JP2008253958A - Method and apparatus for treating drain water by using negative pressure generating means - Google Patents

Method and apparatus for treating drain water by using negative pressure generating means Download PDF

Info

Publication number
JP2008253958A
JP2008253958A JP2007101735A JP2007101735A JP2008253958A JP 2008253958 A JP2008253958 A JP 2008253958A JP 2007101735 A JP2007101735 A JP 2007101735A JP 2007101735 A JP2007101735 A JP 2007101735A JP 2008253958 A JP2008253958 A JP 2008253958A
Authority
JP
Japan
Prior art keywords
drain
drain water
water
negative pressure
tank
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
JP2007101735A
Other languages
Japanese (ja)
Inventor
Akihiro Takemae
昭宏 竹前
Tatsu Matsuhashi
竜 松橋
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.)
Orion Machinery Co Ltd
Original Assignee
Orion Machinery 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 Orion Machinery Co Ltd filed Critical Orion Machinery Co Ltd
Priority to JP2007101735A priority Critical patent/JP2008253958A/en
Publication of JP2008253958A publication Critical patent/JP2008253958A/en
Pending legal-status Critical Current

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for treating drain water from an oil separation apparatus, wherein the inexpensive and compact apparatus is used while sending drain water actively. <P>SOLUTION: The apparatus for treating drain water is composed of a pretreatment tank opened to the atmosphere, a water level-determining means and an airtight posttreatment tank. The posttreatment tank has: a drain water inlet, which is connected to an upstream-side pipeline through a drain check valve, at the lower part thereof; a drain water outlet, which is connected to a downstream-side pipeline through a check valve, on the upper side surface thereof; and a negative pressure generating means, which generates negative pressure according to the determination of the water level judgement means, at the uppermost part thereof. The negative pressure generating means is controlled by an air pressure control circuit according to the water level judgement. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、コンプレッサ等から排出されるドレン水の処理方法、特に安価でコンパクトな装置が求められる場合に適する処理方法とドレン水処理装置に関する。   The present invention relates to a method for treating drain water discharged from a compressor or the like, and more particularly, to a treatment method and a drain water treatment device suitable when an inexpensive and compact device is required.

ドレン処理装置においては、ドレン発生源からのドレン水を吸着処理槽、電解処理槽等の機器に通して排水可能な水質にまで浄化する必要がある。現在使われているドレン水処理装置では、ドレン水の送水手段として、圧縮空気による圧送、水頭差による流下、電動ポンプによる送水などの方式を用いている。   In the drain treatment apparatus, it is necessary to purify the drain water from the drain generation source to a water quality that can be drained by passing it through devices such as an adsorption treatment tank and an electrolytic treatment tank. In the drain water treatment apparatus currently used, as a drain water feeding means, a method such as pressure feeding with compressed air, flowing down due to a water head difference, water feeding with an electric pump is used.

圧縮空気を直接用いる方式は、ドレントラップが作動するとドレン水が本管の圧縮空気と共に噴出するので、この排圧を直接利用してドレン水を圧送させるものである。この方式は電源を必要とせず設計の自由度も高いが、各部の構造をすべてドレン管の圧力(内圧)に対応できる安全性を考慮したものにする必要があり、コスト高になる欠点がある。   In the method using the compressed air directly, the drain water is jetted together with the compressed air in the main pipe when the drain trap is operated, so that the drain water is directly used to pump the drain water. This method does not require a power supply and has a high degree of freedom in design. However, it is necessary to consider the safety of each part structure to handle the pressure (internal pressure) of the drain pipe, and there is a drawback that the cost increases. .

水頭差を利用する方式は、噴出したドレン水をいったん貯溜して大気開放したのち、貯溜槽の下方の配管系統に導き、ドレン水の自重を利用してドレン水を送るものである。この方式では動力を用いず内圧も高くならないので構造はシンプルであるが、機器の配置が制約される、配管内のドレン水を強制的に一掃できないので吸着材の目詰まりの際に対応できない等の問題がある。   In the method using the water head difference, the discharged drain water is temporarily stored and released to the atmosphere, then guided to a piping system below the storage tank, and the drain water is sent using its own weight. In this method, the power is not used and the internal pressure does not increase, so the structure is simple.However, the arrangement of the equipment is restricted, and the drain water in the piping cannot be forcibly cleared, so it cannot cope with clogging of the adsorbent. There is a problem.

そこで別の方法として、噴出したドレン水をいったん大気開放したのち、電動ポンプを用いて能動的に加圧送水する方法がある。この方法は、必要な部分のみを加圧することができて合理的であるが、送水に電気を使用するため、電力のほか漏電等の安全対策にコストがかかる、吸着材の目詰まりの際は空運転によるポンプの焼き付きのおそれがある、等の問題がある。従って各方式に一長一短があり、決定的なものはなかった。   Therefore, as another method, there is a method in which the discharged drain water is once released into the atmosphere and then actively pressurized and fed using an electric pump. This method is rational because it can pressurize only the necessary parts, but because electricity is used for water supply, it costs money for safety measures such as electric leakage as well as power, and when adsorbents are clogged There are problems such as the possibility of seizing the pump during idling. Therefore, each method had advantages and disadvantages, and none was decisive.

特開2001−17961号公報記載の発明は、大気開放式の前処理槽と密閉式の後処理槽の間に2個の逆止弁を介して圧送ユニットを接続し、圧送ユニットは一方で本管からの加圧空気と大気圧とに切り換え可能な電磁弁に接続したものである。ドレントラップの作動により噴出したドレン水はいったん大気開放式の前処理槽に導入して不純物を粗取りされたのち、自重で前処理槽の下端から圧送ユニットに入る。圧送ユニット内の水位が所定高さになると圧送ユニット内のフロートスイッチの作用により本管に接続した電磁弁が数回開き、ドレン水はその圧力で断続的に後段に配置された後処理槽へ給送され、必要な後処理が行われ、浄化水となって排出される。この方式は電動ポンプによるものと同様に能動的な加圧送水を行うので前段に大気開放式の処理槽を使用でき、加圧空気による攪拌効果も期待できるうえ、電気を使用しないため比較的コストが安い等の特長を有する。
特開2001−17961号公報
In the invention described in Japanese Patent Application Laid-Open No. 2001-17961, a pressure feeding unit is connected between two open check valves between a pre-treatment tank open to the atmosphere and a sealed post-treatment tank. It is connected to a solenoid valve that can be switched between pressurized air from the pipe and atmospheric pressure. The drain water ejected by the operation of the drain trap is once introduced into a pretreatment tank that is open to the atmosphere, and after impurities are roughly removed, it enters the pressure feeding unit from its lower end by its own weight. When the water level in the pumping unit reaches a predetermined height, the solenoid valve connected to the main pipe opens several times by the action of the float switch in the pumping unit, and the drain water is intermittently placed at the subsequent stage by the pressure to the post-treatment tank. It is fed, the necessary post-processing is performed, and it is discharged as purified water. This method performs active pressurized water supply as with an electric pump, so an open-air treatment tank can be used in the previous stage, and a stirring effect by pressurized air can be expected. Has features such as low price.
JP 2001-17961 A

特許文献1記載の技術は様々の長所を有し設置目的によっては十分満足の行くものであるが、後処理槽が内圧を受けるためある程度大型でコスト高の容器を使用せざるを得ず、より安価でコンパクトな装置が求められる使用条件では問題となっていた。そこで本発明は、油水分離装置のドレン水の処理方法において、能動的なドレン送水を行いつつ、いっそう安価でコンパクトな装置ですむ方法を提供することを目的とする。   The technology described in Patent Document 1 has various advantages and is sufficiently satisfactory depending on the purpose of installation, but the post-treatment tank is subject to internal pressure, and thus a large and expensive container must be used. This has been a problem under use conditions where an inexpensive and compact device is required. Accordingly, an object of the present invention is to provide a method for treating a drain water of an oil / water separator so that a more inexpensive and compact apparatus can be used while actively draining water.

本出願の請求項1記載の発明は、吸着処理槽を使用したドレン水の処理において、いったん大気開放したドレン水を吸着材を充填した吸着処理槽に導入し、該吸着材の下流側より負圧発生手段で吸引することによりドレン水を給送するドレン水の処理方法により、上記の課題を解決する。ドレン水の強制送水には加圧手段を用いるのが一般的であるが、従来の処理方法における耐圧容器の大型化などの問題をなくするために、逆に負圧発生手段で吸引するという新しい構成を採用したものである。使用条件により特に安価でコンパクトな装置が求められる場合に最適な処理方法を提供する。   In the first aspect of the present application, in the drain water treatment using the adsorption treatment tank, the drain water once released to the atmosphere is introduced into the adsorption treatment tank filled with the adsorbent, and the negative water is discharged from the downstream side of the adsorbent. The above problem is solved by a drain water treatment method in which drain water is fed by being sucked by a pressure generating means. Although it is common to use a pressurizing means for the forced water supply of drain water, in order to eliminate the problems such as an increase in the size of the pressure vessel in the conventional treatment method, a new method of suctioning with the negative pressure generating means is used. The configuration is adopted. An optimum processing method is provided when a particularly inexpensive and compact apparatus is required depending on use conditions.

本出願の請求項2記載の発明は、請求項1記載のドレン水処理方法において、負圧発生手段を圧縮空気配管に一次流側(主エア)を接続されたエゼクタとしたものである。エゼクタで負圧を発生させることにより、電動ポンプ等を使用しなくても本管の圧縮空気を利用してドレンを送水することができ、環境配慮に優れた無電源の装置を実現することができる。   The invention according to claim 2 of the present application is the drain water treatment method according to claim 1, wherein the negative pressure generating means is an ejector in which the primary flow side (main air) is connected to the compressed air pipe. By generating negative pressure with the ejector, it is possible to supply drainage using the compressed air of the main pipe without using an electric pump, etc., and to realize an environmentally friendly and non-powered device it can.

本出願の請求項3記載の発明は、請求項1または2記載のドレン水処理方法において、吸着処理槽の前段に水位判定手段を設け、上流側水位が設定水位以下である場合に前記負圧発生手段を作動させるようにしたものである。前段に一定以上のドレン水が貯溜されている場合のみ強制送水を行うようにして、いっそう省エネルギー性を高めたものである。   The invention according to claim 3 of the present application is the drain water treatment method according to claim 1 or 2, wherein the water pressure determination means is provided in the front stage of the adsorption treatment tank, and the negative pressure is obtained when the upstream water level is equal to or lower than the set water level. The generating means is operated. Energy saving is further improved by performing forced water supply only when a certain amount or more of drain water is stored in the previous stage.

本出願の請求項4記載の発明は、大気開放された前処理槽と、水位判定手段と、密閉型の後処理槽とから構成され、前記後処理槽は下部にドレン逆止弁を介して上流側配管に接続されたドレン水入口を有し、上部側面には逆止弁を介して下流配管に接続されたドレン水出口を有し、最上部に水位判定手段の判定に従って負圧を発生する負圧発生手段が設置されているドレン水処理装置により、上記の課題を解決する。本発明は前処理槽と後処理槽を設けた二段階の処理を行うものであるが、後処理槽の最上部に負圧発生手段を設け下側のドレン水入口から流入したドレン水を強制的に上昇させて上側のドレン水出口から排出することにより、特に請求項3に記載したドレン水処理方法を合理的に実現するものである。ドレン水入口及び出口に設けた逆止弁はドレン水の逆流を防止している。   Invention of Claim 4 of this application is comprised from the pre-processing tank open | released to air | atmosphere, a water level determination means, and a closed-type post-processing tank, and the said post-processing tank is via a drain check valve in the lower part. It has a drain water inlet connected to the upstream pipe, and has a drain water outlet connected to the downstream pipe via a check valve on the upper side, and generates negative pressure at the top according to the judgment of the water level judgment means The above problem is solved by a drain water treatment device in which negative pressure generating means is installed. The present invention performs a two-stage process with a pre-treatment tank and a post-treatment tank, but a negative pressure generating means is provided at the top of the post-treatment tank to force the drain water flowing from the lower drain water inlet. In particular, the drain water treatment method according to claim 3 is rationally realized by raising the temperature and discharging it from the upper drain water outlet. Check valves provided at the drain water inlet and outlet prevent the back flow of drain water.

さらに好ましくは水位判定にもとづく負圧発生手段の制御を無電源の空気圧制御手段によって行うことにより、無電源の装置が実現される。前後の処理槽の中間部から支管を分岐させ、開水面を設けてフロートスイッチを設置する。フロートは後述のエア作動バルブの入力信号を加圧側と大気圧側に切換えるメカニカルバルブに連結されている。フロートが所定高さを越えるとメカニカルバルブが作動してエア作動バルブに作動信号を送り、エア作動バルブがエゼクタの一次側を大気圧側から加圧側に切換えてエゼクタに圧縮空気を供給し、負圧を発生させる。エア作動バルブの入力信号は併設された遅延回路により一定時間保持される。このようにして電気的な制御回路を用いることなく、所定のタイミングで負圧を発生させることができる。   More preferably, a device without a power source is realized by controlling the negative pressure generating unit based on the water level determination by a pneumatic control unit without a power source. A branch pipe is branched from the middle part of the front and rear treatment tanks, an open water surface is provided and a float switch is installed. The float is connected to a mechanical valve that switches an input signal of an air operated valve, which will be described later, between a pressurizing side and an atmospheric pressure side. When the float exceeds the specified height, the mechanical valve is activated to send an actuation signal to the air actuated valve. The air actuated valve switches the primary side of the ejector from the atmospheric pressure side to the pressurized side and supplies compressed air to the ejector. Generate pressure. The input signal of the air actuated valve is held for a certain time by a delay circuit provided therewith. Thus, a negative pressure can be generated at a predetermined timing without using an electrical control circuit.

以下、図面を参照しながら、本発明の具体的な実施形態について説明する。図1は本発明のドレン水処理方法を用いたドレン処理装置の一例を示す説明図であり、実線はドレン水配管、破線は空気配管を表している。図において、1は前処理槽、2は水位判定手段、3は後処理槽、4は空気圧制御手段を示す。   Hereinafter, specific embodiments of the present invention will be described with reference to the drawings. FIG. 1 is an explanatory view showing an example of a drain treatment apparatus using the drain water treatment method of the present invention, in which a solid line represents a drain water pipe and a broken line represents an air pipe. In the figure, 1 is a pretreatment tank, 2 is a water level determination means, 3 is a post-treatment tank, and 4 is an air pressure control means.

本実施例の前処理槽1は、ドレン水を貯溜するほかに、コンプレッサからドレン水と共に排出される圧縮空気を大気中に放出し、ドレン水に元々粗大な油粒子として含まれる油分を吸着等により処理する機能を有する。前処理槽1は油分の粗取りに適した前処理吸着材101が充填された円柱型の容器102からなり、容器102の頂部は、圧縮空気配管のドレン発生源に図示しないドレントラップを介して接続されたドレン入口103が設けられている。ドレン入口103は一部が容器内側へ突出するようにされ、その周囲には多数の通気口104が設けられている。容器102の上部の側面には、液面に浮上した油等を排出するオーバーフロー管105が接続され、下部の側面にはドレン出口106が設けられている。   The pretreatment tank 1 of the present embodiment not only stores drain water, but also releases compressed air discharged from the compressor together with the drain water into the atmosphere, and adsorbs oil components originally contained as coarse oil particles in the drain water. It has the function to process by. The pretreatment tank 1 is composed of a cylindrical container 102 filled with a pretreatment adsorbent 101 suitable for rough oil removal, and the top of the container 102 is connected to a drain generation source of a compressed air pipe via a drain trap (not shown). A connected drain inlet 103 is provided. A part of the drain inlet 103 protrudes to the inside of the container, and a number of vent holes 104 are provided around the drain inlet 103. An overflow pipe 105 that discharges oil and the like floating on the liquid surface is connected to the upper side surface of the container 102, and a drain outlet 106 is provided on the lower side surface.

ドレン入口103から圧縮空気と共に流入したドレンは、大気開放された前処理槽1の上部の空間において減圧されて気液分離され、液体部分のみが自重で前処理吸着材101の内部を流下しながら油分を粗取りされる。この間に余分な圧力空気は容器頂部の通気孔104から排出され、比重差により液面に浮上した油粒子はオーバーフロー管105から排出される。吸着材101を通過したドレン水は容器102の下部に貯溜され、一部は水頭圧によりドレン出口106から水位判定手段2及び後処理槽3へ流出する。   The drain that flows in along with the compressed air from the drain inlet 103 is depressurized and separated into gas and liquid in the space above the pretreatment tank 1 that is open to the atmosphere, and only the liquid part flows under the pretreatment adsorbent 101 under its own weight. The oil is roughly removed. During this time, excess pressurized air is discharged from the vent 104 at the top of the container, and oil particles that have floated to the liquid surface due to the difference in specific gravity are discharged from the overflow pipe 105. The drain water that has passed through the adsorbent 101 is stored in the lower part of the container 102, and part of the drain water flows out from the drain outlet 106 to the water level determination means 2 and the post-treatment tank 3 due to water head pressure.

前処理槽1のドレン出口106に接続されたドレン配管からは排水用のドレン弁V1と水位判定手段2への支管がそれぞれ分岐している。水位判定手段2は上向きの支管の先端の拡径部201とその中に設けられたフロート202からなる。フロート202は空気圧制御手段4のメカニカルバルブ401と連結され、前処理槽1内部のドレン水が所定の高さとなった時に作動するフロートスイッチを構成している。ドレン本管はさらに延び、逆止弁V2を介して後処理槽3に接続されている。   From the drain pipe connected to the drain outlet 106 of the pretreatment tank 1, a drain valve V1 for drainage and a branch pipe to the water level determination means 2 are branched. The water level determination means 2 is composed of an enlarged diameter portion 201 at the tip of the upward branch pipe and a float 202 provided therein. The float 202 is connected to the mechanical valve 401 of the air pressure control means 4 and constitutes a float switch that operates when the drain water in the pretreatment tank 1 reaches a predetermined height. The drain main pipe further extends and is connected to the post-treatment tank 3 via a check valve V2.

後処理槽3は、細かい油粒子を吸着可能な後処理吸着材301が充填された円柱型の容器302からなる。容器302の上部には吸着材が配置されない真空溜まりが設けられており、頂部に負圧発生手段であるエゼクタ403の負圧側配管が接続されている。容器302の下部側面にはドレン入口303が設けられ、逆止弁V2を介してドレン本管に接続されている。また上部側面にはドレン出口304が設けられ、逆止弁V3を介して下流側配管に接続されている。   The post-treatment tank 3 includes a cylindrical container 302 filled with a post-treatment adsorbent 301 capable of adsorbing fine oil particles. A vacuum reservoir in which no adsorbent is disposed is provided at the top of the container 302, and a negative pressure side pipe of an ejector 403, which is a negative pressure generating means, is connected to the top. A drain inlet 303 is provided on the lower side surface of the container 302 and is connected to a drain main pipe via a check valve V2. Further, a drain outlet 304 is provided on the upper side surface, and is connected to the downstream pipe via a check valve V3.

負圧発生手段が作動すると真空溜まりの内部が減圧され、ドレン本管に対して負圧となるので、ドレン入口303よりドレン水が流入して、後処理吸着材301の内部を上昇する。この間にドレン水は微細な油分を吸着され、排水可能な水質にまで浄化される。ドレン出口304の高さを越える位置にある処理水は水頭により出口304より流出し、図示しない放流口から放流される。このときドレン入口303の逆止弁V2は、後処理槽3の負圧が解除された時に水頭圧でドレン水が逆流するのを防ぐ。またドレン出口304の逆止弁V3は、後処理槽3に負圧が供給された時にドレン出口から大気又はドレン水が流入するのを防ぐ。   When the negative pressure generating means is activated, the inside of the vacuum reservoir is depressurized and becomes negative pressure with respect to the drain main pipe, so that drain water flows from the drain inlet 303 and rises inside the post-treatment adsorbent 301. During this time, the drain water is adsorbed with fine oil and purified to a water quality that can be drained. The treated water at a position exceeding the height of the drain outlet 304 flows out from the outlet 304 by the water head and is discharged from a discharge port (not shown). At this time, the check valve V2 at the drain inlet 303 prevents the drain water from flowing backward due to the head pressure when the negative pressure in the post-treatment tank 3 is released. The check valve V3 at the drain outlet 304 prevents air or drain water from flowing from the drain outlet when a negative pressure is supplied to the post-treatment tank 3.

次に空気圧制御手段について説明する。フロート202に連結されたメカニカルバルブ401は圧縮空気配管とエア作動バルブ402のPIL端子に接続されており、フロート202の動作に従ってエア作動バルブ402の入力信号を加圧側と大気圧側に切換える。エア作動バルブ402は圧縮空気配管とエゼクタ403に接続されており、PIL入力信号に従ってエゼクタ403の一次側への圧縮空気(主エア)を供給し又は遮断する。エゼクタ403は一次側に圧縮空気が供給される時に後処理槽3に接続された負圧側配管に負圧を発生させる。タイムディレーバルブ404と逆止弁405とは、エア作動バルブ402の入力信号を一定時間の間保持するための遅延回路として作用する。   Next, the air pressure control means will be described. The mechanical valve 401 connected to the float 202 is connected to the compressed air piping and the PIL terminal of the air operating valve 402, and the input signal of the air operating valve 402 is switched between the pressure side and the atmospheric pressure side according to the operation of the float 202. The air operation valve 402 is connected to the compressed air piping and the ejector 403, and supplies or blocks compressed air (main air) to the primary side of the ejector 403 according to the PIL input signal. The ejector 403 generates negative pressure in the negative pressure side pipe connected to the post-treatment tank 3 when compressed air is supplied to the primary side. The time delay valve 404 and the check valve 405 act as a delay circuit for holding the input signal of the air operation valve 402 for a certain time.

図2は各部の作動タイミングを示すタイムチャートである。ドレン水の貯溜によりフロート202が所定高さを越えると、メカニカルバルブ401が作動してエア作動バルブ402に作動信号を送り、エア作動バルブ402がエゼクタ403の一次側に圧縮空気を供給しすることにより負圧を発生させる。負圧が後処理槽3上部に供給されると、まもなくドレン入口303より後処理槽3内にドレン水が流入し、水位判定手段2内の水位が下降するのでフロート202及びメカニカルバルブ402は元の状態に復帰するが、タイムディレーバルブ404に設定された一定時間の間はPIL手前の逆止弁405でメカニカルバルブ401からの信号を保持し、エアー作動バルブ403から圧縮空気が供給され、エアーエゼクタ404が負圧を発生する。この間に前処理槽1及び水位判定手段2内に残ったドレン水も後処理槽3に送られる。   FIG. 2 is a time chart showing the operation timing of each part. When the float 202 exceeds a predetermined height due to accumulation of drain water, the mechanical valve 401 is activated to send an operation signal to the air operation valve 402, and the air operation valve 402 supplies compressed air to the primary side of the ejector 403. To generate negative pressure. When the negative pressure is supplied to the upper portion of the post-treatment tank 3, drain water will soon flow into the post-treatment tank 3 from the drain inlet 303, and the water level in the water level determination means 2 will drop, so the float 202 and the mechanical valve 402 The signal from the mechanical valve 401 is held by the check valve 405 before the PIL for a predetermined time set in the time delay valve 404, and compressed air is supplied from the air operating valve 403, The ejector 404 generates a negative pressure. During this time, the drain water remaining in the pretreatment tank 1 and the water level determination means 2 is also sent to the posttreatment tank 3.

本発明のドレン処理方法及びドレン処理装置では、各処理系等の構成部品が外圧設計となるため、従来の内圧品と比較して装置の小型軽量化が可能となり、また破裂等の危険がないから安全面でも優位となる。従ってドレン発生源毎に設置されるような安価でコンパクトな処理装置として有利なものである。また本装置は無電源の装置であるから、環境配慮にも優れ、多大な利用可能性がある。   In the drain processing method and the drain processing apparatus of the present invention, components such as each processing system are designed with an external pressure, so that the apparatus can be made smaller and lighter than conventional internal pressure products, and there is no risk of rupture or the like. Therefore, it is also superior in terms of safety. Therefore, it is advantageous as an inexpensive and compact processing apparatus installed for each drain generation source. Moreover, since this apparatus is a non-powered apparatus, it is excellent in environmental consideration and has a great potential for use.

本発明のドレン水処理方法を用いたドレン処理装置の一例を示す説明図である。It is explanatory drawing which shows an example of the drain processing apparatus using the drain water processing method of this invention. 図1の装置の各部の動作順序を示すタイミングチャートである。It is a timing chart which shows the operation | movement order of each part of the apparatus of FIG.

符号の説明Explanation of symbols

1 前処理槽
101 前処理吸着材
102 容器
103 ドレン入口
104 通気口
105 オーバーフロー管
106 ドレン出口
2 水位判定手段
201 拡径部
202 フロート
3 後処理槽
301 後処理吸着材
302 容器
303 ドレン入口
304 ドレン出口
4 空気圧制御手段
401 メカニカルバルブ
402 エア作動バルブ
403 エゼクタ
404 タイムディレーバルブ
405 逆止弁
DESCRIPTION OF SYMBOLS 1 Pretreatment tank 101 Pretreatment adsorbent 102 Container 103 Drain inlet 104 Ventilation hole 105 Overflow pipe 106 Drain outlet 2 Water level judgment means 201 Expanded diameter 202 Float 3 Posttreatment tank 301 Posttreatment adsorbent 302 Container 303 Drain inlet 304 Drain outlet 4 Pneumatic control means 401 Mechanical valve 402 Air operated valve 403 Ejector 404 Time delay valve 405 Check valve

Claims (4)

吸着処理槽を使用したドレン水の処理において、いったん大気開放したドレン水を吸着材を充填した吸着処理槽に導入し、該吸着材の下流側より負圧発生手段で吸引することによりドレン水を給送するドレン水の処理方法。 In the drain water treatment using the adsorption treatment tank, the drain water once released to the atmosphere is introduced into the adsorption treatment tank filled with the adsorbent, and the drain water is sucked by the negative pressure generating means from the downstream side of the adsorbent. Treatment method of drain water to be fed. 前記負圧発生手段が、圧縮空気配管に一次流側を接続されたエゼクタであることを特徴とする請求項1記載のドレン水の処理方法。 The drain water treatment method according to claim 1, wherein the negative pressure generating means is an ejector having a primary flow side connected to a compressed air pipe. 前記吸着処理槽の前段に水位判定手段を設け、上流側水位が設定水位以上である場合に前記負圧発生手段を作動させることを特徴とする請求項1または2記載のドレン水の処理方法。 The method for treating drain water according to claim 1 or 2, wherein a water level determination means is provided in a preceding stage of the adsorption treatment tank, and the negative pressure generation means is operated when the upstream water level is equal to or higher than a set water level. 大気開放された前処理槽と、水位判定手段と、密閉型の後処理槽とから構成され、前記後処理槽は下部にドレン逆止弁を介して上流側配管に接続されたドレン水入口を有し、上部側面には逆止弁を介して下流配管に接続されたドレン水出口を有し、最上部に水位判定手段の判定に従って負圧を発生する負圧発生手段が設置されているドレン水処理装置。 The pretreatment tank opened to the atmosphere, a water level determination means, and a sealed type posttreatment tank, the posttreatment tank has a drain water inlet connected to an upstream pipe via a drain check valve at the bottom. A drain having a drain water outlet connected to the downstream pipe via a check valve on the upper side surface, and a drain generating means for generating a negative pressure according to the determination of the water level determining means is installed at the top Water treatment equipment.
JP2007101735A 2007-04-09 2007-04-09 Method and apparatus for treating drain water by using negative pressure generating means Pending JP2008253958A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007101735A JP2008253958A (en) 2007-04-09 2007-04-09 Method and apparatus for treating drain water by using negative pressure generating means

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007101735A JP2008253958A (en) 2007-04-09 2007-04-09 Method and apparatus for treating drain water by using negative pressure generating means

Publications (1)

Publication Number Publication Date
JP2008253958A true JP2008253958A (en) 2008-10-23

Family

ID=39978096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007101735A Pending JP2008253958A (en) 2007-04-09 2007-04-09 Method and apparatus for treating drain water by using negative pressure generating means

Country Status (1)

Country Link
JP (1) JP2008253958A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012130845A (en) * 2010-12-21 2012-07-12 Orion Machinery Co Ltd Method for treating drain water
CN103626320A (en) * 2013-12-05 2014-03-12 朱明扬 Efficient oil-water separating device and system for treating cleaning sewage

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012130845A (en) * 2010-12-21 2012-07-12 Orion Machinery Co Ltd Method for treating drain water
CN103626320A (en) * 2013-12-05 2014-03-12 朱明扬 Efficient oil-water separating device and system for treating cleaning sewage
CN103626320B (en) * 2013-12-05 2015-02-04 朱明扬 Efficient oil-water separating device and system for treating cleaning sewage

Similar Documents

Publication Publication Date Title
JP2011020025A (en) Oil-water separator
US20150265980A1 (en) Air diffusion device, air diffusion method, and water treatment device
CN105269705A (en) Processing apparatus
KR20080074100A (en) Automatic gas discharging device for lithium-bromid machine and method thereof
CN100522835C (en) Method and apparatus for treating waste water containing low-concentration perfluoro ammonium caprylate
JP2010012418A (en) Floating oil recovery device and floating oil recovery method
JP2008253958A (en) Method and apparatus for treating drain water by using negative pressure generating means
US3070935A (en) Water degasifier
JP5347132B2 (en) Sludge concentration method and sludge concentration system
JP5548412B2 (en) Oil / water separator
JP4262568B2 (en) Oil / water separator
JP6470103B2 (en) Fuel cell that separates gas from cooling water
US20170209831A1 (en) Air drier
CN106745509B (en) Vacuum oil-water separator
CN104192982A (en) MBR pulse aeration device free of extra power and aeration system with same
JP2015211952A (en) Collection device for floating foreign material
JP2006051484A (en) Method for separating oil from drain water and oil separating apparatus
JP2006122766A (en) Method and apparatus for oil-water separation
JP3842951B2 (en) Oil / water separator
JP2009183890A (en) Oil and water separation apparatus
JP2020091020A (en) Life extension system of oil for hydraulic circuit
JP2005007378A (en) Charcoal type water purification device
JP2005279469A (en) Apparatus and method for concentrating sludge
CN102678537A (en) Actuator for automatic discharging device of air flotation circulating pump
JP5639203B2 (en) Absorption tower cleaning method and digestion gas purification apparatus