JPH0474077B2 - - Google Patents

Info

Publication number
JPH0474077B2
JPH0474077B2 JP18812981A JP18812981A JPH0474077B2 JP H0474077 B2 JPH0474077 B2 JP H0474077B2 JP 18812981 A JP18812981 A JP 18812981A JP 18812981 A JP18812981 A JP 18812981A JP H0474077 B2 JPH0474077 B2 JP H0474077B2
Authority
JP
Japan
Prior art keywords
aeration
human waste
centrifugal
sludge
centrifugal filtration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP18812981A
Other languages
Japanese (ja)
Other versions
JPS5889995A (en
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 filed Critical
Priority to JP56188129A priority Critical patent/JPS5889995A/en
Publication of JPS5889995A publication Critical patent/JPS5889995A/en
Publication of JPH0474077B2 publication Critical patent/JPH0474077B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 この発明はし尿処理において、曝気処理工程以
後の汚泥混合液から汚泥を回収する遠心過工
程,曝気槽にし尿を投入するし尿投入工程及び放
流水を得るための遠心分離工程を、昼間の作業時
間帯に行うし尿処理方法の改良に関するものであ
る。
Detailed Description of the Invention The present invention relates to human waste treatment, which includes a centrifugal filtration step for recovering sludge from a sludge mixture after the aeration treatment step, a human waste input step for introducing human waste into an aeration tank, and a centrifugal separation for obtaining effluent water. The present invention relates to an improvement in a human waste disposal method in which the process is carried out during daytime working hours.

従来のし尿処理方法として、例えば第1図に示
す処理方法が実施されている。このような方法を
実施している処理場では、最終沈殿池での処理が
良好に行なわれているか否かが問題となる。特に
小規模の処理場では作業員のいない夜間に放流水
質が悪化した場合等に朝まで全く対処策が講じら
れず、水質の悪い処理水を放流したり、処理機能
が害されることもあつた。
As a conventional human waste treatment method, for example, the treatment method shown in FIG. 1 has been implemented. In treatment plants implementing such methods, the question is whether the treatment in the final sedimentation tank is being carried out satisfactorily. In particular, at small-scale treatment plants, if the quality of discharged water deteriorated during the night when no workers were present, no countermeasures were taken until the morning, resulting in the discharge of poor-quality treated water or the treatment function being impaired. .

この発明は上記の欠点を解消するため、曝気処
理工程は連続運転としても、入手を必要とする遠
心過工程,し尿投入工程及び遠心分離工程を昼
間の作業時間帯に、それぞれ効率よくなされるよ
うに、各工程のサイクルを定めたし尿処理方法を
提供することを目的とする。
In order to solve the above-mentioned drawbacks, this invention aims to efficiently carry out the centrifugal filtration process, human waste feeding process, and centrifugal separation process during the daytime working hours, even though the aeration process can be operated continuously. The object of the present invention is to provide a human waste treatment method in which the cycles of each step are determined.

以下、この発明の一実施例について第2図から
第6図を参照して説明する。
An embodiment of the present invention will be described below with reference to FIGS. 2 to 6.

この発明の一実施例の工程には第2図に示すよ
うに、バキユームカーからし尿を受け入れ、し尿
中の砂等を除去する仮受槽1と、この砂等の除去
されたし尿を貯留する貯留槽2と、この貯留槽2
からのし尿の夾雑物を除去するスクリーン3と、
夾雑物等が除去されたし尿を曝気する曝気槽4
と、この曝気処理されたし尿を遠心過する遠心
過機5と、さらに遠心分離を行うスクリユーデ
カンタ形の遠心分離機6とが配置されている。
As shown in FIG. 2, the process of an embodiment of the present invention includes a temporary receiving tank 1 that receives human waste from a vacuum car and removes sand, etc. from the human waste, and a storage tank that stores the human waste from which sand and other substances have been removed. 2 and this storage tank 2
A screen 3 for removing impurities from human human waste;
Aeration tank 4 that aerates the human waste from which impurities have been removed
A centrifuge 5 for centrifuging the aerated human waste, and a screw decanter type centrifuge 6 for further centrifuging are arranged.

次にこの発明の動作について説明する。処理さ
れるべきし尿は、まず仮受槽1に投入され、沈殿
処理によつて砂等が除去された後、貯留槽2へ送
られる。
Next, the operation of this invention will be explained. Human waste to be treated is first put into a temporary storage tank 1, and after sand and the like are removed by sedimentation, it is sent to a storage tank 2.

その後、貯留槽2からポンプ(図示せず)によ
つてスクリーン3に送られ、夾雑物が除去される
が、このポンプはし尿投入工程の時間帯のとき
(例えば昼間のみの9〜17時の間)のみ稼動する。
Thereafter, the storage tank 2 is sent to the screen 3 by a pump (not shown) to remove impurities, but this pump is only used during the time period of the human waste feeding process (for example, between 9:00 and 17:00 only during the day). only in operation.

次に夾雑物が除去されたし尿は、曝気槽4に送
られ、連続的に曝気処理を受ける。この曝気工程
は単に1つの曝気槽4であつてもよいが、第3図
に示すように脱窒処理を含んでもよい。
Next, the human waste from which impurities have been removed is sent to the aeration tank 4, where it is continuously subjected to aeration treatment. This aeration step may involve only one aeration tank 4, but may also include denitrification treatment as shown in FIG.

さらに、この曝気工程は第5図に示すように曝
気槽4内に生物付着用の材を充填し付着曝気槽
としてもよい。第2図に示すように上記曝気工程
からの汚泥混合液は作業時間内で遠心過機5に
送られ、ここで遠心過されて(遠心過工程)
大部分の固形物が分離される。ここで、遠心過
機5はそれ程目の細かい布を使用せずに、ある
程度のSS分は通過してもよいこととすると、運
転管理が非常に容易となる。
Furthermore, in this aeration step, as shown in FIG. 5, the aeration tank 4 may be filled with a material for biofouling to form an adhesion aeration tank. As shown in Figure 2, the sludge mixture from the aeration process is sent to the centrifuge 5 within the working time, where it is centrifuged (centrifugal filtration process).
Most of the solids are separated. Here, if the centrifugal machine 5 does not use a very fine cloth and allows a certain amount of SS to pass through, the operation management becomes very easy.

そしてこの遠心過工程で分離された濃縮液
(汚泥)は上記曝気槽4へ返送され、再び曝気処
理されることとなるが、この返送によつて曝気槽
4内の微生物量が高濃度で維持できる。
The concentrated liquid (sludge) separated in this centrifugal filtration step is returned to the aeration tank 4 and subjected to aeration treatment again, but this return maintains the amount of microorganisms in the aeration tank 4 at a high concentration. can.

他方、上記遠心過工程で分離された分離液中
には、ある程度(例えば数百mg/)のSSを含
むので、高分子凝集剤を添加し、凝集した後にデ
カンタ形遠心分離機6でSSを除去する(遠心分
離工程)。
On the other hand, since the separated liquid separated in the above-mentioned centrifugation step contains a certain amount (for example, several hundred mg/) of SS, a polymer flocculant is added, and after flocculation, the SS is collected in a decanter type centrifuge 6. removed (centrifugation step).

分離液から凝集したSSを除去する遠心分離機
6はスクリユーデカンタ形のものがよいが固形物
量が少なく、分離液量が大きくなるために、遠心
分離機6のプールの深さを大きく取り、ケーキ排
出口を軸に非常に近い位置とし、低G(例えば
1000G以下)で差速も小さくして運転するとよ
い。
The centrifugal separator 6 that removes the aggregated SS from the separated liquid should preferably be of the screw decanter type, but since the amount of solids is small and the amount of separated liquid is large, the pool of the centrifugal separator 6 should be made large in depth. Place the cake outlet very close to the axis and use a low G (e.g.
1000G or less) and reduce the differential speed.

ここで上記遠心過機5および遠心分離機6の
運転は両者共昼間の作業時間帯の適当な時間(例
えば9〜17時の間)に設定すれば作業性が非常に
良く、しかも、その作動状態を常に監視できるの
で、し尿処理状態を常に良好に保つことができ
る。
Here, if the operation of the centrifuge 5 and the centrifuge 6 is set at an appropriate time during the daytime working hours (for example, between 9:00 and 17:00), the workability is very good. Since it can be constantly monitored, human waste disposal conditions can always be maintained in good condition.

遠心過工程の所要時間は、処理液量及び遠心
過機の容量と台数によつて決められる。
The time required for the centrifugation process is determined by the amount of liquid to be treated and the capacity and number of centrifuges.

そして、入手を要する遠心過工程,し尿投入
工程,遠心分離工程はすべて昼間の作業時間帯で
行うようにしたので全く問題がない。
Furthermore, the centrifugation process, human waste input process, and centrifugation process, which require obtaining raw materials, are all performed during daytime work hours, so there is no problem at all.

第6図は主な処理工程のタイムスケジユールの
一例を示したもので、上から曝気槽の曝気時間、
曝気槽から汚泥混合液の引抜き時間及びし尿の投
入時間を表わしている。
Figure 6 shows an example of the time schedule for the main treatment steps, starting from the top: aeration time of the aeration tank,
It represents the time for drawing out the sludge mixture from the aeration tank and the time for putting in human waste.

即ち、曝気は24時間連続で行い、遠心過機5
の稼動は8〜12時の間に行い、ここで分離した濃
縮汚泥を曝気槽4へ返送、他方分離液は高分子凝
集剤を添加後、遠心分離機6で処理を行う。そし
て上記濃縮汚泥の曝気槽4への返送が終了した後
に12〜14時の間に新たなし尿の投入を行う。
That is, aeration is performed continuously for 24 hours, and centrifugal
is operated between 8:00 and 12:00, and the concentrated sludge separated here is returned to the aeration tank 4, while the separated liquid is treated with a centrifuge 6 after adding a polymer flocculant. After the return of the thickened sludge to the aeration tank 4 is completed, fresh human waste is added between 12:00 and 14:00.

このように処理がなされ、曝気槽では、処理水
の引抜きが終了後にし尿の投入がなされるので処
理水にし尿が短絡されることはない。
The treatment is carried out in this way, and human waste is added to the aeration tank after the withdrawal of the treated water is completed, so that the treated water and human waste will not be short-circuited.

またし尿投入前に槽内は濃縮され、微生物濃度
が高くなつており、しかも有機物も十分に確保で
きるのでF/M比(食物・生物比)の適正化が可
能となり、しかも投入直後は曝気を連続していて
も、豊富な有機物の存在によつて、嫌気的条件と
なり投入開始前までに硝化生成された硝酸態窒素
の脱窒が活発に起こる。
In addition, the inside of the tank is concentrated and the concentration of microorganisms is high before the human waste is added, and since organic matter can also be sufficiently secured, it is possible to optimize the F/M ratio (food/organism ratio). Even if it is continuous, the presence of abundant organic matter creates anaerobic conditions, and active denitrification of nitrate nitrogen, which was produced by nitrification before the start of input, occurs.

尚、し尿の投入及び汚泥混合液の引抜きは昼間
のみに行うので、作業性がよく、しかも、し尿処
理状態を監視することができる。
Incidentally, since the input of human waste and the withdrawal of the sludge mixture are carried out only during the daytime, workability is good and the state of human waste treatment can be monitored.

以上のように、この発明によれば、曝気処理工
程は昼夜連続的に稼動させるが、これに続く遠心
濾過処理工程と遠心分離工程とは作業者による監
視が可能な昼間の作業時間帯で前記曝気処理工程
の槽内水位レベルに応じて運転制御するようにし
たので、前記遠心濾過処理工程および遠心分離工
程の稼動状況を昼間の作業時間帯だけで監視すれ
ばよく、その監視によつて水質管理および汚泥管
理を確実に行うことができ、従つて、作業者によ
る監視が不可能な夜間に水質が悪化した処理水が
放流されるようなことがなくなる。
As described above, according to the present invention, the aeration process is operated continuously day and night, but the subsequent centrifugal filtration process and centrifugal separation process are carried out during the daytime working hours, which can be monitored by the operator. Since the operation is controlled according to the water level in the tank in the aeration process, it is only necessary to monitor the operation status of the centrifugal filtration process and centrifugal separation process during the daytime working hours, and by monitoring the water quality. Management and sludge management can be performed reliably, and therefore treated water with deteriorated water quality will not be discharged at night when monitoring by workers is impossible.

また、前記曝気処理工程の後続処理としては、
前記遠心濾過処理工程と遠心分離工程とによる二
段分離方式としたことにより、遠心濾過処理工程
で余剰汚泥量をコントロールでき、しかも、次の
遠心分離工程では、凝集剤が添加された分離液を
さらに遠心分離することによつて、分離液中の
SS除去が促進され、このため、処理効率は著し
く向上するなどの効果が得られる。
Further, as a subsequent treatment of the aeration treatment step,
By adopting a two-stage separation system consisting of the centrifugal filtration process and the centrifugal separation process, the amount of excess sludge can be controlled in the centrifugal filtration process, and in the next centrifugation process, the separated liquid to which the flocculant has been added can be controlled. By further centrifuging, the
SS removal is promoted, and as a result, effects such as significantly improved processing efficiency can be obtained.

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

第1図は従来のし尿処理方法の工程を示すフロ
ーシート、第2図はこの発明方法の工程を示すフ
ローシート、第3図から第6図は他の実施例を示
すフローシートを示す。 1…仮受槽、2…貯留槽、3…スクリーン、4
…曝気槽、5…遠心過機、6…遠心分離機。
FIG. 1 is a flow sheet showing the steps of a conventional human waste treatment method, FIG. 2 is a flow sheet showing the steps of the method of the present invention, and FIGS. 3 to 6 are flow sheets showing other embodiments. 1...Temporary storage tank, 2...Storage tank, 3...Screen, 4
...Aeration tank, 5...Centrifuge, 6...Centrifugal separator.

Claims (1)

【特許請求の範囲】[Claims] 1 し尿等の高濃度有機性廃水を昼間の作業時間
帯に不連続的に投入し、その高濃度有機性廃水を
昼夜連続的に曝気処理する曝気処理工程と、この
曝気処理工程で得られた汚泥混合液を前記作業時
間帯内に抜き出して遠心濾過し、得られた汚泥を
前記曝気処理工程に返送する遠心濾過処理工程
と、次いでその遠心濾過処理工程で得られた分離
液に凝集剤を添加して、形成された汚泥のフロツ
クを遠心分離して放流水を得る遠心分離工程とを
備え、前記遠心濾過処理工程と次の前記遠心分離
工程とを、前記曝気処理工程の槽内水位レベルに
応じて前記昼間の作業時間帯で運転制御すること
を特徴とするし尿処理方法。
1. An aeration process in which highly concentrated organic wastewater such as human waste is injected discontinuously during daytime working hours, and the highly concentrated organic wastewater is continuously aerated day and night, and the A centrifugal filtration treatment step in which the sludge mixture is extracted during the working time and centrifugally filtered, and the obtained sludge is returned to the aeration treatment step, and then a flocculant is added to the separated liquid obtained in the centrifugal filtration treatment step. and a centrifugal separation step for centrifuging the formed sludge flocs to obtain effluent water, and the centrifugal filtration step and the next centrifugal separation step are performed at a water level in the tank of the aeration step. A human waste disposal method characterized in that the operation is controlled during the daytime working hours according to the above.
JP56188129A 1981-11-24 1981-11-24 Treatment for night soil Granted JPS5889995A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56188129A JPS5889995A (en) 1981-11-24 1981-11-24 Treatment for night soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56188129A JPS5889995A (en) 1981-11-24 1981-11-24 Treatment for night soil

Publications (2)

Publication Number Publication Date
JPS5889995A JPS5889995A (en) 1983-05-28
JPH0474077B2 true JPH0474077B2 (en) 1992-11-25

Family

ID=16218226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56188129A Granted JPS5889995A (en) 1981-11-24 1981-11-24 Treatment for night soil

Country Status (1)

Country Link
JP (1) JPS5889995A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100352243B1 (en) * 1999-12-10 2002-09-16 에스아이비(주) A Treatment Method for Livestock Wastewater
JP6819878B2 (en) * 2017-06-22 2021-01-27 Jfeエンジニアリング株式会社 Treatment methods and equipment for organic sewage containing fibrous substances

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52135560A (en) * 1976-05-10 1977-11-12 Chiyoda Chem Eng & Constr Co Ltd Microbial treating method of waste water
JPS5518156A (en) * 1978-07-25 1980-02-08 Matsushita Electric Ind Co Ltd Speaker
JPS5638190A (en) * 1979-09-06 1981-04-13 Kubota Ltd Treatment of night soil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52135560A (en) * 1976-05-10 1977-11-12 Chiyoda Chem Eng & Constr Co Ltd Microbial treating method of waste water
JPS5518156A (en) * 1978-07-25 1980-02-08 Matsushita Electric Ind Co Ltd Speaker
JPS5638190A (en) * 1979-09-06 1981-04-13 Kubota Ltd Treatment of night soil

Also Published As

Publication number Publication date
JPS5889995A (en) 1983-05-28

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