JP3183546B2 - Dispensing and measuring device for treated water - Google Patents
Dispensing and measuring device for treated waterInfo
- Publication number
- JP3183546B2 JP3183546B2 JP33117891A JP33117891A JP3183546B2 JP 3183546 B2 JP3183546 B2 JP 3183546B2 JP 33117891 A JP33117891 A JP 33117891A JP 33117891 A JP33117891 A JP 33117891A JP 3183546 B2 JP3183546 B2 JP 3183546B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- chamber
- pipe
- treated water
- distribution
- 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 - Fee Related
Links
Landscapes
- Branch Pipes, Bends, And The Like (AREA)
- Treatment Of Biological Wastes In General (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、主に、屎尿排水と生活
雑排水を合併処理する小型合併処理浄化槽において、汲
み上げられた処理水を適正に配分して、その流出量を可
変調節自在とする処理水の分配計量装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention mainly relates to a small-sized combined treatment septic tank for combining and treating human wastewater and household wastewater. The present invention relates to a device for distributing and measuring treated water.
【0002】[0002]
【従来の技術】本発明者は、先に、特願平2−1831
35号の明細書、図面において、『屎尿排水と生活雑排
水を合併処理するに有用な小型合併処理浄化槽における
排出流量の調整装置』を提案しているが、その第3図に
おいて、沈澱処理された処理水を汲み上げるエアリフト
ポンプ装置を、ポンプ槽に降設したリフト管と、当該リ
フト管に連結したエアリフト用給気管とで構成し、当該
エアリフトポンプ装置で汲み上げられた処理水を箱状の
分配計量装置へ汲み上げた上で、所定の処理工程へ分配
供給するようにしている(勿論、第4図に示すように、
エアリフトポンプ装置に代えて、モータポンプ装置によ
り汲み上げることもできる)。2. Description of the Related Art The present inventor has previously described Japanese Patent Application No. Hei 2-1831.
In the specification and drawings of No. 35, "a device for adjusting the discharge flow rate in a small-scale combined treatment septic tank useful for combining wastewater and household wastewater" is proposed. In FIG. An air lift pump device that pumps up the treated water is composed of a lift pipe descending to the pump tank and an air lift air supply pipe connected to the lift pipe, and the treated water pumped by the air lift pump device is distributed in a box shape. After being pumped to the weighing device, it is distributed and supplied to a predetermined processing step (of course, as shown in FIG. 4,
Instead of the air lift pump device, it can be pumped by a motor pump device).
【0003】この計量装置の構造は、計量箱の中央部に
処理水の流入室を設け、その両側位置に流出室を配設
し、当該流出室と流入室を固定ゲートで間仕切り形成
し、当該固定ゲートに対して昇降ゲートを昇降自在に支
持し、その内、一方の流出室には、循環返送管が連結さ
れ、計量装置に一旦汲み上げた処理水の一部を、嫌気濾
床接触曝気タイプの小型合併処理浄化槽における最先の
夾雑物除去槽へ返送し、それを合併排水と混ぜ合わせて
浄化処理に供することで循環させ、最終的に、脱窒処理
された処理水が得られるようにしている。[0003] The structure of this measuring device is such that a treatment water inflow chamber is provided in the center of a measurement box, outflow chambers are arranged on both sides thereof, and the outflow chamber and the inflow chamber are partitioned by a fixed gate. A lift gate is supported to the fixed gate so as to be able to move up and down freely, and a circulation return pipe is connected to one of the outflow chambers. It is returned to the first contaminant removal tank in the small-scale merger treatment septic tank, which is mixed with the merged wastewater and subjected to purification treatment to circulate so that finally denitrified treated water can be obtained. ing.
【0004】また、他方の流出室には、次の消毒槽への
移流管が連結され、計量装置に汲み上げた処理水の一部
を移流させて消毒処理に供するようにしている。また、
中央部の流出室には、計量装置に一旦汲み上げた処理水
をポンプ槽へ返送する返送管が連結され、そのポンプ能
力によるが、消毒槽への流出量と夾雑物除去槽への循環
返送量を差し引いた余剰分が、再びポンプ槽へ返送され
るようにしている。[0004] Further, an advection pipe to the next disinfecting tank is connected to the other outflow chamber, and a part of the treated water pumped to the measuring device is transferred to be supplied to the disinfecting treatment. Also,
A return pipe for returning the treated water once pumped to the measuring device to the pump tank is connected to the outflow chamber in the center, and depending on the pump capacity, the amount of outflow to the disinfection tank and the amount of circulation to the contaminant removal tank The surplus obtained by subtracting is returned to the pump tank again.
【0005】そこで、計量装置に汲み上げられた処理水
を3方向へ分配流出させるには、固定ゲートに対して昇
降ゲートを適宜高さに引き上げ、当該昇降ゲートの3角
堰を越流させることで、計量装置による流出量の分配調
整機能が発揮されるようにしている。[0005] Therefore, in order to distribute and discharge the treated water pumped into the measuring device in three directions, the lift gate is raised to an appropriate height with respect to the fixed gate, and the triangular weir of the lift gate overflows. In addition, the function of adjusting the distribution of the outflow by the metering device is exerted.
【0006】ところが、前記の先行技術に開示した分配
計量装置によるときは、汲み上げられた処理水を3方向
へ適正割合で配分するに、昇降ゲートを適宜上げ下げし
て、その3角堰からの溢流量を調節する溢流構造の分配
計量装置である為、その調節加減がし難いものであっ
た。However, in the case of the dispensing and measuring device disclosed in the above-mentioned prior art, in order to distribute the pumped treated water in three directions at an appropriate ratio, the elevation gate is appropriately raised and lowered to overflow the triangular weir. Since it is a distribution metering device having an overflow structure for adjusting a flow rate, it is difficult to adjust the flow rate.
【0007】特に、処理対象人員によって処理容量が種
々のタイプの小型合併処理浄化槽が製作されるのである
が、それに応じて次工程の消毒槽への移流量や最先工程
の夾雑物除去槽(又は嫌気濾床槽の最先部、或は、嫌気
濾床槽の第1室)への循環返送量を、適正な配分割合に
調節することが必要となる。その為には、処理容量が種
々異なるタイプの小型合併処理浄化槽であっても、計量
装置からの流出量を手軽に、また、適正に可変調節でき
る分配計量装置であることが望ましい。In particular, small-sized combined treatment / purification tanks of various types with different processing capacities are manufactured depending on the number of persons to be treated. Accordingly, the flow rate to the disinfection tank in the next process and the foreign matter removal tank ( Alternatively, it is necessary to adjust the circulating return amount to the forefront part of the anaerobic filter tank or the first chamber of the anaerobic filter tank to an appropriate distribution ratio . Therefore, it is desirable that the dispensing and weighing device be capable of easily and appropriately variably adjusting the amount of outflow from the weighing device, even in the case of a small-sized combined treatment septic tank having various types of processing capacity.
【0008】この点、従来、実開昭53−56112号
公報には、分流器本体内を、上端縁が水平な堰により流
入室と流出室とに分割すると共に、該流出室内を堰に沿
って移動可能な仕切板によって複数の分岐室に分割し、
流入室には液体の流入口を、また、各分岐室には各々液
体の流出口を設けてなる分流器が提案され、これにて任
意の流量比を得ることができるようにしている。 In this regard, conventionally, Japanese Utility Model Application Laid-Open No. 53-56112
In the official gazette, the inside of the flow divider main body is flowed by a weir whose top edge is horizontal.
It is divided into an entrance room and an outflow room, and the outflow room is along a weir.
Divided into a plurality of branch rooms by a movable partition plate,
A liquid inlet is provided in the inflow chamber, and a liquid is provided in each branch chamber.
A shunt with a body outlet has been proposed,
A desired flow ratio can be obtained.
【0009】[0009]
【発明が解決しようとする課題】ところが、実開昭53
−56112号公報に記載の分流器の場合には、流出室
を移動可能な仕切板を嵌め込んで分割するにすぎない
為、当該仕切板の分割位置が分岐室の一方に偏って嵌め
込まれるような場合には、その一方と他方にかかる水圧
負荷の変動によって、その区画位置が位置ズレを惹き起
こしたり、仕切板が 倒壊してしまう事態が発生し易い。 The object of the invention is to be Solved However, Japanese Utility Model 53
In the case of the flow divider described in Japanese Patent No.
Is simply divided by inserting a movable partition plate
Therefore, the dividing position of the partition plate is fitted to one side of the branch chamber
The water pressure on one and the other
Due to fluctuations in load, the position of the section causes a position shift.
Rubbing or a situation in which the partition plate collapses easily occurs.
【0010】また、小型合併浄化槽の分配計量装置に汲
み上げられる処理水は、その汲み上げ時の流勢によって
は、その流入室が大きく波動する傾向ともなる。その
上、通常、エアリフトポンプ装置により分配計量装置の
流入室に汲み上げられることから、汲み上げられた処理
水中に、空気泡が多量に混入した状態で汲み上げられ、
時として発泡現象が発生する事態ともなる。このような
事態を想定したとき、前記した実開昭53―56112
号公報に記載の分流器では、水平堰からの溢流量をコン
スタントに維持し難くい。[0010] In addition, the distribution and measurement device of the small-sized combined septic tank is pumped.
The treated water that is pumped up depends on the current at the time of pumping.
In addition, the inflow chamber tends to vibrate greatly. That
Above, usually, air distribution pump device
Because the water is pumped into the inflow chamber,
Pumped up in water with a lot of air bubbles mixed in,
Occasionally, a foaming phenomenon occurs. When such a situation is assumed, the above-mentioned Japanese Utility Model Publication No.
In the flow divider described in Japanese Patent Application Laid-Open Publication No. H11-146, it is difficult to constantly maintain the overflow from the horizontal weir.
【0011】[0011]
【課題を解決するための手段】そこで、本発明では、前
記の課題を解決するために、請求項1に記載するよう
に、計量箱の内部を溢流平堰板8で流入室X側と分配室
Z側に間仕切り形成し、当該溢流平堰板8の溢流幅の割
合を、分配室Zを区画する平堰区分板9a,9bにより
可変調節してなる処理水の分配計量装置において、前記
流入室Xと分配室Zとの間に中間室Yに区画し、当該中
間室Yと前記流入室Xとを潜流堰板7で間仕切り形成
し、中間室Yと分配室Zとを溢流平堰板8で間仕切り形
成し、前記分配室Zを構成する溢流平堰板8の背面内壁
面と、計量箱の背面板部2の内壁面に係合溝8a,2a
を等間隔に凹凸形成すると共に、前記分配室Zの底板部
5にも前記係合溝8a,2aを結ぶ係合溝5aを凹凸形
成し、前記分配室Zの適宜位置の係合溝8a,2a,5
aに平堰区分板9a,9bを差し込むようにしてなる処
理水の分配計量装置を提供したのである。Therefore SUMMARY OF THE INVENTION In the present invention, in order to solve the above problems, as described in claim 1
Then, the inside of the measuring box is filled with the overflow flat weir plate 8 and the inflow chamber X side and the distribution chamber.
A partition is formed on the Z side, and the overflow flat weir plate 8 is divided by the overflow width.
The combination is performed by flat weir partition plates 9a and 9b that partition the distribution chamber Z.
In the apparatus for distributing and measuring treated water variably adjusted,
An intermediate chamber Y is defined between the inflow chamber X and the distribution chamber Z.
A partition is formed between the inter-room Y and the inflow chamber X by the submerged weir plate 7.
Then, the intermediate chamber Y and the distribution chamber Z are partitioned by an overflow flat weir plate 8.
Inner wall on the back side of the overflow flat weir plate 8 forming the distribution chamber Z
Grooves 8a, 2a on the inner surface of the back plate 2 of the measuring box.
Are formed at regular intervals, and the bottom plate portion of the distribution chamber Z is formed.
5, the engaging groove 5a connecting the engaging grooves 8a and 2a
And the engagement grooves 8a, 2a, 5 at appropriate positions in the distribution chamber Z.
Thus, there is provided a device for distributing and measuring treated water in which the flat weir partition plates 9a and 9b are inserted into a.
【0012】[0012]
【作用】而して、エアリフトポンプ作用によって分配計
量装置Kの流入室Xへ汲み上げられた処理水は、当該流
入室Xで流入勢力が抑えられることで整流化すると共
に、潜流堰板7を潜流して次の中間室Yまで到達する間
に、汲み上げられた処理水に含まれる空気泡や発泡した
泡成分が潜流堰板7に制止された上で消泡化する。これ
にて整流化と消泡化がなされた処理水は、中間室Yから
溢流平堰板8を溢流 して分配室Zへと流入する。また、
分配室Z側には平堰区分板9a,9bが差し込まれ、サ
イド分割室Z 1 ,Z 3 とセンタ分割室Z 2 に間仕切られて
いる為、溢流平堰板8の有効溢流幅を均等に溢流して分
配室Z側へ流入する。これにより、個々の分割室Z 1 〜
Z 3 への流入量が配分調節される結果、個々の分割室Z 1
〜Z 3 からの適正な流出量が確保される。 The distribution meter is operated by the air lift pump.
The treated water pumped into the inflow chamber X of the quantity device K
When the inflowing force is suppressed by entering the room X,
At the same time, while submerging the submerged weir plate 7 to reach the next intermediate chamber Y
In addition, air bubbles and foams contained in the pumped treated water
The foam component is stopped by the submerged weir plate 7 and then defoamed. this
The rectified and defoamed treated water in
The overflow flat weir plate 8 overflows and flows into the distribution chamber Z. Also,
Flat weir dividing plates 9a and 9b are inserted into the distribution chamber Z side,
Partitioned between the id divided chamber Z 1, Z 3 and center dividing chamber Z 2
The effective overflow width of the overflow flat weir plate 8
It flows into the distribution room Z side. Thereby, the individual divided chambers Z 1 to
Results inflow into Z 3 is adjusted allocation of individual divided chamber Z 1
Proper outflow from to Z 3 is secured.
【0013】[0013]
【実施例】以下、本発明に係る分配計量装置Kの実施例
と、それをエアリフトポンプ装置Pの上方部にセットし
た場合について説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a dispensing and weighing device K according to the present invention and a case where the dispensing and weighing device K is set above an air lift pump device P will be described.
【0014】(分配計量装置について) 図1〜図4において、Kは合成樹脂製の計量装置であっ
て、正・背面板部1,2と左右の側面板部3,4と底板
部5とから矩形箱状の有底構造に一体形成され、その計
量箱の内部を正面板部1側の流入室Xと背面板部2側の
分配室Zとその間の中間室Yに区画して並設している。(Distribution and Measuring Apparatus) In FIGS. 1 to 4, K denotes a measuring apparatus made of a synthetic resin, and includes front and rear plate portions 1 and 2, left and right side plate portions 3 and 4, and a bottom plate portion 5. Are formed integrally in a rectangular box-shaped bottomed structure, and the inside of the weighing box is divided and arranged in parallel into an inflow chamber X on the front plate part 1 side, a distribution chamber Z on the back plate part 2 side, and an intermediate chamber Y therebetween. are doing.
【0015】6は正面板部1の中央上方位置に嵌着固定
した流入配管用管継ぎ手であって、ポンプ槽Fから汲み
上げられる処理水を流入室Xへ供給する。7は流入室X
と中間室Yを間仕切り形成する潜流堰板であって、その
左右両端部を側面板部3,4の内壁上半部に両端固定す
ると共に、その下部側を連通自在に開口形成し、流入室
Xに流入した処理水を潜流させて中間室Yへ移流するよ
うにしている。Reference numeral 6 denotes a pipe joint for an inflow pipe which is fitted and fixed at a position above the center of the front plate portion 1 and supplies treated water pumped up from a pump tank F to an inflow chamber X. 7 is the inflow chamber X
Submerged weir plate forming a partition between the inflow chamber and the intermediate chamber Y, the left and right ends of which are fixed to the upper halves of the inner walls of the side plates 3 and 4 and the lower side thereof is formed so as to be freely communicable. The treated water flowing into X is made to flow underground and transferred to the intermediate chamber Y.
【0016】8は中間室Yと分配室Zを間仕切り形成す
る上面が平坦な溢流堰板(以下、溢流平堰板という)で
あって、その左右両端部を側面板部3,4の下半部に両
端固定し、その下端部を底板部5に固定すると共にその
上部側を解放している。8a,2a,5aは分配室Zの
内面に略等間隔に凹凸形成した係合溝であって、溢流平
堰板8の背面部に係合溝8aを連設し、背面板部2の内
壁面の係合溝2aを連設し、此等の係合溝8a,2aを
前後対称的に凹凸形成すると共に、その間の底板部5に
も凹凸形成した係合溝5aを連設している。Reference numeral 8 denotes an overflow weir plate (hereinafter, referred to as an overflow flat weir plate) having a flat upper surface which forms a partition between the intermediate chamber Y and the distribution chamber Z. Both ends are fixed to the lower half, the lower end is fixed to the bottom plate 5 and the upper side is open. Reference numerals 8a, 2a and 5a denote engagement grooves formed on the inner surface of the distribution chamber Z at substantially equal intervals so that the engagement grooves 8a are continuously provided on the rear surface of the overflow flat weir plate 8. the engagement groove 2a of the inner wall surface provided continuously, the engagement groove 8a of these things, with 2a to the front and rear symmetrical manner roughening, continuously provided the engagement groove 5a were also uneven therebetween of the bottom plate 5 ing.
【0017】9a,9bは溢流平堰板8を分配室Z側で
区分する平堰区分板であって、これを分配室Zに凹成し
た係合溝8a,2a,5aの適宜位置に上方から差し込
むことで、分配室Zの内部を左右幅方向に3室程度に間
仕切り形成している。即ち、左右に間隔を隔てて差し込
まれる2枚の平堰区分板9a,9bによって、分配室Z
の内部を、中央位置のセンタ分割室Z2と、左右両側位
置のサイド分割室Z1,Z2に区画し、これにて溢流平堰
板8を溢流する処理水のサイド分割室Z1,Z3への流入
量と、センタ分割室Z2への流入量の配分割合が調節さ
れる結果、サイド分割室Z1,Z3からの流出量と、セン
タ分割室Z2からの流出量が適正に調節されることにな
る。Reference numerals 9a and 9b denote flat weir partitioning plates for dividing the overflow flat weir plate 8 on the distribution chamber Z side. The flat weir partitioning plates 9a and 9b are located at appropriate positions of the engaging grooves 8a, 2a and 5a formed in the distribution chamber Z. By inserting from above, the inside of the distribution chamber Z is partitioned into about three chambers in the left-right width direction. That is, the distribution chamber Z is formed by the two flat weir dividing plates 9a and 9b inserted into the left and right at an interval.
Is divided into a center divided chamber Z 2 at a central position and side divided chambers Z 1 and Z 2 at both left and right positions, whereby the side divided chamber Z of treated water overflowing the overflow flat weir plate 8. 1, the inflow into Z 3, results allocations of inflow into the center dividing chamber Z 2 is adjusted, the outflow from the side split chamber Z 1, Z 3, the outflow from the center dividing chamber Z 2 The amount will be adjusted appropriately.
【0018】10a〜10cは略同一径の流出配管用管
継ぎ手であって、サイド分割室Z1,Z3の側面板部3,
4の下方部に管継ぎ手10a,10cが嵌着固定され、
また、センタ分割室Z2の底板部5に管継ぎ手10bが
嵌着固定されている。8bは溢流平堰板8の左右両端部
に斜め上方へ傾設した立ち上げ部であって、側面板部
3,4の内側に管継ぎ手10a,10cが僅かに突出し
ている長さ分だけ溢流幅を狭めた関係としているが、当
該管継ぎ手10a,10cを側面板部3,4と面一又は
その外側面側に直接固定したような場合には、立ち上げ
部8bは不要となる。Reference numerals 10a to 10c denote pipe joints for outflow pipes having substantially the same diameter, and the side plate portions 3, 3 of the side divided chambers Z 1 and Z 3.
4. Pipe joints 10a and 10c are fitted and fixed to the lower part of
Further, pipe joint 10b is fitted and fixed to the bottom plate 5 of the center dividing chamber Z 2. Reference numeral 8b denotes a rising portion which is inclined obliquely upward at both left and right ends of the overflow flat weir plate 8, and corresponds to the length of the pipe joints 10a and 10c slightly protruding inside the side plate portions 3 and 4. Although the overflow width is narrowed, when the pipe joints 10a and 10c are directly flush with the side plates 3 and 4 or directly on the outer side thereof, the rising portion 8b becomes unnecessary. .
【0019】(エアリフトポンプ装置について) 前記の分配計量装置Kは、図5〜図10に示す嫌気濾床
接触曝気タイプの小型合併処理浄化槽S1,S2における
槽上方部の適所に配置され、沈澱槽Dで沈澱処理された
処理水が流入するポンプ槽Fと、次の消毒槽Eと、最先
位置の夾雑物除去槽A又は嫌気濾床槽Bの最先部或は嫌
気濾床槽の第1室B1に対して配管構成されるのである
が、その内、本発明の分配計量装置Kが組み込まれるポ
ンプ槽Fと、そのエアリフトポンプ装置Pの構成を図4
に基づいて説明する。(Regarding the Air Lift Pump Device) The distribution and metering device K is disposed at an appropriate position above the tanks of the small-sized combined treatment / purification tanks S 1 and S 2 of the anaerobic filter bed contact aeration type shown in FIGS. A pump tank F into which the treated water subjected to the precipitation treatment in the sedimentation tank D flows, a next disinfecting tank E, and a foremost part of the impurity removing tank A or the anaerobic filter bed tank B at the foremost position or an anaerobic filter bed tank. first chamber although being piping configured for B 1, of which, a pump tank F for dispensing metering device K of the present invention is incorporated, the configuration of the air lift pump device P 4 of
It will be described based on.
【0020】11はポンプ槽Fの内部に降設した処理水
のリフト管であって、その基端部側を分配計量装置Kの
流入配管用管継ぎ手6に連結し、その下端部をポンプ槽
Fの槽底部に開口形成している。12はポンプ槽Fの内
部に降設したエアリフト用給気管であって、その下端部
を、リフト管11の下端寄りの位置に嵌合した異径のT
型管継ぎ手11aに配管し、エアリフト作用によってポ
ンプ槽Fの処理水を汲み上げるようにしている。Numeral 11 denotes a lift pipe for treated water which is set down inside the pump tank F. The base end of the lift pipe is connected to the inlet pipe joint 6 of the distributing / metering device K, and the lower end thereof is connected to the pump tank. An opening is formed at the bottom of the tank of F. Reference numeral 12 denotes an air-lifting air supply pipe which is lowered inside the pump tank F, and has a lower end fitted to a position near the lower end of the lift pipe 11 having a different diameter.
The pipe is connected to the mold pipe joint 11a, and the treated water in the pump tank F is pumped up by an air lift action.
【0021】13は小型合併処理浄化槽S1,S2におけ
る消毒槽Eへの移流管であって、その基端部を一方のサ
イド分割室Z3の管継ぎ手10cに連結している。14
は汲み上げられた処理水の循環返送管であって、その基
端部を他方のサイド分割室Z1における管継ぎ手10a
に連結し、その先端部を後記する応用例1の小型合併処
理浄化槽S1における最先の夾雑物除去槽A、又は、嫌
気濾床槽Bの最先部、或は、応用例2の小型合併処理浄
化槽S2における嫌気濾床槽の第1室B1に臨ませてい
る。Reference numeral 13 denotes an advection pipe to the disinfection tank E in the small-sized combined treatment / purification tanks S 1 and S 2 , the base end of which is connected to the pipe joint 10 c of the one side divided chamber Z 3 . 14
A circulation return pipe of treated water is pumped, the pipe fittings 10a and the base end portion of the other side divided chamber Z 1
Linked to its tip portion to below the application example 1 of a small combined treatment of the earliest in the septic tank S 1 contaminant removing tank A, or earliest parts of the anaerobic filter bed chamber B, or, in Application Example 2 Small and to face the first chamber B 1 of anaerobic filter bed chamber in combined treatment septic tank S 2.
【0022】15は分配計量装置Kに一旦汲み上げられ
た処理水の返送管であって、その基端部をセンタ分割室
Z2の管継ぎ手10bに連結し、他端部をポンプ槽Fの
上方部に連結している。16は沈澱槽Dの上層部の処理
水中に横設した集水管であって、T型管継ぎ手16aに
よって連結した前後の集水管16を連通自在に連結配管
し、それを沈澱槽Dにおけるローレベルの水位線Lより
下側の処理水中に水没状態で横設すると共に、当該集水
管16の前後両端部を栓継ぎ手16bで閉栓している。
17は集水管16への通水孔であって、集水管16の上
下位置(左右両側位置と下部位置でも可)に幅方向に間
隔を隔てて穿設している。[0022] 15 is a return pipe of the treated water pumped up once the dispensing metering device K, connecting the proximal end to the pipe joint 10b of the center dividing chamber Z 2, above the pump tank F and the other end Connected to the department. Reference numeral 16 denotes a water collecting pipe provided in the upper part of the settling tank D in the treated water. The collecting pipe 16 is connected to the front and rear collecting pipes 16 connected by a T-type pipe joint 16a so as to be able to communicate with each other. The water collecting pipe 16 is closed horizontally by plug joints 16b while being horizontally submerged in the treated water below the water level line L.
Reference numeral 17 denotes a water passage hole for the water collecting pipe 16, which is formed at an upper and lower position of the water collecting pipe 16 (or at both left and right positions and a lower position) at intervals in the width direction.
【0023】18は集水管16の管継ぎ手16aの上部
側に連結したT型管継ぎ手であって、その側方への突出
部を、沈澱槽Dにおけるローレベルの水位線L上の位置
で、ポンプ槽F上方部の外側面に連結固定している。1
9は管継ぎ手18の上部側に連結した点検筒であって、
その上端部に螺合したプラグ20を取り外すことによ
り、集水管16からポンプ槽Fへの処理水の流入状況が
観察できるようにしている。尚、11bはリフト管11
の上端部に継設したT型管継ぎ手であって、その上部側
にプラグ20aを螺合し、リフト管11の内部を点検可
能としている。Numeral 18 denotes a T-shaped pipe joint connected to the upper side of the pipe joint 16a of the water collecting pipe 16, and its laterally projecting portion is positioned at a low level water level line L in the settling tank D, It is connected and fixed to the outer surface of the upper part of the pump tank F. 1
9 is an inspection cylinder connected to the upper side of the pipe joint 18,
By removing the plug 20 screwed to the upper end, the inflow of the treated water from the water collecting pipe 16 to the pump tank F can be observed. 11b is the lift pipe 11
Is a T-shaped pipe joint that is connected to the upper end portion of the lift pipe 11, and a plug 20a is screwed into the T-shaped pipe joint so that the inside of the lift pipe 11 can be inspected.
【0024】(処理水の分配計量工程について) そこで、槽外のブロア(図示せず)からエアリフト用給
気管12への給気作用を受けると、ポンプ槽Fの処理水
は、リフト管11の下端開口部から引き込まれ、そのエ
アリフト作用によって管内を上昇して分配計量装置Kの
流入室Xへと汲み上げられる。流入室Xへ流入した処理
水は、潜流堰板7を潜流して中間室Yへ流入し、更に
は、溢流平堰板8を溢流して分配室Zへと流入する。(Regarding the Process of Distributing and Measuring Treated Water) When the air supplied from the blower (not shown) outside the tank is supplied to the air lift supply pipe 12, the treated water in the pump tank F is discharged from the lift pipe 11. It is drawn in from the lower end opening, rises in the pipe by its air lift action, and is pumped into the inflow chamber X of the distribution and metering device K. The treated water that has flowed into the inflow chamber X flows through the submerged weir plate 7 and flows into the intermediate chamber Y, and further overflows the overflow flat weir plate 8 and flows into the distribution chamber Z.
【0025】分配室Z側には平堰区分板9a,9bが差
し込まれ、サイド分割室Z1,Z3とセンタ分割室Z2に
間仕切られている為、溢流平堰板8の有効溢流幅を均等
に溢流して分割室Z側に流入する処理水は、当該平堰区
分板9a,9bの差し込み位置により、個々の分割室Z
1〜Z3への流入量が配分調節される結果、個々の分割室
Z1〜Z3から適正な流出量が確保されることになる。The flat weir dividing plates 9a and 9b are inserted into the distribution chamber Z side, and are partitioned into the side divided chambers Z 1 and Z 3 and the center divided chamber Z 2. The treated water flowing into the divided chamber Z after overflowing the flow width uniformly flows into the individual divided chambers Z depending on the insertion positions of the flat weir partition plates 9a and 9b.
Results inflow into 1 to Z 3 is adjusted allocation, so that a proper outflow of individual divided chamber Z 1 to Z 3 is secured.
【0026】具体的には、立ち上げ部8bを除く溢流平
堰板8の有効溢流幅が30cmで、エアリフトポンプ装
置Pの揚水能力が毎分30リットルである場合、通常、
溢流平堰板8を毎分30リットルの処理水が分配室Z側
へ溢流して流入することになるが、その際、平堰区分板
9a,9bが差し込まれる係合溝8a,2a,5aを、
溢流平堰板8と背面板部2に沿って1cmピッチで凹凸
形成されていれば、その有効溢流幅の1cmから毎分1
リットルの処理水が分配室Z側へ流入することになる。Specifically, when the effective overflow width of the overflow flat weir plate 8 excluding the rising portion 8b is 30 cm and the pumping capacity of the air lift pump device P is 30 liters per minute,
Treated water of 30 liters per minute overflows the overflow flat weir plate 8 and flows into the distribution chamber Z side. At this time, the engagement grooves 8a, 2a, and 2b into which the flat weir partition plates 9a, 9b are inserted. 5a,
If the unevenness is formed at a pitch of 1 cm along the overflow flat weir plate 8 and the back plate part 2, the effective overflow width is 1 cm / min.
One liter of the treated water flows into the distribution chamber Z.
【0027】そこで、次の消毒槽Eへ毎分1リットル、
夾雑物除去槽Aへ毎分4リットルの流出量を確保する為
には、一方の平堰区分板9bの差し込み位置を計量箱の
側面板部4から1cm隔てた位置(実際は、立ち上げ部
8bの幅を加算する必要がある)に、また、他方の平堰
区分板9aの差し込み位置を、側面板部3から4cm隔
てた位置(同じく、立ち上げ部8bの幅を加算する必要
がある)にある係合溝8a,2a,5aに嵌合支持する
ことで、サイド分割室Z1,Z3への流入量が適正に配分
される。その結果、平堰区分板9a,9bの間の溢流幅
25cmからは、センタ分割室Z2へ毎分25リットル
が溢流されることになる。Then, 1 liter per minute to the next disinfecting tank E,
In order to secure a flow rate of 4 liters per minute to the impurity removing tank A, the insertion position of one of the flat weir partition plates 9b is separated from the side plate 4 of the measuring box by 1 cm (actually, the rising portion 8b And the insertion position of the other flat weir dividing plate 9a is separated by 4 cm from the side plate portion 3 (similarly, the width of the rising portion 8b needs to be added). engaging groove 8a in, 2a, by fitting the support to 5a, inflow into side divided chamber Z 1, Z 3 is properly distributed. As a result, from the overflow width of 25 cm between the flat weir partition plates 9a and 9b, 25 liters per minute overflows into the center divided chamber Z2.
【0028】尚、集水管16とポンプ槽Fとは沈澱槽D
のローレベルの水位線Lで連通しており、当該ローレベ
ルの水位線Lとハイレベルの水位線Hとの間にある槽外
の処理水は、当然ながらポンプ槽F内の処理水が汲み上
げられるに伴って集水管16の通水孔17から管内へ流
入した上で、分配計量装置Kへ汲み上げられることで、
小型合併処理浄化槽S1,S2における排出流量の調節が
日を通じて効率良く行われる。The collecting pipe 16 and the pump tank F are connected to a settling tank D.
The low-level water level line L communicates with the low-level water level line L and the high-level water level line H. The treated water outside the tank is naturally pumped by the treated water in the pump tank F. As the water flows into the pipe from the water hole 17 of the water collecting pipe 16 as it is drained, it is pumped up to the distribution metering device K,
Adjustment of the discharge flow rate in the small-sized combined treatment septic tanks S 1 and S 2 is efficiently performed throughout the day.
【0029】然も、ポンプ槽Fに流入した処理水を、エ
アリフトポンプ装置Pでポンプアップする場合、リフト
管11への給気量が略一定であると、その揚水能力は、
処理水の水位の変動による影響を受け、水位が上昇する
と揚水能力が上昇し、また、水位が下がってくると揚水
能力が落ちる傾向となり、やがては、処理水を汲み上げ
ない空運転の状態でも対応できるため、非常に都合がよ
い。When the treated water flowing into the pump tank F is pumped up by the air lift pump device P, if the amount of air supplied to the lift pipe 11 is substantially constant, the pumping capacity is
Due to the effect of fluctuations in the treated water level, the pumping capacity increases when the water level rises, and the pumping capacity tends to decrease when the water level decreases. It is very convenient because it can be done.
【0030】[0030]
【応用例】次に、本発明の分配計量装置Kとそのエアリ
フトポンプ装置Pを、小型合併処理浄化槽S1,S2に組
み込んだ場合の応用例を図5〜図10に従って説明す
る。Next, an application example in which the dispensing and weighing device K of the present invention and the air lift pump device P thereof are incorporated in small-sized combined treatment / purification tanks S 1 and S 2 will be described with reference to FIGS.
【0031】 (小型合併処理浄化槽の第1例について) 先ず、図5〜図7に示す嫌気濾床接触曝気タイプのカテ
ゴリーに属する第1例の小型合併処理浄化槽S1の全体
構造を説明する。この浄化槽S1の内部には、屎尿排水
と生活雑排水からなる合併排水が流入する一方の流入管
21側から、他方の処理水の放流管22にかけて、浄化
処理の工程順に応じて複数の処理槽A〜Fが区画形成さ
れた槽構造としている。その内、Aは合併排水の流入管
21側の最前部に区画形成した夾雑物除去槽であって、
屎尿排水や生活雑排水の中に混入されて浄化処理できな
い夾雑物を沈澱分離させることで除去する。(First Example of Small Merged Septic Tank) First, the overall structure of the first small merged septic tank S 1 of the first example belonging to the category of the anaerobic filter bed contact aeration type shown in FIGS. 5 to 7 will be described. Inside the septic tank S 1, from one inlet pipe 21 side of the merger wastewater consisting life gray water and human waste effluent flows, over the discharge tube 22 of the other of the treated water, a plurality of processes in accordance with the order of steps of the purification process The tanks A to F have a partitioned tank structure. Among them, A is a contaminant removal tank partitioned and formed at the forefront on the inflow pipe 21 side of the combined wastewater,
Impurities that cannot be purified by being mixed into human wastewater or household wastewater are removed by sedimentation.
【0032】Bは夾雑物除去槽Aに隣接して区画形成さ
れた次の嫌気濾床槽であって、当該嫌気濾床槽Bに設け
た嫌気性微生物の濾床23(以下、嫌気濾床という)
に、嫌気性微生物を棲息させることで嫌気処理に供され
る。Cは嫌気濾床槽Bに隣接して区画形成された次の接
触曝気槽であって、当該接触曝気槽Cに設けた接触濾材
の濾床24(以下、単に好気濾床という)に、好気性微
生物を棲息させることで好気処理に供される。Reference numeral B denotes a next anaerobic filter bed tank formed adjacent to the impurity removing tank A. The anaerobic filter bed 23 (hereinafter referred to as anaerobic filter bed) provided in the anaerobic filter tank B is provided. That)
In addition, anaerobic microorganisms inhabit and are subjected to anaerobic treatment. C is the next contact aeration tank partitioned and formed adjacent to the anaerobic filter tank B, and is provided on a filter bed 24 (hereinafter simply referred to as an aerobic filter bed) of a contact filter medium provided in the contact aeration tank C. It is subjected to aerobic treatment by inhabiting aerobic microorganisms.
【0033】Dは接触曝気槽Cに隣接して区画形成され
た次の沈澱槽であって、接触曝気槽Cで接触曝気処理さ
れて潜流した処理水を静置処理する。Eは沈澱槽Dの後
部上方位置に区画形成した消毒槽であって、通常、沈澱
槽Dの処理水の上澄みを消毒処理して、放流管22から
外部排出されるようにしている。Reference numeral D denotes a next sedimentation tank formed adjacently to the contact aeration tank C, in which the treated water subjected to the contact aeration treatment in the contact aeration tank C and buried is allowed to stand still. E denotes a disinfecting tank formed at a position above the rear part of the sedimentation tank D. Usually, the supernatant of the treated water in the sedimentation tank D is disinfected and discharged from the discharge pipe 22 to the outside.
【0034】25は夾雑物除去槽Aの流入管21側に区
画形成した流入ガイドであって、当該流入ガイド25と
流入管21側との間には、流入水を夾雑物除去槽Aの下
方へ向かって案内する角筒状の降流通路26を構成して
いる。27は夾雑物除去槽Aと嫌気濾床槽Bとを間仕切
る前部側の隔壁(以下、前部隔壁ともいう)であって、
その上方部には、左右幅方向に間隔を隔てて、夾雑物除
去槽Aからの移流口28が開口形成され、当該移流口2
8を含む前部隔壁27の前側には、左右幅方向に間隔を
隔てて形成した移流ガイド29が設けられ、当該移流ガ
イド29と前部隔壁27との間には、清掃口を兼ねる角
筒状移流通路30が構成される。従って、夾雑物除去槽
Aの槽底部に堆積した汚泥分を含む夾雑物は、当該移流
通路30を利用して、通常、1年当たり1回程度の割合
でバキュームカーで定期的に汲み出される。An inflow guide 25 is formed on the inflow pipe 21 side of the contaminant removal tank A. Between the inflow guide 25 and the inflow pipe 21 side, inflow water flows below the contaminant removal tank A. A downward flow passage 26 in the form of a square tube is provided to guide the flow toward the downstream side. Reference numeral 27 denotes a front partition (hereinafter, also referred to as a front partition) partitioning the impurity removing tank A and the anaerobic filter bed tank B,
In the upper part thereof, an advection port 28 from the contaminant removal tank A is formed at intervals in the left-right width direction.
An advection guide 29 formed at an interval in the left-right width direction is provided on the front side of the front partition wall 27 including the partition wall 8, and a rectangular tube serving as a cleaning port is provided between the advection guide 29 and the front partition wall 27. The advection passage 30 is formed. Therefore, the impurities including the sludge deposited on the bottom of the impurity removal tank A are usually pumped out by the vacuum car at a rate of about once a year using the advection passage 30. .
【0035】31は嫌気濾床槽Bと次の接触曝気槽Cを
間仕切る中間部の隔壁(以下、中間隔壁という)であっ
て、その上方部の中央位置には、前部隔壁27の場合と
略同じ高さ位置に嫌気濾床槽Bからの移流口32が開口
形成され、当該移流口32を含む中間隔壁31の前側に
は移流ガイド33が設けられ、当該移流ガイド33と中
間隔壁31との間には、清掃口を兼ねる角筒状移流通路
34を形成している。35は接触曝気槽Cの前部側の下
端位置に横設状態に配管した散気装置であって、接触曝
気槽Cに槽内循環流を形成することで、好気濾床24に
棲息する好気性微生物に対する酸素供給機能と槽内流の
循環を促進している。Reference numeral 31 denotes an intermediate partition wall (hereinafter referred to as an intermediate partition wall) for partitioning the anaerobic filter tank B from the next contact aeration tank C. An advection port 32 from the anaerobic filter bed B is formed at approximately the same height as the opening, an advection guide 33 is provided in front of the intermediate partition 31 including the advection port 32, and the advection guide 33 and the intermediate partition 31 are provided. A rectangular tubular advection passage 34 also serving as a cleaning port is formed between the two. Numeral 35 denotes an air diffuser arranged in a horizontal state at a lower end position on the front side of the contact aeration tank C, and inhabits the aerobic filter bed 24 by forming a circulation flow in the contact aeration tank C. It promotes the oxygen supply function for aerobic microorganisms and the circulation of the tank flow.
【0036】36は接触曝気槽Cの昇流通路であって、
散気装置35の直上部で、好気濾床24の前側と中間隔
壁31とを上下連通自在に開口形成され、当該昇流通路
36には、散気装置35への給気管37を配管構成して
いる。38は接触曝気槽Cと次の沈澱槽Dを間仕切る後
部側の隔壁(以下、後部隔壁という)であって、その下
端部には、接触曝気処理された処理水を次の沈澱槽D側
へ向かって移流させる潜流口39を開口形成している。Reference numeral 36 denotes an upflow passage of the contact aeration tank C,
Immediately above the air diffuser 35, the front side of the aerobic filter bed 24 and the intermediate partition wall 31 are formed so as to be freely openable and communicable with each other. are doing. Reference numeral 38 denotes a rear partition wall (hereinafter, referred to as a rear partition wall) for partitioning the contact aeration tank C and the next settling tank D, and the treated water subjected to the contact aeration treatment is provided at its lower end with the next settling tank D side. An opening is formed in the latent flow port 39 for advancing toward the bottom.
【0037】40は沈澱槽Dの処理水がオーバーフロー
する緊急避難時を想定して機能させる邪魔板であって、
消毒槽Eの前部側の上方部に、ハイレベルの水位線Hと
直交状に間仕切り形成され、沈澱槽Dの表層部に浮遊す
るスカムが、邪魔板40の後部側の移流口41から流出
しないようにしている。従って、比較的短時間に流入す
る合併排水とその処理水は、前記のオーバーフローを想
定した沈澱槽Dにおけるハイレベルの水位線Hの高さ範
囲内であって、然も、最先の夾雑物除去槽Aから嫌気濾
床槽B、好気濾床槽C、沈澱槽Dにかけての上層部側に
最大限貯溜されるようにしている。Reference numeral 40 denotes a baffle plate which functions assuming an emergency evacuation when the treated water in the settling tank D overflows.
A scum formed in the upper part on the front side of the disinfecting tank E at right angles to the high-level water level line H and floating on the surface of the sedimentation tank D flows out of the aft port 41 on the rear side of the baffle plate 40. I try not to. Accordingly, the combined wastewater and the treated water flowing in a relatively short time are within the height range of the high level water level line H in the settling tank D assuming the above-mentioned overflow. From the removal tank A to the anaerobic filter bed tank B, the aerobic filter bed tank C, and the sedimentation tank D, the maximum amount is stored in the upper layer side.
【0038】42は消毒槽Eの前壁上端部に設けた処理
水の消毒用受け樋であって、当該受け樋42には消毒筒
43が立ち上げられている。44は消毒槽Eを間仕切る
隔壁であって、その下端には消毒処理された排水が移流
する潜流口45を開口形成している。46は接触曝気槽
Cの槽底部に横設状態で配管構成した逆洗装置であっ
て、散気装置35への給気を停止した後、当該逆洗装置
46への給気作用によって、接触濾材24の内部を上昇
させる上向き流を定期的に作用させることにより、接触
濾材24に付着している汚泥分を逆洗洗浄する。Reference numeral 42 denotes a receiving trough for disinfecting treated water provided at the upper end of the front wall of the disinfecting tank E. In the receiving trough 42, a disinfecting cylinder 43 is set up. Reference numeral 44 denotes a partition for partitioning the disinfecting tank E, and a lower end thereof is formed with a latent flow opening 45 through which the disinfected wastewater flows. Numeral 46 denotes a backwashing device which is arranged in a horizontal state at the bottom of the contact aeration tank C. The backwashing device 46 stops supplying air to the diffuser 35 and then contacts the backwashing device 46 by supplying air to the backwashing device 46. The sludge adhering to the contact filter medium 24 is backwashed and washed by periodically applying an upward flow for raising the inside of the filter medium 24.
【0039】47は接触曝気槽Cの後部中央位置に立設
支持した剥離汚泥の引き抜き管であって、その下端部を
潜流口39の前部側に開口形成し、引き抜き管47の下
端部寄りの位置に嵌合支持した異径の管継ぎ手47A
に、剥離汚泥のエアリフト用給気管48を配管してい
る。49は剥離汚泥の移送管であって、その基端部を引
き抜き管47の上端部に連結し、その先端部を夾雑物除
去槽Aに臨ませている。Reference numeral 47 denotes a stripping pipe for separating sludge which is erected and supported at the center of the rear part of the contact aeration tank C. The lower end of the pipe is formed at the front side of the submerged outlet 39 and is located near the lower end of the drawing pipe 47. Pipe joint 47A of different diameter fitted and supported at the position
In addition, a supply pipe 48 for air lift of the separated sludge is provided. Reference numeral 49 denotes a transfer pipe for the exfoliated sludge, the base end of which is connected to the upper end of the drawing pipe 47, and the front end of which faces the impurity removing tank A.
【0040】前記の小型合併処理浄化槽S1において、
本発明の分配計量装置Kが組み込まれるポンプ槽Fは、
接触曝気槽Cと沈澱槽Dとの後部隔壁38の境界部分の
前部側中央位置に立設固定している。尚、リフト管11
のエアリフト用給気管12は、槽外にセットした流量調
整用ブロア(図示せず)からの給気本管50と配管構成
され、それ以外の散気用給気管37と、剥離汚泥の引き
抜き管47のエアリフト用給気管48と、逆洗装置46
への逆洗用給気管51は、同じく、槽外にセットした曝
気用ブロア(図示せず)からの給気本管52と分岐配管
している。In the small-sized combined treatment septic tank S 1 ,
The pump tank F in which the dispensing and weighing device K of the present invention is incorporated,
It is erected and fixed at the front center of the boundary between the contact aeration tank C and the settling tank D at the rear partition 38. The lift pipe 11
The air-lift air supply pipe 12 is constituted by a pipe connected to an air supply main pipe 50 from a flow rate adjustment blower (not shown) set outside the tank, and other air supply pipes 37 for diffusion and a pipe for pulling out separated sludge. 47, an air lift air supply pipe 48 and a backwashing device 46;
The backwash air supply pipe 51 is also branched from an air supply main pipe 52 from an aeration blower (not shown) set outside the tank.
【0041】(浄化処理工程について) 次に、前記の小型合併処理浄化槽S1における浄化処理
工程を説明するに、先ず、当該浄化槽S1における水位
線が、図5に示すようにローレベルの水位線Lにあると
仮定した場合、即ち、比較的短時間に合併排水が多量に
流入した場合でなく、通常時の流入量程度の屎尿排水又
は比較的少量の生活雑排水が流入する場合について説明
する。(Regarding the Purification Process) Next, a description will be given of the purification process in the above-mentioned small-scale combined treatment septic tank S 1. First, the water level line in the septic tank S 1 is changed to a low level water level as shown in FIG. The case where it is assumed to be on the line L, that is, not the case where a large amount of merged wastewater flows in a relatively short time, but the case where human wastewater or a relatively small amount of household wastewater flows in about the normal inflow amount will be described. I do.
【0042】(夾雑物除去工程) 通常時の流入量程度の屎尿排水又は比較的少量の生活雑
排水が排水されると、先ず、流入管21から夾雑物除去
槽Aの流入ガイド25に案内されて夾雑物除去槽A内へ
流入し、生活雑排水に混入して処理不能な夾雑物を沈澱
させて比較的時間をかけて分離除去が行われ、やがて移
流通路30へ入り込む。(Contaminant Removal Step) When human wastewater having a flow rate of about the normal amount or a relatively small amount of household wastewater is drained, first, the wastewater is guided from the inflow pipe 21 to the inflow guide 25 of the contaminant removal tank A. Then, it flows into the impurity removal tank A, mixes into the household wastewater, precipitates unprocessable impurities, and is separated and removed over a relatively long period of time.
【0043】(嫌気処理工程) また、前記の屎尿排水や生活雑排水の流入により、予め
移流通路30に貯溜されていた処理水は、前部隔壁27
の移流口28を越流して次の嫌気濾床槽Bへ送り出され
て流入し、嫌気濾床23を沈降しながら通過する過程
で、嫌気性微生物による嫌気処理が行われた上で、嫌気
濾床槽Bの後部側の移流通路34へ入り込む。(Anaerobic treatment step) The treated water previously stored in the advection passage 30 due to the inflow of the human wastewater or household wastewater is removed from the front partition wall 27.
In the process of being sent out and flowing into the next anaerobic filter bed B after passing through the advection port 28 of the anaerobic filter bed and passing through the anaerobic filter bed 23 while settling, the anaerobic treatment by the anaerobic microorganisms is performed, It enters the advection passage 34 on the rear side of the floor tank B.
【0044】(好気処理工程) また、夾雑物が除去された排水が嫌気濾床槽Bへ流入す
ると、予め移流通路34に貯溜されていた処理水は、中
間隔壁31の移流口32を越流し、今度は、好気性微生
物による好気処理を行う接触曝気槽Cへ流入する。この
接触曝気槽Cでは、散気装置35による槽内循環流が形
成されており、その好気濾床24を繰り返し循環するこ
とで、好気性微生物による好気処理が行われる。(Aerobic treatment step) When the wastewater from which impurities have been removed flows into the anaerobic filter bed tank B, the treated water previously stored in the advection passage 34 passes through the advection port 32 of the intermediate partition 31. Then, it flows into the contact aeration tank C for performing aerobic treatment by aerobic microorganisms. In the contact aeration tank C, a circulation flow in the tank is formed by the diffuser 35, and the aerobic filter bed 24 is repeatedly circulated to perform the aerobic treatment by the aerobic microorganisms.
【0045】(沈澱処理工程) やがて、好気処理の終わった処理水は、後部隔壁38の
下端部の潜流口39から沈澱槽Dへと徐々に流れ込ん
で、沈澱処理に供される。(Precipitation Treatment Step) The treated water that has been subjected to the aerobic treatment gradually flows into the precipitation tank D from the submerged outlet 39 at the lower end of the rear partition 38 and is subjected to the precipitation treatment.
【0046】(汲み上げ工程) 沈澱槽Dに流入した処理水の内、ローレベルの水位線L
の上層部に滞留する上澄み液は、集水管16の通水孔1
7からポンプ槽Fへと流入する。ポンプ槽Fへ流入した
処理水は、リフト管11の下端開口部から流入し、エア
リフト用給気管12からリフト管11への給気作用によ
って発生する多量の気泡によって、当該リフト管11内
を上昇移動することで分配計量装置Kへ汲み上げられ
る。(Pumping Step) Of the treated water flowing into the sedimentation tank D, the low level water level line L
The supernatant liquid staying in the upper layer portion of the water collection pipe 16 is
7 flows into the pump tank F. The treated water that has flowed into the pump tank F flows from the lower end opening of the lift pipe 11 and rises in the lift pipe 11 due to a large amount of air bubbles generated by the air supply operation from the air lift air supply pipe 12 to the lift pipe 11. By moving, it is pumped up to the distribution and metering device K.
【0047】(分流工程) 分配計量装置Kへ汲み上げられた処理水は、計量箱の溢
流平堰板8の溢流幅を、分配室Zを間仕切る平堰区分板
9a,9bの差し込み位置によって配分調節し、次の消
毒槽Eへの移流量と、最先の夾雑物除去槽Aへの循環返
送量と、ポンプ槽Fへの返送量が適度に流量調整されて
分流される。具体的には、小型合併処理浄化槽S1の大
きさが、処理対象人員が5人槽で、エアリフトポンプ装
置Pの揚水能力が、毎分30リットル程度の能力である
場合に、消毒槽Eへは毎分1リットル程度、夾雑物除去
槽Aへの返送量は毎分4リットル程度、その残り毎分2
5 程度が再びポンプ槽F内へ返送される。(Diversion step) The treated water pumped into the distribution and metering device K determines the overflow width of the overflow flat weir plate 8 of the measuring box and the insertion position of the flat weir partition plates 9a and 9b that partition the distribution chamber Z. Then, the flow rate to the next disinfecting tank E, the amount of circulating return to the first impurity removing tank A, and the amount of return to the pump tank F are appropriately adjusted and divided. Specifically, when the size of the small-sized combined treatment septic tank S1 is five tanks for processing and the pumping capacity of the air lift pump device P is about 30 liters per minute, Approximately 1 liter per minute, amount returned to impurity removal tank A is approximately 4 liters per minute, and the rest is 2 liters per minute.
About 5 is returned to the pump tank F again.
【0048】(消毒工程) その内、分配計量装置Kの移流管13から受け樋42へ
流出した処理水は、消毒筒43で消毒処理された上で、
放流管22から槽外へ排出される。(Disinfection Step) The treated water flowing out of the advection pipe 13 of the distribution and metering device K to the receiving gutter 42 is subjected to a disinfection treatment by a disinfection cylinder 43.
The water is discharged from the discharge pipe 22 to the outside of the tank.
【0049】(循環工程) また、分配計量装置Kへ汲み上げられた処理水の一部
を、最先の夾雑物除去槽Aへ返送した場合には、一旦処
理された処理水が、嫌気性微生物による嫌気処理の工程
中に適度に混在して、再び嫌気処理に供された上で、好
気処理に供されることで、最終的には、脱窒処理された
処理水が得られることになる。(Circulation Step) When a part of the treated water pumped to the distribution and metering device K is returned to the first foreign matter removal tank A, the treated water once treated is converted into an anaerobic microorganism. In the process of the anaerobic treatment by the moderately mixed, after being subjected to the anaerobic treatment again, and subjected to the aerobic treatment, finally, the denitrified treated water is obtained Become.
【0050】(排出流量の調整工程) 次に、前記の工程順に浄化処理が行われる小型合併処理
浄化槽S1において、朝方の7時台における主に洗濯排
水や台所排水等の生活雑排水を含む合併排水と、夕方の
6時台における風呂排水や台所排水等の生活雑排水を含
む合併排水が、日平均流入汚水量の6倍程度のピーク割
合で多量に流入するパターンが発生したとする。(Step of Adjusting Discharge Flow Rate) Next, in the small-sized combined treatment septic tank S 1 in which the purification treatment is performed in the order of the above-described steps, the waste water mainly including washing wastewater and kitchen wastewater at the 7 o'clock in the morning is included. It is assumed that a pattern occurs in which the combined drainage and the combined drainage including household wastewater such as bath drainage and kitchen drainage at 6 o'clock in the evening flow in large quantities at a peak ratio of about six times the average daily inflow sewage amount.
【0051】この場合、先ず、それを消毒槽Eを除く複
数の処理槽A〜Dのハイレベルの水位線Hの範囲内に滞
留させて浄化処理する一方、沈澱処理されてローレベル
の水位線Lの上層部に滞留する処理水を、集水管16の
通水孔17からポンプ槽Fへ流入させ、当該流入水をエ
アリフトポンプ装置Pで日を通じてコンスタントに汲み
上げると共に、本発明の分配計量装置Kにより分流させ
ることで、日を通じてコンスタントに槽外への排出に対
処する。In this case, first, it is kept in the range of the high level water level H of the plurality of processing tanks A to D excluding the disinfecting tank E to perform the purification treatment, while the sedimentation treatment is performed to make the low level water level line H. The treated water staying in the upper part of L is flowed into the pump tank F from the water hole 17 of the water collecting pipe 16 and the inflow water is constantly pumped up by the air lift pump device P throughout the day. By diverting the water, it constantly handles the discharge outside the tank throughout the day.
【0052】これにて比較的短時間に流入する合併排水
による影響を、複数の処理槽A〜Dのローレベルの水位
線Lとハイレベルの水位線Hの範囲で受け止め、ローレ
ベルの水位線Lの上層部に滞留する沈澱処理された処理
水を、エアリフトポンプ装置Pで日を通じて、或は、比
較的長い時間をかけて比較的コンスタントに処理水が汲
み上げられることで、可能な限り定量的に次の消毒処理
工程等への移流と槽外への放流が行われることになる。Thus, the influence of the merged wastewater flowing in a relatively short time is received within the range of the low-level water level line L and the high-level water level line H of the plurality of treatment tanks A to D, and the low-level water level line is obtained. The treated water remaining in the upper layer of L is pumped through the air by the air lift pump device P throughout the day or relatively constantly over a relatively long period of time, so that the treated water is as quantitatively as possible. Then, the transfer to the next disinfection process and the like and the discharge to the outside of the tank are performed.
【0053】その為、比較的短時間に多量に排出される
合併排水に対して、従来装置のように滞留時間の長短に
よる処理斑を引き起こす虞れなく、放流排水に対する処
理性能をコンスタントに維持することができ、此種の小
型合併処理浄化槽S1による生活雑排水を含む合併排水
の浄化処理に画期的な諸効果を齎す。Therefore, with respect to the combined wastewater discharged in a large amount in a relatively short time, there is no possibility of causing unevenness in treatment due to the length of the residence time unlike the conventional apparatus, and the treatment performance for the discharged wastewater is constantly maintained. it can, bring a breakthrough various effects to the purification process of the merger waste water containing life gray water due to the small size merger processing septic tank S1 of此種.
【0054】具体的には、5人槽程度の小型合併処理浄
化槽S1において、ハイレベルの水位線Hとローレベル
の水位線Lとの間に貯溜できる最大限の流入調整容量V
=500リットル程度、その流量調整高さ、即ち、ハイ
レベルの水位線Hとローレベルの水位線Lとの高位差を
20cm程度とし、その設定放流量を毎分0.5〜1リ
ットル程度の範囲内とすれば、比較的短時間に多量に流
入する合併排水に対する良好な流量調整機能が発揮され
る。尚、前記の場合に循環返送管14の先端部を夾雑物
除去槽Aに臨設させたが、嫌気濾床槽Bの最先部寄りの
位置に臨設させることもできる。Specifically, the maximum inflow adjustment capacity V that can be stored between the high-level water level line H and the low-level water level line L in the small-scale combined treatment / purification tank S 1 of about five tanks.
= 500 liters, the flow control height thereof, that is, the high level difference between the high level water level line H and the low level water level line L is about 20 cm, and the set discharge flow rate is about 0.5 to 1 liter per minute. Within this range, a good flow rate adjusting function for the combined drainage that flows in a large amount in a relatively short time is exhibited. In the above-mentioned case, the tip of the circulation return pipe 14 is provided at the impurity removing tank A, but it may be provided at a position near the foremost part of the anaerobic filter bed tank B.
【0055】 (小型合併処理浄化槽の第2例について) 次に、図8〜図10に示す小型合併処理浄化槽S2の場
合には、第1例の小型合併処理浄化槽S1における夾雑
物除去槽Aに代えて、嫌気濾床槽Bを前後2室に分割
し、その前部側を嫌気濾床槽第1室B1、その後部側を
嫌気濾床槽第2室B2に間仕切り形成している。その他
の相違点としては、第1例の場合と異なり、剥離汚泥の
引き抜き管47を接触曝気槽Cの前部側に縦設してい
る。また、ポンプ槽Fと槽外の集水管16とを連通自在
に配管した上で、ポンプ槽F内での流入管53をローレ
ベルの水位線Lと同じ高さ位置まで立ち上げ配管してい
る。それ以外の構成は、第1例と略同様であるので、そ
の説明を省略する。Next, in the case of the small-sized combined treatment / purification tank S 2 shown in FIGS. 8 to 10, in the case of the small-sized combined treatment / purification tank S 1 of the first example, the contaminant removal tank is used. Instead of A, the anaerobic filter bed tank B is divided into two front and rear chambers, the front side of which is partitioned into a first anaerobic filter tank chamber B 1 and the rear side thereof is partitioned into a second anaerobic filter tank chamber B 2. ing. Another difference is that unlike the case of the first example, a stripping pipe 47 for separating sludge is provided vertically at the front side of the contact aeration tank C. Further, after the pump tank F and the water collecting pipe 16 outside the tank are communicatively connected to each other, the inflow pipe 53 in the pump tank F is set up to the same level as the low-level water level line L. . The other configuration is substantially the same as that of the first example, and the description thereof is omitted.
【0056】(その他) 尚、沈澱分離接触曝気タイプの小型合併処理浄化槽(図
示せず)の場合には、前記の第1例や第2例の小型合併
処理浄化槽S1,S2とは異なり、嫌気濾床槽B又は嫌気
濾床槽の第1室B1と第2室B2がない代わりに、第1応
用例における夾雑物除去槽Aに相当する最前部に、即
ち、屎尿排水と生活雑排水の流入管21側に沈澱分離槽
A1を区画形成し、次の中間部を接触曝気槽Cに区画
し、また、処理水の放流管22側の後部側に沈澱槽Dに
区画形成した上で、接触曝気槽Cと沈澱槽Dの境界部分
にポンプ槽Fを配設し、沈澱槽Dの後部上方位置に消毒
槽Eを区画形成してなる槽構造、より具体的には、特願
平2−183135号の明細書とその添付図面の第6図
に図示したように構成される。(Others) In the case of a small-sized combined treatment / purification tank (not shown) of the sedimentation / separation / contact aeration type, it is different from the small-sized combined treatment / purification tanks S 1 and S 2 of the first and second examples. , and instead the second chamber B 2 is not first chamber B 1 of anaerobic filter bed chamber B or anaerobic filter bed chamber, the foremost portion corresponding to contaminant removal tank a in the first application example, i.e., the raw sewage wastewater life is defined and formed in the inflow pipe 21 side and the precipitate separation tank a 1 of wastewater, partition the next intermediate portion to the contact aeration tank C, also divided into precipitation tank D on the rear side of the discharge tube 22 side of the treated water After the formation, a pump tank F is disposed at the boundary between the contact aeration tank C and the precipitation tank D, and a disinfection tank E is formed at a position above the rear part of the precipitation tank D, more specifically, a tank structure. The configuration is as shown in the specification of Japanese Patent Application No. 2-183135 and FIG. 6 of the accompanying drawings.
【0057】この場合は、浄化処理工程中に嫌気処理工
程がなく、脱窒処理を行わないタイプであることから、
本発明の分配計量装置Hにおける分配室Zを、1枚の平
堰区分板9で2室に間仕切り形成し、次の沈澱槽Eへの
移流管13が管継ぎ手10cに配管され、また、ポンプ
槽Fへの返送管15が管継ぎ手10bに配管される反
面、管継ぎ手10aを栓継ぎ手(図示せず)で閉成する
か、或は、予め、管継ぎ手10aのない分配計量装置K
を使用することで対処することになる。In this case, since there is no anaerobic treatment step in the purification treatment step and no denitrification treatment is performed,
The distribution chamber Z in the distribution metering device H of the present invention is partitioned into two chambers by one flat weir partition plate 9, and the advection pipe 13 to the next settling tank E is piped to the pipe joint 10c. While the return pipe 15 to the tank F is piped to the pipe joint 10b, the pipe joint 10a is closed with a plug joint (not shown), or the distribution metering device K without the pipe joint 10a is previously provided.
It will be addressed by the use of.
【0058】[0058]
【発明の効果】本発明は、前記の請求項1に記載するよ
うに、計量箱の内部を溢流平堰板8で流入室X側と分配
室Z側に間仕切り形成し、当該溢流平堰板8の溢流幅の
割合を 、分配室Zを区画する平堰区分板9a,9bによ
り可変調節してなる処理水の分配計量装置において、前
記流入室Xと分配室Zとの間に中間室Yに区画し、当該
中間室Yと前記流入室Xとを潜流堰板7で間仕切り形成
し、中間室Yと分配室Zとを溢流平堰板8で間仕切り形
成し、前記分配室Zを構成する溢流平堰板8の背面内壁
面と、計量箱の背面板部2の内壁面に係合溝8a,2a
を等間隔に凹凸形成すると共に、前記分配室Zの底板部
5にも前記係合溝8a,2aを結ぶ係合溝5aを凹凸形
成し、前記分配室Zの適宜位置の係合溝8a,2a,5
aに平堰区分板9a,9bを差し込むようにしてなる処
理水の分配計量装置を提供したので、処理水を溢流平堰
板8を溢流させて分配室Zへ流入させるに、溢流平堰板
8の溢流幅を分配室Z側に差し込まれる平堰区分板9
a,9bの差し込み位置を代えることで、個々の分割室
Z1〜Z3への流入割合を適正に配分調節することで、個
々の分割室Z1〜Z3からの流出量を簡易迅速に可変調節
することができ、これを、屎尿排水と生活雑排水を合併
処理する小型合併処理浄化槽に組み込めば、汲み上げら
れた処理水に対する効果的な流量調整に対処することが
できる。 According to the present invention, there is provided the present invention as set forth in claim 1.
As described above, the inside of the measuring box is distributed to the inflow chamber X side by the overflow flat weir plate 8.
A partition is formed on the chamber Z side, and the overflow width of the overflow flat weir plate 8 is
The ratio is determined by the flat weir partition plates 9a and 9b that partition the distribution chamber Z.
Of the treated water distribution and metering device
The intermediate chamber Y is partitioned between the inflow chamber X and the distribution chamber Z.
A partition is formed between the intermediate chamber Y and the inflow chamber X by a submerged weir plate 7.
Then, the intermediate chamber Y and the distribution chamber Z are partitioned by an overflow flat weir plate 8.
Inner wall on the back side of the overflow flat weir plate 8 forming the distribution chamber Z
Grooves 8a, 2a on the inner surface of the back plate 2 of the measuring box.
Are formed at regular intervals, and the bottom plate portion of the distribution chamber Z is formed.
5, the engaging groove 5a connecting the engaging grooves 8a and 2a
And the engagement grooves 8a, 2a, 5 at appropriate positions in the distribution chamber Z.
a is provided with a treatment water distribution and metering device in which the flat weir dividing plates 9a and 9b are inserted into the distribution damper a. A flat weir dividing plate 9 into which the overflow width of the flowing weir plate 8 is inserted into the distribution chamber Z side
By changing the insertion positions of the a and 9b, the inflow rate into each of the divided chambers Z 1 to Z 3 is appropriately distributed and adjusted, so that the outflow from each of the divided chambers Z 1 to Z 3 can be easily and quickly performed. If it can be variably adjusted and incorporated into a small-sized combined treatment septic tank that combines and treats human wastewater and household wastewater, it is possible to cope with effective flow rate adjustment of the pumped treated water .
【0059】その際、本発明の分配計量装置では、分配
室Zを構成する溢流平堰板8の背面内壁面と、計量箱の
背面板部2の内壁面に係合溝8a,2aを等間隔に凹凸
形成すると共に、前記分配室Zの底板部5にも前記係合
溝8a,2aを結ぶ係合溝5aを凹凸形成し、前記分配
室Zの適宜位置の係合溝8a,2a,5aに平堰区分板
9a,9bを差し込むことで、当該平堰区分板9a,9
bを所定の位置に確実に保持する。その為、平堰区分板
9a,9bにかかる水圧負荷の変動により、その位置ズ
レを惹き起こしたり、倒壊するようなこともない。 At this time, the dispensing and weighing device of the present invention
The inner wall surface of the back surface of the overflow flat weir plate 8 constituting the chamber Z and the measuring box
Engagement grooves 8a, 2a are formed at regular intervals on the inner wall surface of back plate 2.
And also engages with the bottom plate 5 of the distribution chamber Z.
The engaging groove 5a connecting the grooves 8a and 2a is formed with irregularities, and
A flat weir dividing plate is provided in the engagement grooves 8a, 2a, 5a at appropriate positions in the chamber Z.
9a, 9b, the flat weir partition plates 9a, 9
b is securely held at a predetermined position. Therefore, the flat weir divider
Due to the fluctuation of the hydraulic load applied to 9a and 9b,
It doesn't wake or collapse.
【0060】また、流入室Xと分配室Zとの間に中間室
Yに区画し、当該中間室Yと前記流入室Xとを潜流堰板
7で間仕切り形成しているので、エアリフトポンプ作用
によって分配計量装置Kの流入室Xへ汲み上げられた処
理水は、当該流入室Xで流入勢力が抑えられることで整
流化すると共に、潜流堰板7を潜流して次の中間室Yへ
移流する間に、汲み上げられた処理水に含まれる空気泡
や発泡した泡成分が、当該潜流堰板7に制止されて消泡
化する。これにて整流化と消泡化がなされた処理水が、
中間室Yから溢流平堰板8を溢流して分配室Zへと流入
するに、当該溢流平堰板8の有効溢流幅を均等に溢流し
て分配室Z側へと流入する。その為、個々の分割室Z1
〜Z3から所定の流出量を確保することができ、その精
度の高い分配計量装置としての有用性を発揮する等の諸
効果を齎す。Further , an intermediate chamber is provided between the inflow chamber X and the distribution chamber Z.
Y, and the intermediate chamber Y and the inflow chamber X are submerged weir plates.
7, the partition is formed, so the air lift pump works
Is pumped into the inflow chamber X of the dispensing and weighing device K by the
The water is regulated by reducing the inflow force in the inflow chamber X.
While flowing through the submerged weir plate 7 to the next intermediate chamber Y.
Air bubbles in the treated water pumped during advection
And the foamed foam component is stopped by the submerged weir plate 7 and defoamed.
Become The rectified and defoamed treated water is
When the overflow flat weir plate 8 overflows from the intermediate chamber Y and flows into the distribution chamber Z, the effective overflow width of the overflow flat weir plate 8 uniformly overflows and flows into the distribution chamber Z side. Therefore, each divided room Z 1
It is possible to secure a predetermined outflow from to Z 3, leading to various effects such as to exert utility as high partition metering device with its accuracy.
【図1】本発明の分配計量装置を、背面側から見た一部
切り欠き斜視図である。FIG. 1 is a partially cutaway perspective view of a dispensing and weighing device of the present invention as viewed from the rear side.
【図2】分配計量装置の平面図である。FIG. 2 is a plan view of the dispensing and weighing device.
【図3】分配計量装置の縦断側面図である。FIG. 3 is a vertical sectional side view of the dispensing and weighing device.
【図4】本発明の分配計量装置とエアリフトポンプ槽と
を組み合わせた状態を示す一部切り欠き斜視図である。FIG. 4 is a partially cutaway perspective view showing a state where the dispensing and measuring device of the present invention and an air lift pump tank are combined.
【図5】本発明の分配計量装置とそのエアリフトポンプ
槽を、嫌気濾床接触曝気タイプの小型合併処理浄化槽の
第1応用例に組み込んだ状態を示す縦断正面図である。FIG. 5 is a vertical sectional front view showing a state in which the dispensing and measuring device of the present invention and its air lift pump tank are incorporated in a first application example of a small-sized combined treatment / purification tank of an anaerobic filter bed contact aeration type.
【図6】第1応用例の平面図である。FIG. 6 is a plan view of a first application example.
【図7】第1応用例の縦断側面図である。FIG. 7 is a vertical sectional side view of the first application example.
【図8】嫌気濾床接触曝気タイプの小型合併処理浄化槽
の第2応用例に組み込んだ状態を示す縦断正面図であ
る。FIG. 8 is a vertical sectional front view showing a state in which the small-sized combined treatment / purification tank of the anaerobic filter bed contact aeration type is incorporated in a second application example.
【図9】第2応用例の平面図である。FIG. 9 is a plan view of a second application example.
【図10】第2応用例の縦断側面図である。FIG. 10 is a vertical side view of a second application example.
K 分配計量装置 X 流入室 Y 中間室 Z 分配室 Z1〜Z3 分割室 F ポンプ槽 P エアリフトポンプ装置 1,2 正・背面板部 3,4 側面板部 5 底板部 6 流入配管用管継ぎ手 7 潜流堰板 8 溢流平堰板 2a,5a,8a 係合溝 9a,9b 平堰区分板 10a〜10b 流出配管用管継ぎ手 11 リフト管 12 給気管 13 移流管 14 循環返送管 15 返送管 16 集水管 17 通水孔 18 管継ぎ手 19 点検筒 20,20a プラグ S1,S2 小型合併処理浄化槽 A 夾雑物除去槽 A1 沈澱分離槽 B 嫌気濾床槽 B1 嫌気濾床槽第1室 B2 嫌気濾床槽第2室 C 接触曝気槽 D 沈澱槽 E 消毒槽 F ポンプ槽 P エアリフトポンプ装置 H ハイレベルの水位線 L ローレベルの水位線 21 流入管 22 放流管 23 嫌気濾床 24 好気濾床 25 流入ガイド 26 降流通路 27 前部隔壁 28 移流口 29 移流ガイド 30 移流通路 31 中間隔壁 32 移流口 33 移流ガイド 34 移流通路 35 散気装置 36 昇流通路 37 散気用給気管 38 後部隔壁 39 潜流口 40 邪魔板 41 移流口 42 受け樋 43 消毒筒 44 消毒隔壁 45 潜流口 46 逆洗装置 47 引き抜き管 48,51 給気管 49 移送管 50,52 給気本管K Distribution metering device X Inflow chamber Y Intermediate chamber Z Distribution chamber Z 1 to Z 3 divided chamber F Pump tank P Air lift pump device 1, Front / back plate portion 3, 4 Side plate portion 5 Bottom plate portion 6 Pipe joint for inflow pipe 7 Submerged weir plate 8 Overflow flat weir plate 2a, 5a, 8a Engagement groove 9a, 9b Flat weir dividing plate 10a-10b Outlet piping pipe joint 11 Lift pipe 12 Air supply pipe 13 Transfer pipe 14 Circulation return pipe 15 Return pipe 16 water collecting pipe 17 water passage holes 18 fitting 19 inspection tube 20,20a plug S 1, S 2 smaller combined treatment septic tank A contaminant removal tank A 1 sedimentation separation tank B anaerobic filter bed chamber B 1 anaerobic filter bed chamber first chamber B 2 Anaerobic filter bed second chamber C Contact aeration tank D Precipitation tank E Disinfection tank F Pump tank P Air lift pump device H High level water level L Low level water level line 21 Inlet pipe 22 Outlet pipe 23 Anaerobic filter bed 24 Aerobic Filter bed 25 Inlet guide 26 Downflow passage 27 Front partition wall 28 Advection port 29 Advection guide 30 Advection passage 31 Intermediate partition wall 32 Advection port 33 Advection guide 34 Advection passage 35 Air diffuser 36 Upflow passage 37 Air supply air pipe 38 Back partition 39 Submerged flow Mouth 40 Baffle plate 41 Convergence opening 42 Receiving gutter 43 Disinfection cylinder 44 Disinfection partition 45 Submerged opening 46 Backwashing device 47 Extraction tube 48,51 Air supply tube 49 Transfer tube 50,52 Air supply main line
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平2−222780(JP,A) 実開 昭53−56112(JP,U) 実開 昭63−32699(JP,U) 実願 平1−4325号(実開 平2− 95597号)の願書に添付した明細書及び 図面の内容を撮影したマイクロフィルム (JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 3/00 F16L 41/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-2-222780 (JP, A) JP-A-53-56112 (JP, U) JP-A-63-32699 (JP, U) JP-A-1- Microfilm (JP, U) photographing the contents of the specification and drawings attached to the application form No. 4325 (Japanese Utility Model Application No. 2-95597) (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3 / 00 F16L 41/00
Claims (3)
側と分配室Z側に間仕切り形成し、 当該溢流平堰板8の溢流幅の割合を、分配室Zを区画す
る平堰区分板9a,9bにより可変調節してなる処理水
の分配計量装置において、 前記流入室Xと分配室Zとの間に中間室Yに区画し、 当該中間室Yと前記流入室Xとを潜流堰板7で間仕切り
形成し、 中間室Yと分配室Zとを溢流平堰板8で間仕切り形成
し、 前記分配室Zを構成する溢流平堰板8の背面内壁面と、
計量箱の背面板部2の内壁面に係 合溝8a,2aを等間
隔に凹凸形成すると共に、前記分配室Zの底板部5にも前記係合溝8a,2aを結
ぶ係合溝5aを凹凸形成し、 前記分配室Zの適宜位置の係合溝8a,2a,5aに平
堰区分板9a,9bを差し込む ように構成したことを特
徴とする処理水の分配計量装置。The inside of a measuring box is filled with an inflow chamber X by an overflow flat weir plate 8.
And partition formed with side distribution chamber Z side, the percentage of overflow width of the overflow flat sheathing board 8, flat dam segment plate 9a defining the distribution chamber Z, 9b variable adjusting comprising treated water distribution metering by In the apparatus , an intermediate chamber Y is defined between the inflow chamber X and the distribution chamber Z, and the intermediate chamber Y and the inflow chamber X are partitioned by the submerged weir plate 7.
And the intermediate chamber Y and the distribution chamber Z are partitioned by the overflow flat weir plate 8.
And a rear inner wall surface of the overflow flat sheathing board 8 constituting the distribution chamber Z,
Forming an inner wall surface engaging groove 8a of the back plate portion 2 of the weighing boxes, as well as irregularities formed 2a a at regular intervals, the even bottom plate 5 of the distributor chamber Z engagement groove 8a, the 2a
The engaging groove 5a is formed in a concave and convex manner, and the engaging groove 8a, 2a, 5a at an appropriate position in the distribution chamber Z is flattened.
A dispensing and measuring device for treated water, wherein the partition plates 9a and 9b are inserted .
上げるリフト管11を、分割室Z1〜Z3にはポンプ槽F
への返送管15と、消毒槽Eへの移流管13と、夾雑物
除去槽A又は嫌気濾床槽Bの最先部或は嫌気濾床槽の第
1室B1への循環返送管14を配管してなる請求項1に
記載の処理水の分配計量装置。2. An inflow chamber X is provided with a lift pipe 11 for pumping treated water from a pump tank F, and divided chambers Z 1 to Z 3 are provided with a pump tank F.
Pipe 15 to the disinfection tank E, and the circulation return pipe 14 to the forefront of the impurity removal tank A or the anaerobic filter bed tank B or to the first chamber B1 of the anaerobic filter bed tank. 2. The apparatus for distributing and measuring treated water according to claim 1, wherein the apparatus is piped.
該集水管16とポンプ槽Fとを連通自在に連結し、当該
ポンプ槽Fに処理水のリフト管11とエアリフト用給気
管12を配管し、その内、リフト管11の上部を計量箱
の流入室Xに連結してなる請求項1又は請求項2に記載
の処理水の分配計量装置。3. A water collecting pipe 16 is submerged and supported in the settling tank D, and the water collecting pipe 16 and the pump tank F are communicably connected to each other. The treated water lift pipe 11 and the air lift air supply pipe 12 are connected to the pump tank F. 3. The apparatus for distributing and measuring treated water according to claim 1, wherein an upper portion of the lift pipe 11 is connected to the inflow chamber X of the measuring box.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33117891A JP3183546B2 (en) | 1991-11-19 | 1991-11-19 | Dispensing and measuring device for treated water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33117891A JP3183546B2 (en) | 1991-11-19 | 1991-11-19 | Dispensing and measuring device for treated water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05138184A JPH05138184A (en) | 1993-06-01 |
JP3183546B2 true JP3183546B2 (en) | 2001-07-09 |
Family
ID=18240763
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33117891A Expired - Fee Related JP3183546B2 (en) | 1991-11-19 | 1991-11-19 | Dispensing and measuring device for treated water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3183546B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001241096A (en) * | 2000-02-29 | 2001-09-04 | Hitachi Chem Co Ltd | Septic tank |
CN105585193B (en) * | 2015-12-30 | 2018-09-25 | 阮卜琴 | A kind of water intake mechanism of sewage treatment equipment |
-
1991
- 1991-11-19 JP JP33117891A patent/JP3183546B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05138184A (en) | 1993-06-01 |
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