JPH0344320Y2 - - Google Patents
Info
- Publication number
- JPH0344320Y2 JPH0344320Y2 JP1988004066U JP406688U JPH0344320Y2 JP H0344320 Y2 JPH0344320 Y2 JP H0344320Y2 JP 1988004066 U JP1988004066 U JP 1988004066U JP 406688 U JP406688 U JP 406688U JP H0344320 Y2 JPH0344320 Y2 JP H0344320Y2
- Authority
- JP
- Japan
- Prior art keywords
- supernatant water
- sludge
- baffle member
- water discharge
- sewage treatment
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 54
- 239000006228 supernatant Substances 0.000 claims description 48
- 239000010802 sludge Substances 0.000 claims description 35
- 239000010865 sewage Substances 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 16
- 238000005273 aeration Methods 0.000 claims description 8
- 238000005096 rolling process Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 4
- 238000004891 communication Methods 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
この考案は、有機性汚水の曝気、沈澱、排出工
程を同一槽内で行なつて活性汚泥法により浄化処
理する回分式処理装置に設置する上澄水排出装置
に関するものである。[Detailed description of the invention] (Industrial application field) This invention is installed in a batch-type treatment equipment that performs the aeration, precipitation, and discharge processes of organic sewage in the same tank and purifies it using the activated sludge method. This relates to a supernatant water discharge device.
(従来技術)
従来、回分式汚水処理装置の上澄水排出装置と
して、例えば第3図に示すようなものがある。即
ち第3図において、処理槽51内には汚水を流入
させることができ、この処理槽51の底面側には
外部と連通した流出管52が配設されており、こ
の流出管52の端部には揺動可能に弾性材よりな
る排出管53が接続されており、この排出管23
の上端部は上澄水を排出させることのできるトラ
フ54と接続されており、このトラフ54の一部
にはウエヤ55が付設されているとともに、トラ
フ54には空気タンク56,56が付設されて構
成されている。(Prior Art) Conventionally, as a supernatant water discharge device for a batch type sewage treatment device, there is a device as shown in FIG. 3, for example. That is, in FIG. 3, wastewater can flow into a treatment tank 51, and an outflow pipe 52 communicating with the outside is provided on the bottom side of this treatment tank 51. A discharge pipe 53 made of an elastic material is swingably connected to the discharge pipe 23.
The upper end is connected to a trough 54 from which supernatant water can be discharged, and a wearer 55 is attached to a part of this trough 54, and air tanks 56, 56 are attached to the trough 54. It is configured.
(考案が解決しようとする課題)
上記従来構造の上澄水排出装置においては、処
理槽51内に流入された汚水が処理槽51内で先
ず曝気され、曝気後に処理槽51内で汚泥の沈澱
が成され、沈澱後に上方より上澄水をトラフ54
を介して排出管53より流出管52に流出させる
ことができ、上澄水の水面の下降に従つて空気タ
ンク56が下方に移動し徐々に上澄水を外部へ排
出可能に構成されているが、前記曝気工程中にも
ウエヤ55から汚水がトラフ54内に流入するこ
とが多く、又、沈澱後の排出工程においてトラフ
54と排出管53内に流入している汚水をも排出
工程初期には上澄水とともに排出することとなる
ため、初期の上澄水は再び処理槽51内に循環さ
せて再処理する必要があり、処理水の仕分けが複
雑となるという問題点があつた。(Problem to be solved by the invention) In the above-mentioned conventional supernatant water discharge device, the sewage that has flowed into the treatment tank 51 is first aerated in the treatment tank 51, and after the aeration, sludge sedimentation occurs in the treatment tank 51. After precipitation, the supernatant water is poured into a trough 54 from above.
The air tank 56 is configured to move downward as the water level of the supernatant water drops, and gradually discharge the supernatant water to the outside. During the aeration process, sewage often flows into the trough 54 from the wearer 55, and the sewage that has flowed into the trough 54 and the discharge pipe 53 during the discharge process after settling is also discharged into the trough 54 at the beginning of the discharge process. Since it is discharged together with clear water, it is necessary to circulate the initial supernatant water into the treatment tank 51 again for reprocessing, which poses a problem in that the sorting of the treated water becomes complicated.
又、従来構造においては排出管53が揺動する
ため、動く部分が多くメンテナンスが困難となる
という問題点があり、又、排出管53は弾性部材
にて構成されるため、その耐久性等に問題点があ
つた。 In addition, in the conventional structure, since the discharge pipe 53 swings, there is a problem that there are many moving parts, making maintenance difficult.Also, since the discharge pipe 53 is made of an elastic member, its durability etc. There was a problem.
本考案は上記従来の問題点に鑑み案出したもの
であつて、メンテナンスが容易で上澄水の排出を
良好に行なうことができ、かつ設備費等が安価で
処理効率の大なる上澄水排出装置を提供せんこと
を目的とするものである。 The present invention was devised in view of the above-mentioned conventional problems, and is a supernatant water discharge device that is easy to maintain, can discharge supernatant water well, has low equipment costs, and has high processing efficiency. The purpose is not to provide
(課題を解決するための手段)
上記目的を達成するために本考案はその要旨
を、有機性汚水の曝気、沈澱、排出工程を同一槽
内で行なう回分式汚水処理装置の上澄水排出装置
であつて、該上澄水排出装置は、汚水処理槽内の
汚泥界面上に固定状に配設された汚泥巻き上がり
防止用の阻流部材と、該阻流部材上に固設された
上澄水排出ポンプと、前記阻流部材に集積する汚
泥を外部に排出可能に阻流部材の底面に連結され
たエアリフト装置とを主体として構成したことで
ある。(Means for Solving the Problems) In order to achieve the above object, the present invention is based on a supernatant water discharge device for a batch-type sewage treatment system that performs aeration, precipitation, and discharge processes of organic sewage in the same tank. The supernatant water discharge device includes a baffle member fixedly disposed on the sludge interface in the sewage treatment tank to prevent sludge from rolling up, and a supernatant water discharge device fixedly installed on the baffle member. The present invention is mainly composed of a pump and an air lift device connected to the bottom surface of the baffle member so as to be able to discharge sludge accumulated on the baffle member to the outside.
(作用)
処理槽内の汚泥界面上に阻流部材が固定状に配
設され、かつ阻流部材の上部に上澄水排出ポンプ
が固定状に設置されているため、従来のような可
動部分がなく設備費等を安価にし得るとともに、
運転操作を容易化させることができる。又、沈澱
工程時に汚泥が阻流部材上に集積した時にも、集
積した汚泥をエアリフト装置を介し良好に外部に
排出することができるため、上澄水排出ポンプか
らは上澄水のみを良好に引き抜くことができる。(Function) The baffle member is fixedly disposed on the sludge interface in the treatment tank, and the supernatant water discharge pump is fixedly installed above the baffle member, so there are no moving parts like in the past. In addition to reducing equipment costs, etc.,
Driving operations can be made easier. In addition, even when sludge accumulates on the baffle member during the settling process, the accumulated sludge can be efficiently discharged to the outside via the air lift device, so only the supernatant water can be effectively drawn out from the supernatant water discharge pump. I can do it.
(実施例)
以下、本考案の一実施例を図面に基づいて説明
する。(Example) Hereinafter, an example of the present invention will be described based on the drawings.
第1図は本実施例の全体概略構成図を示し、第
2図には要部拡大図を示す。 FIG. 1 shows an overall schematic configuration diagram of this embodiment, and FIG. 2 shows an enlarged view of the main parts.
図において、汚水処理槽1は断面円形状に形成
され、その内部に汚水を流入可能となつており、
汚水が汚水処理槽1内に流入された時には第1図
中のH・W・Lで示す満水ラインまで汚水が満た
される。 In the figure, a sewage treatment tank 1 is formed with a circular cross section, and sewage can flow into the tank.
When sewage flows into the sewage treatment tank 1, it is filled with sewage up to the full water line indicated by H, W, and L in FIG.
この汚水処理槽1のほぼ中央部には阻流部材2
が配設されており、この阻流部材2は第2図で拡
大して示すように、上方が拡開状に開放されたロ
ート状にFRP等の素材により形成されたもので
あり、この阻流部材2は汚水処理槽1の固定され
たもので、この固定脚3,3により汚水処理槽1
内に固設されている。この阻流部材2の配設位置
は第1図にO・Lで示す汚泥界面の上方に位置
し、汚泥界面O・Lは沈澱工程において下方に沈
澱される汚泥の上面を示すものであり、この汚泥
界面O・Lは実験値等により算出されるラインで
あり、この汚泥界面O・Lより僅か上方に阻流部
材2が固定される。 A baffle member 2 is located approximately in the center of this sewage treatment tank 1.
As shown in the enlarged view in Fig. 2, this current blocking member 2 is formed of a material such as FRP and has a funnel shape with an expanded upper part. The flow member 2 is a fixed part of the sewage treatment tank 1, and the fixed legs 3, 3 allow the sewage treatment tank 1 to be fixed.
Fixed inside. The arrangement position of this baffle member 2 is located above the sludge interface indicated by O and L in FIG. This sludge interface O.L is a line calculated based on experimental values, etc., and the baffle member 2 is fixed slightly above this sludge interface O.L.
この阻流部材2の上方には脚棒4,4を介して
上澄水排出ポンプ5が固設されており、この上澄
水排出ポンプ5の上端には処理水ピツト等に連通
された上澄水排出管6が連結されている。 A supernatant water discharge pump 5 is fixedly installed above this baffle member 2 via leg rods 4, 4, and a supernatant water discharge pump 5 is connected to a treated water pit or the like at the upper end of the supernatant water discharge pump 5. A tube 6 is connected.
又、阻流部材2の底面中央部には垂下状に連通
管7が接続されており、この連通管7の下端は曲
折されてエアリフト管8に接続されており、エア
リフト管8の汚泥濃縮貯留槽に配管されている。 In addition, a communication pipe 7 is connected to the center of the bottom surface of the baffle member 2 in a hanging manner, and the lower end of this communication pipe 7 is bent and connected to an air lift pipe 8. It is piped to the tank.
又、このエアリフト管8の下端部にはエア圧送
管9が分岐状に接続されている。 Further, an air pressure feed pipe 9 is connected to the lower end of the air lift pipe 8 in a branched manner.
又、前記固定脚3の下方部位には散気装置11
が配設されており、この散気装置11は例えば多
孔質のセラミツク管等により構成されており、外
部の図示しないブロア等と連通状に接続されたも
ので、ブロアを介しこの散気装置11内にエアが
圧送され、エアは散気装置11より汚水処理槽1
内の汚水中に散気されて汚水の曝気が成されるも
のである。 Further, an air diffuser 11 is provided below the fixed leg 3.
The air diffuser 11 is made of, for example, a porous ceramic tube, and is connected in communication with an external blower (not shown). Air is pumped into the sewage treatment tank 1 from the air diffuser 11.
The wastewater is aerated by being diffused into the wastewater.
又、汚水処理槽1の内部には汚泥引き抜きポン
プ10が配設されており、沈澱した汚泥を外部に
引き抜くことができる構造となつている。 Furthermore, a sludge extraction pump 10 is disposed inside the sewage treatment tank 1, and is configured to be able to extract settled sludge to the outside.
このように構成された本例上澄水排出装置にお
いては、先ず汚水処理槽1内に外部より汚水が流
入されて、H・W・Lラインまで汚水が流入され
た後に、前述した如く散気装置11を介し汚水中
にエアが曝気され、汚水処理槽1内で曝気工程が
開始される。この曝気工程は例えば4時間程度行
なわれるものである。 In this embodiment of the supernatant water discharge device configured as described above, sewage first flows into the sewage treatment tank 1 from the outside, and after flowing into the H, W, and L lines, the air diffuser is installed as described above. Air is aerated into the wastewater through the wastewater treatment tank 1, and an aeration process is started within the wastewater treatment tank 1. This aeration step is carried out for about 4 hours, for example.
曝気工程が終了した後に1時間程度の沈澱工程
となり、その時に汚水中の汚泥は下方に沈下して
前述した汚泥界面O・Lの下方に汚泥が沈澱し、
その上方には上澄水が分離されることとなる。 After the aeration process is completed, a settling process takes place for about 1 hour, at which time the sludge in the sewage sinks downward, and the sludge settles below the sludge interface O/L mentioned above.
Supernatant water will be separated above it.
本例においては、沈澱工程中において阻流部材
2の上面側に汚泥が集積されることとなるが、阻
流部材2に集積された汚泥は沈澱工程の終了時
に、前記散気装置11にエアを供給するためのブ
ロアより前記エア圧送管9にエアが約30秒程度圧
送されて、圧送されたエアはエア圧送管9よりエ
アリフト管8に循環される。この時に阻流部材2
の上面側に集積した汚泥は連通管7を介し引き抜
かれ、エアリフト管8をエアリフト作用により上
昇して汚泥濃縮貯留槽へと引き抜かれる。そのた
め、沈澱工程後に行なわれる排出工程時には阻流
部材2の上面側に汚泥は存在しないこととなる。
この状態で前記上澄水排出ポンプ5が作動される
ことにより、上澄水が上澄水排出管6を介し外部
に排出される。 In this example, sludge is accumulated on the upper surface side of the baffle member 2 during the settling process, but the sludge accumulated on the baffle member 2 is transferred to the air diffuser 11 at the end of the settling process. Air is force-fed to the air pressure feed pipe 9 for about 30 seconds by a blower for supplying the air, and the pressure-fed air is circulated from the air pressure feed pipe 9 to the air lift pipe 8. At this time, the baffle member 2
The sludge accumulated on the upper surface side of the sludge is pulled out through the communication pipe 7, ascends the air lift pipe 8 by the air lift action, and is drawn into the sludge concentration storage tank. Therefore, no sludge exists on the upper surface side of the baffle member 2 during the discharge process performed after the settling process.
By operating the supernatant water discharge pump 5 in this state, the supernatant water is discharged to the outside via the supernatant water discharge pipe 6.
上澄水排出ポンプ5が作動する時には上澄水は
上澄水排出ポンプ5の下方より吸引されて上澄水
排出管6の排出されるが、本例においては上澄水
排出ポンプ5の下方に阻流部材2が配設されてい
るため、上澄水排出ポンプ5の作動時に下方の汚
泥が巻き上げられることがなく、良好に上澄水の
みを外部に引き抜くことができる。 When the supernatant water discharge pump 5 operates, supernatant water is sucked from below the supernatant water discharge pump 5 and discharged from the supernatant water discharge pipe 6, but in this example, a baffle member 2 is provided below the supernatant water discharge pump 5. , the sludge below is not kicked up when the supernatant water discharge pump 5 is operated, and only the supernatant water can be drawn out to the outside.
尚、この阻流部材2が存在しない時には第1図
で示すL・W・Lラインが上澄水の引抜可能な最
低位置となり、このL・W・Lラインより下方で
上澄水排出ポンプ5を作動させて吸い上げると、
汚泥が巻き上げられて汚泥も同時に吸い上げられ
ることとなるが、本例では上澄水排出ポンプ5の
下方に阻流部材2が配置されているため、上澄水
排出ポンプ5の配設位置をL・W・Lラインより
下方側に設置することができ、上澄水を引抜可能
な最低水位を従来よりも下方位置とすることがで
き、第1図のAで示す汚泥界面O・LとL・W・
Lライン間の余裕高さを従来よりも狭く設定する
ことができ、従来ではこの余裕高さAは25cm以上
必要であつたものが、本例では12〜13cm程度とす
ることができ、余裕高さAを少なくすることがで
きることにより、従来装置よりも上澄水を引き抜
く量が増大して処理能力が格段に向上される。 In addition, when this baffle member 2 is not present, the L, W, and L lines shown in FIG. If you let it suck up,
The sludge is rolled up and the sludge is also sucked up at the same time, but in this example, since the baffle member 2 is arranged below the supernatant water discharge pump 5, the arrangement position of the supernatant water discharge pump 5 is changed from L to W.・It can be installed below the L line, and the lowest water level at which supernatant water can be drawn out can be set lower than before.
The margin height between the L lines can be set narrower than before. Conventionally, the margin height A required 25 cm or more, but in this example, it can be set to about 12 to 13 cm, reducing the margin height. By being able to reduce the depth A, the amount of supernatant water that can be drawn out is increased compared to conventional devices, and the processing capacity is significantly improved.
このように本例においては、従来のように可動
式ではなく固定式の上澄水排出装置としたため、
装置全体の耐久性が増大してメンテナンスが容易
となり設備費が低減されるものである。しかも、
上澄水の排出工程においては阻流部材2により汚
泥の巻き上がりが防止されて、その分、余裕高さ
Aを少なくすることができ、上澄水の引抜能力が
増大されて処理効率が向上される。 In this way, in this example, we used a fixed supernatant water discharge device instead of a movable one like in the past.
The durability of the entire device is increased, maintenance is facilitated, and equipment costs are reduced. Moreover,
In the process of discharging supernatant water, the baffle member 2 prevents sludge from rolling up, and the margin height A can be reduced accordingly, increasing the ability to draw out supernatant water and improving treatment efficiency. .
尚、本例においては汚水処理槽1を断面円形状
のものとしたが、断面角状のものであつても良
く、又、阻流部材2は本例ではロート状のものと
したが、汚泥の巻き上げを有効に阻止することの
できるものであれば他の形状のものであつても良
い。 In this example, the sewage treatment tank 1 has a circular cross section, but it may also have an angular cross section, and the baffle member 2 is funnel-shaped in this example, but the sludge It may be of any other shape as long as it can effectively prevent the winding up.
(考案の効果)
本考案の上澄水排出装置は、汚水処理槽内の汚
泥界面上に固定状に配設された汚泥巻き上がり防
止用の阻流部材と、該阻流部材上に固設された上
澄水排出ポンプと、前記阻流部材に集積する汚泥
を外部に排出可能に阻流部材の底面に連結された
エアリフト装置とを主体として構成したことによ
り、上澄水の排出工程において阻流部材により有
効に汚泥の巻き上がりが防止されて、その分、余
裕高さを少なくすることができ、上澄水をより多
く引き抜くことができ、処理能力を極めて増大さ
れる。(Effect of the invention) The supernatant water discharge device of the present invention includes a baffle member fixedly disposed on the sludge interface in a sewage treatment tank to prevent sludge from rolling up, and a baffle member fixedly installed on the baffle member. The structure mainly consists of a supernatant water discharge pump and an air lift device connected to the bottom of the baffle member so that the sludge accumulated on the baffle member can be discharged to the outside. As a result, rolling up of sludge is effectively prevented, the extra height can be reduced accordingly, more supernatant water can be drawn out, and the processing capacity can be greatly increased.
又、装置全体が汚水処理槽内に固設されたもの
であるため、設備費が安価でメンテナンスが容易
となり、又、可動部分がないため耐久性が極めて
向上する効果を有する。 Furthermore, since the entire device is fixedly installed within the sewage treatment tank, the equipment cost is low and maintenance is easy, and since there are no moving parts, durability is greatly improved.
図は本考案の一実施例を示し、第1図は本例上
澄水排出装置の概略構成図、第2図は第1図の要
部拡大図、第3図は従来装置の概略構成図であ
る。
1…汚水処理槽、2…阻流部材、3…固定脚、
5…上澄水排出ポンプ、6…上澄水排出管、7…
連通管、8…エアリフト管}エアリフト装置、9
…エア圧送管、O・L…汚泥界面、A…余裕高
さ。
The figures show one embodiment of the present invention. Figure 1 is a schematic diagram of the supernatant water discharge device of this example, Figure 2 is an enlarged view of the main parts of Figure 1, and Figure 3 is a schematic diagram of the conventional device. be. 1... Sewage treatment tank, 2... Blocking member, 3... Fixed leg,
5...Supernatant water discharge pump, 6...Supernatant water discharge pipe, 7...
Communication pipe, 8... Air lift pipe} Air lift device, 9
...Air pressure pipe, O/L...Sludge interface, A...Marginal height.
Claims (1)
で行なう回分式汚水処理装置の上澄水排出装置で
あつて、該上澄水排出装置は、汚水処理槽内の汚
泥界面上の固定状に配設された汚泥巻き上がり防
止用の阻流部材と、該阻流部材上に固設された上
澄水排出ポンプと、前記阻流部材に集積する汚泥
を外部に排出可能に阻流部材の底面に連結された
エアリフト装置とを主体として構成されているこ
とを特徴とする回分式汚水処理装置の上澄水排出
装置。 This is a supernatant water discharge device for a batch-type sewage treatment system that performs aeration, precipitation, and discharge processes of organic sewage in the same tank, and the supernatant water discharge device is arranged in a fixed manner on the sludge interface in the sewage treatment tank. A baffle member is installed to prevent sludge from rolling up, a supernatant water discharge pump is fixedly installed on the baffle member, and a bottom surface of the baffle member is provided so that the sludge accumulated on the baffle member can be discharged to the outside. 1. A supernatant water discharge device for a batch-type sewage treatment device, characterized in that it is mainly configured with a connected air lift device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1988004066U JPH0344320Y2 (en) | 1988-01-16 | 1988-01-16 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1988004066U JPH0344320Y2 (en) | 1988-01-16 | 1988-01-16 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01110899U JPH01110899U (en) | 1989-07-26 |
| JPH0344320Y2 true JPH0344320Y2 (en) | 1991-09-18 |
Family
ID=31206249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1988004066U Expired JPH0344320Y2 (en) | 1988-01-16 | 1988-01-16 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0344320Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP7285717B2 (en) * | 2019-07-23 | 2023-06-02 | アルテミラ製缶株式会社 | Thickener |
-
1988
- 1988-01-16 JP JP1988004066U patent/JPH0344320Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01110899U (en) | 1989-07-26 |
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