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JP2524290B2 - Method and apparatus for insolubilizing heavy metals in contaminated soil - Google Patents
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JP2524290B2 - Method and apparatus for insolubilizing heavy metals in contaminated soil - Google Patents

Method and apparatus for insolubilizing heavy metals in contaminated soil

Info

Publication number
JP2524290B2
JP2524290B2 JP4269513A JP26951392A JP2524290B2 JP 2524290 B2 JP2524290 B2 JP 2524290B2 JP 4269513 A JP4269513 A JP 4269513A JP 26951392 A JP26951392 A JP 26951392A JP 2524290 B2 JP2524290 B2 JP 2524290B2
Authority
JP
Japan
Prior art keywords
water
anode
cathode
contaminated soil
tube
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
JP4269513A
Other languages
Japanese (ja)
Other versions
JPH06158635A (en
Inventor
照彦 山嵜
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP4269513A priority Critical patent/JP2524290B2/en
Publication of JPH06158635A publication Critical patent/JPH06158635A/en
Application granted granted Critical
Publication of JP2524290B2 publication Critical patent/JP2524290B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Landscapes

  • Investigation Of Foundation Soil And Reinforcement Of Foundation Soil By Compacting Or Drainage (AREA)
  • Fire-Extinguishing Compositions (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、公害の原因である重金
属類が土壌中に存在し、土壌が汚染されている場合、汚
染土壌を掘削、移動することなく、原位置において汚染
された土中水を排水し、地中にある重金属類を不溶化し
て処理し、土壌を再利用することを可能にする汚染土壌
中の重金属類を不溶化する方法とその装置に関するもの
である。
BACKGROUND OF THE INVENTION The present invention relates to a soil contaminated in situ without excavating or moving the contaminated soil when heavy metals which cause pollution are present in the soil and the soil is contaminated. TECHNICAL FIELD The present invention relates to a method and an apparatus for insolubilizing heavy metals in contaminated soil, which enables waste water to be drained, insoluble heavy metals in the ground to be treated, and soil to be reused.

【0002】[0002]

【従来の技術】公害を生ずる重金属類を扱う各種産業の
工場の地盤には、これら諸設備から漏洩した重金属類に
よって、または産業廃棄物によって土壌が汚染された場
合の従来の処理方法としては、前記汚染土壌を掘削して
他に搬出するか、または前記掘削土壌を細粉化して混合
機で安定剤と混合して埋め戻すか、または他から搬入し
た新しい土と置き換える等の方法によって、汚染土壌の
区域を再生させるという方法が用いられていた。
2. Description of the Related Art On the ground of factories of various industries that handle heavy metals that cause pollution, as conventional treatment methods when soil is polluted by heavy metals leaked from these facilities or by industrial waste, Contamination by excavating the contaminated soil and carrying it out to the other, or by pulverizing the excavated soil and mixing it with a stabilizer in a mixer to backfill it, or replacing it with new soil brought in from another place The method of regenerating the area of soil was used.

【0003】[0003]

【発明が解決しようとする課題】前記のように従来は、
重金属類によって汚染された土壌を原位置で処理し、こ
れを再利用する方法がなく、従って汚染された土壌を掘
削して、取り出しこれを細粉化して、安定剤と混合した
後にこれを埋め戻すか、または汚染土壌を他の処理施設
に運搬して、他から新しい土を搬入して埋め戻して置き
換えるかの、いずれかの方法が用いられていたが、掘
削、混合また搬出入の際において汚染土が飛散するとい
う問題点があり、更に作業時の騒音や搬出入の際に周辺
住民に二次的公害を与える等の問題点があった。
As described above, conventionally,
There is no way to treat the soil contaminated by heavy metals in-situ and recycle it, therefore the contaminated soil should be excavated, taken out and finely ground and mixed with stabilizers before filling it. Either returning or transporting the contaminated soil to another treatment facility and then importing new soil from another to backfill and replace it, but during excavation, mixing or unloading There was a problem that contaminated soil was scattered in the area, and there were problems such as noise during the work and secondary pollution to surrounding residents when carrying in and out.

【0004】本発明は、前記従来の問題点を解決するこ
とを目的とする汚染土壌の処理方法およびその装置を提
供しようとするものである。
The present invention is intended to provide a method for treating contaminated soil and an apparatus thereof for the purpose of solving the above conventional problems.

【0005】[0005]

【課題を解決するための手段】本発明は、陽極と陰極の
電極を兼ねた多数の通水孔を穿設した複数本の中空管
を、陽極用と陰極用に対向して管列を形成して汚染土壌
の深さより深く貫入設置すると共に、前記陽極と陰極と
の極性の転換ができるように設置する一方、前記各電極
に直流電流を通電して直流電圧を負荷し、陽極管中に硫
化ナトリウムまたは硫酸鉄の水溶液を注入して、両極間
の汚染土壌中に作用する電気浸透現象を利用して前記陽
極管から通水孔を介して前記水溶液を吐出して汚染土壌
中に均等に浸透させて、該水溶液を汚染土壌中の重金属
類に接触させ不溶化の化学的反応を生ぜしめて、汚染さ
れた土中水、または余剰の不溶化用の水溶液を通水孔を
介して陰極管に集水し、然る後水質検査を行い、所定の
水質基準値に達するまで、前記水溶液の陽極管からの吐
出、汚染土壌への浸透および陰極管への集水を繰返すと
いう手段を採用することにより、上記問題点を解決し
た。
SUMMARY OF THE INVENTION According to the present invention, a plurality of hollow tubes having a large number of water passage holes which also serve as electrodes of an anode and a cathode are bored to form a row of tubes facing each other for the anode and the cathode. While forming and penetrating deeper than the depth of the contaminated soil, while installing so that the polarity of the anode and the cathode can be switched, a direct current is applied to each of the electrodes to apply a direct current voltage to the anode tube. An aqueous solution of sodium sulfide or iron sulfate is injected into the electrode, and the electroosmosis phenomenon that acts on the contaminated soil between the two electrodes is used to discharge the aqueous solution from the anode tube through the water holes to evenly distribute it in the contaminated soil. In contact with the heavy metal in the contaminated soil to cause an insolubilizing chemical reaction, and contaminated soil water or excess insolubilizing aqueous solution is passed through the water holes to the cathode tube. After collecting water and then inspecting water quality, the specified water quality standard value is reached. In, by adopting a means of repeated collecting water discharged from the anode tube of the aqueous solution, the penetration and cathode tubes to contaminated soil, has solved the above problems.

【0006】[0006]

【作用】上記構成より成る本発明によれば、重金属類に
よる汚染土壌区域内に陽極用の管列と、陰極用の管列と
を対向するように、汚染土壌の汚染深度よりも深く貫入
設置して、これに直流電流を通電して両極間の汚染土壌
中に作用する電気浸透現象を利用して、前記陽極側の管
列から重金属類の不溶化に必要な硫化ナトリウムまたは
硫酸鉄の水溶液を吐出し、電気浸透現象によって汚染土
壌中に前記水溶液を均等に浸透させ、更に該水溶液を陰
極側の管列に集水するというサイクルを繰返すことによ
り、前記水溶液による不溶化の化学反応の外に、電気化
学的な作用による酸化還元反応を利用して重金属類を原
位置で不溶化する。
According to the present invention having the above-described structure, the anode row and the cathode row are installed to penetrate deeper than the pollution depth of the contaminated soil so that the anode row and the cathode row are opposed to each other in the soil area contaminated by heavy metals. Then, by applying a direct current to this and utilizing the electroosmosis phenomenon that acts in the contaminated soil between the two electrodes, an aqueous solution of sodium sulfide or iron sulfate necessary for insolubilization of heavy metals from the anode side tube row is obtained. Discharge, by uniformly permeating the aqueous solution into the contaminated soil by the electroosmosis phenomenon, by further repeating the cycle of collecting the aqueous solution in the tube row on the cathode side, in addition to the chemical reaction of insolubilization by the aqueous solution, In-situ insolubilization of heavy metals by utilizing redox reaction by electrochemical action.

【0007】[0007]

【実施例】本発明方法は、陽極と陰極の電極を兼ねた多
数の通水孔を穿設した複数本の中空管を、陽極用と陰極
用に対向して管列を形成して汚染土壌の深さより深く貫
入設置すると共に、前記陽極と陰極との極性の転換がで
きるように設置する一方、前記各電極に直流電流を通電
して直流電圧を負荷し、陽極管中に硫化ナトリウムまた
は硫酸鉄の水溶液を注入して、両極間の汚染土壌中に作
用する電気浸透現象を利用して前記陽極管から通水孔を
介して前記水溶液を吐出して汚染土壌中に均等に浸透さ
せて、該水溶液を汚染土壌中の重金属類に接触させ不溶
化の化学的反応を生ぜしめて、汚染された土中水、また
は余剰の不溶化用の水溶液を通水孔を介して陰極管に集
水し、然る後水質検査を行い、所定の水質基準値に達す
るまで、前記水溶液の陽極管からの吐出、汚染土壌への
浸透および陰極管への集水を繰返すことにより、汚染土
壌中の重金属類を不溶化するものである。以下更に前記
方法とその装置につき、図面に基づいて詳細に説明す
る。
EXAMPLE The method of the present invention is contaminated by forming a plurality of hollow tubes having a large number of water passage holes, which also serve as anode and cathode electrodes, facing each other for the anode and the cathode to form a row of tubes. While being installed deeper than the depth of the soil, while being installed so that the polarity of the anode and cathode can be switched, a DC voltage is applied to each of the electrodes by applying a DC current, and sodium sulfide in the anode tube or By injecting an aqueous solution of iron sulfate, and utilizing the electroosmosis phenomenon that acts on the contaminated soil between the two electrodes, the aqueous solution is discharged from the anode tube through the water passage holes to allow it to penetrate into the contaminated soil evenly. , Contacting the heavy metal in the contaminated soil to cause a chemical reaction of insolubilization, contaminated soil water, or excess surplus of the insolubilizing aqueous solution to collect water into the cathode tube through the water holes, After that, a water quality test is performed and the water-soluble Discharged from the anode tube, by repeating the collecting water to penetrate and cathode tubes to contaminated soil is to insolubilize the heavy metals in contaminated soil. The above method and apparatus will be described in detail below with reference to the drawings.

【0008】重金属類によって汚染された汚染土壌1の
区域内にその土壌の土質工学的な特性を調査して、その
地盤を構成している土質の透水係数の値を基準にした間
隔で、陽極と陰極の電極を兼用する複数本の有底の中空
管2を、陽極用と陰極用に対向して管列を形成して汚染
土壌1の深さより深く地中に貫入設置する。
In the area of the contaminated soil 1 contaminated by heavy metals, the soil engineering characteristics of the soil are investigated, and the anode is set at intervals based on the value of the hydraulic conductivity of the soil constituting the ground. A plurality of bottomed hollow tubes 2 which also serve as cathode electrodes are formed so as to face each other for the anode and the cathode to form a row of tubes and penetrate into the ground deeper than the depth of the contaminated soil 1.

【0009】前記中空管2の外周壁面には、硫化ナトリ
ウムまたは硫酸鉄の水溶液を土壌中に吐出し、且つ土壌
中の前記水溶液を集水ができるように多数の通水孔3を
穿設すると共に、前記各中空管2の地表より突出した部
分に接続端子等の接続装置4を装着する。
A large number of water passage holes 3 are formed on the outer peripheral wall surface of the hollow tube 2 so that an aqueous solution of sodium sulfide or iron sulfate can be discharged into the soil and the aqueous solution in the soil can be collected. At the same time, the connection device 4 such as a connection terminal is attached to the portion of each hollow tube 2 protruding from the surface of the earth.

【0010】前記汚染土壌1中に陽極用と陰極用の電極
として夫々対向して2列の管列A,Bを対として貫入設
置された2組の各中空管2a,2bのうち、2列の陽極
用の管列Aを構成する各中空管2aには、給水槽5に一
端を連通した送水導管6に突設されたコック7に、前記
各中空管2aの上方部から突出した連通管8を連結して
送水導管6が連通固定され、更に直流電源9の陽極側の
コード10に、陽極側の管列Aの各中空管2aの接続装
置4より引き出したリード線11を接続する。
Of the two sets of hollow tubes 2a and 2b which are installed in the contaminated soil 1 as two pairs of tube rows A and B facing each other as electrodes for anode and cathode, respectively, 2 In each hollow tube 2a constituting the row A of tubes for the anode, a cock 7 projecting from a water supply conduit 6 having one end communicating with the water tank 5 is projected from an upper portion of each hollow tube 2a. The water supply conduit 6 is connected and fixed by connecting the connected communication pipes 8, and the lead wire 11 drawn from the connection device 4 of each hollow pipe 2a of the anode side tube row A is connected to the anode side cord 10 of the DC power supply 9. Connect.

【0011】また、2列の陰極用の管列Bを構成する各
中空管2bには、気水分離槽12に一端を連通し他集水
導管13に突設されたコック7に、前記各中空管2bの
上方部から突出した連通管8を連結して集水導管13が
連通固定され、更に直流電源9の陰極側のコード14
に、陰極側の管列Bの各中空管2bの接続装置4より引
き出したリード線15を接続する。
Each of the hollow tubes 2b constituting the two rows of cathode tubes B is connected to the steam / water separation tank 12 at one end thereof by a cock 7 projecting from another water collecting conduit 13, The water collection conduit 13 is connected and fixed by connecting the communication pipes 8 projecting from the upper portion of each hollow pipe 2b, and further the cord 14 on the cathode side of the DC power supply 9 is connected.
The lead wire 15 drawn from the connecting device 4 of each hollow tube 2b of the tube row B on the cathode side is connected to.

【0012】図1,図2には2組の管列A,Bが図示さ
れているが、処理面積が大きい場合には更に多くの管列
を配設する。なお、図中、16は給水槽5と送水導管6
間に配設されたゲートバルブ、17は気水分離槽12と
集水導管13間に配設されたゲートバルブである。
Although two sets of tube rows A and B are shown in FIGS. 1 and 2, more tube rows are arranged when the processing area is large. In the figure, 16 is a water supply tank 5 and a water supply conduit 6.
A gate valve 17 is provided between the water vapor separation tank 12 and the water collecting conduit 13.

【0013】前記気水分離槽12は排水ポンプ18を介
在せしめた排水連結管19によって沈殿槽20に連結さ
れ、且つ該沈殿槽20は送水ポンプ21を介在せしめた
送水連結管22によって吸着槽23に連結され、更に前
記吸着槽23は給水ポンプ24を介在せしめた給水連結
管25によって給水槽5に連結されると共に、該給水槽
5は前記したようにゲートバルブ16を介して送水導管
6に連結されている。そして、これらは一連にサイクル
を形成するように設置され、汚染土壌1中の汚染された
土中水や、給水槽5から送水導管6に送られた硫化ナト
リウムまたは硫酸鉄の水溶液は、水質基準をクリアーす
るまで外部に排出しないような設置構成である。
The air / water separation tank 12 is connected to a settling tank 20 by a drainage connecting pipe 19 with a drainage pump 18 interposed, and the settling tank 20 is adsorbed by a water supply connecting pipe 22 with a water feeding pump 21. Further, the adsorption tank 23 is connected to the water supply tank 5 by a water supply connection pipe 25 having a water supply pump 24 interposed, and the water supply tank 5 is connected to the water supply conduit 6 via the gate valve 16 as described above. It is connected. These are installed so as to form a cycle in series, and the contaminated soil water in the contaminated soil 1 and the aqueous solution of sodium sulfide or iron sulfate sent from the water supply tank 5 to the water supply conduit 6 are water quality standards. It is installed so that it is not discharged until it is cleared.

【0014】一方、前記給水槽5には硫化ナトリウムま
たは硫酸鉄を適宜の濃度に調整する溶解槽26が、中間
に送液ポンプ27を介在せしめた送液連結管28によっ
て連結されており、前記溶解槽26で適宜の濃度に調整
された硫化ナトリウムまたは硫酸鉄の水溶液は、送液ポ
ンプ27により送液連結管28を介して給水槽5に送ら
れ、更に前記給水槽5からゲートバルブ16を介して送
水導管6に流れ、該送水導管6に取付けたコック7を介
して連通管8を通り、陽極側の管列Aの各中空管2aの
通水孔3から汚染土壌1中に吐出され、電気浸透現象の
発生している汚染土壌1中にある重金属類に接して、不
溶化の化学的反応を生ぜしめて、汚染された土中水、ま
たは余剰の不溶化用の水溶液を陰極側の管列Bの中空管
2bの通水孔3から各中空管2b内に集水する。
On the other hand, a dissolution tank 26 for adjusting the concentration of sodium sulfide or iron sulfate to an appropriate concentration is connected to the water supply tank 5 by a liquid supply connecting pipe 28 with a liquid supply pump 27 interposed in between. The aqueous solution of sodium sulfide or iron sulfate adjusted to an appropriate concentration in the dissolution tank 26 is sent to the water supply tank 5 by the liquid supply pump 27 via the liquid supply connection pipe 28, and further, the gate valve 16 is supplied from the water supply tank 5 to the water supply tank 5. Through the communication pipe 8 through the cock 7 attached to the water supply conduit 6, and discharged into the contaminated soil 1 from the water passage hole 3 of each hollow tube 2a of the anode side tube row A. In contact with heavy metals present in the contaminated soil 1 where the electroosmosis phenomenon is occurring, a chemical reaction of insolubilization is generated, and contaminated soil water or excess insolubilizing aqueous solution is used on the cathode side tube. Is it the water passage hole 3 of the hollow tube 2b in row B? Catchment to the respective hollow tube 2b.

【0015】前記各中空管2b内に集水された前記汚染
された土中水、または余剰の不溶化用の水溶液は、揚水
されて連通管8,コック7を経て集水導管13に送ら
れ、更にゲートバルブ17を介して気水分離槽12に流
入する。そして、前記気水分離槽12によって空気と分
離された前記水溶液は、排水ポンプ18によって排水連
結管19を介して沈殿槽20に流入し、該沈殿槽20に
おいて沈降剤の処理によって水溶液中に含有する微細な
土粒子等と分離され、水溶液のみは送水ポンプ21によ
って送水連結管22を介して吸着槽23に送水される。
前記吸着槽23内において水溶液中に混入している重金
属類の極めて微細な粒子は吸着処理され、該処理後の水
溶液は給水ポンプ24によって給水連結管25を介して
給水槽5に入り、水溶液の濃度が調整されて再度ゲート
バルブ16,送水導管6,コック7,連通管8、陽極側
の各中空管2aへと送水されて、以下前記同様のサイク
ルを繰返しながら、土中の重金属類の不溶化の作業が繰
返されるのである。
The contaminated soil water collected in each hollow tube 2b or the surplus insolubilizing aqueous solution is pumped and sent to the water collecting conduit 13 through the communicating pipe 8 and the cock 7. Further, it flows into the steam separation tank 12 via the gate valve 17. Then, the aqueous solution separated from the air by the air-water separation tank 12 flows into the settling tank 20 by the drainage pump 18 through the drainage connecting pipe 19, and is contained in the aqueous solution by the treatment of the settling agent in the settling tank 20. The water solution is separated from the fine soil particles and the like, and only the aqueous solution is supplied to the adsorption tank 23 by the water supply pump 21 through the water supply connecting pipe 22.
In the adsorption tank 23, extremely fine particles of heavy metals mixed in the aqueous solution are adsorbed, and the treated aqueous solution enters the water supply tank 5 via the water supply connecting pipe 25 by the water supply pump 24, and the The concentration is adjusted and water is again fed to the gate valve 16, the water supply conduit 6, the cock 7, the communication pipe 8 and each hollow pipe 2a on the anode side, and while repeating the same cycle as described above, the heavy metals in the soil are removed. The process of insolubilization is repeated.

【0016】前記電気浸透現象の発生している土壌中で
は、陽極の領域は酸性領域となり、陰極の領域はアルカ
リ領域になるため、両極間にある物質には酸化還元の反
応を生じ、この現象のため土壌中の重金属類にも影響が
認められ、電気浸透現象によって浸透した硫化ナトリウ
ムまたは硫酸鉄の水溶液との化学的反応に強い効果を与
える。このために、長い通電時間の場合は時々各管列
A,Bの極性を自由に随時転換をして効率的に汚染土壌
中の重金属類を不溶化することが必要となり、この場合
は図示していない転換装置により、極性を転換すると同
時に、陽極側の各中空管への硫化ナトリウムまたは硫酸
鉄の水溶液の注入は中止して、電気的作用による酸化還
元の作用のみを汚染土壌1中に作用させる。
In the soil in which the electroosmosis phenomenon occurs, the area of the anode becomes the acidic area and the area of the cathode becomes the alkaline area, so that the substance between both electrodes undergoes a redox reaction, and this phenomenon occurs. Therefore, heavy metals in soil are also affected, and it exerts a strong effect on the chemical reaction with the aqueous solution of sodium sulfide or iron sulfate infiltrated by the electroosmosis phenomenon. For this reason, in the case of a long energization time, it is sometimes necessary to freely change the polarities of the tube rows A and B at any time to efficiently insolubilize heavy metals in the contaminated soil. In this case, it is shown in the figure. At the same time, the polarity is changed by the conversion device, and at the same time, the injection of the aqueous solution of sodium sulfide or iron sulfate into each hollow tube on the anode side is stopped, and only the action of redox due to the electrical action acts on the contaminated soil 1. Let

【0017】前記サイクルを繰返して適宜水質検査を行
い所定の水質基準値に達すると、これら一連の作業が停
止され、汚染土壌中の重金属類の不溶化処理が完了す
る。
When the water quality inspection is appropriately performed by repeating the above cycle and a predetermined water quality reference value is reached, these series of operations are stopped and the insolubilization treatment of heavy metals in the contaminated soil is completed.

【0018】[0018]

【発明の効果】本発明は上述のようであるから、従来の
土の置き換え等のように、他の作業に影響を与えること
なく、原位置のまま汚染土壌の重金属類を不溶化するこ
とが可能であり、また汚染土壌の区域部分に、その汚染
の深度より深く陽極用および陰極用の中空管を貫入設置
し、この中空管に囲まれた区域の範囲のみの土壌に電気
浸透現象が作用するので、この範囲以外の地域まで汚染
物質を流動させることはない。更に、本発明によれば汚
染土壌の掘削、混合、搬出入が不要であるため、汚染土
の飛散、作業による騒音がなく、作業者および周辺住民
への二次的公害がないという優れた効果を奏するのであ
る。
Since the present invention is as described above, it is possible to insolubilize heavy metals in contaminated soil in its original position without affecting other operations such as conventional soil replacement. In addition, hollow tubes for anode and cathode are installed deeper than the depth of pollution in the area of contaminated soil, and electroosmosis phenomenon occurs only in the area of the area surrounded by this hollow tube. As it works, it does not flow pollutants to areas outside this range. Further, according to the present invention, since excavation, mixing, and carrying-in / out of contaminated soil are unnecessary, there is no scattering of contaminated soil, no noise due to work, and no secondary pollution to workers and neighboring residents. Is played.

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

【図1】本発明装置全体の概略平面図である。FIG. 1 is a schematic plan view of the entire device of the present invention.

【図2】本発明装置の縦断面図である。FIG. 2 is a vertical cross-sectional view of the device of the present invention.

【符号の説明】[Explanation of symbols]

1 汚染土壌、 2 中空管、 2a 陽極側の中空
管、 2b 陰極側の中空管、 3 通水孔、 5 給
水槽、 6 送水導管、 7 コック、 8 連通管、
9 直流電源、 12 気水分離槽、 13 集水導
管、 16,17ゲートバルブ、 20 沈殿槽、 2
6 溶解槽、 A 陽極側の管列、 B陰極側の管列。
1 contaminated soil, 2 hollow tubes, 2a hollow tubes on the anode side, 2b hollow tubes on the cathode side, 3 water holes, 5 water supply tanks, 6 water supply conduits, 7 cocks, 8 communication tubes,
9 DC power source, 12 steam separation tank, 13 water collection conduit, 16, 17 gate valve, 20 sedimentation tank, 2
6 Dissolution tank, A anode side tube row, B cathode side tube row.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 陽極と陰極の電極を兼ねた多数の通水孔
を穿設した複数本の中空管を、陽極用と陰極用に対向し
て管列を形成して汚染土壌の深さより深く貫入設置する
と共に、前記陽極と陰極との極性の転換ができるように
設置する一方、前記各電極に直流電流を通電して直流電
圧を負荷し、陽極管中に硫化ナトリウムまたは硫酸鉄の
水溶液を注入して、両極間の汚染土壌中に作用する電気
浸透現象を利用して前記陽極管から通水孔を介して前記
水溶液を吐出して汚染土壌中に均等に浸透させて、該水
溶液を汚染土壌中の重金属類に接触させ不溶化の化学的
反応を生ぜしめて、汚染された土中水、または余剰の不
溶化用の水溶液を通水孔を介して陰極管に集水し、然る
後水質検査を行い、所定の水質基準値に達するまで、前
記水溶液の陽極管からの吐出、汚染土壌への浸透および
陰極管への集水を繰返すことを特徴とする汚染土壌中の
重金属類を不溶化する方法。
1. A plurality of hollow tubes having a large number of water holes that also serve as electrodes for an anode and a cathode are formed to form a row of tubes facing each other for the anode and the cathode, and Along with deeply penetrating the installation, the anode and the cathode are installed so that the polarity can be switched, while a DC current is applied to each of the electrodes to apply a DC voltage, and an aqueous solution of sodium sulfide or iron sulfate in the anode tube. Is injected, and by utilizing the electroosmosis phenomenon that acts on the contaminated soil between the two electrodes, the aqueous solution is discharged from the anode tube through the water passages and uniformly permeated into the contaminated soil, By contacting heavy metals in contaminated soil and causing insolubilization chemical reaction, contaminated soil water or excess insolubilization aqueous solution is collected in the cathode tube through the water hole, and then water quality Perform an inspection and check whether the above-mentioned aqueous solution anode tube A method for insolubilizing heavy metals in contaminated soil, characterized by repeating discharge from the contaminated soil, permeation into the contaminated soil, and water collection to the cathode tube.
【請求項2】 陽極と陰極の電極を兼ねた多数の通水孔
を穿設した複数本の中空管を、陽極用と陰極用に対向し
て管列を形成して汚染土壌の深さより深く貫入設置する
と共に、前記陽極と陰極との極性の転換ができるように
設置する一方、前記陽極管には、給水槽にゲートバルブ
を介して一端を連通した送水導管が連通固定されると共
に、前記陰極管には、気水分離槽にゲートバルブを介し
て一端を連通した集水導管が連通固定され、更に前記気
水分離槽と給水槽間には沈殿槽および吸着槽が配設され
ると共に、前記給水槽に硫化ナトリウムまたは硫酸鉄を
適宜の濃度に調整して送水する溶解槽を連通固定し、更
に直流電流の陽極側に前記陽極管を接続し、且つ前記直
流電流の陰極側に前記陰極管を接続したことを特徴とす
る汚染土壌中の重金属類を不溶化する装置。
2. A plurality of hollow tubes having a large number of water passage holes which also serve as electrodes of an anode and a cathode are formed to form a row of tubes facing each other for the anode and the cathode, and Along with deeply penetrating the installation, the anode and the cathode are installed so that the polarity can be switched, while the anode tube is connected and fixed to a water supply conduit having one end connected to a water tank through a gate valve. A water collecting conduit, one end of which communicates with a gas / water separation tank via a gate valve, is connected and fixed to the cathode tube, and a precipitation tank and an adsorption tank are further disposed between the water / water separation tank and the water supply tank. Along with fixing the dissolution tank for sending water by adjusting the concentration of sodium sulfide or iron sulfate to an appropriate concentration in the water supply tank, further connecting the anode tube to the anode side of direct current, and to the cathode side of the direct current. Heavy metal in contaminated soil characterized by connecting the cathode tube A device to insolubilize genera.
JP4269513A 1992-09-11 1992-09-11 Method and apparatus for insolubilizing heavy metals in contaminated soil Expired - Fee Related JP2524290B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4269513A JP2524290B2 (en) 1992-09-11 1992-09-11 Method and apparatus for insolubilizing heavy metals in contaminated soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4269513A JP2524290B2 (en) 1992-09-11 1992-09-11 Method and apparatus for insolubilizing heavy metals in contaminated soil

Publications (2)

Publication Number Publication Date
JPH06158635A JPH06158635A (en) 1994-06-07
JP2524290B2 true JP2524290B2 (en) 1996-08-14

Family

ID=17473457

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4269513A Expired - Fee Related JP2524290B2 (en) 1992-09-11 1992-09-11 Method and apparatus for insolubilizing heavy metals in contaminated soil

Country Status (1)

Country Link
JP (1) JP2524290B2 (en)

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* Cited by examiner, † Cited by third party
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JP2006342961A (en) * 2005-05-09 2006-12-21 Nippon Shiigatekku Kk Piping connection structure
CN110293125A (en) * 2019-04-28 2019-10-01 南通大学 It is a kind of original position electro reclamation and reinforce ultra-soft Polluted Soil device and method

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JP4718585B2 (en) * 2008-07-07 2011-07-06 登坂 卓也 Treatment method of contaminated soil
JP6621138B2 (en) * 2016-02-01 2019-12-18 国立大学法人秋田大学 Decontamination equipment and decontamination method for contaminated soil
CN117619874B (en) * 2023-12-28 2025-12-26 常州大学 An apparatus and method for in-situ remediation of organically contaminated soil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006342961A (en) * 2005-05-09 2006-12-21 Nippon Shiigatekku Kk Piping connection structure
CN110293125A (en) * 2019-04-28 2019-10-01 南通大学 It is a kind of original position electro reclamation and reinforce ultra-soft Polluted Soil device and method

Also Published As

Publication number Publication date
JPH06158635A (en) 1994-06-07

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