JP3373788B2 - Contaminated groundwater purification equipment - Google Patents

Contaminated groundwater purification equipment

Info

Publication number
JP3373788B2
JP3373788B2 JP22997198A JP22997198A JP3373788B2 JP 3373788 B2 JP3373788 B2 JP 3373788B2 JP 22997198 A JP22997198 A JP 22997198A JP 22997198 A JP22997198 A JP 22997198A JP 3373788 B2 JP3373788 B2 JP 3373788B2
Authority
JP
Japan
Prior art keywords
pipe
gas
liquid separation
well
separation 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.)
Expired - Fee Related
Application number
JP22997198A
Other languages
Japanese (ja)
Other versions
JP2000042531A (en
Inventor
基治 根岸
Original Assignee
株式会社日さく
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 株式会社日さく filed Critical 株式会社日さく
Priority to JP22997198A priority Critical patent/JP3373788B2/en
Publication of JP2000042531A publication Critical patent/JP2000042531A/en
Application granted granted Critical
Publication of JP3373788B2 publication Critical patent/JP3373788B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、有機塩素系化合物
によって汚染された地下水の浄化装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for purifying groundwater contaminated with organic chlorine compounds.

【0002】[0002]

【従来の技術】有機塩素系化合物によって汚染された地
下水の浄化を行う方法としては、従来、井管中に水中モ
ータポンプを設置して地下水を揚水する方法やこの方法
に地下水に空気を送る管を併設するエアースパージング
方法が採られていたが、水中モータポンプによる揚水法
では、第1に汚染地下水を地上に揚水して地上で曝気処
理する方法であるため、作業効率がきわめて悪く、特に
低濃度の汚染地下水の場合には経済効率が問題となって
いたし、第2にモータポンプ部が井管内にあるため、そ
のメンテナンスに時間とコストがかかっていた。
2. Description of the Related Art Conventional methods for purifying groundwater contaminated with organochlorine compounds include a method of pumping groundwater by installing a submersible motor pump in a well pipe or a pipe for sending air to the groundwater. The air sparging method was also used, but in the pumping method using a submersible motor pump, the first is the method of pumping contaminated groundwater to the ground and performing aeration treatment on the ground. In the case of contaminated groundwater with a concentration, economic efficiency became a problem, and secondly, because the motor pump part was inside the well pipe, its maintenance took time and cost.

【0003】[0003]

【発明が解決しようとする課題】本発明は、このような
従来工法による揚水の欠点を一掃し、汚染地下水の揚水
をエアーリフトによって行うことにより装置を簡素化
し、メンテナンスを容易に行うことができるようにコス
トの縮減を図るとともに、地下汚染物質の処理効率を増
大することを目的とするものである。
SUMMARY OF THE INVENTION The present invention eliminates the drawbacks of pumping water by the conventional method and simplifies the apparatus by pumping the contaminated groundwater by an air lift, and facilitates maintenance. The purpose is to reduce costs and increase the efficiency of underground pollutant treatment.

【0004】[0004]

【課題を解決するための手段】本発明においては、井管
内の揚水管の下側部に及んで,地上に設置したコンプレ
ッサに連通する送気管を挿入するとともにこのコンプレ
ッサに連通する他の送気管を井管の適所に及んで挿入
し、前記揚水管を地上に設置した気液分離槽に連通し、
この気液分離槽において分離した汚染物質を吸着処理器
へ送るとともに分離後の地下水を前記井管に戻すように
して成る汚染地下水の浄化方法を実施するために、次の
装置が考えられる。
According to the present invention, an air supply pipe communicating with a compressor installed on the ground is inserted to extend to the lower side of a pumping pipe in a well pipe and another air supply pipe communicates with this compressor. Inserted into the well pipe in place, communicate the pumping pipe to the gas-liquid separation tank installed on the ground,
In order to carry out the method for purifying contaminated groundwater by sending the pollutants separated in the gas-liquid separation tank to the adsorption treatment device and returning the separated groundwater to the wells, the following device can be considered.

【0005】第1に、飽和帯と不飽和帯に臨む位置にそ
れぞれスクリーンを設けた井管の地下水面位置にパッカ
ーを取付け、地上に設置したコンプレッサに連設する一
方の送気管を前記井管内の揚水管の下側部に及んで挿入
するとともに他方の送気管を前記井管の上部スクリーン
付近に及んで挿入し、前記揚水管を地上に設置した気液
分離槽に連設し、この気液分離槽からの排気管を汚染物
質吸着器に連設するとともに気液分離槽からの戻水管を
前記井管に連通して成る浄化装置である。
[0005] First, a packer is installed at the water table position of the well pipe having screens at positions facing the saturated zone and the unsaturated zone, respectively, and one air pipe connected to a compressor installed on the ground is provided in the well pipe. Of the pumping pipe, and the other air pipe is inserted near the upper screen of the well pipe, and the pumping pipe is connected to the gas-liquid separation tank installed on the ground. This is a purification device in which an exhaust pipe from a liquid separation tank is connected to a contaminant adsorber and a return water pipe from a gas-liquid separation tank is connected to the well pipe.

【0006】第2に、井管内の揚水管の下側部に及ん
で、地上に設置したコンプレッサに連設する一方の送気
管を挿入するとともに他方の送気管を井管のスクリーン
付近に及んで挿入し、前記揚水管を地上に設置した気液
分離槽に連設し、この気液分離槽からの排気管を汚染物
質吸着器に連設するとともに気液分離槽からの戻水管を
前記井管に連通して成る浄化装置である。
Secondly, one air pipe connected to a compressor installed on the ground is inserted to reach the lower side of the pump pipe in the well pipe, and the other air pipe is extended near the screen of the well pipe. Insert the pumping pipe to the gas-liquid separation tank installed on the ground, connect the exhaust pipe from the gas-liquid separation tank to the contaminant adsorber and the return pipe from the gas-liquid separation tank to the well. It is a purification device that communicates with a pipe.

【0007】[0007]

【発明の実施の形態】図1に示した装置例では、井管の
飽和帯(帯水層)にある下部スクリーンから流入する汚
染地下水は、揚水管の下側部において地上のコンプレッ
サから送り込まれた圧縮空気によるエアーリフト効果に
より押し上げられ、地上の気液分離槽に導入される。こ
の際、前記汚染地下水は送り込まれた圧縮空気によるエ
アーレーション効果によって、気液分離が促進されるこ
とになる。
BEST MODE FOR CARRYING OUT THE INVENTION In the apparatus example shown in FIG. 1, contaminated groundwater flowing in from a lower screen in a saturated zone (aquifer) of a well pipe is sent from a compressor on the ground at a lower side of a pumping pipe. It is pushed up by the air lift effect of compressed air and introduced into the gas-liquid separation tank on the ground. At this time, the contaminated groundwater is promoted in gas-liquid separation due to the aeration effect of the compressed air sent in.

【0008】汚染地下水中の汚染物質は揮発性の物質で
あるから、圧縮空気によるエアーレーション効果により
分離が促進され、気液分離槽において容易に分離され
る。汚染気体は排気管から活性炭吸着器へ送られ、ここ
で吸着処理された後、外部へ放出され、また分離後の地
下水は戻水管から井管へ戻され、パッカー上部に滞留し
た後、上部スクリーンから地下水面の上位にある不飽和
帯(非帯水層)に還元注入するようになる。
Since the pollutants in the contaminated groundwater are volatile substances, the separation is promoted by the aeration effect of the compressed air and is easily separated in the gas-liquid separation tank. The polluted gas is sent from the exhaust pipe to the activated carbon adsorber, where it is adsorbed and then released to the outside, and the separated groundwater is returned from the return pipe to the well pipe and stays at the upper part of the packer, then the upper screen. Will start reducing injection into the unsaturated zone (non-aquifer) above the water table.

【0009】井管に戻された地下水は、コンプレッサか
ら送り込まれた圧縮空気に出会うから、これによるエア
ーレーション化によって、前記戻された地下水中に残留
汚染物質のあるときは、さらに再気化分離を促進され、
汚染物質が除去された地下水が上部スクリーンから不飽
和帯(非帯水層)に注入されるようになる。再気化分離
した汚染気体は、井管上部の排気管から排出され、汚染
物質吸着器を経由して外部に排出される。
The groundwater returned to the well pipe encounters the compressed air sent from the compressor. Therefore, if residual pollutants are contained in the returned groundwater by the aeration by this, further re-vaporization separation is performed. Promoted,
Groundwater from which pollutants have been removed will be injected into the unsaturated zone (non-aquifer) from the upper screen. The re-vaporized and separated pollutant gas is discharged from the exhaust pipe in the upper part of the well pipe and discharged to the outside via the pollutant adsorber.

【0010】図2に示した装置例では、井管の飽和帯に
あるスクリーンから流入する汚染地下水は、揚水管の下
側部において地上のコンプレッサから送り込まれた圧縮
空気によるエアーリフト効果により押し上げられ、地上
の気液分離槽に導入される。この際、前記汚染地下水は
送り込まれた圧縮空気によるエアーレーション効果によ
って、気液分離が促進されることになる。
In the device example shown in FIG. 2, the contaminated groundwater flowing in from the screen in the saturation zone of the well pipe is pushed up by the air lift effect by the compressed air sent from the compressor on the ground at the lower side of the pump pipe. , Is introduced into the gas-liquid separation tank on the ground. At this time, the contaminated groundwater is promoted in gas-liquid separation due to the aeration effect of the compressed air sent in.

【0011】この気液分離槽において分離された揮発性
の汚染気体は、排気管から汚染物質吸着器へ送られ、こ
こで吸着処理された後、大気層へ放出され、また分離後
の地下水は注入管から井管へ戻されて滞留するから、こ
の地下水を新規採取の汚染地下水とともに循環処理する
ようになる。
The volatile pollutant gas separated in this gas-liquid separation tank is sent from an exhaust pipe to a pollutant adsorber, where it is adsorbed and released into the atmospheric layer, and ground water after separation is Since it is returned from the injection pipe to the well and stays there, this groundwater will be circulated along with the newly collected contaminated groundwater.

【0012】前記コンプレッサからは別の送気管が井管
のスクリーン付近に臨設しているから、飽和帯から採取
された汚染地下水に対しエアーレーションを起して揮発
性物質の気散化を促進する。
Since a separate air pipe from the compressor is provided near the screen of the well pipe, aeration is caused to the contaminated groundwater collected from the saturated zone to promote the vaporization of volatile substances. .

【0013】このように、この装置例では、井管内と揚
水管内の2個所において汚染地下水のエアーレーション
化を行って揚水するようになる。
As described above, in this example of the apparatus, the contaminated groundwater is aerated at two points in the well pipe and the pumping pipe to pump the water.

【0014】[0014]

【実施例】本発明にあっては、2つの装置が実施例とし
て考えられる。
EXAMPLES In the present invention, two devices are conceivable as examples.

【0015】まず、図1に示した第1の実施例について
説明する。
First, the first embodiment shown in FIG. 1 will be described.

【0016】1は井管で、この井管内には揚水管2に挿
入した一方の送気管3と単独に挿入した他方の送気管4
を設置するが、一方の送気管3の下端部は揚水管2の下
側部付近に達し、他方の送気管4の下端部は後記パッカ
ー5上方部の不飽和帯付近に達する。
Reference numeral 1 denotes a well pipe in which one air feed pipe 3 inserted into the pumping pipe 2 and the other air feed pipe 4 inserted independently.
The lower end of one of the air supply pipes 3 reaches near the lower side of the pumping pipe 2, and the lower end of the other air supply pipe 4 reaches near the unsaturated zone above the packer 5 described later.

【0017】5は地下水面位置の井管1内に取付けたパ
ッカーで、このパッカーによって地下水面下方の飽和帯
(帯水層)aと同上方の不飽和帯(非帯水層)bとを仕
切る。
Reference numeral 5 is a packer mounted in the well 1 at the position of the water table, which is used to create a saturated zone (aquifer) a below the water table and an unsaturated zone (non-aquifer) b above the water table. Partition.

【0018】前記パッカー5の位置によって、井管1に
は地下水を還元注入する上部スクリーン6と地下水を採
取する下部スクリーン7とが設けられている。
Depending on the position of the packer 5, the well pipe 1 is provided with an upper screen 6 for reducing and injecting groundwater and a lower screen 7 for collecting groundwater.

【0019】8は地上に設置したコンプレッサで、この
コンプレッサには前記2本の送気管3,4が連設する。
Reference numeral 8 is a compressor installed on the ground, and the two air supply pipes 3 and 4 are connected to the compressor in series.

【0020】前記コンプレッサ8から送気管3に入った
圧縮空気は、揚水管2の下側部において、前記井管1の
スクリーン7を通過し揚水管2に入った汚染地下水に供
給され、これによって汚染地下水はエアーリフト効果に
よって押し上げられるようになる。
The compressed air that has entered the air supply pipe 3 from the compressor 8 is supplied to the contaminated groundwater that has entered the pumping pipe 2 after passing through the screen 7 of the well pipe 1 at the lower side of the pumping pipe 2. Contaminated groundwater will be pushed up by the airlift effect.

【0021】コンプレッサ8から送気管4に入った圧縮
空気は、井管1の上側部の上部スクリーン6付近におい
て放散し、後記する地上における分離ずみ汚染地下水を
エアーレーション化し、汚染物質を再気散して浄化した
地下水として井管1の上部スクリーン6に還元注入す
る。
The compressed air that has entered the air supply pipe 4 from the compressor 8 is diffused near the upper screen 6 on the upper side of the well pipe 1 to aerate the separated contaminated groundwater on the ground, which will be described later, and re-evaporate the pollutants. Then, it is reduced and injected into the upper screen 6 of the well 1 as purified groundwater.

【0022】9は地上に設置した気液分離槽で、この気
液分離槽の上部には前記揚水管2の上部2’が連設し、
また気液分離槽9の下部には分離ずみ地下水の戻水管1
0を前記井管1上部との間に連設する。
Reference numeral 9 is a gas-liquid separation tank installed on the ground, and an upper part 2'of the pumping pipe 2 is continuously provided on the upper part of the gas-liquid separation tank,
In the lower part of the gas-liquid separation tank 9, the return pipe 1 for separated groundwater
0 is connected continuously with the upper part of the well tube 1.

【0023】前記気液分離槽9において、地下水から分
離した汚染物質を空気とともに排気管11を通って活性
炭による汚染物質吸着器12へ送り、ここで汚染物質を
完全に吸着分離した後、空気を外部に排出する。
In the gas-liquid separation tank 9, the pollutants separated from the groundwater are sent together with the air through the exhaust pipe 11 to the pollutant adsorber 12 using activated carbon, where the pollutants are completely adsorbed and separated, and then the air is removed. Discharge to the outside.

【0024】前記汚染物質吸着器12には、井管1の上
部に連通した内部空気の排気管13を連設する。
An exhaust pipe 13 for internal air, which communicates with the upper portion of the well pipe 1, is connected to the pollutant adsorber 12.

【0025】14は前記汚染物質吸着器12の底部に蓄
まろうとする水分を再び前記気液分離槽9に戻す戻水管
で、前記気液分離槽9からは外部に通ずる排水管15を
設ける。
Reference numeral 14 is a return pipe for returning the water, which is about to be stored in the bottom portion of the pollutant adsorber 12, to the gas-liquid separation tank 9 again, and a drain pipe 15 communicating with the outside from the gas-liquid separation tank 9 is provided.

【0026】次に、図2に示した第2の実施例について
説明する。
Next, the second embodiment shown in FIG. 2 will be described.

【0027】21は井管で、この井管は揚水管22の下
側部に達する送気管23と単独に揚水管22の入口付近
に達する送気管24を設置する。
Reference numeral 21 denotes a well pipe, and this well pipe is provided with an air supply pipe 23 reaching the lower side of the pumping pipe 22 and independently an air supply pipe 24 reaching the vicinity of the inlet of the pumping pipe 22.

【0028】25は前記井管21の下部に設けたスクリ
ーンで、ここから地下水を採取する。
Reference numeral 25 is a screen provided under the well pipe 21 from which ground water is collected.

【0029】26は地上に設置したコンプレッサで、こ
のコンプレッサには前記2本の送気管23,24が連設
する。
Reference numeral 26 is a compressor installed on the ground, to which the two air supply pipes 23 and 24 are connected.

【0030】前記コンプレッサ26から送気管23に入
った圧縮空気は、揚水管22の下側部において、前記井
管21のスクリーン25を通過して揚水管22に入った
汚染地下水に供給され、これによって汚染地下水はエア
ーリフト効果によって押し上げられるようになる。
The compressed air that has entered the air supply pipe 23 from the compressor 26 is supplied to the contaminated groundwater that has entered the pumping pipe 22 after passing through the screen 25 of the well pipe 21 at the lower side of the pumping pipe 22. The contaminated groundwater will be pushed up by the airlift effect.

【0031】コンプレッサ26から送気管24に入った
圧縮空気は、井管21の下側部の揚水管22の下側部付
近に放散し、井管21のスクリーン25から井管1内に
入った汚染地下水に供給され、エアーレーション効果に
よって気液分離が促進される。
The compressed air that has entered the air supply pipe 24 from the compressor 26 diffuses to the lower part of the well pipe 21 near the lower part of the pumping pipe 22, and enters the well pipe 1 from the screen 25 of the well pipe 21. It is supplied to contaminated groundwater, and gas-liquid separation is promoted by the aeration effect.

【0032】27は地上に設置した気液分離槽で、この
気液分離槽の上部には前記揚水管22の上部22’が連
設し、また気液分離槽27の下部には分離ずみ地下水の
戻水管28を前記井管1の上部との間に連設する。
27 is a gas-liquid separation tank installed on the ground. The upper part 22 'of the pumping pipe 22 is connected to the upper part of the gas-liquid separation tank, and the separated groundwater is provided under the gas-liquid separation tank 27. The return water pipe 28 is connected to the upper part of the well pipe 1.

【0033】前記気液分離槽27において、地下水から
分離した汚染物質を空気とともに排気管29を通って活
性炭による汚染物質吸着器30へ送り、ここで汚染物質
を完全に吸着分離した後に空気を外部へ排出する。
In the gas-liquid separation tank 27, the pollutants separated from the groundwater are sent together with the air through the exhaust pipe 29 to the pollutant adsorber 30 using activated carbon, where the pollutants are completely adsorbed and separated, and then the air is exposed to the outside. To discharge.

【0034】前記汚染物質吸着器30には、井管1の上
部に連通した井管内部空気の排気管31を連設する。
The pollutant adsorber 30 is provided with an exhaust pipe 31 for the air inside the well pipe, which communicates with the upper portion of the well pipe 1.

【0035】32は前記汚染物質吸着器30の底部に蓄
まろうとする水分を前記気液分離槽27に戻す戻水管
で、前記気液分離槽27からは外部に通ずる排水管33
を設ける。
Reference numeral 32 is a return pipe for returning the water, which is about to be stored in the bottom of the pollutant adsorber 30, to the gas-liquid separation tank 27, and a drain pipe 33 communicating from the gas-liquid separation tank 27 to the outside.
To provide.

【0036】[0036]

【発明の効果】本発明にあっては、揮発性の汚染物質を
含む地下水の揚水にエアーリフト方式を採用しているか
ら、汚染地下水の揚水の最初の段階において圧縮空気に
よる曝気作用によって汚染物質の気化分離が促進される
ようになり、効率の良好な地下水の浄化処理を実現する
ことができる。
According to the present invention, since the air lift system is adopted for pumping groundwater containing volatile pollutants, pollutants are aerated by compressed air in the first stage of pumping polluted groundwater. The vaporization and separation of the water will be promoted, and efficient groundwater purification treatment can be realized.

【0037】汚染物質を分離浄化した地下水が井管内に
戻され、これが再び飽和帯に達することにより汚染地下
水を稀釈化した状態にして採取することができ、汚染地
下水の浄化のためのサイクルを形成することができるか
ら、効率の高い浄化処理を行うことができるようにな
る。
The groundwater from which the pollutants have been separated and purified is returned to the well pipe and reaches the saturation zone again, whereby the polluted groundwater can be collected in a diluted state and a cycle for purification of the polluted groundwater is formed. Therefore, highly efficient purification processing can be performed.

【0038】また、各種装置は地上部にあるから、井戸
内の構造が簡素化され、その維持管理が容易となり、コ
ストが安価な経済性の高い装置を提供することができ
る。
Further, since the various devices are located on the ground, the structure inside the well is simplified, the maintenance thereof is facilitated, and it is possible to provide a highly economical device at low cost.

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

【図1】本発明の実施のための一つの装置例FIG. 1 is an example of an apparatus for carrying out the present invention.

【図2】本発明の実施のための他の装置例FIG. 2 is another example of a device for implementing the present invention.

【符号の説明】[Explanation of symbols]

1,21 井管 2,22 揚水管 3,23 送気管 4,24 送気管 5 パッカー 6 スクリーン 7 スクリーン 8,26 コンプレッサ 9,27 気液分離槽 10,28 戻水管 11,29 排気管 12,30 汚染物質吸着器 14,32 戻水管 25 スクリーン 1,21 well tube 2,22 Pumping pipe 3,23 Air pipe 4,24 air pipe 5 packers 6 screens 7 screen 8,26 compressor 9,27 gas-liquid separation tank 10,28 Return pipe 11,29 exhaust pipe 12,30 Pollutant adsorber 14,32 Return pipe 25 screen

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】飽和帯と不飽和帯に臨設する付近にそれぞ
れスクリーンを配設した井管と、この井管内に挿入した
揚水管内部の下側部付近まで延設した一方の送気管と、
井管内に不飽和帯に臨設するスクリーン付近まで延設し
た他方の送気管と、この2本の送気管はそれぞれ地上に
設置したコンプレッサに連設し、井管の地下水面位置に
はパッカーを設置し、前記揚水管は地上に設置した気液
分離槽に連設し、この気液分離槽から排気管を汚染物質
吸着器に連設し、前記気液分離槽から戻水管を前記井管
に連通して成る汚染地下水浄化装置。
1. A well pipe having screens respectively disposed near the saturated zone and the unsaturated zone, and one air pipe extending to the lower side of the pumping pipe inserted into the well pipe.
The other air pipe that extends to the vicinity of the screen located in the unsaturated zone near the screen and these two air pipes are connected to a compressor installed on the ground, and a packer is installed at the water table of the well pipe. Then, the pumping pipe is connected to a gas-liquid separation tank installed on the ground, the exhaust pipe is connected to the pollutant adsorber from the gas-liquid separation tank, and the return pipe is connected to the well pipe from the gas-liquid separation tank. A contaminated groundwater purification device that is connected.
【請求項2】飽和帯に臨設する付近にスクリーンを配設
した井管と、この井管内に挿入した揚水管内部の下側部
付近まで延設した一方の送気管と、井管内にスクリーン
付近まで延設した他方の送気管と、この2本の送気管は
それぞれ地上に設置したコンプレッサに連設し、前記揚
水管は地上に設置した気液分離槽に連設し、この気液分
離槽から排気管を汚染物質吸着器に連設し、前記気液分
離槽から戻水管を前記井管に連通して成る汚染地下水浄
化装置。
2. A well pipe having a screen disposed near the saturation zone, one air pipe extending to the lower side inside the pumping pipe inserted into the well pipe, and a portion of the well pipe near the screen. The other air pipe extending up to and to the two air pipes are connected to a compressor installed on the ground, and the pumping pipe is connected to a gas-liquid separation tank installed on the ground. A contaminated groundwater purification device in which an exhaust pipe is connected to a pollutant adsorber, and a return water pipe is connected from the gas-liquid separation tank to the well pipe.
JP22997198A 1998-08-03 1998-08-03 Contaminated groundwater purification equipment Expired - Fee Related JP3373788B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22997198A JP3373788B2 (en) 1998-08-03 1998-08-03 Contaminated groundwater purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22997198A JP3373788B2 (en) 1998-08-03 1998-08-03 Contaminated groundwater purification equipment

Publications (2)

Publication Number Publication Date
JP2000042531A JP2000042531A (en) 2000-02-15
JP3373788B2 true JP3373788B2 (en) 2003-02-04

Family

ID=16900587

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22997198A Expired - Fee Related JP3373788B2 (en) 1998-08-03 1998-08-03 Contaminated groundwater purification equipment

Country Status (1)

Country Link
JP (1) JP3373788B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100495773B1 (en) * 2002-11-08 2005-06-20 한라산업개발 주식회사 Device for recovery of polluted soil and lnapl with floating and skimming pipe system
JP4709010B2 (en) * 2006-01-04 2011-06-22 パナソニック株式会社 Gas station groundwater purification system and purification method
CN110482737A (en) * 2019-08-02 2019-11-22 中科鼎实环境工程有限公司 For the circulation well repair system of Organic Contamination of Groundwater object
CN113788508B (en) * 2021-08-19 2023-09-29 浙江一龙环保科技有限公司 Groundwater circulation restoration device and system

Also Published As

Publication number Publication date
JP2000042531A (en) 2000-02-15

Similar Documents

Publication Publication Date Title
JP2852117B2 (en) Method and apparatus for two-phase vacuum extraction of soil contaminants
US6254310B1 (en) In-well air stripping and adsorption
US5464309A (en) Dual wall multi-extraction tube recovery well
CA2053446C (en) Process and apparatus for groundwater extraction using a high vacuum process
US5358357A (en) Process and apparatus for high vacuum groundwater extraction
US5197541A (en) Apparatus for two phase vacuum extraction of soil contaminants
US5655852A (en) High vacuum extraction of soil contaminants along preferential flow paths
JPH07265898A (en) Method and device for pollutant removal
US5387057A (en) Contaminated ground site remediation system
JP3373788B2 (en) Contaminated groundwater purification equipment
JPH07284753A (en) Method and apparatus for removing underground contaminant
JP4923266B2 (en) Contaminated water treatment equipment
JP2001146767A (en) Well for cleaning ground water, ground water-cleaning device using it, and ground water-cleaning method
JP4375592B2 (en) Soil and groundwater purification methods
JP2943088B2 (en) Underground parking lot with underground exhaust gas treatment device
JP2001029933A (en) Method and apparatus for cleaning polluted soil
JP2005074289A (en) Cleaning method for hardly-gas/water-permeable contaminated soil and system
JP3060130B2 (en) Underground exhaust gas treatment equipment with wastewater treatment function
JP4292921B2 (en) Purification method and system for hardly air permeable and contaminated soil
JP3060140B2 (en) Air purification device by soil
JP2667541B2 (en) On-site purification system for polluted groundwater
CN214571065U (en) Sewage treatment system for underground water circulation well
JPH06254537A (en) Method for purifying underground water and its device
JP2003154356A (en) Pumping aeration type apparatus and method for purifying ground water
JP2002301465A (en) Cleaning system for soil and ground water polluted with volatile organic compound

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081122

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081122

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091122

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101122

Year of fee payment: 8

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111122

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121122

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131122

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees