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JP3797693B2 - Sludge removal method in septic tank sludge - Google Patents
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JP3797693B2 - Sludge removal method in septic tank sludge - Google Patents

Sludge removal method in septic tank sludge Download PDF

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Publication number
JP3797693B2
JP3797693B2 JP34622195A JP34622195A JP3797693B2 JP 3797693 B2 JP3797693 B2 JP 3797693B2 JP 34622195 A JP34622195 A JP 34622195A JP 34622195 A JP34622195 A JP 34622195A JP 3797693 B2 JP3797693 B2 JP 3797693B2
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Japan
Prior art keywords
sludge
septic tank
concentrator
gravity
pretreatment process
Prior art date
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Expired - Fee Related
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JP34622195A
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JPH09150194A (en
Inventor
良則 久芳
徹太郎 木原
正一郎 森谷
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Co Ltd
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
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Priority to JP34622195A priority Critical patent/JP3797693B2/en
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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、浄化槽汚泥を生物学的方法で処理する工程の前処理工程において汚泥を除去する方法に関するものである。
【0002】
【従来の技術】
地域の処理場に集めたし尿や浄化槽汚泥は、夾雑物・砂を除去する前処理工程を経た後に生物学的処理をしてから放流する。生物学的処理を安定した状態で継続するには、原液中に含まれる砂や夾雑物をあらかじめ除去する前処理を十分に行うことが重要である。すなわち、集めたし尿・浄化槽汚泥はまず沈砂槽に投入し、砂を沈降分離する。つぎに、ロータリースクリーンなどの夾雑物除去装置で、紙・布・プラスチックフィルムなどを除去する。沈砂槽で沈降した砂は真空ポンプで吸引して除砂タンクへ送り、水洗した後に焼却したり埋立てに利用したりする。夾雑物除去装置で除去した夾雑物も、スクリュープレスなどの加圧脱水機で脱水し洗浄した後に同様の最終処理をする。
【0003】
ところで、以前はし尿に対する浄化槽汚泥の割合は比較的小さかったため、し尿と浄化槽汚泥とは最初から同一設備で一緒に処理することが多かった。浄化槽汚泥の割合が次第に大きくなるにつれ、前処理工程を二系列とし、し尿と浄化槽汚泥とを別系統で処理することが多くなった。し尿を処理する前処理工程では前記の従来法で処理するが、浄化槽汚泥を処理する前処理工程では夾雑物を除去した後に汚泥を除去する方が全体の工程を合理的なものにすることができるからである。本発明は、浄化槽汚泥を処理する前処理工程において汚泥を除去する方法に関するものである。
【0004】
汚泥の除去方法としては、これまでは沈降分離・浮上分離・遠心分離などが採用されてきた。
【0005】
【発明が解決しようとする課題】
前記の従来の除去方法には、それぞれ次のような問題点があった。沈降分離方式は広大な設置面積を必要とする上、濃縮性能も悪い。浮上分離方式は、設備が複雑で消費電力もやや大きく濃縮性能も悪い。遠心分離方式は、濃縮性能はよくても消費電力が非常に大きい。
【0006】
そこで、設備が簡単で設備費が安く、安定した運転が容易にできて運転費用も安く、しかも分離性能に優れた汚泥除去方法が求められることとなった。本発明が解決しようとする課題は、そのような汚泥除去方法を提供する点にある。
【0007】
【課題を解決するための手段】
本発明に係るものにおいては、運転が昼間だけの前処理工程において円筒スクリーンを垂直に配置した重力式濃縮機で汚泥を捕捉し、運転停止後はそのまま放置して脱水を進行させる。翌日は脱水汚泥を取り除いた後に、運転を再開する。すなわち、運転停止中の時間も有効活用することで、安価で運転費用も安い重力式濃縮機の利用を可能にしたのである。これにより、経済的かつ効率的な汚泥除去を実現できる。
【0008】
【発明の実施の形態】
汚泥の分離性能としては次の2点が要求される。
▲1▼ 原液に含まれる固形物をできるだけ完全に除去すること(除去性能)
▲2▼ 除去した固形物に含まれる水分ができるだけ少ないこと(濃縮性能)
【0009】
ところで、し尿・浄化槽汚泥の受入れは、通常は昼間だけである。このため、前処理工程は昼間だけの断続運転となる。ところが、生物学的処理は、当然に昼夜に渡る連続運転になる。
【0010】
本発明の発明者は、前処理工程の運転が昼間だけの断続運転である点に着目した。そして、円筒スクリーンを備えた重力式濃縮機を用いることにより非常に簡単な装置で容易に目的を達成できることを確認し、本発明を完成させることができた。
【0011】
本発明に係る浄化槽汚泥中の汚泥除去方法は次のようなものである。すなわち、浄化槽汚泥を生物学的方法で処理する工程の前処理工程において、夾雑物を除去した原液に凝集剤を注入した後に円筒スクリーンを垂直に配置した重力式濃縮機で汚泥を除去する工程を設け、前記の生物学的方法で処理する工程は全日の連続運転とするが前処理工程は昼間だけの断続運転とし、重力式濃縮機においては運転停止後は汚泥を捕捉した状態のまま翌日まで放置して汚泥の脱水を進行させ、翌日は重力式濃縮機の脱水汚泥を取り除いてから前処理工程の運転を再開することを特徴とするものである。重力式濃縮機においては、円筒スクリーンの中央に洗浄液を噴出する洗浄管を設けることが望ましい。
【0012】
本発明の実施の形態を説明する。まず、汚泥除去システムについて全体設備の概要を図1に基づいて説明する。原液は沈砂槽1に送り込む。大きい汚泥は沈降し、残りはせきを越えて隣の受入槽2へ流入する。沈砂槽1の底に沈降した汚泥は真空ポンプ13でタンク12へ送り、やがては埋立処分にする。受入槽2内の原液は破砕ポンプ3により夾雑物除去装置4へ送る。夾雑物除去装置4で分離した夾雑物は加圧脱水機5へ移す。加圧脱水機5で脱水した後の固形分は焼却し、液状分は受入槽2へ戻す。他方、夾雑物除去装置4で夾雑物を取り除かれた残りの原液は中継槽6へ送って溜めておく。
【0013】
中継槽6内の原液はポンプ7で重力式濃縮機8へ送るが、重力式濃縮機8への管路には凝集剤の添加ラインを接続している。添加ラインを介してカチオン系高分子凝集剤を添加し、汚泥をフロック状に凝集させて重力式濃縮機8へ供給する。なお、重力式濃縮機8の詳細は後で図2に基づいて説明する。
【0014】
重力式濃縮機8のスクリーンを通過したろ液は貯溜槽10へ送る。貯溜槽10内の液体は貯溜槽ポンプ11によって生物学的処理工程へ回す。
【0015】
ところで、昼間は以上のような作業を続ける。原液中の汚泥は重力式濃縮機8の内部に次第に堆積していく。夜間にはこれらの前処理工程の運転を止めるが、重力式濃縮機8はそのまま放置する。重力式濃縮機8の内部に堆積した汚泥については夜間も更に脱水が進行する。脱水された汚泥は、翌日前処理工程の運転を再開する前に重力式濃縮機8の排出弁を開いて汚泥ポンプ9により排出する。この汚泥は、生物学的処理工程で得られる汚泥と共に焼却などの処理をする。
【0016】
重力式濃縮機8の1例を図2に示している。本体20は縦型容器状として下部はコーンに形成している。外側スクリーン22の内側にやや小径の内側スクリーン23を同心円状に設けた二重スクリーンを本体20の内部中央に配置している。スクリーン22・23は洗浄性に優れた樹脂性の網で製作し、目開きは1mm程度にすることが望ましい。金網で製作してもよい。
【0017】
外側スクリーン22と内側スクリーン23との間は、上下を閉ざして内部をろ液室24としている。ろ液室24の下部には、断面U字形で全体をリング状とした集水容器30を取り付けている。集水容器30の下部に排出管28の一端を取り付け、排出管28の他端は本体20の外へ出している。二重スクリーンの内部中央には上方から垂直に洗浄管25を配置している。洗浄管25の上方にはロータリジョイントを設けて下端には軸受けを設けている。そして、30度程度の角度差を付けながら上下に等間隔で何個かのスプレーノズル26を取り付けている。このようにして自力で回転するようにしているが、電動機などで回転させるようにしてもよい。
【0018】
本体20内には上方から原液供給管29を挿入し、スクリーン22・23を通過する液がなるべく均等な速度になる位置に原液供給管29の流出口を位置させている。本体20の下端に排出弁21を備えた排出口を設け、排出口の上方に洗浄液排出口31を設けている。
【0019】
図2のものは次のように使用する。排出弁21及び洗浄液排出口31を閉じ、原液供給管29から本体20内へ原液を供給していく。構造は簡単ながら、二重スクリーンによるろ過面積は広い。そして、ろ過された固形物はスクリーンの表面上を滑りながら重力で下降していく。スクリーン全体の表面が絶えず更新されるため、長時間に渡ってろ過を続けることができる。本体20内に固形物がある程度堆積したところで原液の供給を止め、そのまま翌日まで放置する。放置状態でもスクリーン22・23でのろ過は継続するため、固形物の濃縮は更に進む。翌日になったら排出弁21を開いて固形物を排出させる。排出が終わったら排出弁を閉じ、洗浄液排出口31を開けて洗浄管25から洗浄液を流す。洗浄液を噴出しながらスプレーノズル26が回転し、スクリーン22・23を洗浄していく。洗浄が終わったら洗浄液の供給を止めて洗浄液排出口31も閉じ、原液供給管29からの原液の供給を再開する。
【0020】
実験で得た汚泥分離性能についての計測結果を次に示す。
中継槽での固形分濃度 13000 mg/リットル
貯溜槽での固形分濃度 760 mg/リットル
濃縮汚泥の固形分濃度 5 %
【0021】
【発明の効果】
本発明に係るものは、設備が安価で運転費用も安くつく。そして、効率的な汚泥除去ができる。
【図面の簡単な説明】
【図1】発明の実施の形態を示すフローシートである。
【図2】図1に示したものの要部を示す縦断面図である。
【符号の説明】
8 重力式濃縮機
20 本体
21 排出弁
22 外側スクリーン
23 内側スクリーン
24 ろ液室
25 洗浄管
26 スプレーノズル
28 排出管
29 原液供給管
30 集水容器
31 洗浄液排出口
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for removing sludge in a pretreatment step of treating septic tank sludge with a biological method.
[0002]
[Prior art]
Human waste and septic tank sludge collected at the local treatment plant are released after biological treatment after passing through a pretreatment process to remove impurities and sand. In order to continue the biological treatment in a stable state, it is important to sufficiently perform a pretreatment for removing the sand and impurities contained in the stock solution in advance. That is, the collected human waste / septic tank sludge is first put into a sand settling tank to separate and separate the sand. Next, paper, cloth, plastic film, etc. are removed with a contaminant removal device such as a rotary screen. The sand that has settled in the sand settling tank is sucked with a vacuum pump and sent to the sand removal tank, where it is washed with water and then incinerated or used for landfill. The contaminants removed by the contaminant removal device are dehydrated and washed by a pressure dehydrator such as a screw press, and then subjected to the same final treatment.
[0003]
By the way, since the ratio of septic tank sludge to human waste was relatively small before, human waste and septic tank sludge were often treated together in the same equipment from the beginning. As the proportion of septic tank sludge gradually increased, the pretreatment process was divided into two lines, and human waste and septic tank sludge were often treated in separate systems. In the pretreatment process for treating human waste, the above-mentioned conventional method is used, but in the pretreatment process for treating septic tank sludge, it is possible to make the whole process more rational by removing the sludge after removing impurities. Because it can. The present invention relates to a method for removing sludge in a pretreatment process for treating septic tank sludge.
[0004]
As a method for removing sludge, sedimentation separation, flotation separation, centrifugation, and the like have been employed so far.
[0005]
[Problems to be solved by the invention]
The conventional removal methods have the following problems. The sedimentation separation method requires a large installation area and has poor concentration performance. The floating separation method is complicated in equipment, consumes a little power and has poor concentration performance. The centrifugal separation method has very high power consumption even though the concentration performance is good.
[0006]
Therefore, there has been a demand for a sludge removal method that is simple in equipment, low in equipment cost, easy in stable operation, low in operating cost, and excellent in separation performance. The problem to be solved by the present invention is to provide such a sludge removal method.
[0007]
[Means for Solving the Problems]
In the present invention, the sludge is captured by a gravity concentrator in which a cylindrical screen is vertically arranged in a pretreatment process in which the operation is only during the daytime. The next day, after dewatered sludge is removed, operation resumes. In other words, by effectively utilizing the time during which the operation was stopped, it was possible to use a gravity concentrator that was inexpensive and low in operating cost. Thereby, economical and efficient sludge removal is realizable.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
The following two points are required for the sludge separation performance.
(1) Remove solids contained in the stock solution as completely as possible (removal performance)
(2) The water content in the removed solid is as low as possible (concentration performance)
[0009]
By the way, human waste and septic tank sludge are usually accepted only in the daytime. For this reason, the pretreatment process is intermittent operation only in the daytime. However, the biological treatment is naturally a continuous operation day and night.
[0010]
The inventor of the present invention has focused on the point that the operation of the pretreatment process is an intermittent operation only in the daytime. Then, it was confirmed that the object could be easily achieved with a very simple device by using a gravity type concentrator equipped with a cylindrical screen, and the present invention could be completed.
[0011]
The sludge removal method in the septic tank sludge according to the present invention is as follows. That is, in the pretreatment step of treating the septic tank sludge with a biological method, the step of removing the sludge with a gravity type concentrator in which a cylindrical screen is vertically arranged after injecting the flocculant into the stock solution from which contaminants have been removed. The pretreatment process is an intermittent operation only during the day, and in the gravity type concentrator, after the operation is stopped, the sludge is captured until the next day. The dehydration of the sludge is allowed to proceed, and the operation of the pretreatment process is resumed after removing the dewatered sludge from the gravity concentrator on the next day. In the gravity type concentrator, it is desirable to provide a cleaning pipe for ejecting the cleaning liquid at the center of the cylindrical screen.
[0012]
An embodiment of the present invention will be described. First, the outline | summary of the whole installation is demonstrated based on FIG. 1 about a sludge removal system. The stock solution is fed into the sand settling tank 1. Large sludge settles and the remainder flows over the cough and flows into the next receiving tank 2. The sludge that has settled at the bottom of the sand settling tank 1 is sent to the tank 12 by the vacuum pump 13 and eventually disposed of in landfill. The stock solution in the receiving tank 2 is sent to the contaminant removal device 4 by the crushing pump 3. The foreign matter separated by the foreign matter removing device 4 is transferred to the pressure dehydrator 5. The solid content after dehydration by the pressure dehydrator 5 is incinerated, and the liquid content is returned to the receiving tank 2. On the other hand, the remaining stock solution from which the contaminants have been removed by the contaminant removal device 4 is sent to the relay tank 6 and stored.
[0013]
The stock solution in the relay tank 6 is sent to the gravity concentrator 8 by the pump 7, and a flocculant addition line is connected to the pipe line to the gravity concentrator 8. A cationic polymer flocculant is added through the addition line, and the sludge is aggregated in a floc form and supplied to the gravity concentrator 8. Details of the gravity concentrator 8 will be described later with reference to FIG.
[0014]
The filtrate that has passed through the screen of the gravity concentrator 8 is sent to the storage tank 10. The liquid in the reservoir 10 is routed to the biological treatment process by the reservoir pump 11.
[0015]
By the way, the above work continues during the day. The sludge in the stock solution gradually accumulates inside the gravity concentrator 8. The operation of these pretreatment steps is stopped at night, but the gravity concentrator 8 is left as it is. The sludge accumulated in the gravity concentrator 8 is further dehydrated at night. The dewatered sludge is discharged by the sludge pump 9 by opening the discharge valve of the gravity concentrator 8 before restarting the operation of the pretreatment process the next day. This sludge is incinerated with the sludge obtained in the biological treatment process.
[0016]
An example of the gravity concentrator 8 is shown in FIG. The main body 20 has a vertical container shape, and the lower part is formed in a cone. A double screen in which a slightly smaller inner screen 23 is provided concentrically inside the outer screen 22 is arranged in the center of the main body 20. It is desirable that the screens 22 and 23 are made of a resin net having excellent cleaning properties, and the opening is about 1 mm. You may make it with a wire mesh.
[0017]
Between the outer screen 22 and the inner screen 23, the upper and lower sides are closed to make the inside a filtrate chamber 24. A water collection container 30 having a U-shaped cross section and a ring shape as a whole is attached to the lower portion of the filtrate chamber 24. One end of the discharge pipe 28 is attached to the lower part of the water collecting container 30, and the other end of the discharge pipe 28 is extended out of the main body 20. In the center of the double screen, a cleaning tube 25 is arranged vertically from above. A rotary joint is provided above the cleaning pipe 25 and a bearing is provided at the lower end. And several spray nozzles 26 are attached at equal intervals up and down, giving an angle difference of about 30 degrees. Although it is designed to rotate by itself, it may be rotated by an electric motor or the like.
[0018]
An undiluted solution supply pipe 29 is inserted into the main body 20 from above, and the outlet of the undiluted solution supply pipe 29 is positioned at a position where the liquid passing through the screens 22 and 23 becomes as uniform as possible. A discharge port provided with a discharge valve 21 is provided at the lower end of the main body 20, and a cleaning liquid discharge port 31 is provided above the discharge port.
[0019]
The thing of FIG. 2 is used as follows. The discharge valve 21 and the cleaning liquid discharge port 31 are closed, and the raw solution is supplied from the raw solution supply pipe 29 into the main body 20. Although the structure is simple, the filtration area by the double screen is wide. Then, the filtered solid matter descends by gravity while sliding on the surface of the screen. Since the entire surface of the screen is constantly updated, filtration can be continued for a long time. When solid matter accumulates in the main body 20 to some extent, the supply of the stock solution is stopped and left as it is until the next day. Since the filtration through the screens 22 and 23 is continued even when left standing, the concentration of the solid matter further proceeds. On the next day, the discharge valve 21 is opened to discharge the solid matter. When the discharge is completed, the discharge valve is closed, the cleaning liquid discharge port 31 is opened, and the cleaning liquid is allowed to flow from the cleaning pipe 25. The spray nozzle 26 rotates while jetting the cleaning liquid, and the screens 22 and 23 are cleaned. When the cleaning is finished, the supply of the cleaning liquid is stopped, the cleaning liquid discharge port 31 is also closed, and the supply of the raw liquid from the raw liquid supply pipe 29 is resumed.
[0020]
The measurement results on the sludge separation performance obtained in the experiment are shown below.
Solid content concentration in relay tank 13000 mg / liter Solid content concentration in storage tank 760 mg / liter Solid content concentration in concentrated sludge 5%
[0021]
【The invention's effect】
According to the present invention, the equipment is inexpensive and the operation cost is low. And efficient sludge removal can be performed.
[Brief description of the drawings]
FIG. 1 is a flow sheet showing an embodiment of the invention.
FIG. 2 is a longitudinal sectional view showing a main part of what is shown in FIG.
[Explanation of symbols]
8 Gravity Type Concentrator 20 Main Body 21 Discharge Valve 22 Outer Screen 23 Inner Screen 24 Filtrate Chamber 25 Wash Pipe 26 Spray Nozzle 28 Discharge Pipe 29 Stock Solution Supply Pipe 30 Drainage Container 31 Wash Liquid Discharge Port

Claims (2)

浄化槽汚泥を生物学的方法で処理する工程の前処理工程において、夾雑物を除去した原液に凝集剤を注入した後に円筒スクリーンを垂直に配置した重力式濃縮機で汚泥を除去する工程を設け、前記の生物学的方法で処理する工程は全日の連続運転とするが前処理工程は昼間だけの断続運転とし、重力式濃縮機においては運転停止後は汚泥を捕捉した状態のまま翌日まで放置して汚泥の脱水を進行させ、翌日は重力式濃縮機の脱水汚泥を取り除いてから前処理工程の運転を再開することを特徴とする浄化槽汚泥中の汚泥除去方法。In the pretreatment step of treating the septic tank sludge with a biological method, a step of removing the sludge with a gravity concentrator in which a cylindrical screen is vertically arranged after injecting the flocculant into the stock solution from which impurities have been removed is provided. The biological treatment process is a continuous operation all day, but the pretreatment process is an intermittent operation only during the daytime, and in the gravity concentrator, after the operation is stopped, the sludge is trapped and left until the next day. The method for removing sludge from the septic tank sludge is characterized in that the dewatering of the sludge is advanced and the operation of the pretreatment process is resumed after removing the dewatered sludge from the gravity concentrator the next day. 重力式濃縮機が、円筒スクリーンの中央に洗浄液を噴出する洗浄管が設けられたものであることを特徴とする、請求項1に記載の浄化槽汚泥中の汚泥除去方法。The method for removing sludge in septic tank sludge according to claim 1, wherein the gravity type concentrator is provided with a cleaning pipe for ejecting a cleaning liquid in the center of the cylindrical screen.
JP34622195A 1995-11-30 1995-11-30 Sludge removal method in septic tank sludge Expired - Fee Related JP3797693B2 (en)

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JP5051004B2 (en) * 2008-05-30 2012-10-17 栗田工業株式会社 Method and apparatus for treating alkaline waste liquid containing water-soluble resin component
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