JP2001149913A - Cleaning method of contaminated soil - Google Patents
Cleaning method of contaminated soilInfo
- Publication number
- JP2001149913A JP2001149913A JP33345799A JP33345799A JP2001149913A JP 2001149913 A JP2001149913 A JP 2001149913A JP 33345799 A JP33345799 A JP 33345799A JP 33345799 A JP33345799 A JP 33345799A JP 2001149913 A JP2001149913 A JP 2001149913A
- Authority
- JP
- Japan
- Prior art keywords
- water
- cleaning
- cleaning liquid
- washing
- contaminated soil
- 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.)
- Withdrawn
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 55
- 239000002689 soil Substances 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 239000007788 liquid Substances 0.000 claims abstract description 53
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 25
- 239000010419 fine particle Substances 0.000 claims abstract description 22
- 239000011362 coarse particle Substances 0.000 claims abstract description 21
- 239000000243 solution Substances 0.000 claims abstract description 19
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 13
- 235000019353 potassium silicate Nutrition 0.000 claims abstract description 11
- 238000003756 stirring Methods 0.000 claims abstract description 11
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 239000012670 alkaline solution Substances 0.000 claims abstract description 3
- 238000005406 washing Methods 0.000 claims description 58
- 239000000356 contaminant Substances 0.000 claims description 19
- 238000004062 sedimentation Methods 0.000 claims description 14
- 239000002253 acid Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 2
- 239000000306 component Substances 0.000 claims 1
- 239000003921 oil Substances 0.000 abstract description 17
- 238000001556 precipitation Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 4
- 239000003929 acidic solution Substances 0.000 abstract 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 239000004576 sand Substances 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000003513 alkali Substances 0.000 description 6
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 239000004927 clay Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000000701 coagulant Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 238000012216 screening Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 102100033041 Carbonic anhydrase 13 Human genes 0.000 description 1
- 102100032566 Carbonic anhydrase-related protein 10 Human genes 0.000 description 1
- 101000867860 Homo sapiens Carbonic anhydrase 13 Proteins 0.000 description 1
- 101000867836 Homo sapiens Carbonic anhydrase-related protein 10 Proteins 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、灯油、軽油、重油
等の油や重金属等により汚染された土壌を洗浄して清浄
化するための方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning and contaminating soil contaminated with oil such as kerosene, light oil, heavy oil, or heavy metals.
【0002】[0002]
【従来の技術】近年、タンカー事故等により海上に流出
した原油や重油が海岸に漂着して環境汚染を引き起こす
事態がしばしば生じる。そのような場合、油汚染された
土砂を清浄化するため、カセイソーダや過酸化水素水、
あるいは灯油や界面活性剤を用いて汚染土壌から油分を
分離除去する方法が試みられている。2. Description of the Related Art In recent years, a situation often arises in which crude oil or heavy oil that has flown to the sea due to a tanker accident or the like drifts on the shore and causes environmental pollution. In such cases, caustic soda, hydrogen peroxide,
Alternatively, a method of separating and removing oil from contaminated soil using kerosene or a surfactant has been attempted.
【0003】また、土壌が有害な重金属に汚染されてい
る場合、従来においては重金属を汚染土壌から分離除去
するための有効適切な方法は未だ確立されていないこと
から、汚染土壌が周囲に拡散することを防止するべく厳
重に封じ込めるという対策が取られている。[0003] When soil is contaminated with harmful heavy metals, an effective and appropriate method for separating and removing heavy metals from the contaminated soil has not yet been established. In order to prevent this, measures have been taken to strictly contain them.
【0004】[0004]
【発明が解決しようとする課題】しかし、油汚染土壌に
対する上記のような従来の清浄化方法は現地において簡
便、安価に実施できるようなものではないし、重金属汚
染土壌を単に封じ込めるだけでは根本的な解決となら
ず、以上のことから油や重金属等に汚染された土壌を現
地において簡便かつ安価に清浄化し得る有効な手段の開
発が急務であるとされている。However, the conventional cleaning method for oil-contaminated soil as described above cannot be carried out simply and inexpensively on site, and it is fundamental to simply contain heavy metal-contaminated soil. From the above, it is urgently necessary to develop effective means for easily and inexpensively cleaning soil contaminated with oil, heavy metals, and the like.
【0005】[0005]
【課題を解決するための手段】請求項1の発明は、汚染
土壌を洗浄して清浄化するための方法であって、汚染土
壌と洗浄液とを攪拌混合する工程、汚染土壌と洗浄液と
の混合物から粗粒分を分級する工程、粗粒分を洗浄液に
よりさらに洗浄し分級装置により汚染物質を洗浄液とと
もに分離する工程、粗粒分を分級した残余の細粒分を沈
降装置において沈降せしめて固液分離する工程、洗浄液
を回収して汚染物質を分離し処理あるいは処分する工程
とを有するものである。SUMMARY OF THE INVENTION The invention of claim 1 is a method for cleaning and cleaning contaminated soil, comprising the steps of stirring and mixing the contaminated soil and the cleaning liquid; A step of classifying coarse particles from the mixture, a step of further washing the coarse particles with a washing liquid and separating contaminants together with the washing liquid by a classifier, and a step of sedimenting the remaining fine particles obtained by classifying the coarse particles in a sedimentation device to form a solid-liquid And a step of collecting a cleaning liquid to separate and treat or dispose of contaminants.
【0006】請求項2の発明は、請求項1の発明におい
て、汚染物質が油分である場合に洗浄液として水と水ガ
ラスを用いるものである。According to a second aspect of the present invention, in the first aspect of the invention, water and water glass are used as the cleaning liquid when the contaminant is oil.
【0007】請求項3の発明は、請求項1の発明におい
て、汚染物質が重金属である場合に洗浄液として水と酸
またはアルカリ溶液を用いるものである。According to a third aspect of the present invention, in the first aspect of the invention, when the contaminant is a heavy metal, water and an acid or alkali solution are used as the cleaning solution.
【0008】[0008]
【発明の実施の形態】本発明の第1実施形態の洗浄方法
を図1を参照して説明する。本第1実施形態は灯油、軽
油、重油等の油による汚染土壌を対象とするもので、洗
浄液としては水と水ガラス(珪酸ナトリウム溶液)を用
いるものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A cleaning method according to a first embodiment of the present invention will be described with reference to FIG. The first embodiment is intended for soil contaminated with oil such as kerosene, light oil, or heavy oil, and uses water and water glass (sodium silicate solution) as a cleaning liquid.
【0009】本第1実施形態では、現地において掘削し
た汚染土壌を受入ホッパー1に投入し、ベルトコンベア
ー等の搬送装置により混合装置2に供給する。混合装置
2としては解こう機あるいは攪拌機が好適に採用可能で
あり、これに洗浄水を供給して攪拌混合する。In the first embodiment, contaminated soil excavated at the site is put into a receiving hopper 1 and supplied to a mixing device 2 by a conveyor such as a belt conveyor. A pulverizer or a stirrer can be suitably used as the mixing device 2, and washing water is supplied to the mixer to stir and mix.
【0010】所定時間の攪拌混合後、フルイ装置3に移
し、粒径の大きいれき等(粒径がほぼ2mm以上のも
の)を排除する。フルイ装置3を通過した細かい土砂は
1次受槽4から分級装置5に送り、このとき洗浄水を加
える。After stirring and mixing for a predetermined time, the mixture is transferred to a sieve device 3 to remove debris and the like having a large particle size (those having a particle size of about 2 mm or more). The fine earth and sand that has passed through the sieve device 3 is sent from the primary receiving tank 4 to the classifying device 5, where washing water is added.
【0011】分級装置5において約74μm以上の粗粒
分(主として砂)を分級してそれを2次受槽6に送ると
ともに、残余の細粒分であるシルトや粘土は洗浄水とと
もに泥水受槽7へ送る。In the classifier 5, coarse particles (mainly sand) having a size of about 74 μm or more are classified and sent to the secondary receiving tank 6. Silt and clay, which are the remaining fine particles, are sent to the muddy water receiving tank 7 together with washing water. send.
【0012】泥水受槽7に送られた細粒分には凝集剤
(PAC等)を添加して沈降装置8に送り、そこで所定
時間静置し、沈降した細粒分をフィルタープレス等の圧
縮装置9により圧縮して水分除去した後、回収する。細
粒分から分離して沈降装置8の液面に浮上した油分は回
収して処分し、沈降装置8からの洗浄水は圧縮装置9か
らの洗浄水とともに1次洗浄水受槽10に回収して処理
し、新たに供給される洗浄水とともに循環使用する。A coagulant (PAC or the like) is added to the fine particles sent to the muddy water receiving tank 7 and sent to a sedimentation device 8 where the fine particles are settled for a predetermined time, and the sedimented fine particles are compressed by a compression device such as a filter press. After being compressed by 9 to remove water, it is recovered. The oil separated from the fine particles and floated on the liquid surface of the sedimentation device 8 is collected and disposed, and the washing water from the sedimentation device 8 is collected and treated in the primary washing water receiving tank 10 together with the washing water from the compression device 9. Then, it is circulated and used with newly supplied washing water.
【0013】一方、粗粒分は2次受槽6において洗浄液
としての水ガラスと混合し、それらをポンプにより分級
装置11に送る。この分級装置11としては洗浄室を有
するドラム式分級機が好適に採用可能であり、ここで粗
粒分と洗浄液とを攪拌混合すると、水ガラスによる洗浄
により油分が土壌から分離するので、洗浄後の粗粒分を
回収するとともに、分離された汚染物質である油分を含
む洗浄液を2次洗浄水受槽12に送る。2次洗浄水受槽
12では必要に応じて新たな洗浄液を加えてpHを10
以上、水ガラスの濃度を1%以上に調整して循環使用す
る。この2次洗浄液受槽12の液面には分離された油分
が浮上するのでそれを回収して処分する。On the other hand, the coarse particles are mixed with water glass as a cleaning liquid in the secondary receiving tank 6 and sent to a classification device 11 by a pump. A drum type classifier having a washing chamber can be suitably used as the classifier 11, and when the coarse particles and the washing liquid are mixed with stirring, the oil is separated from the soil by washing with water glass. And a washing liquid containing oil, which is a separated contaminant, is sent to the secondary washing water receiving tank 12. In the secondary washing water receiving tank 12, if necessary, a new washing liquid is added to adjust the pH to 10
As described above, the concentration of the water glass is adjusted to 1% or more to be used in circulation. The separated oil floats on the liquid surface of the secondary cleaning liquid receiving tank 12 and is collected and disposed.
【0014】本第1実施形態の洗浄方法によれば、油汚
染土壌を粗粒分(主として砂)と細粒分(シルトや粘
土)に分け、粗粒分を水ガラスにより洗浄して分離した
油分を2次洗浄水受槽12により分離し、細粒分は水洗
浄して沈降装置8において固液分離を行うので、十分な
洗浄効果が得られることはもとより、現地において簡便
かつ効率的に実施することができ、洗浄後の土壌をその
まま現地に戻すことができ、また洗浄液としての水や水
ガラスは再生して繰り返し循環使用でき、したがって洗
浄コストを十分に軽減することができる。According to the cleaning method of the first embodiment, the oil-contaminated soil is divided into coarse particles (mainly sand) and fine particles (silt or clay), and the coarse particles are separated by washing with water glass. The oil is separated by the secondary washing water receiving tank 12, and the fine particles are washed with water and subjected to solid-liquid separation in the sedimentation device 8, so that a sufficient washing effect can be obtained and, moreover, simple and efficient on-site implementation The soil after washing can be returned to the site as it is, and water or water glass as a washing liquid can be regenerated and reused repeatedly, and thus the washing cost can be sufficiently reduced.
【0015】なお、上記方法では、たとえばA重油によ
る5%程度の高濃度汚染土壌を残留濃度が数百ppm程
度にまで清浄化できるが、さらに高度の処理が必要な場
合には、洗浄後の土壌に対しより高度の清浄化処理たと
えばバイオレメディエーション処理を行えば良い。[0015] In the above method, for example, the highly contaminated soil of about 5% by heavy fuel oil A can be cleaned to a residual concentration of about several hundred ppm. The soil may be subjected to a more advanced cleaning treatment, for example, a bioremediation treatment.
【0016】次に、本発明の第2実施形態の洗浄方法を
図2を参照して説明する。本第2実施形態は重金属によ
る汚染土壌を対象とするもので、洗浄液としては、水
と、塩酸や硫酸等の酸溶液、あるいはカセイソーダや珪
酸ナトリウム等のアルカリ溶液を用いるものである。Next, a cleaning method according to a second embodiment of the present invention will be described with reference to FIG. The second embodiment is directed to a soil contaminated with heavy metals, and uses water and an acid solution such as hydrochloric acid or sulfuric acid, or an alkaline solution such as caustic soda or sodium silicate as the washing liquid.
【0017】本第2実施形態では、現地において掘削し
た汚染土壌を受入ホッパー21に投入し、ベルトコンベ
アー等の搬送装置により混合装置22に供給する。混合
装置22としては解こう機あるいは攪拌機が好適に採用
可能であり、これに洗浄液としての酸あるいはアルカリ
溶液を供給して攪拌混合する。In the second embodiment, contaminated soil excavated at the site is put into a receiving hopper 21 and supplied to a mixing device 22 by a conveyor such as a belt conveyor. A pulverizer or a stirrer can be suitably used as the mixing device 22, and an acid or alkali solution as a cleaning liquid is supplied to the mixing device 22 for stirring and mixing.
【0018】所定時間の攪拌混合後、フルイ装置23に
移して粒径の大きいれき等を分別し、水洗浄装置24に
おいて洗浄液を洗い流した後、回収して現地に埋め戻
す。ここで使用した洗浄水は2次洗浄水受槽25に回収
して再利用する。After stirring and mixing for a predetermined time, the mixture is transferred to a sieve device 23 to separate debris and the like having a large particle size. The washing solution is washed away in a water washing device 24, and then collected and backfilled on site. The washing water used here is collected in the secondary washing water receiving tank 25 and reused.
【0019】フルイ装置23を通過した細かい土砂は、
洗浄液とともに1次受槽26から分級装置27に送り、
この分級装置27にも洗浄液を加える。The fine earth and sand that has passed through the screen device 23 is:
The cleaning liquid is sent from the primary receiving tank 26 to the classification device 27,
The cleaning liquid is also added to the classifier 27.
【0020】分級装置27において約74μm以上の粗
粒分(主として砂)を分級してそれを2次受槽28に送
るとともに、残余の細粒分であるシルトや粘土は洗浄液
とともに泥水受槽29へ送る。In the classifier 27, coarse particles (mainly sand) of about 74 μm or more are classified and sent to the secondary receiving tank 28, and the remaining fine particles such as silt and clay are sent to the muddy water receiving tank 29 together with the washing liquid. .
【0021】泥水受槽29に送られた細粒分には必要に
応じてpH調整を行うとともに、凝集剤(PAC等)を
添加して沈降装置30に送り、そこで所定時間静置し、
沈降した細粒分をフィルタープレス等の圧縮装置31に
より圧縮して水分除去した後、回収して現地に埋め戻
す。沈降装置30において細粒分から分離した汚染物質
を含む洗浄液および圧縮装置31からの洗浄液を1次洗
浄水受槽32に回収し、重金属処理装置33において汚
染物質である重金属を分離除去して処分施設へ送り、こ
こで回収した洗浄水は再生して循環使用する。The pH of the fine particles sent to the muddy water receiving tank 29 is adjusted as required, and a coagulant (PAC or the like) is added to the fine particles and sent to the sedimentation device 30, where the fine particles are allowed to stand for a predetermined time.
The sedimented fine particles are compressed by a compression device 31 such as a filter press to remove water, and then collected and backfilled on site. The cleaning liquid containing the contaminants separated from the fine particles in the sedimentation device 30 and the cleaning liquid from the compression device 31 are collected in the primary cleaning water receiving tank 32, and the heavy metals as the contaminants are separated and removed in the heavy metal treatment device 33 to the disposal facility. The washing water collected here is regenerated and recycled.
【0022】一方、粗粒分は2次受槽28において洗浄
水と混合し、それらをポンプにより分級装置34に送
る。この分級装置34としては洗浄室を有するドラム式
分級機が好適に採用可能であり、ここで粗粒分と洗浄水
とを攪拌混合すると、洗浄水による洗浄により汚染物質
が土壌から分離するので、洗浄後の粗粒分を回収して現
地に埋め戻すとともに、分離された汚染物質である重金
属を含む洗浄水を2次洗浄水受槽25から重金属処理装
置33に送り、上記の1次洗浄液受槽32からの洗浄液
とともに処理して重金属を分離除去する。On the other hand, the coarse particles are mixed with the washing water in the secondary receiving tank 28 and sent to a classifier 34 by a pump. As the classifying device 34, a drum type classifier having a washing room can be suitably adopted. When the coarse particles and the washing water are mixed with stirring, the pollutants are separated from the soil by washing with the washing water. The coarse particles after washing are collected and backfilled at the site, and the washing water containing the heavy metals as the separated contaminants is sent from the secondary washing water receiving tank 25 to the heavy metal processing device 33, and the above-mentioned primary washing liquid receiving tank 32 And heavy metals are separated and removed.
【0023】本第2実施形態においては、処理対象の重
金属に応じて適切な酸溶液あるいはアルカリ溶液を用い
ることで優れた洗浄効果が得られるとともに、第1実施
形態と同様に現地において簡便、効率的、安価に実施す
ることができる。In the second embodiment, an excellent cleaning effect can be obtained by using an appropriate acid solution or alkali solution according to the heavy metal to be treated, and, as in the first embodiment, simple and efficient on-site. It can be implemented at reasonable cost.
【0024】図3は本発明の第3実施形態を示す。本第
3実施形態は第2実施形態と同様に重金属汚染土壌を対
象とし、洗浄液としては同じく水と酸溶液あるいはアル
カリ溶液を用いるものであるが、洗浄が容易で量が最も
多い粗粒分(主として砂)を洗浄液により十分に洗浄し
て現地に埋め戻すこととし、比較的量が少ないれきや細
粒分(シルト、粘土)は水洗浄するに留めて処分してし
まうようにしたものである。FIG. 3 shows a third embodiment of the present invention. The third embodiment targets heavy metal-contaminated soil similarly to the second embodiment, and similarly uses water and an acid solution or an alkali solution as a cleaning solution. (Mainly sand) is thoroughly washed with a cleaning solution and backfilled at the site, and relatively small amounts of debris and fine particles (silt, clay) are disposed of only after washing with water. .
【0025】本第3実施形態では、汚染土壌を受入ホッ
パー41から混合装置42に供給し、洗浄水と攪拌混合
する。In the third embodiment, the contaminated soil is supplied from the receiving hopper 41 to the mixing device 42, and is mixed with the washing water by stirring.
【0026】所定時間の攪拌混合後、フルイ装置43に
より粒径の大きいれき等を分別して処分し、フルイ装置
43を通過した細かい土砂は、洗浄水とともに1次受槽
44から分級装置45に送り、この分級装置45にも洗
浄水を供給する。After stirring and mixing for a predetermined time, debris and the like having a large particle diameter are separated and disposed by the sieve device 43, and the fine earth and sand that has passed through the sieve device 43 is sent from the primary receiving tank 44 to the classification device 45 together with the washing water. Wash water is also supplied to the classifier 45.
【0027】分級装置45において約74μm以上の粗
粒分(主として砂)を分級してそれを2次受槽46に送
るとともに、残余の細粒分であるシルトや粘土は洗浄水
とともに泥水受槽47へ送る。The classifier 45 classifies coarse particles (mainly sand) having a size of about 74 μm or more and sends them to the secondary receiving tank 46, and the remaining fine particles such as silt and clay are transferred to the muddy water receiving tank 47 together with the washing water. send.
【0028】泥水受槽47に送られた細粒分は凝集剤
(PAC等)を添加して沈降装置48に送り、そこで所
定時間静置し、沈降した細粒分をフィルタープレス等の
圧縮装置49により圧縮して水分除去した後、回収して
処分する。沈降装置48において細粒分から分離した汚
染物質を含む洗浄水および圧縮装置49からの洗浄水を
1次洗浄水受槽50に回収し、重金属処理装置51にお
いて汚染物質である重金属を分離除去して処分し、ここ
で回収した洗浄液や洗浄水は再生して循環使用する。The fine particles sent to the muddy water receiving tank 47 are added to a coagulant (PAC or the like) and sent to a sedimentation device 48, where they are allowed to stand for a predetermined time, and the sedimented fine particles are compressed by a compression device 49 such as a filter press. After removing water by compressing, collect and dispose. The washing water containing the contaminants separated from the fine particles in the sedimentation device 48 and the washing water from the compression device 49 are collected in the primary washing water receiving tank 50, and the heavy metal as the contaminant is separated and removed in the heavy metal treatment device 51 for disposal. The collected washing liquid and washing water are regenerated and recycled.
【0029】一方、粗粒分は2次受槽46において洗浄
液と攪拌混合すると、洗浄液による洗浄により汚染物質
が土壌から分離するので、洗浄後の粗粒分を回収し、水
洗浄装置53により洗浄液を洗い流した後、現地に埋め
戻す。分級装置52からの汚染物質を含む洗浄液は2次
洗浄液受槽54から重金属処理装置51へ送り、水洗浄
装置53からの洗浄水も同様に重金属処理装置51に送
り、ここで重金属を分離除去するとともに洗浄液を再生
して循環使用する。On the other hand, when the coarse particles are stirred and mixed with the cleaning liquid in the secondary receiving tank 46, the contaminants are separated from the soil by the cleaning with the cleaning liquid. After rinsing, backfill at the site. The cleaning liquid containing contaminants from the classification device 52 is sent from the secondary cleaning liquid receiving tank 54 to the heavy metal processing device 51, and the washing water from the water cleaning device 53 is also sent to the heavy metal processing device 51, where heavy metals are separated and removed. Regenerate and recycle the cleaning solution.
【0030】以上で本発明の実施形態を説明したが、本
発明は上記実施形態に限定されず、本発明の要旨を逸脱
しない範囲で工程の細部や使用する洗浄液、装置類につ
いては適宜の設計的変更が可能であることは当然であ
る。Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and the details of the steps, the cleaning liquid to be used, and the apparatuses are appropriately designed without departing from the gist of the present invention. Naturally, it is possible to make objective changes.
【0031】[0031]
【発明の効果】請求項1の発明は、汚染土壌を粗粒分と
細粒分とに分け、粗粒分については洗浄液により洗浄し
て分級装置により汚染物質を洗浄液とともに分離除去す
るとともに、細粒分については沈降装置において固液分
離するので、十分な洗浄効果が得られて汚染土壌を清浄
化できることはもとより、現地において簡便、安価、効
率的に洗浄処理を行うことができ、油や重金属に汚染さ
れた土壌を大量に処理する場合に適用して好適である。According to the first aspect of the present invention, the contaminated soil is divided into coarse particles and fine particles, and the coarse particles are washed with a cleaning liquid, and the contaminants are separated and removed together with the cleaning liquid by a classifier. Particles are separated into solids and liquids in the sedimentation device, so that sufficient washing effects can be obtained and contaminated soil can be cleaned, and in addition, simple, inexpensive, and efficient washing can be performed locally, and oil and heavy metals can be removed. It is suitable to be applied when a large amount of soil contaminated with water is treated.
【0032】請求項2の発明は、汚染物質が油分である
場合に洗浄液として水と水ガラスを用いるので、水ガラ
スによる油分に対する優れた洗浄効果が得られるととも
に、洗浄液を再生して循環使用することが可能であるの
で経済的である。According to the second aspect of the present invention, since water and water glass are used as the cleaning liquid when the contaminant is oil, an excellent cleaning effect on the oil by the water glass is obtained, and the cleaning liquid is regenerated and recycled. It is economical because it is possible.
【0033】請求項3の発明は、汚染物質が重金属であ
る場合に洗浄液として水と酸溶液またはアルカリ溶液を
用いるので、処理対象の重金属に応じて適切な酸溶液あ
るいはアルカリ溶液を選択して用いることで優れた洗浄
効果が得られるとともに、洗浄液の再生、循環使用も可
能である。According to the third aspect of the present invention, when the contaminant is a heavy metal, water and an acid solution or an alkali solution are used as the cleaning liquid. Therefore, an appropriate acid solution or alkali solution is selected and used according to the heavy metal to be treated. Thereby, an excellent cleaning effect can be obtained, and the cleaning liquid can be regenerated and recycled.
【図面の簡単な説明】[Brief description of the drawings]
【図1】 本発明の第1実施形態を示す系統図である。FIG. 1 is a system diagram showing a first embodiment of the present invention.
【図2】 本発明の第2実施形態を示す系統図である。FIG. 2 is a system diagram showing a second embodiment of the present invention.
【図3】 本発明の第3実施形態を示す系統図である。FIG. 3 is a system diagram showing a third embodiment of the present invention.
2 混合装置 3 フルイ装置 5 分級装置 8 沈降装置 11 分級装置 22 混合装置 23 フルイ装置 27 分級装置 30 沈降装置 33 重金属処理装置 34 分級装置 42 混合装置 43 フルイ装置 45 分級装置 48 沈降装置 51 重金属処理装置 52 分級装置 53 水洗浄装置 2 Mixing device 3 Screening device 5 Classification device 8 Sedimentation device 11 Classification device 22 Mixing device 23 Screening device 27 Classification device 30 Sedimentation device 33 Heavy metal processing device 34 Classification device 42 Mixing device 43 Screening device 45 Classification device 48 Precipitation device 51 Heavy metal processing device 52 Classification device 53 Water washing device
───────────────────────────────────────────────────── フロントページの続き (72)発明者 小田原 卓郎 東京都港区芝浦一丁目2番3号 清水建設 株式会社内 (72)発明者 丹羽 千明 東京都港区芝浦一丁目2番3号 清水建設 株式会社内 Fターム(参考) 4D004 AA41 AB02 AB03 AC07 CA07 CA10 CA13 CA15 CA35 CA40 CC03 CC12 CC13 CC20 DA02 DA10 4D071 AA01 AA42 BB13 DA03 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takuro Odawara 1-3-2 Shibaura, Minato-ku, Tokyo Shimizu Corporation (72) Inventor Chiaki Niwa 1-3-2 Shibaura, Minato-ku, Tokyo Shimizu Corporation In-house F term (reference) 4D004 AA41 AB02 AB03 AC07 CA07 CA10 CA13 CA15 CA35 CA40 CC03 CC12 CC13 CC20 DA02 DA10 4D071 AA01 AA42 BB13 DA03
Claims (3)
程、汚染土壌と洗浄液との混合物から粗粒分を分級する
工程、粗粒分を洗浄液によりさらに洗浄し分級装置によ
り汚染物質を洗浄液とともに分離する工程、粗粒分を分
級した残余の細粒分を沈降装置において沈降せしめて固
液分離する工程、洗浄液を回収して汚染物質を分離し処
理あるいは処分する工程とを有することを特徴とする汚
染土壌の洗浄方法。1. A step of stirring and mixing contaminated soil and a washing liquid; a step of classifying coarse particles from a mixture of the contaminated soil and the washing liquid; a step of further washing the coarse particles with the washing liquid; and separating the contaminants together with the washing liquid by a classifier. Performing a sedimentation process, sedimenting the remaining fine particles in a sedimentation apparatus to separate solid and liquid, and collecting a washing liquid to separate and treat or dispose of contaminants. How to clean contaminated soil.
と水ガラスを用いることを特徴とする請求項1記載の汚
染土壌の洗浄方法。2. The method for cleaning contaminated soil according to claim 1, wherein the contaminant is an oil component, and water and water glass are used as the cleaning liquid.
水と酸溶液またはアルカリ溶液を用いることを特徴とす
る請求項1記載の汚染土壌の洗浄方法。3. The method for cleaning contaminated soil according to claim 1, wherein the contaminant is a heavy metal, and water and an acid solution or an alkaline solution are used as the cleaning liquid.
Priority Applications (1)
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JP33345799A JP2001149913A (en) | 1999-11-24 | 1999-11-24 | Cleaning method of contaminated soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33345799A JP2001149913A (en) | 1999-11-24 | 1999-11-24 | Cleaning method of contaminated soil |
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Publication Number | Publication Date |
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JP2001149913A true JP2001149913A (en) | 2001-06-05 |
Family
ID=18266306
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JP33345799A Withdrawn JP2001149913A (en) | 1999-11-24 | 1999-11-24 | Cleaning method of contaminated soil |
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