JPS62121611A - Method for treating waste water - Google Patents
Method for treating waste waterInfo
- Publication number
- JPS62121611A JPS62121611A JP26125585A JP26125585A JPS62121611A JP S62121611 A JPS62121611 A JP S62121611A JP 26125585 A JP26125585 A JP 26125585A JP 26125585 A JP26125585 A JP 26125585A JP S62121611 A JPS62121611 A JP S62121611A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- screen
- water
- substances
- crusher
- 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
Links
Abstract
Description
【発明の詳細な説明】
イ 発明の目的
(産業上の利用分野)パーキングエリア、サービスエリ
ア、インターチェンジ等には各施設の生活廃水を環境衛
生上必要な水質基準まで処理して放流するための汚水処
理設備がある。本発明はかかる設備における汚水処理方
法、特にし尿浄化槽における汚物等の処理方法に間する
。[Detailed description of the invention] A. Purpose of the invention (industrial application field) Waste water for treating domestic wastewater from each facility to a water quality standard necessary for environmental hygiene and discharging it into parking areas, service areas, interchanges, etc. There is processing equipment. The present invention is directed to a method for treating sewage in such facilities, particularly a method for treating sewage, etc. in a human waste septic tank.
(従来の技術)汚水は第5図の如く前処理槽1、破砕機
2及び処理槽3を経て放流される。沈砂池及びバースク
リーンを備えた前処理槽1は各施設よりの廃水を受け、
水中のきょう雑物及び現在の処理施設で処理できないも
のく例えば、固形物、難水溶性物、ビニール、砂)を取
り除く行程である。汚水流入は、特別な場合を除き、落
差式の流入であり、この行程に最も多く汚物が集まり、
臭気、害虫等の発生を招き易い。水中の浮遊物はここで
バースクリーンにより止められるが、その大半は紙屑、
素塊等の処理可能物である。これらは、単一に除去して
もよいが、除去物は大変処理しにくく、大量に発生し、
また現段階では負荷としてのウエートも大きい。よって
処理可能なものは次の行程に移し、処理不能なものだけ
を除去することが望ましい。しかし、−気に破砕機に流
し込むと破砕機の故障の原因になり得るため、現在は水
道水等によりたたいて物理的に分解し、次の行程に送っ
ている。(Prior Art) Sewage is discharged through a pretreatment tank 1, a crusher 2, and a treatment tank 3 as shown in FIG. A pretreatment tank 1 equipped with a sand settling basin and a bar screen receives wastewater from each facility.
This process removes impurities in the water and those that cannot be treated with current treatment facilities, such as solids, poorly water-soluble materials, vinyl, and sand. Unless there are special circumstances, sewage flows in by a drop type, and the most filth collects in this process.
It is easy to cause odor and pests. Floating objects in the water are stopped here by a bar screen, but most of them are paper waste,
Processable materials such as raw blocks. These may be removed singly, but the removed material is very difficult to treat and is generated in large quantities.
Also, at this stage, the weight as a load is large. Therefore, it is desirable to move the processable items to the next step and remove only the unprocessable items. However, pouring it into the crusher can cause the crusher to malfunction, so currently, it is physically broken down by beating with tap water, etc. before being sent to the next process.
(発明が解決しようとする問題点)上記の水道水等によ
りたたく作業は、単純作業であるが、時間と労力を必要
とする。殊に繁忙時期等は、スクリーンが詰まり水位が
上がり溢流するおそれがあるため、保守員は必要業務の
一つとして適宜スクリーン室を点検しなければならない
。よってこの行程を自動的に行い必要に応じて人力を加
えるようにすることが望まれる。(Problems to be Solved by the Invention) The above-mentioned work of tapping with tap water etc. is a simple work, but requires time and effort. Particularly during busy periods, there is a risk that the screen will become clogged, causing the water level to rise and overflow, so maintenance personnel must inspect the screen room from time to time as part of their necessary duties. Therefore, it is desirable to perform this process automatically and add human power as necessary.
口 発明の構成
(問題点を解決するための手段)調整槽及びばっ気槽を
含む処理槽にて汚水を処理し、この水を処理槽内の消泡
ポンプを利用して前処理槽へ帰還させ散水ノズルからス
クリーンに噴射する。これによりスクリーン上の処理可
能物を分解し、これを前処理槽と処理槽との中間に位置
する破砕機へ送るものとする。Structure of the invention (Means for solving the problem) Sewage is treated in a treatment tank including an adjustment tank and an aeration tank, and this water is returned to a pre-treatment tank using a defoaming pump in the treatment tank. Water is sprayed onto the screen from the water nozzle. This decomposes the processable material on the screen and sends it to a crusher located between the pretreatment tank and the processing tank.
(作用)消泡ポンプ圧により処理水は管路を通ってノズ
ルからスクリーンに向って噴射される。(Operation) The treated water is injected from the nozzle toward the screen through the pipe line by the defoaming pump pressure.
これにより、スクリーン上の処理可能物はたたかれ分解
して次の行程の破砕機へ送られる。As a result, the processable material on the screen is knocked down, broken down, and sent to the crusher for the next step.
(実施例)図面において同一番号は同一または相応部分
を指すものとする。(Embodiment) In the drawings, the same numbers refer to the same or corresponding parts.
汚水は流入口11より流入する。その中の重量物は沈砂
池15に沈み、浮遊物はバースクリーン13に引っかか
って止められ、残りは破砕機2及び処理槽3を経て第1
図右方へ放流される。処理槽3は調整槽31、ばっ気槽
32、沈澱槽33及び滅菌槽34から成る。沈澱槽33
は消泡ポンプ5を備えており、これと前処理槽1内のノ
ズル12とは管路7により連絡している。ノズル12の
1つは水平面に対し約70度の、他の2つは約30度の
角度を保って取り付けられており、この後者のノズルか
らの散水により相当量の処理可能物がスクリーンに引掛
かる前に分解される。Sewage flows in from the inlet 11. The heavy objects therein sink into the sand settling basin 15, the floating objects are caught on the bar screen 13 and stopped, and the rest passes through the crusher 2 and the processing tank 3, and then the first
The water is discharged to the right in the figure. The treatment tank 3 includes an adjustment tank 31, an aeration tank 32, a settling tank 33, and a sterilization tank 34. Sedimentation tank 33
is equipped with a defoaming pump 5, and this and a nozzle 12 in the pretreatment tank 1 are connected through a pipe line 7. One of the nozzles 12 is mounted at an angle of about 70 degrees to the horizontal plane, and the other two at an angle of about 30 degrees, and the water spray from this latter nozzle draws a significant amount of processable material onto the screen. It will be disassembled before hanging.
沈澱槽内の処理水はポンプ5により管路7を通って前処
理槽へ導かれノズルより噴射され、スクリーン13上の
汚物を叩く。汚物のうち処理可能物は分解し破砕機2へ
送られる。従って、この圧力散水により破壊されないビ
ニールや固形物等のみを保守点検により除去すれはよい
。The treated water in the sedimentation tank is guided by the pump 5 through the pipe 7 to the pretreatment tank, and is sprayed from a nozzle to hit the waste on the screen 13. The waste that can be treated is decomposed and sent to the crusher 2. Therefore, it is advisable to remove only vinyl, solid materials, etc. that are not destroyed by this pressure water spraying during maintenance and inspection.
また、タイマー等により、散水時間の間隔を設定し、或
いは、夜間の汚水流入の少ない時間帯は止めておく等の
配慮をすれば、より効果的な汚物処理を達成し得る。Furthermore, more effective waste treatment can be achieved by setting the time interval of watering using a timer or by stopping watering during nighttime hours when there is little inflow of wastewater.
次に散水による除去効果につき考察する。Next, we will discuss the removal effect of watering.
(1)従来の方法
水圧・・−・・◆・φ・0.7kg/cmLビニールホ
ース番争φ013mmφ
ビニールホースを172程度につぶして使用した場合、
流速v==cf21下
=o、sOy「■σ
=9.4m/s
C:ノズル係数=0.8
g二重力加速度
h:位置水頭
流量Q=AV
=π/4×帆00652X9.4
=0.0003m” /s
A:断面積
密度ρ=1000/9.8kg5” /ゴであるから
衝撃力F=ρQV
=:1000/9.8X0.0003
×9.4
=0.29kg
(2)本発明の方法
ポンプ末端吐出圧・・1.0kg/cm”ノズル・・◆
・・・・A=0.00006m2ノズル吐出量・・・φ
1 t5Ps 1時12.2GPM
条件より
流量Q==0.77J!/s
=0.00077m’ /s
流速V=Q/A
=0.0007710.00006
=12.8m/s
衝撃力F=ρQV
=1000/9.8X0.00077
X12.8
=1.Okg
散水角度により力は分散するので、散水角度によりノズ
ルの必要個数がきまる。かくして決定された必要個数の
ノズルを取り付けることにより効果的な洗浄を達成し得
る。(1) Conventional method Water pressure...◆・φ・0.7kg/cmL Vinyl hose number φ013mmφ When using a vinyl hose crushed to about 172, flow rate v = = cf21 lower = o, sOy "■ σ = 9.4 m/s C: Nozzle coefficient = 0.8 g double force acceleration h: Position head flow rate Q = AV = π/4 x sail00652X9.4 = 0.0003 m"/s A: Cross-sectional area density ρ = 1000/9.8kg5"/go, so impact force F = ρQV =: 1000/9.8 cm” nozzle...◆
...A=0.00006m2 Nozzle discharge amount...φ
1 t5Ps 1 hour 12.2GPM From the conditions, flow rate Q = = 0.77J! /s =0.00077m' /s Flow velocity V=Q/A =0.0007710.00006 =12.8m/s Impact force F=ρQV =1000/9.8X0.00077 X12.8 =1. Okg Since the force is dispersed depending on the watering angle, the required number of nozzles is determined by the watering angle. Effective cleaning can be achieved by installing the required number of nozzles thus determined.
土曜、日曜等の比較的汚水流入の多い時期において、従
来の方法と本発明の方法とを比較した。A comparison was made between the conventional method and the method of the present invention during periods when relatively a large amount of sewage flows in, such as Saturdays and Sundays.
きょう雑物除去は従来は1日に0.5〜1.0kg必要
であったが、本方法によれば0.2〜0゜3kgで済ん
だ。スクリーンの清掃時間については、従来は20〜3
0分かかったのに対し、本方法によれば10〜15分で
済み、約半分の時間短縮が為された。Conventionally, 0.5 to 1.0 kg was required to remove impurities per day, but according to this method, only 0.2 to 0.3 kg was required per day. Conventionally, the screen cleaning time was 20 to 3
Whereas it took 0 minutes, according to this method, it only took 10 to 15 minutes, reducing the time by about half.
ハ 発明の効果
本発明によれば、スクリーン清掃のための労力と時間と
を節約でき、しかも効果的な処理可能物の除去を為し得
、従って、汚水の流入がスムーズになって溢流を防止し
得、前処理槽での害虫の発生が少なくなると共に、保守
点検による汚物除去の労力と時間を節約し得る等、種々
の効果を奏する。C. Effects of the Invention According to the present invention, it is possible to save labor and time for cleaning the screen, and moreover, it is possible to effectively remove processable materials, and therefore, the inflow of wastewater is smoother and overflow is prevented. This has various effects, such as reducing the occurrence of pests in the pretreatment tank and saving labor and time for removing dirt during maintenance and inspection.
第1図は本発明の方法の行程図、第2図はスフリーン室
の正面断面図、第3図は同平面図、第4図は同右側面断
面図、第5図は従来の方法の行程図である。
1=前処理槽、2=破砕機、3=処理槽、5=消泡ポン
プ、7=管路、12=散水ノズル、13=スクリーン、
31=調整槽、32=ばっ気槽、33=沈澱槽、34=
滅菌槽。
=8−Fig. 1 is a process diagram of the method of the present invention, Fig. 2 is a front sectional view of the souffle chamber, Fig. 3 is a plan view thereof, Fig. 4 is a right side sectional view of the same, and Fig. 5 is a process diagram of the conventional method. It is a diagram. 1=Pre-treatment tank, 2=Crusher, 3=Processing tank, 5=Defoaming pump, 7=Pipeline, 12=Water nozzle, 13=Screen,
31=adjustment tank, 32=aeration tank, 33=settling tank, 34=
Sterilization tank. =8-
Claims (1)
記処理槽の消泡ポンプを利用して前処理槽へ帰還させ該
水を該前処理槽内にて散水ノズルからスクリーンに噴射
して該スクリーン上の処理可能物を分解し、既記前処理
槽と既記処理槽との中間に位置する破砕機へ送る汚水処
理方法。The water treated in the treatment tank including the adjustment tank and the aeration tank is returned to the pre-treatment tank using the defoaming pump of the treatment tank, and the water is sent to the screen from the watering nozzle in the pre-treatment tank. A sewage treatment method in which the wastewater is injected to decompose the treatable materials on the screen and sent to a crusher located between the pre-treatment tank and the treatment tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26125585A JPS62121611A (en) | 1985-11-22 | 1985-11-22 | Method for treating waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26125585A JPS62121611A (en) | 1985-11-22 | 1985-11-22 | Method for treating waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62121611A true JPS62121611A (en) | 1987-06-02 |
Family
ID=17359286
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26125585A Pending JPS62121611A (en) | 1985-11-22 | 1985-11-22 | Method for treating waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62121611A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5145851B2 (en) * | 1972-11-24 | 1976-12-06 | ||
JPS6031805A (en) * | 1983-08-01 | 1985-02-18 | Kubota Ltd | Screen washing apparatus |
-
1985
- 1985-11-22 JP JP26125585A patent/JPS62121611A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5145851B2 (en) * | 1972-11-24 | 1976-12-06 | ||
JPS6031805A (en) * | 1983-08-01 | 1985-02-18 | Kubota Ltd | Screen washing apparatus |
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