JPH08257570A - Purification of polluted underground water - Google Patents
Purification of polluted underground waterInfo
- Publication number
- JPH08257570A JPH08257570A JP7093138A JP9313895A JPH08257570A JP H08257570 A JPH08257570 A JP H08257570A JP 7093138 A JP7093138 A JP 7093138A JP 9313895 A JP9313895 A JP 9313895A JP H08257570 A JPH08257570 A JP H08257570A
- Authority
- JP
- Japan
- Prior art keywords
- iron powder
- underground water
- pit
- polluted underground
- powder bed
- 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
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Water Treatment By Sorption (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、土壌中を流れる地下水
の浄化方法に関し、更に詳しくは地下水に含有される重
金属や有機塩素化合物を鉄粉の作用により一括除去する
ことを目的とする。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying groundwater flowing in soil, and more specifically, it aims to remove heavy metals and organic chlorine compounds contained in groundwater all together by the action of iron powder.
【0002】[0002]
【従来の技術】従来、重金属等で汚染された土壌を処理
する方法としては、汚染土壌そのものを固化あるいは不
溶化処理して埋め立てを行う埋め立て処分方法や、熱処
理を行って汚染物質が気化したガスを除去することによ
り無害化する熱処理方法が一般的に実施されている。2. Description of the Related Art Conventionally, as a method for treating soil contaminated with heavy metals or the like, a landfill disposal method in which contaminated soil itself is solidified or insolubilized for landfilling, or a gas in which a pollutant is vaporized by heat treatment is used. A heat treatment method for making the material harmless by removing it is generally practiced.
【0003】その他特殊な処理方法として、汚染土壌を
分級して重金属を多く含有する細粒を水等で洗浄する洗
浄分級方法や、土壌中に生息するバクテリアを利用して
汚染物質を処理する生物処理方法も知られている。As other special treatment methods, a cleaning and classification method of classifying contaminated soil and washing fine particles containing a large amount of heavy metals with water or the like, and an organism for treating pollutants by utilizing bacteria inhabiting the soil The processing method is also known.
【0004】以上のように対象とする汚染物質の種類に
よって処理方法も異なるように、これらの方法はいずれ
も一長一短があった。As described above, each treatment method has advantages and disadvantages because the treatment method varies depending on the type of the pollutant to be treated.
【0005】上記、固定安定化法は、無機系の汚染物質
が対象であるが、長期間に渡ると雨水等の作用による浸
出等によりその維持は困難となり、一方、熱処理方法は
有機汚染物質への適用には適しているものの、特にアル
カリ塩による汚染土壌の処理には不適である上、無機系
の重金属に対しても水銀等2〜3種類のものにしか適用
できなかった。The above-mentioned fixing and stabilizing method is intended for inorganic pollutants, but it is difficult to maintain it for a long period of time due to leaching due to the action of rainwater, etc. However, it is not suitable for treating contaminated soil with an alkali salt, and it can be applied only to a few kinds of inorganic heavy metals such as mercury.
【0006】更に、洗浄分級方法も非揮発性物質等には
対応が可能であるが、土壌の掘り出しや汚染物質が深層
に及んでいる場合には採掘費がかかり不適であり、バク
テリアによる生物処理方法も、反応時間が長く更に単鎖
構造の炭水化物に対しては限界があり、無機物に対して
は殆ど適用が不可であった。Further, the cleaning and classification method can also deal with non-volatile substances, but when excavating the soil or when the pollutant extends to a deep layer, the mining cost is unsuitable and the biological treatment by bacteria is not suitable. The method also has a long reaction time and has a limit for carbohydrates having a single-chain structure, and is hardly applicable to inorganic substances.
【0007】上記土壌中の汚染物質は、その後雨水等に
より地下水脈に混入して井戸水等の水資源を害すること
になるため、汚染地下水を揚水して重金属分を除去する
排水処理方法や、揚水した地下水を爆気しながら抽出す
る抽出方法も知られているが、この方法は、揚水時の電
力費や抽出費等のコストがかかるという問題を有してい
た。[0007] Since the pollutants in the soil are then mixed with groundwater veins by rainwater or the like to damage water resources such as well water, a contaminated groundwater is pumped up to remove heavy metals, and a drainage treatment method or pumping There is also known an extraction method for extracting the groundwater while detonating it, but this method has a problem that it costs electricity such as electric power and extraction cost at the time of pumping.
【0008】[0008]
【発明が解決しようとする課題】上記のように汚染土壌
を直接処理する方法は、汚染源が狭い範囲であればコス
トを安く処理できる方法であるが、長期に渡って広い範
囲で汚染された場合には不向きな手法である。The method for directly treating contaminated soil as described above is a method that can be processed at a low cost if the pollution source is in a narrow range, but when it is contaminated in a wide range over a long period of time. Is not suitable for.
【0009】従って本発明は、汚染された地下水を処理
対象として、安価に且つ恒久的に重金属分あるいは有機
塩素化合物を一括除去できる新規な処理法の開発を目的
とする。Therefore, an object of the present invention is to develop a novel treatment method for treating contaminated groundwater at a low cost and capable of permanently removing heavy metal components or organic chlorine compounds collectively.
【0010】[0010]
【課題を解決するための手段】本発明者等は斯かる課題
を解決するために鋭意研究したところ、地下水中に含有
される重金属分にも、また有機塩素化合物の除去にも安
価な鉄粉を使用できることを見い出し本発明法を提供す
ることができた。Means for Solving the Problems The inventors of the present invention have conducted extensive studies to solve such problems, and found that iron powder which is inexpensive for removing heavy metals contained in groundwater and also for removing organic chlorine compounds. It was possible to provide the method of the present invention by discovering that
【0011】すなわち本発明法は、汚染地下水路面まで
ピットを掘削した後、該ピット底面に鉄粉層を設け、上
記汚染地下水をpH2〜7の範囲内で通過せしめること
により、鉄粉で重金属または有機塩素化合物の少なくと
も一種類以上を除去することを特徴とする汚染地下水の
浄化方法である。That is, according to the method of the present invention, after excavating a pit to the contaminated groundwater road surface, an iron powder layer is provided on the bottom surface of the pit, and the contaminated groundwater is allowed to pass within a pH range of 2 to 7, whereby iron powder is added to the heavy metal or A method for purifying contaminated groundwater, which comprises removing at least one kind of organic chlorine compound.
【0012】[0012]
【作用】本発明法によれば、地下水面まで掘削したピッ
ト底面に鉄粉を層状に配置することによって、その鉄粉
層を通過する汚染地下水に含有される汚染物質(主とし
て有機塩素化合物および無機系重金属)が鉄粉中で分解
あるいは吸着、置換等の反応を受けて無害化される。According to the method of the present invention, by arranging iron powder in layers on the bottom surface of the pit excavated to the water table, pollutants (mainly organic chlorine compounds and inorganic compounds) contained in the contaminated ground water passing through the iron powder layer. Heavy metal) is detoxified by being decomposed or adsorbed in iron powder, and subjected to reactions such as substitution.
【0013】このうち有機塩素化合物の分解のメカニズ
ムは解明されていないが、鉄により還元されるものと推
察される。一方、無機系重金属と鉄粉との反応は、還元
反応、置換反応、吸着反応、均一化反応、中和反応、共
沈反応等が各重金属イオン毎に起こって鉄粉に吸着され
る。Of these, the mechanism of decomposition of the organic chlorine compound has not been clarified, but it is presumed that it is reduced by iron. On the other hand, in the reaction between the inorganic heavy metal and the iron powder, a reduction reaction, a substitution reaction, an adsorption reaction, a homogenization reaction, a neutralization reaction, a coprecipitation reaction, etc. occur for each heavy metal ion and are adsorbed on the iron powder.
【0014】尚、一般に地下水の移動は1〜1.5m/
日の速度であるとされ、本発明で処理対象とする汚染地
下水も同程度の速度であると判断されることから、本発
明法では鉄粉層中をSV=1となるように汚染地下水を
通過させた。Generally, the movement of groundwater is 1 to 1.5 m /
The contaminated groundwater to be treated in the present invention is judged to have the same speed as the daily speed, so that the contaminated groundwater in the iron powder layer is SV = 1 in the method of the present invention. Let it pass.
【0015】以下、実施例をもって本発明を詳細に説明
するが、本発明法はこれらに限定されるものではない。The present invention is described in detail below with reference to examples, but the method of the present invention is not limited to these.
【0016】[0016]
【実施例1】図1に示すように汚染源1から流出した地
下水面までピットを掘削した後、該ピット内に鉄粉層を
形成した。Example 1 As shown in FIG. 1, a pit was excavated up to the groundwater surface flowing out from the pollution source 1, and then an iron powder layer was formed in the pit.
【0017】鉄粉層を通過させる前の上流側の汚染地下
水を分析したところ、pH4.9であり、Cr6+0.7
6mg/l、T・Cr1.2mg/l、Ni8.5mg/lの割合で
各種重金属を含有していた。When the contaminated groundwater on the upstream side before being passed through the iron powder layer was analyzed, it was found to have a pH of 4.9 and Cr 6+ 0.7.
Various heavy metals were contained in the proportions of 6 mg / l, T · Cr 1.2 mg / l and Ni 8.5 mg / l.
【0018】該汚染地下水をSV=1の速度で鉄粉層中
を通過させた後の地下水を採取して分析したところ、p
H5.5、Cr6+不検出、T・Cr不検出、Ni0.1
mg/lと重金属を十二分に除去できた。When the contaminated groundwater was passed through the iron powder bed at a speed of SV = 1, groundwater was collected and analyzed.
H5.5, Cr 6+ not detected, T / Cr not detected, Ni0.1
It was possible to remove mg / l and heavy metals more than enough.
【0019】[0019]
【参考例1】重金属含有排水としてpH5.5、C
u2+、Cd2+、Zn2+を各々50mg/l含有する排水を、
実施例1における鉄粉層形成の条件と実質的同条件に充
填したカラム中を通過させたところ、通過後の濾液は、
pH6.6、Cd0.01mg/l、Cu0.01mg/l、Z
n0.01mg/lであり、この程度の汚染排水にも本発明
法を適用できることを確認した。[Reference Example 1] pH 5.5, C as heavy metal-containing wastewater
Waste water containing 50 mg / l each of u 2+ , Cd 2+ and Zn 2+ ,
When passing through a column packed under substantially the same conditions as the iron powder layer forming conditions in Example 1, the filtrate after passing was
pH 6.6, Cd 0.01 mg / l, Cu 0.01 mg / l, Z
It was n0.01 mg / l, and it was confirmed that the method of the present invention can be applied to contaminated wastewater of this level.
【0020】[0020]
【実施例2】トリクロロエチレン、テトラクロロエチレ
ンを各々5mg/l含有する他の汚染地下水を対象とした以
外は、実施例1に示すとほぼ同一の条件下で、鉄粉処理
したところ、鉄粉層中を通過後の地下水は、トリクロロ
エチレン、テトラクロロエチレンが各々0.1mg/l以下
となっており、本発明法は有機塩素化合物除去にも適し
ていることが確認できた。[Example 2] Iron powder was treated under substantially the same conditions as in Example 1 except that the other contaminated groundwater containing 5 mg / l each of trichlorethylene and tetrachloroethylene was targeted. The groundwater after passing contained trichlorethylene and tetrachloroethylene at 0.1 mg / l or less, respectively, and it was confirmed that the method of the present invention is also suitable for removing organic chlorine compounds.
【0021】[0021]
【発明の効果】本発明法は上述のように安価な鉄粉を用
い、汚染地下水の重金属分や有機塩素化合物を一括除去
できる処理方法であり、ある期間経過後に鉄粉を入れ替
えることによって恒久的に汚染地下水を浄化できるもの
である。As described above, the method of the present invention is a treatment method capable of collectively removing heavy metal components and organic chlorine compounds of contaminated groundwater by using inexpensive iron powder as described above, and by permanently replacing iron powder after a certain period of time It can purify contaminated groundwater.
【図1】本発明法の処理システムを説明する概略図であ
る。FIG. 1 is a schematic diagram illustrating a processing system of the method of the present invention.
1 汚染源 2 地下水 3 ピット 4 鉄粉層 5 土中 1 Pollution source 2 Groundwater 3 Pit 4 Iron powder layer 5 Underground
Claims (1)
該ピット底面に鉄粉層を設け、上記汚染地下水をpH2
〜7の範囲内で通過せしめることにより、鉄粉で、重金
属または有機塩素化合物の少なくとも一種類以上を除去
することを特徴とする汚染地下水の浄化方法。1. After excavating a pit to the contaminated water table,
An iron powder layer is provided on the bottom of the pit, and the contaminated groundwater is adjusted to pH 2
A method for purifying contaminated groundwater, characterized in that iron powder removes at least one or more of heavy metals or organic chlorine compounds by allowing the water to pass through within the range of 7 to 7.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09313895A JP3708160B2 (en) | 1995-03-27 | 1995-03-27 | Purification method of contaminated groundwater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP09313895A JP3708160B2 (en) | 1995-03-27 | 1995-03-27 | Purification method of contaminated groundwater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08257570A true JPH08257570A (en) | 1996-10-08 |
JP3708160B2 JP3708160B2 (en) | 2005-10-19 |
Family
ID=14074173
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP09313895A Expired - Lifetime JP3708160B2 (en) | 1995-03-27 | 1995-03-27 | Purification method of contaminated groundwater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3708160B2 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5858267A (en) * | 1996-10-11 | 1999-01-12 | Nec Corporation | Method for treating chlorinated organic compound |
US6497795B1 (en) | 1998-12-16 | 2002-12-24 | Canon Kabushiki Kaisha | Method and apparatus for decomposing gaseous aliphatic hydrocarbon halide compound |
KR100380547B1 (en) * | 2000-11-16 | 2003-04-26 | 한라산업개발 주식회사 | Remediation method of the contaminated ground by injecting reactive material |
US6596190B1 (en) | 1999-07-29 | 2003-07-22 | Hazama Corp. | Remediation agent for contaminated soil and method for the remediation of soil |
US6616815B2 (en) | 1998-06-22 | 2003-09-09 | Canon Kabushiki Kaisha | Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same |
US6699370B2 (en) | 2000-06-16 | 2004-03-02 | Canon Kabushiki Kaisha | Process and system for decomposing pollutants |
US7018514B2 (en) | 2001-11-12 | 2006-03-28 | Canon Kabushiki Kaisha | Method and apparatus for processing substances to be decomposed |
US7163615B2 (en) | 2001-11-12 | 2007-01-16 | Canon Kabushiki Kaisha | Method of treating substance to be degraded and its apparatus |
JP2008149241A (en) * | 2006-12-15 | 2008-07-03 | Kurita Water Ind Ltd | Purifying method of ground water |
-
1995
- 1995-03-27 JP JP09313895A patent/JP3708160B2/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5858267A (en) * | 1996-10-11 | 1999-01-12 | Nec Corporation | Method for treating chlorinated organic compound |
US6616815B2 (en) | 1998-06-22 | 2003-09-09 | Canon Kabushiki Kaisha | Method of decomposing halogenated aliphatic hydrocarbon compounds or aromatic compounds and apparatus to be used for the same as well as method of clarifying exhaust gas and apparatus to be used for the same |
US6497795B1 (en) | 1998-12-16 | 2002-12-24 | Canon Kabushiki Kaisha | Method and apparatus for decomposing gaseous aliphatic hydrocarbon halide compound |
US7163665B2 (en) | 1998-12-16 | 2007-01-16 | Canon Kabushiki Kaisha | Apparatus for decomposing gaseous aliphatic hydrocarbon halide compounds |
US6596190B1 (en) | 1999-07-29 | 2003-07-22 | Hazama Corp. | Remediation agent for contaminated soil and method for the remediation of soil |
US6699370B2 (en) | 2000-06-16 | 2004-03-02 | Canon Kabushiki Kaisha | Process and system for decomposing pollutants |
KR100380547B1 (en) * | 2000-11-16 | 2003-04-26 | 한라산업개발 주식회사 | Remediation method of the contaminated ground by injecting reactive material |
US7018514B2 (en) | 2001-11-12 | 2006-03-28 | Canon Kabushiki Kaisha | Method and apparatus for processing substances to be decomposed |
US7163615B2 (en) | 2001-11-12 | 2007-01-16 | Canon Kabushiki Kaisha | Method of treating substance to be degraded and its apparatus |
JP2008149241A (en) * | 2006-12-15 | 2008-07-03 | Kurita Water Ind Ltd | Purifying method of ground water |
Also Published As
Publication number | Publication date |
---|---|
JP3708160B2 (en) | 2005-10-19 |
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