JPH0359759B2 - - Google Patents
Info
- Publication number
- JPH0359759B2 JPH0359759B2 JP60234725A JP23472585A JPH0359759B2 JP H0359759 B2 JPH0359759 B2 JP H0359759B2 JP 60234725 A JP60234725 A JP 60234725A JP 23472585 A JP23472585 A JP 23472585A JP H0359759 B2 JPH0359759 B2 JP H0359759B2
- Authority
- JP
- Japan
- Prior art keywords
- supernatant liquid
- biological treatment
- level
- water tank
- liquid
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 161
- 239000006228 supernatant Substances 0.000 claims description 119
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 52
- 238000004891 communication Methods 0.000 claims description 18
- 238000000605 extraction Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 16
- 239000010802 sludge Substances 0.000 description 14
- 238000001514 detection method Methods 0.000 description 6
- 238000013459 approach Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- QNRATNLHPGXHMA-XZHTYLCXSA-N (r)-(6-ethoxyquinolin-4-yl)-[(2s,4s,5r)-5-ethyl-1-azabicyclo[2.2.2]octan-2-yl]methanol;hydrochloride Chemical compound Cl.C([C@H]([C@H](C1)CC)C2)CN1[C@@H]2[C@H](O)C1=CC=NC2=CC=C(OCC)C=C21 QNRATNLHPGXHMA-XZHTYLCXSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection 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
【発明の詳細な説明】
「産業上の利用分野」
この発明は、単一の生物処理槽内で少なくとも
曝気工程、汚泥の静置分離工程、上澄液引抜き工
程から成るサイクルを繰返して汚水処理を行う回
分式生物処理装置に係り、特に上澄液を排出する
フロート式の上澄液引抜き管の引抜き流量調節手
段に関する。Detailed Description of the Invention "Industrial Application Field" This invention is a wastewater treatment method that repeats a cycle consisting of at least an aeration process, a sludge standing separation process, and a supernatant liquid withdrawal process in a single biological treatment tank. The present invention relates to a batch-type biological treatment apparatus that performs this process, and particularly to means for adjusting the drawing flow rate of a float-type supernatant liquid drawing pipe for discharging a supernatant liquid.
「従来の技術」
従来、フロート式の上澄液引抜き管を有する回
分式生物処理装置においては、上澄液の引抜き開
始及び終了を、第13図に示すように上澄液引抜
き管1の下降及び上昇により行うか、または第1
4図に示すように上澄液引抜き管2の排出端に設
けた弁8を液面検出器4からの検出信号に基づい
て開閉することにより行つている。そして、上澄
液の引抜きは、生物処理槽5内の液面と上澄液引
抜き管1,2の排出開口とのレベル差による自然
流下にまかせていた。したがつて、上澄液引抜き
管1,2の抜出し口1a,2aと汚泥界面Sが近
づく上澄液引抜き工程の終了間隙には上記のレベ
ル差が小さくなつて上澄液引抜き流量(流速)が
小さくなり、汚泥の巻き込みが回避されるという
利点があつた。また上澄液引抜き管1,2のフロ
ート1b,2bを環状に形成することにより、上
澄液上に浮ぶスカムが上澄液引抜き管1,2の抜
出し口1a,2aに流入するのを防止することが
できるという利点もあつた。"Prior Art" Conventionally, in a batch-type biological treatment apparatus having a float-type supernatant liquid withdrawal tube, the start and end of supernatant liquid withdrawal are determined by the descent of the supernatant liquid withdrawal tube 1, as shown in FIG. and by rising or the first
As shown in FIG. 4, this is done by opening and closing a valve 8 provided at the discharge end of the supernatant liquid drawing pipe 2 based on a detection signal from the liquid level detector 4. The drawing of the supernatant liquid was left to natural flow due to the level difference between the liquid level in the biological treatment tank 5 and the discharge openings of the supernatant liquid drawing pipes 1 and 2. Therefore, in the gap at the end of the supernatant liquid drawing process where the outlet ports 1a, 2a of the supernatant liquid drawing pipes 1, 2 and the sludge interface S approach, the above-mentioned level difference becomes small and the supernatant liquid drawing flow rate (flow rate) increases. This had the advantage of being smaller and avoiding sludge entrainment. Furthermore, by forming the floats 1b and 2b of the supernatant liquid withdrawal tubes 1 and 2 in an annular shape, scum floating on the supernatant liquid is prevented from flowing into the extraction ports 1a and 2a of the supernatant liquid withdrawal tubes 1 and 2. It also had the advantage of being able to do so.
「発明が解決しようとする問題点」
ところが、上記従来の回分式生物処理装置で
は、汚泥の巻き込み防止にも限度があり、沈降性
が悪いSVI(汚泥容量指標)の大きい汚泥は巻き
込まれて上澄液の液質が悪化するという問題があ
つた。そこで、これを解決するために、上澄液引
抜き管1,2の開口端を上澄液引抜き下限レベル
に近づけ、最終の引抜き流量を少なくすると、そ
れに伴つて初期や中期の引抜き流量が少なくなつ
て全体の引抜き時間が長くなるという問題が生じ
る。また、回分式生物処理装置は一時に多量の上
澄液が排出され、次工程の処理装置が大型になる
といつた問題もあつた。"Problems to be Solved by the Invention" However, in the conventional batch-type biological treatment equipment described above, there is a limit to the prevention of sludge entrainment, and sludge with a high SVI (sludge capacity index), which has poor settling properties, gets entrained and rises. There was a problem that the quality of the clear liquid deteriorated. Therefore, in order to solve this problem, the opening ends of the supernatant liquid drawing pipes 1 and 2 are brought closer to the lower limit level for supernatant liquid drawing and the final drawing flow rate is reduced, and the initial and middle drawing flow rates are accordingly reduced. Therefore, the problem arises that the overall drawing time becomes longer. In addition, batch-type biological treatment equipment has the problem that a large amount of supernatant liquid is discharged at one time, resulting in a large-sized treatment equipment for the next process.
この発明は、上記事情に鑑みてなされたもの
で、全体の引抜き工程時間にできるだけ影響を与
えず、上澄液の抜出し口と汚泥界面が近づく上澄
液引抜き工程終了間隙には汚泥の巻き込みを防止
するために非常に小さな流量(流速)で引抜きを
行うことができると共に、次工程の装置が小さく
できる回分式生物処理装置を提供することを目的
とする。 This invention has been made in view of the above circumstances, and is designed to minimize the influence on the overall drawing process time, and to prevent sludge from being drawn into the gap at the end of the supernatant liquid drawing process, where the supernatant liquid drawing port and the sludge interface approach each other. It is an object of the present invention to provide a batch-type biological treatment device that can perform drawing at a very low flow rate (flow rate) to prevent this problem, and also allows the device for the next step to be made smaller.
「問題点を解決するための手段」
上記目的を達成するために、この発明は、生物
処理槽内に設けられ、先端部分にフロートと上澄
液の抜出し口を有して少なくとも該先端部分が水
位の変動に追従する上澄液引抜き管と、上記生物
処理槽の1サイクルで排出される上澄液量以上の
容量を有する処理水槽と、一端が上記上澄液引抜
き管の基端に接続され他端が上記処理水槽の上記
生物処理槽における上澄液引抜き下限レベル以下
の位置で開口し、上記上澄液引抜き管によつて引
抜かれた上澄液を上記処理水槽に導入する連通管
と、所定量の上澄液が上記処理水槽に引抜かれた
ことを直接または間接に検知して上記処理水槽に
受入れられた上澄液を、生物処理槽の次のサイク
ルにおける所定量の上澄液が上記処理水槽に受入
れられたときの処理水槽における液面が上記連通
管の開口位置以上の高さにとどまる範囲におい
て、排出する排出手段とを設けて構成したもので
ある。"Means for Solving the Problems" In order to achieve the above object, the present invention is provided in a biological treatment tank, and has a float and a supernatant extraction port at the tip, so that at least the tip A supernatant liquid withdrawal pipe that follows fluctuations in water level, a treatment water tank having a capacity greater than the amount of supernatant liquid discharged in one cycle of the biological treatment tank, and one end connected to the base end of the supernatant liquid withdrawal pipe. a communicating pipe whose other end opens at a position below the lower limit level for supernatant liquid withdrawal in the biological treatment tank of the treatment water tank, and which introduces the supernatant liquid drawn by the supernatant liquid withdrawal pipe into the treatment water tank; Then, it is directly or indirectly detected that a predetermined amount of supernatant liquid has been drawn into the treated water tank, and the supernatant liquid received in the treated water tank is transferred to a predetermined amount of supernatant liquid in the next cycle of the biological treatment tank. A discharge means is provided for discharging the liquid within a range where the liquid level in the treated water tank remains at a height equal to or higher than the opening position of the communication pipe when the liquid is received in the treated water tank.
「作用」
そして、本発明の回分式生物処理装置において
は、生物処理槽内の上澄液は上澄液引抜き管を通
じて処理水槽に導かれ、生物処理槽の液面が上澄
液引抜き下限レベルに達した以降に排出手段が作
動して処理水槽内に導かれた上澄液が放流され
る。"Operation" In the batch-type biological treatment apparatus of the present invention, the supernatant liquid in the biological treatment tank is led to the treatment water tank through the supernatant liquid drawing pipe, and the liquid level in the biological treatment tank is at the lower limit level for supernatant liquid drawing. After reaching this point, the discharge means is activated and the supernatant liquid introduced into the treated water tank is discharged.
「実施例」
以下、本発明の一実施例を第1図ないし第11
図を参照して説明する。``Example'' Hereinafter, an example of the present invention will be described in Figures 1 to 11.
This will be explained with reference to the figures.
図中10は生物処理槽で、この生物処理槽10
内で第9図に示す原排水の受入れと曝気工程、汚
泥の静置分離工程、上澄液引抜き工程からなるサ
イクルが繰返されるようになつている。そして、
この生物処理槽10の内部に、先端にフロート1
1と上澄液の抜出し口12を有し基端が連通管1
3に接続して生物処理槽10外に連通された上澄
液引抜き管14が配設されると共に、この生物処
理槽10の槽壁10aの上部には、上記上澄液引
抜き管14を起倒する起倒装置15が設置されて
いる。 10 in the figure is a biological treatment tank, and this biological treatment tank 10
The cycle shown in Fig. 9 consisting of receiving raw wastewater and aeration process, standing separation process of sludge, and supernatant liquid drawing process is repeated. and,
Inside this biological treatment tank 10, there is a float 1 at the tip.
1 and a supernatant liquid extraction port 12, and the proximal end is a communicating tube 1.
A supernatant liquid withdrawal pipe 14 is connected to the biological treatment tank 10 and communicated with the outside of the biological treatment tank 10. A tilting device 15 for tilting is installed.
上記上澄液引抜き管14は、所定長さの直管1
4aの先端に45度の曲り管14bを介して上記抜
出し口12を有する集液管14cが連設され、か
つ、上記直管14aの基端に90度の曲り管14d
が連設されたもので、その基端の曲り管14d
が、槽壁10aに固定された上記連通管13の曲
り管に回転継手14eを介して上下に回動自在に
接続されている。そして、上記集液管14cには
左右一対の連結板14f,14fが固定して取付
けられると共に、集液管14cの上方には、4本
のパイプ11a,…を四角形の環状に組合せて形
成した上記フロート11が、集液管14cの抜出
し口12がフロート11の中心下方にくるように
して、その互いに対向する左右のパイプ11aに
渡して取付けた左右一対の取付け板11b,11
bを上記連結板14f,14fに連結軸14gに
よつて連結されて、連結板14f,14fに対し
て上下に回動自在に設けられている。 The supernatant liquid drawing pipe 14 is a straight pipe 1 of a predetermined length.
A liquid collection pipe 14c having the outlet port 12 is connected to the tip of the straight pipe 14a via a 45-degree bent pipe 14b, and a 90-degree bent pipe 14d is connected to the base end of the straight pipe 14a.
are connected in series, and the bent tube 14d at the base end
is connected to the bent pipe of the communication pipe 13 fixed to the tank wall 10a via a rotary joint 14e so as to be freely rotatable up and down. A pair of left and right connecting plates 14f, 14f are fixedly attached to the liquid collecting pipe 14c, and above the liquid collecting pipe 14c, four pipes 11a, . . . are formed by combining them into a rectangular ring shape. The float 11 is attached to a pair of left and right mounting plates 11b, 11 across the left and right pipes 11a facing each other so that the outlet 12 of the liquid collecting pipe 14c is located below the center of the float 11.
b is connected to the connecting plates 14f, 14f by a connecting shaft 14g, and is provided so as to be freely rotatable up and down with respect to the connecting plates 14f, 14f.
また、上記起倒装置15は、アングル材により
形成され、生物処理槽10の槽壁10aの上部に
固定して設置された支持架台16と、この支持架
台16の上部中央に、ロツド17aを下方に向け
た状態で固定して取付けられたエアシリンダ17
と、このエアシリンダ17のロツド17aの先端
に連結部材18を介して固定された前後一対の菱
形の取付け板19,19の左右に軸線を前後に向
けて取付けられ、同一の鉛直面内において回転自
在なる左右一対の可動滑車20a,20bと、上
記エアシリンダ17のロツド17aの伸長端より
若干下方の位置にくるように支持架台16に軸線
を前後に向けて取付けられ、上記可動滑車20
a,20bと同一の鉛直面内において回転自在な
る固定滑車21と、上記左方の可動滑車20aか
ら固定滑車21を経て右方の可動滑車20bに巻
回されると共に、一端が上記上澄液引抜き管14
の連結軸14gにシンブル22aを介して接続さ
れ、他端が、上記支持架台16の下面に鉛直に設
けられたガイド管23の内部に挿入されている2
個の錘24に接続されたワイヤロープ22とから
構成されている。そして、上記エアシリンダ17
のシリンダ本体17bには、スプードコントロー
ラ25a,25bをそれぞれに備えた2本のの空
気管26a,26bが接続され、この2本の空気
管26a,26bは空気供給管27によつて圧縮
空気源28に連絡された四方の電磁切換弁29に
連絡されており、第10図に示す如く、圧縮空気
を下方の空気管26bを通じてシリンダ本体17
bに供給することによりロツド17aを収縮さ
せ、可動滑車20a,20bを上昇させて固定滑
車21から離間させる一方、第1図に示すように
電磁切換弁29を切換えて圧縮空気を上方の空気
管26aからシリンダ本体17bに供給すること
によりロツド17aを伸長させ、可動滑車20
a,20bを下降させて固定滑車21に接近させ
ることができるようになつている。また、上記ガ
イド管23の支持架台16に対する接合部には、
錘24より小径のパイプや上方から見て断面コ字
形の部材等から成るストツパ30が設けられてお
り、このストツパ30により錘24がガイド管2
3から上方へ抜けないようになつている。さら
に、上記支持架台16の内部の前方と後方側に
は、左右一対のアングル材を互いに対向配設して
形成したガイドレール31,31が添設される一
方、上記取付け板19,19と連結部材18の上
下の部位には、車軸32a,32aの両端にそれ
ぞれ車輪32b,32bを備えて成るガイド輪3
2,32が軸線を前後に向けて取付けられ、この
ガイド輪32,32は上記ガイドレール31,3
1に沿つて上下動するようになつている。 The lifting device 15 also includes a support pedestal 16 that is formed of an angle material and is fixedly installed on the upper part of the tank wall 10a of the biological treatment tank 10, and a rod 17a that is placed downwardly at the center of the upper part of the support pedestal 16. Air cylinder 17 fixedly mounted facing toward
A pair of front and rear diamond-shaped mounting plates 19, 19 are fixed to the tip of the rod 17a of the air cylinder 17 via a connecting member 18, and are attached to the left and right of a pair of rhombic mounting plates 19, 19 with their axes facing front and back, and rotate within the same vertical plane. A pair of left and right movable pulleys 20a and 20b are attached to the support pedestal 16 with their axes facing forward and backward so that they are located slightly below the extended end of the rod 17a of the air cylinder 17.
a, 20b, and a fixed pulley 21 rotatable in the same vertical plane as the left movable pulley 20a, the fixed pulley 21, and the right movable pulley 20b. Pulled pipe 14
The connecting shaft 14g is connected to the connecting shaft 14g via a thimble 22a, and the other end is inserted into a guide tube 23 provided vertically on the lower surface of the support frame 16.
The wire rope 22 is connected to several weights 24. And the air cylinder 17
Two air pipes 26a, 26b each equipped with a spude controller 25a, 25b are connected to the cylinder body 17b, and these two air pipes 26a, 26b are connected to compressed air by an air supply pipe 27. As shown in FIG.
b, thereby contracting the rod 17a and raising the movable pulleys 20a and 20b to separate them from the fixed pulley 21. At the same time, as shown in FIG. 26a to the cylinder body 17b, the rod 17a is extended, and the movable pulley 20
a, 20b can be lowered to approach the fixed pulley 21. Further, at the joint portion of the guide tube 23 to the support frame 16,
A stopper 30 is provided, which is made of a pipe with a smaller diameter than the weight 24 or a member having a U-shaped cross section when viewed from above.
It is designed so that it does not slip upward from 3. Furthermore, guide rails 31, 31 formed by arranging a pair of left and right angle members facing each other are attached to the front and rear sides of the interior of the support frame 16, and are connected to the mounting plates 19, 19. At the upper and lower portions of the member 18, there are guide wheels 3 that are provided with wheels 32b, 32b at both ends of axles 32a, 32a, respectively.
2 and 32 are mounted with their axes facing forward and backward, and these guide wheels 32 and 32 are connected to the guide rails 31 and 3.
It is designed to move up and down along 1.
一方、上記生物処理槽10の隣りには、内部に
上記連通管13の外方端が臨ませられた処理水槽
33(上澄液槽)が設置され、この処理水槽33
の内底部には、吐出側に放流管34が接続された
ポンプ35が設置されると共に、処理水槽33に
は、処理水槽33の液面が所定の下限レベル
L2WLになつたときにこれを検知し、その検知信
号により上記ポンプ35を停止する第1レベルス
イツチ36が設けられている。また、上記生物処
理槽10には、上澄液の液面レベルが上澄液引抜
き下限レベルLWLになつたときにこれを検知し、
その検知信号に基づいて上記電磁切換弁29を第
10図の位置に切換えると共に、上記ポンプ35
を起動する第2レベルスイツチ(液面検知器)3
7が設けられている。そして、この実施例におけ
るポンプ35と第1レベルスイツチ36と第2レ
ベルスイツチ37とによつて本発明に係る排出手
段が構成されている。 On the other hand, next to the biological treatment tank 10, there is installed a treated water tank 33 (supernatant liquid tank) in which the outer end of the communication pipe 13 is exposed.
A pump 35 with a discharge pipe 34 connected to the discharge side is installed at the inner bottom of the tank 33, and a pump 35 is installed in the treated water tank 33 to ensure that the liquid level in the treated water tank 33 is at a predetermined lower limit level.
A first level switch 36 is provided which detects when the level reaches L 2 WL and stops the pump 35 based on the detection signal. In addition, the biological treatment tank 10 detects when the liquid level of the supernatant liquid reaches the lower limit level LWL for drawing the supernatant liquid,
Based on the detection signal, the electromagnetic switching valve 29 is switched to the position shown in FIG.
2nd level switch (liquid level detector) 3
7 is provided. The pump 35, first level switch 36, and second level switch 37 in this embodiment constitute a discharge means according to the present invention.
ここで、上記処理水槽33は、上記生物処理槽
10の1サイクルで処理する上澄液の量以上の容
量を有する。また、処理水槽33に設けけた連通
管13の開口の取付け高さは、生物処理槽10の
上澄液引抜き下限レベルLWL以下である。さら
に、上記第1レベルスイツチ36の液面検出位置
高さ(上記下限レベルL2WL)は、生物処理槽1
0の上澄液を上澄液引抜き管14に介して処理水
槽33に流下させる上澄液の引抜きが終了したと
きの処理水槽33の液面(上限レベルH2WL)
を、生物処理槽10の上澄液引抜き下限レベル
LWLに同じレベルと連通管13の開口下端との
間、好ましくは上記上澄液引抜き下限レベル
LWLと同じレベルとし、その上限レベルH2WL
と下限レベルL2WLとの間の容量が生物処理槽1
0の1サイクルで排出される上澄液量と略同一に
なる高さになつている。すなわち、生物処理槽1
0の次のサイクルにおける所定量の上澄液が上記
処理水槽33に受入れられたときの処理水槽33
における液面である上限レベルH2WLが、上記連
通管13の位置以上の高さになるように、処理水
槽33からの上澄液排出が完了したときの液面で
ある下限レベルL2WLを定め、この下限レベル
L2WLに来た液面を第1レベルスイツチ36が検
出するようにするのである。この場合、上記上限
レベルH2WLと下限レベルL2WLとが共に連通管
13の位置以上の高さになつてもさしつかえな
い。 Here, the treated water tank 33 has a capacity greater than the amount of supernatant liquid treated in one cycle of the biological treatment tank 10. Further, the installation height of the opening of the communication pipe 13 provided in the treated water tank 33 is below the lower limit level LWL for drawing out the supernatant liquid of the biological treatment tank 10. Furthermore, the height of the liquid level detection position of the first level switch 36 (the lower limit level L 2 WL) is the same as that of the biological treatment tank 1.
Liquid level in the treated water tank 33 (upper limit level H 2 WL) when the drawing of the supernatant liquid, which is caused to flow down to the treated water tank 33 through the supernatant liquid drawing pipe 14, is completed.
is the lower limit level for drawing out the supernatant liquid of the biological treatment tank 10.
Between the same level as LWL and the lower end of the opening of the communication pipe 13, preferably the lower limit level for supernatant liquid withdrawal.
The same level as LWL, and its upper limit level H 2 WL
The capacity between the lower limit level L 2 WL is biological treatment tank 1
The height is approximately the same as the amount of supernatant liquid discharged in one cycle of 0. That is, biological treatment tank 1
The treated water tank 33 when a predetermined amount of supernatant liquid is received in the treated water tank 33 in the next cycle of 0
The lower limit level L 2 WL, which is the liquid level when the supernatant liquid discharge from the treated water tank 33 is completed, is set so that the upper limit level H 2 WL, which is the liquid level at and this lower limit level
The first level switch 36 is configured to detect the liquid level that has reached L 2 WL. In this case, it is acceptable even if both the upper limit level H 2 WL and the lower limit level L 2 WL are higher than the position of the communication pipe 13.
なお、図中HWLは生物処理槽10の上澄液引
抜き上限レベルで、汚泥の静置分離工程における
生物処理槽10の水位に相当する。 In addition, HWL in the figure is the upper limit level for drawing out the supernatant liquid of the biological treatment tank 10, and corresponds to the water level of the biological treatment tank 10 in the sludge static separation process.
次に、上記構成の生物処理装置の作用について
説明するが、生物処理装置全体の作用の説明に先
立つて先ず起倒装置15の作用を説明する。 Next, the operation of the biological treatment apparatus having the above-mentioned configuration will be explained. Before explaining the operation of the entire biological treatment apparatus, the operation of the raising and lowering device 15 will be explained first.
上記起倒装置15によつて上澄液引抜き管14
を液面上に浮上させるには、電磁切換弁29を第
1図の位置にして圧縮空気を上方の空気管26a
からシリンダ本体17bに供給し、ロツド17a
を伸長させる。すると、可動滑車20a,20b
が下降して固定滑車21に接近するが、ロツド1
7aの伸長端では上澄液引抜き管14を上方に起
立させていたワイヤロープ22の長さに余裕が生
じることになり、これにより上澄液引抜き管14
は回転継手14eの部分で下方に回動して上澄液
液面上に浮上させられる。なおこのとき、ワイヤ
ロープ22はその端部に錘24が設けられている
ため弛むことはないが、上澄液の液面が上澄液引
抜き上限レベルHWLにあるときは第1図の如く
錘24はガイド管23の下端まで下降している。 The supernatant liquid withdrawal pipe 14 is
To float above the liquid surface, set the electromagnetic switching valve 29 to the position shown in Fig. 1 to supply compressed air to the upper air pipe 26a.
is supplied to the cylinder body 17b from the rod 17a.
Stretch. Then, the movable pulleys 20a, 20b
The rod 1 descends and approaches the fixed pulley 21, but the rod 1
At the extended end of 7a, there is an allowance in the length of the wire rope 22 that used to make the supernatant liquid drawing pipe 14 stand up, so that the supernatant liquid drawing pipe 14
is rotated downward at the rotary joint 14e and floated above the supernatant liquid level. At this time, the wire rope 22 does not loosen because a weight 24 is provided at its end, but when the liquid level of the supernatant liquid is at the upper limit level HWL for drawing out the supernatant liquid, the weight 24 is attached to the end of the wire rope 22 as shown in Fig. 1. 24 descends to the lower end of the guide tube 23.
また、起倒装置15によつて上澄液引抜き管1
4を上方に起立させるには、電磁切換弁29を第
10図の位置に切換える。すると、圧縮空気が今
度は下方の空気管26bからシリンダ本体17b
に入つてロツド17aが収縮し、これにより、可
動滑車20a,20bが上昇して固定滑車21か
ら離間していく。ワイヤロープ22は可動滑車2
0a,20bと固定滑車21に交互に巻回されて
いるから、可動滑車20a,20bの上昇に伴つ
てワイヤロープ22が引上げられて先ず錘24が
ストツパ30に当り、錘24がストツパ30に係
止されてそれ以上の上昇ができなくなると、今度
は上澄液引抜き管14がワイヤロープ22を介し
て引上げられて第10図の如くの起立状態とな
る。 In addition, the supernatant liquid drawing pipe 1 is raised by the lifting device 15.
4, the electromagnetic switching valve 29 is switched to the position shown in FIG. Then, compressed air flows from the lower air pipe 26b to the cylinder body 17b.
The rod 17a contracts as the movable pulleys 20a and 20b rise and move away from the fixed pulley 21. The wire rope 22 is a movable pulley 2
Since the wire ropes 22 are wound alternately around the fixed pulleys 21, as the movable pulleys 20a and 20b rise, the weight 24 first hits the stopper 30, and the weight 24 engages with the stopper 30. When the supernatant liquid withdrawal pipe 14 is stopped and cannot rise any further, the supernatant liquid withdrawal pipe 14 is pulled up via the wire rope 22 and becomes an upright state as shown in FIG.
次に、上記構成の生物処理装置において、液面
が上澄液引抜き上限レベルHWLにある生物処理
槽10の上澄液を排出する場合について説明す
る。この場合は起倒装置15を上述したようにし
て作動させて上澄液引抜き管14を液面上に浮上
させる。すると、生物処理槽10内の上澄液は、
生物処理槽10の液面と連通管13の開口とのレ
ベル差により、抜出し口12から上澄液引抜き管
14の内部に入つて自然流下し、連通管13を経
て処理水槽34内に流入する、次いで、処理水槽
33の液面が上昇して連通管13のレベルを越え
ると、上澄液の引抜き量は生物処理槽10の下降
する液面と処理水槽33の上昇する液面とのレベ
ル差によつて決まるので急速に減少し、上澄液引
抜き下限レベルLWLに近くなればなる程レベル
差は小さくなり、その引抜き流量は減少して汚泥
の巻き込みが防止される。そして、生物処理槽1
0の液面が上澄液引抜き下限レベルLWLに達し
てこれを第2レベルスイツチ37が検知すると、
その検知信号によつて起倒装置15の電磁切換弁
29が切換わつて上澄液引抜き管14が上昇し、
生物処理槽10の上澄液引抜きが停止されると共
にポンプ35が起動し、次の原排水の受入れや曝
気工程、静置分離工程の間、すなわち次の上澄液
引抜き工程の開始までに第1レベルスイツチ36
の下限レベルL2WLまで上澄液を排出する。 Next, in the biological treatment apparatus configured as described above, a case will be described in which the supernatant liquid of the biological treatment tank 10 whose liquid level is at the upper limit level HWL for drawing out the supernatant liquid is discharged. In this case, the lifting device 15 is operated as described above to float the supernatant liquid withdrawal tube 14 above the liquid surface. Then, the supernatant liquid in the biological treatment tank 10 is
Due to the level difference between the liquid level in the biological treatment tank 10 and the opening of the communication pipe 13, the supernatant liquid enters the inside of the supernatant liquid withdrawal pipe 14 from the extraction port 12, flows down naturally, and flows into the treated water tank 34 via the communication pipe 13. Then, when the liquid level of the treated water tank 33 rises and exceeds the level of the communication pipe 13, the amount of supernatant liquid to be withdrawn is equal to the level of the descending liquid level of the biological treatment tank 10 and the rising liquid level of the treated water tank 33. Since it is determined by the difference, it rapidly decreases, and the closer it gets to the lower limit level LWL for drawing supernatant liquid, the smaller the level difference becomes, and the drawing flow rate decreases to prevent sludge from being entrained. And biological treatment tank 1
When the liquid level reaches the supernatant liquid withdrawal lower limit level LWL and the second level switch 37 detects this,
In response to the detection signal, the electromagnetic switching valve 29 of the lifting device 15 is switched, and the supernatant liquid withdrawal pipe 14 is raised.
At the same time as the drawing of supernatant liquid from the biological treatment tank 10 is stopped, the pump 35 is started, and the pump 35 is started during the next raw wastewater reception, aeration process, and static separation process, that is, before the start of the next supernatant liquid drawing process. 1 level switch 36
Drain the supernatant liquid to the lower limit level L 2 WL.
したがつて、上記構成の回分式生物処理装置に
おいては、処理水槽33の上記上限レベルH2WL
を第1レベルスイツチ36の位置で調整すること
により、急速に上澄液引抜き量が減少する変曲点
(処理水槽33の液面ぎ連通管13を越える時期)
を移動して、上澄液引抜き時間を調整したり、生
物処理槽10の上澄液引抜き下限レベルLWL付
近の上澄液引抜き流速を汚泥の巻き込みが生じな
いように調整することができる。 Therefore, in the batch type biological treatment apparatus having the above configuration, the above upper limit level H 2 WL of the treatment water tank 33 is
By adjusting the position of the first level switch 36, the inflection point where the amount of supernatant liquid withdrawn rapidly decreases (the time when it exceeds the liquid level communication pipe 13 of the treated water tank 33)
can be moved to adjust the supernatant liquid withdrawal time or to adjust the supernatant liquid withdrawal flow rate near the supernatant liquid withdrawal lower limit level LWL of the biological treatment tank 10 so as not to cause sludge entrainment.
さらに、ポンプ35は次の上澄液引抜き工程の
開始時点までに処理水槽33中の上澄液を排出す
ればよく、従来回分式生物処理装置の欠点とされ
ていた一時に大量の上澄液が排出されるといつた
問題が解決され、ポンプ35も小型になり、また
処理水槽33も滅菌槽等として有効利用でき、さ
らには三次処理を行う次工程の処理設備が小型に
できるといつた利点がある。 Furthermore, the pump 35 only needs to discharge the supernatant liquid in the treated water tank 33 before the start of the next supernatant liquid drawing process, which eliminates the problem of a large amount of supernatant liquid at one time, which has been considered a drawback of conventional batch-type biological treatment equipment. The problem of water being discharged has been solved, the pump 35 has become smaller, the treated water tank 33 can be effectively used as a sterilization tank, etc., and the processing equipment for the next process that performs tertiary treatment can be made smaller. There are advantages.
なお、上澄液引抜き時間または生物処理槽10
の上澄液抜き下限レベルLWL付近の上澄液引抜
き速度をさらに調節できるように第12図に示す
如く連通管13の開口位置を可変にするようにし
てもよい。 In addition, the supernatant liquid withdrawal time or the biological treatment tank 10
In order to further adjust the supernatant liquid withdrawal speed near the supernatant liquid withdrawal lower limit level LWL, the opening position of the communication pipe 13 may be made variable as shown in FIG. 12.
第12図では連通管13の開口端部に回転継手
13aを介して90度の曲り管13bを上下に回動
自在に接続し、該曲り管13bの外方開口の高さ
を変えることにより急速に上澄液引抜き量が減少
する上記変曲点を移動させ、上澄液引抜き時間ま
たは流速の調整ができるようにしている。この場
合も当然、曲り管13bの開口は、上澄液引抜き
下限レベルLWLおよび上限レベルH2WLより下
になければならい。 In FIG. 12, a 90 degree bent pipe 13b is connected to the open end of the communication pipe 13 via a rotary joint 13a so as to be able to rotate up and down, and by changing the height of the outward opening of the bent pipe 13b, The above-mentioned inflection point at which the amount of supernatant liquid withdrawn decreases is moved to allow adjustment of the supernatant liquid withdrawal time or flow rate. Naturally, in this case as well, the opening of the bent pipe 13b must be below the lower limit level LWL for drawing out the supernatant liquid and the upper limit level H 2 WL.
また、以上の実施例では生物処理槽10の1サ
イクルにおける所定量の上澄液が処理水槽33に
引抜かれたことを検知するために、生物処理槽1
0の上澄液の液面レベルを基準とし、上澄液引抜
き下限レベルLWLになつたとき、これを検知し、
その検知信号に基づいて生物処理槽10の上澄液
引抜きを停止させると共にポンプ35を起動させ
る第2レベルスイツチ37を設けたが、これに代
えて処理水槽33に流入した上澄液の液面レベル
を基準とし、該液面が上限レベルH2WLになつた
とき、これを検知する液面検知器を処理水槽33
に設けてもよい。さらに、例えば生物処理槽10
の1サイクルで排出される上澄液が常に一定で生
物処理槽10と処理水槽33の液面レベルの関係
が一定の関係にある場合は、上澄液引抜きを停止
する液面検知器とポンプ35を起動させるレベル
スイツチとを生物処理槽10と処理水槽33に分
けて別々に設けてもよい。また生物処理槽10か
ら処理水槽33への上澄液の引抜きが終了したと
きの処理水槽33の液面(上限レベルH2WL)を
上澄液引抜き下限レベルLWLと同じレベルとす
る場合、上澄液の引抜き終了時にはもはや連通管
13内を上澄液が流れないので、上記第2レベル
スイツチ37に代えて例えばタイマーを用い、予
め上記上澄液のの引抜き時間を多少余裕をそつて
設定し、上澄液の引抜きが完了した後、該タイマ
ーでポンプ35を起動してもよく、要は直接また
は間接に生物処理槽の1サイクルにおける所定量
の上澄液が処理水槽に引抜かれたことを検知する
ものであればよい。 Further, in the above embodiment, in order to detect that a predetermined amount of supernatant liquid in one cycle of the biological treatment tank 10 has been drawn into the treated water tank 33, the biological treatment tank 10
Based on the supernatant liquid level of 0, it is detected when the supernatant liquid withdrawal lower limit level LWL is reached,
A second level switch 37 is provided which stops drawing out the supernatant liquid from the biological treatment tank 10 and starts the pump 35 based on the detection signal. Based on the level, a liquid level detector is installed in the treated water tank 33 to detect when the liquid level reaches the upper limit level H 2 WL.
may be provided. Furthermore, for example, the biological treatment tank 10
If the supernatant liquid discharged in one cycle is always constant and the relationship between the liquid levels in the biological treatment tank 10 and the treated water tank 33 is constant, a liquid level detector and a pump are installed to stop drawing out the supernatant liquid. 35 may be provided separately for the biological treatment tank 10 and the treated water tank 33. In addition, if the liquid level in the treated water tank 33 (upper limit level H 2 WL) when the drawing of the supernatant liquid from the biological treatment tank 10 to the treated water tank 33 is completed is the same level as the lower limit level LWL for drawing out the supernatant liquid, When the drawing of the clear liquid is finished, the supernatant liquid no longer flows through the communication pipe 13, so instead of the second level switch 37, for example, a timer is used, and the time for drawing the supernatant liquid is set in advance with some margin. However, after the drawing of the supernatant liquid is completed, the pump 35 may be activated by the timer, in short, a predetermined amount of the supernatant liquid in one cycle of the biological treatment tank is directly or indirectly drawn into the treated water tank. Any device that can detect this is fine.
さらに以上の実施例では、処理水槽33の液面
が所定の下限レベルL2WLになつたことを検知し
ポンプ35を停止するために第1レベルスイツチ
36を用いたが、これに代えてポンプ35の吐出
側配管に積算流量計を取付け、これにより生物処
理槽10の1サイクルで排出される上澄液量と略
等しい液量が処理水槽33から排出された時点を
検知し上記ポンプ35を停止するようにしてもよ
い。また上記生物処理槽10と処理水槽33が次
工程の装置等より高い位置にあるように構成すれ
ば、上記ポンプ35は当然省略でき、その代りに
電磁弁等により処理水槽33から上澄液の排出を
制御するようにすればよい。したがつて本発明に
係る排出手段は種々の構成が存在する。 Furthermore, in the above embodiment, the first level switch 36 was used to detect that the liquid level in the treated water tank 33 had reached the predetermined lower limit level L2WL and stop the pump 35. An integrated flow meter is attached to the discharge side piping of the biological treatment tank 10, and this detects when a liquid volume approximately equal to the amount of supernatant liquid discharged in one cycle of the biological treatment tank 10 is discharged from the treated water tank 33, and the pump 35 is activated. It may be stopped. Furthermore, if the biological treatment tank 10 and the treated water tank 33 are configured to be located at a higher position than the equipment for the next process, the pump 35 can of course be omitted, and instead, the supernatant liquid is pumped from the treated water tank 33 using a solenoid valve or the like. Emissions should be controlled. Therefore, the ejection means according to the present invention has various configurations.
またさらに、本発明は、上澄液引抜きの開始及
び終了を起倒装置15によらず第14図の如く弁
3を開閉することによつて行う生物処理装置にお
いても同様に適用できることは言うまでもない。 Furthermore, it goes without saying that the present invention can be similarly applied to a biological treatment apparatus in which the drawing of supernatant liquid is started and ended by opening and closing the valve 3 as shown in FIG. 14, not by the raising device 15. .
「発明の効果」
以上説明したように、本発明の回分式生物処理
装置は、生物処理槽の側傍に処理水槽を設置し、
生物処理槽内の上澄液を上澄液引抜き管を通じて
処理水槽内に導くようにしたものであり、生物処
理槽内の液面が上澄液引抜き下限レベルに近づく
と処理水槽の液面が連通管のレベルを越えている
ので、処理水槽に引抜かれる上澄液の流量が非常
に減少するから、沈降性の悪い汚泥の場合でも、
引抜き時間を大巾に増大させることなく汚泥の巻
き込みを確実に防止することができ、また、生物
処理槽の液面が上澄液引抜き下限レベルに達した
以降に処理水槽内の上澄液を排出手段により排出
するようにしたものであるから、一時に大量の上
澄液が排出されるといつた問題が解決され、また
次工程の処理装置を小型化できるといつた効果を
奏する。"Effects of the Invention" As explained above, the batch type biological treatment device of the present invention has a treated water tank installed beside the biological treatment tank,
The supernatant liquid in the biological treatment tank is guided into the treated water tank through a supernatant liquid withdrawal pipe, and when the liquid level in the biological treatment tank approaches the lower limit level for supernatant liquid withdrawal, the liquid level in the treated water tank decreases. Since it exceeds the level of the communication pipe, the flow rate of supernatant liquid drawn into the treatment water tank is greatly reduced, so even in the case of sludge with poor settling properties,
It is possible to reliably prevent the entrainment of sludge without significantly increasing the drawing time, and the supernatant liquid in the treated water tank can be removed after the liquid level in the biological treatment tank reaches the lower limit level for drawing the supernatant liquid. Since the liquid is discharged by a discharge means, the problem of a large amount of supernatant liquid being discharged at one time can be solved, and the processing equipment for the next step can be downsized.
第1図ないし第11図は本発明の一実施例を示
すもので、第1図は全体の断面図、第2図は上澄
液引抜き管の平面図、第3図は同要部断面の側面
図、第4図は第2図の―矢視断面図、第5図
は起倒装置の拡大図、第6図は第5図の―矢
視断面図、第7図は第5図の―矢視断面図、
第8図は第5図の―矢視図、第9図は排水処
理工程の説明図、第10図及び第11図は作用を
説明するための全体の断面図、第12図は他の実
施例を示す部分図、また、第13図及び第14図
はそれぞれ従来例を示す断面略図である。
10…生物処理槽、11…フロート、12…抜
出し口、13…連通管、14…上澄液引抜き管、
33…処理水槽、35…ポンプ、36…第1レベ
ルスイツチ、37…第2レベルスイツチ。
Figures 1 to 11 show an embodiment of the present invention, in which Figure 1 is a cross-sectional view of the entire structure, Figure 2 is a plan view of a supernatant liquid withdrawal pipe, and Figure 3 is a cross-sectional view of the main parts. A side view, FIG. 4 is a cross-sectional view taken in the direction of the arrow in FIG. 2, FIG. 5 is an enlarged view of the lifting device, FIG. - cross-sectional view,
Fig. 8 is a view taken along the - arrow in Fig. 5, Fig. 9 is an explanatory diagram of the wastewater treatment process, Figs. 10 and 11 are overall cross-sectional views for explaining the action, and Fig. 12 is another example of the process. A partial view showing an example, and FIGS. 13 and 14 are schematic cross-sectional views showing a conventional example, respectively. 10... Biological treatment tank, 11... Float, 12... Extraction port, 13... Communication pipe, 14... Supernatant liquid withdrawal pipe,
33...Treatment water tank, 35...Pump, 36...First level switch, 37...Second level switch.
Claims (1)
トと上澄液の抜出し口を有して少なくとも該先端
部分が水位の変動に追従する上澄液引抜き管と、
上記生物処理槽の1サイクルで排出される上澄液
量以上の容量を有する処理水槽と、一端が上記上
澄液引抜き管の基端に接続され他端が上記処理水
槽の上記生物処理槽における上澄液引抜き下限レ
ベル以下の位置で開口し、上記上澄液引抜き管に
よつて引抜かれた上澄液を上記処理水槽に導入す
る連通管と、所定量の上澄液が上記処理水槽に引
抜かれたことを直接または間接に検知して上記処
理水槽に受入れられた上澄液を、生物処理槽の次
のサイクルにおける所定量の上澄液が上記処理水
槽に受入れられたときの処理水槽における液面が
上記連通管の開口位置以上の高さにとどまる範囲
において、排出する排出手段とが備えられている
ことを特徴とする回分式生物処理装置。 2 連通管が生物処理槽の上澄液引抜き下限レベ
ルより下方に設けられていることを特徴とする特
許請求の範囲第1項記載の回分式生物処理装置。[Scope of Claims] 1. A supernatant liquid withdrawal pipe that is installed in a biological treatment tank and has a float and a supernatant liquid extraction port at its tip portion, and at least the tip portion follows fluctuations in water level;
A treatment water tank having a capacity equal to or greater than the amount of supernatant liquid discharged in one cycle of the biological treatment tank; a communication pipe that opens at a position below the lower limit level for supernatant liquid withdrawal and introduces the supernatant liquid drawn by the supernatant liquid withdrawal pipe into the treatment water tank; The supernatant liquid is directly or indirectly detected and received into the treated water tank, and the treated water tank is used when a predetermined amount of supernatant liquid is received into the treated water tank in the next cycle of the biological treatment tank. A batch-type biological treatment apparatus, comprising a discharge means for discharging the liquid within a range where the liquid level remains at a height equal to or higher than the opening position of the communication pipe. 2. The batch-type biological treatment apparatus according to claim 1, wherein the communication pipe is provided below the lower limit level for drawing out the supernatant liquid of the biological treatment tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60234725A JPS6295199A (en) | 1985-10-21 | 1985-10-21 | Batch type biological treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60234725A JPS6295199A (en) | 1985-10-21 | 1985-10-21 | Batch type biological treatment device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6295199A JPS6295199A (en) | 1987-05-01 |
| JPH0359759B2 true JPH0359759B2 (en) | 1991-09-11 |
Family
ID=16975392
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60234725A Granted JPS6295199A (en) | 1985-10-21 | 1985-10-21 | Batch type biological treatment device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6295199A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5885845A (en) * | 1993-12-22 | 1999-03-23 | Nippon Sanso Corporation | Method for detecting inorganic hydrides, inorganic halides and organometallic compounds in a gas using copper hydroxide |
-
1985
- 1985-10-21 JP JP60234725A patent/JPS6295199A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6295199A (en) | 1987-05-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |