JP2003033756A - Decontamination method for hardly water-permeable ground - Google Patents

Decontamination method for hardly water-permeable ground

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Publication number
JP2003033756A
JP2003033756A JP2001222536A JP2001222536A JP2003033756A JP 2003033756 A JP2003033756 A JP 2003033756A JP 2001222536 A JP2001222536 A JP 2001222536A JP 2001222536 A JP2001222536 A JP 2001222536A JP 2003033756 A JP2003033756 A JP 2003033756A
Authority
JP
Japan
Prior art keywords
water
ground
permeable
contaminated
well
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.)
Granted
Application number
JP2001222536A
Other languages
Japanese (ja)
Other versions
JP4713777B2 (en
Inventor
Takeshi Nakazawa
武志 仲沢
Toshihito Kondo
敏仁 近藤
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.)
Fujita Corp
Original Assignee
Fujita Corp
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Filing date
Publication date
Application filed by Fujita Corp filed Critical Fujita Corp
Priority to JP2001222536A priority Critical patent/JP4713777B2/en
Publication of JP2003033756A publication Critical patent/JP2003033756A/en
Application granted granted Critical
Publication of JP4713777B2 publication Critical patent/JP4713777B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a decontamination technology useful for remediation of a hardly water-permeable ground in a deep layer which is not sufficiently dealt with by a method of pumping up an underground water or a replacement method. SOLUTION: A suction well 1 that reaches a contaminated area A in the hardly water-permeability ground G2 or penetrates there through is excavated. Then, a plurality of wells 2 for water supply are excavated in such a way that they surround the periphery of the contaminated area A in the ground G2. The water W containing a contaminant decomposing or decomposition promotion agent is supplied to the well 2 for water supply. At the same time, vacuum suction is performed in the suction well 1 while sealing the portion thereof at which the ground G2 is positioned. Thereby, water in the ground G2 is made to flow forcibly.

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、汚染地盤の浄化方
法に関するものであり、特に、透水係数の低い難透水地
盤の浄化に有効な方法を提供するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning contaminated ground, and more particularly, it provides a method effective for cleaning poorly permeable ground having a low hydraulic conductivity.

【0002】[0002]

【従来の技術】地盤の汚染は、地中に混入した廃棄物等
の汚染源から溶出した汚染物質が地下水に拡散すること
によって生じる。そして、透水係数が10−2〜10
−4cm/秒程度の、比較的地下水の流速が早い砂質土か
らなる易透水性地盤の浄化方法としては、汚染源の周囲
に所要数の井戸を掘削して、汚染された地下水をポンプ
で汲み上げる方法が有効である。また、土の透水係数は
シルト分や粘土分が多いほど小さくなって地下水流が極
めて緩慢となるため、汚染源がこのような難透水性地盤
にある場合は、汚染源及びその周辺地盤を掘削撤去して
良質土により埋め戻すといった置換法が採用されてい
る。
2. Description of the Related Art Ground pollution is caused by diffusion of pollutants eluted from pollution sources such as waste mixed in the ground into groundwater. And the water permeability is 10 −2 to 10
-4 cm / sec. As a method for cleaning easily permeable soil consisting of sandy soil with a relatively high groundwater flow rate, a required number of wells are drilled around the pollution source and the contaminated groundwater is pumped. The pumping method is effective. In addition, since the permeability of soil decreases as the amount of silt and clay increases, the groundwater flow becomes extremely slow.If the pollution source is on such a poorly permeable ground, excavate and remove the pollution source and the surrounding ground. The replacement method of backfilling with high quality soil is adopted.

【0003】ところで近年は、従来不透水層と考えられ
ていた、深度の深いところにある沖積粘土層又は洪積粘
土層からなる地層(例えば深度が10m程度、透水係数
が10−4〜10−5cm/秒程度)でも、トリクロロエ
チレンやテトラクロロエチレンのようなVOC(有機塩
素化合物)等による汚染が確認されるようになり、ま
た、このような難透水性地盤を貫通した汚染分布の存在
も把握されている。これは、トリクロロエチレン等、V
OCは比重が大きいため、地表付近から入り込んでも深
層の難透水性地盤まで徐々に地中を落下するからである
と考えられ、このため、表層付近の易透水性地盤より
も、深層の難透水性地盤に、濃度の高い汚染領域が存在
することがある。
By the way, in recent years, a stratum composed of an alluvial clay layer or a diluvial clay layer, which has been conventionally considered as an impermeable layer, has a deep depth (for example, a depth of about 10 m and a permeability coefficient of 10 −4 to 10 −). 5 cm / sec), contamination by VOC (organic chlorine compounds) such as trichlorethylene and tetrachloroethylene has been confirmed, and the existence of such a contamination distribution that penetrates the poorly permeable ground is also understood. ing. This is trichlorethylene, etc.
It is considered that OC has a large specific gravity, so even if it enters from near the surface, it gradually falls into the deep water-impermeable soil. Highly contaminated areas may exist on the soil.

【0004】ところが、このような難透水性地盤は、上
述のように、地下水流が極めて緩慢であるため、地下水
の汲み上げによる方法では、汲み上げられる地下水の殆
どは砂質土の地盤からのものであるため、難透水性地盤
中の汚染物質を除去することは事実上困難である。
However, since the groundwater flow in such a poorly permeable ground is extremely slow as described above, most of the groundwater pumped by the groundwater pumping method is from the ground of sandy soil. Therefore, it is practically difficult to remove pollutants in the hardly permeable ground.

【0005】また、汚染源及びその周辺地盤を掘削撤去
して良質土により埋め戻す方法は、汚染領域が地中の比
較的浅い位置にある場合には有効な手段であるが、深い
位置にある場合はこのような工法の採用は現実的ではな
い。つまり、汚染領域が深いほど、これを掘削するに
は、掘削量が膨大なものとなるだけでなく、浄化対象で
はない地盤区域の掘削量が多く、極めて効率が悪いから
である。したがって、地下水の汲み上げや置換といった
従来工法だけでは、上述のような難透水性地盤に吸着し
ているVOCの除去には十分に対応することができず、
難透水性地盤に対する有効な汚染浄化技術が求められて
いる。
The method of excavating and removing the pollutant source and the surrounding ground and backfilling with good quality soil is an effective means when the polluted area is at a relatively shallow position in the ground, but when it is at a deep position. It is not realistic to adopt such a construction method. That is, the deeper the contaminated region is, the more excavation amount is required to excavate the contaminated region, and the greater the excavation amount is in the ground area that is not the purification target, which is extremely inefficient. Therefore, conventional methods such as pumping and replacing groundwater cannot sufficiently remove VOCs adsorbed on the above-mentioned impervious soil,
There is a demand for effective pollution control technology for poorly permeable ground.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記のよう
な問題に鑑みてなされたもので、その技術的課題は、地
下水汲み上げや置換法では十分に対応できない深層の難
透水性地盤の汚染修復に有効な汚染浄化技術を提供する
ことにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above problems, and its technical problem is to contaminate deep-layer hardly permeable ground that cannot be sufficiently dealt with by groundwater pumping or replacement methods. It is to provide a pollution purification technology effective for restoration.

【0007】[0007]

【課題を解決するための手段】上述した技術的課題は、
本発明によって有効に解決することができる。すなわち
請求項1の発明に係る難透水性地盤の浄化方法は、難透
水性地盤内へ達し又は貫通する所要数の吸引用井戸を掘
削し、前記難透水性地盤内へ達し又は貫通する所要数の
給水用井戸を前記吸引用井戸との間に前記難透水性地盤
内の汚染領域が存在するように掘削し、前記給水用井戸
に汚染物質分解剤又は汚染物質分解促進剤を含有させた
水を供給すると共に、前記吸引用井戸における前記汚染
領域に位置する部分を密閉して真空吸引することによっ
て、前記難透水性地盤内の水を強制流動させるものであ
る。
The above-mentioned technical problems are as follows.
The present invention can effectively solve the problem. That is, the method for purifying a poorly water-permeable ground according to the invention of claim 1 excavates a required number of suction wells that reach or penetrate into the poorly-permeable ground, and reach the required number of holes to reach or penetrate the hardly-permeable ground. The water supply well is excavated so that a contaminated region in the hardly permeable ground exists between the water supply well and the water supply well containing a pollutant decomposing agent or a pollutant decomposition promoting agent. Is supplied, and the portion of the suction well located in the contaminated region is hermetically sealed and vacuum-sucked to forcefully flow the water in the hardly water-permeable ground.

【0008】請求項2の発明に係る難透水性地盤の浄化
方法は、請求項1における一層好ましい方法として、吸
引用井戸は、汚染領域へ達し又は貫通するように掘削
し、給水用井戸は、前記汚染領域の周囲を取り囲むよう
に掘削するものである。
In the method for cleaning a poorly permeable ground according to the second aspect of the present invention, as a more preferable method in the first aspect, the suction well is excavated so as to reach or penetrate the contaminated region, and the water supply well is The excavation is performed so as to surround the contaminated area.

【0009】請求項3の発明に係る難透水性地盤の浄化
方法は、難透水性地盤の汚染領域内へ達し又は貫通する
給水用井戸を掘削すると共にこの給水用井戸に第一の電
極体を挿入し、前記難透水性地盤内へ達し又は貫通する
所要数の第二の電極体を前記吸引用井戸との間に前記難
透水性地盤内の汚染領域が存在するように挿入し、前記
給水用井戸に汚染物質分解剤又は汚染物質分解促進剤を
含有させた水を供給し、前記第一の電極体を直流電源の
陽極側に接続すると共に、前記第二の電極体を直流電源
の陰極側に接続して両電極間に直流電圧を印加すること
によって、前記難透水性地盤内の水を強制流動させるも
のである。
According to the third aspect of the present invention, there is provided a method for cleaning a poorly water-permeable ground, in which a water supply well reaching or penetrating into a contaminated area of the poorly water-permeable ground is excavated and a first electrode body is provided in the water supply well. Insert, insert a required number of second electrode body reaching or penetrating into the water-impermeable soil so that there is a contaminated area in the water-impermeable soil between the suction well and the water supply Water containing a pollutant decomposer or a pollutant decomposition accelerator is supplied to the well, and the first electrode body is connected to the anode side of the DC power source, and the second electrode body is connected to the cathode of the DC power source. It is connected to the side and a DC voltage is applied between both electrodes to forcibly flow the water in the hardly water-permeable ground.

【0010】請求項4の発明に係る難透水性地盤の浄化
方法は、請求項3における一層好ましい方法として、第
一の電極体が挿入される給水用井戸及び第二の電極体の
うちの一方を、汚染領域へ達し又は貫通するように設
け、他方を、前記汚染領域の周囲を取り囲むように設け
る。
According to a fourth aspect of the present invention, there is provided a method for cleaning a poorly water-permeable ground as a more preferable method according to the third aspect, wherein one of a water supply well into which the first electrode body is inserted and a second electrode body. Is provided so as to reach or penetrate the contaminated area, and the other is provided so as to surround the perimeter of the contaminated area.

【0011】請求項5の発明に係る難透水性地盤の浄化
方法は、請求項1乃至4のいずれかの発明において、汚
染物質分解剤が、鉄コロイド、過マンガン酸カリウム及
び安定化二酸化塩素等から選択されるVOC分解剤から
なるものである。このVOC分解剤は、還元的脱塩素反
応によって、VOC(有機塩素化合物)を直接分解する
ものである。
According to the fifth aspect of the present invention, there is provided a method for cleaning a poorly water-permeable ground according to any one of the first to fourth aspects, in which the pollutant decomposing agent is iron colloid, potassium permanganate, stabilized chlorine dioxide, or the like. From a VOC decomposer selected from This VOC decomposing agent directly decomposes VOC (organic chlorine compound) by a reductive dechlorination reaction.

【0012】請求項6の発明に係る難透水性地盤の浄化
方法は、請求項1乃至4のいずれかの発明において、汚
染物質分解促進剤が、エタノール、メタノール及び廃糖
密等から選択されるVOC分解促進剤からなるものであ
る。このVOC分解促進剤は、VOCを分解する能力を
有する微生物の活動を活発にし、これによって、微生物
によるVOCの分解を促すものである。
According to a sixth aspect of the present invention, there is provided a method for cleaning a poorly water-permeable ground according to any one of the first to fourth aspects, wherein the pollutant decomposition accelerator is selected from ethanol, methanol and waste sugar condensate. It is composed of a VOC decomposition accelerator. This VOC decomposition promoter activates the activity of the microorganism having the ability to decompose VOC, thereby promoting the decomposition of VOC by the microorganism.

【0013】なお、本書で言う難透水性地盤とは、透水
係数が10−4〜10−5cm/秒程度の地盤である。
The term "hardly permeable ground" as used herein means a ground having a water permeability coefficient of about 10 -4 to 10 -5 cm / sec.

【0014】[0014]

【発明の実施の形態】図1は、本発明に係る難透水性地
盤の浄化方法の好ましい第一の実施の形態を示す地盤の
鉛直断面図、図2は本形態における井戸の平面配置を示
す図で、図1における参照符号G1は表層近くにある透
水性の比較的高い(例えば10−4cm/秒程度以上)の
砂質土等からなる易透水性地盤、参照符号G2は、この
易透水性地盤G1より下層の、例えば深度が10m程度
の深い層にあって、沖積粘土層又は洪積粘土層からなる
難透水性地盤、参照符号Aは、この難透水性地盤G2に
おける汚染領域である。
1 is a vertical cross-sectional view of the ground showing a first preferred embodiment of the method for cleaning a poorly permeable ground according to the present invention, and FIG. 2 shows a plane arrangement of wells in the present embodiment. In the figure, reference numeral G1 in FIG. 1 indicates an easily permeable ground made of sandy soil having relatively high water permeability (for example, about 10 −4 cm / sec or more) near the surface layer, and reference numeral G2 indicates this easy permeability. Below the permeable ground G1, for example, in a deep layer with a depth of about 10 m, a hardly permeable ground consisting of alluvial clay layer or diluvial clay layer, reference symbol A is a contaminated area in this hardly permeable ground G2. is there.

【0015】本形態においては、まず地表から、難透水
性地盤G2における汚染領域A内に達する吸引用井戸1
を掘削し、更にこの汚染領域Aを取り囲むように、難透
水性地盤G2内に達する複数の給水用井戸2を掘削す
る。吸引用井戸1には真空ポンプPの吸引ポートに接続
した吸引パイプ3を挿入し、この吸引パイプ3の外周と
吸引用井戸1の内壁との間を、易透水性地盤G1と難透
水性地盤G2との境界の深さにシール材4を充填するこ
とによって密封する。また、給水用井戸2には、鉄コロ
イド、過マンガン酸カリウム及び安定化二酸化塩素等か
ら選択されるVOC分解剤や、あるいはエタノール、メ
タノール及び廃糖密等から選択されるVOC分解促進剤
を添加した水Wを充填する。
In the present embodiment, first, the suction well 1 reaching from the ground surface into the contaminated area A in the hardly water-permeable ground G2.
Is further excavated, and a plurality of water supply wells 2 reaching the inside of the impermeable soil G2 are further excavated so as to surround the contaminated area A. A suction pipe 3 connected to the suction port of the vacuum pump P is inserted into the suction well 1, and a water-permeable ground G1 and a poor water-permeable ground are provided between the outer periphery of the suction pipe 3 and the inner wall of the suction well 1. Sealing is performed by filling the depth of the boundary with G2 with the sealing material 4. Further, to the water supply well 2, a VOC decomposition agent selected from iron colloid, potassium permanganate, stabilized chlorine dioxide, or the like, or a VOC decomposition accelerator selected from ethanol, methanol, waste sugar concentration, or the like is added. The filled water W is filled.

【0016】次に、真空ポンプPを駆動させると、吸引
用井戸1におけるシール材4による密閉空間1a内が真
空吸引される。この密閉空間1aは、難透水性地盤G2
内に位置しているため、難透水性地盤G2内に地下水圧
傾度を生じ、この難透水性地盤G2内の地下水は、密閉
空間1aへ向けて強制的に移動されることになる。そし
て、これに伴い、各給水用井戸2内のVOC分解剤又は
VOC分解促進剤を添加した水Wが、難透水性地盤G2
内へ、その汚染領域Aの周囲から浸透していく。また、
この地下水流WFは、汚染領域Aの周囲から収束する方
向に惹起されるので、VOCの地中拡散を防止しつつそ
の浄化を行うことができる。
Next, when the vacuum pump P is driven, the inside of the closed space 1a by the seal material 4 in the suction well 1 is vacuumed. This closed space 1a is a water-impermeable ground G2.
Since it is located inside, a groundwater pressure gradient is generated in the water-impermeable ground G2, and the groundwater in this water-impermeable ground G2 is forcibly moved toward the closed space 1a. Along with this, the water W added with the VOC decomposition agent or the VOC decomposition accelerator in each water supply well 2 becomes less permeable to the ground G2.
It penetrates in from around the contaminated area A. Also,
Since this groundwater flow WF is induced in the direction of converging from the periphery of the contaminated area A, the groundwater flow WF can be purified while preventing VOC from spreading underground.

【0017】VOC分解剤を含有する水Wを用いる場
合、例えばVOC分解剤としての鉄コロイドは、その平
均粒径がφ0.5μmであり、土粒子間の空隙がこれよ
り大きい場合に使用することができる。そして、このよ
うなVOC分解剤は、難透水性地盤G2の汚染領域Aの
土粒子間隙を通過する過程で、土粒子等に吸着したトリ
クロロエチレンやテトラクロロエチレン等のVOC汚染
物質を、還元的脱塩素反応により分解し、これによって
汚染の浄化が行われる。
When water W containing a VOC decomposing agent is used, for example, iron colloid as a VOC decomposing agent has an average particle size of φ0.5 μm and is used when the voids between soil particles are larger than this. You can Then, such a VOC decomposing agent reductively dechlorinates VOC pollutants such as trichlorethylene and tetrachloroethylene adsorbed on the soil particles in the process of passing through the soil particle gaps in the contaminated area A of the hardly water-permeable ground G2. Is decomposed by this, and the purification of pollution is performed by this.

【0018】また、VOC分解促進剤を含有する水Wを
用いる場合、このVOC分解促進剤は、難透水性地盤G
2の汚染領域Aの土粒子間隙を通過する過程で、地中に
存在する分解微生物(有機塩素化合物に対する分解能を
有する微生物)の分解活性や増殖を促す。このため、微
生物を利用した間接的なVOCの分解を促し、これによ
って汚染の浄化が行われる。
When water W containing a VOC decomposition accelerator is used, this VOC decomposition accelerator is used as a poorly permeable ground G.
In the process of passing through the soil particle gap in the contaminated area A of 2, the decomposition activity and growth of the decomposition microorganisms (microorganisms capable of decomposing organic chlorine compounds) existing in the ground are promoted. Therefore, the indirect decomposition of VOCs by utilizing microorganisms is promoted, thereby purifying the pollution.

【0019】図3は、本発明に係る難透水性地盤の浄化
方法の好ましい第二の実施の形態を示す地盤断面図、図
4は平面図で、先の図1と同様、参照符号G1は表層近
くの砂質土等からなる透水性地盤、参照符号G2は深度
の深い沖積粘土層又は洪積粘土層からなる難透水性地
盤、参照符号Aは、この難透水性地盤G2における汚染
領域である。
FIG. 3 is a sectional view of the ground showing a second preferred embodiment of the method for cleaning a poorly water-permeable ground according to the present invention, FIG. 4 is a plan view, and reference numeral G1 is the same as FIG. 1 above. Permeable ground consisting of sandy soil near the surface layer, reference sign G2 is a poorly permeable ground composed of deep alluvial clay layer or diluvial clay layer, reference sign A is a contaminated area in this poorly permeable ground G2. is there.

【0020】本形態においては、まず地表から、難透水
性地盤G2における汚染領域Aへ向けて給水用井戸5を
掘削し、この給水用井戸5には第一の電極体としての鉄
管6を挿入して、その周囲を砂あるいはれき7等で埋
め、この鉄管6の外周と給水用井戸5の内壁との間を、
易透水性地盤G1と難透水性地盤G2との境界の深さに
シール材4を充填することによって密封する。なお、鉄
管6は、シール材4で密封される高さよりも下の部分に
多数の小孔を開設したものが好ましい。給水用井戸5に
おけるシール材4で密閉された空間4aには、鉄管6を
介して、鉄コロイド、過マンガン酸カリウム及び安定化
二酸化塩素等から選択されるVOC分解剤や、あるいは
エタノール、メタノール及び廃糖密等から選択されるV
OC分解促進剤を添加した水Wを充填する。
In this embodiment, first, a water supply well 5 is excavated from the ground surface toward a contaminated area A in the hardly water-permeable ground G2, and an iron pipe 6 as a first electrode body is inserted into the water supply well 5. Then, the periphery thereof is filled with sand or gravel 7 and the like, and between the outer circumference of the iron pipe 6 and the inner wall of the water supply well 5,
Sealing is performed by filling the depth of the boundary between the easily water-permeable ground G1 and the hardly water-permeable ground G2 with the sealing material 4. It is preferable that the iron pipe 6 has a large number of small holes formed in a portion below the height at which it is sealed by the sealing material 4. In the space 4a sealed by the sealing material 4 in the water supply well 5, a VOC decomposer selected from iron colloid, potassium permanganate, stabilized chlorine dioxide, or the like, or ethanol, methanol, or V selected from waste sugar
Water W containing an OC decomposition accelerator is filled.

【0021】一方、難透水性地盤G2における汚染領域
Aの周囲には、この汚染領域Aを取り囲むように、第二
の電極体としての複数の鉄棒8を挿入する。鉄管6及び
鉄棒8は、導線9を介して直流電源Vに電気的に接続す
る。この場合、鉄管6は直流電源Vにおける陽極に、各
鉄棒8は直流電源Vにおける陰極に接続する。
On the other hand, a plurality of iron bars 8 as the second electrode body are inserted around the contaminated area A in the hardly water-permeable ground G2 so as to surround the contaminated area A. The iron pipe 6 and the iron rod 8 are electrically connected to the DC power supply V via a conductor 9. In this case, the iron pipe 6 is connected to the anode of the DC power supply V, and each iron rod 8 is connected to the cathode of the DC power supply V.

【0022】なお、鉄管6は、シール材4で密封される
高さよりも下の部分、すなわち難透水性地盤G2内に挿
入される部分に多数の小孔を開設したものが好ましい。
また、鉄管6及び鉄棒8は、易透水性地盤G1内の高さ
となる部分を、予め電気絶縁性の合成樹脂チューブなど
で被覆しておくことによって、この鉄管6と鉄棒8の間
で、電流が易透水性地盤G1内を短絡しないようにす
る。
It is preferable that the iron pipe 6 has a large number of small holes at a portion below the height at which it is sealed by the sealing material 4, that is, a portion to be inserted into the water impermeable ground G2.
Further, the iron pipe 6 and the iron rod 8 have a height in the easily water-permeable ground G1 previously covered with an electrically insulating synthetic resin tube or the like, so that the electric current flows between the iron pipe 6 and the iron rod 8. Does not short circuit the easily permeable ground G1.

【0023】この状態で、直流電源Vを駆動させ、給水
用井戸5内の鉄管6とその周囲の鉄棒8に直流電圧を印
加すると、難透水性地盤G2内には、陽極となる鉄管6
(給水用井戸5)側から陰極となる鉄棒8側へ向けて、
電気浸透現象による地下水流WFが惹起され、すなわち
難透水性地盤G2内の地下水が強制的に移動される。そ
して、これに伴い、給水用井戸5内のVOC分解剤又は
VOC分解促進剤を添加した水Wが、難透水性地盤G2
の汚染領域A内からその周囲へ向けて浸透していく。
In this state, when the DC power source V is driven and a DC voltage is applied to the iron pipe 6 in the water supply well 5 and the iron rod 8 around it, the iron pipe 6 serving as an anode is formed in the impermeable ground G2.
From the (water supply well 5) side toward the iron rod 8 side which becomes the cathode,
The groundwater flow WF due to the electroosmosis phenomenon is induced, that is, the groundwater in the hardly permeable ground G2 is forcibly moved. Then, along with this, the water W to which the VOC decomposition agent or the VOC decomposition accelerator in the water supply well 5 is added becomes the water-impermeable ground G2.
Permeates from the inside of the contaminated area A toward the surrounding area.

【0024】鉄管6及び鉄棒8の表面のうち、易透水性
地盤G1内にある部分は絶縁されているので、電流が易
透水性地盤G1を介して短絡することはなく、難透水性
地盤G2での電気浸透による強制地下水流WFが確実に
惹起される。また、各鉄棒8は、鉄管6を中心とする円
筒面に沿って挿入すれば、鉄管6と各鉄棒8との距離が
等しくなるため、鉄管6と各鉄棒8との間の電流、ひい
てはこれによる地下水流WFもほぼ均一になる。
Since the portions of the surfaces of the iron pipe 6 and the iron rod 8 in the easily water-permeable ground G1 are insulated, the electric current is not short-circuited through the easily water-permeable ground G1, and the slightly water-permeable ground G2. Forced groundwater flow WF due to electro-osmosis in S.R. If each iron rod 8 is inserted along a cylindrical surface centered on the iron pipe 6, the distance between the iron pipe 6 and each iron rod 8 becomes equal, so that the electric current between the iron pipe 6 and each iron rod 8 and, by extension, this The groundwater flow WF due to is also almost uniform.

【0025】したがって、先に説明したように、VOC
分解剤を含有する水Wを用いた場合は、難透水性地盤G
2の汚染領域Aの土粒子間隙を通過する過程で、還元的
脱塩素反応によりVOC汚染物質を分解し、VOC分解
促進剤を含有する水Wを用いた場合は、地中に存在する
分解微生物によるVOC分解が促されることによって、
汚染の浄化が行われる。
Therefore, as explained above, the VOC
When water W containing a decomposing agent is used, the water-impermeable ground G
Decomposing microorganisms existing in the ground when water W containing a VOC decomposition accelerator is used by decomposing VOC pollutants by a reductive dechlorination in the process of passing through the soil particle gaps in the second pollution area A. By promoting VOC decomposition by
Purification of pollution is performed.

【0026】なお、本形態においては、電気浸透現象に
よる地下水流WFが、汚染領域Aからその周囲へ向けて
生じるものとしたが、VOCの地中拡散が問題となるよ
うな場合は、図3及び図4とは逆に、給水用井戸5を、
汚染領域Aを取り囲むように掘削して、直流電源Vの陽
極に接続される鉄管6を挿入し、陰極に接続される鉄棒
8を、難透水性地盤G2における汚染領域A内へ挿入す
る。このようにすれば、電気浸透現象による地下水流W
Fが汚染領域Aの周囲から収束する方向に惹起されるの
で、VOCの地中拡散を防止しつつその浄化を行うこと
ができる。
In this embodiment, the groundwater flow WF due to the electroosmosis phenomenon is assumed to be generated from the contaminated area A toward the surrounding area. However, in the case where the underground diffusion of VOCs becomes a problem, FIG. And, contrary to FIG. 4, the water supply well 5 is
Excavation is performed so as to surround the contaminated region A, the iron pipe 6 connected to the anode of the DC power source V is inserted, and the iron rod 8 connected to the cathode is inserted into the contaminated region A in the hardly water-permeable ground G2. By doing this, the groundwater flow W due to the electroosmosis phenomenon
Since F is generated in the direction of converging from the periphery of the contaminated area A, it is possible to purify the VOC while preventing the underground diffusion.

【0027】また、上述した各実施の形態においては、
いずれも、難透水性地盤G2が深度の深いところにある
ものとして説明したが、本発明の方法は、難透水性地盤
G2の汚染領域Aの深さに関係なく適用可能であること
は勿論である。また、本発明は、上述の各形態のよう
に、地下水の浸透速度が極めて緩慢なために地下水の汲
み上げによる地下水流にのみ依存した汚染浄化が期待で
きない難透水性地盤の汚染修復手段として特に有効であ
るが、砂質土や砂質粘土等からなる地盤の浄化にも適用
することも可能である。
Further, in each of the above-mentioned embodiments,
In each of the above explanations, it is assumed that the hardly water-permeable ground G2 is located at a deep depth, but the method of the present invention is of course applicable regardless of the depth of the contaminated area A of the hardly water-permeable ground G2. is there. In addition, the present invention is particularly effective as a pollution remediation means for poorly permeable ground in which the groundwater infiltration rate is extremely slow, and thus the pollution remediation that depends only on the groundwater flow due to the pumping of groundwater cannot be expected, as in the above-described respective embodiments. However, it can also be applied to the purification of the ground consisting of sandy soil or sandy clay.

【0028】[0028]

【発明の効果】請求項1の発明に係る難透水性地盤の浄
化方法によれば、通常は地下水流が極めて緩慢である難
透水性地盤内に、吸引用井戸の真空吸引によって、顕著
な水流を強制的に惹起させ、これによって難透水性地盤
の汚染領域に、給水用井戸から汚染物質分解剤又は汚染
物質分解促進剤を含有させた水を供給するものであるた
め、地下水の汲み上げによる地下水流にのみ依存した汚
染浄化が期待できない難透水性地盤の汚染浄化手段とし
て有効であり、また、良質土との置換による浄化が困難
な、深層の難透水性地盤の汚染浄化手段として有効であ
る。
According to the method of purifying a poorly permeable ground according to the first aspect of the present invention, a remarkable water flow is caused by the vacuum suction of the suction well into the hardly permeable ground where the groundwater flow is usually extremely slow. Since the water containing the pollutant decomposing agent or the pollutant decomposition promoting agent is supplied from the water supply well to the contaminated area of the poorly permeable ground, It is effective as a pollution purification means for difficult-to-permeable soil that cannot be expected to be purified only by the flow, and is also effective as a purification method for deep-permeable, difficult-to-permeable soil that is difficult to clean by substituting good quality soil. .

【0029】請求項2の発明に係る難透水性地盤の浄化
方法によれば、汚染領域の周囲を取り囲むように存在す
る給水用井戸から、汚染物質分解剤又は汚染物質分解促
進剤を含有させた水が汚染領域内へ向けて移動するた
め、汚染物質の拡散を防止しつつ汚染の浄化を行うこと
ができる。
According to the method for purifying poorly permeable ground according to the second aspect of the present invention, the pollutant decomposing agent or the pollutant decomposition accelerating agent is added from the water supply well existing so as to surround the perimeter of the contaminated area. Since the water moves toward the inside of the contaminated area, it is possible to purify the contamination while preventing the diffusion of the contaminants.

【0030】請求項3の発明に係る難透水性地盤の浄化
方法によれば、通常は地下水流が極めて緩慢である難透
水性地盤内に、電気浸透によって顕著な水流を強制的に
惹起させ、これによって難透水性地盤の汚染領域に、給
水用井戸から汚染物質分解剤又は汚染物質分解促進剤を
含有させた水を供給するものであるため、地下水の汲み
上げによる地下水流にのみ依存した汚染浄化が期待でき
ない難透水性地盤の汚染浄化手段として有効であり、ま
た、良質土との置換による浄化が困難な、深層の難透水
性地盤の汚染浄化手段として有効である。
According to the method of purifying a poorly permeable ground according to the third aspect of the invention, a remarkable water flow is forcibly caused by electroosmosis in the hardly permeable ground where the groundwater flow is usually extremely slow, As a result, water containing a pollutant decomposing agent or a pollutant decomposition accelerator is supplied from the water supply well to the contaminated area of the poorly permeable ground.Therefore, purification of pollution that depends only on the groundwater flow by pumping groundwater It is effective as a pollution purification means for difficult-to-permeable soil that cannot be expected, and is also effective as a pollution-cleaning means for deeply permeable soil that is difficult to clean by replacement with good quality soil.

【0031】請求項4の発明に係る難透水性地盤の浄化
方法によれば、汚染領域に設けた電極体と、その周囲を
取り囲むように設けた電極体との間で、汚染物質分解剤
又は汚染物質分解促進剤を含有させた水が電気浸透によ
って放射状に流れるので、効率良く汚染の浄化を行うこ
とができる。
According to the method of cleaning a poorly water-permeable ground according to the invention of claim 4, a pollutant decomposer or a pollutant decomposition agent is provided between the electrode body provided in the contaminated region and the electrode body surrounding the periphery of the electrode body. Since the water containing the pollutant decomposition accelerator flows radially by electroosmosis, the pollution can be efficiently purified.

【0032】請求項5の発明に係る難透水性地盤の浄化
方法によれば、処理水にVOC分解剤を用いるため、難
透水性地盤の汚染領域を強制流動される過程で、還元的
脱塩素反応によって、VOCを分解するため、トリクロ
ロエチレン等に代表されるVOC汚染を有効に修復する
ことができる。
According to the method for purifying hardly water permeable soil according to the fifth aspect of the present invention, since the VOC decomposer is used in the treated water, reductive dechlorination is carried out in the process of forced flow in the contaminated area of the hardly water permeable soil. Since VOCs are decomposed by the reaction, VOC contamination represented by trichlorethylene and the like can be effectively restored.

【0033】請求項6の発明に係る難透水性地盤の浄化
方法によれば、処理水に、VOC分解微生物の活性や増
殖を促すVOC分解促進剤を用いるため、微生物による
VOCの分解能によって、トリクロロエチレン等に代表
されるVOC汚染を有効に修復することができる。
According to the method for purifying poorly permeable ground according to the sixth aspect of the invention, since the VOC decomposition accelerating agent that promotes the activity and growth of the VOC decomposing microorganisms is used in the treated water, trichlorethylene can be decomposed by the VOCs by the microorganisms. It is possible to effectively repair VOC contamination represented by the above.

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

【図1】本発明に係る難透水性地盤の浄化方法の、好ま
しい第一の実施の形態を示す地盤の鉛直断面図である。
FIG. 1 is a vertical cross-sectional view of the ground showing a preferred first embodiment of a method for cleaning a poorly water-permeable ground according to the present invention.

【図2】図1における吸引用井戸と給水用井戸の平面配
置を示す図である。
FIG. 2 is a diagram showing a planar arrangement of a suction well and a water supply well in FIG.

【図3】本発明に係る難透水性地盤の浄化方法の、好ま
しい第二の実施の形態を示す地盤の鉛直断面図である。
FIG. 3 is a vertical cross-sectional view of the ground showing a second preferred embodiment of the method for cleaning a poorly water-permeable ground according to the present invention.

【図4】図4における給水用井戸及び鉄管と鉄棒の平面
配置を示す図である。
FIG. 4 is a diagram showing a plane arrangement of a water supply well, an iron pipe, and an iron bar in FIG.

【符号の説明】[Explanation of symbols]

1 吸引用井戸 1a 密閉空間 2,5 給水用井戸 3 吸引パイプ 4 シール材 6 鉄管(第一の電極体) 8 鉄棒(第二の電極体) A 汚染領域 G1 易透水性地盤 G2 難透水性地盤 V 直流電源 P 真空ポンプ W 処理水 1 suction well 1a closed space 2,5 Water well 3 suction pipe 4 Seal material 6 Iron tube (first electrode body) 8 Iron bar (second electrode body) A contaminated area G1 easily permeable ground G2 Hardly permeable ground V DC power supply P vacuum pump W treated water

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) E02D 3/10 105 Fターム(参考) 2D043 DA04 EB06 4D004 AA41 AB06 AC07 CA18 CA37 CC11 CC20 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) E02D 3/10 105 F term (reference) 2D043 DA04 EB06 4D004 AA41 AB06 AC07 CA18 CA37 CC11 CC20

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 難透水性地盤内へ達し又は貫通する所要
数の吸引用井戸を掘削し、前記難透水性地盤内へ達し又
は貫通する所要数の給水用井戸を前記吸引用井戸との間
に前記難透水性地盤内の汚染領域が存在するように掘削
し、前記給水用井戸に汚染物質分解剤又は汚染物質分解
促進剤を含有させた水を供給すると共に、前記吸引用井
戸における前記難透水性地盤内に位置する部分を密閉し
て真空吸引することによって、前記難透水性地盤内の水
を強制流動させることを特徴とする汚染地盤浄化工法。
1. A required number of suction wells reaching or penetrating into the water-impermeable ground are excavated, and a required number of water supply wells reaching or penetrating into the water-impermeable ground are provided between the suction wells. The excavation is performed so that there is a contaminated area in the hardly water-permeable ground, and water containing a pollutant decomposing agent or a pollutant decomposition accelerator is supplied to the water supply well, and the difficulty in the suction well is increased. A method for cleaning a contaminated ground, characterized in that the water in the hardly water-permeable ground is forced to flow by hermetically sealing a portion located in the water-permeable ground and vacuum suction.
【請求項2】 吸引用井戸は、汚染領域へ達し又は貫通
するように掘削し、給水用井戸は、前記汚染領域の周囲
を取り囲むように掘削することを特徴とする請求項1に
記載の汚染地盤浄化工法。
2. The pollution according to claim 1, wherein the suction well is drilled to reach or penetrate the contaminated area, and the water supply well is drilled to surround the perimeter of the contaminated area. Ground purification method.
【請求項3】 難透水性地盤の汚染領域内へ達し又は貫
通する給水用井戸を掘削すると共にこの給水用井戸に第
一の電極体を挿入し、前記難透水性地盤内へ達し又は貫
通する所要数の第二の電極体を前記吸引用井戸との間に
前記難透水性地盤内の汚染領域が存在するように挿入
し、前記給水用井戸に汚染物質分解剤又は汚染物質分解
促進剤を含有させた水を供給し、前記第一の電極体を直
流電源の陽極側に接続すると共に、前記第二の電極体を
直流電源の陰極側に接続して両電極間に直流電圧を印加
することによって、前記難透水性地盤内の水を強制流動
させることを特徴とする汚染地盤浄化工法。
3. A water supply well reaching or penetrating into a contaminated area of the water-impermeable ground is excavated, and a first electrode body is inserted into the water-supply well to reach or penetrate the water-impermeable ground. Insert a required number of second electrode bodies so that there is a contaminated region in the hardly water-permeable ground between the suction well, and a pollutant decomposer or pollutant decomposition accelerator in the water supply well. The contained water is supplied, and the first electrode body is connected to the anode side of the DC power supply, and the second electrode body is connected to the cathode side of the DC power supply to apply a DC voltage between both electrodes. Therefore, the contaminated ground purification method is characterized in that the water in the hardly water-permeable ground is forced to flow.
【請求項4】 第一の電極体が挿入される給水用井戸及
び第二の電極体のうちの一方を、汚染領域へ達し又は貫
通するように設け、他方を、前記汚染領域の周囲を取り
囲むように設けることを特徴とする請求項3に記載の汚
染地盤浄化工法。
4. One of the water supply well into which the first electrode body is inserted and the second electrode body are provided so as to reach or penetrate the contaminated region, and the other surrounds the periphery of the contaminated region. The contaminated ground purification method according to claim 3, wherein the method is provided as follows.
【請求項5】 汚染物質分解剤は、鉄コロイド、過マン
ガン酸カリウム及び安定化二酸化塩素等から選択される
VOC分解剤であることを特徴とする請求項1乃至4の
いずれかに記載の難透水性地盤の浄化方法。
5. The difficulty according to claim 1, wherein the pollutant decomposer is a VOC decomposer selected from iron colloid, potassium permanganate, stabilized chlorine dioxide and the like. Method for cleaning permeable ground.
【請求項6】 汚染物質分解促進剤は、エタノール、メ
タノール及び廃糖密等から選択されるVOC分解促進剤
であることを特徴とする請求項1乃至4のいずれかに記
載の難透水性地盤の浄化方法。
6. The hardly water-permeable ground according to any one of claims 1 to 4, wherein the pollutant decomposition accelerator is a VOC decomposition accelerator selected from ethanol, methanol, and waste sugar concentrate. Purification method.
JP2001222536A 2001-07-24 2001-07-24 Purification method for poorly permeable ground Expired - Lifetime JP4713777B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2423766A (en) * 2005-03-03 2006-09-06 Rockbourne Environmental Ltd Waste treatment
JP2008307539A (en) * 2008-08-28 2008-12-25 Ohbayashi Corp Cleaning method and system of contaminated soil
JP2012180734A (en) * 2011-02-09 2012-09-20 Asahi Techno:Kk Ground improvement method
CN102704488A (en) * 2012-04-24 2012-10-03 王军 Novel soft soil foundation pit excavation method

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