JPH0782729A - Purification method of contaminated soil and purification device used for method concerned - Google Patents
Purification method of contaminated soil and purification device used for method concernedInfo
- Publication number
- JPH0782729A JPH0782729A JP5227599A JP22759993A JPH0782729A JP H0782729 A JPH0782729 A JP H0782729A JP 5227599 A JP5227599 A JP 5227599A JP 22759993 A JP22759993 A JP 22759993A JP H0782729 A JPH0782729 A JP H0782729A
- Authority
- JP
- Japan
- Prior art keywords
- water
- pumping
- contaminated soil
- groundwater
- 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.)
- Granted
Links
- 239000002689 soil Substances 0.000 title claims abstract description 77
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000000746 purification Methods 0.000 title abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 79
- 238000005086 pumping Methods 0.000 claims abstract description 56
- 239000000126 substance Substances 0.000 claims abstract description 56
- 239000003673 groundwater Substances 0.000 claims abstract description 48
- 239000003344 environmental pollutant Substances 0.000 claims description 63
- 231100000719 pollutant Toxicity 0.000 claims description 63
- 238000004140 cleaning Methods 0.000 claims description 32
- 238000011084 recovery Methods 0.000 claims description 28
- 238000002347 injection Methods 0.000 claims description 18
- 239000007924 injection Substances 0.000 claims description 18
- 238000010828 elution Methods 0.000 claims description 16
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 4
- 230000002378 acidificating effect Effects 0.000 claims description 4
- 239000003456 ion exchange resin Substances 0.000 claims description 4
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 13
- 239000000356 contaminant Substances 0.000 abstract description 12
- 238000000926 separation method Methods 0.000 abstract description 4
- 238000011282 treatment Methods 0.000 description 21
- 238000011221 initial treatment Methods 0.000 description 9
- 239000012535 impurity Substances 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- -1 polyethylene Polymers 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 239000012466 permeate Substances 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 238000001223 reverse osmosis Methods 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 229920002558 Curdlan Polymers 0.000 description 1
- 239000001879 Curdlan Substances 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 229910000792 Monel Inorganic materials 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920003235 aromatic polyamide Polymers 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 229940078035 curdlan Drugs 0.000 description 1
- 235000019316 curdlan Nutrition 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
Landscapes
- Investigation Of Foundation Soil And Reinforcement Of Foundation Soil By Compacting Or Drainage (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、汚染土壌の清浄化に好
適な汚染土壌の清浄化方法及び該方法に使用される清浄
化装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning contaminated soil suitable for cleaning contaminated soil and a cleaning device used in the method.
【0002】[0002]
【従来の技術】一般に、工場の周辺の地盤は、工場排水
の漏出等により汚染されている場合が多い。このような
地盤を対象として地下水の利用を含む土地利用をする場
合には、汚染物質を除去する必要がある。2. Description of the Related Art Generally, the ground around a factory is often contaminated by leakage of factory wastewater. When using land including the use of groundwater for such ground, it is necessary to remove pollutants.
【0003】従来、このような地盤の汚染物質を除去す
るためには有効な手段がなく、汚染された土壌をそのま
ま回収し、廃棄して、新しい土壌に置換する手段、又
は、汚染された土壌から汚染物質が流出しないように封
じ込める手段がとられていた。Conventionally, there is no effective means for removing such pollutants of the ground, and means for recovering the contaminated soil as it is, discarding it, and replacing it with new soil, or a contaminated soil. Measures have been taken to contain the pollutants from the spillway.
【0004】ここで、汚染された地盤の土壌を回収、廃
棄する場合には、汚染された土壌を廃棄する廃棄場の土
地確保が困難であるとともに、廃棄土壌、及び新しい土
壌の運搬費等の多大なコストを要し、汚染物質の封じ込
めを行う場合でも、大規模な施設を構築しなければなら
ず、多大なコストを要するといった問題がある。[0004] Here, when the soil of the contaminated soil is collected and discarded, it is difficult to secure land at the disposal site where the contaminated soil is discarded, and the transportation cost of the discarded soil and new soil, etc. There is a problem that a large amount of cost is required and a large-scale facility must be constructed even if the pollutant is contained, which requires a large amount of cost.
【0005】かかる問題を解決するために、出願人は以
下のような地下水の清浄化装置を提案している(特願平
5−113466号参照)。In order to solve such a problem, the applicant has proposed the following groundwater purification device (see Japanese Patent Application No. 5-113466).
【0006】すなわち、図2に示すように、地盤1に揚
水孔2を掘削すると共に、この揚水孔2から所定距離離
間した位置に注水孔3を掘削し、前記揚水孔2内に揚水
ポンプ4を配置し、この揚水ポンプ4から、地上を経て
前記注水孔3内に至る導水路5を敷設すると共に、地上
における該導水路5中に前記揚水ポンプ4から揚水され
た地下水中に含まれる汚染物質あるいは、不純物を除去
する濾過装置6,7と、この濾過装置6,7によって浄
化された処理水を注水孔3側へ圧送する圧送ポンプ8
と、この圧送ポンプ8によって圧送される処理水をさら
に浄化する逆浸透膜装置9とを、この順に介装してなる
ものである。なお、図中7a,9aは除去された汚染物
質や不純物を回収するための回収口である。That is, as shown in FIG. 2, a pumping hole 2 is drilled in the ground 1, a water injection hole 3 is drilled at a position separated from the pumping hole 2 by a predetermined distance, and a pumping pump 4 is installed in the pumping hole 2. And laying a water conduit 5 from the pumping pump 4 to the inside of the water injection hole 3 via the ground, and contamination contained in groundwater pumped from the pumping pump 4 in the water conduit 5 on the ground. Filtering devices 6 and 7 for removing substances or impurities, and a pressure pump 8 for pumping the treated water purified by the filtering devices 6 and 7 to the water injection hole 3 side.
And a reverse osmosis membrane device 9 for further purifying the treated water pumped by the pressure pump 8. In the figure, 7a and 9a are recovery ports for recovering the removed contaminants and impurities.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、一般に
地盤は負荷電状態となっているので重金属等の陽イオン
が地盤に吸着され易く、前記した地下水の清浄化装置に
よって地下水流が発生されても、重金属等の汚染物質は
土壌から容易に離脱あるいは溶出し難く、したがって、
汚染土壌の清浄化を完全に行うことができないといった
問題がある。However, since the ground is generally in a negatively charged state, cations such as heavy metals are easily adsorbed on the ground, and even if a groundwater flow is generated by the above-mentioned groundwater cleaning device, Pollutants such as heavy metals are not easily released or eluted from the soil, therefore
There is a problem that the contaminated soil cannot be completely cleaned.
【0008】本発明は、上記事情に鑑みてなされたもの
で、地下水に含まれる汚染物質(不純物をも含む。)を
回収することができ、しかも、負荷電状態となった土壌
に吸着された重金属等の汚染物質を効率よく離脱・溶出
させることができ、もって、汚染土壌の清浄化を完全な
らしめることができる汚染土壌の清浄化方法及び該方法
に使用される清浄化装置を提供することを目的とする。The present invention has been made in view of the above circumstances and is capable of recovering pollutants (including impurities) contained in groundwater and adsorbed to negatively charged soil. To provide a method for cleaning a contaminated soil and a cleaning device used for the method, which can efficiently remove and elute pollutants such as heavy metals and can completely clean the contaminated soil. With the goal.
【0009】[0009]
【課題を解決するための手段】本発明の汚染土壌の清浄
化方法は、汚染土壌を含む地盤を掘削して形成された揚
水孔から地下水を揚水し、揚水された地下水を汚染物質
回収装置を通した後、地盤を掘削して形成された注水孔
に注水する汚染土壌の清浄化方法であって、前記汚染物
質回収装置から排出された処理水に汚染物質の土壌から
の離脱や溶出を促進する薬品を添加することを特徴とす
る。なお、前記薬品は低pHの酸性物質又はイオン交換
樹脂の粉末であることが好ましい。The method for cleaning contaminated soil according to the present invention comprises pumping groundwater from a pumping hole formed by excavating the ground containing the contaminated soil, and pumping the groundwater to a pollutant recovery device. This is a method for cleaning contaminated soil in which water is injected into a water injection hole formed by excavating the ground after the passage, and promotes separation and elution of pollutants from soil in treated water discharged from the pollutant recovery device. It is characterized by adding a chemical that does. The chemical is preferably a low pH acidic substance or an ion exchange resin powder.
【0010】本発明の汚染土壌の清浄化装置は、汚染土
壌を含む地盤を掘削して形成された揚水孔から地下水を
揚水する揚水装置と、この揚水装置により揚水された地
下水を地盤を掘削して形成された注水孔に導く導水路
と、この導水路に介装された汚染物質回収装置とを備え
る汚染土壌の清浄化装置であって、前記汚染物質回収装
置から排出された処理水に汚染物質の土壌からの離脱や
溶出を促進する薬品を添加する薬品添加装置を設けたこ
とを特徴とする。The cleaning apparatus for polluted soil according to the present invention is a pumping apparatus for pumping groundwater from a pumping hole formed by excavating the ground containing the polluted soil, and groundwater for pumping groundwater by the pumping apparatus. An apparatus for purifying contaminated soil, comprising: a water conduit leading to a water injection hole formed by the above; and a pollutant recovery device interposed in this water conduit, wherein the treated water discharged from the pollutant recovery device is contaminated. It is characterized in that a chemical addition device for adding a chemical that promotes release and elution of the substance from the soil is provided.
【0011】[0011]
【作用】本発明の汚染土壌の清浄化方法においては、揚
水孔から地下水を揚水し、揚水された地下水を汚染物質
回収装置を通した後、注水孔に注水されるとともに、汚
染物質回収装置から排出された処理水に汚染物質の土壌
からの離脱や溶出を促進する薬品を添加するようにして
いるので、前記処理水を地盤内に注入すると薬品が添加
された処理水が地盤内に浸透し、汚染土壌に吸着された
重金属等の汚染物の離脱・溶出が促進されて地下水に溶
出し、再び揚水孔から揚水されて汚染物質回収装置によ
り汚染物質が除去される。このように、揚水、汚染物質
の回収、薬品の添加、注水とからなるサイクルを繰り返
すことにより、汚染物質を効率よく離脱・溶出させて、
汚染土壌の清浄化を完全ならしめることが可能となる。In the method for cleaning contaminated soil according to the present invention, the groundwater is pumped from the pumping hole, the pumped groundwater is passed through the pollutant collecting device, and then the groundwater is poured into the pouring hole. Since a chemical that promotes the release and elution of pollutants from the soil is added to the discharged treated water, when the treated water is injected into the ground, the treated water containing the chemical penetrates into the ground. The removal and elution of pollutants such as heavy metals adsorbed on the contaminated soil is promoted to elute into the groundwater, and the water is pumped again from the pumping hole, and the pollutants are removed by the pollutant recovery device. In this way, by repeating the cycle of pumping water, collecting pollutants, adding chemicals, and injecting water, pollutants can be efficiently released and eluted,
It is possible to completely clean the contaminated soil.
【0012】本発明の汚染土壌の清浄化装置において
は、揚水装置により、地下水が、揚水孔から導水路内を
通って地上へ上昇し、地上へ上昇した地下水は、汚染物
質回収装置を通過し、地下水に含まれていた汚染物質
(不純物をも含む。)が除去され、処理水は、注水孔に
注水されるとともに、汚染物質回収装置から排出された
処理水に、薬品添加装置により汚染物質の土壌からの離
脱や溶出を促進する薬品が添加される。したがって、前
記処理水を地盤内に注入すると薬品が添加された処理水
が地盤内に浸透し、汚染土壌に吸着された重金属等の汚
染物の離脱・溶出が促進されて地下水に溶出し、再び揚
水孔から揚水されて汚染物質回収装置により汚染物質が
除去される。このように、揚水、汚染物質の回収、薬品
の添加、注水とからなるサイクルを繰り返すことによ
り、汚染物質を効率よく離脱・溶出させて、汚染土壌の
清浄化を完全ならしめることが可能となる。In the apparatus for cleaning polluted soil of the present invention, the pumping device causes groundwater to rise above the ground through the pumping hole into the headrace, and the groundwater that rises above the ground passes through the pollutant recovery device. The pollutants (including impurities) contained in the groundwater are removed, and the treated water is poured into the water injection hole, and the treated water discharged from the pollutant recovery device is polluted by the chemical addition device. A chemical that promotes the release and elution of the soil from the soil is added. Therefore, when the treated water is injected into the ground, the treated water into which the chemical has been added permeates into the ground, and the desorption / elution of contaminants such as heavy metals adsorbed on the contaminated soil is promoted to elute into the groundwater, and again. Water is pumped from the pumping hole and pollutants are removed by the pollutant recovery device. In this way, by repeating the cycle of pumping water, collecting pollutants, adding chemicals, and injecting water, it becomes possible to remove and elute pollutants efficiently, and to completely clean the contaminated soil. .
【0013】[0013]
【実施例】本発明の一実施例の汚染土壌の清浄化装置に
ついて図1を参照しながら説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS A cleaning apparatus for polluted soil according to an embodiment of the present invention will be described with reference to FIG.
【0014】この実施例の汚染土壌の清浄化装置10
は、工場排水等により汚染された地盤に適用した場合を
示すものである。Cleaning apparatus 10 for polluted soil according to this embodiment
Shows the case where it is applied to the ground contaminated by factory wastewater.
【0015】図において符号11は地盤であり、この地
盤11には、揚水孔12が掘削され、この揚水孔12か
ら所定距離離間した位置に注水孔13が掘削されてい
る。In the figure, reference numeral 11 is the ground, and a pumping hole 12 is excavated in the ground 11, and a water injection hole 13 is drilled at a position separated from the pumping hole 12 by a predetermined distance.
【0016】揚水孔12内には、揚水ポンプ(本発明の
揚水装置に相当)14が配置されており、この揚水ポン
プ14から地上を経て注水孔13内に至る導水管15
(本発明の導水路に相当)が敷設されている。この導水
管15の地上部分には、1次処理装置16(濾過装
置)、2次処理装置17(濾過装置)、圧送ポンプ1
8、3次処理装置19(逆浸透膜装置)及び薬品添加装
置20が、導水管5内を移動する地下水の方向に、この
順で介装されている。なお、1次処理装置16、2次処
理装置17及び3次処理装置19は、本発明の汚染物質
回収装置に相当する。A pumping pump (corresponding to the pumping device of the present invention) 14 is disposed in the pumping hole 12, and a water conduit 15 extends from the pumping pump 14 to the inside of the pumping hole 13 via the ground.
(Corresponding to the headrace of the present invention) is laid. At the above-ground portion of the water pipe 15, the primary treatment device 16 (filter device), the secondary treatment device 17 (filter device), the pressure pump 1
8. A tertiary treatment device 19 (reverse osmosis membrane device) and a chemical addition device 20 are provided in this order in the direction of groundwater moving in the water conduit 5. The primary treatment device 16, the secondary treatment device 17, and the tertiary treatment device 19 correspond to the contaminant recovery device of the present invention.
【0017】前記1次処理装置16は、適切な粒径を有
する砂等を充填した沈砂タンクからなるものであって、
この1次処理装置16は、地下水中の浮遊物質等の粒径
の大きい物質を除去する機能を有する。The primary treatment device 16 is composed of a sedimentation tank filled with sand or the like having an appropriate particle size.
The primary treatment device 16 has a function of removing substances having a large particle size such as suspended substances in groundwater.
【0018】前記2次処理装置17は、ステンレス鋼、
真鍮、モネル、ニッケル等のメタル系、あるいは、アル
ミナ、アルミニウムシリケート、磁器質、炭化ケイ素、
ガラス・シリカ繊維等の無機系、あるいは、ポリエチレ
ン、ポリアミド、ポリオレフィン、ポリテトラフルオロ
エチレン等の有機高分子系等の素材からなる精密濾過膜
あるいは、酢酸セルロース及びその誘導体、ポリアクリ
ロニトリル、ポリスルホン、ポリエーテルスルホン、高
分子電解質錯合体、芳香族ポリアミド、ポリビニルアル
コール、キトサン、アセチルカードラン、架橋ポリアミ
ド、架橋ポリイミド、ポリフッ化ビニリデン、ポリテト
ラフルオロエチレン等の素材からなる限外濾過膜によっ
て構成され、地下水に含まれる数100μmから0.0
1μm程度の粒径の物質を除去する機能を有する。ま
た、この2次処理装置7には、除去された物質を回収す
る回収口17aが設けられている。The secondary processing device 17 is made of stainless steel,
Metals such as brass, monel, nickel, alumina, aluminum silicate, porcelain, silicon carbide,
Microfiltration membrane made of inorganic material such as glass / silica fiber or organic polymer material such as polyethylene, polyamide, polyolefin, polytetrafluoroethylene, or cellulose acetate and its derivatives, polyacrylonitrile, polysulfone, polyether Sulfone, polyelectrolyte complex, aromatic polyamide, polyvinyl alcohol, chitosan, acetyl curdlan, crosslinked polyamide, crosslinked polyimide, polyvinylidene fluoride, polytetrafluoroethylene, etc. Included number 100 μm to 0.0
It has a function of removing a substance having a particle diameter of about 1 μm. The secondary processing device 7 is also provided with a recovery port 17a for recovering the removed substance.
【0019】前記圧送ポンプ18は、1次処理装置16
及び2次処理装置17によって浄化された処理水を注水
孔13側へ圧送する機能を有する。The pressure feed pump 18 is a primary treatment device 16
It also has a function of pumping the treated water purified by the secondary treatment device 17 to the water injection hole 13 side.
【0020】前記3次処理装置19は、酢酸セルロース
系、ポリアミド系、複素環ポリマー系、水溶性ポリマー
架橋系、重合性モノマー系、フッ素系等の素材を用いた
逆浸透膜からなるものであって、地下水に含まれる10
nmから0.1nm程度の粒径の物質を除去する機能を
有する。また、この3次処理装置19には、除去された
物質を回収するための回収口19aが設けられている。The tertiary treatment device 19 is composed of a reverse osmosis membrane using materials such as cellulose acetate type, polyamide type, heterocyclic polymer type, water-soluble polymer cross-linking type, polymerizable monomer type and fluorine type. 10 included in groundwater
It has a function of removing a substance having a particle diameter of about 0.1 nm to 0.1 nm. The tertiary treatment device 19 is also provided with a recovery port 19a for recovering the removed substance.
【0021】前記薬品添加装置20は、薬品を吐出する
薬品吐出部(図示せず)と、この薬品吐出部から吐出さ
れた薬品と前記3次処理装置19から排出された処理水
とを撹拌・混合する撹拌槽(図示せず)とを備えてい
る。前記薬品としては、汚染物質の土壌からの離脱や溶
出を促進するものが適宜選択されるが、例えば、低pH
の酸性物質やイオン交換樹脂の粉末等が用いられる。The chemical addition device 20 stirs a chemical discharge portion (not shown) for discharging the chemical, the chemical discharged from the chemical discharge portion and the treated water discharged from the tertiary treatment device 19. And a stirring tank (not shown) for mixing. As the chemical, a chemical that promotes release and elution of pollutants from the soil is appropriately selected, for example, low pH
The acidic substance, the ion-exchange resin powder, and the like are used.
【0022】次に、前記汚染土壌の清浄化装置10の作
用について説明するとともに、本発明の一実施例の汚染
土壌の清浄化方法について説明する。Next, the operation of the contaminated soil cleaning apparatus 10 will be described, and the contaminated soil cleaning method of one embodiment of the present invention will be described.
【0023】まず、揚水ポンプ14を駆動することによ
って地下水が導水管15内を上昇する。この地下水は、
地上に位置する1次処理装置16及び2次処理装置17
を通過する。この際、1次処理装置16、2次処理装置
17とによって、地下水に含まれていた汚染物質が除去
される。また、2次処理装置17によって除去された汚
染物質は、回収口17aから回収される。First, groundwater rises in the water pipe 15 by driving the pumping pump 14. This groundwater is
Primary processing device 16 and secondary processing device 17 located on the ground
Pass through. At this time, the contaminants contained in the groundwater are removed by the primary treatment device 16 and the secondary treatment device 17. Further, the contaminants removed by the secondary processing device 17 are recovered from the recovery port 17a.
【0024】処理水は、圧送ポンプ18を駆動すること
によって圧送され、3次処理装置19を通過する。この
際、3次処理装置19によって、処理水に含まれている
極めて細かい汚染物質が除去される。また、3次処理装
置19によって除去された物質は、回収口19aから回
収される。The treated water is pressure-fed by driving the pressure-feed pump 18, and passes through the tertiary treatment device 19. At this time, the tertiary treatment device 19 removes extremely fine contaminants contained in the treated water. The substance removed by the tertiary treatment device 19 is recovered from the recovery port 19a.
【0025】さらに、3次処理装置19から排出された
処理水に、薬品添加装置20によって薬品が添加され
る。Further, chemicals are added to the treated water discharged from the tertiary treatment device 19 by the chemical addition device 20.
【0026】この後、薬品が添加された処理水は注水孔
13に達し、注水孔13から地盤1に容易に浸透する。
そして、処理水に添加された薬品が汚染土壌に吸着され
た重金属等の汚染物質に作用してこれらの土壌からの離
脱又は溶出が促進される。ここで、薬品として低pHの
酸性物質を用いた場合には、地盤の負荷電状態が緩和さ
れ重金属等の陽イオンが土壌から離脱し易くなり、薬品
としてイオン交換樹脂の粉末を用いた場合には、直接重
金属等と反応して重金属等が土壌から離脱する。After that, the treated water to which the chemical is added reaches the water injection hole 13 and easily permeates into the ground 1 through the water injection hole 13.
Then, the chemicals added to the treated water act on the pollutants such as heavy metals adsorbed on the contaminated soil to promote their release or elution from these soils. Here, when an acidic substance having a low pH is used as a chemical, the negatively charged state of the ground is eased and cations such as heavy metals are easily released from the soil, and when an ion exchange resin powder is used as a chemical. Reacts directly with heavy metals, etc., and the heavy metals, etc. separate from the soil.
【0027】このように、汚染物質が離脱あるいは溶出
した地下水が再び前記揚水孔12から揚水されて1次〜
3次処理装置16,17,19により処理されるといっ
たサイクルが繰り返されることにより、汚染土壌が漸次
清浄化される。そして、揚水された地下水内に汚染物質
が検出されないかあるいは許容値以下になるまで、前記
サイクルを継続する。In this way, the groundwater from which the pollutants have been released or eluted is pumped again from the pumping holes 12 and the primary to
The contaminated soil is gradually cleaned by repeating the cycle of being treated by the tertiary treatment devices 16, 17, and 19. Then, the cycle is continued until no pollutants are detected in the pumped groundwater or the pollutants are below the allowable value.
【0028】本実施例の汚染土壌の清浄化装置10及び
清浄化方法よれば、地下水に含まれる汚染物質が、1次
処理装置16、2次処理装置17及び3次処理装置19
によって除去され、外部に回収されるため、清浄化され
た地下水のみが、地盤11に注水、還元される。これに
よって地盤11内の汚染物質を地下水を介して除去する
ことができる。According to the contaminated soil cleaning device 10 and the cleaning method of this embodiment, the pollutants contained in the groundwater are treated as the primary treatment device 16, the secondary treatment device 17, and the tertiary treatment device 19.
Since it is removed by and is collected outside, only the cleaned groundwater is injected and returned to the ground 11. As a result, the pollutants in the ground 11 can be removed via groundwater.
【0029】さらに、3次処理装置19から排出される
処理水に、薬品添加装置20により汚染物質の離脱ある
いは溶出を促進する薬品が添加されているので、処理水
を地盤11内に注入すると薬品が添加された処理水が地
盤11内に浸透し、汚染土壌に吸着された重金属等の汚
染物の離脱・溶出が促進されて地下水に溶出し、再び揚
水孔から揚水されて汚染物質回収装置により汚染物質が
除去される。このように、揚水、汚染物質の回収、薬品
の添加、注水とからなるサイクルを繰り返すことによ
り、汚染物質を効率よく離脱・溶出させて、汚染土壌の
清浄化を完全ならしめることができる。Furthermore, the treated water discharged from the tertiary treatment device 19 is added with a chemical that promotes the removal or elution of pollutants by the chemical addition device 20. Therefore, when the treated water is injected into the ground 11, the chemical is added. The treated water with added water permeates into the ground 11, promotes the removal and elution of pollutants such as heavy metals adsorbed on the contaminated soil, elutes into the groundwater, and is pumped up again from the pumping hole and by the pollutant recovery device. Pollutants are removed. In this way, by repeating the cycle of pumping water, collecting pollutants, adding chemicals, and injecting water, pollutants can be efficiently released and eluted to completely clean the contaminated soil.
【0030】前記実施例では、揚水孔12から地下水を
揚水して注入孔13から注水するといった循環方式であ
り作業が単純であるといった利点がある。さらに、揚水
の水質分析により清浄化効果を確認しながら清浄化作業
を進めることができる。The above-mentioned embodiment has a merit that the work is simple because it is a circulation system in which groundwater is pumped from the pumping hole 12 and poured from the injection hole 13. Furthermore, the cleaning work can be carried out while confirming the cleaning effect by analyzing the quality of the pumped water.
【0031】ところで、土壌汚染は地下水面よりも上部
の不飽和帯に分布する場合が多いが、注入孔13から注
入する流量を大きく設定して地下水面を強制的に上昇さ
せて不飽和帯を飽和帯にして、前記清浄化方法を適用す
ることで、不飽和帯に分布する汚染土壌を清浄化するこ
ともできる。By the way, soil contamination is often distributed in the unsaturated zone above the water table, but the flow rate injected from the injection hole 13 is set to a large value to forcibly raise the water table to form the unsaturated zone. By applying the cleaning method to the saturated zone, the contaminated soil distributed in the unsaturated zone can be cleaned.
【0032】なお、本実施例では3つの処理装置16,
17,19を用いて汚染物質の除去を行なったが、地盤
1の汚染状況によって、例えば1次処理装置16と2次
処理装置17を1つの装置として構成したり、処理装置
の数を増加させてもよい。In this embodiment, the three processing units 16,
Although the contaminants were removed using 17 and 19, depending on the contamination status of the ground 1, for example, the primary treatment device 16 and the secondary treatment device 17 may be configured as one device, or the number of treatment devices may be increased. May be.
【0033】また、揚水孔2及び注水孔3が位置する帯
水層は、同一の帯水層としても、異なる帯水層としても
何ら問題はない。The aquifers in which the pumping holes 2 and the pouring holes 3 are located may be the same aquifer or different aquifers without any problem.
【0034】また、前記実施例では、揚水孔12と注水
孔13とを別々に掘削して設けているが、1つの掘削孔
をパッカー等の仕切り部材で上下に仕切り、例えば下部
の掘削孔を揚水孔として構成し、上部の掘削孔として構
成し、下部と上部とを前記実施例に示すような清浄化装
置を配置するようにしてもよい。この場合には、仕切り
部材の配置される部分に不透水層が位置するようにする
ことが好ましい。Further, in the above embodiment, the pumping hole 12 and the water injection hole 13 are separately excavated, but one excavating hole is vertically divided by a partition member such as a packer, and for example, the lower excavating hole is formed. It may be configured as a water pumping hole and as an upper drilling hole, and the lower part and the upper part may be provided with the cleaning device as shown in the above embodiment. In this case, it is preferable that the impermeable layer is located at the portion where the partition member is arranged.
【0035】[0035]
【発明の効果】以上のように、本発明の汚染土壌の清浄
化方法によれば、汚染土壌を含む地盤を掘削して形成さ
れた揚水孔から地下水を揚水し、揚水された地下水を汚
染物質回収装置を通した後、地盤を掘削して形成された
注水孔に注水する汚染土壌の清浄化方法であって、前記
汚染物質回収装置から排出された処理水に汚染物質の土
壌からの離脱や溶出を促進する薬品を添加するので、地
下水に含まれる汚染物質を、汚染物質回収装置によって
除去することができ、薬品が添加された処理水を地盤内
に浸透させ、汚染土壌に吸着された重金属等の汚染物の
離脱・溶出を促進し、再び揚水孔から揚水して汚染物質
回収装置により汚染物質を効率的に除去することがで
き、汚染土壌の清浄化を完全ならしめることができる。As described above, according to the method for cleaning polluted soil of the present invention, groundwater is pumped from the pumping hole formed by excavating the soil containing the polluted soil, and the pumped groundwater is polluted. A method for cleaning contaminated soil, which comprises pouring water into a water injection hole formed by excavating the ground after passing through a recovery device, wherein the treated water discharged from the pollutant recovery device separates pollutants from soil and Since a chemical that promotes elution is added, the pollutants contained in groundwater can be removed by a pollutant recovery device, and the treated water containing the chemical is allowed to penetrate into the ground, and the heavy metals adsorbed on the polluted soil. It is possible to promote the removal and elution of pollutants such as, and to pump water again from the pumping holes to efficiently remove pollutants by the pollutant recovery device, and to completely clean polluted soil.
【0036】また、本発明の汚染土壌の清浄化装置によ
れば、汚染土壌を含む地盤を掘削して形成された揚水孔
から地下水を揚水する揚水装置と、この揚水装置により
揚水された地下水を地盤を掘削して形成された注水孔に
導く導水路と、この導水路に介装された汚染物質回収装
置とを備える汚染土壌の清浄化装置であって、前記汚染
物質回収装置から排出された処理水に汚染物質の土壌か
らの離脱や溶出を促進する薬品を添加する薬品添加装置
を設けたので、汚染物質回収装置により地下水に含まれ
ていた汚染物質を除去することができ、薬品添加装置に
より薬品が添加された処理水を地盤内に浸透させ、汚染
土壌に吸着された重金属等の汚染物の離脱・溶出を促進
し、再び揚水孔から揚水して汚染物質回収装置により汚
染物質を効率的に除去することができ、汚染土壌の清浄
化を完全ならしめることができる。Further, according to the contaminated soil cleaning apparatus of the present invention, the pumping apparatus for pumping groundwater from the pumping hole formed by excavating the soil containing the polluted soil, and the groundwater pumped by this pumping apparatus. A device for purifying contaminated soil, comprising a water conduit leading to a water injection hole formed by excavating the ground, and a pollutant collecting device interposed in the water conduit, which is discharged from the pollutant collecting device. Since a chemical addition device is added to the treated water to add a chemical that promotes the release and elution of pollutants from the soil, it is possible to remove the pollutants contained in the groundwater with the pollutant recovery device. The permeation of treated water with added chemicals into the ground promotes the removal and elution of pollutants such as heavy metals adsorbed on contaminated soil, and pumps water from the pumping hole again to efficiently pollutants with the pollutant recovery device. To Can be removed by, it is possible that makes it complete the cleaning of the contaminated soil.
【図1】本発明の一実施例の汚染土壌の清浄化装置を示
す縦断面図である。FIG. 1 is a vertical cross-sectional view showing an apparatus for cleaning contaminated soil according to an embodiment of the present invention.
【図2】本発明の先行技術の地下水の清浄化装置を示す
縦断面である。FIG. 2 is a longitudinal section showing a prior art groundwater cleaning device of the present invention.
10 汚染土壌の清浄化装置 11 地盤 12 揚水孔 13 注水孔 14 揚水ポンプ(揚水装置) 15 導水管(導水路) 16 1次処理装置(汚染物質回収装置) 17 2次処理装置(汚染物質回収装置) 19 3次処理装置(汚染物質回収装置) 20 薬品添加装置 10 Cleaner for contaminated soil 11 Ground 12 Pumping hole 13 Water injection hole 14 Pumping pump (pumping device) 15 Water pipe (conducting channel) 16 Primary treatment device (pollutant recovery device) 17 Secondary treatment device (pollutant recovery device) ) 19 Tertiary treatment device (pollutant recovery device) 20 Chemical addition device
Claims (4)
た揚水孔から地下水を揚水し、揚水された地下水を汚染
物質回収装置を通した後、地盤を掘削して形成された注
水孔に注水する汚染土壌の清浄化方法であって、前記汚
染物質回収装置から排出された処理水に汚染物質の土壌
からの離脱や溶出を促進する薬品を添加することを特徴
とする汚染土壌の清浄化方法。1. A groundwater is pumped from a pumping hole formed by excavating a soil containing contaminated soil, the pumped groundwater is passed through a pollutant recovery device, and then the groundwater is formed into a water injection hole formed by excavating the ground. A method for cleaning contaminated soil, which comprises pouring water into the treated water discharged from the pollutant recovery device and adding a chemical that promotes release and elution of the pollutant from the soil. Method.
を特徴とする請求項1記載の汚染土壌の清浄化方法。2. The method for cleaning contaminated soil according to claim 1, wherein the chemical is an acidic substance having a low pH.
ことを特徴とする請求項1記載の汚染土壌の清浄化方
法。3. The method for cleaning contaminated soil according to claim 1, wherein the chemical is a powder of an ion exchange resin.
た揚水孔から地下水を揚水する揚水装置と、この揚水装
置により揚水された地下水を地盤を掘削して形成された
注水孔に導く導水路と、この導水路に介装された汚染物
質回収装置とを備えた汚染土壌の清浄化装置であって、
前記汚染物質回収装置から排出された処理水に汚染物質
の土壌からの離脱や溶出を促進する薬品を添加する薬品
添加装置を設けたことを特徴とする汚染土壌の清浄化装
置。4. A pumping device for pumping groundwater from a pumping hole formed by excavating the ground containing contaminated soil, and a conduit for guiding the groundwater pumped by the pumping device to a water injection hole formed by excavating the ground. A device for cleaning contaminated soil, comprising a waterway and a pollutant recovery device interposed in the waterway,
A cleaning device for contaminated soil, comprising a chemical addition device for adding a chemical that promotes release and elution of pollutants from soil to the treated water discharged from the pollutant recovery device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22759993A JP3232494B2 (en) | 1993-09-13 | 1993-09-13 | Method for cleaning contaminated soil and cleaning apparatus used in the method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22759993A JP3232494B2 (en) | 1993-09-13 | 1993-09-13 | Method for cleaning contaminated soil and cleaning apparatus used in the method |
Publications (2)
Publication Number | Publication Date |
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JPH0782729A true JPH0782729A (en) | 1995-03-28 |
JP3232494B2 JP3232494B2 (en) | 2001-11-26 |
Family
ID=16863462
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JP22759993A Expired - Fee Related JP3232494B2 (en) | 1993-09-13 | 1993-09-13 | Method for cleaning contaminated soil and cleaning apparatus used in the method |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003033756A (en) * | 2001-07-24 | 2003-02-04 | Fujita Corp | Decontamination method for hardly water-permeable ground |
JP2005299123A (en) * | 2004-04-07 | 2005-10-27 | East Japan Railway Co | Recharge method and recharge structure |
JP2010000452A (en) * | 2008-06-20 | 2010-01-07 | Takenaka Komuten Co Ltd | Cleaning well and cleaning method of contaminated soil |
-
1993
- 1993-09-13 JP JP22759993A patent/JP3232494B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003033756A (en) * | 2001-07-24 | 2003-02-04 | Fujita Corp | Decontamination method for hardly water-permeable ground |
JP4713777B2 (en) * | 2001-07-24 | 2011-06-29 | 株式会社フジタ | Purification method for poorly permeable ground |
JP2005299123A (en) * | 2004-04-07 | 2005-10-27 | East Japan Railway Co | Recharge method and recharge structure |
JP4585221B2 (en) * | 2004-04-07 | 2010-11-24 | 東日本旅客鉄道株式会社 | Condensation method and condensate structure used therefor |
JP2010000452A (en) * | 2008-06-20 | 2010-01-07 | Takenaka Komuten Co Ltd | Cleaning well and cleaning method of contaminated soil |
Also Published As
Publication number | Publication date |
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JP3232494B2 (en) | 2001-11-26 |
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