-11-17 2003-03-29 한국과학기술연구원 Aqua-composting BNR Device and Method for Clearing Wastewater Employing the Same
JP2003095769A (en) * 2001-09-20 2003-04-03 Seihachiro Miura Method of manufacturing compost fertilizer
JP2003238278A (en) * 2002-02-12 2003-08-27 Seihachiro Miura Method of composting sewer sludge
JP2020058979A (en) * 2018-10-10 2020-04-16 日本仮設株式会社 Sludge dehydration device
CN112010511A (en) * 2020-09-09 2020-12-01 福建环球环保科技发展有限公司 Small complete equipment for treating production wastewater and treatment process thereof

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