JPS5861890A - Treatment for sewage - Google Patents

Treatment for sewage

Info

Publication number
JPS5861890A
JPS5861890A JP56159962A JP15996281A JPS5861890A JP S5861890 A JPS5861890 A JP S5861890A JP 56159962 A JP56159962 A JP 56159962A JP 15996281 A JP15996281 A JP 15996281A JP S5861890 A JPS5861890 A JP S5861890A
Authority
JP
Japan
Prior art keywords
sludge
tank
treatment
night soil
mixture
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
JP56159962A
Other languages
Japanese (ja)
Inventor
Kaoru Chigusa
千種 薫
Yutaka Takemoto
竹本 裕
Takashi Ito
伊東 崇
Ikuko Hayashi
林 郁子
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.)
Nishihara Environment Co Ltd
Original Assignee
Nishihara Environmental Sanitation Research Corp
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 Nishihara Environmental Sanitation Research Corp filed Critical Nishihara Environmental Sanitation Research Corp
Priority to JP56159962A priority Critical patent/JPS5861890A/en
Publication of JPS5861890A publication Critical patent/JPS5861890A/en
Pending 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

Abstract

PURPOSE:To treat law night soil and the sludge in a purifying tank simultaneously by settling and separating the activated sludge in a liquid mixture after aeration of the night soil, returning part thereof to the aeration treatment and aerating the sludge in an inflow purifying tank and the excess sludge mixture. CONSTITUTION:After law night soil receives pretreatments such as settling in a pretreating tank 1, the night soil is stored in a storage tank 2, from which the same is introduced into a tank 3 for primary treatment where the night soil receives an anaerobic or aerobic digestion treatment. The liquid after the primary treatment is fed together with diluting water to a tank 4 for secondary treatment, where the liquid receives secondary treatment by aeration and is fed into a settling tank 5 so that the liquid is subjected to the sepn. of activated sludge. The sludge of the purifying tank treated together with the low night soil is treated in a pretreatment tank 6, thereafter the sludge is stored in a storage tank 7, from which the sludge is fed into an aerating tank 8. In the tank 8, the sludge of the purifying tank and the activated sludge drawn from the tank 5 are mixed, and the mixture is aerated for, for example, about 3 days.

Description

【発明の詳細な説明】 このM明は、生し尿と浄化槽汚泥とを同時に処理する汚
水処理方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to a sewage treatment method that simultaneously treats human waste and septic tank sludge.

し尿逃鳳場に搬入されるし尿浄化槽汚泥は、水洗化人口
の増大にともなって年々その絶対量が増加している。現
行の構造基準によると、浄化槽汚泥1ま前処理を受けて
からいったん貯留され、その後は生し尿と温合されて、
し尿処理施設で混合処理されるようになっている。しか
し浄化槽汚泥は、生し尿と比較してBODなどの含有量
が着るしく少ない丸め、し尿処理施設の運転条件が低負
荷傾向になシやすい、tた浄化槽汚泥の性質は、浄化槽
の形態などによって着るしく異なるので、し尿処理施設
でのII&l14に件が変動し、処理水質が不安定にな
るのを避けられない。
The absolute amount of human waste septic tank sludge delivered to human waste removal sites is increasing year by year as the number of people using water washing increases. According to current structural standards, septic tank sludge undergoes pre-treatment and is then stored, after which it is heated with raw human waste.
It is now mixed and processed at human waste treatment facilities. However, septic tank sludge has a relatively low content of BOD and other substances compared to raw human waste, and the operating conditions of human waste treatment facilities tend to be low-load.The properties of septic tank sludge vary depending on the form of the septic tank. Since the clothes are different, it is inevitable that the situation at the human waste treatment facility will fluctuate and the quality of the treated water will become unstable.

この発明は、し尿処理施設を蝦過条袢のもとて安定に運
転しながら、浄化槽汚泥を効率よく処理することができ
る汚水処理方法を提供することを目的としている。
An object of the present invention is to provide a sewage treatment method that can efficiently treat septic tank sludge while operating a human waste treatment facility stably under a sewage system.

つぎにこの発明方法の工程の一例を図面にしたがって説
明する。図において、処理すべき生し尿は、まず前旭通
槽1内で伊沈などの前処理全党は九のち貯留槽2にいつ
九ん貯留され、適尚な流量で1次処理4113に導入さ
れて、ここで嫌気性または好気性消化処理を受ける。こ
の1次処理を受は九液体は、適量の希釈水とともに2次
処理槽4に送られ、ばっ気による2次処理を受けたのち
、沈殿槽5に送られて活性汚泥の分離が行なわれる。
Next, an example of the steps of the method of this invention will be explained with reference to the drawings. In the figure, the raw human waste to be treated is first treated in the front Asahi tank 1, then all the pre-treatment substances such as Isin are stored in the storage tank 2, and then introduced into the primary treatment 4113 at an appropriate flow rate. Here, they undergo anaerobic or aerobic digestion. After this primary treatment, the liquid is sent to the secondary treatment tank 4 along with an appropriate amount of dilution water, where it undergoes secondary treatment by aeration, and then sent to the settling tank 5 where activated sludge is separated. .

そして上澄水は処理水として排出され、活性汚泥の一部
が返送汚泥として2次処理槽4に戻される。
The supernatant water is then discharged as treated water, and a portion of the activated sludge is returned to the secondary treatment tank 4 as return sludge.

、以上の処理は、一般的なし尿゛処理の場合と同、じで
あるので、その詳細な滅明は省略する。
Since the above processing is the same as that of general human waste processing, detailed explanation thereof will be omitted.

一方、生し尿とともに処理される浄化槽汚泥は、前処理
槽6で前処理され九のち貯留槽7に貯留され、つぎのば
っ気貯留槽8に送られる。このばっ気貯留槽8では、貯
留Wi7から送られた浄化槽汚泥と、沈殿槽5から引抜
かれた活性汚泥とが混合され、この混合物が比較的長時
間、たとえは約3日間にわ九ってばっ気される。沈殿槽
7から引抜かれ九直後の活性汚泥は高い生吻学的活性を
保有しているので、この活性汚泥と混性された浄化槽汚
泥は、ばっ気を受けながら浄化され、そして凝集性およ
び沈降性のすぐれた汚泥を生成する。
On the other hand, the septic tank sludge that is treated together with human waste is pretreated in a pretreatment tank 6, then stored in a storage tank 7, and sent to the next aeration storage tank 8. In this aeration storage tank 8, the septic tank sludge sent from the storage Wi7 and the activated sludge pulled out from the settling tank 5 are mixed, and this mixture is kept for a relatively long time, for example, about 3 days. I'm exposed. The activated sludge immediately after being pulled out from the settling tank 7 has high anastomological activity, so the septic tank sludge mixed with this activated sludge is purified while being aerated, and the flocculation and sedimentation properties are reduced. Generates sludge with excellent quality.

ばっ気貯貿槽8で所定時間のばっ気処理を受は九浄化槽
汚泥は、−縮槽9に送られ、ここで汚泥の澁縮が行われ
る。そして濃縮汚泥は、つぎの脱水61110でさらに
脱水され九のち、脱水ケーキとして排出される。一方、
―縮槽9及び脱水機10で汚泥から分離された分離液は
、ともに2次処理槽4に導入される。この分離液は、S
Sをほとんど含んでいないばかりでなく、ばっ気貯貿槽
8内で充分にはり気処理されているために、その水質は
有機物ll1tLが璽わめて低く、2次処理槽4に導入
されても、1次旭履を受けたし尿の処理に支障を与える
ことはなく、を九負荷の変動にも殆んど関与しない。
After being aerated for a predetermined period of time in the aeration storage tank 8, the sludge from the septic tank is sent to the shrinkage tank 9, where the sludge is shrunk. The thickened sludge is further dehydrated in the next dewatering step 61110, and then discharged as a dehydrated cake. on the other hand,
- The separated liquid separated from the sludge in the shrinking tank 9 and the dehydrator 10 are both introduced into the secondary treatment tank 4. This separated liquid is S
Not only does it contain almost no S, but also because it has been sufficiently aerated in the aeration storage tank 8, its water quality is extremely low in organic matter. However, it does not interfere with the treatment of human waste that has undergone the primary filtration, and has little influence on fluctuations in the load.

籐1図の工程にしたがって行われた実験に供され良生し
尿および浄化槽汚泥の水質分析値を、沈殿槽5から引抜
いた余剰汚泥のものとあわせて次頁の第1表に示す。
The water quality analysis values of the fresh human waste and septic tank sludge subjected to the experiment conducted according to the process shown in Figure 1 are shown in Table 1 on the next page, together with those of the excess sludge extracted from the settling tank 5.

tたgl@に示し九浄化槽汚泥と余剰汚泥とを3:10
M合でばり気貯留榴8に流入させ、3日間にわたってば
っ気し友のち汚泥から分離して得た分離液の水質を第2
表に示す。
The ratio of 9 septic tank sludge and excess sludge shown in ttagl@ is 3:10.
The water quality of the separated liquid obtained by flowing it into the sludge storage tank 8 and aerating it for 3 days was then separated from the sludge.
Shown in the table.

第   1   表 #12表 第21!&から明らかなように、2次処理槽4に導入さ
れる分離液の水質はきわめて良好であシ、そしてこの水
質は流入浄化槽汚泥の性状にはとんと影響されずKはぼ
一定である。このため一連のし尿処環条件が浄化槽汚泥
側の条件で左右されることがなくなり、常に安定した処
理を行うことができる。
Table 1 #12 Table 21! As is clear from &, the water quality of the separated liquid introduced into the secondary treatment tank 4 is extremely good, and this water quality is not affected by the properties of the inflowing septic tank sludge, and K is almost constant. Therefore, the series of human waste treatment conditions are not influenced by the conditions on the septic tank sludge side, and stable treatment can be performed at all times.

以上のようにこの発明方法においては、浄化槽汚泥は、
し尿処理プロセスの1次処理工程に生し尿とと4に導入
される従来の方法とは異な9、し尿処理プロセスで得ら
れ九余剰汚泥と混合されたのちにあらかじめはり気処通
され、さらに汚泥を分離し要分離液の形態で、し尿処理
プロセスのばっ気部層工程に導入される。シ九がって浄
化槽汚泥の流入量やそのvk状が変動しても、し尿処理
プロセスがその影響上受けることはなくなり、常に安定
した処理水質が確保される。
As described above, in the method of this invention, the septic tank sludge is
Unlike the conventional method in which human waste is introduced into the primary treatment step of the human waste treatment process, the raw human waste is mixed with surplus sludge obtained in the human waste treatment process, and then passed through an aeration chamber in advance. The sludge is separated and the separated liquid is introduced into the aeration stage of the human waste treatment process. Even if the amount of inflow of septic tank sludge or its vk condition changes over time, the human waste treatment process will not be affected by this, and a stable treated water quality will always be ensured.

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

図はこの発明方法の工程の一例を示すフローシートであ
る。 1・・・前処理槽、2・・・貯留槽、6・・・1次処埴
檜、4・・・2次処理槽、5・・・沈殿槽、6・・・前
処理槽、7・・・貯留槽、8・・・ばり気貯留槽、9・
・・淡縮槽、1゜・・・脱水機。
The figure is a flow sheet showing an example of the steps of the method of this invention. 1... Pretreatment tank, 2... Storage tank, 6... Primary treatment hinoki, 4... Secondary treatment tank, 5... Sedimentation tank, 6... Pretreatment tank, 7 ...Storage tank, 8...Flash storage tank, 9.
... desalination tank, 1° ... dehydrator.

Claims (2)

【特許請求の範囲】[Claims] (1)シ尿をばり気処理するばつ気#l&通工程と、こ
のばり気Ja通工場な−た温合液中に含まれている活性
汚泥を沈殿分離する沈殿工程と、分離され良活性汚泥の
一部を上記ばり気逃理に返送し、残余を余剰汚握として
取り出す工程と、流入浄化槽汚泥と上記余剰汚泥との混
合物をば9気処履する工程と、ばつ馬処鳳された上記混
合物からm浄物を分離し、分離tt−上記ばり気処通工
楊に送る工―とからなる汚水処理方法。
(1) The aeration process in which the human waste is aerated, the precipitation process in which the activated sludge contained in the heated mixture is separated by precipitation, and the activated sludge is separated and activated. A step in which a part of the sludge is returned to the above-mentioned flash relief and the remainder is taken out as surplus sludge, a step in which the mixture of the inflow septic tank sludge and the above-mentioned surplus sludge is treated with air, and A sewage treatment method comprising the steps of separating m-purified matter from the above-mentioned mixture and sending it to the above-mentioned flash treatment facility.
(2)上記流入浄化槽汚泥と上記余剰汚泥との混合比が
約s=1である特許請求の範囲第1項記載の汚水処理方
法。
(2) The sewage treatment method according to claim 1, wherein the mixing ratio of the inflow septic tank sludge and the excess sludge is about s=1.
JP56159962A 1981-10-07 1981-10-07 Treatment for sewage Pending JPS5861890A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56159962A JPS5861890A (en) 1981-10-07 1981-10-07 Treatment for sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56159962A JPS5861890A (en) 1981-10-07 1981-10-07 Treatment for sewage

Publications (1)

Publication Number Publication Date
JPS5861890A true JPS5861890A (en) 1983-04-13

Family

ID=15704968

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56159962A Pending JPS5861890A (en) 1981-10-07 1981-10-07 Treatment for sewage

Country Status (1)

Country Link
JP (1) JPS5861890A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318251A (en) * 1976-07-31 1978-02-20 Hachiya Kougiyou Kk Treating method of sludge of excrement and purifying tank
JPS5435414A (en) * 1977-08-22 1979-03-15 Chronister Clyde H Selffoperated fluid seal valve
JPS56126498A (en) * 1980-03-10 1981-10-03 Ebara Infilco Co Ltd Treatment of sludge in night soil purifying tank

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318251A (en) * 1976-07-31 1978-02-20 Hachiya Kougiyou Kk Treating method of sludge of excrement and purifying tank
JPS5435414A (en) * 1977-08-22 1979-03-15 Chronister Clyde H Selffoperated fluid seal valve
JPS56126498A (en) * 1980-03-10 1981-10-03 Ebara Infilco Co Ltd Treatment of sludge in night soil purifying tank

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