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JP4091482B2 - Purification method and purification body of contaminated ground by freezing and suction - Google Patents
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JP4091482B2 - Purification method and purification body of contaminated ground by freezing and suction - Google Patents

Purification method and purification body of contaminated ground by freezing and suction Download PDF

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Publication number
JP4091482B2
JP4091482B2 JP2003161672A JP2003161672A JP4091482B2 JP 4091482 B2 JP4091482 B2 JP 4091482B2 JP 2003161672 A JP2003161672 A JP 2003161672A JP 2003161672 A JP2003161672 A JP 2003161672A JP 4091482 B2 JP4091482 B2 JP 4091482B2
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underground
suction
ground
freezing
contaminated
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JP2004358404A (en
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譲 伊藤
雅史 嘉門
和昭 日置
忠明 野村
民征 深石
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Kinjo Rubber Co Ltd
Seiken Co Ltd
Fudo Tetra Corp
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Kinjo Rubber Co Ltd
Seiken Co Ltd
Fudo Tetra Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、油類や揮発性有機化合物などで汚染された汚染地盤の浄化方法及び浄化体に関し、詳しくは汚染物質が原液状態で存在する地下水位以浅の汚染源からの原液の吸引とその周辺の汚染間隙水の吸引を行う汚染地盤の浄化方法及び浄化体に関するものである。
【0002】
【従来の技術】
半導体製造工場などの洗浄工程において多量に使用されるトリクロロエチレン等の揮発性有機化合物は、漏れなどにより土壌又は地下水を汚染する可能性があり、この場合、工場跡地の再利用の障害となったり、地下水の利用が制限されたりする問題がある。トリクロロエチレンなどの高密度非水溶性液体(DNAPL)は、土壌に進入すると地下水位以浅の不飽和帯を浸透して、地下水面との境界で一旦停止する。そして、地下水位以浅の土壌間隙には、水、空気及びDNAPLとが共存する汚染領域が形成される。これはDNAPLが飽和帯への浸透に当たって大きな浸透圧が必要なためである。また、ガソリン、灯油、軽油及び重油などの油類は、密度が水よりも軽いため、地下水面以下に浸透することはなく、不飽和帯の間隙と間隙水を汚染する。
【0003】
地下水位以浅の土壌中に溜まったDNAPLや油類などの汚染物質を積極的に取り除く方法としては、土壌ガス吸引法が一般的である。この方法は、地下水位以浅の不飽和帯に抽出井を設けて、真空ポンプやブロア等の吸引手段で抽出井内の圧力を下げ、井戸内に揮発した物質を地上に回収するものである。しかし、このような方法は、抽出井内の吸引圧により土壌中の間隙が圧縮されたり、吸引圧の及ぶ範囲が制限されたりする。特に抽出井から遠方にある土壌では浄化効率が大きく低下する。すなわち、従来の土壌ガス吸引法では、比較的大きな間隙とその周辺のみが浄化されるものの、その他の領域ではほとんど浄化されないという問題がある。
【0004】
これを解決するものとして、特許文献1の特開平11−169837号公報には、汚染地盤領域を凍結する工程に続き、その後該地盤から土壌内ガスを吸引し汚染蒸気を抽出する汚染地盤の浄化方法が開示されている。しかし、この汚染地盤の浄化方法は、地盤の凍結と解凍により土壌微粒子間に微小な撹乱を起こし、その後土壌中に存在するガス状汚染物質の吸引効果を高めるようにしたものであり、凍結地盤中に液状の汚染物質を残存せしめ、これを吸引、除去するものではない。
【0005】
【特許文献1】
特開平11−169837号公報(請求項1、段落番号0010)
【0006】
【発明が解決しようとする課題】
従って、本発明の目的は、地下水位以浅の土壌中に存在する原液状態の汚染物質及びその周辺の汚染間隙水を効率的に吸引、除去し、処理時間の短縮及び処理コストの低減を図る汚染地盤の浄化方法及び浄化体を提供することにある。
【0007】
【課題を解決するための手段】
かかる実情において、本発明者等は鋭意検討を行なった結果、水とDNAPL原液の凝固点の相違及び油類と水の密度の相違から、地下水位以浅の凍結地盤中においてDNAPLと油類を液状物として存在させることができ、この凍結地盤中の液状物を吸引管などの吸引手段で吸引、除去すれば、極めて容易且つ効率的であり、処理時間の短縮と処理コストの低減が図れること等を見出し、本発明を完成するに至った。
【0011】
すなわち、本発明は、地下水位以浅の土壌中に汚染物質が存在する汚染地盤に適宜のピッチで地中凍結管を、該地中凍結管間に適宜のピッチで地中吸引体を、該地中凍結管近傍に地中注入体をそれぞれ配設する浄化体配設工程と、汚染地盤領域を凍結する凍結工程と、該凍結状態を維持したまま該地中吸引体から液状汚染物質を吸引する原液吸引工程と、汚染地盤領域を解凍する工程と、解凍された汚染地盤領域の残部の汚染物質を前記地中吸引体から空気又は水を供給して前記地中注入体から吸引する汚染物質吸引工程と、解凍された汚染地盤領域の残部の汚染物質を前記地中注入体から空気又は水を供給して前記地中吸引体から吸引する汚染物質吸引工程を行なうことを特徴とする汚染地盤の浄化方法を提供するものである。地下水以浅の融解土壌の飽和度が低い場合、地中吸引体と地中注入体間で空気の供給とガス状汚染物質の吸引を行い、地下水以浅の融解土壌の飽和度が高い場合、地中吸引体と地中注入体間で水の供給と汚染間隙水の吸引を行えば、押出しと吸引の両作用により、浄化効率を一層高めることができる。
【0012】
また、本発明は、地下水位以浅の土壌中に汚染物質が存在する汚染地盤に構築される浄化体であって、適宜のピッチで配設される地中凍結管と、該地中凍結管間に配設され凍結地盤中に存在する液状汚染物質を吸引する地中吸引体と、該地中凍結管近傍に配設され空気又は水を供給する地中注入体とを備え、前記地中吸引体は空気又は水を供給する供給体を兼用し、地中注入体は、汚染物質を吸引する吸引体を兼用する浄化体を提供するものである。また、本発明は、前記地中吸引体及び地中注入体は、吸引管又は柱状ドレーンである前記浄化体を提供するものである。本発明の浄化体によれば、前記浄化方法の発明を確実に実施できる。
【0013】
【発明の実施の形態】
次に、本発明の参考例となる第1の実施の形態における汚染地盤の浄化方法及び浄化体を図1及び図2を参照して説明する。図1は本実施の形態例における浄化体の概略断面図、図2は本実施の形態例における浄化体の概略平面図である。本実施の形態例の浄化体10は、地下水位(W.L.)以浅の土壌中に汚染物質が存在する汚染地盤に構築されるものであって、適宜のピッチで配設される地中凍結管1と、地中凍結管1、1間に適宜のピッチで配設される地中吸引体2を備える。また、地上には、不図示の冷凍機、冷媒循環ポンプ及び配管などの冷凍手段、真空ポンプなどの吸引手段及び汚染物質分解手段などが設置される。
【0014】
本例の浄化体10が構築される汚染地盤4としては、地下水位以浅の地盤中に汚染物質7が存在するものであれば、特に制限されず、その地盤は砂質、粘土層、互層等の自然地盤や埋め立てられた人工地盤などが挙げられる。また、汚染物質7としては、特に制限されず、例えばその密度が水よりも重く、水に溶け難く且つ凝固点が−10℃以下の高密度非水溶性液体(DNAPL)及びその密度が水よりも軽い油類が挙げられる。DNAPLとしては、凝固点が−86℃のトリクロロエチレン、凝固点が−22℃のテトラクロロエチレン、凝固点が−57℃のジクロロエチレン及び凝固点が−97℃のジクロロエタン等が挙げられる。DNAPLは土壌に進入すると地下水位以浅の不飽和帯を浸透して、地下水面との境界71で一旦停止する。そして、地下水位以浅の土壌間隙には、水、空気及びDNAPLとが共存する汚染領域が形成される。これはDNAPLが飽和帯への浸透に当たって大きな浸透圧が必要なためである。また、油類としては、凝固点が−30〜−95℃の種々の成分を含むガソンリン、凝固点が−10〜−30℃の種々の成分を含む灯油などが挙げられる。油類は密度が水よりも軽いため、地下水面以下に浸透することはなく、地下水面との境界71に滞留すると共に間隙水を汚染する。このようなDNAPLや油類の汚染物質は、飽和地盤を氷点以下で且つ汚染物質の凝固点以上の温度で凍結した際、凍結地盤中に液状物で存在する。
【0015】
地中凍結管1は、汚染地盤領域8を凍結させるものであり、汚染地盤領域8にほぼ均等に配設される。地中凍結管1は公知の地中凍結工法で用いるものと同様のものが用いられる。公知の地中凍結工法としては、ブラインと呼ばれる冷媒を冷凍機を使って−20℃〜−30℃に冷却し、これを地盤中に埋設した凍結管1に循環ポンプで送り込んで地盤を冷却する凍結工法が挙げられる。地中凍結管1の本数は、凍結設備能力、凍土温度等により適宜決定される。汚染地盤領域8は、汚染物質の原液7が存在する領域(図2中、実線の範囲)を少なくとも含むものであり、本例では図2中、二点鎖線で囲む領域8を言う。
【0016】
地中吸引体2としては、地上の真空ポンプなどの吸引手段に接続される地中に埋設される構造体であり、例えば吸引管又は柱状ドレーンが挙げられる。本例では側周面に多数の通水穴23が付設された有穴中空管21であり、汚染土壌の各所から汚染物質を吸引し易いようにすると共に、中空部にはヒーター22を設け、凍結工程における水分の凍結による通水穴23の閉塞を防止している。また、通水穴23周りは不図示の不織布などで覆うことが、通水穴23の目詰まりを防止することができる点で好ましい。地中吸引体2として柱状ドレーンを用いる場合も、内部ヒーター22や不織布などを設けることが好ましい。柱状ドレーンとしては、プラスチックボードドレーンが挙げられる。地中吸引体2の配設位置としては、特に制限されないが、図2に示すように、汚染地盤領域8であって且つ凍結管1の間、すなわち隣接する複数の凍結管1のほぼ中間位置に配設させることが、凍結で生じる吐き出し効果で、地中凍結管1から遠ざかる方向へ押しやられた間隙水以外の汚染物質原液を容易に且つ効率的に吸引、除去できる点で好ましい。
【0017】
本第1の実施の形態において、この浄化体10を用いて汚染地盤を浄化する方法を以下に説明する。浄化体配設工程は、事前の地盤調査により、汚染物質及び汚染地盤領域を特定した後、行なわれるものである。すなわち、地下水位以浅の土壌4中に汚染物質7が存在する汚染地盤4に適宜のピッチで地中凍結管1と地中吸引体2を配設する。この際、地上の冷凍機や真空ポンプの設置も行なう。
【0018】
次いで、地下水位以浅の汚染地盤領域8を凍結すると共に該汚染物質を液状物で保持する凍結工程を行う。凍結地盤の温度は、汚染物質の凝固点により決定され、氷点以下で且つ汚染物質の凝固点以上の温度である。汚染地盤領域8をこのような凍結地盤とすれば、該汚染地盤領域は間隙が圧縮されることがない凍結地盤の硬い骨格を形成でき、また凍結地盤中に原液の汚染物質7を液状物として存在させることができる。なお、図1中、二点鎖線で囲まれた範囲5が凍土である。
【0019】
凍結工程においては、地中吸引体2のヒーター22を可動させ、有穴中空管21の通水穴23や中空部が凍結により閉塞しないようにしておく。また、凍結工程において、汚染地盤が飽和度の高い地盤であれば、該地盤の間隙水が徐々に凍結すると、吐き出し現象が生じる。この現象は、凍結の際、間隙水以外の液状物等が地中凍結管1から遠ざかる現象であり、自然界で見られるものである。これにより、汚染物質である原液は自然に地中吸引体2に集まるようになる。この状態で原液吸引工程に入る。なお、地中吸引体2におけるヒーター22の可動は原液吸引工程で可動させてもよい。
【0020】
原液吸引工程は、該凍結状態を維持したまま地中吸引体2から液状汚染物質7を吸引する工程である。地上にある吸引手段を可動させると、地中吸引体2の通水穴23から汚染物質の原液が吸引される。この場合、地中吸引体2周りには汚染物質の原液が集まっており、吸引効率が高められる。図2中、矢印は汚染物質原液の流れを示す。
【0021】
この第1の実施の形態例における汚染地盤の浄化方法及び浄化体によれば、地下水位以浅の不飽和地盤を、氷点以下で且つ汚染物質の凝固点以上の温度で凍結するため、該不飽和地盤は凍土の硬い骨格を形成できる。このため、間隙が圧縮されて吸引力が低下することがないため、1本の吸引管当たりの影響範囲が広くなる。また、不飽和地盤中、間隙水は凍結状態であり汚染物質は液状物として存在させることができるため、汚染物質の吸引回収効率がよい。このため、浄化処理時間の短縮と処理コストの低減が図れる。また、凍結地盤は一時的なものであり、解凍後、2次汚染の心配はない。また、解凍後の地盤中に存在する汚染間隙水及び間隙中の汚染物質は、更に地中吸引体2で吸引除去することができる。
【0022】
次に、本発明の参考例となる第2の実施の形態における汚染地盤の浄化方法及び浄化体を図3及び図4を参照して説明する。図3は本実施の形態例における浄化体の概略断面図、図4は本実施の形態例における浄化体の概略平面図である。本例において、図1及び図2と同一構成要素には同一符号を付して、その説明を省略し異なる点について主に説明する。すなわち、第2の実施の形態における浄化体10aは、第1の実施の形態における浄化体10に対して、地中凍結管1の近傍に地中注入体3を更に配設させた点及び地中注入体3の一端を不図示の地上の空気供給手段に接続した点である。すなわち、前記原液吸引工程において、地中注入体3から空気を凍結地盤中に注入して地中吸引体2から液状汚染物質を吸引する。なお、図3及び図4中、矢印は汚染地下水の流れである。第2の実施の形態における浄化体10aを用いれば、第1の実施の形態における浄化体10と同様の効果を奏する他、液状汚染物質の回収効率が更に向上する。
【0023】
次に、第3の実施の形態における汚染地盤の浄化方法及び浄化体を図5及び図6を参照して説明する。図5は本実施の形態例における浄化体の概略断面図、図6は本実施の形態例における浄化体の概略平面図である。本例において、図1及び図2と同一構成要素には同一符号を付して、その説明を省略し異なる点について主に説明する。すなわち、第3の実施の形態における浄化体10bは、第1の実施の形態における浄化体10に対して、地中凍結管1の近傍に地中注入体3を更に配設させ、これにより、解凍後の融解地盤9中における汚染間隙水及び間隙中の汚染物質の吸引効率を高めるようにしたものである。地中注入体3は第2の実施の形態例で用いたものと同様のものが使用できる。第3の実施の形態例においても、地中凍結管1の近傍とは、第2の実施の形態例の地中注入体と同様の意味である。
【0024】
図5及び図6は、汚染地盤領域の解凍後の状態を示し、原液の周辺の汚染間隙水及び間隙中の汚染物質は解凍後の融解地盤9中に存在している(不図示)。解凍工程としては、特に制限されず、自然放置で解凍し常温とする方法、不図示の地中加熱管で急速加熱する方法又は地中凍結管1に温水を流し解凍する方法などが挙げられる。このうち、地中凍結管1に温水を流し解凍する方法が簡易且つ迅速な解凍が行なえる点で好ましい。汚染物質吸引工程は、例えば融解地盤9の飽和度が高い場合、地中凍結管1の近傍にある地中注入体3を水供給体として使用し、地中吸引体2を汚染間隙水吸引体として使用し、地中注入体3から水を供給すると共に、地中吸引体2から汚染間隙水を吸引する。これにより、循環系の流路が形成され、残部の汚染間隙水を容易且つ効率的に除去できる。なお、地中注入体3は不図示の地上水供給手段に接続されている。図4中、矢印は汚染地下水の流れである。
【0025】
また、融解地盤9の飽和度が低い場合、地中凍結管1の近傍にある地中注入体3を空気供給体として使用し、地中吸引体2を土壌の間隙に存在するガス状汚染物質吸引体として使用し、地中注入体3から空気を供給すると共に、地中吸引体2からガス状汚染物質を吸引する。これにより、循環系の流路が形成され、残部の汚染物質を容易且つ効率的に除去できる。なお、この場合、地中注入体3は不図示の地上空気供給手段に接続される。
【0026】
第3の実施の形態における汚染地盤の浄化方法によれば、地中注入体3から空気又は水を供給し、地中吸引体2から汚染間隙水又は間隙中のガス状汚染物質を吸引するため、押出しと吸引の両作用により、浄化効率を一層高めることができる。特に地中凍結管を暖めながら解凍する場合、該地中凍結管に近接する地盤の開いた間隙から、水や空気を供給できるため、工期が短縮すると共に循環が円滑に行われ浄化効率が向上する。
【0027】
また、第3の実施の形態における汚染地盤の浄化方法の変形例として、地中吸引体2を水供給体又は空気供給体として使用し、地中注入体3を汚染間隙水吸引体又はガス状汚染物質吸引体として使用することもできる。すなわち、地中吸引体2から水を供給すると共に、地中注入体3から汚染間隙水を吸引すれば、同様に循環系の流路が形成され、汚染間隙水を容易且つ効率的に除去できる。この場合、凍結の際、前記吐き出し効果とは逆に、間隙水が地中凍結管1に移動する凍上における水分移動現象を利用できる。この現象は地盤の間隙水が徐々に凍結しアイスレンズと呼ばれる氷層が形成され、更に温度低下が進行すると、未凍結部分から凍結面に向かって水が補給される自然現象であり、汚染間隙水が地中凍結管1に集まり易くなる。従って、解凍後、この集まった汚染間隙水を直ちに地中注入体3で吸引できると共に、更に供給水で押出すため浄化効率が一層向上する。
【0028】
【発明の効果】
本発明の浄化方法によれば、地下水以浅の融解土壌の飽和度が低い場合、地中吸引体と地中注入体間で空気の供給とガス状汚染物質の吸引を行い、地下水以浅の融解土壌の飽和度が高い場合、地中吸引体と地中注入体間で水の供給と汚染間隙水の吸引を行えば、押出しと吸引の両作用により、浄化効率を一層高めることができる。このように、本発明の浄化方法によれば、汚染物質が原液状態、ガス状態及び間隙水に溶解した3態様で存在する地下水位以浅の汚染地盤を確実に浄化修復できる。
また、本発明の浄化体によれば、前記浄化方法の発明を確実に実施できる。
【図面の簡単な説明】
【図1】第1の実施の形態例における浄化体の概略断面図である。
【図2】第1の実施の形態例における浄化体の概略平面図である。
【図3】第2の実施の形態例における浄化体の概略断面図である。
【図4】第2の実施の形態例における浄化体の概略平面図である。
【図5】第3の実施の形態例における浄化体の解凍後の状態を示す概略断面図である。
【図6】第3の実施の形態例における浄化体の概略平面図である。
【符号の説明】
1 地中凍結管
2 地中吸引体
3 地中注入体
4 汚染地盤
5 凍土
7 汚染物質(原液)
8 汚染地盤領域
9 融解地盤
10、10a、10b 浄化体
21、31 有穴中空管
22、32 ヒーター
23、33 通水穴
71 地下水面との境界
W.L. 地下水位
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for purifying contaminated ground contaminated with oils, volatile organic compounds, and the like, and more specifically, the suction of the stock solution from a source of contamination below the groundwater level where the pollutant exists in the stock solution state and the surrounding area. The present invention relates to a purification method and a purification body for contaminated ground that sucks contaminated pore water.
[0002]
[Prior art]
Volatile organic compounds such as trichlorethylene, which are used in large quantities in the cleaning process of semiconductor manufacturing plants, etc., may contaminate the soil or groundwater due to leakage, etc. There is a problem that the use of groundwater is restricted. When a high-density water-insoluble liquid (DNAPL) such as trichlorethylene enters the soil, it penetrates the unsaturated zone shallower than the groundwater level and temporarily stops at the boundary with the groundwater surface. And in the soil gap shallower than the groundwater level, a contaminated area where water, air and DNAPL coexist is formed. This is because DNAPL requires a large osmotic pressure to penetrate into the saturation zone. In addition, oils such as gasoline, kerosene, light oil and heavy oil are lighter in density than water, and therefore do not penetrate below the groundwater surface and contaminate the gaps and pore water in the unsaturated zone.
[0003]
As a method for actively removing contaminants such as DNAPL and oils accumulated in the soil shallower than the groundwater level, a soil gas suction method is generally used. In this method, an extraction well is provided in an unsaturated zone shallower than the groundwater level, and the pressure in the extraction well is reduced by a suction means such as a vacuum pump or a blower, and the material volatilized in the well is recovered on the ground. However, in such a method, the gap in the soil is compressed by the suction pressure in the extraction well, or the range covered by the suction pressure is limited. Especially in the soil far from the extraction well, the purification efficiency is greatly reduced. That is, the conventional soil gas suction method has a problem that although only a relatively large gap and its periphery are purified, it is hardly purified in other regions.
[0004]
As a solution to this problem, Japanese Patent Application Laid-Open No. 11-169837 of Patent Document 1 discloses a purification of contaminated ground that is followed by a step of freezing a contaminated ground area, and then sucking in soil gas from the ground and extracting contaminated vapor. A method is disclosed. However, this method of remediation of contaminated ground is to cause minute disturbance between the soil fine particles by freezing and thawing of the ground, and then to enhance the suction effect of gaseous pollutants present in the soil. It does not leave liquid contaminants in the interior, which are sucked and removed.
[0005]
[Patent Document 1]
JP-A-11-169837 (Claim 1, paragraph number 0010)
[0006]
[Problems to be solved by the invention]
Therefore, an object of the present invention is to efficiently suck and remove the pollutant in the raw liquid state existing in the soil shallower than the groundwater level and the contaminated pore water around it, thereby reducing the processing time and the processing cost. It is providing the purification method and purification body of a ground.
[0007]
[Means for Solving the Problems]
In such a situation, the present inventors have conducted intensive studies, and as a result, due to the difference in the freezing point of water and DNAPL stock solution and the difference in the density of oils and water, the DNAPL and oils are liquid substances in the frozen ground below the groundwater level. If the liquid material in the frozen ground is sucked and removed by suction means such as a suction tube, it is extremely easy and efficient, and the processing time and processing cost can be reduced. The headline and the present invention were completed.
[0011]
That is, the present invention is a ground freeze tube at an appropriate pitch in Contaminated Land the presence of contaminants in the soil of the ground water level shallower than the ground attractant in an appropriate pitch between during該地cryotubes, 該地 A purification body disposing step for disposing an underground injection body in the vicinity of the intermediate freezing pipe, a freezing step for freezing the contaminated ground area, and a liquid pollutant is sucked from the underground suction body while maintaining the frozen state. Concentrating material suction step , step of thawing the contaminated ground region, and contaminant suction of sucking the remaining contaminants of the thawed contaminated ground region from the underground injection body by supplying air or water from the underground suction body And a pollutant suction step of sucking the remaining contaminants of the thawed contaminated ground area from the underground suction body by supplying air or water from the underground injection body . A purification method is provided. When the saturation level of the melted soil below groundwater is low, air is supplied and gaseous pollutants are sucked between the underground suction body and the underground injection body. If the supply of water and the suction of contaminated pore water are performed between the suction body and the underground injection body, the purification efficiency can be further enhanced by the action of both extrusion and suction.
[0012]
Further, the present invention is a purification body constructed in a contaminated ground where contaminants exist in soil shallower than the groundwater level, and between the underground freezing pipe disposed at an appropriate pitch and the underground freezing pipe comprising a ground suction member is arranged to suck the liquid contaminants present frozen in the ground, and a ground injectors for supplying air or water disposed near freezing tube該地 to the ground suction the body also serves as a supplying member for supplying the air or water, underground injection member is to provide a purifier you also serves as a suction member for sucking contaminants. Moreover, this invention provides the said purification body whose said underground suction body and underground injection body are a suction pipe or a columnar drain. According to the purification body of the present invention, the invention of the purification method can be reliably implemented.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Next, the purification method and purification body of the contaminated ground in the first embodiment as a reference example of the present invention will be described with reference to FIGS. 1 and 2. FIG. 1 is a schematic cross-sectional view of a purification body in the present embodiment, and FIG. 2 is a schematic plan view of the purification body in the present embodiment. The purification body 10 according to the present embodiment is constructed on a contaminated ground in which contaminants exist in soil shallower than the groundwater level (W.L.), and is disposed in an appropriate pitch. The freezing pipe 1 and the underground suction body 2 disposed at an appropriate pitch between the underground freezing pipes 1 and 1 are provided. On the ground, a refrigerator (not shown), a refrigeration means such as a refrigerant circulation pump and piping, a suction means such as a vacuum pump, and a pollutant decomposition means are installed.
[0014]
The contaminated ground 4 on which the purification body 10 of the present example is constructed is not particularly limited as long as the contaminant 7 exists in the ground shallower than the groundwater level, and the ground is sandy, clay layer, alternating layer, etc. Natural ground or reclaimed artificial ground. Further, the contaminant 7 is not particularly limited. For example, the density is heavier than water, difficult to dissolve in water, and has a freezing point of −10 ° C. or lower, and the density thereof is higher than that of water. Light oils are listed. Examples of DNAPL include trichloroethylene having a freezing point of −86 ° C., tetrachloroethylene having a freezing point of −22 ° C., dichloroethylene having a freezing point of −57 ° C., and dichloroethane having a freezing point of −97 ° C. When DNAPL enters the soil, it penetrates the unsaturated zone below the groundwater level and stops once at the boundary 71 with the groundwater surface. And in the soil gap shallower than the groundwater level, a contaminated area where water, air and DNAPL coexist is formed. This is because DNAPL requires a large osmotic pressure to penetrate into the saturation zone. Examples of oils include gason phosphorus containing various components having a freezing point of −30 to −95 ° C., and kerosene containing various components having a freezing point of −10 to −30 ° C. Since oils are lighter in density than water, they do not penetrate below the groundwater surface, stay at the boundary 71 with the groundwater surface and contaminate pore water. Such DNAPL and oil pollutants are present in liquid form in the frozen ground when the saturated ground is frozen at a temperature below the freezing point and above the freezing point of the pollutant.
[0015]
The underground freezing pipe 1 freezes the contaminated ground region 8 and is disposed almost uniformly in the contaminated ground region 8. The underground freezing tube 1 is the same as that used in a known underground freezing method. As a known underground freezing method, a refrigerant called brine is cooled to −20 ° C. to −30 ° C. using a refrigerator, and this is sent to the freezing pipe 1 embedded in the ground with a circulation pump to cool the ground. Freezing method is mentioned. The number of underground freezing pipes 1 is appropriately determined according to freezing equipment capacity, frozen soil temperature, and the like. The contaminated ground region 8 includes at least a region (range of solid line in FIG. 2) where the stock solution 7 of contaminant is present, and in this example, refers to a region 8 surrounded by a two-dot chain line in FIG.
[0016]
The underground suction body 2 is a structure embedded in the ground connected to suction means such as a vacuum pump on the ground, and examples thereof include a suction pipe or a columnar drain. In this example, it is a perforated hollow tube 21 provided with a large number of water passage holes 23 on the side peripheral surface, and it is easy to suck contaminants from various places of the contaminated soil, and a heater 22 is provided in the hollow portion. Further, the water passage hole 23 is prevented from being blocked by freezing of water in the freezing step. Further, it is preferable that the periphery of the water passage hole 23 is covered with a non-illustrated nonwoven fabric or the like because clogging of the water passage hole 23 can be prevented. Also when a columnar drain is used as the underground suction body 2, it is preferable to provide an internal heater 22 or a nonwoven fabric. An example of the columnar drain is a plastic board drain. The arrangement position of the underground suction body 2 is not particularly limited. However, as shown in FIG. 2, as shown in FIG. 2, it is the contaminated ground region 8 and between the freezing pipes 1, that is, an almost intermediate position between the adjacent freezing pipes 1. It is preferable to dispose them in terms of the discharge effect caused by freezing, because the pollutant stock solution other than pore water pushed away from the underground freezing tube 1 can be sucked and removed easily and efficiently.
[0017]
In the first embodiment, a method for purifying the contaminated ground using the purification body 10 will be described below. A purification body arrangement | positioning process is performed after specifying a pollutant and a contamination ground area | region by a prior ground investigation. That is, the underground freezing pipe 1 and the underground suction body 2 are arranged at an appropriate pitch on the contaminated ground 4 where the contaminant 7 exists in the soil 4 shallower than the groundwater level. At this time, a ground refrigerator and a vacuum pump are also installed.
[0018]
Next, a freezing process is performed in which the contaminated ground region 8 shallower than the groundwater level is frozen and the pollutant is held in liquid form. The temperature of the frozen ground is determined by the freezing point of the pollutant, and is a temperature below the freezing point and above the freezing point of the pollutant. If the contaminated ground region 8 is such a frozen ground, the contaminated ground region can form a hard skeleton of the frozen ground in which the gap is not compressed, and the raw contaminant 7 is converted into a liquid matter in the frozen ground. Can exist. In FIG. 1, a range 5 surrounded by a two-dot chain line is frozen soil.
[0019]
In the freezing step, the heater 22 of the underground suction body 2 is moved so that the water passage hole 23 and the hollow portion of the hollow hollow tube 21 are not blocked by freezing. Further, in the freezing process, if the contaminated ground is a highly saturated ground, the discharge phenomenon occurs when the pore water in the ground is gradually frozen. This phenomenon is a phenomenon in which liquid substances other than pore water move away from the underground freezing pipe 1 during freezing and are found in nature. Thereby, the undiluted solution which is a pollutant naturally gathers in the underground suction body 2. In this state, the stock solution suction process is started. The heater 22 in the underground suction body 2 may be moved in the stock solution suction step.
[0020]
The stock solution suction step is a step of sucking the liquid contaminant 7 from the underground suction body 2 while maintaining the frozen state. When the suction means on the ground is moved, the stock solution of the pollutant is sucked from the water passage hole 23 of the underground suction body 2. In this case, a stock solution of contaminants is collected around the underground suction body 2 and the suction efficiency is improved. In FIG. 2, the arrows indicate the flow of the pollutant concentrate.
[0021]
According to the contaminated ground purification method and purification body in the first embodiment, the unsaturated ground shallow below the groundwater level is frozen at a temperature below the freezing point and above the freezing point of the pollutant. Can form a hard skeleton of frozen soil. For this reason, since the gap is not compressed and the suction force is not reduced, the range of influence per suction pipe is widened. Further, in the unsaturated ground, the pore water is in a frozen state, and the pollutant can be present as a liquid, so that the efficiency of sucking and collecting the pollutant is good. For this reason, the purification processing time can be shortened and the processing cost can be reduced. Also, the frozen ground is temporary and there is no concern of secondary contamination after thawing. Further, the contaminated pore water existing in the ground after thawing and the contaminant in the gap can be further removed by suction with the underground suction body 2.
[0022]
Next, a contaminated ground purification method and purification body according to a second embodiment, which is a reference example of the present invention, will be described with reference to FIGS. FIG. 3 is a schematic sectional view of the purification body in the present embodiment, and FIG. 4 is a schematic plan view of the purification body in the present embodiment. In this example, the same components as those in FIGS. 1 and 2 are denoted by the same reference numerals, and the description thereof will be omitted, and different points will be mainly described. That is, the purifying body 10a in the second embodiment is different from the purifying body 10 in the first embodiment in that the underground injection body 3 is further disposed in the vicinity of the underground freezing pipe 1 and the ground. One end of the medium injection body 3 is connected to a ground air supply means (not shown). That is, in the stock solution suction step, air is injected from the underground injection body 3 into the frozen ground, and the liquid contaminant is sucked from the underground suction body 2. In addition, in FIG.3 and FIG.4, the arrow is a flow of contaminated groundwater. If the purification body 10a in 2nd Embodiment is used, there exists an effect similar to the purification body 10 in 1st Embodiment, and the collection | recovery efficiency of a liquid contaminant will further improve.
[0023]
Next, the contaminated ground purification method and purification body in the third embodiment will be described with reference to FIGS. FIG. 5 is a schematic cross-sectional view of the purification body in the present embodiment, and FIG. 6 is a schematic plan view of the purification body in the present embodiment. In this example, the same components as those in FIGS. 1 and 2 are denoted by the same reference numerals, and the description thereof will be omitted, and different points will be mainly described. That is, the purifying body 10b in the third embodiment further disposes the underground injection body 3 in the vicinity of the underground freezing pipe 1 with respect to the purifying body 10 in the first embodiment. The suction efficiency of the contaminated pore water and the contaminant in the gap in the melted ground 9 after thawing is increased. The underground injection body 3 can be the same as that used in the second embodiment. Also in the third embodiment, the vicinity of the underground freezing tube 1 has the same meaning as the underground injection body of the second embodiment.
[0024]
5 and 6 show the state after the thawing of the contaminated ground area, and the contaminated pore water around the undiluted solution and the contaminants in the gap are present in the melted ground 9 after thawing (not shown). The thawing step is not particularly limited, and includes a method of thawing to stand at room temperature by natural standing, a method of rapid heating with a ground heating tube (not shown), or a method of thawing by flowing warm water into the underground freezing tube 1. Among these, the method of pouring warm water into the underground freezing tube 1 and thawing is preferable in that simple and quick thawing can be performed. In the pollutant sucking step, for example, when the melting ground 9 is highly saturated, the underground injection body 3 in the vicinity of the underground freezing pipe 1 is used as a water supply body, and the underground suction body 2 is used as the contaminated pore water suction body. In addition to supplying water from the underground injection body 3, the contaminated pore water is sucked from the underground suction body 2. Thereby, a flow path of the circulation system is formed, and the remaining contaminated pore water can be removed easily and efficiently. The underground injection body 3 is connected to a ground water supply means (not shown). In FIG. 4, arrows indicate the flow of contaminated groundwater.
[0025]
Further, when the degree of saturation of the melted ground 9 is low, the underground injection body 3 in the vicinity of the underground freezing pipe 1 is used as an air supply body, and the underground suction body 2 is a gaseous contaminant present in the soil gap. Used as a suction body, air is supplied from the underground injection body 3 and gaseous contaminants are suctioned from the underground suction body 2. Thereby, a circulation channel is formed, and the remaining contaminants can be removed easily and efficiently. In this case, the underground injection body 3 is connected to a ground air supply means (not shown).
[0026]
According to the method for purifying contaminated ground in the third embodiment, air or water is supplied from the underground injection body 3 and the contaminated pore water or gaseous contaminants in the gap is sucked from the underground suction body 2. The purification efficiency can be further enhanced by the action of both extrusion and suction. Especially when thawing while warming the underground freezing pipe, water and air can be supplied from the open gap in the ground close to the underground freezing pipe, shortening the construction period and smoothing the circulation, improving the purification efficiency To do.
[0027]
Further, as a modified example of the contaminated ground purification method in the third embodiment, the underground suction body 2 is used as a water supply body or an air supply body, and the underground injection body 3 is used as a contaminated pore water suction body or a gaseous state. It can also be used as a contaminant suction body. That is, if water is supplied from the underground suction body 2 and the contaminated pore water is sucked from the underground injection body 3, a circulation channel is similarly formed, and the contaminated pore water can be easily and efficiently removed. . In this case, in the case of freezing, the water movement phenomenon on freezing where pore water moves to the underground freezing pipe 1 can be used contrary to the discharge effect. This phenomenon is a natural phenomenon in which the pore water in the ground gradually freezes to form an ice layer called an ice lens, and when the temperature further decreases, water is replenished from the unfrozen part toward the frozen surface. Water easily collects in the underground freezing pipe 1. Therefore, after the thawing, the collected contaminated pore water can be immediately sucked by the underground injecting body 3, and further the purification efficiency is further improved because it is pushed out by the supply water.
[0028]
【The invention's effect】
In accordance with the purification method of the present invention, if a low saturation melting soil groundwater shallower, subjected to suction of the feed gaseous pollutants in the air between the ground attractant and ground injectors, melting of ground water shallower When the degree of saturation of the soil is high, the purification efficiency can be further enhanced by both the extrusion and suction actions if water is supplied and the contaminated pore water is sucked between the underground suction body and the underground injection body. As described above, according to the purification method of the present invention, it is possible to reliably purify and repair the contaminated ground below the groundwater level, which is present in three modes in which the contaminant is dissolved in the raw solution state, the gas state, and the pore water.
Moreover, according to the purification body of this invention, invention of the said purification method can be implemented reliably.
[Brief description of the drawings]
FIG. 1 is a schematic cross-sectional view of a purification body in a first embodiment.
FIG. 2 is a schematic plan view of a purification body in the first embodiment.
FIG. 3 is a schematic cross-sectional view of a purification body in a second embodiment.
FIG. 4 is a schematic plan view of a purification body in a second embodiment.
FIG. 5 is a schematic cross-sectional view showing a state after the thawing of the purifier in the third embodiment.
FIG. 6 is a schematic plan view of a purification body in a third embodiment.
[Explanation of symbols]
1 Underground freezing pipe 2 Underground suction body 3 Underground injection body 4 Contaminated ground 5 Frozen soil 7 Contaminant (stock solution)
8 Contaminated ground area 9 Melted ground 10, 10a, 10b Purified body 21, 31 Perforated hollow tube 22, 32 Heater 23, 33 Water passage hole 71 Boundary with groundwater surface W.L. Groundwater level

Claims (3)

地下水位以浅の土壌中に汚染物質が存在する汚染地盤に適宜のピッチで地中凍結管を、該地中凍結管間に適宜のピッチで地中吸引体を、該地中凍結管近傍に地中注入体をそれぞれ配設する浄化体配設工程と、汚染地盤領域を凍結する凍結工程と、該凍結状態を維持したまま該地中吸引体から液状汚染物質を吸引する原液吸引工程と、汚染地盤領域を解凍する工程と、解凍された汚染地盤領域の残部の汚染物質を前記地中吸引体から空気又は水を供給して前記地中注入体から吸引する汚染物質吸引工程と、解凍された汚染地盤領域の残部の汚染物質を前記地中注入体から空気又は水を供給して前記地中吸引体から吸引する汚染物質吸引工程を行なうことを特徴とする汚染地盤の浄化方法。Underground freezing pipes at an appropriate pitch on the contaminated ground where contaminants exist in the soil shallower than the groundwater level , underground suction bodies at an appropriate pitch between the underground freezing pipes , and ground in the vicinity of the underground freezing pipe A purification body disposing step for disposing a medium injection body, a freezing step for freezing the contaminated ground area, a stock solution aspirating step for sucking liquid contaminants from the underground suction body while maintaining the frozen state, and contamination A step of thawing the ground region, a contaminant suction step of supplying air or water from the ground suction body and sucking the remaining contaminants of the thawed contaminated ground region from the ground injection body, and A method for purifying contaminated ground, comprising performing a pollutant suction step of supplying air or water from the underground injecting body and sucking the remaining contaminants in the contaminated ground area from the underground suction body . 地下水位以浅の土壌中に汚染物質が存在する汚染地盤に構築される浄化体であって、適宜のピッチで配設される地中凍結管と、該地中凍結管間に配設され凍結地盤中に存在する液状汚染物質を吸引する地中吸引体と、該地中凍結管近傍に配設され空気又は水を供給する地中注入体とを備え、前記地中吸引体は空気又は水を供給する供給体を兼用し、地中注入体は、汚染物質を吸引する吸引体を兼用することを特徴とする浄化体。A purification body constructed on a contaminated ground in which contaminants exist in soil shallower than the groundwater level, and an underground freezing pipe disposed at an appropriate pitch, and a frozen ground disposed between the underground freezing pipes An underground suction body for sucking liquid contaminants present therein, and an underground injection body that is disposed in the vicinity of the underground freezing pipe and supplies air or water. The underground suction body receives air or water. also serves as a supplier for supplying, underground injection body purifier characterized that you alternate the suction body for sucking contaminants. 前記地中吸引体及び地中注入体は、吸引管又は柱状ドレーンであることを特徴とする請求項記載の浄化体。The purifying body according to claim 2, wherein the underground suction body and the underground injection body are suction pipes or columnar drains.
JP2003161672A 2003-06-06 2003-06-06 Purification method and purification body of contaminated ground by freezing and suction Expired - Lifetime JP4091482B2 (en)

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JP4098653B2 (en) * 2003-03-28 2008-06-11 譲 伊藤 Purification method and purification body of contaminated ground by freezing and suction

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