KR101270065B1 - Chemistry washing method - Google Patents

Chemistry washing method Download PDF

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KR101270065B1
KR101270065B1 KR1020120075542A KR20120075542A KR101270065B1 KR 101270065 B1 KR101270065 B1 KR 101270065B1 KR 1020120075542 A KR1020120075542 A KR 1020120075542A KR 20120075542 A KR20120075542 A KR 20120075542A KR 101270065 B1 KR101270065 B1 KR 101270065B1
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South Korea
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washing
tank
soil
process water
aggregate
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KR1020120075542A
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Korean (ko)
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김철
조희정
안성균
김장환
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(주)금송이엔지
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/02Extraction using liquids, e.g. washing, leaching, flotation
    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62DCHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D3/00Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
    • A62D3/30Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/08Reclamation of contaminated soil chemically

Abstract

PURPOSE: A heavy metal contaminated soil washing method is provided to enhance the washing efficiencies, reduce the cost and reduce the generation of sludge. CONSTITUTION: A heavy metal contaminated soil washing method comprises the following steps: (S1) classifying polluted soil by particle sizes and washing the classified polluted soil by circulating process water; (S2) washing the polluted soil aggregates using chemicals, a high speed agitator, and a jet mill; (S3) repeatedly spraying and washing the polluted aggregates; and (S4) precipitating minute polluted soil by particle sizes and sludge processing. The previous step (S1) comprises the following steps: washing aggregates with a size of 40mm or greater after sieving by a screen; agitating the aggregates with a size of 40mm or less with the processing water; isolating the agitated processing water into the polluted soil with a size of 1mm or greater and aggregates with a size of 1mm or less; sprinkle washing the aggregates with a size of 1mm and dehydrating and discharging the same; supplying the aggregates with a size of 1mm or less and processing water to an adjusting bath; supplying the aggregates with a size of 1mm and the processing water from the adjusting bath to hydrocyclone; and delivering the graded soil in the hydrocyclone to a chemistry washing tub and delivering the processing water to a log washer. [Reference numerals] (S1) Circulation washing step; (S2) Chemical washing step; (S3) Continuous washing step; (S4) Sediment soil processing step

Description

중금속 오염토양 세척방법 { Chemistry Washing Method }Heavy Metal Contaminated Soil Cleaning Method {Chemistry Washing Method}

본 발명은 중금속 오염토양 세척방법에 관한 것으로서, 보다 상세하게는 오염된 토양을 골재별로 분리한 후 화학세척하고 화학세척시 사용되는 세척수를 순환시켜 재차 공급함으로서, 세척효율을 향상시키며 원가를 절감할 수 있는 중금속 오염토양 세척방법에 관한 것이다.
The present invention relates to a heavy metal contaminated soil washing method, and more particularly, by separating the contaminated soil by aggregate, and chemically cleaning and circulating the washing water used for chemical washing to supply it again, thereby improving washing efficiency and reducing costs. The present invention relates to a heavy metal contaminated soil cleaning method.

토양오염의 경우 일단 오염이 되고 나면 지표수 및 지하수의 수질에도 악영향을 미치게 되는 등 주변 환경에 2차 오염을 유발시킬 가능성이 있으므로 오염된 토양은 반드시 현장에서 빠른 시간 내에 정화시켜 복원되어야 한다.In case of soil pollution, once contaminated, it may adversely affect the surface water and groundwater quality, causing secondary pollution to the surrounding environment. Therefore, contaminated soil must be purified and restored at the site as soon as possible.

상기와 같은 관점에서 토양 세척기법은 이미 1970년대 말 미국에서 처음 개발되어 현재는 미국을 비롯하여 독일 네덜란드 등 많은 나라에서 사용빈도가 가장 높은 특허기술중의 하나로서 각 지역, 각 국의 적용범위가 매우 광범위하다.In view of the above, the soil washing technique was first developed in the United States in the late 1970s and is currently one of the most frequently used patent technologies in many countries, including the United States, Germany and the Netherlands. Extensive

적용범위가 넓기 때문에 다양한 유기 오염물질 및 중금속이 다량으로 배출되고 있는 현 실정에 비추어 보아 현장 적용이 크고 경제적으로도 효율성이 뛰어난 정화기법의 하나로 인식되고 있다.Due to its wide range of applications, it is recognized as one of the most efficient and economically efficient purification methods in view of the current situation in which a large amount of various organic pollutants and heavy metals are emitted.

최근 들어 정유공장을 비롯한 각종 유류 취급 공장지역 내의 토양오염이 심각한 사회문제로 대두되고 있으며, 이러한 오염토양을 효율적으로 굴착하고, 이를 복원하기 위해 노력하고 있다.Recently, soil pollution in various oil handling plant areas including oil refineries has been a serious social problem, and efforts have been made to efficiently excavate and restore such soils.

통상적으로 볼 때 토양세척기법은 크게 Ex-situ 세척기법과 In-situ 세척기법으로 나눌 수 있다.In general, soil washing techniques can be largely divided into Ex-situ washing method and In-situ washing method.

상기 Ex-situ 세척기법은 흔히 토양 세척(Soil Washing)이라고도 하는데 토양내 오염 내 물질의 분포 및 토양의 물리/화학적 특성을 파악하여 처리범위의 오염토양을 굴착한 후, 적절한 세척용액을 이용하여 오염된 토양을 세척하는 기법으로 on-site 처리와 off-site 처리로 나눌 수 있다.The ex-situ washing technique is also commonly referred to as soil washing, and after grasping the distribution of substances in soil and physical / chemical characteristics of the soil to excavate the contaminated soil in the treatment range, it is contaminated using an appropriate washing solution. Soil washing method can be divided into on-site treatment and off-site treatment.

상기 In-situ 세척기법은 토양을 굴착하지 않고 세척용액 주입정, 세척용액 배출정, 세척유출수 처리시설, 펌프 및 계장시설, 휘발물질 처리시설 등을 오염된 부지에 설치하여 토양 내에서 세척수를 순환시켜 세척하는 기법으로 처리시간이 길며, 토양공극이 막혀 세척장치에 있어 세척용액의 회수가 어려운 단점이 있다.The in-situ washing technique circulates the washing water in the soil by installing a washing solution injection well, a washing solution discharge well, a effluent treatment facility, a pump and instrumentation facility, and a volatile material treatment facility without polluting the soil. The treatment time is long, and the soil voids are clogged, which makes it difficult to recover the washing solution in the washing apparatus.

토양세척기법은 오염물질에 대한 토양의 혼합정도, 입경분포, 비중에 의해 세척효율이 좌우된다.Soil washing technique depends on the degree of mixing of soil with pollutants, particle size distribution and specific gravity.

여기서, 토양 세척은 구체적으로 오염된 토양을 세척수와 함께 투입하여 가압, 진동, 회전 및 교반 등을 통하여 세척하고 망상(網狀)의 스크린을 통과시킴으로써 세척된 토양 입자와 세척수를 분리하여 세척된 토양은 기본적으로 스크린에 의하여 세척수와 분리되는 방식이므로 소정 입경(粒徑) 이상의 토사만이 수거되고 그 미만의 입경을 가지는 토사는 세척수와 함께 배출된다.Here, the soil washing is specifically put contaminated soil with the wash water to wash through pressure, vibration, rotation and stirring, and passed through the screen of the mesh (網狀) to separate the washed soil particles and the wash water to wash the soil Since the soil is basically separated from the washing water by the screen, only soil having a predetermined particle size or more is collected, and soil having a particle size of less than that is discharged together with the washing water.

따라서, 입경별로 다수의 토양세척장치를 단계적으로 구성하거나 토양세척장치 내 스크린을 다단으로 구성하는 등의 방식이 적용되며, 토양을 구성하는 다양한 입경의 토사를 분류하는 선별장치 또는 탈수장치도 기본적인 작동방식이 전술한 토양세척장치와 유사하므로 실제 토양의 세척 공정에 있어서는 선별장치, 토양세척장치 및 탈수장치가 혼용되고 있다.Therefore, a method of constructing a plurality of soil washing devices in stages or constructing a screen in the soil washing apparatus in multiple stages by particle size is applied, and a sorting device or a dewatering device for classifying soils of various particle sizes constituting soil is also basically operated. Since the method is similar to the above-described soil washing apparatus, the sorting apparatus, the soil washing apparatus, and the dehydration apparatus are mixed in the actual soil washing process.

최근에는 오염된 토양을 복원 세척하는 방법이 공개번호 10-2010-0077497(잔류성 유기화합물 및 중금속에 오염된 토양의 복원 세척방법)로 특허출원된 후 공개되어 있으며, 오염된 토양을 세척한 후 세척에 투입된 세척수를 순환하여 공급하여 세척효율을 높이고 원가를 절감하며, 화학세척 후 배출되는 토양을 연속세정하여 토양에 포함된 오염성분을 살수세정 및 탈수하므로 세척효율을 향상시키고, 아울러 화학세척 후 침사조에서 침사되는 미분의 토양을 입경별로 분리하여 응집, 탈수시켜 슬러지 발생을 저감하는 기술이 지속적으로 개발되고 있다.
Recently, the method of restoring and cleaning contaminated soil has been disclosed after patent application of the Korean Patent Publication No. 10-2010-0077497 (Repairing and cleaning method of soil contaminated with residual organic compounds and heavy metals). It improves washing efficiency by reducing the cost and improves the washing efficiency by circulating and supplying the washing water injected into the water, and improves the washing efficiency by sprinkling and dehydrating pollutants contained in the soil by continuously washing the soil discharged after chemical washing. The technology to reduce sludge generation by separating the sediment of fine soil settling in the sand by the particle diameter and coagulating and dehydrating is continuously developed.

본 발명은 상기한 시대적인 요구에 부응하고자 개발된 것으로서, 본 발명의 목적은 오염된 토양을 골재별로 분리한 후 세척하고 세척시 사용되는 세척수를 순환시켜 재차 공급함으로서, 세척효율을 향상시키며 원가를 절감하고, 연속 살수세정 및 탈수하는 중금속 오염토양 세척방법를 제공하는데 그 목적이 있다.The present invention was developed to meet the demands of the times, the object of the present invention is to separate the polluted soil by aggregate and to wash and to supply again by circulating the washing water used for washing, improving the cleaning efficiency and cost The purpose of the present invention is to provide a method for washing heavy metal contaminated soil, which is reduced, and continuously sprayed and dehydrated.

본 발명의 또 다른 목적은 세척 후 배출되는 미분의 오염토를 연속세척하여 미분에 포함된 오염성분을 세척함과 아울러 화학세척 후 침사되는 미분의 토양를 입경별로 분리하여 응집, 탈수시켜 슬러지 발생을 저감시키는 중금속 오염토양 세척방법를 제공하는데 또 다른 목적이 있다.
Another object of the present invention is to continuously clean the contaminated soil of the fine powder discharged after washing to wash the contaminants contained in the fine powder, and also to separate the soil of fine powder sedimented after chemical washing by particle size to agglomerate and dehydrate to reduce sludge generation. Another purpose is to provide a heavy metal contaminated soil cleaning method.

본 발명은 오염토를 입경별로 분류한 후 공정수를 순환 공급되게 구성시켜 분류된 오염토를 세척하는 순환세척단계와 상기 순환세척단계를 거친 오염토 골재를 화학세척단계를 거쳐 반복 살수세정 및 탈수하는 연속세척단계와 상기 화학세척단계를 거쳐 침사조로 이동된 미분의 오염토를 분리, 탈수하여 슬러지화하는 침사토양처리단계로 이루어진 것을 특징으로 한다.According to the present invention, after the soil is classified by particle diameter, the process water is circulated to be supplied to the process, and the circulating washing step of washing the classified soil and the circulating washing aggregate are repeatedly washed and dehydrated through the chemical washing step. The sedimentation soil treatment step of separating and dewatering the contaminated soil of fine powder transferred to the sedimentation tank through the continuous washing step and the chemical washing step is characterized in that it consists of.

또한, 상기 세척단계는 상부에 스크린을 갖는 로그와셔에 공정수와 오염토를 투입하되, 상기 오염토는 입경이 40mm이상의 골재는 상기 스크린에 의해 걸러져 세척되고, 입경이 40mm이하의 골재는 상기 로그와셔 내부에 투입되어 내부에 마련되는 패덜(Paddle)에 의해 상기 공정수와 교반시키는 교반공정와 상기 로그와셔에서 교반된 공정수와 오염토를 탈수 스크린으로 공급받아 1mm이상의 골재와 1mm이하의 골재를 분리하는 분리공정과 상기 탈수 스크린에서 1mm이상의 골재를 벨트콘베이어로 배출하여 완료토로 보내는 공정과 상기 탈수 스크린에서 1mm이하의 골재와 공정수를 조정조로 공급하는 공정과 상기 조정조에서 하이드로 사이클론으로 1mm이하의 골재와 공정수를 공급하는 공정과 상기 조정조에서 전달된 골재는 화학세척조로 전달하고, 공정수는 재차 로그와셔로 전달하는 순환공정로 이루어진 것을 특징으로 한다.In addition, the washing step is to put the process water and contaminated soil in the log washer having a screen on the top, the contaminated soil is the aggregate of more than 40mm particle is washed by the screen, the aggregate is less than 40mm aggregate aggregate A stirring process for stirring with the process water and a process water stirred in the log washer and a contaminated soil are supplied to a dewatering screen by a paddle provided inside the washer and separated therein to separate aggregates of 1 mm or more and aggregates of 1 mm or less. The separation process and the discharge of more than 1mm aggregate from the dewatering screen to the belt conveyor to send to the finished soil and the process of supplying less than 1mm aggregate and process water from the dewatering screen to the control tank and aggregate less than 1mm to the hydrocyclone in the adjustment tank And the process for supplying the process water and the aggregate delivered from the adjusting tank is delivered to the chemical washing tank, the process water The cycle consisting of the step of transfer into the next log washer is characterized.

또한, 상기 연속세척단계는 상기 화학세척조에서 세척된 골재를 공급받아 1차 진동스크린 위에서 세정수로 세척 후 탈수시키는 1차 샌드 세척공정과, 상기 1차 샌드 세척공정을 거친 골재를 재차 2차 진동스크린에서 세정수로 세척 후 탈수시키는 2차 샌드 세척공정으로 이루어진 것을 특징으로 한다.In addition, the continuous washing step receives the aggregate washed in the chemical washing tank, the first sand washing step of washing and dehydrating after washing with the washing water on the first vibrating screen, and the second vibration of the aggregate after the first sand washing process again It is characterized by consisting of a second sand washing step of dehydration after washing with washing water in the screen.

또한, 상기 침사토양처리단계는 상기 화학세척조로부터 오염토의 미세입자가 포함된 공정수를 침사조로 공급받은 후 상기 공정수에 포함된 미세입자의 입경크기에 따라 약품반응조 및 침사보조탱크로 공급시키는 공정과 상기 약품반응조로 부터 제 1 고속응집농축조로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집한 후 응집된 미세입자들을 제 1 필터프레스를 통해 배출시키는 공정과 상기 침사보조탱크로 부터 제 2 고속응집농축조로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집한 후 응집된 미세입자들을 제 2 필터프레스를 통해 배출시키는 공정과 상기 제 1 고속응집농축조와 상기 제 2 고속응집농축조에서 제 1 침전조와 제 2 침전조로 각각 공정수를 공급받아 미세입자를 침전시킨 후 상기 제 1 침전조와 상기 제 2 침전조의 침전된 미세입자를 재차 상기 제 1 고속응집농축조와 상기 제 2 고속응집농축조로 공급시키는 공정과 상기 제 1 침전조와 상기 제 2 침전조의 공정수를 집수탱크로 이동시킨 후 여과조를 거쳐 공정수 탱크로 유입시키는 공정으로 이루어진 것을 특징으로 한다.
In addition, the step of treating the sedimentation soil is a step of supplying the process water containing the fine particles of contaminated soil from the chemical cleaning tank to the settling tank and supplying it to the chemical reaction tank and the settling auxiliary tank according to the particle size of the fine particles included in the process water. And the process water is supplied from the chemical reaction tank to the first high-speed agglomeration concentrate tank, and a coagulant is supplied to coagulate the microparticles contained in the process water, and then the coagulated microparticles are fed through the first filter press. The process water is discharged and the process water is supplied from the sedimentation auxiliary tank to the second high-speed agglomeration concentration tank, and a coagulation agent is supplied to agglomerate the microparticles contained in the process water, and the coagulated microparticles are collected. Discharging through a filter press, and the first settling tank and the first settling tank in the first and second high Supplying process water to each of the two settling tanks to precipitate the fine particles, and then supplying the precipitated fine particles of the first settling tank and the second settling tank to the first high-density concentrating tank and the second high-density concentrating tank again; After moving the process water of the first settling tank and the second settling tank to the collecting tank, it is characterized in that the step consisting of flowing into the process water tank through the filtration tank.

본 발명인 중금속 오염토양 세척방법은 오염된 토양을 골재별로 분리한 후 세척하고 세척시 사용되는 세척수를 순환시켜 재차 공급함으로서, 세척효율을 향상시키며 원가를 절감할 수 있는 효과가 있다.Heavy metal contaminated soil washing method of the present invention is to separate the contaminated soil by aggregate, and to wash and supply again by circulating the washing water used for washing, improving the cleaning efficiency and reduce the cost.

또한, 화학세척 후 배출되는 골재를 연속세척하여 골재에 포함된 오염성분을 세척함과 아울러 화학세척 후 침사되는 미분의 오염토를 입경별로 분리하여 응집, 탈수시켜 슬러지 발생을 저감시키는 효과가 있다.
In addition, by continuously washing the aggregate discharged after the chemical cleaning to wash the contaminants contained in the aggregate, and also to separate the contaminated soil of fine dust settled after the chemical cleaning by particle diameter, there is an effect to reduce the sludge generation.

도 1은 본 발명에 따른 중금속 오염토양 세척방법의 순서를 나타낸 블럭도이다.
도 2는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 순환세척단계 및 화학세척단계를 나타낸 도면이다.
도 3은 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 연속세척단계를 나타낸 블럭도이다.
도 4는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 연속세척단계를 나타낸 계략도이다.
도 5는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 침사토양처리단계를 나타낸 도면이다.
1 is a block diagram showing the procedure of the heavy metal contaminated soil washing method according to the present invention.
2 is a view showing a circulating washing step and a chemical washing step according to the heavy metal contaminated soil washing method according to the present invention.
3 is a block diagram showing a continuous washing step according to the heavy metal contaminated soil washing method according to the present invention.
Figure 4 is a schematic diagram showing a continuous washing step according to the heavy metal contaminated soil washing method according to the present invention.
5 is a view showing the sedimentation soil treatment step in the heavy metal contaminated soil washing method according to the present invention.

이하, 첨부된 도면들을 참조하여 본 발명에 따른 중금속 오염토양 세척방법의 바람직한 실시예를 첨부된 도면을 참조하여 설명한다. 이 과정에서 도면에 도시된 선들의 두께나 구성요소의 크기 등은 설명의 명료성과 편의상 과장되게 도시되어 있을 수 있다. 또한, 후술되는 용어들은 본 고안에서의 기능을 고려하여 정의된 용어들로서 이는 사용자, 운용자의 의도 또는 관례에 따라 달라질 수 있다. 그러므로, 이러한 용어들에 대한 정의는 본 명세서 전반에 걸친 내용을 토대로 내려져야 할 것이다.Hereinafter, with reference to the accompanying drawings will be described a preferred embodiment of a heavy metal contaminated soil washing method according to the present invention with reference to the accompanying drawings. In this process, the thicknesses of the lines and the sizes of the components shown in the drawings may be exaggerated for clarity and convenience of explanation. In addition, the terms described below are defined in consideration of the functions in the present invention, and this may vary depending on the intention or custom of the user, the operator. Therefore, definitions of these terms should be made based on the contents throughout this specification.

또한, 하기 실시예는 본 발명의 권리범위를 한정하는 것이 아니라 단지 예시로 제시하는 것이며, 본 기술 사상을 통해 구현되는 다양한 실시예가 있을 수 있다.In addition, the following embodiments are not intended to limit the scope of the present invention, but merely as an example, and various embodiments may be implemented through the present invention.

도 1은 본 발명에 따른 중금속 오염토양 세척방법의 순서를 나타낸 블럭도이며, 도 2는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 순환세척단계 및 화학세척단계를 나타낸 도면이고, 도 3은 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 연속세척단계를 나타낸 블럭도이며, 도 4는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 따른 연속세척단계를 나타낸 계략도이고, 도 5는 본 발명에 따른 중금속 오염토양 세척방법에 있어, 침사토양세척단계를 나타낸 도면이다.1 is a block diagram showing the order of the heavy metal contaminated soil washing method according to the invention, Figure 2 is a view showing a circulating washing step and a chemical washing step according to the heavy metal contaminated soil washing method according to the invention, Figure 3 In the heavy metal contaminated soil washing method according to the present invention, is a block diagram showing a continuous washing step according to, Figure 4 is a schematic diagram showing a continuous washing step according to the heavy metal contaminated soil washing method according to the invention, Figure 5 In the heavy metal contaminated soil washing method according to the invention, it is a view showing the step of washing the soil.

도면에 도시된 바와 같이 본 발명인 중금속 오염토양 세척방법(이하 설명의 편의상 오염토양 세척방법이라 명명함)은 오염토를 입경별로 분류한 후 공정수를 순환 공급되게 구성시켜 분류된 오염토를 세척하는 순환세척단계(S1)와 상기 세척단계(S1)를 거친 오염토 골재를 화학세척하는 화학세척단계(S2)와 상기 화학세척단계(S2)를 거쳐 반복 살수 및 세척하는 연속세척단계(S3)와 상기 화학세척단계(S2)를 거쳐 침사조로 이동된 미분의 오염토를 세척하는 침사토양처리단계(S4)로 이루어진다.As shown in the drawings, the present inventors heavy metal contaminated soil washing method (hereinafter referred to as contaminated soil washing method for convenience of description) is to classify the contaminated soil by particle size and to configure the process water to be circulated supply to wash the contaminated soil Circulating washing step (S1) and the continuous washing step (S3) to repeatedly spray and wash through the chemical washing step (S2) and the chemical cleaning step (S2) and the chemical cleaning step of the soil contaminated through the washing step (S1) and It consists of a sedimentation soil treatment step (S4) for washing the contaminated soil of fine powder moved to the sedimentation tank through the chemical washing step (S2).

상기 세척단계(S1)는 상부 스크린(120)과 하부 로그와셔(110)로 상부 스크린(120)으로 공정수와 오염토를 투입하게 되며, 하부에 교반공간을 갖는 로그와셔(110)가 오염토와 공정수를 교반한다. 상기 오염토에 포함되는 입경이 40mm이상의 골재는 상기 스크린(120)에 의해 걸러져 분리된 후 상기 스크린 상부에서 분사되는 물에 의해 세척되고, 입경이 40mm이하의 골재는 상기 스크린을 통과하여 상기 로그와셔(110) 내부에 투입되어 내부에 마련되는 회전축과 상기 회전축에 형성되는 다수의 교반날개로 이루어진 패덜(Paddle)에 의해 상기 공정수와 교반됨과 아울러 이동되는 교반공정을 거치게 되고, 상기 로그와셔(110)에서 교반된 공정수와 오염토는 탈수 스크린(130)으로 이동되어 상기 탈수 스크린(130)을 통과하지 못하는 1mm이상의 골재와 통과된 1mm이하의 골재를 분리하는 분리공정을 거치게 된다.The washing step (S1) is to put the process water and contaminated soil to the upper screen 120 to the upper screen 120 and the lower log washer 110, the log washer 110 having a stirring space in the lower soil contaminated And the process water is stirred. Aggregate with a particle diameter of 40 mm or more included in the contaminated soil is filtered out by the screen 120 and then washed by water sprayed from the upper part of the screen, and an aggregate having a particle diameter of 40 mm or less passes through the screen and the log washer. (110) a paddle (Paddle) made of a rotating shaft provided in the inside and a plurality of agitating blades formed on the rotating shaft is stirred with the process water and is moved through the stirring process, the log washer 110 Agitated process water and contaminated soil in the) is moved to the dewatering screen 130 is subjected to a separation process of separating more than 1mm aggregate and less than 1mm aggregate passed through the dewatering screen 130.

이후, 상기 탈수 스크린(130)에서 분리된 1mm이상의 골재는 벨트콘베이어(180)를 거쳐 완료토로 보내어지게 되고, 상기 탈수 스크린(130)을 통과한 1mm이하의 토양과 공정수를 조정조(150)로 공급하는 공정을 거친 다음 이송펌프(160)를 통해 상기 조정조(150)에서 하이드로 사이클론(170)으로 1mm이하의 토양과 공정수를 공급하여 고액분급시키며, 상기 사이클론(170)에서 나가는 공정수를 재차 로그와셔(110)와 화학세척조(140)으로 전달하여 순환되게 함과 아울러 사이클론에서 분급되어진 1mm이하의 토양을 화학세척조(140)에 전달하게 됨으로서, 오염토를 화학세척조에 전달하여 화학세척하는 화학세척단계(S2)를 수행하게 됨과 아울러 공정수를 순환시켜 상기 로그와셔(110)에 공급할 수 있게 된다. 이때, 상술된 공정수는 사이클론에서 고액분급되고 난 후 분급되지 못한 1mm이하의 미분이 공정수에 포함되어 이동된다.Then, the aggregate of 1mm or more separated from the dewatering screen 130 is sent to the finished soil via the belt conveyor 180, the soil and process water of 1mm or less passed through the dewatering screen 130 to the adjustment tank 150 After the process of supplying and supplying the soil and the process water of 1mm or less from the adjusting tank 150 to the hydrocyclone 170 through the transfer pump 160, and classifies the liquid-liquid, and the process water exiting from the cyclone 170 again It is delivered to the log washer 110 and the chemical cleaning tank 140 to circulate, and delivers the soil of 1 mm or less classified in the cyclone to the chemical cleaning tank 140, and delivers the contaminated soil to the chemical cleaning tank for chemical cleaning. In addition to performing the washing step (S2) it can be supplied to the log washer 110 by circulating the process water. At this time, the above-mentioned process water is moved to include the fine powder of less than 1mm that is not classified after the solid-liquid classification in the cyclone.

이때, 상기 화학세척조(140)는 내부에 다수의 교반실을 갖으며 각각의 교반실에서 유입되는 공정수, 오염토 및 화학약품을 고속교반기를 통해 교반시켜, 오염된 토양의 체류되는 시간을 늘려 세척효율을 향상시키는 것으로서, 오염된 토양은 입도가 작을수록 입도가 큰 토양과 비교하여 농도가 높으므로, 입도가 작은 토양을 순환시켜 세척시간을 길게 하는 것이 바람직하다.At this time, the chemical washing tank 140 has a plurality of stirring chambers therein and by stirring the process water, contaminated soil and chemicals introduced from each stirring chamber through a high speed stirrer, to increase the residence time of the contaminated soil In order to improve the cleaning efficiency, the contaminated soil has a higher concentration as compared to the soil having a larger particle size, so that it is preferable to circulate the soil having a small particle size to lengthen the washing time.

또한, 교반실 내부에 제트밀이 마련되어 외부에서 전달되는 압축공기를 서로 마주보게 배치된 노즐을 통해 배출시켜 오염토 입자간 상호 충돌시킴으로서, 입자의 오염물질을 분리시키게 된다.
In addition, a jet mill is provided inside the stirring chamber to discharge the compressed air delivered from the outside through nozzles disposed to face each other, thereby colliding with the soil particles to separate the contaminants of the particles.

상기 연속세척단계(S3)는 세척효율이 떨어지는 미분의 오염토에 비해 면적이 커 상대적으로 세척효율이 큰 화학세척된 1mm이하의 골재를 상기 화학세척조에서 공급받아 세척한 후 세척이 종료된 완료토를 형성시키는 것으로서, 이러한 연속세척단계(S2)는 상기 화학세척조에서 상부에 설치된 샌드 1번 사이클론(220)으로 토양을 고액분급하여 샌드 1번 진동스크린(210)에 공급받아 세정수로 세척 후 진동탈수시키는 1차 샌드 세척공정을 거친 후 상기 1차 샌드 세척공정을 거친 토양을 재차 2번 사이클론(240)으로 2차 진동스크린(230)에 공급받아 세정수로 세척 후 진동탈수시키는 2차 샌드 세척공정으로 이루어지며, 상기 2차 샌드 세척공정이 종료된 골재는 완료토로서, 벨트콘베이어로 이동되어 적치되며, 토양정화 검증 후 건축물의 골재 및 사용용도에 따라 되메움되는 것도 가능하다.The continuous washing step (S3) is less than the contaminated soil of fine powder, the washing area is less than 1mm of aggregates, the cleaning efficiency is supplied from the chemical washing tank and the cleaning soil is finished, the finished soil As to form, such a continuous washing step (S2) is a solid-liquid classification of the soil in the sand No. 1 cyclone 220 installed in the upper part in the chemical washing tank is supplied to the sand No. 1 vibrating screen 210 and washed with washing water and then vibrated After the first sand washing process for dehydration, the second sand washing process is applied to the second vibrating screen 230 by the second cyclone 240 to wash the soil after the first sand washing process, and then washed with washing water, followed by the second sand washing. Aggregate made by the process, the second sand washing process is completed as a complete soil, is moved to the belt conveyor and deposited, depending on the aggregate and use of the building after the soil purification verification It is also possible to backfill.

이때, 화학세척조에서 상기 샌드 1차 진동스크린(210)으로 공급되는 토양의 크기는 1mm로 한정되는 것은 아니며 토양의 종류와 오염된 정도에 따라 1mm보다 작거나 큰 골재도 공급시키는 것도 가능하다.
At this time, the size of the soil supplied to the sand primary vibrating screen 210 in the chemical washing tank is not limited to 1 mm, and may also supply aggregates smaller or larger than 1 mm depending on the type of soil and the degree of contamination.

상기 침사토양세척단계(S4)는 상기 화학세척조로부터 오염토의 미세입자가 포함된 공정수를 침사조(310)로 공급받은 후 상기 공정수에 포함된 미세입자의 입경크기에 따라 약품반응조(320) 및 침사보조탱크(330)로 공급시키는 공정을 거친 다음 상기 약품반응조(320)로 부터 제 1 고속응집농축조(321)로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집 한 후 응집 농축된 플럭(Floc)을 제 1 필터프레스(322)를 통해 슬러지 형태로 외부로 배출시키게 된다.The immersion soil washing step (S4) is a chemical reaction tank 320 according to the particle size of the fine particles contained in the process water after receiving the process water containing the fine particles of contaminated soil from the chemical washing tank to the immersion tank (310) And after receiving the process water from the chemical reaction tank 320 to the first high-speed condensing concentration tank 321 and agglomerating fine particles contained in the process water. After supplying the flocculant and condensing at high speed, the flocculated concentrated floc is discharged to the outside in the form of sludge through the first filter press 322.

이후, 상기 침사보조탱크(330)로 부터 제 2 고속응집농축조(331)로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집한 후 응집 농축된 미세입자들을 제 2 필터프레스(332)를 통해 배출시키는 공정을 거치게 되고, 상기 제 1 고속응집농축조(321)와 상기 제 2 고속응집농축조(331)에서 제 1 침전조(323)와 제 2 침전조(333)로 각각 공정수를 공급받아 공정수에 포함되는 잔류된 미세입자를 일정시간동안 침전시킨 후 상기 제 1 침전조(323)와 상기 제 2 침전조(333)의 침전된 미세입자를 재차 상기 제 1 고속응집농축조(321)와 상기 제 2 고속응집농축조(331)로 공급시키는 공정을 거친 다음 상기 제 1 침전조(323)와 상기 제 2 침전조(333)의 공정수를 집수탱크(340)로 이동시킨 후 여과조(350)를 거쳐 공정수 탱크(360)로 유입시킴으로서, 일련의 오염토 세척공정을 마치게 된다. Thereafter, the process water is supplied from the sedimentation auxiliary tank 330 to the second high speed agglomeration concentration tank 331, and a coagulant is supplied to the micro agglomerates to aggregate the fine particles contained in the process water. The fine particles are discharged through the second filter press 332, and the first settling tank 323 and the second settling tank 321 and the second set of high-density condensing tank 331 333) is supplied with the process water, respectively, and the remaining fine particles contained in the process water are precipitated for a predetermined time, and then the precipitated fine particles of the first precipitation tank 323 and the second precipitation tank 333 are again present. After passing through the process of supplying to the high speed concentration tank 321 and the second high speed concentration tank 331, the process water of the first precipitation tank 323 and the second precipitation tank 333 is moved to the collecting tank 340. After entering the process water tank 360 through the filtration tank 350 By doing so, a series of contaminated soil cleaning processes are completed.

상기와 같이 침사토양처리단계(S4)에서는 공정수에 포함된 오염골재의 입경에 따라 구분하여 약품반응조 또는 침사보조탱크(330)로 유입시킴으로서, 세척효율을 극대화 시킬 수 있게 된다.As described above, in the sedimentation soil treatment step (S4), by dividing according to the particle size of the contaminated aggregate included in the process water into the chemical reaction tank or the sedimentation auxiliary tank 330, it is possible to maximize the washing efficiency.

이때, 상기 침사보조탱크(330,330')를 다수개 설치하여 오염골재의 입경 또는 오염정도에 따라 구분하여 골재를 각각 공급한 후 각각의 고속응집농축조(321,331)로 전달되도록 하는 것도 가능하다.At this time, it is also possible to install a plurality of the sedimentation auxiliary tank (330, 330 ') to be supplied to each of the high-speed aggregation concentration tank (321, 331) after supplying the aggregate, respectively, according to the particle size or the degree of contamination of the contaminated aggregate.

바람직하게는, 상기 여과조에 의해 여과되어 공정수 탱크로 유입된 공정수는 외부에서 공급되는 공정수와 함께 재차 로그와셔로 순환되게 공급함으로서, 재활용할 수 있게 된다.
Preferably, the process water filtered by the filtration tank and introduced into the process water tank may be recycled by being supplied to the log washer again with the process water supplied from the outside.

S1 : 순환세척단계 S2 : 화학세척단계
S3 : 연속세척단계 S4 : 침사토양처리단계
110 : 로크와셔 120 : 스크린
130 : 탈수 스크린 140 : 화학세척조
150 : 조정조 160 : 이송펌프
170 : 사이클론
210 : 1차 진동스크린 220 : 1차 사이클론펌프
230 : 2차 진동스크린 240 : 2차 사이클론 펌프
310 : 침사조 320 : 약품반응조
321 : 제 1 고속응집농축조 322 : 제 1 필터프레스
323 : 제 1 침전조 330,330' : 침사보조탱크
331 : 제 2 고속응집농축조 332 : 제 2 필터프레스
333 : 제 2 침전조 340 : 집수탱크
350 : 여과조 360 : 공정수탱크
S1: circulating washing step S2: chemical washing step
S3: Continuous washing step S4: Sedimentation soil treatment step
110: lock washer 120: screen
130: dewatering screen 140: chemical cleaning tank
150: adjustment tank 160: transfer pump
170: cyclone
210: 1st vibration screen 220: 1st cyclone pump
230: 2nd vibrating screen 240: 2nd cyclone pump
310: sedimentation tank 320: chemical reaction tank
321: first high speed condensation concentration tank 322: first filter press
323: 1st sedimentation tank 330,330 ': sedimentation auxiliary tank
331: 2nd high speed condensation concentration tank 332: 2nd filter press
333: second settling tank 340: collecting tank
350: filtration tank 360: process water tank

Claims (4)

오염토를 입경별로 분류한 후 공정수를 순환 공급되게 구성시켜 분류된 오염토를 세척하는 순환세척단계와 상기 순환세척단계를 거친 오염토 골재를 화학약품 및 고속교반기, 제트밀을 이용하여 세척하는 화학세척단계와 상기 화학세척단계를 거친 오염토 골재를 반복 살수 및 세척하는 연속세척단계와 상기 화학세척단계를 거쳐 침사조로 이동된 미분의 오염토를 입경별 침사하여 침사된 입경별로 슬러지 처리하는 침사토양세척단계로 이루어어지되,
상기 순환세척단계는 상부에 스크린을 갖는 로그와셔에 공정수와 오염토를 투입하되, 상기 오염토는 입경이 40mm이상의 골재는 상기 스크린에 의해 걸러져 세척되고, 입경이 40mm이하의 골재는 상기 로그와셔 내부에 투입되어 내부에 마련되는 패덜(Paddle)에 의해 상기 공정수와 교반시키는 교반공정;
상기 로그와셔에서 교반된 공정수와 오염토를 탈수 스크린으로 공급받아 1mm이상의 골재와 1mm이하의 골재를 분리하는 분리공정;
상기 탈수 스크린에서 1mm이상의 골재를 살수 세정 후 탈수하여 벨트콘베이어로 배출시키는 공정;
상기 탈수 스크린에서 1mm이하의 골재와 공정수를 조정조로 공급하는 공정;
상기 조정조에서 하이드로 사이클론으로 1mm이하의 골재와 공정수를 공급하는 공정; 및
상기 조정조에서 전달된 골재는 하이드로 사이클론에서 분급된 토양은 화학세척조로 전달하고, 공정수는 재차 로그와셔로 전달하는 순환공정으로 이루어지고,
상기 침사토양세척단계는 상기 화학세척조로부터 오염토의 미세입자가 포함된 공정수를 침사조로 공급받은 후 상기 공정수에 포함된 미세입자의 입경크기에 따라 약품반응조 및 침사보조탱크로 공급시키는 공정;
상기 약품반응조로 부터 제 1 고속응집농축조로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집한 후 응집된 미세입자들을 제 1 필터프레스를 통해 배출시키는 공정;
상기 침사보조탱크로 부터 제 2 고속응집농축조로 공정수를 공급받음과 아울러 상기 공정수에 포함된 미세입자를 응집시키도록 응집제를 공급받아 고속응집한 후 응집된 미세입자들을 제 2 필터프레스를 통해 배출시키는 공정;
상기 제 1 고속응집농축조와 상기 제 2 고속응집농축조에서 제 1 침전조와 제 2 침전조로 각각 공정수를 공급받아 미세입자를 침전시킨 후 상기 제 1 침전조와 상기 제 2 침전조의 침전된 미세입자를 재차 상기 제 1 고속응집농축조와 상기 제 2 고속응집농축조로 공급시키는 공정; 및
상기 제 1 침전조와 상기 제 2 침전조의 공정수를 집수탱크로 이동시킨 후 여과조를 거쳐 공정수 탱크로 유입시키는 공정으로 이루어진 것을 특징으로 하는 중금속 오염토양 세척방법.
After classifying the contaminated soil by particle size, the process water is circulated and supplied to clean the classified soil and the contaminated soil aggregate after the circulation washing step is cleaned by chemical, high speed stirrer, and jet mill. Continuous washing step of repeatedly spraying and washing the contaminated soil aggregate after the chemical washing step and the chemical washing step and the fine soil contaminated by fine particles transferred to the sedimentation tank through the chemical washing step by sedimentation by sludge treatment Soil washing stage,
The circulation washing step is to put the process water and contaminated soil in a log washer having a screen on the top, the contaminated soil is the aggregate of more than 40mm particle is filtered by the screen and washed, the aggregate of less than 40mm is the log washer A stirring step of stirring with the process water by a paddle (Paddle) is introduced into the inside;
Separating process of separating the aggregate of more than 1mm and aggregate less than 1mm by receiving the process water and contaminated soil stirred in the log washer to the dewatering screen;
Spraying the aggregate of 1 mm or more from the dewatering screen by sprinkling cleaning, and then draining it to a belt conveyor;
Supplying aggregate and process water of 1 mm or less from the dewatering screen to an adjustment tank;
Supplying aggregate and process water of 1 mm or less to the hydrocyclone in the adjusting tank; And
Aggregate delivered from the adjustment tank is made of a circulating process to deliver the soil classified in the hydrocyclone to the chemical washing tank, the process water is again delivered to the log washer,
The saline soil washing step includes the step of receiving the process water containing the fine particles of contaminated soil from the chemical washing tank and supplying it to the chemical reaction tank and the salivary auxiliary tank according to the particle size of the fine particles included in the process water;
The process water is supplied from the chemical reaction tank to the first high-speed aggregating tank, and a coagulant is supplied to agglomerate the fine particles contained in the process water, and the coagulated microparticles are discharged through the first filter press. Making process;
The process water is supplied from the sedimentation auxiliary tank to the second high-speed agglomeration concentrate tank, and a coagulant is supplied to agglomerate the fine particles contained in the process water, and then the high-density agglomerated microparticles are collected through a second filter press. Discharge process;
Receiving the process water from the first high-speed agglomeration concentration tank and the second high-speed agglomeration concentration tank to the first settling tank and the second settling tank, respectively, precipitates the fine particles, and again precipitates the fine particles of the first settling tank and the second settling tank. Supplying the first high speed condensation concentration tank and the second high speed condensation concentration tank; And
The process of washing the heavy metal contaminated soil comprising the step of moving the process water of the first settling tank and the second settling tank to a collection tank and then flowing the process water into a process water tank.
삭제delete 제 1 항에 있어서,
상기 연속세척단계는 상기 화학세척조에서 세척된 골재를 공급받아 1차 진동스크린 위에서 세정수로 세척 후 탈수시키는 1차 샌드 세척공정과,
상기 1차 샌드 세척공정을 거친 골재를 재차 2차 진동스크린에서 세정수로 세척 후 탈수시키는 2차 샌드 세척공정으로 이루어진 것을 특징으로 하는 중금속 오염토양 세척방법.
The method of claim 1,
The continuous washing step is a first sand washing process for receiving the aggregates washed in the chemical washing tank washing with deionized water on the first vibrating screen and then dehydrating,
The heavy sand contaminated soil washing method comprising the second sand washing step of washing the aggregate after the first sand washing step again with the washing water in the second vibrating screen.
삭제delete
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KR20210086798A (en) 2019-12-30 2021-07-09 주식회사 엘림글로벌 Decontamination Method for Contaminated Soil in Decommissioning Nuclear Power Plant
CN114160560A (en) * 2021-11-16 2022-03-11 容春山 Soil repair system of usefulness is administered to environment

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