JP2002355663A - Soil cleaning system with high pressure jet and method for the same - Google Patents

Soil cleaning system with high pressure jet and method for the same

Info

Publication number
JP2002355663A
JP2002355663A JP2001161134A JP2001161134A JP2002355663A JP 2002355663 A JP2002355663 A JP 2002355663A JP 2001161134 A JP2001161134 A JP 2001161134A JP 2001161134 A JP2001161134 A JP 2001161134A JP 2002355663 A JP2002355663 A JP 2002355663A
Authority
JP
Japan
Prior art keywords
water
soil
sand
sediment
solid
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
JP2001161134A
Other languages
Japanese (ja)
Inventor
Yosuke Shikata
洋介 志方
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.)
ICHINOMIYA KIMITAKE
Original Assignee
ICHINOMIYA KIMITAKE
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 ICHINOMIYA KIMITAKE filed Critical ICHINOMIYA KIMITAKE
Priority to JP2001161134A priority Critical patent/JP2002355663A/en
Publication of JP2002355663A publication Critical patent/JP2002355663A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To remove pollutants at an extremely low cost, with efficiency and in a short period of time because the pollutants stuck into soil can be removed by making a highly concentrated polluted-soil collide with a driven high pressure water in the course of sucking the highly concentrated polluted-soil from the ground by a gas mixed jet pump and sending it by pressure in a pipe. SOLUTION: The system is provided with a pressure-feed and cleaning device 12 where the pollutants stuck to earth and sand particles are separated and cleaned by making the three phases of gas, liquid and solid collide with each other by making the driven high pressure water collide with the polluted soil in the course of sucking the polluted soil from one end of the pipe 11 by using the gas mixed jet pump 10 and transporting the sucked polluted soil through the pipe 11, the first precipitation vessel 17 for solid-liquid separation which is composed of a water vessel filled with a cleaning water, receiving waste water containing the earth and sand cleaned by the device 12, and making the earth and sand precipitate, the second precipitation vessel 20 for solid-liquid separation which receives an overflow water from the first precipitation vessel, a sand filter 25 receiving the overflow water from the second precipitation vessel and filtering it by sand filter medium, and a circulation-water receiving vessel 30 receiving the water filtered by the sand filter.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、混気ジェットポン
プによる高圧噴流土壌洗浄システム、及び洗浄方法に関
し、特に、特に深層、浅層、或いは高濃度汚染、低濃度
汚染を問わず、低コストかつ効率的に汚染土壌を回収し
て浄化した上で、再び土壌中に戻すようにした高圧噴流
土壌洗浄システム及び洗浄方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-pressure jet soil cleaning system and a cleaning method using an air-mixing jet pump, and more particularly to a low-cost and low-concentration soil irrespective of a deep layer, a shallow layer, or a high-concentration or low-concentration contamination. The present invention relates to a high-pressure jet soil cleaning system and a cleaning method for efficiently collecting and purifying contaminated soil and returning the soil to soil again.

【0002】[0002]

【従来の技術】近年、土壌や地下水を汚染する物質とし
て、揮発性有機化合物(例えば、トリクロロエチレン、
ベンゼン、テトラクロロエチレン等)、石油系の炭化水
素が問題となっており、これらの汚染物質は土壌中に棲
息するある種のバクテリア(微生物)により長時間をか
けて分解されて無害化(バイオレメディエーション)す
るが、高濃度に汚染された土壌は、バクテリアの増殖、
活動に不可欠な酸素が欠乏した状態にあるため、人為的
にバクテリアの栄養剤や酸化還元剤を供給して増殖を促
進しない限り、短い期間内に汚染土壌を浄化することは
困難である。しかし、仮に人工的にバクテリアの増殖を
促進する対策を講じたとしても、土壌を十分に浄化して
無害化するためには、数年以上の長期間を要するのが普
通であり、社会的なニーズを満たすに足る浄化効率を備
えた浄化工法であるとは言い難い。
2. Description of the Related Art In recent years, volatile organic compounds (eg, trichloroethylene,
Benzene, tetrachloroethylene, etc.) and petroleum hydrocarbons have become a problem, and these pollutants are decomposed over time by certain bacteria (microorganisms) living in the soil, rendering them harmless (bioremediation). However, the highly contaminated soil can cause bacterial growth,
Due to the lack of oxygen essential for activities, it is difficult to clean up contaminated soil within a short period of time unless artificially supplying bacterial nutrients or redox agents to promote growth. However, even if measures are taken to artificially promote the growth of bacteria, it usually takes a long time of several years or more to sufficiently purify and detoxify the soil, It is hard to say that it is a purification method that has sufficient purification efficiency to meet the needs.

【0003】そこで、従来から、土壌汚染、地下水汚染
に対する対策として、ウェルポイント、或いはディープ
ウェルを、地盤内の汚染土壌部分に打設し、ウェルポイ
ント等を介して揚水して地下水位を低減させる一方で、
リチャージ工法によって別の場所から注水を行う浄化工
法が種々提案されている。この浄化工法は、例えばウェ
ルポイントを介して汚染土壌内の地下水を揚水し、揚水
した地下水を地上の浄化設備によって浄化した後で、他
の場所から地中に戻すという手法が中心である。しか
し、高度に汚染した土壌は、土粒子間隙が汚染物質で占
められており、土粒子間隙に水、空気(ガス)が浸入し
得ない透水性の悪い状況にある。このため、ウェルポイ
ント、或いはディープウェルを打設して揚水、注水作業
を実施したとしても、地層の層境等に十分な水みちを形
成することは困難であり、汚染土壌内に広く水流を形成
して浸透循環を促進し、土壌中に含まれる多くの汚染物
質を除去することは困難である。特に、シルト質の土壌
等のように、透水係数が低い土壌にあっては、ウェルポ
イント等を用いた浄化工法によって満足な結果を得るこ
とは困難である。つまり、従来の汚染土壌浄化工法は、
ウェルポイント、或いはディープウェルを地盤に打設し
て揚水してから、地中に戻すだけの単純な方法であった
ため、十分な浄化効果を発揮することができず、土壌の
浄化不良が常に問題となっていた。このため、作業のや
り直し、作業の長期化、投資金額の累積化等が問題とな
っている。また、このように揚水と注水の組み合わせに
よって土壌を浄化する従来の方法では、タールや重金属
による汚染土壌、汚染地下水の修復は困難であった。こ
のため、タールや重金属による汚染土壌等を浄化する手
法としては、汚染土壌を非汚染土壌に入れ替える土壌置
換工法が行われていたが、この工法は確実な効果を発揮
できるものの、大量の土壌入れ替えを行うために必要な
コスト、設備、工期、エネルギー環境収支の点で問題で
あり、実用性が低いという欠点を有している。
Therefore, conventionally, as a countermeasure against soil contamination and groundwater contamination, a well point or a deep well is cast in a contaminated soil portion in the ground, and the groundwater level is reduced by pumping water through the well point or the like. On the other hand,
Various purification methods for injecting water from another place by the recharge method have been proposed. This purification method mainly focuses on, for example, pumping groundwater in contaminated soil via a well point, purifying the pumped groundwater with a purification facility on the ground, and returning the groundwater from another place to the ground. However, in highly contaminated soil, the gap between the soil particles is occupied by contaminants, and water and air (gas) cannot penetrate into the gap between the soil particles. For this reason, even if a well point or a deep well is cast and pumping and water injection work is performed, it is difficult to form a sufficient water path at the stratum boundary of the stratum, etc. It is difficult to form and promote osmotic circulation and remove many pollutants contained in soil. In particular, it is difficult to obtain satisfactory results by a purification method using a well point or the like in a soil having a low permeability, such as a silty soil. In other words, the conventional contaminated soil purification method
Since it was a simple method of casting a well point or deep well on the ground, pumping water, and then returning it to the ground, it was not possible to exert a sufficient purification effect, and poor purification of the soil was always a problem Had become. Therefore, redoing work, prolonging work, accumulating investment amounts, and the like have become problems. Further, in the conventional method of purifying the soil by the combination of the pumping and the water injection, it is difficult to repair the contaminated soil and the contaminated groundwater by tar and heavy metals. For this reason, as a method of purifying soil contaminated by tar and heavy metals, a soil replacement method of replacing contaminated soil with non-contaminated soil has been performed. This is a problem in terms of cost, equipment, construction period, and energy environment balance required for performing the method, and has a drawback of low practicality.

【0004】また、汚染土壌領域の外周を遮水壁で封じ
込めるシーリングソイル工法も知られているが、この工
法を実施した場合には汚染物質は汚染土壌領域内に永久
的に残存し、土地利用が制限される、という欠点を有す
る。また、現位置洗浄工法は、汚染土壌中に有用バクテ
リア、或いは薬剤等を注入して汚染の解消を待つ工法で
あるが、確実性が低く、且つ汚染の低減に多大な時間を
要するという欠点を有する。また、タールや重金属汚染
に対しては効果が充分でないという欠点をも有する。更
に、土壌洗浄法は、汚染土壌を掘削して取り出し、プラ
ントに設置した回転ドラム内に投入して洗浄処理を施し
た上で、地盤に埋め戻すという作業を実施する工法であ
るが、大量の土砂を効率的に処理するためにはプラント
設備が大規模にならざるを得ないため、高コストなエネ
ルギー多消費型システムとなり、且つ土地利用の制限等
の立地条件等にも影響されるため一般的ではない。
[0004] A sealing soil method is also known in which the outer periphery of the contaminated soil area is sealed with a water impervious wall. However, when this method is implemented, the contaminants remain permanently in the contaminated soil area, and land use is reduced. Is limited. The in-situ cleaning method is a method of injecting useful bacteria or chemicals into the contaminated soil and waiting for the elimination of the contamination, but has the disadvantage that the reliability is low and that much time is required to reduce the contamination. Have. It also has the disadvantage that the effect on tar and heavy metal contamination is not sufficient. Furthermore, the soil washing method is a method of excavating and taking out contaminated soil, throwing it into a rotating drum installed in a plant, performing a washing process, and then burying the soil in the ground. In order to treat soil efficiently, plant facilities must be large-scale, resulting in a high-cost, energy-intensive system, and are affected by location conditions such as land use restrictions. Not a target.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記に鑑みて
なされたものであり、大規模、高コストでエネルギーを
大量に消費するプラント設備が一切不要でありながら、
揮発性有機化合物(例えば、トリクロロエチレン、ベン
ゼン、テトラクロロエチレン等)、油系の炭化水素、石
炭系の汚染物質により汚染された土壌のみならず、ター
ル、重金属等により高濃度汚染された土壌を短期間に効
率よく取り出して設備内で洗浄し、埋め戻すことができ
る高圧噴流土壌洗浄システム及び洗浄方法を提供するこ
とを課題とする。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above, and has no need for a large-scale, high-cost, large-scale energy-consuming plant facility.
Not only soils contaminated with volatile organic compounds (eg, trichloroethylene, benzene, tetrachloroethylene, etc.), oil-based hydrocarbons and coal-based pollutants, but also soils highly contaminated with tar, heavy metals, etc. in a short period of time An object of the present invention is to provide a high-pressure jet soil cleaning system and a cleaning method that can be efficiently taken out, washed in the facility, and backfilled.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するた
め、請求項1の発明は、混気ジェットポンプを利用して
管体の一端から汚染土壌を吸引し、吸引した汚染土壌を
管体内を搬送する過程で該汚染土壌に駆動高圧水を噴出
させて気体、固体、液体の三相を衝突させて土砂粒子に
付着した汚染物質を分離、洗浄する圧送洗浄装置と、洗
浄水を満たした水槽から成り、前記圧送洗浄装置により
洗浄を受けた土砂を含む排水を受け入れて土砂を沈殿さ
せる固液分離用の第1の沈殿槽と、該第1の沈殿槽から
の溢流水を受け入れる固液分離用の第2の沈殿槽と、該
第2の沈殿槽からの溢流水を受け入れて砂濾材により濾
過する砂濾過装置と、該砂濾過装置により濾過された水
を受け入れる循環水用受水槽と、を備えたことを特徴と
する。請求項2の発明は、請求項1において、前記循環
水用受水槽内の水を前記圧送洗浄装置、前記第1の沈殿
槽、又は前記第2の沈殿槽の少なくとも一つに対して循
環供給することを特徴とする。請求項3の発明は、請求
項1又は2に記載の発明において、前記第1の沈殿槽、
又は前記第2の沈殿槽内に沈殿した洗浄済み土砂を、地
盤内に戻すための高圧噴流土砂搬送装置を備えたことを
特徴とする。
According to a first aspect of the present invention, a contaminated soil is sucked from one end of a pipe using an air-mixing jet pump, and the sucked contaminated soil is passed through the pipe. A pressure-feed cleaning device for ejecting driving high-pressure water to the contaminated soil in the transporting process to collide three phases of gas, solid, and liquid to separate and clean contaminants attached to the soil particles, and a water tank filled with cleaning water A first sedimentation tank for solid-liquid separation for receiving wastewater containing sediment washed by the pressure-feed cleaning device and sedimenting the sediment, and a solid-liquid separation for receiving overflow water from the first sedimentation tank A second sedimentation tank, a sand filtration device for receiving the overflow water from the second sedimentation bath and filtering with a sand filter medium, and a circulating water receiving tank for receiving the water filtered by the sand filtration device; It is characterized by having. According to a second aspect of the present invention, in the first aspect, the water in the circulating water receiving tank is circulated and supplied to at least one of the pressure-feed cleaning device, the first sedimentation tank, or the second sedimentation tank. It is characterized by doing. The invention according to claim 3 is the invention according to claim 1 or 2, wherein the first settling tank,
Alternatively, there is provided a high-pressure jet sediment transport device for returning the washed sediment settled in the second settling tank to the ground.

【0007】請求項4の発明は、混気ジェットポンプを
利用して管体の一端から汚染土壌を吸引し、吸引した汚
染土壌を管体内を搬送する過程で該汚染土壌に駆動高圧
水を衝突させて気体、固体、液体の三相を衝突させて土
砂粒子表面に付着した汚染物質を分離、洗浄する圧送洗
浄ステップと、前記圧送洗浄装置により洗浄を受けた土
砂を含む排水を、洗浄水を満たした第1の沈殿槽内に供
給して土砂を沈殿させる第1の固液分離ステップと、前
記第1の沈殿槽からの溢流水を第2の沈殿槽内に供給し
て土砂を沈殿させる第2の固液分離ステップと、前記第
2の沈殿槽からの溢流水を受け入れて砂濾材により濾過
する砂濾過ステップと、前記砂濾材により濾過された水
を循環利用する循環利用ステップと、を備えたことを特
徴とする。請求項5の発明は、前記第1の固液分離ステ
ップにて固液分離されて第1の沈殿槽内に堆積した土砂
を高圧噴流土砂搬送装置によって吸引搬送して一旦保留
する保留ステップと、前記保留ステップにて一旦保留し
た土砂を再び前記混気ジェットポンプを利用して管体の
一端から吸引し、吸引した汚染土壌を管体内を搬送する
過程で汚染土壌に駆動高圧水を衝突させて気体、固体、
液体の三相を衝突させて土砂粒子表面に付着した汚染物
質を分離、洗浄する再圧送洗浄ステップと、前記圧送洗
浄装置により再度洗浄を受けた土砂を洗浄水を満たした
第1の沈殿槽内に供給して土砂を沈殿させる2度目の第
1の固液分離ステップと、を少なくとも備えたことを特
徴とする。
According to a fourth aspect of the present invention, contaminated soil is sucked from one end of a pipe using an air-jet pump, and driving high-pressure water collides with the contaminated soil in the process of transporting the sucked contaminated soil through the pipe. Gas, solid, and three phases of liquids are caused to collide with each other to separate and contaminate the contaminants attached to the surface of the earth and sand particles. A first solid-liquid separation step of feeding the filled first sedimentation tank to sediment the earth and sand, and supplying overflow water from the first sedimentation tank to the second sedimentation tank to sediment the earth and sand A second solid-liquid separation step, a sand filtration step of receiving overflow water from the second sedimentation tank and filtering it with a sand filter medium, and a circulating use step of circulating and using the water filtered by the sand filter medium. It is characterized by having. The invention of claim 5 is a holding step of sucking and transporting the sediment separated in the first solid-liquid separation step in the first solid-liquid separation step and deposited in the first sedimentation tank by a high-pressure jet sediment transport device, and temporarily retaining the soil. The sediment once held in the holding step is sucked again from one end of the pipe using the air-jet pump, and the high-pressure water is caused to collide with the contaminated soil in the process of transporting the sucked contaminated soil through the pipe. Gas, solid,
A re-pressure cleaning step of separating and cleaning contaminants adhering to the surface of the earth and sand particles by colliding the three phases of liquid, and a first settling tank filled with cleaning water by re-cleaning the soil and sand by the pressure cleaning apparatus. And a second first solid-liquid separation step of supplying sediment to settle the earth and sand.

【0008】[0008]

【発明の実施の形態】以下、本発明を図面に示した実施
の形態により詳細に説明する。図1は本発明の一実施形
態に係る高圧噴流土壌洗浄システム及び洗浄方法を実施
するための設備図、図2はそのシステムを実施する方法
を説明する図である。図1に示した高圧噴流土壌洗浄シ
ステム1は、汚染土壌を含んだ土壌改良区画3に設置さ
れるプラント設備2から成る。このプラント設備2は、
混気ジェットポンプから成る高圧噴流装置10を利用し
て管体11の一端から汚染土壌Sを吸引し、吸引した汚
染土壌Sを管体内を搬送する過程で汚染土壌にジェット
水を衝突させて気体、固体、液体の三相を衝突させて土
砂粒子に付着した汚染物質を分離、洗浄する圧送洗浄装
置12と、洗浄水16を満たした水槽15から成り、圧
送洗浄装置12により洗浄を受けた土砂13を受け入れ
て土砂13を沈殿させる固液分離用の土砂受水槽(一次
沈殿槽)17と、該土砂受水槽17からの溢流水を受け
入れる固液分離用の二次沈殿槽20と、該二次沈殿槽2
0からの溢流水を受け入れて砂濾材26により濾過する
砂濾過装置25と、該砂濾過装置25により濾過された
水を受け入れる循環水用受水槽30と、土砂受水槽17
内に沈殿した土砂を吸引して一旦保留位置に保留する高
圧噴流土砂搬送装置31と、を備える。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to embodiments shown in the drawings. FIG. 1 is a facility diagram for implementing a high-pressure jet soil cleaning system and a cleaning method according to an embodiment of the present invention, and FIG. 2 is a diagram illustrating a method for implementing the system. The high pressure jet soil cleaning system 1 shown in FIG. 1 includes plant equipment 2 installed in a soil improvement section 3 containing contaminated soil. This plant equipment 2
The contaminated soil S is sucked from one end of the pipe 11 using the high-pressure jet device 10 composed of an air-mixing jet pump, and the contaminated soil S is jetted against the contaminated soil in the process of transporting the sucked contaminated soil S through the pipe. And a water tank 15 filled with cleaning water 16 by separating and washing contaminants adhering to earth and sand particles by colliding three phases of solid and liquid, and sediment washed by the pressure washing apparatus 12 A sediment receiving tank (primary sedimentation tank) 17 for receiving solid 13 and sedimenting sediment 13, a secondary sedimentation tank 20 for solid-liquid separation for receiving overflow water from the sediment receiving tank 17, Next sedimentation tank 2
A sand filtration device 25 for receiving the overflow water from 0 and filtering it with a sand filter medium 26, a circulating water receiving tank 30 for receiving the water filtered by the sand filtration device 25, and a sediment receiving tank 17
And a high-pressure jet sediment transporting device 31 for sucking the sediment deposited therein and temporarily retaining the sediment at a retaining position.

【0009】圧送洗浄装置12は、高圧噴流装置(混気
ジェットポンプ)10を利用して管体11の一端から汚
染土壌Sを吸引し、吸引した汚染土壌Sを管体内を搬送
する過程で汚染土壌にジェット水を衝突させて気体、固
体、液体の三相を衝突させて土砂粒子に付着した汚染物
質を除去する手段である。高圧噴流装置10は、図3に
示した如く、管体11の途中の屈曲部(ベント部分)、
即ち互いに屈曲して連通接続した吸引側の管体11aと
排出側の管体11bとの接続部に接続した圧力水管36
と、圧力水管36の途中に連通した気体(外気)導入管
37と、圧力水管36の上流側に配置されて圧力水管内
に駆動高圧水を供給する圧力水供給源38と、を有す
る。圧力水管36は、排出側の管体11bの軸方向に駆
動高圧水(例えば、(5〜250kg/cm2)を噴出
するように接続される。駆動高圧水の初速v0は、30
〜60m/secで、駆動高圧水(ジェット水)の境界
面には負圧が発生する。従って、圧力水供給源38から
圧送される駆動高圧水を圧力水管36先端のノズル36
aから排出側の管体11b内に噴射させると、噴出した
駆動高圧水のエジェクター作用により、気体導入管37
から大気が吸入されて混気状態の圧力水になると共に、
混気状態の駆動高圧水が排出側管体11b内に噴出する
ことにより、吸引側管体11aの内部が真空状態となっ
て土壌の吸い上げが行われ、吸引側管体11aから排出
側管体11bに圧送される。この吸引、圧送は、駆動高
圧水の噴出が続く限り継続して行われる。この際、管体
11内のO点にて吸い上げられてきた土壌と駆動高圧水
とが衝突し、気、固、液の三相状態の衝突が持続され
る。この三相状態の衝突の結果、土砂に付着していた汚
染物質が分離され、或いは分離され易い状態となる。排
出側管体11bは、少なくともその先端部を揺動可能に
構成する。
The pressure-feed cleaning device 12 sucks the contaminated soil S from one end of the tube 11 using a high-pressure jet device (air-mixing jet pump) 10 and contaminates the contaminated soil S in the process of being transported through the tube. This is a means for removing contaminants adhering to sediment particles by colliding three phases of gas, solid and liquid by colliding jet water with soil. As shown in FIG. 3, the high-pressure jet device 10 includes a bent portion (vent portion) in the middle of the pipe 11,
That is, the pressure water pipe 36 connected to the connection between the suction-side pipe 11a and the discharge-side pipe 11b that are bent and connected to each other.
And a gas (outside air) introduction pipe 37 communicating in the middle of the pressure water pipe 36, and a pressure water supply source 38 arranged upstream of the pressure water pipe 36 to supply high-pressure driving water into the pressure water pipe. Pressure water pipe 36 is axially driven high-pressure water on the discharge side of the tube 11b (e.g., (5~250kg / cm 2) initial velocity v 0 of the. Driving high-pressure water is connected to eject the 30
At 〜60 m / sec, a negative pressure is generated at the interface between the driving high-pressure water (jet water). Therefore, the driving high-pressure water fed from the pressure water supply source 38 is supplied to the nozzle 36 at the tip of the pressure water pipe 36.
a into the pipe 11b on the discharge side, the ejected driving high-pressure water is ejected by the gas ejector pipe 37b.
Atmosphere is sucked in from and becomes mixed pressure water,
The driving high-pressure water in the mixed state is jetted into the discharge side pipe 11b, so that the inside of the suction side pipe 11a is in a vacuum state and the soil is sucked up, and the suction side pipe 11a is discharged from the suction side pipe 11a. 11b. The suction and the pressure feeding are continuously performed as long as the ejection of the driving high-pressure water continues. At this time, the soil sucked up at the point O in the pipe 11 collides with the driving high-pressure water, and the collision of gas, solid, and liquid in a three-phase state is maintained. As a result of the collision in the three-phase state, the contaminants adhering to the earth and sand are separated or easily separated. The discharge-side tube 11b is configured so that at least its tip can swing.

【0010】次に、図4は、土砂受水槽(一次沈殿槽)
17の構成例を示す断面図であり、この土砂受水槽17
は、洗浄水(例えば、水道水等の清水))16を満たし
た水槽15から成り、水槽15内には前記排出管体11
bの排出口を入り込ませる。水槽15の平面積は、例え
ば3×12=36m2とし、有効貯水量は、約100m3
とする。排出管体11bの排出口は、水槽15の一方の
端縁15aに近い位置に配置する。排出管体11bの排
出口からは、洗浄水(駆動高圧水)と共に洗浄土砂、汚
染物質、泡状の気体が排出される。排出される洗浄土砂
と洗浄水との固液比は、1:3(25%)程度となるよ
うに設定し、排出量は100m3/H程度とする。この
際、管体11bから排出される土砂のうち比重の大きい
ものは水槽15内に沈殿する一方で、比重の軽いシルト
分等は水中に浮遊して濁水を形成する。また、管体11
bから排出される比重の軽い油分は同時に排出されるエ
アーによるエアレーションによって攪拌分離されて水面
に浮上する。管体11bの排出口から離れた他端縁15
b寄りの位置には、オイルセパレータ41を配置して水
16上に浮上した油が次段の第2の沈殿槽17に移動す
ることを防止している。水16に浮いた油は、図示しな
い油吸着シート、界面活性剤による処理、その他の任意
の除去手段により除去する。水槽15の他端縁15b
は、排出管体11bの排出口を配置した一端縁15aよ
りも低く構成するか、排出穴を設けることにより、排出
管体11bからの排出量(流入量)に見合う水量が他端
縁15b側より外へ溢れ出て次の二次沈殿槽20へ流入
する。この際、土砂分はほとんど土砂受水槽17側で固
液分離された状態で沈降し、比重の軽い粘度及び汚染物
質は水の流れに沿ってより早く排出される。なお、その
中間の比重であるシルト分、及び揮発性汚染物質は、一
部は水槽内に沈降し、一部は滞留し、一部は排出され
る。土砂受水槽17は、複数台用意しておき、沈殿した
土砂量が所要量まで増大した時点で、隣接配置した新た
な土砂受水槽17内に排出管体11bの先端を移動して
新たに排出を開始する。このため、洗浄作業を中断する
ことなく、連続して行うことができる。具体的には、一
つの土砂受水槽17に対しては、1時間程度排出管体1
1bからの排出を継続してから、別の土砂受水槽17に
移行する。
Next, FIG. 4 shows a sediment receiving tank (primary sedimentation tank).
17 is a cross-sectional view illustrating a configuration example of the sediment receiving tank 17.
Comprises a water tank 15 filled with washing water (for example, fresh water such as tap water) 16, and the discharge pipe 11 is provided in the water tank 15.
Insert the outlet of b. The flat area of the water tank 15 is, for example, 3 × 12 = 36 m 2 , and the effective water storage amount is about 100 m 3
And The discharge port of the discharge pipe 11b is arranged at a position near one end 15a of the water tank 15. From the discharge port of the discharge pipe 11b, the cleaning water (driving high-pressure water), cleaning soil, contaminants, and gas bubbles are discharged. The solid-liquid ratio between the discharged washing soil and the cleaning water is set to be about 1: 3 (25%), and the discharge amount is about 100 m 3 / H. At this time, of the earth and sand discharged from the pipe 11b, those having a large specific gravity settle in the water tank 15, while silts having a light specific gravity float in water to form turbid water. The pipe 11
The oil having a low specific gravity discharged from b is agitated and separated by aeration by air discharged at the same time, and floats on the water surface. The other end 15 away from the outlet of the tube 11b
An oil separator 41 is disposed at a position closer to b to prevent oil floating on the water 16 from moving to the second settling tank 17 at the next stage. The oil floating on the water 16 is removed by an oil adsorbing sheet (not shown), treatment with a surfactant, or any other removing means. The other end 15b of the water tank 15
Is configured to be lower than one end 15a where the discharge port of the discharge pipe 11b is arranged, or by providing a discharge hole, so that the amount of water corresponding to the discharge (inflow) from the discharge pipe 11b is closer to the other end 15b. It overflows to the outside and flows into the next secondary sedimentation tank 20. At this time, most of the sediment settles down in a state where the sediment is solid-liquid separated on the side of the sediment receiving tank 17, and the light-weighted viscosities and pollutants are discharged earlier along the flow of water. The silt content and volatile contaminants having intermediate specific gravities are partially settled in the water tank, partially retained, and partially discharged. A plurality of sediment receiving tanks 17 are prepared, and when the amount of settled sediment increases to a required amount, the tip of the discharge pipe 11b is moved to a new sediment receiving tank 17 disposed adjacent to newly discharge the sediment receiving tank 17. To start. Therefore, the cleaning operation can be performed continuously without interruption. Specifically, for one sediment receiving tank 17, the discharge pipe 1
After the discharge from 1b is continued, the process proceeds to another sediment receiving tank 17.

【0011】排出管体11bからの排出を停止した土砂
受水槽17には、その後清水(後述する循環水)を25
3/H程度30分間送水し、水槽15内で水側に移行
した汚染物質をできるだけ沈降させないで、次段の二次
沈殿槽20へ排水する。30分後に送水を停止すると、
水槽15内の水位を静かに低下させ、水位が半分以下に
低下した時点で、高濃度水として後述する土壌の再洗浄
ラインに吸引圧送する。この時点で、水槽15内に沈殿
した土砂13の汚染濃度が充分に低下していることが確
認された場合には、高圧噴流土砂搬送装置31により土
砂13を吸引して元の地盤に埋め戻す。また、汚染濃度
が充分に低下していない場合には、高圧噴流土砂搬送装
置31により土砂13を吸引して一旦保留位置に搬送し
て堆積ささせてから、再度高圧噴流装置10による吸
引、洗浄、土砂受水槽17への排出を繰り返す。なお、
ここで吸引した土砂を一旦保留する位置としては、格別
の保留槽の如きものを土壌を掘削する等により設けても
良いし、或いは先に掘削済みの汚染土壌地盤(他の場
所)を利用しても良い。
After the discharge from the discharge pipe 11b is stopped, 25 g of fresh water (circulating water, which will be described later) is supplied to the sediment receiving tank 17.
Water is supplied for about 30 minutes at about m 3 / H, and the contaminants that have migrated to the water side in the water tank 15 are drained to the next secondary sedimentation tank 20 without sedimentation as much as possible. If you stop water supply after 30 minutes,
The water level in the water tank 15 is gently lowered, and when the water level drops to half or less, the water is suctioned and pumped as high-concentration water to a soil rewashing line described later. At this time, if it is confirmed that the contamination concentration of the sediment 13 settled in the water tank 15 is sufficiently reduced, the high-pressure jet sediment transporting device 31 sucks the soil 13 and bury it in the original ground. . If the contamination concentration is not sufficiently reduced, the high-pressure jet sediment transporting device 31 sucks the soil 13, transports it to the holding position and deposits it, and then sucks and cleans the soil again using the high-pressure jet device 10. The discharge to the sediment receiving tank 17 is repeated. In addition,
As a position for temporarily storing the sucked earth and sand, a special storage tank may be provided by excavating the soil or the like, or a previously excavated contaminated soil ground (another place) may be used. May be.

【0012】次に、図5は、二次沈殿槽20及び砂濾過
装置25の構成例を示す断面図である。二次沈殿槽20
と砂濾過装置25は、別体構成としても良いが、このよ
うに一体化することにより、コンパクト化、連続処理の
効率化を図ることができる。この設備20,25は、前
記土砂受水槽17に隣接した地盤を地表面から略円錐形
(或いは、円筒形)に掘削することにより形成したピッ
ト(掘削穴)50と、ピット50の全周に掘削土を盛り
土することにより形成した土盛51と、ピット50内面
に敷き詰めた防水シート52と、ピット50の中心部に
立設固定した中空円筒状のケーシング53(高さ3.5
m)と、ケーシング53内に充填した砂濾材26(高さ
3.0m)と、を備える。砂濾材26は砂濾過装置25
を構成し、ケーシング53の外側に位置するピット50
内部が二次沈殿槽20を構成する。二次沈殿槽20内に
は予め清水を満たしておく。ピット50は、例えば掘削
深を2.0m、底部径(R1)を5.0mとする。土盛
51は、掘削土を利用してピット周囲に形成し、最終的
には水槽表面径(R2)を15.0m、水深3.5m程
度の沈殿槽とする。ケーシング53は、金属等充分な剛
性を有した板材料から成る直径3.0m程度の中空円筒
体であり、これをピット底部中央に立設固定し、その内
部には砂濾材26を充填すると共に、砂濾材26の中心
部に吸引用配管(直径15cm程度)55を適度な深さ
までセットする。吸引用配管55の他端は吸引ポンプと
接続し、循環水用受水槽30へ吸引した水を供給する。
土砂受水槽17から排出されてきた溢水がケーシング5
3の外径側に位置する二次沈殿槽20内に排水される
と、排水に含まれたシルト分を中心とした土粒子が二次
沈殿槽20内にて沈降し、二次沈殿槽20内が満水状態
になった後で排水が継続されることにより排水に含まれ
た汚染物質の多くはケーシング53を乗り越えて砂濾材
26内に流入する。汚染物質を含んだ水は、砂濾材を通
過する過程で汚染物質の大半が砂濾材によって吸着、捕
捉され、ケーシング53の底部に達した時点では洗浄が
完了した状態となっている。このため、吸引用配管55
の先端部から砂濾材底部の濾過済み水を吸引し、循環水
受水槽30に戻して駆動水等として再利用することがで
きる。
Next, FIG. 5 is a sectional view showing a configuration example of the secondary sedimentation tank 20 and the sand filtration device 25. Secondary sedimentation tank 20
The sand filter 25 and the sand filtration device 25 may be configured separately, but by integrating them in this way, it is possible to reduce the size and increase the efficiency of continuous processing. The facilities 20 and 25 include a pit (drilled hole) 50 formed by excavating the ground adjacent to the sediment receiving tank 17 into a substantially conical (or cylindrical) shape from the ground surface, and An embankment 51 formed by embankment of excavated soil, a waterproof sheet 52 spread over the inner surface of the pit 50, and a hollow cylindrical casing 53 (height 3.5) erected and fixed at the center of the pit 50.
m), and the sand filter medium 26 (3.0 m in height) filled in the casing 53. The sand filter medium 26 is a sand filter 25
And a pit 50 located outside the casing 53.
The inside constitutes the secondary sedimentation tank 20. The secondary sedimentation tank 20 is filled with fresh water in advance. The pit 50 has, for example, an excavation depth of 2.0 m and a bottom diameter (R1) of 5.0 m. The embankment 51 is formed around the pit by using excavated soil, and is finally a sedimentation tank having a water tank surface diameter (R2) of about 15.0 m and a water depth of about 3.5 m. The casing 53 is a hollow cylindrical body having a diameter of about 3.0 m made of a plate material having sufficient rigidity such as metal, and is erected and fixed at the center of the bottom of the pit. Then, a suction pipe (about 15 cm in diameter) 55 is set at an appropriate depth in the center of the sand filter medium 26. The other end of the suction pipe 55 is connected to a suction pump, and supplies the sucked water to the circulating water receiving tank 30.
The overflow water discharged from the sediment receiving tank 17 is
When the water is drained into the secondary sedimentation tank 20 located on the outer diameter side of No. 3, soil particles centered on the silt content contained in the wastewater settle down in the secondary sedimentation tank 20, As the drainage is continued after the inside is full, most of the pollutants contained in the drainage flow over the casing 53 and flow into the sand filter medium 26. Most of the contaminant-containing water is adsorbed and captured by the sand filter medium while passing through the sand filter medium, and when the water reaches the bottom of the casing 53, the washing is completed. For this reason, the suction pipe 55
The filtered water at the bottom of the sand filter medium is sucked from the tip of the filter and returned to the circulating water receiving tank 30 to be reused as driving water or the like.

【0013】なお、目詰まり等によって砂濾材26の濾
過抵抗が高まった場合には、ケーシング内の砂濾材26
を高圧噴流装置10の吸引管体11aによって吸引する
ことにより洗浄することによって、再利用することがで
きる。また、砂濾材26内に発生したスラッジや、濾材
洗浄水については、図示しない高度処理装置により高度
処理を施した上で、場外処分、或いは下水道処分を施
す。なお、ここで高度処理とは、脱水固化、中和、凝集
沈殿、活性炭処理等を含む。また、沈殿槽20底部の堆
積物は、汚染濃度をチェックした上で、汚染の程度が許
容値を超えている場合には敷地の一部で薄層巻き出しに
よる紫外線処理によって汚染濃度を基準値以下に低下さ
せた上で、埋め戻し材として利用する。また、汚染の程
度が許容値以下である場合には、高圧噴流土砂搬送装置
31を利用して吸引して元の地盤内に埋め戻す。なお、
埋め戻しに際しては、埋め戻した土砂と、これから吸引
して洗浄処理を施す汚染土砂とが地盤内に混合しないよ
うに埋め戻し場所を異ならせる等の配慮が必要である。
尚、汚染物質がタールである場合に、タール内にベンゼ
ン、シアン等を含む場合には、例えば、砂濾過装置25
の後段に、曝気揮散処理、PH処理装置(アルカリ塩素
法処理装置)、活性炭吸着装置を配置する。循環水用受
水槽30に戻された水は、汚染物質が除去され洗浄が完
了した状態となっているため、これを圧送洗浄装置12
に供給して駆動高圧水として再利用したり、土砂受水層
17及び二次沈殿槽20に供給する水として利用しても
良い。なお、高圧噴流装置10による吸引から開始さ
れ、高圧噴流土砂搬送装置31による埋め戻しにより終
了する一連の工程の実施によって洗浄が不十分の場合に
は、再度同じ工程を繰り返し実施することにより、洗浄
は完了する。また、この工法では、真空吸引管である吸
引側管体11aを汚染土壌中に圧入して吸引掘削できる
ため、ピンポイントによる汚染土壌の洗浄が可能であ
る。また、土壌の汚染濃度、流度分布、汚染物質に応じ
て、上記各種処理槽、装置類の組み合わせ使用が可能で
あり、設備投資コストを最小限にすることができる。洗
浄水として、循環水を使用できるので、上下水道代を含
めて水処理コストを最小限に抑えることができる。本発
明のシステム、及び方法により効果的に洗浄できる汚染
物質は、油系のみならず、金属系汚染物質をも含む。
If the filtering resistance of the sand filter medium 26 is increased due to clogging or the like, the sand filter medium 26 in the casing may be damaged.
Can be reused by washing by suctioning by the suction pipe 11a of the high-pressure jet device 10. In addition, sludge generated in the sand filter medium 26 and filter medium washing water are subjected to advanced treatment by an advanced treatment device (not shown), and then subjected to off-site disposal or sewer disposal. Here, the advanced treatment includes dehydration solidification, neutralization, coagulation sedimentation, activated carbon treatment and the like. The sediment at the bottom of the sedimentation tank 20 is checked for contamination concentration, and if the degree of contamination exceeds the allowable value, the contamination concentration is set to a standard value by ultraviolet treatment by unwinding a thin layer at a part of the site. After being reduced to the following, it is used as a backfill material. If the degree of contamination is equal to or less than the allowable value, the high-pressure jet soil transport device 31 is used to suck and backfill the original ground. In addition,
At the time of backfilling, it is necessary to consider different backfilling places so that the backfilled soil and the contaminated soil which is to be suctioned and subjected to the cleaning process are not mixed in the ground.
When the contaminant is tar, if the tar contains benzene, cyan, etc., for example, a sand filter 25
In the subsequent stage, an aeration and volatilization treatment, a PH treatment device (alkali chlorine treatment device), and an activated carbon adsorption device are arranged. The water returned to the circulating water receiving tank 30 is in a state where the contaminants have been removed and the cleaning has been completed.
May be reused as driving high-pressure water, or may be used as water supplied to the sediment receiving layer 17 and the secondary sedimentation tank 20. In the case where cleaning is insufficient by performing a series of steps starting from suction by the high-pressure jet device 10 and ending by backfilling by the high-pressure jet sediment transporting device 31, the same process is repeated to perform cleaning. Is completed. In addition, in this method, the suction side pipe 11a, which is a vacuum suction pipe, can be pressed into the contaminated soil and can be sucked and excavated, so that the contaminated soil can be washed with a pinpoint. In addition, the above-described various treatment tanks and equipment can be used in combination according to the soil contamination concentration, flow rate distribution, and contaminants, thereby minimizing equipment investment costs. Since circulating water can be used as the washing water, water treatment costs including water and sewage charges can be minimized. Contaminants that can be effectively cleaned by the systems and methods of the present invention include not only oil-based, but also metal-based contaminants.

【0014】次に、本発明の洗浄方法を構成する各ステ
ップについて、図2に基づいて説明する。先ず、圧送洗
浄装置12を用いた圧送洗浄ステップ(S1)では、高
圧噴流装置10(混気ジェットポンプ)を利用して管体
11の一端11aから汚染土壌を吸引し、吸引した汚染
土壌を管体11内を搬送する過程で汚染土壌にジェット
水を衝突させて気体、固体、液体の三相を衝突させて土
砂粒子表面に付着した汚染物質を分離、洗浄する。この
ため、管体11bから排出された土砂からは大半の汚染
物質が分離されて水側へ移行した状態にある。次の第1
の固液分離ステップ(S2)では、圧送洗浄装置12に
より洗浄を受けた土砂を含む排水を、洗浄水を満たした
第1の沈殿槽17内に供給して土砂を沈殿させる。沈殿
した土砂の汚染濃度が許容値を下回っている場合には、
そのまま高圧噴流土砂搬送装置31を用いて吸引し元の
地盤に埋め戻す。また、排水中の油については、水槽1
5内の水16に浮いた状態でこれを分離し、除去する。
第1の固液分離ステップにて水槽15内に沈殿した土砂
の汚染濃度が許容値を上回っている場合には、高圧噴流
土砂搬送装置31によって一旦保留位置に搬送して堆積
させた上で、圧送洗浄装置12による吸引を行って再洗
浄を行い、再び水槽15内に沈殿した土砂が許容汚染濃
度を下回っている場合には高圧噴流土砂搬送装置31に
よって元の地盤内に埋め戻す。洗浄に使用した水は、二
次沈殿槽20から砂濾過装置25へ排水して順次洗浄す
る。
Next, each step constituting the cleaning method of the present invention will be described with reference to FIG. First, in the pressure-feed cleaning step (S1) using the pressure-feed cleaning device 12, the contaminated soil is sucked from one end 11a of the pipe 11 using the high-pressure jet device 10 (air-mixing jet pump), and the sucked contaminated soil is piped. In the process of transporting inside the body 11, jet water collides with the contaminated soil to cause three phases of gas, solid, and liquid to collide with each other to separate and wash contaminants attached to the surface of the earth and sand particles. For this reason, most of the pollutants are separated from the earth and sand discharged from the pipe 11b and are shifted to the water side. Next first
In the solid-liquid separation step (S2), wastewater containing soil washed by the pressure-feed cleaning device 12 is supplied into the first sedimentation tank 17 filled with washing water to sediment the earth and sand. If the concentration of sediment in the sediment is lower than the allowable value,
Using the high pressure jet soil transport device 31 as it is, it is sucked and buried in the original ground. In addition, for oil in drainage, water tank 1
This is separated and removed while floating on the water 16 in 5.
If the contamination concentration of the sediment deposited in the water tank 15 in the first solid-liquid separation step is higher than the allowable value, the high-pressure jet sediment transportation device 31 once transports the soil to the holding position and deposits the same. Suction is performed by the pressure-feed cleaning device 12 to perform re-cleaning. When the sediment deposited in the water tank 15 is lower than the allowable contamination concentration again, the soil is returned to the original ground by the high-pressure jet sediment transport device 31. The water used for the washing is drained from the secondary sedimentation tank 20 to the sand filtration device 25 and washed sequentially.

【0015】続く、第2の固液分離ステップ(S3)で
は、第1の沈殿槽17からの溢流水を第2の沈殿槽20
内に供給して土砂を沈殿させる。第2の沈殿槽20内に
沈殿した土砂(主としてシルト)の汚染濃度が充分に低
下している場合には、高圧噴流土砂搬送装置31を利用
して元の地盤内に埋め戻す。汚染濃度が充分に低下して
いない場合には、敷地の一部で薄層巻き出しによる紫外
線処理によって汚染濃度を基準値以下に低下させた上
で、埋め戻し材として利用するか、或いは場外廃棄処分
とする。続く、砂濾過ステップ(S4)では、第2の沈
殿槽20からの溢流水を砂濾材26内に受け入れて砂濾
材により濾過する。砂濾材26内に発生したスラッジ
や、濾材洗浄水については、高度処理装置により高度処
理を施した上で、場外処分、或いは下水道処分を施す。
循環利用ステップ(S5)では、砂濾材26により濾過
された水を循環水用受水槽30に一旦貯めておき、上記
各ステップにおいて再利用するために供給する。以上の
構成を備えた洗浄システム、及び洗浄方法によれば、土
粒子間隙に汚染物質が緊密に充填されて、空気、水がほ
とんど存在しない高濃度汚染状態にある土壌、例えば透
水性の悪いシルト質の高濃度汚染土壌に対しても、低コ
ストで、短期間に効率的な洗浄を行うことが可能とな
る。
In the subsequent second solid-liquid separation step (S3), the overflow water from the first sedimentation tank 17 is removed from the second sedimentation tank 20.
To feed the soil and sediment the soil. If the contaminant concentration of the sediment (mainly silt) settled in the second sedimentation tank 20 is sufficiently reduced, it is backfilled in the original ground by using the high-pressure jet sediment transporting device 31. If the contamination concentration is not sufficiently reduced, reduce the contamination concentration to a level below the reference value by ultraviolet treatment by unwinding a thin layer at a part of the site, and then use it as a backfill material or dispose of off-site Dispose of. In the subsequent sand filtration step (S4), the overflow water from the second sedimentation tank 20 is received in the sand filter medium 26 and filtered by the sand filter medium. Sludge generated in the sand filter medium 26 and filter medium washing water are subjected to advanced treatment by an advanced treatment device, and then subjected to off-site disposal or sewer disposal.
In the circulating use step (S5), the water filtered by the sand filter medium 26 is temporarily stored in the circulating water receiving tank 30, and supplied for reuse in each of the above steps. According to the cleaning system and the cleaning method having the above-described configuration, the soil particles are tightly filled with the contaminants, and the soil is in a high-concentration contaminated state where air and water hardly exist. Even for high quality contaminated soil, efficient cleaning can be performed at low cost in a short period of time.

【0016】次に、タール等の石炭系汚染物質によって
汚染された土壌は、過去提案されたいかなる浄化工法に
よっても浄化が容易ではなかった。重金属類(六価クロ
ム、砒素等)、PCB、硝酸性窒素等の汚染物質につい
ても、同様に浄化は困難とされていた。これに対し、本
発明の洗浄システム、及び方法によれば、汚染物質等を
含む土壌を吸引した上で、混気ジェットポンプからの高
圧ジェット水を衝突させるので、土壌に強く付着した汚
染物質を確実に分離して水側へ移行させることができる
ため、汚染物質を除去した土壌を元の地盤に戻すことが
できる。なお、本発明による土壌洗浄工法と、他の従来
の工法を組み合わせ使用することにより、更に効率的な
浄化が実現可能となることはいうまでもない。
Next, soil contaminated with coal-based pollutants such as tar has not been easily purified by any purification method proposed in the past. It has also been considered difficult to purify pollutants such as heavy metals (hexavalent chromium, arsenic, etc.), PCB, nitrate nitrogen and the like. On the other hand, according to the cleaning system and the method of the present invention, after suctioning the soil containing the pollutant and the like, the high-pressure jet water from the air-mix jet pump is collided, so that the pollutant strongly adhered to the soil is removed. Since the soil can be reliably separated and transferred to the water side, the soil from which the pollutants have been removed can be returned to the original ground. It goes without saying that more efficient purification can be realized by using the soil cleaning method according to the present invention in combination with another conventional method.

【0017】[0017]

【発明の効果】以上のように本発明の洗浄システム、及
び洗浄方法によれば、低濃度汚染された土壌は勿論、高
濃度汚染された土壌を混気ジェットポンプにて地盤中か
ら吸引し管体内を圧送する過程で、駆動高圧水と衝突さ
せることによって、土壌に付着した汚染物質を除去する
ので、極めて低コスト、且つ効率的に、短期間で汚染物
質を除去することができる。特に、粘土、シルト等の土
壌密度が高い汚染土壌に対しても効率の良い成果を得る
ことができる。従って、従来の如く大量の土壌を地上に
ドラム内に搬送してドラムを回転させながら汚染物質を
分離するという場合に発生する不具合である設備の大型
化、高コスト化、立地条件の制限等々という不具合がな
くなる。また、混気ジェットポンプによって固液分離さ
れ、汚染物質が除去された土砂を水槽内に沈殿させてか
らこれを高圧噴流土砂搬送装置によって吸引し元の地盤
に埋め戻すので、埋め戻し作業も高効率に行うことがで
きる。また、一連の工程で洗浄等に使用した水を洗浄し
てから、循環水用受水槽内に供給して、各工程に循環供
給して再利用するようにしているので、水の使用量を必
要最小限に限定し、コスト増を防ぐことができる。ま
た、工程の一部、又は全部を複数回繰り返すことによ
り、一度の工程によって洗浄し切れない場合に対応する
ことができる。
As described above, according to the cleaning system and the cleaning method of the present invention, not only the soil contaminated with a low concentration but also the soil contaminated with a high concentration is sucked from the ground by an air-mixing jet pump. In the process of pumping the inside of the body, the contaminants attached to the soil are removed by colliding with the driving high-pressure water, so that the contaminants can be efficiently removed at a very low cost and in a short period of time. In particular, efficient results can be obtained even for contaminated soil with a high soil density such as clay and silt. Therefore, the problems that occur when a large amount of soil is conveyed into the drum on the ground and the contaminant is separated while rotating the drum as in the past, such as enlargement of equipment, increase in cost, restriction on location conditions, etc. There are no defects. In addition, the sediment from which solids and liquids have been separated by the air-mixing jet pump and from which contaminants have been removed is settled in the water tank, and then suctioned by the high-pressure jet sediment transport device and backfilled into the original ground, so that the backfill work is also high. It can be done efficiently. In addition, since the water used for washing in a series of steps is washed, it is supplied into the circulating water receiving tank, circulated and supplied to each step, and reused. It can be limited to the minimum necessary to prevent an increase in cost. In addition, by repeating a part or all of the steps a plurality of times, it is possible to cope with a case where the cleaning cannot be performed in one step.

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

【図1】本発明の一実施形態に係る高圧噴流土壌洗浄シ
ステム及び洗浄方法を実施するための設備図。
FIG. 1 is a facility diagram for implementing a high-pressure jet soil cleaning system and a cleaning method according to an embodiment of the present invention.

【図2】本発明の洗浄方法を説明するための図。FIG. 2 is a view for explaining a cleaning method of the present invention.

【図3】圧送洗浄装置の内部構成説明図。FIG. 3 is an explanatory diagram of an internal configuration of a pressure-feed cleaning apparatus.

【図4】第1の沈殿槽の構成図。FIG. 4 is a configuration diagram of a first sedimentation tank.

【図5】第2の沈殿槽及び砂濾過装置の構成説明図。FIG. 5 is a configuration explanatory view of a second settling tank and a sand filtration device.

【符号の説明】[Explanation of symbols]

1 高圧噴流土壌洗浄システム、2 プラント設備、3
土壌改良区画、10高圧噴流装置、11 管体、11
a 吸引側管体、11b 排出側管体、12圧送洗浄装
置、13 土砂、15 水槽、16 洗浄水、17 土
砂受水槽(一次沈殿槽)、20 二次沈殿槽、25 砂
濾過装置、26 砂濾材、30 循環水用受水槽、31
高圧噴流土砂搬送装置、36 圧力水管、36a ノ
ズル、37 気体(外気)導入管、38 圧力水供給
源、50 ピット、51 土盛、52 防水シート、5
3 ケーシング。
1 High pressure jet soil washing system, 2 plant equipment, 3
Soil improvement section, 10 high-pressure jet device, 11 pipe, 11
a suction side pipe, 11b discharge side pipe, 12 pressure washing device, 13 earth and sand, 15 water tank, 16 washing water, 17 earth and sand receiving tank (primary sedimentation tank), 20 secondary sedimentation tank, 25 sand filtration device, 26 sand Filter media, 30 Circulating water receiving tank, 31
High pressure jet sediment transporting device, 36 pressure water pipe, 36a nozzle, 37 gas (outside air) introduction pipe, 38 pressure water supply source, 50 pits, 51 embankment, 52 waterproof sheet, 5
3 Casing.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 11/00 B09B 5/00 ZABS E02D 3/00 101 B01D 23/16 (72)発明者 志方 洋介 東京都三鷹市牟礼2−5−17 Fターム(参考) 2D043 CA01 CA20 EB06 4D004 AA41 AB02 AB03 AB06 AC07 CA13 CA40 CB42 CC03 DA02 DA07 4D041 BA01 BB04 CB07 4D059 AA09 AA10 AA11 AA18 BH01 BH04 BH06 BK06 CB01 4D071 AA62 AB03 AB25 CA05 DA15──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 11/00 B09B 5/00 ZABS E02D 3/00 101 B01D 23/16 (72) Inventor Yosuke Shikata Tokyo 2-5-17 Mure, Mitaka F-term (reference) 2D043 CA01 CA20 EB06 4D004 AA41 AB02 AB03 AB06 AC07 CA13 CA40 CB42 CC03 DA02 DA07 4D041 BA01 BB04 CB07 4D059 AA09 AA10 AA11 AA18 BH01 BH04 BH06 BK06 ACB4 DA034

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 混気ジェットポンプを利用して管体の一
端から汚染土壌を吸引し、吸引した汚染土壌を管体内を
搬送する過程で該汚染土壌に駆動高圧水を噴出させて気
体、固体、液体の三相を衝突させて土砂粒子に付着した
汚染物質を分離、洗浄する圧送洗浄装置と、 洗浄水を満たした水槽から成り、前記圧送洗浄装置によ
り洗浄を受けた土砂を含む排水を受け入れて土砂を沈殿
させる固液分離用の第1の沈殿槽と、 該第1の沈殿槽からの溢流水を受け入れる固液分離用の
第2の沈殿槽と、 該第2の沈殿槽からの溢流水を受け入れて砂濾材により
濾過する砂濾過装置と、 該砂濾過装置により濾過された水を受け入れる循環水用
受水槽と、 を備えたことを特徴とする高圧噴流土壌洗浄システム。
1. A method in which contaminated soil is sucked from one end of a pipe using an air-mixing jet pump, and driving high-pressure water is ejected to the contaminated soil in the process of transporting the sucked contaminated soil through the pipe, thereby forming gas or solid. A pressurized cleaning device that separates and cleans contaminants attached to the sediment particles by colliding three phases of liquid, and a water tank filled with cleaning water, and receives wastewater containing sediment washed by the pressurized cleaning device. A first sedimentation tank for solid-liquid separation for sedimenting earth and sand, a second sedimentation tank for solid-liquid separation for receiving overflow water from the first sedimentation tank, and an overflow from the second sedimentation tank A high pressure jet soil washing system, comprising: a sand filtration device that receives running water and filters through a sand filter medium; and a circulating water receiving tank that receives water filtered by the sand filtration device.
【請求項2】 前記循環水用受水槽内の水を前記圧送洗
浄装置、前記第1の沈殿槽、又は前記第2の沈殿槽の少
なくとも一つに対して循環供給することを特徴とする請
求項1に記載の高圧噴流土壌洗浄システム。
2. The method according to claim 1, wherein the water in the circulating water receiving tank is circulated and supplied to at least one of the pressure-feed cleaning device, the first settling tank, and the second settling tank. Item 2. A high pressure jet soil washing system according to item 1.
【請求項3】 前記第1の沈殿槽、又は前記第2の沈殿
槽内に沈殿した洗浄済み土砂を、地盤内に戻すための高
圧噴流土砂搬送装置を備えたことを特徴とする請求項1
又は2に記載の高圧噴流土壌洗浄システム。
3. A high-pressure jet sediment transport device for returning the washed sediment settled in the first settling tank or the second settling tank to the ground.
Or the high pressure jet soil washing system according to 2.
【請求項4】 混気ジェットポンプを利用して管体の一
端から汚染土壌を吸引し、吸引した汚染土壌を管体内を
搬送する過程で該汚染土壌に駆動高圧水を衝突させて気
体、固体、液体の三相を衝突させて土砂粒子表面に付着
した汚染物質を分離、洗浄する圧送洗浄ステップと、 前記圧送洗浄装置により洗浄を受けた土砂を含む排水
を、洗浄水を満たした第1の沈殿槽内に供給して土砂を
沈殿させる第1の固液分離ステップと、 前記第1の沈殿槽からの溢流水を第2の沈殿槽内に供給
して土砂を沈殿させる第2の固液分離ステップと、 前記第2の沈殿槽からの溢流水を受け入れて砂濾材によ
り濾過する砂濾過ステップと、 前記砂濾材により濾過された水を循環利用する循環利用
ステップと、 を備えたことを特徴とする高圧噴流土壌洗浄方法。
4. A method in which contaminated soil is sucked from one end of a pipe using an air-mixing jet pump, and driving high-pressure water collides with the contaminated soil in the process of transporting the sucked contaminated soil through the pipe to form gas or solid. A pressurized washing step of separating and washing contaminants adhering to the surface of the earth and sand particles by colliding three phases of liquid; and a wastewater containing earth and sand that has been washed by the pumping and washing apparatus, the first of which is filled with washing water. A first solid-liquid separation step of supplying the sedimentation tank to sediment the soil, and a second solid-liquid separation step of supplying overflow water from the first sedimentation tank to the second sedimentation tank to sediment the earth and sand. A separation step; a sand filtration step of receiving overflow water from the second sedimentation tank and filtering it with a sand filter medium; and a circulating use step of circulating and using the water filtered by the sand filter medium. And high pressure jet soil washing method.
【請求項5】 前記第1の固液分離ステップにて固液分
離されて第1の沈殿槽内に堆積した土砂を高圧噴流土砂
搬送装置によって吸引搬送して一旦保留する保留ステッ
プと、 前記保留ステップにて一旦保留した土砂を再び前記混気
ジェットポンプを利用して管体の一端から吸引し、吸引
した汚染土壌を管体内を搬送する過程で汚染土壌に駆動
高圧水を衝突させて気体、固体、液体の三相を衝突させ
て土砂粒子表面に付着した汚染物質を分離、洗浄する再
圧送洗浄ステップと、 前記圧送洗浄装置により再度洗浄を受けた土砂を洗浄水
を満たした第1の沈殿槽内に供給して土砂を沈殿させる
2度目の第1の固液分離ステップと、を少なくとも備え
たことを特徴とする請求項4に記載の高圧噴流土壌洗浄
方法。
5. A holding step of sucking and conveying the sediment separated in the first solid-liquid separation step in the first solid-liquid separation step and deposited in the first sedimentation tank by a high-pressure jet sediment conveying device, and temporarily holding the sediment; The soil once held in the step is sucked again from one end of the pipe using the air-jet jet pump, and in the process of transporting the sucked contaminated soil through the pipe, driving high-pressure water collides with the contaminated soil to form a gas, A re-pressure cleaning step of separating and cleaning contaminants adhering to the surface of the earth and sand particles by colliding three phases of solid and liquid, and a first sediment filled with cleaning water by re-cleaning the soil and sand by the pressure cleaning apparatus. The high pressure jet soil cleaning method according to claim 4, further comprising at least a second first solid-liquid separation step of feeding the water into the tank to settle the earth and sand.
JP2001161134A 2001-05-29 2001-05-29 Soil cleaning system with high pressure jet and method for the same Pending JP2002355663A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2002355663A true JP2002355663A (en) 2002-12-10

Family

ID=19004457

Family Applications (1)

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Country Link
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010284624A (en) * 2009-06-15 2010-12-24 Dojo Kankyo Process Kenkyusho:Kk Apparatus of producing mixture of soil and water using high pressure water
CN102233299A (en) * 2010-04-28 2011-11-09 郑州鑫智抛磨材料有限公司 Automatic micro-powder grader
JP2014051887A (en) * 2012-09-05 2014-03-20 Penta Ocean Construction Co Ltd Sediment transportation mixture gas jet pump and dredge method using the same
JP2014091907A (en) * 2012-10-31 2014-05-19 Penta Ocean Construction Co Ltd System and method for separating mixture of sediment mixed with mixture
CN106906834A (en) * 2017-05-03 2017-06-30 上海格林曼环境技术有限公司 A kind of modified multiphase extraction system and method based on Application of light well point precipitation technique
JP2017124359A (en) * 2016-01-13 2017-07-20 五洋建設株式会社 Processing method and processing system of contaminated muddy water
KR101782207B1 (en) * 2015-05-20 2017-09-28 한준수 Constructing method and apparatus to construct suction pile from ground to underground or sea level

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010284624A (en) * 2009-06-15 2010-12-24 Dojo Kankyo Process Kenkyusho:Kk Apparatus of producing mixture of soil and water using high pressure water
CN102233299A (en) * 2010-04-28 2011-11-09 郑州鑫智抛磨材料有限公司 Automatic micro-powder grader
JP2014051887A (en) * 2012-09-05 2014-03-20 Penta Ocean Construction Co Ltd Sediment transportation mixture gas jet pump and dredge method using the same
JP2014091907A (en) * 2012-10-31 2014-05-19 Penta Ocean Construction Co Ltd System and method for separating mixture of sediment mixed with mixture
KR101782207B1 (en) * 2015-05-20 2017-09-28 한준수 Constructing method and apparatus to construct suction pile from ground to underground or sea level
JP2017124359A (en) * 2016-01-13 2017-07-20 五洋建設株式会社 Processing method and processing system of contaminated muddy water
CN106906834A (en) * 2017-05-03 2017-06-30 上海格林曼环境技术有限公司 A kind of modified multiphase extraction system and method based on Application of light well point precipitation technique

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