JP2002177940A - Method of cleaning contaminated soil - Google Patents

Method of cleaning contaminated soil

Info

Publication number
JP2002177940A
JP2002177940A JP2000383381A JP2000383381A JP2002177940A JP 2002177940 A JP2002177940 A JP 2002177940A JP 2000383381 A JP2000383381 A JP 2000383381A JP 2000383381 A JP2000383381 A JP 2000383381A JP 2002177940 A JP2002177940 A JP 2002177940A
Authority
JP
Japan
Prior art keywords
soil
contaminated
distillation
contaminated soil
treatment
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.)
Pending
Application number
JP2000383381A
Other languages
Japanese (ja)
Inventor
Ryosuke Shiratani
良輔 白谷
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.)
ECO UP KK
Original Assignee
ECO UP KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ECO UP KK filed Critical ECO UP KK
Priority to JP2000383381A priority Critical patent/JP2002177940A/en
Publication of JP2002177940A publication Critical patent/JP2002177940A/en
Pending legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To separate and remove hardly decomposable hazardous materials, such as PCBs or PCDDs(polychlorinated-dibenzo-p-dioxins) and the like without impairing the characteristics of the soil contaminated by the hardly decomposable hazardous materials and to reuse the treated soil as the farming land. SOLUTION: The hardly decomposable hazardous materials are separated and removed by putting the contaminated soil into a distillation flask and adding water thereto, then subjecting the soil to steam distillation.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明が属する技術分野】本発明は、有機性有害物質等
により汚染された土壌の浄化方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying soil contaminated with organic harmful substances and the like.

【0002】[0002]

【従来の技術】従来、有害物質等により汚染された土壌
は、これをセメント等の固化剤により有害物質を不溶化
した後、地中に埋め込み処分されるか、重炭酸ナトリウ
ムなどの薬品を添加後、加熱分解か、加温により揮発性
有害物質を揮散・脱離させる方法、あるいは焼成炉で焼
却・分解処理する方法が一般的であった。
2. Description of the Related Art Conventionally, soil contaminated with harmful substances and the like is insolubilized with a solidifying agent such as cement and then buried in the ground, or after adding a chemical such as sodium bicarbonate. In general, a method in which volatile harmful substances are volatilized and desorbed by heat decomposition or heating, or a method in which incineration and decomposition treatment is performed in a baking furnace is common.

【0003】[0003]

【発明が解決しようとする課題】従来の浄化処理方法で
は処理後の土壌の性状が大きく変化するか、処理に用い
た薬品が残存するか、あるいは高沸点の難分解性有機塩
素化合物が脱離できない等の問題点があった。このた
め、処理後の土壌を緑農地土壌に再利用することができ
なかった。本発明は、汚染土壌を浄化するとともに、浄
化処理土壌を緑農地に再利用することを目的にしたもの
である。
In the conventional purification treatment method, the properties of the soil after the treatment significantly change, the chemicals used for the treatment remain, or the high-boiling-point hardly decomposable organic chlorine compound is desorbed. There were problems such as inability to do so. For this reason, the soil after the treatment could not be reused as green farmland soil. An object of the present invention is to purify contaminated soil and reuse purified soil for green farmland.

【0004】[0004]

【課題を解決するための手段】本発明は、汚染土壌を水
蒸気蒸留処理することにより、100゜Cの温度で、土
壌の性状を大きく損なわずに、高沸点のPCB、ダイオキ
シン類および難分解性有機化合物を汚染土壌より分離除
去することができた。
SUMMARY OF THE INVENTION The present invention provides a high-boiling-point PCB, dioxins and a hard-to-decompose material by subjecting contaminated soil to steam distillation at a temperature of 100 ° C. without significantly impairing the properties of the soil. Organic compounds could be separated and removed from the contaminated soil.

【0005】なお、本発明でいう汚染土壌とは、有害物
質等を何らかの理由で、工場敷地、一般居住地又は公共
用地に、漏洩、散布した事により,それらの物質によっ
て汚染せしめた土地、農耕地、土砂、水底土砂および汚
泥類などを指す。本発明でいう有害物質等とは、PCB,コ
プラナーPCB,ダイオキシン類、揮発性有機化合物、残留
農薬、環境ホルモンなどの難分解性有機化合物質を指
す。
[0005] The term "contaminated soil" as used in the present invention refers to lands or agricultural soils that are contaminated by toxic substances or the like when they are leaked or sprayed onto factory premises, general residential areas or public lands for some reason. It refers to ground, earth and sand, submarine sediment, sludge, etc. The harmful substances and the like in the present invention refer to hardly decomposable organic compounds such as PCB, coplanar PCB, dioxins, volatile organic compounds, residual agricultural chemicals, and environmental hormones.

【0006】本発明において用いる汚染土壌は、港湾、
湖沼、河川、運河、水路などの底部付近から浚渫された
浚渫土砂、塵芥焼却場周辺の汚染土壌、焼却にともなっ
て発生する飛灰、焼却残灰、汚泥類あるいは浄水場から
発生する浄水ケーキである。これらの汚染土壌は、必要
により、脱水機などの物理的手段を用いて、事前に水分
を減少させてから用いるか、飛灰などの場合は適当に加
水してから用いる。さらに、事前にスラリー状にして、
機械攪拌あるいは超音波処理することも、蒸留分離の効
率をあげるのに有効である。また、目的とする除去物資
により、水蒸気蒸留を行う前に、酸又はアルカリでpH
を調整すると、蒸留分離が容易におこなえるので有効で
ある。
The contaminated soil used in the present invention is a harbor,
Dredged soil and dredged from the bottom of lakes, rivers, canals, waterways, etc. is there. If necessary, these contaminated soils may be used after reducing the water content in advance using a physical means such as a dehydrator, or may be used after appropriately adding water in the case of fly ash or the like. In addition, make a slurry in advance,
Mechanical stirring or ultrasonic treatment is also effective for increasing the efficiency of the distillation separation. Further, depending on the target substance to be removed, the pH is adjusted with an acid or alkali before steam distillation.
Is effective because distillation separation can be easily performed.

【0007】ここで用いる添加剤は、特に制限はなく、
工業用薬品でよく、多少の不純物を含んでいても差し支
えない。
The additives used here are not particularly limited.
It may be an industrial chemical and may contain some impurities.

【0008】蒸留処理に際して、添加する水の量は汚染
土壌1重量部に対し、約1〜10部が好ましく、さらに
好ましくは約3〜5部である。これより添加水の比率が
多いと蒸留エネルギー効率が低下し、少ないと、混合攪
拌が十分でなく、有害物質の除去効率が低下する。
[0008] In the distillation treatment, the amount of water to be added is preferably about 1 to 10 parts, more preferably about 3 to 5 parts per part by weight of the contaminated soil. If the ratio of the added water is higher than this, the distillation energy efficiency decreases, and if the ratio is lower, the mixing and stirring are not sufficient, and the efficiency of removing harmful substances decreases.

【0009】有害物質を蒸留分離するために必要な蒸留
時間は、各種の条件で一概には規定できないが、約5分
から60分である。PCBなどの高沸点化合物は10分間
の蒸留処理で、約60%以上が除去されるが、それ以降
は、徐々にしか留出されない。
[0009] The distillation time required to separate harmful substances by distillation cannot be specified unconditionally under various conditions, but is about 5 to 60 minutes. About 60% or more of high-boiling compounds such as PCBs are removed by a distillation treatment for 10 minutes, but thereafter, only a small amount is distilled out gradually.

【0010】上記のように蒸留処理することにより、汚
染土壌に残存する大部分の有害有機化合物が除去され
る。同時に、アンモニアあるいは硫化水素のような悪臭
成分もほぼ完全に除去することができる。この事によ
り、汚染土壌が浄化され、農耕地土壌あるいは一般居住
地土壌として、再利用できるようになる。
Most of the harmful organic compounds remaining in the contaminated soil are removed by the distillation treatment as described above. At the same time, malodorous components such as ammonia or hydrogen sulfide can be almost completely removed. As a result, the contaminated soil is purified and can be reused as agricultural soil or general residential soil.

【0011】[0011]

【実施例】図―1は、本発明の実験に用いた水蒸気蒸留
装置の一例である。
FIG. 1 shows an example of a steam distillation apparatus used in the experiment of the present invention.

【0012】以下に、参考例、実施例および比較例によ
り本発明を説明する。 (参考例1)汚染土壌の性状例 PCBおよびコプラナーPCBが一定程度残存する港湾の水底
土砂(浚渫土)の例を示すと、その性状は表―1のとお
りである。
Hereinafter, the present invention will be described by reference examples, examples and comparative examples. (Reference Example 1) Properties of contaminated soil Table 1 shows an example of seabed sediment (dredge soil) in a port where a certain amount of PCB and coplanar PCB remain.

【0013】[0013]

【表―1】表―1 港湾水底土砂の性状 [Table-1] Table-1 Properties of the bottom of the port water

【0014】表―1のように、港湾水底土砂(浚渫土)
の場合は、ダイオキシン類(ダイオキシンおよびジベン
ゾフラン)は居住地土壌基準(1000pg/g)の5
分の1以下であるが、コプラナーPCBが110pg−TEQ
/kg乾土残存している。同時に、PCBも約5.1mg/
kg乾土残存している。アンモニア性窒素、全硫化物の
ほか、亜鉛も土壌管理基準(120mg/kg乾土)を
上回っている。このため、農耕地土壌には適さない。
[0014] As shown in Table 1, the bottom of the harbor water bottom (dredge soil)
In the case of, the dioxins (dioxin and dibenzofuran) are 5% of the standard value of the residential soil (1000 pg / g).
1/10 or less, but coplanar PCB is 110pg-TEQ
/ kg dry soil remains. At the same time, about 5.1 mg /
kg of dry soil remains. In addition to ammonia nitrogen and total sulfide, zinc also exceeds the soil management standard (120 mg / kg dry soil). For this reason, it is not suitable for farmland soil.

【0015】(実施例1)参考例―1の港湾水底土砂
(浚渫土)を予め、5mmのふるいを通過させ、レキお
よび粗大ゴミを除去したのち、乾土当たり、20gを三
角フラスコに取る。これに0.1モル/lの塩酸100
mlをこれに加え、30分間室温で振とう後、遠心分離
(3000rpm、5分間)し、上澄液を別のビーカー
に集め、残土を100mlの水で洗浄する。洗浄残土に
0.1モル/lの消石灰液50mlを添加した後、水蒸
気蒸留を行った。水蒸気発生速度は5g/分で15分間
水蒸気蒸留処理を行った。処理後の残土、留出液中のPC
B等の含有量は表―2のとおりである。
(Embodiment 1) The bottom of the port water (dredged soil) of Reference Example-1 was passed through a 5 mm sieve in advance to remove rake and coarse dust, and then 20 g per dry soil was placed in an Erlenmeyer flask. 0.1 mol / l hydrochloric acid 100
The mixture is shaken at room temperature for 30 minutes, centrifuged (3000 rpm, 5 minutes), the supernatant is collected in a separate beaker, and the remaining soil is washed with 100 ml of water. After 50 ml of a 0.1 mol / l slaked lime solution was added to the washed residue, steam distillation was performed. The steam distillation rate was 5 g / min for 15 minutes. Residual soil after treatment, PC in distillate
The content of B etc. is as shown in Table-2.

【0016】[0016]

【表―2】表―2 港湾水底土砂(浚渫土)の
水蒸気蒸留処理後の成分濃度
[Table-2] Table-2 Concentration of components after steam distillation of harbor water bottom sediment (dredge soil)

【0017】港湾水底土砂(浚渫土)を水蒸気蒸留した
結果、ダイオキシン類は72%が土砂より除去削減され
た。同様に、コプラナーPCBは83%が除去され、PCBは
90%が除去された。同時に、アンモニア性窒素および
全硫化物含有濃度も90%以上除去された。亜鉛も処理
前の10分の1以下になり、農耕地土壌の管理基準より、
低い濃度になった。
As a result of steam distillation of the bottom sediment (dredged soil) of the port water, dioxins were reduced by 72% from the sediment. Similarly, 83% of the coplanar PCB was removed and 90% of the PCB was removed. At the same time, the concentration of ammonia nitrogen and total sulfide content was removed by 90% or more. Zinc is also reduced to one-tenth or less before treatment.
The concentration became low.

【0018】[0018]

【実施例2】3種類の土壌に、ダイオキシン類の1種で
ある1,3,6,8−TCDD(テトラクロロジオキシン)を乾
土当たり5,000pg/g(5μg/g)となるように添加し
たのち、10分間の水蒸気蒸留処理を行った。残土中の
1,3,6,8−TCDDの含有量を分析し、ダイオキシンの
除去率を調べた。供試土壌は火山性クロボク土、新第三
紀泥岩残積土及び高有機質港湾水底土砂を用いた。10分
間蒸留のダイオキシン除去率はクロボク土=68.0%、
泥岩残積土=65.2%および港湾水底土砂=53.8%であっ
た。
[Example 2] 1,3,6,8-TCDD (tetrachlorodioxin), one of dioxins, was added to three kinds of soils at a concentration of 5,000 pg / g (5 µg / g) per dry soil. After that, steam distillation treatment was performed for 10 minutes. The content of 1,3,6,8-TCDD in the residual soil was analyzed, and the dioxin removal rate was examined. The test soil used was volcanic Kuroboku soil, Neogene mudstone residual soil, and high-organic port water bottom sediment. Dioxin removal rate of 10 minutes distillation is 68.0% Kuroboku soil,
Mudstone residual soil = 65.2% and port bottom sediment = 53.8%.

【0019】[0019]

【表−3】表−3 ダイオキシン(1,3,
6,8−TCDD)添加土壌からのダイオキシン除去例(水
蒸気蒸留10分間)
[Table-3] Table-3 Dioxin (1,3,3)
Example of dioxin removal from 6,8-TCDD) added soil (steam distillation for 10 minutes)

【0020】(比較例1)実施例1に用いた港湾水底土
砂を、同じ三角フラスコに入れ、水蒸気を吹き込むこと
なく、フラスコを直接加熱して、15分間沸騰させた。
その、結果PCBは、67%が除去された。
(Comparative Example 1) The seabed sediment used in Example 1 was placed in the same Erlenmeyer flask, and the flask was directly heated without blowing steam and boiled for 15 minutes.
As a result, 67% of the PCB was removed.

【0021】[0021]

【表−4】表−4 加温蒸発処理によるPCB濃度変化 [Table-4] Table-4 Change in PCB concentration by heating evaporation

【0022】[0022]

【発明の効果】以上説明したように、本発明によれば、
PCBあるいはダイオキシン類等によって汚染された水底
土砂又は陸上の土壌の性状を損なう事なく浄化できるの
で、処理後の土壌は農耕地等に還元・再利用利用するこ
とができる。このため、環境浄化および土地利用の有効
活用に役立つようにしたものであり、実益は大である。
As described above, according to the present invention,
Since the soil can be purified without impairing the properties of underwater soil and soil or land on land contaminated by PCBs or dioxins, the treated soil can be reduced and reused on agricultural land. For this reason, it is intended to contribute to environmental purification and effective use of land use, and the actual profit is great.

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

【図1】本発明の実験に用いた水蒸気蒸留装置の一例で
ある。
FIG. 1 is an example of a steam distillation apparatus used in an experiment of the present invention.

【符号の説明】[Explanation of symbols]

1 水槽 6 蒸留水 2 吸い上げろ過装置 7 冷却管 3 水蒸気発生装置 8 受器 4 蒸留フラスコ 9 留出液と共に回
収されたPCB 5 供試試料
DESCRIPTION OF SYMBOLS 1 Water tank 6 Distilled water 2 Suction filtration device 7 Cooling pipe 3 Steam generator 8 Receiver 4 Distillation flask 9 PCB collected with distillate 5 Test sample

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 PCB、ダイオキシン類またはその他の有
機性有害物質によって汚染された土壌に水蒸気を吹き込
み、水蒸気蒸留法によって有害物質を除去する事を特徴
とする汚染土壌の浄化方法。
1. A method for purifying contaminated soil, comprising blowing steam into soil contaminated with PCBs, dioxins or other organic harmful substances, and removing the harmful substances by a steam distillation method.
JP2000383381A 2000-12-18 2000-12-18 Method of cleaning contaminated soil Pending JP2002177940A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000383381A JP2002177940A (en) 2000-12-18 2000-12-18 Method of cleaning contaminated soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000383381A JP2002177940A (en) 2000-12-18 2000-12-18 Method of cleaning contaminated soil

Publications (1)

Publication Number Publication Date
JP2002177940A true JP2002177940A (en) 2002-06-25

Family

ID=18851045

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000383381A Pending JP2002177940A (en) 2000-12-18 2000-12-18 Method of cleaning contaminated soil

Country Status (1)

Country Link
JP (1) JP2002177940A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004230355A (en) * 2003-02-03 2004-08-19 Nippon Soda Co Ltd Method for removing residual organic solvent in solid material
CN114535061A (en) * 2022-01-17 2022-05-27 江苏国润检测科技有限公司 Dioxin distribution and separation device and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004230355A (en) * 2003-02-03 2004-08-19 Nippon Soda Co Ltd Method for removing residual organic solvent in solid material
CN114535061A (en) * 2022-01-17 2022-05-27 江苏国润检测科技有限公司 Dioxin distribution and separation device and method

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