JP2002177977A - Fluid transfer equipment and swage septic tank - Google Patents

Fluid transfer equipment and swage septic tank

Info

Publication number
JP2002177977A
JP2002177977A JP2000373700A JP2000373700A JP2002177977A JP 2002177977 A JP2002177977 A JP 2002177977A JP 2000373700 A JP2000373700 A JP 2000373700A JP 2000373700 A JP2000373700 A JP 2000373700A JP 2002177977 A JP2002177977 A JP 2002177977A
Authority
JP
Japan
Prior art keywords
fluid
pipe
air
tank
fluid transfer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2000373700A
Other languages
Japanese (ja)
Inventor
Koji Tsukamoto
幸二 塚本
Koji Komata
康二 小俣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP2000373700A priority Critical patent/JP2002177977A/en
Publication of JP2002177977A publication Critical patent/JP2002177977A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To cost effectively provide fluid transfer equipment and septic tank which are simple in structure, are less restricted on the places of installation, make simplification possible and have a constant flow rate characteristic. SOLUTION: The fluid transfer equipment which is installed with an air pipe opened into a fluid storage tank and capable of discharging air into a lifting pipe and ladles up the fluid by discharging the air into the lifting pipe to lower the apparent specific gravity of the fluid in the lifting pipe is provided with a return/advection pipe 20 which changes the flow of fluid from the ascending flow in the lifting pipe to an approximately horizontal flow at a point for advecting the fluid in the upper part of the lifting pipe 200B and further changes the flow to a perpendicular direction on a horizontal plane. The return/ advection pipe 20 is provided with a weir 2 for liquid return formed by partly notching the pipe and is further provided with a submerged weir (a second fluid transfer rate regulating means) 22 capable of changing the opening area at the port of the liquid advection pipe.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、定量の流体を移送
する移送装置、及び流体移送装置を設けた汚水浄化槽に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a transfer device for transferring a fixed amount of fluid, and a sewage purification tank provided with the fluid transfer device.

【0002】[0002]

【従来の技術】従来より、流体の移送手段として、揚水
管内へ空気を吐出させることにより配管内見かけ比重を
低下させることで流体移送を行う装置、例えばエアリフ
トポンプが知られており、この装置は流体汲み上げ高さ
の影響を受けにくく定量流体移送を達成することができ
る。ここで、定量流体移送装置、および装置を配設した
浄化槽を図面を参照して説明する。図6は、従来例の汚
水浄化槽の断面説明図、図7は槽内に配設されている流
体移送手段としてのエアリフトポンプの要部の斜視図で
ある。汚水浄化槽1は、間仕切2によって複数の処理槽
に区画され、汚水はこの複数の処理槽を順次通過して浄
化される。汚水は流入口3から流出口4へ至るまでに、
上流側から順次、第1嫌気濾床槽5(流入負荷調整槽と
しても機能する槽)、第2嫌気濾床槽6、好気濾床槽
7、処理水槽8及び消毒槽9を通過途上浄化され消毒さ
れて排出される。第1嫌気濾床槽5はその水位を最低水
位(L.W.L)から最高水位(H.W.L)まで変動
可能に構成されており、流入水の変動は、第1嫌気濾床
槽5水位の変動により吸収され、流入水の変動が第2嫌
気濾床槽6以降の槽へ直接に影響することはない。この
ように第1嫌気濾床槽5は、流入負荷調整機能を果たし
ている。第1嫌気濾床槽5と第2嫌気濾床槽6の境界部
にはエアリフトポンプ10が配されており、その揚水管
の開口部12(L.W.Lと同水準に位置する)から汚
水を吸い込み、第2嫌気濾床槽6へ汚水を移送してい
る。なお、エアリフトポンプ10は、可動部分が少ない
・故障が少ない・空気量の調整により自由に液移送速度
が変えられる、等の利点から家庭用の汚水浄化槽によく
用いられている。
2. Description of the Related Art Conventionally, a device for transferring a fluid by discharging air into a pumping pipe to reduce the apparent specific gravity in the pipe, for example, an air lift pump has been known as a means for transferring the fluid. It is hardly affected by the fluid pumping height and can achieve a constant fluid transfer. Here, the quantitative fluid transfer device and the septic tank provided with the device will be described with reference to the drawings. FIG. 6 is an explanatory sectional view of a conventional sewage purification tank, and FIG. 7 is a perspective view of a main part of an air lift pump as a fluid transfer means provided in the tank. The sewage purification tank 1 is divided into a plurality of treatment tanks by a partition 2, and sewage is sequentially purified through the plurality of treatment tanks. Sewage flows from the inlet 3 to the outlet 4
From the upstream side, the first anaerobic filter bed tank 5 (a tank also functioning as an inflow load adjusting tank), the second anaerobic filter bed tank 6, the aerobic filter bed tank 7, the treatment water tank 8, and the disinfecting tank 9 are sequentially purified on the way. Is disinfected and discharged. The first anaerobic filter bed tank 5 is configured so that its water level can be varied from a minimum water level (LWL) to a maximum water level (HWL). The change in the water level in the tank 5 is absorbed, and the change in the inflow water does not directly affect the tanks after the second anaerobic filter bed tank 6. Thus, the first anaerobic filter bed tank 5 has an inflow load adjusting function. An air lift pump 10 is disposed at the boundary between the first anaerobic filter bed tank 5 and the second anaerobic filter bed tank 6, and is opened from the opening 12 of the pumping pipe (located at the same level as LWL). Sewage is sucked and transferred to the second anaerobic filter bed tank 6. In addition, the air lift pump 10 is often used for domestic sewage purification tanks because it has few moving parts, few failures, and the liquid transfer speed can be freely changed by adjusting the amount of air.

【0003】エアリフトポンプ10の部分斜視図を図7
に示す。エアリフトポンプ10は揚水管11に空気管1
3から空気を吐出させ、揚水管11内の見かけ比重を低
下させることによりエアリフトチーズ16から第2嫌気
濾床槽6に第1嫌気濾床槽5の水を移送している。この
構成のエアリフトポンプ10は構造が比較的簡単である
が、液移送速度(定量性)が第1嫌気濾床槽5内の液水
位に影響を受けやすい難点がある。
FIG. 7 is a partial perspective view of the air lift pump 10.
Shown in The air lift pump 10 has an air pipe 1
3, the water in the first anaerobic filter bed tank 5 is transferred from the airlift cheese 16 to the second anaerobic filter bed tank 6 by lowering the apparent specific gravity in the pumping pipe 11. The air lift pump 10 having this configuration has a relatively simple structure, but has a drawback that the liquid transfer speed (quantitative property) is easily affected by the liquid level in the first anaerobic filter tank 5.

【0004】そこで、上記難点を克服するために、流量
調整枡をもつエアリフトポンプや2段階に液を汲み上げ
る2段式エアリフトポンプ(特開平6−285484号
公報)も提案されている。
In order to overcome the above-mentioned difficulties, there have been proposed an air lift pump having a flow rate adjusting chamber and a two-stage air lift pump for pumping a liquid in two stages (Japanese Patent Laid-Open No. 6-285484).

【0005】[0005]

【発明が解決しようとする課題】しかしながら、2段式
のエアリフトポンプや流量調整枡によって移送水量の安
定化を図ることにより定量性は得られるものの、大型化
すると共にその機構が複雑化するため管理方法も複雑化
することはいうまでもない。また、部品点数が増加する
ため組立工数増及びコスト増に関する課題もあった。更
に、小スペース化が求められている汚水浄化槽において
は、ポンプ(流体移送装置)の構造が大型化してしまう
ため、装置の配置や配管取り回し等への課題もあった。
However, although stabilization of the amount of water to be transferred can be achieved by using a two-stage air lift pump or a flow rate adjusting basin, quantitative performance can be obtained. Needless to say, the method becomes complicated. In addition, since the number of parts increases, there are also problems related to an increase in the number of assembling steps and an increase in cost. Furthermore, in a sewage purifying tank that requires a small space, the structure of a pump (fluid transfer device) becomes large, and thus there are also problems with the arrangement of the device and piping management.

【0006】そこで、本発明の目的は、構造が簡単で設
置場所への制約が少なく、且つ簡便化が可能な定流量性
のある流体移送装置および浄化槽を経済的に提供するこ
とにある。
SUMMARY OF THE INVENTION An object of the present invention is to economically provide a fluid transfer device having a constant flow rate and a septic tank which has a simple structure, has less restrictions on an installation place, and can be simplified.

【0007】さらに、本発明の目的は、移送量の調整が
容易な流体移送装置および浄化槽を提供することにあ
る。
Another object of the present invention is to provide a fluid transfer device and a septic tank in which the transfer amount can be easily adjusted.

【0008】[0008]

【課題を解決するための手段】本発明は、流体貯留槽内
に開口し揚水管内部に空気を吐出可能な空気管を設置し
て該揚水管内に空気を吐出させることにより該揚水管内
の流体の見かけ比重を低下させて該流体の汲み上げを行
う流体移送装置において、揚水管上部の流体を移流させ
る個所に流体の流れを揚水管内の上昇流から略水平方向
への流れに変更し、さらに水平面上直角方向とする返送
兼移流管を設け、返送兼移流管には管の一部を切欠した
液返送用堰、さらに、液移流管口に開口面積を変更可能
な潜り堰(第2の流体移送量調整手段)を設けたことを
特徴とする。
SUMMARY OF THE INVENTION According to the present invention, there is provided an air pipe which is opened in a fluid storage tank and is capable of discharging air inside a pumping pipe, and discharges air into the pumping pipe to discharge the fluid in the pumping pipe. In the fluid transfer device for pumping the fluid by reducing the apparent specific gravity of the fluid, the fluid flow is changed from a rising flow in the water pumping pipe to a flow in a substantially horizontal direction at a location where the fluid is transferred to the upper part of the water pumping pipe. A return and advection pipe having a direction perpendicular to the upper direction is provided. The return and advection pipe has a liquid return weir in which a part of the pipe is cut off. Transfer amount adjusting means).

【0009】そして、前記空気管から揚水管内に供給す
る空気量を第1の流体移送調整手段により調整すること
により、流体移送量を変更可能にしたことを特徴とす
る。
The amount of air to be supplied can be changed by adjusting the amount of air supplied from the air pipe into the pumping pipe by the first fluid transfer adjusting means.

【0010】また、汚水浄化槽は、空気管から揚水管内
に供給する空気量を調整することにより、流体移送量を
変更可能にした第1の流体移送量調整手段と、液移流管
に堰高さを変更して流体移送量の調整を可能にした第2
の流体移送量調整手段を設けた流体移送装置を配設した
ことを特徴とする。
Further, the sewage purification tank has a first fluid transfer amount adjusting means capable of changing a fluid transfer amount by adjusting an amount of air supplied from an air pipe into the pumping pipe, and a weir height in the liquid transfer pipe. To enable adjustment of the fluid transfer volume by changing
Wherein a fluid transfer device provided with the fluid transfer amount adjusting means is provided.

【0011】(作用)本発明によれば、第1の移送量調
整手段により空気管から揚水管内へ供給する空気量を調
整して、液の移送速度と移送量を変更可能とし、さら
に、第2の移送量調整手段により移流管の開口面積を変
更させ流体移送量の調整を可能にすると共に、余剰の汚
水は返送するため、流体汲み上げ高さの影響を受けにく
く、かつ、定量移送を可能とする。
(Operation) According to the present invention, the amount of air supplied from the air pipe to the pumping pipe is adjusted by the first transfer amount adjusting means, so that the liquid transfer speed and the transfer amount can be changed. By changing the opening area of the advection tube by means of the transfer amount adjusting means (2), it is possible to adjust the amount of fluid transfer, and because excess wastewater is returned, it is hardly affected by the height of pumping up the fluid, and it is possible to transfer quantitatively And

【0012】[0012]

【発明の実施の形態】図1は本発明の流体移送装置を設
置した汚水浄化槽の縦断面図である。なお、従来例で示
した汚水浄化槽と同様な構成部分には同一符号を付して
その説明を省略している。
FIG. 1 is a longitudinal sectional view of a sewage purification tank provided with a fluid transfer device according to the present invention. Note that the same components as those of the sewage purification tank shown in the conventional example are denoted by the same reference numerals, and description thereof is omitted.

【0013】この汚水浄化槽100は、浄化槽内を間仕
切2で仕切って複数の処理槽を形成している。
In the sewage purification tank 100, a plurality of treatment tanks are formed by partitioning the inside of the purification tank with a partition 2.

【0014】第1嫌気濾床槽5は、流入口3から流入し
た汚水を貯留して嫌気処理するとともに、流入水の水位
を高水位(H.W.L.)と低水位(L.W.L.)の
間で変動させることにより下流側の処理槽へ移流する汚
水の量を安定化するバッファタンク(流入負荷調整槽)
の機能を持たせている。そして、この第1嫌気濾床槽5
に貯留する汚水は、流体移送装置200によって汲み上
げて第2嫌気濾床槽6に移送する。この実施の形態にお
いて、流体移送装置200は、第1嫌気濾床槽5から第
2嫌気濾床槽6への汚水移流に使用しているが、流量調
整容量や配管を考慮して、第2嫌気濾床槽6、好気濾床
槽7、処理水槽8における各々の移流部の何れか、若し
くは複数箇所に設置可能である。
The first anaerobic filter bed tank 5 stores sewage flowing from the inflow port 3 and performs anaerobic treatment, and adjusts the water level of the inflow water to a high water level (HWL) and a low water level (LW). .L.) To stabilize the amount of sewage transferred to the downstream treatment tank (inflow load adjustment tank).
Function. And this 1st anaerobic filter bed tank 5
The sewage stored in the tank is pumped up by the fluid transfer device 200 and transferred to the second anaerobic filter bed tank 6. In this embodiment, the fluid transfer device 200 is used for the transfer of sewage from the first anaerobic filter bed tank 5 to the second anaerobic filter bed tank 6. It can be installed at any of the advection sections in the anaerobic filter bed tank 6, the aerobic filter bed tank 7, and the treated water tank 8, or at a plurality of locations.

【0015】流体移送装置200は、下部をU字形状管
に連結し揚水管の開口部211を低水位L.W.L以下
のレベルに位置させて開口させた第1の揚水管200A
と、空気供給機構に連結される空気管を内装する第2の
揚水管200Bと、第1の揚水管200Aと第2の揚水
管200Bとを連結するU字状管200Cとを備えてい
る。そして、第2の揚水管200B内に空気を吐出させ
ることにより第2の揚水管200A内の汚水(流体)の
見かけ比重を低下させて第1の揚水管200Aから汚水
を汲み上げる構成である。
The fluid transfer device 200 has a lower portion connected to a U-shaped tube, and an opening 211 of the water pumping tube having a low water level L.L. W. First pumping pipe 200A which is opened at a level lower than L
, A second pumping pipe 200B having an air pipe connected to the air supply mechanism therein, and a U-shaped pipe 200C connecting the first pumping pipe 200A and the second pumping pipe 200B. Then, by discharging air into the second pumping pipe 200B, the apparent specific gravity of the sewage (fluid) in the second pumping pipe 200A is reduced, and the sewage is pumped up from the first pumping pipe 200A.

【0016】このようにして流体移送装置200で汲み
上げられて第2嫌気濾床槽6に移送された汚水は、この
第2嫌気濾床槽6内で嫌気処理された後に好気濾床槽7
に移流して好気処理され、更に処理水槽8、消毒槽9を
経由して流出口4から放流される。
The sewage thus pumped up by the fluid transfer device 200 and transferred to the second anaerobic filter tank 6 is subjected to anaerobic treatment in the second anaerobic filter tank 6 and then to the aerobic filter tank 7.
The water is then aerobic-treated and further discharged from the outlet 4 via the treatment water tank 8 and the disinfection tank 9.

【0017】流体移送装置200は、使用する環境に対
して耐久性が要求される。従って、使用する環境にもよ
るが、構成部品(槽壁、仕切板など)の材質は、金属、
具体的にはステンレス、アルミ、アルミ合金、鋼材等の
使用が好適である。また、プラスチック、具体的にはポ
リエチレン、ポリプロピレン、ポリブデン、塩化ビニル
等が配管(たとえば第1・第2の揚水管、U字状管な
ど)として使用するのが好適である。各々の部品の接合
は、ねじ込み式、溶接(溶着)、接着等が可能である。
The fluid transfer device 200 is required to have durability against the environment in which it is used. Therefore, depending on the environment in which it is used, the material of the component parts (tank wall, partition plate, etc.) is
Specifically, it is preferable to use stainless steel, aluminum, aluminum alloy, steel material or the like. Further, it is preferable to use plastics, specifically, polyethylene, polypropylene, polybutene, vinyl chloride, and the like as pipes (for example, first and second pumping pipes, U-shaped pipes, and the like). Each component can be joined by screwing, welding (welding), bonding, or the like.

【0018】次に、流体移送装置200を説明する。図
2は流体移送装置における流体移送口部の縦断側面図、
図3は斜視図、図4は返送兼移流管の作用説明図であ
る。
Next, the fluid transfer device 200 will be described. FIG. 2 is a longitudinal side view of a fluid transfer port in the fluid transfer device,
FIG. 3 is a perspective view, and FIG. 4 is an operation explanatory view of the return and advection pipe.

【0019】図1に示すように一端を吸込みの開口部2
11とした第1の揚水管200AにU字状管200Cを
介して連結した第2の揚水管200Bは、その上部にエ
アリフトチーズ25を接続する。第2の揚水管200B
内に空気を吐出させる空気管27は、エアリフトチーズ
25を貫通して第2の揚水管200B内に同心円状に挿
入されて設置されている。空気管27は、給気配管29
から調整バルブ28を介して、点線矢印で示すように第
2の揚水管200B内に空気を供給する。空気管27の
先端の噴気口270は、汲み上げ高さにもよるが、低水
位(L.W.L)から下方への距離L1(図1参照)を
250mm以上とし、この位置に開口させ空気を吐出す
るようにすることが望ましい。また、U字状管200C
の上部開口は、第1の揚水管200Aの吸込み口211
からの距離L2(図1参照)を270mm以上とするこ
とが望ましい。
As shown in FIG. 1, one end of the opening 2 has a suction.
An air lift cheese 25 is connected to the upper part of the second pumping pipe 200B which is connected to the first pumping pipe 200A set to 11 via a U-shaped pipe 200C. Second pumping pipe 200B
An air pipe 27 for discharging air into the second pumping pipe 200B is inserted through the air lift cheese 25 and installed concentrically in the second water pumping pipe 200B. The air pipe 27 is provided with an air supply pipe 29.
Then, air is supplied into the second pumping pipe 200B through the adjustment valve 28 as shown by a dotted arrow. The air outlet 270 at the tip of the air pipe 27 has a distance L1 (see FIG. 1) downward from the low water level (LWL) of 250 mm or more, depending on the pumping height, and is opened at this position to open the air. Is desirably discharged. Also, U-shaped tube 200C
The upper opening of the suction port 211 of the first pumping pipe 200A
It is desirable that the distance L2 from the distance (see FIG. 1) be 270 mm or more.

【0020】第2の揚水管200Bとエアリフトチーズ
25の内周面と空気管27の外周面との間には、吐出し
た空気と汚水を上昇させて汲み上げるための隙間Uを確
保している。なお、空気管27は、第2の揚水管200
B及びエアリフトチーズ25の外側に配管し、第2の揚
水管200Bの下部の側面から挿入するように変形する
ことも可能である。この場合の空気管挿入位置は吸込み
の開口部211から約270mm以上とすることが望ま
しい。
A gap U is provided between the second pumping pipe 200B, the inner peripheral surface of the air lift cheese 25, and the outer peripheral surface of the air pipe 27 for raising the discharged air and sewage and pumping it up. The air pipe 27 is connected to the second pumping pipe 200.
B and the outside of the air lift cheese 25 may be deformed so as to be inserted from the lower side surface of the second pumping pipe 200B. In this case, it is desirable that the air tube insertion position be approximately 270 mm or more from the suction opening 211.

【0021】エアリフトチーズ25には、第2の揚水管
200Bの汲み上げ方向に垂直に延設する返送兼移流管
20を設けている。返送兼移流管20は同一水平面でL
字形状に曲折する返送堰部21を連接している。返送堰
部21は上部を切欠して開放したほぼ断面半円形状の樋
状となっている。返送堰部21は移流管23に連結して
いる。移流管23は次室である第2の嫌気濾床槽6内に
汚水を移送するように開口している。返送堰部21と移
流管23との境界部分であって移流管の移流口230に
は潜り堰22を設けている。
The air lift cheese 25 is provided with a return and advection pipe 20 which extends perpendicularly to the pumping direction of the second pumping pipe 200B. Return and advection pipe 20 is L
A return weir 21 that bends into a letter shape is connected. The return weir 21 has a trough-like shape with a semicircular cross section that is opened by cutting out the upper part. The return weir 21 is connected to the advection tube 23. The advection pipe 23 is opened to transfer the sewage into the second anaerobic filter bed tank 6 which is the next chamber. A submerged weir 22 is provided at a boundary between the return weir 21 and the advection pipe 23 at the advection port 230 of the advection pipe.

【0022】潜り堰22は上下方向、矢印y方向に移動
可能であって、移流管23の移流口230の開口面積を
調節する。例えば、潜り堰22を上部に移動させること
により移流口230の開口は大きくなり、潜り堰22を
下部に移動させることにより移流口230の開口は小さ
くなる。返送兼移流管20はエアリフトチーズ25に一
体成型によって設ける、または別部品として接続するこ
とによって配設される。
The descent weir 22 is movable in the vertical direction and the direction of the arrow y, and adjusts the opening area of the advection port 230 of the advection tube 23. For example, by moving the submersible weir 22 to the upper part, the opening of the advection port 230 becomes larger, and by moving the submersible weir 22 to the lower part, the opening of the advection port 230 becomes smaller. The return and advection pipe 20 is provided by being integrally formed with the air lift cheese 25 or by being connected as a separate part.

【0023】このように構成される流体移送装置200
の水の流れを図1乃至図4を用いて説明する。まず、第
1の揚水管200Aの揚水管の開口部211から流入し
た汚水はU字管200Cを通って第2の揚水管200B
に流入する。そして、吐出する空気により見かけ比重が
低下した汚水は第2の揚水管200Bの空気管27との
間隙Uを上昇する。そして、返送兼移流管20に流入す
る。このとき返送兼移流管20に流入する汚水の量、お
よび汚水の上昇速度は、空気管27からの空気の吐出量
により調節される。空気の吐出量は調整バルブ28によ
り調整される。このように、空気の吐出量による汚水の
移送量、および速度の調整を行う手段を第1の移送量調
整手段という。
The fluid transfer device 200 thus configured
The flow of water will be described with reference to FIGS. First, the sewage flowing from the opening 211 of the pumping pipe of the first pumping pipe 200A passes through the U-shaped pipe 200C and the second pumping pipe 200B.
Flows into. Then, the sewage whose apparent specific gravity has decreased due to the discharged air rises in the gap U between the second pumping pipe 200B and the air pipe 27. Then, it flows into the return and advection pipe 20. At this time, the amount of sewage flowing into the return and advection pipe 20 and the rising speed of the sewage are adjusted by the amount of air discharged from the air pipe 27. The discharge amount of the air is adjusted by the adjustment valve 28. The means for adjusting the transfer amount and speed of the wastewater based on the air discharge amount in this way is referred to as first transfer amount adjusting means.

【0024】すなわち、この段階で空気は上昇し、汚水
は矢印wで示すように、上昇流から略水平方向への流れ
に変更され、気液分離される。そして、汚水は返送堰部
21から移流管23に流入して矢印w2で示すように第
2の嫌気濾床槽6に移送される。ここで、潜り堰22を
上部に移動して移流口230の面積を大きくすることに
より、第2の嫌気濾床槽6への汚水の移送量は多くな
る。また、潜り堰22を下方に移動して移流口230の
面積を小さくすることにより、第2の嫌気濾床槽6への
汚水の移送量は少なくなる。そして、移流口230の面
積より多量の汚水が汲み上げられたときは、余剰の汚水
は樋形状の返送堰部21の堰を乗り越えて矢印w1で示
すように、第1の嫌気濾床槽5に返送される。このよう
に潜り堰22による移送量の調整、および返送堰部21
による余剰汚水の返送調整を第2の移送量調整機構とい
う。このように、第2の移送量調整機構を備えた返送兼
移流管20は、第1の揚水管200Aおよび第2の揚水
管200Bにより、第1嫌気濾床槽5から汲み上げた汚
水を所定の流量で次段の第2嫌気濾床槽6に移送しつつ
余剰の汚水を第1嫌気濾床槽5に返送するものである。
That is, at this stage, the air rises, and the sewage is changed from a rising flow to a flow in a substantially horizontal direction as indicated by an arrow w, and gas-liquid separation is performed. Then, the sewage flows from the return dam 21 into the advection pipe 23 and is transferred to the second anaerobic filter bed tank 6 as indicated by an arrow w2. Here, by moving the dive weir 22 to the upper part to increase the area of the advection port 230, the transfer amount of the sewage to the second anaerobic filter bed tank 6 is increased. In addition, by moving the descent weir 22 downward to reduce the area of the advection port 230, the transfer amount of the sewage to the second anaerobic filter bed tank 6 is reduced. When a large amount of sewage is pumped up from the area of the advection port 230, the excess sewage passes over the weir of the gutter-shaped return weir 21 and enters the first anaerobic filter tank 5 as shown by an arrow w1. Will be returned. In this way, the adjustment of the transfer amount by the descent weir 22 and the return weir 21
The return adjustment of the excess wastewater is referred to as a second transfer amount adjustment mechanism. As described above, the return and advection pipe 20 provided with the second transfer amount adjusting mechanism is configured so that the sewage pumped from the first anaerobic filter bed tank 5 by the first pumping pipe 200A and the second pumping pipe 200B is provided in a predetermined manner. The excess sewage is returned to the first anaerobic filter bed tank 5 while being transferred to the second anaerobic filter bed tank 6 in the next stage at a flow rate.

【0025】この構成よりなる流体移送装置200は、
移流口230の潜り堰22を上下動させることにより堰
高さを変更することで移流口230の開口面積を調整
し、移送水量を調整可能にしている。また、手動で潜り
堰22の操作が可能なように潜り堰22には上部に取っ
手または引っ掛り220を設けている。さらに、潜り堰
22の側面等適所に、目盛り225を刻むことにより、
計量せずとも移送量の設定が可能となる。
The fluid transfer device 200 having this configuration is
By moving the descent weir 22 of the advection port 230 up and down to change the weir height, the opening area of the advection port 230 is adjusted, and the amount of transferred water is adjustable. Further, a handle or catch 220 is provided on the upper part of the dive weir 22 so that the dive weir 22 can be manually operated. Furthermore, by engraving a scale 225 at an appropriate place such as the side of the dive weir 22,
The transfer amount can be set without measuring.

【0026】このように汚水浄化槽100において、流
入口3から第1嫌気濾床槽5に流入した汚水は高水位
(HWL)と低水位(LWL)の間で変動するように貯
留され、嫌気処理される。そして、流体移送装置200
において、給気配管29から調整バルブ28を介して空
気管27に給気された空気は、噴気口270から揚水管
200B内に空気を吐出することにより揚水管内の汚水
の見かけ比重を低下させて汚水を上昇させて汲み上げ
る。第1の流体移送量調整手段である調整バルブ28に
より汚水の上昇速度、および汲み上げ量が調整されなが
ら汲み上げられた汚水は、エアリフトチーズ25内に達
すると気液分離されて水分は返送兼移流管20内に流れ
込む。そして、返送堰部21に案内されて移流口230
から潜り堰22をくぐって第2嫌気濾床槽6に流れ出
る。このとき、返送兼移流管20内の汚水は、第2の流
体移送量調整手段である汚水返送部に形成した返送堰部
21と移流口230に設けた潜り堰22とによりほぼ一
定に制御されるので、安定した移流量となる。
As described above, in the sewage purification tank 100, the sewage flowing into the first anaerobic filter bed tank 5 from the inlet 3 is stored so as to fluctuate between a high water level (HWL) and a low water level (LWL), and is subjected to anaerobic treatment. Is done. And the fluid transfer device 200
In the above, the air supplied from the air supply pipe 29 to the air pipe 27 through the adjustment valve 28 discharges air from the fuze port 270 into the water pumping pipe 200B to lower the apparent specific gravity of the sewage in the water pumping pipe. Raise and pump sewage. The sewage pumped up while the rising speed and the pumping amount of the sewage are adjusted by the adjusting valve 28, which is the first fluid transfer amount adjusting means, is separated into gas and liquid when reaching the inside of the air lift cheese 25, and the water is returned and transferred. It flows into 20. Then, it is guided to the return weir 21 and the advection port 230
And flows through the dive weir 22 into the second anaerobic filter bed tank 6. At this time, the sewage in the return and advection pipe 20 is controlled to be substantially constant by the return weir 21 formed in the sewage return unit serving as the second fluid transfer amount adjusting means and the descent weir 22 provided in the advection port 230. Therefore, the flow rate becomes stable.

【0027】すなわち、本発明に係る流体移送装置20
0における汚水汲み上げ流量は給気量を調整バルブ28
によって制御する第1の移送量調整機構と、潜り堰22
の高さを変えることによって第2嫌気濾床槽6への移送
量を調整する第2の移送量調整機構により実行される。
That is, the fluid transfer device 20 according to the present invention
The sewage pumping flow rate at zero adjusts the air supply amount.
The first transfer amount adjusting mechanism controlled by the
This is performed by a second transfer amount adjusting mechanism that adjusts the transfer amount to the second anaerobic filter bed tank 6 by changing the height of the filter bed.

【0028】第2嫌気濾床槽6に一定の流量で流れ込ん
だ汚水は、さらに嫌気処理した後に好気濾床槽7に移流
して好気処理され、さらに処理水槽8を経て消毒槽9で
消毒滅菌されて流出口4から放流される。
The sewage flowing into the second anaerobic filter bed tank 6 at a constant flow rate is further anaerobically treated, then transferred to the aerobic filter bed tank 7 for aerobic treatment, and further passed through the treated water tank 8 to the disinfection tank 9. It is sterilized and discharged from the outlet 4.

【0029】また、図5に示す流体移送装置はエアリフ
トチーズに連接する返送兼移流管20における返送堰部
210の配設長さを長い寸法に構成すると共に、返送堰
部210に連設する移流管23を返送堰部210と同一
平面であって返送兼移流管20に平行に設けている。こ
の構成により、多量の汚水が汲み上げられて返送兼移流
管20に流入した場合、長い返送堰部210を通過途
上、返送可能であると共に、また、装置の設置場所を特
定しない。
In the fluid transfer device shown in FIG. 5, the length of the return weir 210 in the return and advancing pipe 20 connected to the air lift cheese is set to be long, and the advection connected to the return weir 210 is increased. The pipe 23 is provided on the same plane as the return weir 210 and parallel to the return and advection pipe 20. With this configuration, when a large amount of sewage is pumped up and flows into the return and advection pipe 20, it can be returned while passing through the long return weir 210, and the installation location of the device is not specified.

【0030】以上説明したように、この流体移送装置、
および浄化槽は汚水移送量を揚水管への給気量によって
調節する第1の流体調整移送手段(機構)、または潜り
堰の移動によって調節する第2の流体移送手段(機構)
の一方または両方の組み合わせによって定量化すること
ができる。
As described above, this fluid transfer device
And a septic tank, a first fluid adjusting and transferring means (mechanism) for adjusting a transfer amount of sewage by an amount of air supplied to a pumping pipe, or a second fluid transferring means (mechanism) for adjusting by moving a dive weir
Can be quantified by one or a combination of both.

【0031】このような流体移送装置は、その大きさが
従来から用いられている流体移送装置と大差ないために
設置場所に格別の配慮は不要であり、また、必要な空気
量も従来の流量調整枡式のものに比べて少ないため、新
たな空気源を必要としない。従って、従来の汚水浄化槽
にそのまま取り付けることが可能であり、その取付位置
も第1嫌気濾床槽から第2嫌気濾床槽への移流部に限ら
ず、流量調整容量や配置等を考慮して他の移流部に設置
することも可能であり、更に、流量調整機能を持たない
汚水浄化槽に後付けで設置することが可能である。
Such a fluid transfer device does not need to be specially considered at an installation place because its size is not much different from a conventionally used fluid transfer device. There is no need for a new air source because it is smaller than that of the adjusting basin type. Therefore, it is possible to directly attach to the conventional sewage purification tank, and the attachment position is not limited to the advection part from the first anaerobic filter bed tank to the second anaerobic filter bed tank, but also takes into account the flow control capacity and arrangement. It can be installed in another advection section, and can be installed later in a sewage purification tank without a flow rate adjusting function.

【0032】[0032]

【発明の効果】本発明によれば、液移送速度(定量性)
が安定しており、構造が簡単で部品点数やその組立工数
も多くなく経済的に提供できる。また、コンパクトなた
め設置場所への制約が少ない。さらに、本発明は、汚水
を効率よく、安定して処理できる。
According to the present invention, the liquid transfer speed (quantitative)
However, the structure is simple, the number of parts and the number of assembling steps are small, and it can be provided economically. In addition, since it is compact, there are few restrictions on the installation location. Further, the present invention can efficiently and stably treat sewage.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の汚水浄化槽の概略断面図。FIG. 1 is a schematic sectional view of a sewage purification tank of the present invention.

【図2】本発明の流体移送装置(エアリフトポンプ)の
概略断面図。
FIG. 2 is a schematic sectional view of a fluid transfer device (air lift pump) of the present invention.

【図3】本発明のエアリフトポンプの要部斜視図。FIG. 3 is a perspective view of a main part of the air lift pump of the present invention.

【図4】本発明の返送兼移流管の斜視説明図。FIG. 4 is an explanatory perspective view of a return and advection pipe of the present invention.

【図5】本発明の返送兼移流管の他の実施例を示す斜視
図。
FIG. 5 is a perspective view showing another embodiment of the return and advection pipe of the present invention.

【図6】従来の汚水浄化槽の概略断面図。FIG. 6 is a schematic sectional view of a conventional sewage purification tank.

【図7】従来のエアリフトポンプの概略断面図。FIG. 7 is a schematic sectional view of a conventional air lift pump.

【符号の説明】[Explanation of symbols]

1、100 汚水浄化槽 2 間仕切 3 流入口 4 流出口 5 第1嫌気濾床槽 6 第2嫌気濾床槽 7 好気濾床槽 8 処理水槽 9 消毒槽 10、200 流体移送装置(エアリフトポンプ) 11、200A,200B 揚水管 12、211 揚水管の開口部 16、25 エアリフトチーズ 13、27 空気管 18、28 調整バルブ 20 返送兼移流管 21、210 返送堰部 22 潜り堰 23 移流管 29 給気配管 200C U字管 220 引っ掛り 225 目盛り 230 移流口 270 噴気口 1, 100 sewage purification tank 2 partition 3 inflow port 4 outflow port 5 first anaerobic filter bed tank 6 second anaerobic filter bed tank 7 aerobic filter bed tank 8 treatment water tank 9 disinfection tank 10, 200 fluid transfer device (air lift pump) 11 , 200A, 200B Pumping pipe 12, 211 Opening of pumping pipe 16, 25 Air lift cheese 13, 27 Air pipe 18, 28 Adjusting valve 20 Return and advection pipe 21, 210 Return weir part 22 Submerged weir 23 Advection pipe 29 Supply air pipe 200C U-tube 220 Hook 225 Scale 230 Advection 270 Fume

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 移送元から流体を汲み上げる揚水管と、
揚水管の内部に空気を吐出可能に配設する空気管と、汲
み上げた流体を移送先に移送する揚水管に連設する移流
管とを備え、 前記揚水管の流体の汲み上げ量は第1の流体移送量調整
手段により揚水管内に供給する空気量を調整することに
より調整されると共に、移送先への流体の移送量は、第
2の流体移送量調整手段により移流管の開口面積を調整
することにより調整されるよう構成されてなる流体移送
装置。
1. A pumping pipe for pumping fluid from a transfer source,
An air pipe arranged to discharge air inside the pumping pipe; and an advection pipe connected to the pumping pipe for transferring the pumped fluid to the transfer destination, wherein the pumping amount of the fluid in the pumping pipe is first. The amount of air supplied to the pumping pipe is adjusted by the fluid transfer amount adjusting means, and the amount of fluid transferred to the transfer destination is adjusted by the second fluid transfer amount adjusting means. The fluid transfer device is configured to be adjusted by the following.
【請求項2】 前記第1の流体移送量調整手段は空気管
に配設される調整バルブである請求項1記載の流体移送
装置。
2. The fluid transfer device according to claim 1, wherein the first fluid transfer amount adjusting means is an adjustment valve disposed in an air pipe.
【請求項3】 前記第2の流体移送量調整手段は、移流
管の開口部に配設される堰高さを変更可能な潜り堰であ
る請求項1記載の流体移送装置。
3. The fluid transfer device according to claim 1, wherein the second fluid transfer amount adjusting means is a dive weir provided at an opening of the advection pipe and capable of changing a height of the weir.
【請求項4】 前記第2の流体移送量調整手段は、移流
管の一部を切欠いて形成する流体を移送元に返送する返
送堰である請求項1記載の流体移送装置。
4. The fluid transfer device according to claim 1, wherein the second fluid transfer amount adjusting means is a return weir that returns a fluid formed by cutting off a part of the advection pipe to a transfer source.
【請求項5】 槽内を複数の流体貯留槽に形成すると共
に、流体貯留槽内に開口した揚水管内部に空気を吐出可
能な空気管を設置して該揚水管内に空気を吐出させるこ
とにより該揚水管内の流体の見かけ比重を低下させて流
体の汲み上げを行う流体移送装置を配設し、移送元槽か
ら次槽へと流体を移送するよう構成される汚水浄化槽に
おいて、 前記流体移送装置は揚水管上部に汲み上げた流体を次槽
に移送する移流管を配設すると共に、揚水管の流体の汲
み上げ量は空気管からの空気の供給量を調整する第1の
流体移送量調整手段により調整され、次槽への流体の移
送量は移送管の開口面積を調整する第2の流体移送調整
手段により調整されるよう構成されてなる汚水浄化槽。
5. A method according to claim 1, wherein the inside of the tank is formed into a plurality of fluid storage tanks, and an air pipe capable of discharging air is installed in a pumping pipe opened in the fluid storage tank to discharge air into the pumping pipe. A sewage purifying tank configured to transfer a fluid from a transfer source tank to a next tank by disposing a fluid transfer device that lowers the apparent specific gravity of the fluid in the pumping pipe to pump up the fluid, An advection pipe for transferring the pumped fluid to the next tank is provided above the pumping pipe, and the pumping rate of the fluid in the pumping pipe is adjusted by first fluid transfer rate adjusting means for adjusting the supply rate of air from the air pipe. A sewage treatment tank configured to adjust the amount of fluid transferred to the next tank by a second fluid transfer adjusting means for adjusting the opening area of the transfer pipe.
【請求項6】 前記流体移送装置の揚水管は、流体貯留
槽の低水面と同一面、あるいは僅かに前記水面より低い
位置で開口するよう配設される請求項5記載の汚水浄化
槽。
6. The sewage treatment tank according to claim 5, wherein the pumping pipe of the fluid transfer device is disposed so as to open on the same plane as the low water surface of the fluid storage tank or at a position slightly lower than the water surface.
【請求項7】 前記揚水管の第1の流体移送量調整手段
は空気管に配設する空気調整バルブである請求項5記載
の浄化槽。
7. The septic tank according to claim 5, wherein the first fluid transfer amount adjusting means of the pumping pipe is an air adjusting valve provided in the air pipe.
【請求項8】 前記移送管の第2の流体移送量調整手段
は、移流管の開口部に配設される堰高さを変更可能な潜
り堰である請求項5記載の浄化槽。
8. The septic tank according to claim 5, wherein the second fluid transfer amount adjusting means of the transfer pipe is a dive weir provided at an opening of the advection pipe and capable of changing a height of the weir.
【請求項9】 前記第2の流体移送量調整手段は、移送
管の一部を切欠いて形成する流体を装置配設流体貯留槽
内に返送する返送堰である請求項5記載の浄化槽。
9. The septic tank according to claim 5, wherein the second fluid transfer amount adjusting means is a return weir that returns a fluid formed by cutting out a part of the transfer pipe into a fluid storage tank provided in the apparatus.
JP2000373700A 2000-12-08 2000-12-08 Fluid transfer equipment and swage septic tank Pending JP2002177977A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000373700A JP2002177977A (en) 2000-12-08 2000-12-08 Fluid transfer equipment and swage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000373700A JP2002177977A (en) 2000-12-08 2000-12-08 Fluid transfer equipment and swage septic tank

Publications (1)

Publication Number Publication Date
JP2002177977A true JP2002177977A (en) 2002-06-25

Family

ID=18843021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000373700A Pending JP2002177977A (en) 2000-12-08 2000-12-08 Fluid transfer equipment and swage septic tank

Country Status (1)

Country Link
JP (1) JP2002177977A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011190693A (en) * 2010-03-11 2011-09-29 Fuji Clean Co Ltd Water transfer pump and water treatment device
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011190693A (en) * 2010-03-11 2011-09-29 Fuji Clean Co Ltd Water transfer pump and water treatment device
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

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