JPH0957262A - Method for dissolving air in treated water in septic tank and septic tank - Google Patents
Method for dissolving air in treated water in septic tank and septic tankInfo
- Publication number
- JPH0957262A JPH0957262A JP21558295A JP21558295A JPH0957262A JP H0957262 A JPH0957262 A JP H0957262A JP 21558295 A JP21558295 A JP 21558295A JP 21558295 A JP21558295 A JP 21558295A JP H0957262 A JPH0957262 A JP H0957262A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- membrane separation
- water treatment
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
(57)【要約】
【課題】 簡単な構成によって、膜分離槽にエア溶解さ
せることのできる技術を提供すること。
【解決手段】 複数の水処理槽を備えてなり、前記水処
理槽の少なくとも1つを膜分離槽E2から構成してあ
り、前記膜分離槽E2とは異なる水処理槽に、被処理水
移送用の機械式ポンプP2を設けるとともに、被処理水
を前記膜分離槽E2とは異なる水処理槽から前記膜分離
槽E2に移送する移送管A2を前記機械式ポンプP2に
連設してある浄化槽における被処理水へのエア溶解方法
において、前記移送管A2に気泡を供給する。
(57) Abstract: To provide a technique capable of air-dissolving in a membrane separation tank with a simple configuration. SOLUTION: A plurality of water treatment tanks are provided, at least one of the water treatment tanks is composed of a membrane separation tank E2, and the treated water is transferred to a water treatment tank different from the membrane separation tank E2. And a mechanical pump P2 for water, and a septic tank in which a transfer pipe A2 for transferring water to be treated from a water treatment tank different from the membrane separation tank E2 to the membrane separation tank E2 is connected to the mechanical pump P2. In the method for dissolving air in the water to be treated, the bubbles are supplied to the transfer pipe A2.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、複数の水処理槽を
備えてなり、前記水処理槽の少なくとも1つを膜分離槽
から構成してある浄化槽に関し、特に、その浄化槽の膜
分離槽にエア溶解させる浄化槽、もしくは、浄化槽にお
ける被処理水へのエア溶解方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank comprising a plurality of water treatment tanks, at least one of which is a membrane separation tank. The present invention relates to a septic tank in which air is dissolved, or a method for dissolving air in water to be treated in the septic tank.
【0002】[0002]
【従来の技術】従来、この種の浄化槽は、単に、前記膜
分離槽とは異なる水処理槽に、被処理水移送用の機械式
ポンプを設けるとともに、被処理水を前記膜分離槽とは
異なる水処理槽から前記膜分離槽に移送する移送管を前
記機械式ポンプ、もしくはエアリフトポンプに連設して
あるものが知られており、通常膜分離槽では活性汚泥に
よる高度処理が行われ、大量の溶存酸素(以下DOと略
称する)が必要になるものの、このような浄化槽の被処
理水へのDO供給は、前記膜分離槽に被処理水循環用の
散気管を設けておき、その散気管からの気泡によるエア
溶解によって行われていた。2. Description of the Related Art Conventionally, in this type of septic tank, a mechanical pump for transferring treated water is simply provided in a water treatment tank different from the membrane separation tank, and the treated water is separated from the membrane separation tank. It is known that the transfer pipes that transfer from different water treatment tanks to the membrane separation tank are connected to the mechanical pump or the air lift pump, and in the normal membrane separation tank, advanced treatment with activated sludge is performed, Although a large amount of dissolved oxygen (hereinafter abbreviated as DO) is required, such a DO supply to the water to be treated in the septic tank is provided with an air diffuser pipe for circulating the water to be treated in the membrane separation tank. It was done by air dissolution by air bubbles from the trachea.
【0003】[0003]
【発明が解決しようとする課題】ところが、上述の浄化
槽によれば、散気管からの絵供給に基づくエア溶解量
は、浄化槽の高さ(正確には前記散気管の水深)が高く
すれば増加させられるものの、浄化槽は、通常、地下に
埋設されるため、浄化槽の高さを高くすると、浄化槽の
施工に浄化槽埋設用のピットを深く掘らねばならないな
ど施工費用、工程手間が嵩むという不都合が生じるた
め、むやみに高くすることができないという現状があ
り、また、散気管のエア供給を小さな気泡にして酸素溶
解効率を高めることも考えられるが、本来必要となる被
処理水循環機能が損なわれやすいという問題点があっ
た。However, according to the above-mentioned septic tank, the amount of air dissolved based on the picture supply from the air diffuser increases as the height of the septic tank (more precisely, the water depth of the air diffuser) increases. However, since septic tanks are usually buried underground, increasing the height of septic tanks causes the inconvenience of construction costs and process labor, such as having to dig deep into the septic tank embedding pit to construct septic tanks. Therefore, there is a current situation that it cannot be increased unnecessarily, and it is possible to increase the oxygen dissolution efficiency by making the air supply of the air diffuser into small bubbles, but it is easy to impair the originally required function of circulating the treated water. There was a problem.
【0004】従って、本発明の目的は、上記実情に鑑
み、簡単な構成によって、膜分離槽にエア溶解させるこ
とのできる技術を提供することにある。Therefore, in view of the above situation, an object of the present invention is to provide a technique capable of air-dissolving in a membrane separation tank with a simple structure.
【0005】[0005]
〔構成〕この目的を達成するための本発明の請求項1に
かかる特徴構成は、複数の水処理槽を備えてなり、前記
水処理槽の少なくとも1つを膜分離槽から構成してあ
り、前記膜分離槽とは異なる水処理槽に、被処理水移送
用の機械式ポンプを設けるとともに、被処理水を前記膜
分離槽とは異なる水処理槽から前記膜分離槽に移送する
移送管を前記機械式ポンプに連設してある浄化槽におけ
る被処理水へのエア溶解方法において、前記被処理水移
送管に気泡を供給することにあり、その作用効果は以下
の通りである。[Structure] The characteristic structure according to claim 1 of the present invention for achieving this object comprises a plurality of water treatment tanks, and at least one of the water treatment tanks is constituted by a membrane separation tank, A mechanical pump for transferring treated water is provided in a water treatment tank different from the membrane separation tank, and a transfer pipe for transferring the treated water from the water treatment tank different from the membrane separation tank to the membrane separation tank. In the method for dissolving air in treated water in a septic tank connected to the mechanical pump, bubbles are supplied to the treated water transfer pipe, and the effects thereof are as follows.
【0006】〔作用・効果〕つまり、上述の構成におい
ては、被処理水移送用の機械式ポンプは、単純に被処理
水を前記膜分離槽とは異なる水処理槽から前記膜分離槽
に移送するのみならず、その被処理水の移送中に、前記
被処理水移送管中に気泡が供給されるため、前記被処理
水移送管中で、前記被処理水にエア溶解される。そのた
め、膜分離槽では、被処理水に十分空気溶解した状態に
なりやすく、前記膜分離槽内の活性汚泥が酸素不足に陥
りにくく、安定した活性汚泥処理を行えるとともに、被
処理水の濾過水が、十分生物処理されたものになって、
外部に放流される廃水の水質が向上する。[Operation / Effect] That is, in the above-mentioned configuration, the mechanical pump for transferring the water to be treated simply transfers the water to be treated from the water treatment tank different from the membrane separation tank to the membrane separation tank. In addition, air bubbles are supplied into the treated water transfer pipe during the treatment water transfer, so that the treated water is air-dissolved in the treated water transfer pipe. Therefore, in the membrane separation tank, it tends to be in a state of being sufficiently air-dissolved in the water to be treated, activated sludge in the membrane separation tank is less likely to fall into oxygen deficiency, and stable activated sludge treatment can be performed, and the filtered water of the water to be treated is filtered. However, it has become fully biologically treated,
The quality of wastewater discharged to the outside is improved.
【0007】〔構成〕また、本発明の請求項2にかかる
特徴構成は、複数の水処理槽を備えてなり、前記水処理
槽の少なくとも1つを膜分離槽から構成してあり、前記
膜分離槽とは異なる水処理槽に、被処理水移送用のエア
リフトポンプを設けるとともに、被処理水を前記膜分離
槽とは異なる水処理槽から前記膜分離槽に移送する移送
管を前記エアリフトポンプに連設してある浄化槽におけ
る被処理水へのエア溶解方法において、前記移送管にエ
アリフト用の気泡よりも小さな微細気泡を供給すること
にあり、その作用効果は以下の通りである。[Structure] The characteristic structure according to claim 2 of the present invention comprises a plurality of water treatment tanks, wherein at least one of the water treatment tanks is constituted by a membrane separation tank. An air lift pump for transferring treated water is provided in a water treatment tank different from the separation tank, and a transfer pipe for transferring the treated water from the water treatment tank different from the membrane separation tank to the membrane separation tank is the air lift pump. In the method of dissolving air in the water to be treated in the septic tank continuously provided, fine bubbles smaller than the bubbles for air lift are supplied to the transfer pipe, and the action and effect are as follows.
【0008】〔作用・効果〕つまり、上述の構成におい
ては、被処理水移送用のポンプがエアリフトポンプであ
ったとしても、通常、エアリフト用に供給される気泡は
比較的大きく、比較的短時間に水面に達するため酸素溶
解効率が低くなり、酸素を溶解させるという機能がほと
んど得られず、逆に、微細な気泡のみではエアリフトの
ための揚底が得られないという不都合が生じるおそれが
あるのに対して、エアリフト用の気泡とは別途に、微細
気泡を供給するので、エアリフト機能を維持したまま空
気溶解の機能を付与することが出来る。 〔構成〕また、本発明の請求項3にかかる特徴構成は、
複数の水処理槽を備えてなり、前記水処理槽の少なくと
も1つを膜分離槽から構成してあり、前記膜分離槽とは
異なる水処理槽に、被処理水移送用の機械式ポンプを設
けるとともに、被処理水を前記膜分離槽とは異なる水処
理槽から前記膜分離槽に移送する移送管を前記機械式ポ
ンプに連設してある浄化槽において、前記移送管に気泡
を供給自在な給気装置を設けてあることにあり、その作
用効果は以下の通りである。[Operation / Effect] That is, in the above-mentioned configuration, even if the pump for transferring the water to be treated is an air lift pump, normally, the bubbles supplied for the air lift are relatively large and relatively short time. Since it reaches the water surface, the oxygen dissolution efficiency becomes low, and the function of dissolving oxygen is hardly obtained, and conversely, there is a possibility that a bottom for air lift cannot be obtained with only fine bubbles. On the other hand, since the fine bubbles are supplied separately from the air-lifting bubbles, the air-dissolving function can be imparted while maintaining the air-lifting function. [Structure] The characteristic structure according to claim 3 of the present invention is as follows.
A plurality of water treatment tanks are provided, at least one of the water treatment tanks is composed of a membrane separation tank, and a mechanical pump for transferring treated water is provided in a water treatment tank different from the membrane separation tank. In addition, in a septic tank in which a transfer pipe that transfers water to be treated from a water treatment tank different from the membrane separation tank to the membrane separation tank is connected to the mechanical pump, bubbles can be freely supplied to the transfer pipe. Since the air supply device is provided, its function and effect are as follows.
【0009】〔作用・効果〕つまり、移送管に気泡を供
給自在な給気装置を設けてあるために、従来の浄化槽に
対して簡単な構成を加えるだけで請求項1にかかる浄化
槽における被処理水へのエア溶解方法に対して、好適な
構成を得ることが出来る。 〔構成〕また、本発明の請求項4にかかる特徴構成は、
複数の水処理槽を備えてなり、前記水処理槽の少なくと
も1つを膜分離槽から構成してあり、前記膜分離槽とは
異なる水処理槽に、被処理水移送用のエアリフトポンプ
を設けるとともに、被処理水を前記膜分離槽とは異なる
水処理槽から前記膜分離槽に移送する移送管を前記エア
リフトポンプに連設してある浄化槽において、前記移送
管に気泡を供給自在な給気装置を設けてあることにあ
り、また、本発明の請求項5にかかる特徴構成は、請求
項4に記載の特徴構成に加え、前記エアリフトポンプ
に、エアリフト用の気泡よりも小さな微細気泡を供給自
在な給気装置を設けてあることにあり、その作用効果は
以下の通りである。[Operation / Effect] That is, since the transfer pipe is provided with an air supply device capable of supplying bubbles, the object to be treated in the septic tank according to claim 1 is simply added to the conventional septic tank. A suitable configuration can be obtained for the method of dissolving air in water. [Structure] The characteristic structure according to claim 4 of the present invention is as follows.
A plurality of water treatment tanks are provided, at least one of the water treatment tanks is a membrane separation tank, and an air lift pump for transferring water to be treated is provided in a water treatment tank different from the membrane separation tank. At the same time, in a septic tank in which a transfer pipe for transferring the water to be treated from a water treatment tank different from the membrane separation tank to the membrane separation tank is connected to the air lift pump, a supply air capable of supplying bubbles to the transfer pipe. Further, in addition to the characteristic structure according to claim 4, the device according to claim 5 of the present invention supplies fine air bubbles smaller than the air lift bubbles to the air lift pump. A free air supply device is provided, and its function and effect are as follows.
【0010】〔作用・効果〕つまり、上述の構成によれ
ば、被処理水に空気溶解容易な気泡を移送管に供給でき
るのでエアリフトポンプを設けてなる浄化槽であって
も、被処理水へのエア溶解が不十分となるのを抑制でき
る。尚、前記給気装置によって供給すべき気泡は、微細
な気泡であるほど水中での滞留時間が長く、また、気泡
の単位容積当たりの表面積が大きく、気液接触効率が高
くなるので、酸素溶解効率が高くなって有利である。[Operations / Effects] That is, according to the above-mentioned configuration, since bubbles capable of easily dissolving air in the water to be treated can be supplied to the transfer pipe, even in the septic tank provided with the air lift pump, It is possible to suppress insufficient air dissolution. The finer the bubbles to be supplied by the air supply device, the longer the residence time in water, the larger the surface area per unit volume of the bubbles, and the higher the gas-liquid contact efficiency. This is advantageous because the efficiency is high.
【0011】〔構成〕また、本発明の請求項6にかかる
特徴構成は、請求項3〜5のいずれかに記載の特徴構成
に加え、前記移送管に前記膜分離槽とは異なる水処理槽
と前記膜分離槽との間に横架してなる横管部を設け、前
記横管部に前記給気装置を設けてあることにあり、その
作用効果は以下の通りである。[Structure] In addition to the characteristic structure according to any one of claims 3 to 5, the characteristic structure according to claim 6 of the present invention is a water treatment tank different from the membrane separation tank in the transfer pipe. The horizontal pipe portion is provided between the membrane separation tank and the membrane separation tank, and the air supply device is provided in the horizontal pipe portion. The function and effect are as follows.
【0012】〔作用・効果〕つまり、前記横管部に給気
装置を設ければ、浄化槽の上部に給気装置が配設される
ことになり、前記給気装置のメンテナンスが容易である
とともに、水圧に抗してエア供給する必要もないから、
エア供給に要する動力も小さくて済む。[Operations / Effects] That is, if an air supply device is provided in the lateral pipe portion, the air supply device is arranged above the septic tank, and the maintenance of the air supply device is easy. Since there is no need to supply air against water pressure,
It requires less power to supply air.
【0013】尚、前記給気装置としては、例えばエジェ
クタが用いられ、この場合、被処理水移送用のポンプの
動力を用い、エジェクタによって移送管内にエア供給す
ることができるから、前記機械式ポンプあるいは、エア
リフトポンプの被処理水搬送力を用いてエア供給するこ
とができ、前記移送管に簡単な構成の変化を加えるだけ
で効率よくエア溶解効率を向上させることができる。As the air supply device, for example, an ejector is used. In this case, the power of the pump for transferring the water to be treated can be used to supply air into the transfer pipe by the ejector. Therefore, the mechanical pump is used. Alternatively, air can be supplied by using the treated water carrying force of the air lift pump, and the air dissolving efficiency can be efficiently improved by simply changing the configuration of the transfer pipe.
【0014】[0014]
【発明の実施の形態】以下に本発明の実施の形態を図面
に基づいて説明する。図1に示すように、本発明の浄化
槽は、円筒状の浄化槽本体Xの両端を鑑部X1,X2を
設けて内部に密閉空間を形成するとともに、内部の密閉
空間に仕切り壁を設けて区分けして、上流側から、流量
調整槽N、脱窒素槽E1、膜分離槽E2、放流ポンプ槽
Tを上流側から順に形成してあり、前記各槽の上部に
は、メンテナンス等に用いるマンホールHを設けてあ
る。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, the septic tank of the present invention is divided into two parts of a cylindrical septic tank body X by providing inspection parts X1 and X2 at both ends to form a closed space inside and partition walls provided inside the closed space. Then, from the upstream side, a flow rate adjusting tank N, a denitrification tank E1, a membrane separation tank E2, and a discharge pump tank T are sequentially formed from the upstream side, and a manhole H used for maintenance or the like is formed above the respective tanks. Is provided.
【0015】前記流量調整槽Nは、前記浄化槽本体Xの
一方の鑑部X1に設けてなる流入口Iから浄化槽内に流
入した被処理水の原水を受けて、その被処理水中の夾雑
物を沈殿除去しつつ、内部に生育する嫌気性菌により、
被処理水を嫌気処理しつつ、被処理水を一時貯留する水
処理室内に、被処理水を脱窒素槽E1に移送する第一ポ
ンプP1を設け、被処理水が大量に流入した場合や、長
期にわたって被処理水の流入が無い場合にも、被処理水
を定常的に脱窒素槽E1に移送して、後続の各水処理室
での水処理に支障をきたさないようにしてある。The flow rate adjusting tank N receives the raw water of the water to be treated that has flowed into the septic tank from the inlet I provided in the one portion X1 of the septic tank main body X, and removes the impurities in the water to be treated. While removing the precipitate, anaerobic bacteria growing inside,
A first pump P1 for transferring the water to be treated to the denitrification tank E1 is provided in the water treatment chamber for temporarily storing the water to be treated while performing the anaerobic treatment of the water to be treated, Even when there is no inflow of the water to be treated for a long period of time, the water to be treated is constantly transferred to the denitrification tank E1 so as not to hinder the water treatment in each of the subsequent water treatment chambers.
【0016】前記脱窒素槽E1は、前記流量調整槽Nに
隣接する水処理室に、前記流量調整槽Nからの被処理水
を流入させる流入管A1を、前記第一ポンプP1に接続
して設け、被処理水の流入路を構成してある。また、第
二ポンプP2を内装し、その第二ポンプP2に移送管A
2を設け、被処理水を前記膜分離槽E2へ移送する構成
にしてある。また、槽内の被処理水を攪拌循環させる攪
拌ポンプP4を内装してあり、槽内の被処理水の混合を
図り、BOD負荷の高い被処理水と、硝化済の被処理水
とを混合し、高度な脱窒処理を行える構成にしてある。The denitrification tank E1 is connected to the first pump P1 with an inflow pipe A1 for introducing water to be treated from the flow rate adjusting tank N into a water treatment chamber adjacent to the flow rate adjusting tank N. It is provided and constitutes an inflow path for the water to be treated. In addition, a second pump P2 is provided inside, and a transfer pipe A
2 is provided to transfer the water to be treated to the membrane separation tank E2. In addition, a stirring pump P4 that stirs and circulates the treated water in the tank is installed, and the treated water in the tank is mixed to mix the treated water having a high BOD load with the nitrified treated water. However, it is configured so that it can perform advanced denitrification processing.
【0017】前記第二ポンプP2は、水中浸漬型の機械
式ポンプ(いわゆる水中ポンプ)であり、前記第二ポン
プP2には、縦管1を接続するとともに、前記縦管1の
上部に前記脱窒素槽E1と前記膜分離槽E2との間に横
架してなる横管2を接続して前記移送管A2を構成して
あり、前記横管2には、エア吸入して微細気泡を前記横
管2内に供給するエジェクタ3Aを設けてある。The second pump P2 is an underwater immersion type mechanical pump (so-called submersible pump), and a vertical pipe 1 is connected to the second pump P2, and the desorption is provided on the upper portion of the vertical pipe 1. The transfer tube A2 is configured by connecting a horizontal tube 2 which is horizontally installed between the nitrogen tank E1 and the membrane separation tank E2, and air is sucked into the horizontal tube 2 to generate fine bubbles. An ejector 3A for supplying into the lateral pipe 2 is provided.
【0018】前記膜分離槽E2は、前記脱窒素槽E1と
の間を仕切る隔壁に、前記流入路を設けるとともに、前
記脱窒素槽E1から過剰に流入した被処理水を前記脱窒
素槽E1に返送する返送口A4を設けて、被処理水の返
送路を構成してある。また、多数の平板状の濾過膜板を
直立状態で平行に並設してなる膜分離装置Mを内装して
なり、前記膜分離装置Mは、濾過膜板の多数を整列して
保持する濾過膜板保持枠を設け、下部に前記濾過膜板保
持枠を支持する脚部を設け、前記脚部間にその濾過膜板
に気泡を供給して、その膜面に汚泥等の付着しすぎるの
を防止し、かつ、前記膜分離槽E2内に循環流を形成し
ながら被処理水に酸素を供給する散気装置Dを内装して
構成してある。また、前記膜分離装置Mのそれぞれの濾
過膜板には取水管M4を連設するとともに、前記取水管
M4からの濾過水を合流させて膜分離槽E1外へ導く集
水管M5を接続してあり、前記膜分離槽E2の水面より
も下方で前記膜分離槽E2に隣接する放流ポンプ槽Tに
連通接続してある。In the membrane separation tank E2, the inflow passage is provided in a partition wall that separates the denitrification tank E1 from the denitrification tank E1, and the water to be treated that has excessively flown into the denitrification tank E1 is supplied to the denitrification tank E1. A return port A4 for returning the water is provided to form a return path for the water to be treated. In addition, a membrane separation device M in which a large number of flat plate-shaped filtration membrane plates are arranged in parallel in an upright state is installed, and the membrane separation device M is a filtration device that holds a large number of filtration membrane plates in alignment. A membrane plate holding frame is provided, and a leg portion for supporting the filtration membrane plate holding frame is provided at the lower portion, and air bubbles are supplied to the filtration membrane plate between the leg portions so that sludge or the like adheres too much to the membrane surface. And a diffusing device D for supplying oxygen to the water to be treated while forming a circulating flow in the membrane separation tank E2. In addition, a water intake pipe M4 is connected to each of the filtration membrane plates of the membrane separation device M, and a water collection pipe M5 that joins the filtered water from the water intake pipe M4 and guides it to the outside of the membrane separation tank E1 is connected. Yes, it is connected to the discharge pump tank T adjacent to the membrane separation tank E2 below the water surface of the membrane separation tank E2.
【0019】前記放流ポンプ槽は、消毒槽Q1と、貯留
槽Q2とからなり、前記消毒槽Q1は、前記膜分離槽E
2と、前記放流ポンプ槽Tとを仕切る隔壁に処理水受け
容器を設け、その壁面に小孔を設けて構成してあり、前
記消毒槽Q1に流入した濾過水は、消毒されたのち貯留
槽Q2に流入する。前記貯留槽Q2は、第三ポンプP3
を内装してあり、前記処理水を貯留したのち、放流ポン
プP1で処理水を汲み上げ、排出管5を介して放流口Z
から浄化槽外へ放流可能に構成してある。これにより、
消毒済の処理水が前記貯留槽Tからほぼ定量的に浄化槽
外に放流される。The discharge pump tank comprises a disinfection tank Q1 and a storage tank Q2, and the disinfection tank Q1 is the membrane separation tank E.
2 and the discharge pump tank T are provided with a treated water receiving container on a partition wall, and a small hole is provided on the wall surface thereof. The filtered water flowing into the disinfecting tank Q1 is sterilized and then stored in the storage tank. It flows into Q2. The storage tank Q2 is a third pump P3.
After storing the treated water, the treated water is pumped up by the discharge pump P1 and discharged through the discharge pipe 5 to the discharge port Z.
It is configured so that it can be discharged to the outside of the septic tank. This allows
The disinfected treated water is discharged from the storage tank T to the outside of the septic tank almost quantitatively.
【0020】〔別実施形態〕以下に別の実施の形態を説
明する。先の実施の形態では、移送ポンプP2を水中浸
漬型の機械式ポンプ(いわゆる水中ポンプ)で構成した
が、これに限らず、エアリフトポンプPaで構成してあ
ってもよく、また、前記移送管A2を、前記第二ポンプ
P2に縦管1を接続するとともに、前記縦管1の上部に
前記脱窒素槽E1と前記膜分離槽E2との間に横架して
なる横管2を接続して構成し、前記横管2に、エア吸入
して前記横管2内に微細気泡を供給するエジェクタ3A
を設けて構成したが、前記縦管1にエジェクタを設けて
構成してあってもよく、さらには、給気装置3は、エジ
ェクタ3Aに替えて、ブロワでエア供給して微細気泡を
移送管内に送る構成であってもよい。つまり、図2に示
すように構成してあってもよい。図2においては、エア
リフト用の縦管に比較的大きな気泡を供給する空気供給
部1aを設けるとともに、前記気泡よりも小さな微細気
泡を供給する供給部3Bを設けてあり、共にブロワに接
続してある。[Another Embodiment] Another embodiment will be described below. In the above embodiment, the transfer pump P2 is configured by a submersible mechanical pump (so-called submersible pump), but the present invention is not limited to this, and it may be configured by an air lift pump Pa. A2 is connected to the vertical pipe 1 to the second pump P2, and a horizontal pipe 2 is connected to the upper portion of the vertical pipe 1 so as to extend horizontally between the denitrification tank E1 and the membrane separation tank E2. And an ejector 3A for sucking air into the lateral tube 2 to supply fine bubbles into the lateral tube 2.
Although the vertical pipe 1 may be provided with an ejector, the air supply device 3 may supply air with a blower instead of the ejector 3A to supply fine air bubbles in the transfer pipe. It may be configured to send to. That is, it may be configured as shown in FIG. In FIG. 2, a vertical pipe for air lift is provided with an air supply unit 1a for supplying relatively large bubbles, and a supply unit 3B for supplying fine bubbles smaller than the bubbles, both of which are connected to a blower. is there.
【0021】尚、特許請求の範囲の項に、図面との対照
を便利にするために符号を記すが、該記入により本発明
は添付図面の構成に限定されるものではない。It should be noted that reference numerals are added to the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図1】浄化槽の縦断側面図FIG. 1 is a vertical side view of a septic tank.
【図2】別実施形態における浄化槽の縦断側面図FIG. 2 is a vertical sectional side view of a septic tank according to another embodiment.
2 横管部 3 給気装置 3A エジェクタ A2 移送管 P2 機械式ポンプ Pa エアリフトポンプ E2 膜分離槽 2 Horizontal pipe part 3 Air supply device 3A Ejector A2 Transfer pipe P2 Mechanical pump Pa Air lift pump E2 Membrane separation tank
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岩橋 正修 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masahisa Iwahashi 1 share at 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside Kubota Shiga Factory (72) Inventor Katsumi Hamada 1 share at 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Kubota Shiga Factory
Claims (6)
理槽の少なくとも1つを膜分離槽(E2)から構成して
あり、前記膜分離槽(E2)とは異なる水処理槽に、被
処理水移送用の機械式ポンプ(P2)を設けるととも
に、被処理水を前記膜分離槽(E2)とは異なる水処理
槽から前記膜分離槽(E2)に移送する移送管(A2)
を前記機械式ポンプ(P2)に連設してある浄化槽にお
ける被処理水へのエア溶解方法であって、 前記移送管(A2)に気泡を供給する浄化槽における被
処理水へのエア溶解方法。1. A water treatment tank comprising a plurality of water treatment tanks, wherein at least one of the water treatment tanks comprises a membrane separation tank (E2), and the water treatment tank is different from the membrane separation tank (E2). , A transfer pipe (A2) which is provided with a mechanical pump (P2) for transferring treated water and transfers the treated water from a water treatment tank different from the membrane separation tank (E2) to the membrane separation tank (E2)
Is a method for dissolving air in the water to be treated in the septic tank connected to the mechanical pump (P2), wherein the air is dissolved in the water in the septic tank for supplying air bubbles to the transfer pipe (A2).
理槽の少なくとも1つを膜分離槽(E2)から構成して
あり、前記膜分離槽(E2)とは異なる水処理槽に、被
処理水移送用のエアリフトポンプ(Pa)を設けるとと
もに、被処理水を前記膜分離槽(E2)とは異なる水処
理槽から前記膜分離槽(E2)に移送する移送管(A
2)を前記エアリフトポンプ(Pa)に連設してある浄
化槽における被処理水へのエア溶解方法であって、 前記移送管(A2)にエアリフト用の気泡よりも小さな
微細気泡を供給する浄化槽における被処理水へのエア溶
解方法。2. A water treatment tank comprising a plurality of water treatment tanks, wherein at least one of the water treatment tanks is composed of a membrane separation tank (E2), and the water treatment tank is different from the membrane separation tank (E2). An air lift pump (Pa) for transferring treated water is provided, and a transfer pipe (A) for transferring the treated water from a water treatment tank different from the membrane separation tank (E2) to the membrane separation tank (E2).
2) is a method for dissolving air in water to be treated in a septic tank connected to the air lift pump (Pa), wherein the transfer pipe (A2) supplies fine air bubbles smaller than air lift air bubbles. Method of dissolving air in water to be treated.
理槽の少なくとも1つを膜分離槽(E2)から構成して
あり、前記膜分離槽(E2)とは異なる水処理槽に、被
処理水移送用の機械式ポンプ(P2)を設けるととも
に、被処理水を前記膜分離槽(E2)とは異なる水処理
槽から前記膜分離槽(E2)に移送する移送管(A2)
を前記機械式ポンプ(P2)に連設してある浄化槽であ
って、 前記移送管(A2)に気泡を供給自在な給気装置(3)
を設けてある浄化槽。3. A water treatment tank comprising a plurality of water treatment tanks, at least one of said water treatment tanks being composed of a membrane separation tank (E2), which is different from said membrane separation tank (E2). , A transfer pipe (A2) which is provided with a mechanical pump (P2) for transferring treated water and transfers the treated water from a water treatment tank different from the membrane separation tank (E2) to the membrane separation tank (E2)
An air supply device (3) for continuously supplying air bubbles to the transfer pipe (A2), which is a septic tank continuously connected to the mechanical pump (P2).
A septic tank equipped with.
理槽の少なくとも1つを膜分離槽(E2)から構成して
あり、前記膜分離槽(E2)とは異なる水処理槽に、被
処理水移送用のエアリフトポンプ(Pa)を設けるとと
もに、被処理水を前記膜分離槽(E2)とは異なる水処
理槽から前記膜分離槽(E2)に移送する移送管(A
2)を前記エアリフトポンプに連設してある浄化槽であ
って、 前記移送管(A2)に気泡を供給自在な給気装置(3)
を設けてある浄化槽。4. A water treatment tank comprising a plurality of water treatment tanks, wherein at least one of the water treatment tanks is composed of a membrane separation tank (E2), and the water treatment tank is different from the membrane separation tank (E2). An air lift pump (Pa) for transferring treated water is provided, and a transfer pipe (A) for transferring the treated water from a water treatment tank different from the membrane separation tank (E2) to the membrane separation tank (E2).
A septic tank in which 2) is connected to the air lift pump, and an air supply device (3) capable of supplying bubbles to the transfer pipe (A2).
A septic tank equipped with.
リフト用の気泡よりも小さな微細気泡を供給自在な給気
装置(3)を設けてある請求項4に記載の浄化槽。5. The septic tank according to claim 4, wherein the air lift pump (Pa) is provided with an air supply device (3) capable of supplying fine air bubbles smaller than air lift air bubbles.
2)とは異なる水処理槽と前記膜分離槽(E2)との間
に横架してなる横管部(2)を設け、前記横管部(2)
に前記給気装置(3)を設けてある請求項3〜5のいず
れかに記載の浄化槽。6. The membrane separation tank (E) is attached to the transfer pipe (A2).
A horizontal pipe section (2) is provided between the water treatment tank different from 2) and the membrane separation tank (E2), and the horizontal pipe section (2) is provided.
The septic tank according to any one of claims 3 to 5, wherein the air supply device (3) is provided in the.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21558295A JPH0957262A (en) | 1995-08-24 | 1995-08-24 | Method for dissolving air in treated water in septic tank and septic tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21558295A JPH0957262A (en) | 1995-08-24 | 1995-08-24 | Method for dissolving air in treated water in septic tank and septic tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0957262A true JPH0957262A (en) | 1997-03-04 |
Family
ID=16674830
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21558295A Pending JPH0957262A (en) | 1995-08-24 | 1995-08-24 | Method for dissolving air in treated water in septic tank and septic tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0957262A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011001918A (en) * | 2009-06-19 | 2011-01-06 | Kubota Corp | Air lift pump device |
| JP2014031797A (en) * | 2013-11-21 | 2014-02-20 | Kubota Corp | Air lift pump device |
| JP2014031798A (en) * | 2013-11-21 | 2014-02-20 | Kubota Corp | Air lift pump device |
-
1995
- 1995-08-24 JP JP21558295A patent/JPH0957262A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011001918A (en) * | 2009-06-19 | 2011-01-06 | Kubota Corp | Air lift pump device |
| JP2014031797A (en) * | 2013-11-21 | 2014-02-20 | Kubota Corp | Air lift pump device |
| JP2014031798A (en) * | 2013-11-21 | 2014-02-20 | Kubota Corp | Air lift pump device |
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