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JP3918657B2 - Method and apparatus for purifying contaminated soil - Google Patents

Method and apparatus for purifying contaminated soil Download PDF

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Publication number
JP3918657B2
JP3918657B2 JP2002190523A JP2002190523A JP3918657B2 JP 3918657 B2 JP3918657 B2 JP 3918657B2 JP 2002190523 A JP2002190523 A JP 2002190523A JP 2002190523 A JP2002190523 A JP 2002190523A JP 3918657 B2 JP3918657 B2 JP 3918657B2
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soil
separating
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JP2004033812A (en
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浩司 渕上
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JFE Engineering Corp
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JFE Engineering Corp
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Description

【0001】
【産業上の利用分野】
本発明は、汚染物質を含有する土壌等を処理する方法および装置に関するものであり、汚染土壌の他に埋立廃棄物や河川・湖沼あるいは海域の底泥、さらには水処理プロセスから発生する汚泥や脱水ケーキの浄化処理にも適用できる。
【0002】
【従来の技術】
汚染土壌等の浄化方法としては、熱分解する方法や微生物によって浄化する方法および薬剤により洗浄する方法等が従来知られている。熱分解する方法は、大量の汚染土壌をダイオキシン類等の汚染物質が分解する温度まで加温するためのエネルギーコストが高く、また微生物によって浄化する方法は浄化処理が終了するまでに年単位の期間を要するという欠点があった。薬剤により洗浄する方法に関しては、例えば特許第3182546号にトリクロロエチレン等で汚染された土壌を界面活性剤で洗浄する方法が示されている。しかし、本方法では洗浄水に含まれる汚染物質の除去に活性炭吸着処理を用いており、界面活性剤および土壌中の様々な有機物質を高濃度に含む洗浄液を活性炭処理するためにその交換頻度が高くなり、高価な活性炭を大量に使用するという問題があった。
【0003】
【発明が解決しようとする課題】
この発明は上記のような問題点を解決するためになされたもので、汚染土壌等に含有される汚染物質を効率よく除去する、汚染土壌等の浄化方法および浄化装置を提供することを目的とする。
【0004】
【課題を解決するための手段】
請求項1、2、3の発明は、難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄することによって、該難分解性有機物質を土壌の固形分から液相に移行させる工程と、この工程の後に、該混合物を固液分離し、固相を浄化物として取り出す工程と、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程とを備えた汚染土壌の浄化方法において、
前記界面活性剤がアミノ酸型両性界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相に酸を混合する工程であることを特徴とする汚染土壌の浄化方法、
前記界面活性剤がポリエチレングリコール型非イオン界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相を加温して曇点より高い温度にする工程であることを特徴とする汚染土壌の浄化方法、又は、
前記界面活性剤がアニオン型界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相にカルシウムを主成分とする無機化合物を添加する工程であることを特徴とする汚染土壌の浄化方法である。
この方法では、液相中の汚染物質および界面活性剤が結合した状態のままで液相から分離するため、清澄な液相が得られる。
【0006】
また、請求項の発明は、界面活性剤と難分解性有機物質の結合体を分離された液相に界面活性剤を添加し、難分解性有機物質で汚染された土壌の洗浄に再度利用することを特徴とする処理方法である。この方法では、処理された液相を再利用することによって、補給水量および系外への排水量を大幅に削減することができる。
【0007】
また、請求項の発明は、液相から分離された界面活性剤と難分解性有機物質の結合体を焼却炉、溶融炉または熱分解炉に投入して汚染物質を加熱分解することを特徴とする処理方法である。この方法では、液相から分離された汚染物質を加熱分解することによって完全に無害化できる。
【0008】
また、請求項6,7,8の発明は、難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄する混合手段、該混合物を固液分離する固液分離手段、及び固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する分離手段とを備えた汚染土壌の浄化装置において、
前記界面活性剤がアミノ酸型両性界面活性剤であり、前記分離手段が、前記液相に酸を混合する手段を有することを特徴とする汚染土壌の浄化装置、
前記界面活性剤がポリエチレングリコール型非イオン界面活性剤であり、前記分離手段が、前記液相を加温して曇点より高い温度にする手段を有することを特徴とする汚染土壌の浄化装置、又は、
前記界面活性剤がアニオン型界面活性剤であり、前記分離手段が、前記液相にカルシウムを主成分とする無機化合物を添加する手段を有することを特徴とする汚染土壌の浄化装置である。
本装置によって本発明の浄化方法を具現化することが出来る。
【0009】
【発明の実施の形態】
以下、本発明に関わる汚染土壌等の浄化方法および浄化装置の実施形態を図に基づいて説明する。
【0010】
(実施形態1)
図1は、本発明に関わる汚染土壌等の浄化方法の一実施形態を示したものである。同図において、1は第一混和槽、2は界面活性剤注入管、3は遠心脱水機、4は酸注入管、5は凝集剤注入管、6は第二混和槽、7は沈殿槽である。
【0011】
汚染物質を含む土壌等は第一混和槽1で界面活性剤注入管2から供給される界面活性剤と混和され、汚染土壌等に含有される汚染物質が液相へ移行する。次いで、遠心脱水機3へ供給され、界面活性剤と汚染物質の結合体を含む液相と、汚染物質が除去された固相とに分離される。固相はそのまま浄化物として取り出される。液相は、第二混和槽6において酸注入管4から供給される酸と凝集剤注入管5から供給される凝集剤と混和され、界面活性剤と汚染物質の結合体は不溶化・凝集された後、沈殿槽7においてスラッジとして沈殿分離される。スラッジは最終的に焼却炉にて焼却処理され、汚染物質は熱分解される。
【0012】
ここで、汚染物質とはダイオキシン類や環境ホルモン類、農薬、PCB等の難分解性有機物質やフッ素・ホウ素・重金属等の無機物質、さらにはこれらの物質と土壌微粒子とが吸着している結合体等であり、特定の物質に限定されるものではない。また、土壌等とは土壌、埋立廃棄物、河川・湖沼あるいは海域の底泥、さらには水処理プロセスから発生する汚泥やその脱水ケーキ等を指す。
【0013】
汚染土壌等の汚染物質含有量ができるだけ高い状態で処理を行った方が界面活性剤と汚染物質の接触効率が高まるため、混合操作を容易にできる範囲において、必要に応じて濃縮処理等を行って汚染土壌等中の有機物含有量を高めた後に界面活性剤と汚染土壌等との混合を実施する方が好ましい。もちろん、土壌等の処理においてそのままの形態では混合操作が困難である場合には、水分を混合操作が容易に行えるまで添加して処理を実施することもできる。
【0014】
本発明で用いる界面活性剤としては、アニオン型、カチオン型、両性型、非イオン型等の様々な界面活性剤を用いることができる。例えば、アニオン型としては、セッケン等のカルボン酸塩、硫酸エステル塩、スルホン酸塩等が、カチオン型として、アミン塩、第4級アンモニウム塩等が、両性型としてはアミノ酸型、ベタイン型等が、非イオン型としてはポリエチレングリコール型等を用いることが出来る。
【0015】
汚染土壌等と界面活性剤との混合・洗浄手段は本実施例に限定されるものではないが、通常攪拌機付の混和槽が用いられる。また、超音波照射手段を併用すると汚染土壌等と界面活性剤との接触効率を高めることができ好適である。このようにすることにより、汚染物質を土壌等の固形分から液相へ移行させることができる。
【0016】
汚染土壌等の固液分離手段としては、遠心脱水機の他に、スクリーン、沈殿槽、フィルタープレス等様々なものを用いることが出来る。
【0017】
液相からの界面活性剤と汚染物質との結合体の分離手段は、適用する界面活性剤の特性に応じて数種類の手段から選択することが出来る。適用する界面活性剤がアミノ酸型両性界面活性剤の場合には、本実施形態のように洗浄操作後に酸を添加してpHを等電点に調整することによって、不溶化することが出来る。また、ポリエチレングリコール型非イオン界面活性剤の場合には加温して曇点より高い温度とすることによって不溶化することが出来る。また、アニオン型界面活性剤の場合にはカルシウム等を主成分とする無機化合物を添加することによって、不溶性の塩を形成させることが出来る。不溶化させた界面活性剤と汚染物質の結合体は、その比重によって浮上または沈降といった手段で分離することができる。また、場合によっては遠心分離を適用することも出来る。
【0018】
なお、単に不溶化させることのみでは分離し難い場合には、凝集剤を添加・混和してフロックを形成させることにより分離を促進させることも可能である。この際に用いられる凝集剤としては、塩化第二鉄やポリ硫酸第二鉄等の鉄塩や、硫酸ばんどやPACのようなアルミニウム塩等が適用可能であり、さらにポリアクリルアミド等の有機高分子化合物を併用することも出来る。
【0019】
一方、起泡性のある界面活性剤を用いる場合には、液相を曝気するか、あるいは液相に気体が過飽和に溶解した加圧水を注入することによって多数の気泡を形成させ、気泡表面に界面活性剤と汚染物質の結合体をスカムとして濃縮して除去することができる。
【0020】
界面活性剤と汚染物質の結合体を分離した液相は、再度浄化処理に用いることが出来る。例えば、界面活性剤を添加して汚染土壌等と接触させることや、洗浄後の土壌に残存する界面活性剤のリンスに用いることが可能である。
【0021】
液相から分離された界面活性剤と汚染物質の結合体は処理前の汚染土壌に比べて濃縮されるため、量が著しく減少する。したがって、オゾン注入による酸化分解や紫外線照射による脱塩素等の様々な手段を用いて低コストに無害化することが可能であるが、加熱方式により短時間でほぼ完全に分解することができる。特に既設の焼却炉、溶融炉または熱分解炉が土壌浄化設備の近傍に存在する場合には、液相から分離された界面活性剤と汚染物質の結合体を該加熱方式設備で処理することにより、設備の建設費を削減できるため好適である。
【0022】
(実施形態2)
図2は、本発明に関わる汚染土壌等の浄化方法の別の実施形態を示したものである。同図において、1は第一混和槽、2は界面活性剤注入管、3は遠心脱水機、4は酸注入管、5は凝集剤注入管、8はpH調整槽、9は中和槽、10はアルカリ注入管、11は処理水循環管、12は第三混和槽、13は浮上分離槽、14は加圧水注入管である。
【0023】
汚染土壌等はpH調整槽8で酸注入管4から供給される酸、処理水循環管11より供給される処理水および補給水と混和され、汚染土壌等に含有されるカルシウム化合物を溶解させる。次に中和槽9においてアルカリ注入管10より供給されるアルカリと混和されてpHを中性に調整される。引き続いて第一混和槽1において界面活性剤注入管2から供給される界面活性剤と混合された後に遠心脱水機3において界面活性剤と汚染物質の結合体を含む液相と、汚染物質が除去された固相とに分離される。液相は、浮上分離槽13において凝集剤注入管5から供給される凝集剤および加圧水注入管14から供給される空気を過飽和に溶解した加圧水と混和され、界面活性剤および汚染物質の結合体は気泡表面に濃縮された後、スカムとして浮上分離され、残余が処理水となる。一方、遠心脱水機で取り出された固相はいったん第三混和槽12において処理水と混合された後に再度遠心脱水機3で固液分離されることにより、残留する界面活性剤と汚染物質の結合体を洗い出した後に浄化物として取り出される。
【0024】
汚染土壌等が石灰成分や鉄、マンガン等の金属成分の含有量が多くこれらが汚染物質と界面活性剤との接触を妨げて高い洗浄効率が得られない場合は、本実施形態のように汚染土壌等と界面活性剤の混合前あるいは混合中に酸を混合して石灰成分や金属成分を溶解させると接触効率が向上して良好な洗浄効果が得られる。一方、汚染土壌等がフミン酸等の有機物の含有量が多く、対象汚染物質と界面活性剤との接触を妨げて高い洗浄効率が得られない場合は、汚染土壌等と界面活性剤の混合前あるいは混合中にアルカリを混合してフミン酸等の有機物を溶解させると接触効率が向上して良好な洗浄効果が得られる。
【0025】
また、本実施形態のように得られた処理水を遠心脱水後の固形分のリンスや界面活性剤の溶解、浄化対象物の水分調整に用いることによって、全体の使用水量を低減でき、浄化コストの低減と排水量の削減の効果が得られる。
【0026】
【実施例】
ダイオキシン類で汚染された土壌を図2に示した処理方法で処理した結果を表1に示した。但し、処理条件は次の通りである。
【0027】
[実施例処理方法]
・界面活性剤の種類:ノニオン界面活性剤(アルコール系)
・界面活性剤との反応時間:30分
・反応温度:常温
・界面活性剤注入率:0.5wt%
【表1】

Figure 0003918657
【0028】
【0029】
【発明の効果】
本発明による処理方法は汚染土壌等と界面活性剤とを撹拌・混合することによって、汚染土壌等に含有される汚染物質を高効率に除去すると共に、洗浄水中の界面活性剤と汚染物質との結合体を効率的に水相から分離するといった効果を奏する。
【図面の簡単な説明】
【図1】本発明に係る汚染土壌等の浄化方法の実施形態を示す図。
【図2】本発明に係る汚染土壌等の浄化方法の別の実施形態を示す図。
【符号の説明】
1…第一混和槽、2…界面活性剤注入管、3…遠心脱水機、4…酸注入管、5…凝集剤注入管、6…第二混和槽、7…沈殿槽、8…pH調整槽、9…中和槽、10…アルカリ注入管、11…処理水循環管、12…第三混和槽、13…浮上分離槽、14…加圧水注入管。[0001]
[Industrial application fields]
The present invention relates to a method and apparatus for treating soil containing pollutants, in addition to contaminated soil, landfill waste, rivers / lakes or bottom mud of sea areas, and sludge generated from water treatment processes. It can also be applied to purification treatment of dehydrated cake.
[0002]
[Prior art]
As a purification method for contaminated soil and the like, a thermal decomposition method, a purification method using microorganisms, a cleaning method using a chemical, and the like are conventionally known. The thermal decomposition method has a high energy cost for heating a large amount of contaminated soil to a temperature at which pollutants such as dioxins are decomposed, and the method of purifying with microorganisms is a yearly period before the purification treatment is completed. There was a drawback of requiring. Regarding a method of cleaning with a chemical, for example, Japanese Patent No. 3182546 shows a method of cleaning soil contaminated with trichlorethylene or the like with a surfactant. However, this method uses activated carbon adsorption treatment to remove contaminants contained in the washing water, and the replacement frequency is high because the washing solution containing surfactants and various organic substances in the soil at high concentrations is treated with activated carbon. There was a problem that it used a large amount of expensive activated carbon.
[0003]
[Problems to be solved by the invention]
The present invention has been made to solve the above-described problems, and an object thereof is to provide a purification method and a purification device for contaminated soil and the like that efficiently remove contaminants contained in the contaminated soil and the like. To do.
[0004]
[Means for Solving the Problems]
The inventions of claims 1, 2, and 3 transfer the persistent organic substance from the solid matter of the soil to the liquid phase by mixing and washing the soil contaminated with the persistent organic substance and the surfactant. A step of separating the mixture into a solid-liquid separation after this step and taking out the solid phase as a purified product, and separating the combined surfactant and the hardly decomposable organic substance from the solid-liquid separated liquid phase In the purification method of contaminated soil comprising a process,
The surfactant is an amino acid type amphoteric surfactant, and the step of separating the conjugate of the surfactant and the hardly decomposable organic substance from the solid-liquid separated liquid phase is a step of mixing an acid with the liquid phase. A method for purifying contaminated soil, characterized by
The surfactant is a polyethylene glycol type nonionic surfactant, and the step of separating the binder of the surfactant and the hardly decomposable organic substance from the solid-liquid separated liquid phase is performed by heating the liquid phase. A method for purifying contaminated soil, characterized by being a step of raising the temperature above the cloud point , or
It said surfactant is an anionic surfactant, separating the conjugate of surfactants and flame decomposable organic matter from the solid-liquid separated liquid phase, composed mainly of calcium in the liquid phase It is a purification method for contaminated soil, which is a step of adding an inorganic compound.
In this method, since the contaminants and the surfactant in the liquid phase are separated from the liquid phase while being bonded, a clear liquid phase is obtained.
[0006]
The invention of claim 4 is the surfactant is added to the separated liquid phase conjugate of surfactant and hardly decomposable organic substances, used again for cleaning soil contaminated with persistent organic substances It is a processing method characterized by doing. In this method, by reusing the treated liquid phase, the amount of makeup water and the amount of discharged water outside the system can be greatly reduced.
[0007]
Further, the invention of claim 5 is characterized in that a contaminant and a hard-to-decompose organic substance combination separated from a liquid phase is put into an incinerator, a melting furnace or a thermal decomposition furnace to thermally decompose the pollutant. It is a processing method. In this method, contaminants separated from the liquid phase can be completely detoxified by thermally decomposing them.
[0008]
The inventions of claims 6, 7 and 8 include a mixing means for mixing and washing the soil contaminated with a hardly decomposable organic substance and a surfactant, a solid-liquid separation means for solid-liquid separation of the mixture, and a solid In the apparatus for purifying contaminated soil, comprising a separation means for separating the surfactant and the complex of the hardly decomposable organic substance from the liquid phase separated from the liquid,
The apparatus for purifying contaminated soil, wherein the surfactant is an amino acid type amphoteric surfactant, and the separation means includes means for mixing an acid with the liquid phase,
The contaminated soil purification apparatus, wherein the surfactant is a polyethylene glycol type nonionic surfactant, and the separation means has means for heating the liquid phase to a temperature higher than the cloud point . Or
Wherein a surfactant is an anionic surfactant, wherein the separating means is a purifying apparatus for contaminated soil, characterized in that it comprises means for adding an inorganic compound mainly containing calcium in the liquid phase.
This apparatus can embody the purification method of the present invention.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of a purification method and a purification device for contaminated soil and the like according to the present invention will be described with reference to the drawings.
[0010]
(Embodiment 1)
FIG. 1 shows an embodiment of a purification method for contaminated soil and the like according to the present invention. In the figure, 1 is a first mixing tank, 2 is a surfactant injection pipe, 3 is a centrifugal dehydrator, 4 is an acid injection pipe, 5 is a flocculant injection pipe, 6 is a second mixing tank, and 7 is a precipitation tank. is there.
[0011]
The soil containing the pollutant is mixed with the surfactant supplied from the surfactant injection pipe 2 in the first mixing tank 1, and the pollutant contained in the contaminated soil or the like moves to the liquid phase. Next, it is supplied to the centrifugal dehydrator 3 and separated into a liquid phase containing a conjugate of a surfactant and a contaminant and a solid phase from which the contaminant has been removed. The solid phase is taken out as a purified product. The liquid phase was mixed with the acid supplied from the acid injection pipe 4 and the coagulant supplied from the coagulant injection pipe 5 in the second mixing tank 6, and the surfactant / contaminant conjugate was insolubilized and aggregated. Thereafter, it is precipitated and separated as sludge in the settling tank 7. The sludge is finally incinerated in an incinerator and the pollutants are pyrolyzed.
[0012]
Here, pollutants are dioxins, environmental hormones, agricultural chemicals, persistent organic substances such as PCBs, inorganic substances such as fluorine, boron, and heavy metals, and bonds that adsorb these substances and soil particles. It is a body and the like and is not limited to a specific substance. In addition, the soil and the like refer to soil, landfill waste, river / lake / marsh or sea bottom mud, and sludge generated from the water treatment process and dehydrated cake thereof.
[0013]
Since the contact efficiency between the surfactant and the pollutant increases when the content of the pollutant such as contaminated soil is as high as possible, the concentration treatment is performed as necessary within the range where the mixing operation can be easily performed. It is preferable to carry out the mixing of the surfactant and the contaminated soil after increasing the organic matter content in the contaminated soil. Of course, when the mixing operation is difficult in the form of soil or the like as it is, it is possible to add water until the mixing operation can be easily performed.
[0014]
As the surfactant used in the present invention, various surfactants such as an anionic type, a cationic type, an amphoteric type and a nonionic type can be used. For example, as anion type, carboxylate such as soap, sulfate ester salt, sulfonate, etc., as cation type, amine salt, quaternary ammonium salt, etc., as amphoteric type, amino acid type, betaine type, etc. As the nonionic type, a polyethylene glycol type or the like can be used.
[0015]
The mixing / cleaning means for contaminated soil or the like and the surfactant is not limited to this embodiment, but a mixing tank with a stirrer is usually used. In addition, the combined use of ultrasonic irradiation means is preferable because it can increase the contact efficiency between the contaminated soil and the surfactant. By doing in this way, a pollutant can be transferred from solid content, such as soil, to a liquid phase.
[0016]
As solid-liquid separation means for contaminated soil and the like, various devices such as a screen, a sedimentation tank, and a filter press can be used in addition to a centrifugal dehydrator.
[0017]
The means for separating the combined body of the surfactant and the contaminant from the liquid phase can be selected from several types according to the characteristics of the surfactant to be applied. When the surfactant to be applied is an amino acid type amphoteric surfactant, it can be insolubilized by adding an acid after the washing operation and adjusting the pH to the isoelectric point as in this embodiment. In the case of a polyethylene glycol type nonionic surfactant, it can be insolubilized by heating to a temperature higher than the cloud point. In the case of an anionic surfactant, an insoluble salt can be formed by adding an inorganic compound mainly composed of calcium or the like. The insolubilized surfactant / contaminant conjugate can be separated by means of levitation or sedimentation depending on its specific gravity. In some cases, centrifugation can be applied.
[0018]
In addition, when it is difficult to separate only by insolubilization, it is possible to promote separation by adding and mixing flocculants to form floc. As the flocculant used in this case, iron salts such as ferric chloride and polyferric sulfate, aluminum salts such as sulphates and PACs, etc. can be applied. Molecular compounds can also be used in combination.
[0019]
On the other hand, in the case of using a foaming surfactant, a large number of bubbles are formed by aeration of the liquid phase or injection of pressurized water in which the gas is supersaturated in the liquid phase, and the interface is formed on the surface of the bubbles. The active agent / contaminant conjugate can be concentrated and removed as scum.
[0020]
The liquid phase from which the combination of the surfactant and the contaminant is separated can be used again for the purification treatment. For example, it is possible to add a surfactant to bring it into contact with contaminated soil or the like, or to rinse the surfactant remaining in the soil after washing.
[0021]
Since the combination of the surfactant and the pollutant separated from the liquid phase is concentrated as compared with the contaminated soil before the treatment, the amount is significantly reduced. Therefore, it can be made harmless at low cost by using various means such as oxidative decomposition by ozone injection and dechlorination by ultraviolet irradiation, but it can be almost completely decomposed in a short time by a heating method. In particular, when an existing incinerator, melting furnace or pyrolysis furnace exists in the vicinity of the soil purification facility, the combined surfactant / pollutant separated from the liquid phase is treated with the heating system facility. This is preferable because the construction cost of the equipment can be reduced.
[0022]
(Embodiment 2)
FIG. 2 shows another embodiment of the purification method for contaminated soil and the like according to the present invention. In the figure, 1 is a first mixing tank, 2 is a surfactant injection pipe, 3 is a centrifugal dehydrator, 4 is an acid injection pipe, 5 is a flocculant injection pipe, 8 is a pH adjustment tank, 9 is a neutralization tank, 10 is an alkali injection pipe, 11 is a treated water circulation pipe, 12 is a third mixing tank, 13 is a floating separation tank, and 14 is a pressurized water injection pipe.
[0023]
The contaminated soil and the like are mixed with the acid supplied from the acid injection pipe 4 in the pH adjusting tank 8, the treated water supplied from the treated water circulation pipe 11 and the make-up water, and dissolve calcium compounds contained in the contaminated soil and the like. Next, the neutralization tank 9 is mixed with the alkali supplied from the alkali injection pipe 10 to adjust the pH to neutral. Subsequently, after being mixed with the surfactant supplied from the surfactant injection tube 2 in the first mixing tank 1, the liquid phase containing the combination of the surfactant and the contaminant and the contaminant are removed in the centrifugal dehydrator 3. The solid phase is separated. The liquid phase is mixed with the coagulant supplied from the coagulant injection pipe 5 and the pressurized water in which the air supplied from the pressurized water injection pipe 14 is supersaturated in the flotation separation tank 13, and the combined surfactant and contaminants are After being concentrated on the bubble surface, it is floated and separated as scum, and the remainder becomes treated water. On the other hand, the solid phase taken out by the centrifugal dehydrator is once mixed with the treated water in the third mixing tank 12, and then solid-liquid separated again by the centrifugal dehydrator 3, thereby binding the remaining surfactant and contaminants. After the body is washed out, it is taken out as a purified product.
[0024]
If the contaminated soil has a high content of metal components such as lime, iron, manganese, etc., and these impede contact between the contaminants and the surfactant and high cleaning efficiency cannot be obtained, the contamination will occur as in this embodiment. When the acid is mixed before or during the mixing of the soil and the surfactant with the surfactant to dissolve the lime component and the metal component, the contact efficiency is improved and a good cleaning effect is obtained. On the other hand, if the contaminated soil has a high content of organic substances such as humic acid and the contact between the target pollutant and the surfactant cannot be achieved and high cleaning efficiency cannot be obtained, before mixing the contaminated soil and the surfactant Alternatively, when an alkali is mixed during mixing to dissolve organic substances such as humic acid, the contact efficiency is improved and a good cleaning effect is obtained.
[0025]
In addition, by using the treated water obtained as in the present embodiment for rinsing the solid content after centrifugal dehydration, dissolving the surfactant, and adjusting the water content of the purification target, the total amount of water used can be reduced, and the purification cost The effect of reducing the amount of wastewater and the amount of drainage can be obtained.
[0026]
【Example】
Table 1 shows the results of treatment of soil contaminated with dioxins by the treatment method shown in FIG. However, the processing conditions are as follows.
[0027]
[Example processing method]
・ Surfactant type: Nonionic surfactant (alcohol)
・ Reaction time with surfactant: 30 minutes ・ Reaction temperature: room temperature ・ Surfactant injection rate: 0.5 wt%
[Table 1]
Figure 0003918657
[0028]
[0029]
【The invention's effect】
The treatment method according to the present invention stirs and mixes the contaminated soil and the surfactant to efficiently remove the pollutants contained in the contaminated soil and the like. There exists an effect of isolate | separating a conjugate | bonded_body from an aqueous phase efficiently.
[Brief description of the drawings]
FIG. 1 is a diagram showing an embodiment of a purification method for contaminated soil and the like according to the present invention.
FIG. 2 is a view showing another embodiment of the purification method for contaminated soil and the like according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... 1st mixing tank, 2 ... Surfactant injection pipe, 3 ... Centrifugal dehydrator, 4 ... Acid injection pipe, 5 ... Flocculant injection pipe, 6 ... Second mixing tank, 7 ... Precipitation tank, 8 ... pH adjustment A tank, 9 ... neutralization tank, 10 ... alkali injection pipe, 11 ... treated water circulation pipe, 12 ... third mixing tank, 13 ... flotation separation tank, 14 ... pressurized water injection pipe.

Claims (8)

難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄することによって、該難分解性有機物質を土壌の固形分から液相に移行させる工程と、この工程の後に、該混合物を固液分離し、固相を浄化物として取り出す工程と、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程とを備えた汚染土壌の浄化方法において、
前記界面活性剤がアミノ酸型両性界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相に酸を混合する工程であることを特徴とする汚染土壌の浄化方法。
Mixing and washing the soil contaminated with the persistent organic substance and the surfactant to transfer the persistent organic substance from the solid content of the soil to the liquid phase, and after this process, In a method for purifying contaminated soil, comprising a step of solid-liquid separation and taking out a solid phase as a purified product, and a step of separating a combined body of a surfactant and the hardly decomposable organic substance from the liquid phase subjected to solid-liquid separation. ,
The surfactant is an amino acid type amphoteric surfactant, and the step of separating the conjugate of the surfactant and the hardly decomposable organic substance from the solid-liquid separated liquid phase is a step of mixing an acid with the liquid phase. A method for purifying contaminated soil, characterized in that there is.
難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄することによって、該難分解性有機物質を土壌の固形分から液相に移行させる工程と、この工程の後に、該混合物を固液分離し、固相を浄化物として取り出す工程と、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程とを備えた汚染土壌の浄化方法において、
前記界面活性剤がポリエチレングリコール型非イオン界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相を加温して曇点より高い温度にする工程であることを特徴とする汚染土壌の浄化方法。
Mixing and washing the soil contaminated with the persistent organic substance and the surfactant to transfer the persistent organic substance from the solid content of the soil to the liquid phase, and after this process, In a method for purifying contaminated soil, comprising a step of solid-liquid separation and taking out a solid phase as a purified product, and a step of separating a combined body of a surfactant and the hardly decomposable organic substance from the liquid phase subjected to solid-liquid separation. ,
The surfactant is a polyethylene glycol type nonionic surfactant, and the step of separating the binder of the surfactant and the hardly decomposable organic substance from the solid-liquid separated liquid phase is performed by heating the liquid phase. A method for purifying contaminated soil, characterized by being a step of raising the temperature above the cloud point .
難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄することによって、該難分解性有機物質を土壌の固形分から液相に移行させる工程と、この工程の後に、該混合物を固液分離し、固相を浄化物として取り出す工程と、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程とを備えた汚染土壌の浄化方法において、
前記界面活性剤がアニオン型界面活性剤であり、固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する工程は、液相にカルシウムを主成分とする無機化合物を添加する工程であることを特徴とする汚染土壌の浄化方法。
Mixing and washing the soil contaminated with the persistent organic substance and the surfactant to transfer the persistent organic substance from the solid content of the soil to the liquid phase, and after this process, In a method for purifying contaminated soil, comprising a step of solid-liquid separation and taking out a solid phase as a purified product, and a step of separating a combined body of a surfactant and the hardly decomposable organic substance from the liquid phase subjected to solid-liquid separation. ,
It said surfactant is an anionic surfactant, separating the conjugate of surfactants and flame decomposable organic matter from the solid-liquid separated liquid phase, composed mainly of calcium in the liquid phase A method for purifying contaminated soil, comprising adding an inorganic compound.
界面活性剤と難分解性有機物質の結合体を分離された液相を難分解性有機物質で汚染された土壌の洗浄に再度利用することを特徴とする請求項1乃至3の何れかに記載の処理方法。4. The liquid phase obtained by separating a conjugate of a surfactant and a hardly decomposable organic substance is reused for washing soil contaminated with the hardly decomposable organic substance. Processing method. 液相から分離された界面活性剤と難分解性有機物質の結合体を焼却炉、溶融炉または熱分解炉に投入して難分解性有機物質を加熱分解することを特徴とする請求項1乃至4の何れかに記載の処理方法。  A combination of a surfactant and a hardly decomposable organic substance separated from a liquid phase is put into an incinerator, a melting furnace or a pyrolysis furnace to thermally decompose the hardly decomposable organic substance. 5. The processing method according to any one of 4. 難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄する混合手段、該混合物を固液分離する固液分離手段、及び固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する分離手段とを備えた汚染土壌の浄化装置において、
前記界面活性剤がアミノ酸型両性界面活性剤であり、前記分離手段が、前記液相に酸を混合する手段を有することを特徴とする汚染土壌の浄化装置。
Mixing means for mixing and washing the soil contaminated with the hardly decomposable organic substance and the surfactant, solid-liquid separation means for separating the mixture into solid and liquid, and the surfactant and the difficulty from the solid-liquid separated liquid phase In a purification apparatus for contaminated soil, comprising a separating means for separating a combined body of degradable organic substances,
The apparatus for purifying contaminated soil, wherein the surfactant is an amino acid type amphoteric surfactant, and the separation means has means for mixing an acid with the liquid phase.
難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄する混合手段、該混合物を固液分離する固液分離手段、及び固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する分離手段とを備えた汚染土壌の浄化装置において、
前記界面活性剤がポリエチレングリコール型非イオン界面活性剤であり、前記分離手段が、前記液相を加温して曇点より高い温度にする手段を有することを特徴とする汚染土壌の浄化装置。
Mixing means for mixing and washing the soil contaminated with the hardly decomposable organic substance and the surfactant, solid-liquid separation means for separating the mixture into solid and liquid, and the surfactant and the difficulty from the solid-liquid separated liquid phase In a purification apparatus for contaminated soil, comprising a separating means for separating a combined body of degradable organic substances,
The apparatus for purifying contaminated soil, wherein the surfactant is a polyethylene glycol type nonionic surfactant, and the separation means has means for heating the liquid phase to a temperature higher than the cloud point .
難分解性有機物質で汚染された土壌と界面活性剤とを混合・洗浄する混合手段、該混合物を固液分離する固液分離手段、及び固液分離された液相から界面活性剤と該難分解性有機物質の結合体を分離する分離手段とを備えた汚染土壌の浄化装置において、
前記界面活性剤がアニオン型界面活性剤であり、前記分離手段が、前記液相にカルシウムを主成分とする無機化合物を添加する手段を有することを特徴とする汚染土壌の浄化装置。
Mixing means for mixing and washing the soil contaminated with the hardly decomposable organic substance and the surfactant, solid-liquid separation means for separating the mixture into solid and liquid, and the surfactant and the difficulty from the solid-liquid separated liquid phase In a purification apparatus for contaminated soil, comprising a separating means for separating a combined body of degradable organic substances,
Wherein a surfactant is an anionic surfactant, wherein the separating means, purifier of contaminated soil, characterized in that it comprises means for adding an inorganic compound mainly containing calcium in the liquid phase.
JP2002190523A 2002-06-28 2002-06-28 Method and apparatus for purifying contaminated soil Expired - Fee Related JP3918657B2 (en)

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