JPH0550050A - Device for removing deposit in pipe - Google Patents
Device for removing deposit in pipeInfo
- Publication number
- JPH0550050A JPH0550050A JP3235531A JP23553191A JPH0550050A JP H0550050 A JPH0550050 A JP H0550050A JP 3235531 A JP3235531 A JP 3235531A JP 23553191 A JP23553191 A JP 23553191A JP H0550050 A JPH0550050 A JP H0550050A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- pig
- pump
- waste liquid
- drainage
- 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.)
- Withdrawn
Links
Landscapes
- Sewage (AREA)
- Cleaning In General (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は管の内壁に付着した付着
物を除去する装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for removing deposits adhering to the inner wall of a pipe.
【0002】[0002]
【従来の技術】自動車等の塗装を行う部署からは窒素化
合物や他の有機物を含む有機質廃液が多量に排出される
ため、通常これを生物学的方法によって浄化処理するよ
うにしている。2. Description of the Related Art Since a large amount of organic waste liquid containing nitrogen compounds and other organic substances is discharged from a painting department of an automobile or the like, it is usually purified by a biological method.
【0003】ところが、このような浄化処理を長期に亘
って行ってゆくと、塗装前処理工程での処理排液や電着
工程での電着排液が排水管の内壁に沈降付着して管路が
狭窄し、これがもとでポンプがオーバーヒートしたり、
排出量の減少に伴って前処理槽や電着槽から廃液がオー
バーフローしたり、さらには凝集槽への廃液の流入量が
減少することにより曝気槽や沈降槽内のBOD成分酸化
菌や硝化菌の濃度分布に変動をきたして、浄化処理が十
分でないままに排水を外部に放出してしまうといった不
都合が生じる。However, when such a purification treatment is carried out for a long period of time, the treated drainage liquid in the pre-painting treatment process and the electrodeposited drainage liquid in the electrodeposition process settle and adhere to the inner wall of the drain pipe. The passage is constricted, which causes the pump to overheat,
The waste liquid overflows from the pretreatment tank and the electrodeposition tank as the discharge amount decreases, and further, the flow amount of the waste liquid into the coagulation tank decreases, so that the BOD component oxidizing bacteria and nitrifying bacteria in the aeration tank and the sedimentation tank are reduced. However, there is a problem in that the concentration distribution of the wastewater fluctuates, and the wastewater is discharged to the outside without sufficient purification treatment.
【0004】このような問題に対してこれまでは、排水
管路の一部に設けた継手管の部分から内部にポリウレタ
ン発泡材よりなるピグを挿入し、これを廃液送出用ポン
プにより圧送しながら排水管内の沈降硬化物を除去する
ようにしていたが、この操作には通常硬度が順に小さく
なるようなピグを用いて4回行う必要があるため、その
都度継手管を取外したり接続したりしなければならない
繁雑な手間がかかるばかりでなく、排水管に付設したポ
ンプによってはピグを十分に圧送することができず、こ
の結果、これらが排水管路中で詰ったりあるいは十分に
付着物を除去することができないといった不都合を有し
ていた。In order to solve such a problem, a pig made of polyurethane foam is inserted into the inside of a joint pipe provided in a part of a drainage pipe, and this is pumped by a waste liquid delivery pump. The settling-hardened material in the drainage pipe was removed, but this operation usually needs to be performed four times using a pig whose hardness gradually decreases, so the fitting pipe must be removed or connected each time. Not only is it complicated and time-consuming, but the pumps attached to the drainage pipes cannot pump the pigs sufficiently, and as a result, they clog the drainage pipes or sufficiently remove deposits. It had the inconvenience of being unable to do so.
【0005】[0005]
【発明が解決しようとする課題】本発明はこのような問
題に鑑みてなされたもので、その目的とするところは、
継手管を脱着することなく、しかも必要な圧送力をもっ
てピグによる管路内の付着物を確実に除去することので
きる新たな管内付着物の除去装置を提供することにあ
る。SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and its object is to:
It is an object of the present invention to provide a new device for removing deposits in a pipe, which can reliably remove deposits in a pipe line by a pig without detaching the joint pipe and with a necessary pumping force.
【0006】[0006]
【課題を解決するための手段】すなわち、本発明はこの
ような課題を達成するための管内付着物の除去装置とし
て、排水管路の基端部に、排液送出ポンプを迂回するバ
イパス管を併設し、このバイパス管に、上流側から下流
側に向けてピグ圧送用のポンプと常時閉塞状態に保持さ
れるピグ挿入部を配設し、このピグ挿入部から管内に挿
入したピグを専用のピグ圧送用ポンプによって排水管路
内に圧送しつつ、管路内の付着物を除去するようにした
ものである。That is, according to the present invention, a bypass pipe bypassing a drainage delivery pump is provided at the base end of a drainage pipe line as a device for removing deposits in a pipe for achieving such a subject. Along with this bypass pipe, a pump for pumping pigs from the upstream side to the downstream side and a pig insertion part that is always kept in a closed state are arranged, and the pig inserted from this pig insertion part into the pipe is dedicated. The pigs are pumped into the drainage pipe while being pumped into the drainage pipe to remove the deposits.
【0007】[0007]
【実施例】そこで以下に図示した実施例について説明す
る。図1は、有機質廃液を活性汚泥法により浄化する装
置に対して適用した本発明の一実施例を示したものであ
る。EXAMPLES The examples shown below will be described below. FIG. 1 shows an embodiment of the present invention applied to an apparatus for purifying organic waste liquid by an activated sludge method.
【0008】はじめにこの浄化装置の概要構成と、この
装置を用いた排水の生物学的浄化処理法について説明す
ると、塗装前処理工程あるいは電着工程で排出される窒
素化合物や他の有機物を含む有機質排水は、一旦収容槽
1内に収容され、ついで、排水管10により凝集槽2に
導かれ、ここで硫酸アルミニウム、塩化第2鉄等の無機
質凝集剤及び有機質凝集剤により塗料成分の凝集除去が
行われる。First, the general structure of this purification apparatus and the biological purification method of wastewater using this apparatus will be described. Organic substances containing nitrogen compounds and other organic substances discharged in the pre-painting treatment step or the electrodeposition step. The wastewater is temporarily stored in the storage tank 1 and then guided to the coagulation tank 2 by the drainage pipe 10, where the coagulation and removal of the paint components is carried out by the inorganic coagulant such as aluminum sulfate and ferric chloride and the organic coagulant. Done.
【0009】塗料成分の凝集除去が行われた廃液は、つ
ぎにBOD成分酸化菌もしくは硝化菌を含む汚泥を貯え
た高負荷曝気槽3に導入され、ここでエアレーションと
液中攪拌とにより高速曝気処理され、ここからオーバー
フローした汚泥を含む廃液は、ついでBOD成分酸化菌
もしくは硝化菌を含む汚泥を貯えた標準曝気槽4に導か
れ、ここでエアレーション法により曝気処理されて、B
OD成分は硝酸性窒素あるいは亜硝酸性窒素に酸化ある
いは硝化される。The waste liquid from which the paint components have been coagulated and removed is then introduced into a high-load aeration tank 3 in which sludge containing BOD component oxidizing bacteria or nitrifying bacteria is stored, where high-speed aeration is performed by aeration and submerged stirring. The waste liquid containing sludge that has been treated and overflowed from there is then introduced into a standard aeration tank 4 that stores sludge containing BOD-oxidizing bacteria or nitrifying bacteria, where it is aerated by the aeration method,
The OD component is oxidized or nitrified into nitrate nitrogen or nitrite nitrogen.
【0010】これらの汚泥を含んだ廃液はさらに沈降槽
5に導入され、ここで硝酸性窒素、亜硝酸性窒素及び汚
泥は沈降分離されて、上澄液は後の工程へと排出され、
また沈降分離された汚泥は、循環ポンプ6により循環管
路7を経て上記した高負荷曝気槽3及び標準曝気槽4へ
回収されて再使用される。The waste liquid containing these sludges is further introduced into the sedimentation tank 5, where the nitrate nitrogen, the nitrite nitrogen and the sludge are separated by sedimentation, and the supernatant liquid is discharged to the subsequent step,
The sludge that has been separated by settling is collected by the circulation pump 6 through the circulation pipe 7 into the high-load aeration tank 3 and the standard aeration tank 4 and reused.
【0011】ところで、本発明の特徴部分をなす管路内
付着物の除去装置は、上記した収容槽1と凝集槽2を結
ぶ排水管10に配設されている。この排水管10には、
基端部の上流側に排水管10の管路開閉用の第1の弁1
1が設けられ、またこの第1の弁11の下流側には後述
するバイパス管20が接続する前後2つの三方継手1
2、13が接合されていて、これらの三方継手12、1
3の間には管路内の清浄時に排水管10の管路を閉塞す
る第2の弁14を介してその下流側に廃液送出用のポン
プ15が配設されている。By the way, the apparatus for removing deposits in a conduit, which is a feature of the present invention, is arranged in the drain pipe 10 connecting the above-mentioned storage tank 1 and coagulation tank 2. In this drain pipe 10,
The first valve 1 for opening and closing the pipeline of the drainage pipe 10 is provided on the upstream side of the base end portion.
1 is provided on the downstream side of the first valve 11, and two front and rear three-way joints 1 to which a bypass pipe 20 described later is connected.
2 and 13 are joined together, and these three-way joints 12, 1
A pump 15 for delivering waste liquid is disposed downstream of the second valve 14 that closes the pipeline of the drainage pipe 10 when the inside of the pipeline is clean.
【0012】一方、廃液送出用ポンプを迂回するように
前後2つの三方継手12、13を介して排水管10の基
端部に接続されたバイパス管20は、排水管10と同じ
口径をなす管として構成され、このバイパス管20の上
流側には、管路内の清浄時にこのバイパス管20の管路
を開放する第3の弁21が設けられていて、その下流側
には、廃液送出用ポンプ15より強力なピグ圧送用ポン
プ22が配設され、さらにその下流側には、このバイパ
ス管20内にピグを挿入するための三方継手24が接続
されている。On the other hand, the bypass pipe 20 connected to the base end portion of the drain pipe 10 via two front and rear three-way joints 12 and 13 so as to bypass the waste liquid delivery pump has the same diameter as the drain pipe 10. A third valve 21 is provided on the upstream side of the bypass pipe 20 to open the pipeline of the bypass pipe 20 when the inside of the pipeline is cleaned. A pig pressure feeding pump 22 which is stronger than the pump 15 is provided, and a three-way joint 24 for inserting a pig into the bypass pipe 20 is connected to the downstream side thereof.
【0013】このピグ挿入用の三方継手24は、図2に
示したように、その解放管端25が常時蓋体26により
閉塞されていて、排水管10内の付着物を除去する際に
のみ蓋体26を開放してここから後述する2つのピグ2
7、28を挿入するように構成されている。As shown in FIG. 2, the three-way joint 24 for inserting a pig has the open pipe end 25 always closed by the lid 26, and only when removing the deposit in the drain pipe 10. With the lid 26 open, two pigs 2 to be described later will be described.
It is configured to insert 7, 28.
【0014】このピグ挿入用三方継手24の開放管端2
5からは、短いロープ29によって結合された2つのピ
グ27、28を挿入し、これらを強力なピグ圧送用ポン
プ22によりバイパス管20から三方継手13を経て排
水管10内に送り込んで、排水管10の内壁に沈降し付
着硬化した前処理廃液や電着廃液を除去するように構成
されている。The open pipe end 2 of the three-way joint 24 for inserting a pig
From FIG. 5, two pigs 27, 28 connected by a short rope 29 are inserted, and these are sent from the bypass pipe 20 to the drain pipe 10 through the three-way joint 13 by the powerful pig pump 22 for draining the drain pipe. It is configured to remove the pretreatment waste liquid and the electrodeposition waste liquid that have settled on the inner wall of 10 and adhered and hardened.
【0015】この廃液除去に使用される2つのピグ2
7、28は、ポリウレタン発泡体のような適度の弾性を
有する耐蝕材により成形され、さらにこれらのピグ2
7、28は、先に挿入される第1のピグ27の方が後に
挿入される第2のピグ28より硬い素材により形成され
る。Two pigs 2 used for removing this waste liquid
7 and 28 are made of a corrosion-resistant material having an appropriate elasticity such as polyurethane foam.
The first and second pigs 27 and 28 that are inserted first are made of a material that is harder than the second pig 28 that is inserted later.
【0016】またこれらのピグ27、28は、第1のピ
グ30の外径d∃が排水管10の内径Dより0.3乃至
0.5mm程度大きく、また第2のピグ28の径dÅが排
水管10の内径Dより0.5乃至0.7mm大きく形成さ
れている。実験によれば、第1のピグ27の外径d∃が
d∃<D+0.3mmであると十分な清浄効果が得られ
ず、また第2のピグ28の外径dÅがdÅ>D+0.7
mmであると、圧送用ポンプ22に多大の負荷がかかりば
かりでなく清浄効果にさしたる差が生じないことが判っ
た。In these pigs 27 and 28, the outer diameter d∃ of the first pig 30 is larger than the inner diameter D of the drain pipe 10 by about 0.3 to 0.5 mm, and the diameter dÅ of the second pig 28 is larger. The inner diameter D of the drainage pipe 10 is made larger by 0.5 to 0.7 mm. According to the experiment, if the outer diameter d∃ of the first pig 27 is d∃ <D + 0.3 mm, a sufficient cleaning effect cannot be obtained, and the outer diameter dÅ of the second pig 28 is dÅ> D + 0.7.
It has been found that when the value is mm, not only a great load is applied to the pump 22 for pumping, but also a difference in cleaning effect does not occur.
【0017】このように構成された浄化装置は、通常、
第3の弁21によってバイパス管20を閉塞した状態で
使用される。そしてこの状態で、前処理工程あるいは電
着工程で排出される窒素化合物や他の有機物を含む有機
質廃液を収容槽1から凝集槽2に導いて、硫酸アルミニ
ウム、塩化第2鉄等の無機質凝集剤及び有機質凝集剤に
より塗料成分を凝集除去し、ついでここからの廃液を高
負荷曝気槽3と標準曝気槽4に順次導いてエアレーショ
ン法により曝気するとともに、この中のBOD成分酸化
菌もしくは硝化菌を含む汚泥によりBOD成分を酸化も
しくは硝化し、さらにここから汚泥とともに廃液を沈降
槽5に導いて、生物学的に浄化処理した廃液のうちその
上澄み液のみを外部に排出する。The purifying device constructed as described above is usually
It is used with the bypass valve 20 closed by the third valve 21. Then, in this state, an organic waste liquid containing a nitrogen compound and other organic substances discharged in the pretreatment step or the electrodeposition step is introduced from the storage tank 1 to the aggregating tank 2, and the inorganic aggregating agent such as aluminum sulfate and ferric chloride is introduced. And the organic flocculant is used to coagulate and remove the paint components, and then the waste liquid from this is guided to the high load aeration tank 3 and the standard aeration tank 4 in order to be aerated by the aeration method, and the BOD component oxidizing bacteria or nitrifying bacteria therein The BOD component is oxidized or nitrified by the contained sludge, and the waste liquid together with the sludge is guided to the settling tank 5 from this, and only the supernatant liquid of the biologically purified waste liquid is discharged to the outside.
【0018】ところで、このような処理を長期にわたっ
て行うと、収容槽1と凝集槽2を結ぶ排水管10の内壁
には、前処理廃液や電着廃液が沈着して管路が狭窄し、
排水送出用ポンプ15がオーバーヒートしたり、収容槽
1や凝集槽2から排水がオーバーフローするような事態
が生じるから、ある一定の使用期間が経過したら、廃液
送出用ポンプ15の上流側に位置する第2の弁14を閉
止する。By the way, if such a treatment is carried out for a long period of time, the pretreatment waste liquid and the electrodeposition waste liquid are deposited on the inner wall of the drainage pipe 10 connecting the storage tank 1 and the coagulation tank 2 and the pipeline is narrowed,
Since the drainage pump 15 overheats and the drainage overflows from the storage tank 1 and the coagulation tank 2, after a certain period of use, the drainage pump 15 located upstream The valve 14 of No. 2 is closed.
【0019】そして、第3の弁21を閉塞したままの状
態で、ピグ挿入用三方継手24から蓋体26を外し、こ
こからロープ29によって結合された第1のピグ27と
第2のピグ28をこの順に継手24内に挿入して蓋体2
6を閉める。Then, with the third valve 21 still closed, the lid 26 is removed from the three-way joint 24 for pig insertion, and from there, the first pig 27 and the second pig 28 joined by the rope 29. Insert in this order into the joint 24 and cover 2
Close 6
【0020】ついでこの状態のもとで第3の弁21を開
くとともに、ピグ圧送用ポンプ22を始動させると、2
つのピグ27、28は、この専用のポンプ22によって
強く押圧されつつバイパス管20から排水管10内へ押
出され、先行する硬度の大なる第1のピグ27によっ
て、はじめに排水管10の内壁に付着した付着物を粗落
としするとともに、後続するやや大径の第2のピグ28
により排水管10の内壁に残存する付着物を払拭し、1
回の操作によって排水管10内の清浄を完全に終了す
る。Then, under this condition, the third valve 21 is opened and the pig pressure-feeding pump 22 is started.
The two pigs 27, 28 are pushed out from the bypass pipe 20 into the drain pipe 10 while being strongly pressed by the dedicated pump 22, and are first attached to the inner wall of the drain pipe 10 by the preceding first pig 27 having high hardness. Roughly remove the adhered deposits, and the second pig 28 with a slightly larger diameter that follows
Wipe off the deposits remaining on the inner wall of the drain pipe 10 by
The cleaning of the inside of the drainage pipe 10 is completely completed by performing the operation once.
【0021】そしてこれらのピグ27、28が凝集槽2
内に排出されて所定の清浄処理が終了したら、第3の弁
を閉じてバイパス管20の管路を閉塞するとともに、第
2の弁14を開いて再び廃液処理の可能な状態に戻す。These pigs 27 and 28 are used in the flocculation tank 2
When it is discharged into the interior and the predetermined cleaning process is completed, the third valve is closed to close the conduit of the bypass pipe 20, and the second valve 14 is opened to restore the waste liquid processable state.
【0022】なお上述した実施例では、硬軟2つのピグ
27、28を用いるようにしたものであるが、排水管1
0内の清浄の難易によっては、3連あるいは4連のピグ
を用いることができ、また従来のもののように1つずつ
ピグを挿入して排水管10内を清浄するようにしてもよ
い。In the above-described embodiment, the two hard and soft pigs 27 and 28 are used, but the drain pipe 1
Depending on the difficulty of cleaning inside 0, three or four pigs can be used, and as in the conventional case, one pig may be inserted to clean the inside of the drainage pipe 10.
【0023】[0023]
【発明の効果】以上述べたように本発明によれば、廃液
送出用ポンプを迂回するようにして排水管路の基端部に
併設したバイパス管に、上流側から下流側に向けてピグ
圧送用のポンプとピグ挿入部を配設したので、ピグ挿入
部からピグを挿入して、これをピグ圧送用ポンプにより
圧送するだけの操作によって、排水管路の清浄をきわめ
て簡単にかつ効率よく行うことができる。As described above, according to the present invention, the pig is pumped from the upstream side to the downstream side to the bypass pipe provided at the base end of the drainage pipe so as to bypass the waste liquid delivery pump. Since the pump and the pig insertion part are installed, the pig can be inserted from the pig insertion part and the pump for pumping the pig can be used to pump it to clean the drainage pipe very easily and efficiently. be able to.
【0024】しかも、廃液送出用ポンプに頼ることな
く、バイパス管路に配設した専用のピグ圧送用ポンプに
よりピグを圧送するようにしたので、このポンプにピグ
の圧送に必要な能力を付与させるだけで、ピグの詰りを
生じさせることなく管路内の清浄作業をきわめて能率よ
く行わせることができる。Moreover, since the pig is pumped by the dedicated pump for pumping the pig arranged in the bypass line without relying on the pump for pumping the waste liquid, this pump is provided with the capability necessary for pumping the pig. Only by doing so, it is possible to perform the cleaning work in the pipe line extremely efficiently without causing clogging of the pig.
【図1】本発明の一実施例をなす装置を備えた廃液浄化
装置の一例を示した図である。FIG. 1 is a diagram showing an example of a waste liquid purification apparatus provided with an apparatus that constitutes an embodiment of the present invention.
【図2】同上装置の要部を示した断面図である。FIG. 2 is a sectional view showing a main part of the same device.
1 収容槽 2 凝集槽 10 排水管 15 廃液送出用ポンプ 20 バイパス管 22 ピグ圧送用ポンプ 24 ピグ挿入用三方継手 26 蓋体 27、28 ピグ 1 Storage Tank 2 Coagulation Tank 10 Drain Pipe 15 Waste Liquid Delivery Pump 20 Bypass Pipe 22 Pig Pressure Delivery Pump 24 Pig Three Way Joint 26 Lid 27, 28 Pig
Claims (1)
迂回するバイパス管を併設して、該バイパス管に、上流
側から下流側に向けてピグ圧送用のポンプと常時閉塞状
態に保持されるピグ挿入部を配設した管内付着物の除去
装置。1. A bypass pipe bypassing a drainage delivery pump is provided at a base end portion of a drainage pipe line, and the bypass pipe is constantly closed with a pump for pig pressure feed from an upstream side to a downstream side. A device for removing deposits in a pipe, which is provided with a pig insertion portion that is held by the pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3235531A JPH0550050A (en) | 1991-08-22 | 1991-08-22 | Device for removing deposit in pipe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3235531A JPH0550050A (en) | 1991-08-22 | 1991-08-22 | Device for removing deposit in pipe |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0550050A true JPH0550050A (en) | 1993-03-02 |
Family
ID=16987358
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3235531A Withdrawn JPH0550050A (en) | 1991-08-22 | 1991-08-22 | Device for removing deposit in pipe |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0550050A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011094798A1 (en) * | 2010-02-07 | 2011-08-11 | Ian Doig | Pipeline conveyor systems |
KR101359330B1 (en) * | 2013-10-04 | 2014-03-12 | (주)이오렉스 | Apparatus for preventing scale within drinking water pipes |
JP2018155092A (en) * | 2017-03-15 | 2018-10-04 | 株式会社栗本鐵工所 | Method for removing contaminant on inner face of pipeline |
-
1991
- 1991-08-22 JP JP3235531A patent/JPH0550050A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011094798A1 (en) * | 2010-02-07 | 2011-08-11 | Ian Doig | Pipeline conveyor systems |
CN102811931A (en) * | 2010-02-07 | 2012-12-05 | 伊恩·多伊格 | Pipeline conveying system |
AU2011213541B2 (en) * | 2010-02-07 | 2015-07-30 | Ian Doig | Pipeline conveyor systems |
KR101359330B1 (en) * | 2013-10-04 | 2014-03-12 | (주)이오렉스 | Apparatus for preventing scale within drinking water pipes |
JP2018155092A (en) * | 2017-03-15 | 2018-10-04 | 株式会社栗本鐵工所 | Method for removing contaminant on inner face of pipeline |
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