JP2006043602A - Treatment system for contaminated soil - Google Patents

Treatment system for contaminated soil Download PDF

Info

Publication number
JP2006043602A
JP2006043602A JP2004229119A JP2004229119A JP2006043602A JP 2006043602 A JP2006043602 A JP 2006043602A JP 2004229119 A JP2004229119 A JP 2004229119A JP 2004229119 A JP2004229119 A JP 2004229119A JP 2006043602 A JP2006043602 A JP 2006043602A
Authority
JP
Japan
Prior art keywords
casing
water
permeable
contaminated soil
pumping
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
JP2004229119A
Other languages
Japanese (ja)
Inventor
Minoru Kanazawa
稔 金澤
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.)
Obayashi Corp
Original Assignee
Obayashi Corp
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 Obayashi Corp filed Critical Obayashi Corp
Priority to JP2004229119A priority Critical patent/JP2006043602A/en
Publication of JP2006043602A publication Critical patent/JP2006043602A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Water Treatment By Sorption (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To surely recover ground water and gas in soil comprising contaminants even if the recovery of the contaminants is difficult since the presence of a layer hard to permeate water or a layer hard to permeate gas obstructs the same. <P>SOLUTION: Regarding the treatment system 1 for contaminated soil, the inside of contaminated soil 2 is provided with a pumping well 3, and the pumping well is mainly composed of a casing 4 made of a hollow cylindrical steel tube and gravel 5 as a gas-water permeable material arranged so as to surround the circumferential face and the bottom face thereof. The lower end of the casing is provided with a strainer part 7 as shown in figure (b), further, the upper position of the strainer part is provided with an adsorbent cartridge 10 capable of adsorbing the contaminants within the casing 4, and in the upper part of the adsorbent cartridge 10, a storage pump 8 and a column pipe 9 communicating with the storage pump are installed within the casing. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、主として有機塩素化合物を汚染物質として含む汚染土壌を無害化する汚染土壌の処理システムに関する。   The present invention relates to a contaminated soil treatment system for detoxifying contaminated soil mainly containing an organic chlorine compound as a contaminant.

工場跡地の土壌内には、揮発性有機塩素化合物、燃料油や機械油、ダイオキシン類、あるいはカドミウム、鉛、銅、亜鉛、ニッケル、クロムなどの重金属といったさまざまな汚染物質が土壌に混入していることがある。   Various pollutants such as volatile organochlorine compounds, fuel oils and machine oils, dioxins, or heavy metals such as cadmium, lead, copper, zinc, nickel, and chromium are mixed in the soil of the factory site. Sometimes.

かかる汚染物質で汚染された汚染土をそのまま放置すると、該土に混入している汚染物質が周囲に拡散し、周辺住民の生活に支障を来すとともに、雨水によって土粒子から遊離した場合には、地下水等に混入して水質を汚濁させる原因ともなる。そのため、上述した汚染物質で汚染された土については、さまざまな方法を使って浄化しなければならない。   If the contaminated soil contaminated with such contaminants is left as it is, the contaminants mixed in the soil will diffuse to the surroundings, hindering the lives of the surrounding residents, and if they are released from the soil particles by rainwater In addition, it may cause contamination of groundwater by contaminating water quality. Therefore, the soil contaminated with the above-mentioned pollutants must be cleaned using various methods.

土壌内の汚染物質を原位置で浄化処理する方法としては、従来からさまざまな方法が開発されており、掘削曝気法、揚水曝気法等をはじめ、土壌ガス吸引法、汚染土壌に注水しこれを揚水して地上で処理するいわゆる通水洗浄法、空気を送り込んでその気泡に汚染物質を連行させる、いわゆる気泡連行浄化法、空気圧入とガス吸引を組み合わせたエアスパージング法、土中菌の微生物活性を利用したバイオレメディエーションによる方法など多種多様な方法が知られている。   Various methods have been developed to purify the pollutants in the soil in-situ, including the excavation aeration method and the pumped aeration method, as well as the soil gas suction method and water injection into the contaminated soil. So-called water washing method that pumps water and treats on the ground, so-called bubble entrainment purification method that sends air and entrains pollutants in the bubbles, air sparging method that combines air pressure and gas suction, microbial activity of soil fungi A wide variety of methods are known, such as a method using bioremediation using a biotin.

ここで、主に機械部品などの脱脂洗浄に使用されるトリクロロエチレンや、ドライクリーニングの洗浄液として使用されるテトラクロロエチレンといった揮発性有機塩素化合物は、土壌ガス吸引法やエアスパージング法を用いて気化回収を図ることが多い。   Here, volatile organochlorine compounds such as trichlorethylene, which is mainly used for degreasing cleaning of machine parts, and tetrachloroethylene, which is used as a cleaning liquid for dry cleaning, are vaporized and recovered using a soil gas suction method or an air sparging method. There are many cases.

特開2000−42537号公報JP 2000-42537 A

ここで、揮発性有機塩素化合物といってもその蒸気圧はさまざまであり、例えばトリクロロエチレンの蒸気圧は7.8 kPa(20℃)、テトラクロロエチレンの蒸気圧は1.9 kPa(20℃)であるため、トリクロロエチレンは気化回収しやすいが、テトラクロロエチレンは気化回収に時間がかかる。   Here, even if it is a volatile organochlorine compound, its vapor pressure varies.For example, the vapor pressure of trichlorethylene is 7.8 kPa (20 ° C), and the vapor pressure of tetrachlorethylene is 1.9 kPa (20 ° C). Although it is easy to evaporate and recover, tetrachloroethylene takes time to evaporate and recover.

すなわち、上述した掘削曝気法、揚水曝気法、土壌ガス吸引法等を用いて気化回収を図ろうとしても、揮発性有機塩素化合物の種類によっては、蒸気圧が低いために曝気による気化が遅くなり、回収処理に長時間を要するという問題を生じていた。   In other words, vaporization and recovery using the above-described excavation aeration method, pumped water aeration method, soil gas suction method, etc. may slow down vaporization due to aeration because of the low vapor pressure depending on the type of volatile organic chlorine compound. The recovery process takes a long time.

また、重金属については曝気による回収は困難であるという問題や、地上で処理する土壌ガス吸引法や通水洗浄法では地上での処理設備が必要となるため、汚染サイトの広さによっては、かかる処理方法を採用できないことがあるという問題も生じていた。   In addition, it is difficult to recover heavy metals by aeration, and the ground gas treatment method and water flow cleaning method require ground treatment facilities, so this may depend on the size of the contaminated site. There has also been a problem that the processing method may not be adopted.

加えて、土壌、特に堆積岩を主体とする土壌は、異なる土質性状からなる複数の層が堆積してなるものであることは言うまでもないが、かかる層に難透水層や難透気層が存在する場合、揚水曝気法、通水洗浄法、ガス吸引法などを用いて地下水を揚水しあるいはガスを吸引しようとしても、揚水箇所あるいは吸引箇所と難透水層や難透気層との相対位置関係によっては、難透水層や難透気層の存在が障害となって揚水や吸引による汚染物質の回収が困難になるという問題も生じていた。   In addition, it goes without saying that soils, especially soils mainly composed of sedimentary rocks, are composed of multiple layers of different soil properties, but there are poorly permeable and hardly permeable layers in such layers. If the groundwater is pumped or the gas is sucked using the pumping aeration method, the flushing method, the gas suction method, etc., depending on the relative positional relationship between the pumping point or the suction point and the hardly permeable layer or hardly permeable layer However, the presence of the poorly permeable layer and the hardly permeable layer has been a problem, and it has become difficult to collect contaminants by pumping or sucking.

本発明は、上述した事情を考慮してなされたもので、難透水層や難透気層の存在が障害となって汚染物質の回収が困難な場合であっても、汚染物質が含まれた土壌内の地下水やガスを確実に回収することが可能な汚染土壌の処理システムを提供することを目的とする。   The present invention has been made in consideration of the above-described circumstances, and even if it is difficult to recover the pollutant due to the presence of the hardly water-permeable layer or the hardly air-permeable layer, the contaminant is included. An object of the present invention is to provide a contaminated soil treatment system capable of reliably collecting groundwater and gas in the soil.

上記目的を達成するため、本発明に係る汚染土壌の処理システムは請求項1に記載したように、揮発性有機塩素化合物、重金属等の汚染物質を含む汚染土壌内に揚水井を設けてなる汚染土壌の処理システムにおいて、前記揚水井をケーシングとその周面及び底面を取り囲むように配置された透水材とから構成するとともに前記ケーシングの下端に吸水用開口が形成されたストレーナ部を設け、前記ケーシング内の前記ストレーナ部の上方位置に前記汚染物質を吸着可能な吸着材を充填するとともに該吸着材の上方に揚水ポンプ及び該揚水ポンプに連通接続された揚水管を設置したものである。   In order to achieve the above-mentioned object, the contaminated soil treatment system according to the present invention is, as described in claim 1, a pollution in which a pumping well is provided in contaminated soil containing contaminants such as volatile organic chlorine compounds and heavy metals. In the soil treatment system, the pumping well is composed of a casing and a water-permeable material arranged so as to surround the circumferential surface and the bottom surface thereof, and a strainer portion having a water absorption opening formed at the lower end of the casing is provided, and the casing An adsorbent capable of adsorbing the pollutant is filled in an upper position of the strainer portion, and a pumping pump connected to the pumping pump is connected to the upper portion of the adsorbent.

また、本発明に係る汚染土壌の処理システムは、前記透水材を透気可能な透気透水材とするとともに、前記吸水用開口を吸気可能な吸気吸水用開口とし、前記揚水管の地上側吐出口に接続される真空ポンプと前記ケーシングの頂部に取り付けられる気密性キャップとを備えたものである。   Further, the contaminated soil treatment system according to the present invention is configured such that the water permeable material is an air permeable water permeable material, and the water intake opening is an intake water intake opening capable of intake air, and the ground discharge of the pump pipe is performed. A vacuum pump connected to the outlet and an airtight cap attached to the top of the casing.

本発明に係る汚染土壌の処理システムにおいては、揚水井をケーシングとその周面及び底面を取り囲むように配置された透水材とから構成するとともに前記ケーシングの下端に吸水用開口が形成されたストレーナ部を設け、前記ケーシング内の前記ストレーナ部の上方位置に前記汚染物質を吸着可能な吸着材を充填するとともに該吸着材の上方に揚水ポンプ及び該揚水ポンプに連通接続された揚水管を設置してある。   In the contaminated soil treatment system according to the present invention, the water well is composed of a casing and a water-permeable material disposed so as to surround the peripheral surface and the bottom surface thereof, and a strainer portion in which a water absorption opening is formed at the lower end of the casing. An adsorbent capable of adsorbing the pollutant at a position above the strainer portion in the casing, and a pumping pump connected to the pump and the pump connected to the pump. is there.

かかる構成において、揚水ポンプを駆動すると、揚水井周辺の地下水が揚水井に集水され、ストレーナ部の吸水用開口を介して吸着材に強制的に流入される流れが形成される。そして、吸着材に流入した地下水に含まれる汚染物質は、吸着材を通過する際に吸着除去される。   In such a configuration, when the pump is driven, groundwater around the pumping well is collected in the pumping well, and a flow is formed that is forced into the adsorbent through the water absorption opening of the strainer section. And the contaminant contained in the groundwater which flowed into the adsorbent is adsorbed and removed when passing through the adsorbent.

なお、吸着材によって汚染物質が除去された地下水は、揚水管を介して地上に揚水されるが、かかる地下水については、汚染土壌に再度戻して循環使用するなど適宜、有効利用すればよい。   The groundwater from which contaminants have been removed by the adsorbent is pumped to the ground via a pumping pipe. Such groundwater may be effectively used as appropriate, for example, by returning it to the contaminated soil and using it again.

ここで、本発明においては、揚水井をケーシングとその周面及び底面を取り囲むように配置された透水材とから構成してあるため、汚染土壌内の各層はそれぞれが透水材に連通した状態となっており、それゆえ、各層を流れ、あるいは滞留する地下水は、いったん透水材に流入し、次いで、該透水材内を流下した後、上述したように、ストレーナ部の吸水用開口を介して吸着材に強制的に流入される。   Here, in the present invention, since the pumping well is composed of a casing and a water-permeable material arranged so as to surround the peripheral surface and the bottom surface thereof, each layer in the contaminated soil is in a state where each layer communicates with the water-permeable material. Therefore, the groundwater that flows or stays in each layer once flows into the water-permeable material and then flows down through the water-permeable material, and then adsorbs through the water-absorbing openings of the strainer section as described above. It is forced into the material.

そのため、汚染土壌内に難透水層や透水層が複雑に積層している場合であっても、各透水層内の地下水は確実に揚水井に回収されることとなり、従来のように、難透水層の存在が邪魔になって透水層内の地下水を集水することができないといった事態を未然に回避することができる。   For this reason, even if difficultly permeable layers or permeable layers are laminated in the contaminated soil, the groundwater in each permeable layer is surely collected in the pumping well. It is possible to avoid a situation in which the existence of the layer becomes an obstacle and the groundwater in the permeable layer cannot be collected.

揚水井は、必要に応じて平面的に縦横に配置し、そのピッチを例えば3〜5mとすることが考えられる。また、揚水井の下端は、汚染物質が拡散している範囲の地下水を集水できるよう、汚染地下水が流れ、あるいは滞留している帯水層(飽和層であるか、不飽和層であるかは問わない)の下方にある難透水層あるいは不透水層まで貫入する。ちなみに、難透水層あるいは不透水層の下に別の帯水層があって該帯水層に存在する地下水も汚染されているのであれば、揚水井を上述した難透水層あるいは不透水層に貫通させ、さらにその下方にある別の難透水層あるいは不透水層にその下端を貫入する。   It is conceivable that the pumping wells are arranged vertically and horizontally in a plane as necessary, and the pitch is set to 3 to 5 m, for example. In addition, the bottom of the pumping well is aquifer (contains saturated or unsaturated) where contaminated groundwater flows or stays in order to collect groundwater in the area where pollutants are diffused. It penetrates to the hardly permeable layer or impervious layer below. By the way, if there is another aquifer under the impermeable layer or impermeable layer and the groundwater present in the aquifer is also contaminated, the pumping well is changed to the above-mentioned impermeable layer or impermeable layer. Further, the lower end is penetrated into another hardly water-permeable layer or water-impermeable layer below it.

ケーシングは、揚水ポンプが配置できる程度の内径、例えば小型の揚水ポンプを使用するのであれば、内径が100〜120mm程度の円筒中空鋼管で構成することができるが、地下水が該ケーシング内に充填された吸着材を確実に通過するためには、不透水性でなければならないことは言うまでもない。   The casing can be made of a cylindrical hollow steel pipe with an inner diameter of about 100 to 120 mm if an inner diameter that allows the arrangement of the pump is used, for example, a small pump, but groundwater is filled in the casing. Needless to say, in order to pass the adsorbent reliably, it must be impermeable.

透水材は、例えば砂利、砕石等の粗粒材で構成することができるが、該透水材を介して汚染土壌内のすべての層がケーシングの下端に設けられたストレーナ部と連通するよう、ケーシングの周面及び底面に連続的に配置する。   The water-permeable material can be composed of coarse particles such as gravel and crushed stone, but the casing is configured so that all layers in the contaminated soil communicate with the strainer provided at the lower end of the casing via the water-permeable material. It arrange | positions continuously on the surrounding surface and bottom face.

ストレーナ部は、ケーシングの下端近傍に透水孔等の吸水用開口を形成することで構成してもよいし、ケーシングとほぼ同径の中空多孔管を該ケーシングの下端に接合するようにしてもかまわない。   The strainer portion may be configured by forming a water absorption opening such as a water permeable hole in the vicinity of the lower end of the casing, or a hollow porous tube having the same diameter as the casing may be joined to the lower end of the casing. Absent.

吸着材は、ストレーナ部から流入した地下水が確実に該吸着材を通過するよう、例えばケーシング内に隙間なく充填するようにするとともに、吸着材の全断面がすべて有効に吸着作用を発揮するよう、ストレーナ部の上方位置に充填ないしは配置する。さらに、吸着材は、例えばケーシングを円筒中空鋼管とした場合、全体として外径がケーシングの内径にほぼ等しい円筒形をなすことになるが、その長さについては、汚染物質の濃度、地下水の水位や流速等を適宜勘案して決定すればよい。   The adsorbent is filled without any gaps in the casing, for example, so that the groundwater flowing in from the strainer part surely passes through the adsorbent, and the entire cross section of the adsorbent exhibits an effective adsorption action. Fill or place above the strainer. Furthermore, for example, when the casing is a cylindrical hollow steel pipe, the adsorbent has a cylindrical shape whose outer diameter is approximately equal to the inner diameter of the casing as a whole. And the flow rate and the like may be determined appropriately.

吸着材は、例えば活性炭をはじめ、木炭の粉末、珪藻土、ゼオライトなど公知の吸着材から適宜選択することができる。   The adsorbent can be appropriately selected from known adsorbents such as activated carbon, charcoal powder, diatomaceous earth, and zeolite.

揚水ポンプは、やはり吸着材の全断面がすべて有効に吸着作用を発揮するよう、その取水位置が吸着材の上方にくるように配置する。   The pump is also arranged so that the water intake position is above the adsorbent so that all the cross sections of the adsorbent exhibit effective adsorption.

ここで、揚水によって地下水位が低下し、あるいはもともと地下水位が低いために、汚染土壌内の特定層が不飽和層となることが考えられる。   Here, it is conceivable that the specific layer in the contaminated soil becomes an unsaturated layer because the groundwater level is lowered by pumping or the groundwater level is originally low.

かかるサイトの場合には、前記透水材を透気可能な透気透水材とするとともに、前記吸水用開口を吸気可能な吸気吸水用開口とし、前記揚水管の地上側吐出口に接続される真空ポンプと前記ケーシングの頂部に取り付けられる気密性キャップとを備えるようにすればよい。   In the case of such a site, the water-permeable material is a gas-permeable and water-permeable material that can be permeable, and the water-absorbing opening is an intake-and-water-absorbing opening that can be sucked, and is connected to the ground-side discharge port of the pumping pipe What is necessary is just to provide the airtight cap attached to the top part of a pump and the said casing.

かかる構成において、ケーシングの頂部に気密性キャップを取り付けた上、揚水ポンプの地上側吐出口に真空ポンプを接続し、しかる後、真空ポンプを駆動するようにすれば、不飽和層内で気体の状態で存在する汚染物質は、空気に連行されるようにしていったん透気透水材に流入し、次いで、該透気透水材内を流下した後、ストレーナ部の吸気吸水用開口を介して吸着材に強制的に流入される。   In such a configuration, if an airtight cap is attached to the top of the casing, a vacuum pump is connected to the ground-side discharge port of the pump, and then the vacuum pump is driven, gas in the unsaturated layer can be obtained. The pollutants present in the state once flow into the air-permeable and water-permeable material so as to be entrained by the air, and then flow down through the air-permeable and water-permeable material, and then the adsorbent through the intake water absorption opening of the strainer portion. It is forced to flow into.

そのため、汚染土壌内に難透気層や透気層が複雑に積層している場合であっても、各透気層内の汚染物質は、空気中にガス化した状態で確実に揚水井に回収されることとなり、従来のように、難透気層の存在が邪魔になって透気層内の汚染物質を集気することができないといった事態を未然に回避することができる。   For this reason, even if difficultly permeable layers or permeable layers are laminated in the contaminated soil, the contaminants in each permeable layer must be reliably gasified in the air in the pumping well. Thus, it is possible to avoid a situation in which the presence of the hardly permeable layer is obstructive and the contaminants in the permeable layer cannot be collected.

以下、本発明に係る汚染土壌の処理システムの実施の形態について、添付図面を参照して説明する。なお、従来技術と実質的に同一の部品等については同一の符号を付してその説明を省略する。   Embodiments of a contaminated soil treatment system according to the present invention will be described below with reference to the accompanying drawings. Note that components that are substantially the same as those of the prior art are assigned the same reference numerals, and descriptions thereof are omitted.

図1は、本実施形態に係る汚染土壌の処理システムを示した図である。同図(a)に示すように本実施形態に係る汚染土壌の処理システム1は、揮発性有機塩素化合物、重金属等の汚染物質を含む汚染土壌2内に揚水井3を設けてあり、該揚水井は、中空円筒鋼管からなるケーシング4と、その周面及び底面を取り囲むように配置された透気透水材としての砂利5とから概ね構成してある。   FIG. 1 is a diagram showing a contaminated soil treatment system according to the present embodiment. As shown in FIG. 1 (a), a contaminated soil treatment system 1 according to this embodiment includes a pumping well 3 in a contaminated soil 2 containing contaminants such as volatile organic chlorine compounds and heavy metals. The well is generally composed of a casing 4 made of a hollow cylindrical steel pipe and gravel 5 as an air-permeable and water-permeable material arranged so as to surround the peripheral surface and the bottom surface thereof.

ここで、ケーシングの下端には同図(b)に示すように、吸気吸水用開口である孔6が形成されたストレーナ部7を設けてあるとともに、該ストレーナ部の上方位置には、上述した汚染物質を吸着可能な吸着材カートリッジ10をケーシング4内に設けてあるとともに、該吸着材カートリッジ10の上方にはさらに、揚水ポンプ8及び該揚水ポンプに連通接続された揚水管9をケーシング4内に設置してある。   Here, the lower end of the casing is provided with a strainer portion 7 in which a hole 6 serving as an intake water intake opening is formed, as shown in FIG. An adsorbent cartridge 10 capable of adsorbing contaminants is provided in the casing 4, and further, above the adsorbent cartridge 10, a pumping pump 8 and a pumping pipe 9 connected to the pumping pump are connected to the casing 4. It is installed in.

吸着材カートリッジ10は、ケーシング4の内面に当接する円筒体11内に活性炭からなる吸着材12を充填してなり、該円筒体をその頂部にて揚水ポンプ8の台座に固定することで、揚水ポンプを引き上げれば、吸着材12を新しいものに交換できるようになっているとともに、吸着材カートリッジ10とケーシング4の内面との間が水密かつ気密になるように、かつケーシング4への挿入作業及び取出し作業がスムーズに行われるように、円筒体11の周面を、平滑処理したゴム等の弾性円筒体で構成してある。   The adsorbent cartridge 10 is formed by filling an adsorbent 12 made of activated carbon into a cylindrical body 11 that is in contact with the inner surface of the casing 4, and fixing the cylindrical body to the pedestal of the pumping pump 8 at the top thereof. If the pump is pulled up, the adsorbent 12 can be replaced with a new one, and the adsorbent cartridge 10 and the inner surface of the casing 4 become watertight and airtight, and inserted into the casing 4. In addition, the peripheral surface of the cylindrical body 11 is constituted by an elastic cylindrical body such as rubber subjected to smooth processing so that the take-out operation can be performed smoothly.

一方、揚水管9の地上側吐出口は、切替弁14a及び切替弁14bからなる切替装置14を介して二股に分岐させてあり、切替弁14bには真空ポンプ13を接続してあるとともに、図1(c)に示すようにケーシング4の頂部には気密性キャップ15を取り付けてある。   On the other hand, the discharge port on the ground side of the pumping pipe 9 is bifurcated via a switching device 14 including a switching valve 14a and a switching valve 14b, and a vacuum pump 13 is connected to the switching valve 14b. An airtight cap 15 is attached to the top of the casing 4 as shown in 1 (c).

本実施形態に係る汚染土壌の処理システム1を構築するには、まず、ケーシング4の外径に透気透水材である砂利5の厚みを加えた径の揚水孔を汚染土壌2に掘削形成する。   In order to construct the contaminated soil treatment system 1 according to the present embodiment, first, a pumping hole having a diameter obtained by adding the thickness of the gravel 5 which is an air permeable material to the outer diameter of the casing 4 is formed by excavation in the contaminated soil 2. .

汚染土壌2は、図1(a)に示すように、透気透水層21と難透気透水層22とが複雑に積層した地盤となっている。   As shown in FIG. 1A, the contaminated soil 2 is a ground in which an air permeable water permeable layer 21 and a hardly air permeable water permeable layer 22 are laminated in a complicated manner.

揚水孔の掘削形成は、例えば泥水を満たしながら行うことで孔壁の崩落を防止するようにするのが望ましい。   It is desirable to prevent the collapse of the hole wall by, for example, performing the excavation formation of the pumping hole while filling muddy water.

次に、揚水孔の掘削形成が終了したならば、必要に応じてその底部に沈殿しているスライムを除去する。   Next, when the excavation formation of the pumping hole is completed, the slime precipitated at the bottom portion is removed as necessary.

次に、透気透水材である砂利5を揚水孔に投入して孔底に敷き詰める。   Next, the gravel 5 which is an air permeable permeation | transmission material is thrown into a water pumping hole, and it spreads on the hole bottom.

次に、ストレーナ部7が予め形成されたケーシング4を揚水孔に建て込み、次いで、透水材カートリッジ10、揚水ポンプ8及び揚水管9をケーシング4内に挿入する。なお、透水材カートリッジ10や揚水ポンプ8あるいは揚水管9は、ケーシング4内に先行挿入した状態で揚水孔に建て込むようにしてもかまわない。   Next, the casing 4 in which the strainer portion 7 is formed in advance is built in the pumping hole, and then the water-permeable material cartridge 10, the pumping pump 8 and the pumping pipe 9 are inserted into the casing 4. Note that the water permeable material cartridge 10, the pumping pump 8, or the pumping pipe 9 may be built in the pumping hole in a state of being inserted into the casing 4 in advance.

次に、ケーシング4の周面及に透気透水材である砂利5を投入し、必要に応じて適宜締め固めることで、ケーシング4の周面及び底面を透気透水材としての砂利5で取り囲む。   Next, gravel 5 which is an air permeable permeation material is thrown into the peripheral surface of casing 4 and is compacted as necessary, so that the peripheral surface and bottom surface of casing 4 are surrounded by gravel 5 as an air permeable water permeable material. .

本実施形態に係る汚染土壌の処理システム1においては、揚水井3をケーシング4とその周面及び底面を取り囲むように配置された透気透水材である砂利5とから構成するとともに、ケーシング4の下端にストレーナ部7を設け、該ストレーナ部の上方位置に汚染物質を吸着可能な吸着材カートリッジ10を挿入するとともに該吸着材カートリッジの上方に揚水ポンプ8及び該揚水ポンプに連通接続された揚水管9を設置してある。   In the contaminated soil treatment system 1 according to the present embodiment, the pumping well 3 is composed of the casing 4 and gravel 5 which is an air permeable material disposed so as to surround the peripheral surface and the bottom surface thereof. A strainer section 7 is provided at the lower end, an adsorbent cartridge 10 capable of adsorbing contaminants is inserted above the strainer section, and a pumping pump 8 and a pumping pipe connected to the pump are connected above the adsorbent cartridge. 9 is installed.

かかる構成において地下水位が高い場合、切替弁14aを開いて切替弁14bを閉じ、かかる状態で揚水ポンプ8を駆動する。   In such a configuration, when the groundwater level is high, the switching valve 14a is opened and the switching valve 14b is closed, and the pumping pump 8 is driven in this state.

このようにすると、揚水井周辺の地下水が揚水井3に集水され、ストレーナ部7の吸気吸水用開口である孔6を介して吸着材カートリッジ10に強制的に流入される流れが形成される。   In this way, groundwater around the pumping well is collected in the pumping well 3, and a flow is formed that is forced to flow into the adsorbent cartridge 10 through the hole 6 that is the intake water intake opening of the strainer section 7. .

そして、吸着材カートリッジ10に流入した地下水に含まれているトリクロロエチレン、テトラクロロエチレンなどの有機塩素化合物や、カドミウム、鉛、銅、亜鉛、ニッケル、クロムなどの重金属といった汚染物質は、吸着材12を通過する際に吸着除去される。   Contaminants such as organic chlorine compounds such as trichlorethylene and tetrachloroethylene and heavy metals such as cadmium, lead, copper, zinc, nickel, and chromium contained in the groundwater flowing into the adsorbent cartridge 10 pass through the adsorbent 12. It is adsorbed and removed.

なお、吸着材12によって汚染物質が除去された地下水は、揚水管9を介して地上に揚水されるが、かかる地下水については、汚染土壌2に再度戻して循環使用するなど適宜、有効利用すればよい。   The groundwater from which the pollutants have been removed by the adsorbent 12 is pumped to the ground via the pumping pipe 9, and such groundwater can be reused and returned to the contaminated soil 2 for effective use as appropriate. Good.

ここで、本実施形態においては、揚水井3をケーシング4とその周面及び底面を取り囲むように配置された砂利5からなる透気透水材とから構成してあるため、汚染土壌2内の透気透水層21や難透気透水層22は、それぞれが透気透水材に連通した状態となる。   Here, in this embodiment, since the pumping well 3 is comprised from the casing 4 and the air permeable material which consists of the gravel 5 arrange | positioned so that the surrounding surface and bottom face may be surrounded, the permeability in the contaminated soil 2 is comprised. The air permeable layer 21 and the hardly permeable air permeable layer 22 are in a state of communicating with the air permeable material.

そのため、透気透水層21を流れ、あるいは滞留する地下水は図2に示すように、砂利5で構成された透気透水材にいったん流入し、次いで、該透気透水材内を流下した後、上述したように、ストレーナ部7の吸気吸水用開口である孔6を介して吸着材12に強制的に流入される。   Therefore, as shown in FIG. 2, the groundwater that flows or stays in the air permeable layer 21 once flows into the air permeable material composed of gravel 5, and then flows down in the air permeable material. As described above, it is forced to flow into the adsorbent 12 through the hole 6 that is the intake water intake opening of the strainer portion 7.

一方、地下水位が低い場合、切替弁14aを閉じ切替弁14bを開くとともに、気密性キャップ15をケーシング4の頂部に取り付け、かかる状態で真空ポンプ13を駆動する。   On the other hand, when the groundwater level is low, the switching valve 14a is closed and the switching valve 14b is opened, the airtight cap 15 is attached to the top of the casing 4, and the vacuum pump 13 is driven in this state.

このようにすると、揚水井周辺のガスが揚水井3に集気され、ストレーナ部7の吸気吸水用開口である孔6を介して吸着材カートリッジ10に強制的に流入される流れが形成される。   In this way, the gas around the pumping well is collected in the pumping well 3, and a flow is formed that is forced to flow into the adsorbent cartridge 10 through the hole 6 that is the intake water intake opening of the strainer section 7. .

そして、吸着材カートリッジ10に流入したガスに含まれている上述した汚染物質は、吸着材12を通過する際に吸着除去される。   The above-described contaminants contained in the gas flowing into the adsorbent cartridge 10 are adsorbed and removed when passing through the adsorbent 12.

ここで、本実施形態においては、上述したように、汚染土壌2内の透気透水層21や難透気透水層22は、それぞれが透気透水材に連通した状態となる。   Here, in this embodiment, as above-mentioned, the air-permeable water-permeable layer 21 and the hardly air-permeable water-permeable layer 22 in the contaminated soil 2 will be in the state which each communicated with the air-permeable water-permeable material.

そのため、透気透水層21を流れ、あるいは滞留するガスは、図2と同様、砂利5で構成された透気透水材にいったん流入し、次いで、該透気透水材内を流下した後、上述したように、ストレーナ部7の吸気吸水用開口である孔6を介して吸着材12に強制的に流入される。   Therefore, the gas flowing or staying in the air-permeable / permeable layer 21 once flows into the air-permeable and water-permeable material composed of gravel 5 and then flows down in the air-permeable and water-permeable material as in FIG. As described above, it is forced to flow into the adsorbent 12 through the hole 6 which is the intake water intake opening of the strainer portion 7.

以上説明したように、本実施形態に係る汚染土壌の処理システム1によれば、汚染土壌2内に難透気透水層22や透気透水層21が複雑に積層している場合であっても、各透気透水層内の地下水やガスは、確実に揚水井3に回収されることとなり、従来のように、難透気透水層の存在が邪魔になって透気透水層内の地下水やガスを回収することができないといった事態を未然に回避することが可能となる。   As described above, according to the contaminated soil treatment system 1 according to the present embodiment, even if the hardly permeable air permeable layer 22 and the permeable air permeable layer 21 are laminated in a complicated manner in the contaminated soil 2. The groundwater and gas in each permeable permeation layer are surely collected in the pumping well 3, and as in the conventional case, the presence of the hardly permeable permeation layer obstructs the groundwater and gas in the permeable permeation layer. It is possible to avoid the situation where the gas cannot be recovered.

本実施形態では特に言及しなかったが、吸着材カートリッジ10を、ケーシング4の内面に当接する円筒体11内に活性炭からなる吸着材12を充填して構成してあるとともに円筒体11をその頂部にて揚水ポンプ8の台座に固定してあるため、必要に応じて吸着材12を交換することができる。   Although not particularly mentioned in the present embodiment, the adsorbent cartridge 10 is configured by filling the adsorbent 12 made of activated carbon into the cylindrical body 11 in contact with the inner surface of the casing 4 and the cylindrical body 11 at the top thereof. , The adsorbent 12 can be replaced as needed.

すなわち、吸着材カートリッジ10を揚水ポンプ8ごと地上に引き上げ、次いで、吸着材カートリッジ10ごと交換するか、吸着材12だけを交換するかした後、揚水ポンプ8の台座に固定し直し、しかる後、ケーシング4内に挿入するようにすればよい。なお、揚水ポンプ8の撤去に伴い、ケーシング4内には汚染物質を含んだ地下水が流入する懸念があるが、新しい吸着材カートリッジ10を揚水ポンプ8とともにケーシング4に挿入する際、該揚水ポンプを駆動して揚水しながら吸着材カートリッジ10をケーシング4内に挿入するようにすれば、ケーシング内に流入している汚染水は、吸着材12を通過した上で揚水されるので、吸着材カートリッジの交換にあたって、なんら問題は生じない。汚染ガスの場合にも、吸着材カートリッジ10の取出し・挿入時を除き、気密性キャップ15をケーシング4の頂部に被せた状態で真空ポンプを駆動させつつ、吸着材カートリッジ10の昇降を行えば、やはりなんら問題は生じない。   That is, the adsorbent cartridge 10 is lifted to the ground together with the pump 8 and then either the entire adsorbent cartridge 10 is replaced or only the adsorbent 12 is replaced, and then fixed to the pedestal of the pump 8, What is necessary is just to insert in the casing 4. Although there is a concern that the groundwater containing pollutants flows into the casing 4 with the removal of the pumping pump 8, when the new adsorbent cartridge 10 is inserted into the casing 4 together with the pumping pump 8, the pumping pump is If the adsorbent cartridge 10 is inserted into the casing 4 while being driven and pumped, the contaminated water flowing into the casing passes through the adsorbent 12 and is pumped. There will be no problem with the exchange. Even in the case of contaminated gas, except when the adsorbent cartridge 10 is taken out and inserted, if the adsorbent cartridge 10 is moved up and down while driving the vacuum pump with the airtight cap 15 placed on the top of the casing 4, After all, no problem arises.

また、本実施形態では、吸着材12を活性炭で構成したが、汚染物質を吸着する材料としてかかる材料に限定されるものではないことは言うまでもない。   Moreover, in this embodiment, although the adsorbent 12 was comprised with activated carbon, it cannot be overemphasized that it is not limited to this material as a material which adsorb | sucks a contaminant.

また、本実施形態では、吸着材12を円筒体11内に入れることでカートリッジ式としたが、交換の要不要にかかわらず、吸着材12を直接ケーシング4に挿入するようにしてもかまわない。   In the present embodiment, the adsorbent 12 is placed in the cylindrical body 11 so as to be a cartridge type. However, the adsorbent 12 may be directly inserted into the casing 4 regardless of whether or not replacement is necessary.

また、本実施形態では、汚染物質が地下水に含まれている態様だけではなく、空気に含まれている態様も考慮したシステムとしたが、地下水位が高いサイトであってガス吸引を考慮する必要がないのであれば、切替装置14や真空ポンプ13を省略するとともに、砂利5を透水材とすればよい。   Further, in this embodiment, the system takes into consideration not only the mode in which the pollutant is contained in the groundwater but also the mode in which the pollutant is contained in the air. However, it is necessary to consider gas suction at a site where the groundwater level is high. If not, the switching device 14 and the vacuum pump 13 may be omitted and the gravel 5 may be a water permeable material.

また、本実施形態では特に言及しなかったが、砂利5で構成された透気透水材の一部をモルタル充填等で不透気透水材とすることで、浄化対象となる地層を選択することができる。   In addition, although not particularly mentioned in the present embodiment, by selecting a layer to be purified by using a part of the air-permeable and water-permeable material composed of gravel 5 as an air-impermeable and water-permeable material by mortar filling or the like. Can do.

図3は、地盤内にほぼ水平に拡がる難透気透水層22の下にある透気透水層に存在する汚染地下水あるいは汚染ガスを対象とした例であり、該難透気透水層より上方の砂利5の空隙にモルタルを充填することで不透気透水材31を形成してある。   FIG. 3 shows an example of contaminated groundwater or polluted gas existing in the air-permeable permeation layer under the non-air-permeable permeation layer 22 that extends almost horizontally in the ground. The air-impermeable water-permeable material 31 is formed by filling mortar in the gaps of the gravel 5.

本実施形態に係る汚染土壌の処理システムの概略図。Schematic of the processing system of the contaminated soil which concerns on this embodiment. 本実施形態に係る汚染土壌の処理システムの作用を示した図。The figure which showed the effect | action of the processing system of the contaminated soil which concerns on this embodiment. 変形例に係る汚染土壌の処理システムの概略図。Schematic of the processing system of the contaminated soil which concerns on a modification.

符号の説明Explanation of symbols

1 汚染土壌の処理システム
2 汚染土壌
3 揚水井
4 ケーシング
5 砂利(透気透水材、透水材)
7 ストレーナ部
8 揚水ポンプ
9 揚水管
12 吸着材
13 真空ポンプ
15 気密性キャップ
1 Contaminated soil treatment system 2 Contaminated soil 3 Pumping well 4 Casing 5 Gravel (air-permeable water-permeable material, water-permeable material)
7 Strainer section 8 Pumping pump 9 Pumping pipe 12 Adsorbent 13 Vacuum pump 15 Airtight cap

Claims (2)

揮発性有機塩素化合物、重金属等の汚染物質を含む汚染土壌内に揚水井を設けてなる汚染土壌の処理システムにおいて、
前記揚水井をケーシングとその周面及び底面を取り囲むように配置された透水材とから構成するとともに前記ケーシングの下端に吸水用開口が形成されたストレーナ部を設け、前記ケーシング内の前記ストレーナ部の上方位置に前記汚染物質を吸着可能な吸着材を充填するとともに該吸着材の上方に揚水ポンプ及び該揚水ポンプに連通接続された揚水管を設置したことを特徴とする汚染土壌の処理システム。
In the contaminated soil treatment system, which has a pumping well in the contaminated soil containing pollutants such as volatile organic chlorine compounds and heavy metals,
The pumping well is composed of a casing and a water-permeable material arranged so as to surround the peripheral surface and the bottom surface thereof, and is provided with a strainer portion in which a water absorption opening is formed at the lower end of the casing, and the strainer portion in the casing A contaminated soil treatment system, wherein an adsorbent capable of adsorbing the pollutant is filled in an upper position, and a pumping pump connected to the pumping pump and a pumping pipe connected to the pump are installed above the adsorbent.
前記透水材を透気可能な透気透水材とするとともに、前記吸水用開口を吸気可能な吸気吸水用開口とし、前記揚水管の地上側吐出口に接続される真空ポンプと前記ケーシングの頂部に取り付けられる気密性キャップとを備えた請求項1記載の汚染土壌の処理システム。 The water permeable material is an air permeable water permeable material that can be permeable, the water intake opening is an intake water intake opening that can be sucked, and a vacuum pump that is connected to the ground-side discharge port of the pumping pipe and the top of the casing. 2. The contaminated soil treatment system according to claim 1, further comprising an airtight cap attached thereto.
JP2004229119A 2004-08-05 2004-08-05 Treatment system for contaminated soil Pending JP2006043602A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004229119A JP2006043602A (en) 2004-08-05 2004-08-05 Treatment system for contaminated soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004229119A JP2006043602A (en) 2004-08-05 2004-08-05 Treatment system for contaminated soil

Publications (1)

Publication Number Publication Date
JP2006043602A true JP2006043602A (en) 2006-02-16

Family

ID=36022768

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004229119A Pending JP2006043602A (en) 2004-08-05 2004-08-05 Treatment system for contaminated soil

Country Status (1)

Country Link
JP (1) JP2006043602A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009050818A (en) * 2007-08-29 2009-03-12 Jfe Mineral Co Ltd Method for purifying contaminated soil and contaminated ground water
JP2009106879A (en) * 2007-10-31 2009-05-21 Sun Quest:Kk Construction method for cleaning soil
JP2009297617A (en) * 2008-06-11 2009-12-24 Takeo Suzuki Method for improving contaminated soil
JP2012086222A (en) * 2012-01-06 2012-05-10 Kumagai Gumi Co Ltd Method for cleaning underground oil-contaminated soil
JP2014054610A (en) * 2012-09-13 2014-03-27 Ohbayashi Corp Device and method for purifying groundwater
JP2016137417A (en) * 2015-01-26 2016-08-04 清水建設株式会社 Groundwater decontamination system and groundwater decontamination method
JP2016165670A (en) * 2015-03-09 2016-09-15 株式会社大林組 Underground purification wall
CN109502795A (en) * 2018-10-29 2019-03-22 山东省水利科学研究院 Individual well embedded mobile reactor
CN114054488A (en) * 2021-11-03 2022-02-18 浙江坤德创新岩土工程有限公司 Method for driving fluid to uniformly flow underground by negative pressure

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009050818A (en) * 2007-08-29 2009-03-12 Jfe Mineral Co Ltd Method for purifying contaminated soil and contaminated ground water
JP2009106879A (en) * 2007-10-31 2009-05-21 Sun Quest:Kk Construction method for cleaning soil
JP2009297617A (en) * 2008-06-11 2009-12-24 Takeo Suzuki Method for improving contaminated soil
JP2012086222A (en) * 2012-01-06 2012-05-10 Kumagai Gumi Co Ltd Method for cleaning underground oil-contaminated soil
JP2014054610A (en) * 2012-09-13 2014-03-27 Ohbayashi Corp Device and method for purifying groundwater
JP2016137417A (en) * 2015-01-26 2016-08-04 清水建設株式会社 Groundwater decontamination system and groundwater decontamination method
JP2016165670A (en) * 2015-03-09 2016-09-15 株式会社大林組 Underground purification wall
CN109502795A (en) * 2018-10-29 2019-03-22 山东省水利科学研究院 Individual well embedded mobile reactor
CN109502795B (en) * 2018-10-29 2024-03-01 山东省水利科学研究院 Single well embedded movable reactor
CN114054488A (en) * 2021-11-03 2022-02-18 浙江坤德创新岩土工程有限公司 Method for driving fluid to uniformly flow underground by negative pressure
CN114054488B (en) * 2021-11-03 2022-10-14 浙江坤德创新岩土工程有限公司 Method for driving fluid to uniformly flow underground by negative pressure

Similar Documents

Publication Publication Date Title
US6174108B1 (en) In-well air stripping and gas adsorption
JP3728510B2 (en) Soil pollution countermeasure method and soil pollution countermeasure system
JP2006043602A (en) Treatment system for contaminated soil
JP4923472B2 (en) Water wash structure for contaminated soil and water wash method using the same
JP4657008B2 (en) Contaminated ground purification system and purification method of contaminated ground
JP5205010B2 (en) In-situ purification method for contaminated groundwater
KR101720098B1 (en) Apparatus for remediating polluted ground water by VOCs
KR101691425B1 (en) Complex Purification System of Oil-polluted Underground Water by Physical and Chemical
JP5218853B2 (en) Recontamination prevention method after remediation of contaminated soil
JP4166891B2 (en) Method and apparatus for sucking harmful gas from underground pollutants
JP4556471B2 (en) Purification method for contaminated soil
JP2019000767A (en) Well for cleanup and soil cleanup method
JP2008212856A (en) Soil environment improvement apparatus and soil cleaning method
CN209940624U (en) Circulating well
JP3975426B2 (en) Contamination purification system for volatile organic compounds and its operation method
JP2002301465A (en) Cleaning system for soil and ground water polluted with volatile organic compound
JP2005074289A (en) Cleaning method for hardly-gas/water-permeable contaminated soil and system
JP4919998B2 (en) Purification method for oil contaminated parts
JP3830606B2 (en) Purification method for contaminated ground
JP2001029933A (en) Method and apparatus for cleaning polluted soil
JP2003154356A (en) Pumping aeration type apparatus and method for purifying ground water
JP2005074297A (en) Cleaning method for hardly-gas/water-permeable contaminated soil and system
JP4416535B2 (en) Purification method of soil with poor air permeability and permeability
JP3934580B2 (en) Contaminated ground purification method using both in-situ agitation and air injection suction, and purification device used therefor
JP2006088009A (en) Purification method of contamination of soil and ground water

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20070710

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20080325

RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20080401

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20090824

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090901

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20100105