JP2001334290A - Method for cleaning sludge soil, slurry or the like - Google Patents

Method for cleaning sludge soil, slurry or the like

Info

Publication number
JP2001334290A
JP2001334290A JP2000159279A JP2000159279A JP2001334290A JP 2001334290 A JP2001334290 A JP 2001334290A JP 2000159279 A JP2000159279 A JP 2000159279A JP 2000159279 A JP2000159279 A JP 2000159279A JP 2001334290 A JP2001334290 A JP 2001334290A
Authority
JP
Japan
Prior art keywords
hydrophobic organic
tank
spherical resin
solid phase
organic substance
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2000159279A
Other languages
Japanese (ja)
Other versions
JP3703366B2 (en
Inventor
Tomohiko Sasaki
智彦 佐々木
Yasuo Horii
安雄 堀井
Koichi Nakagawa
浩一 中河
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.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP2000159279A priority Critical patent/JP3703366B2/en
Publication of JP2001334290A publication Critical patent/JP2001334290A/en
Application granted granted Critical
Publication of JP3703366B2 publication Critical patent/JP3703366B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Physical Water Treatments (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for cleaning sludge soil, a slurry or the like, capable of desorbing hydrophobic organic matter from a solid phase at the normal temperature under atomospheric pressure by reduced energy. SOLUTION: A surfactant and a spherical resin (a) are added to the substance 2 to be treated stored in a reaction tank 1 and the spherical resin (a) floating in the vicinity of the surface of the water in the tank is circulated to the bottom part of the tank through a circulating system 6 and the substance 2 to be treated is irradiated with ultrasonic waves exerting vibrtation and extraction action on the solid phase from an ultrasonic transmitter 9 while the spherical resin (a) is circulated within the tank and hydrophobic organic matter is transferred from the solid phase to a liquid phase by the vibrtation and extraction action to be desorbed from the solid phase and the re-adsorption of the hydrophobic organic matter by the solid phase is prevented by the bonding of the surfactant with the hydrophobic organic matter and the desorbed hydrophobic organic matter is adsorbed by the spherical resin (a).

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、汚染土壌、スラリ
ー等の浄化方法に関し、一般廃棄物や産業廃棄物等の最
終処分場における浸出水、汚染土壌、スラリー等に含ま
れた有害疎水性有機物を脱着する技術に係るものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying contaminated soil, slurry, etc., and relates to a harmful hydrophobic organic substance contained in leachate, contaminated soil, slurry, etc. at a final disposal site for general waste and industrial waste. The present invention relates to a technology for attaching and detaching.

【0002】[0002]

【従来の技術】従来、土壌やスラリー中に含まれる疎水
性有害有機物、例えばダイオキシン類、PCB類、芳香
族炭化水素類などは、固相粒子に非常に強く吸着されて
おり、一般的に処理が非常に困難である。bioremediati
on等の微生物によって有機物を消化する生物学的処理方
式では、水相に含まれる有機物しか処理できない場合が
多い。また、揮発性の高い物質に関しては、熱脱着によ
り固相からの分離も可能であるが、沸点の高い物質には
対応できず、焼却等非常に処理コストの高い方式で対応
せざるを得なかった。
2. Description of the Related Art Conventionally, hydrophobic harmful organic substances, such as dioxins, PCBs, and aromatic hydrocarbons, contained in soil and slurry have been very strongly adsorbed on solid particles, and are generally treated. Is very difficult. bioremediati
In a biological treatment method in which organic substances are digested by microorganisms such as on, in many cases, only organic substances contained in an aqueous phase can be treated. In addition, for highly volatile substances, it is possible to separate them from the solid phase by thermal desorption, but it is not possible to deal with substances with a high boiling point, and it is necessary to deal with very high processing costs such as incineration. Was.

【0003】例えば、固形物中のダイオキシン類を、1
200度以上の高温度条件下において溶融する溶融処理
法や、370度以上、22MPa以上の高温度、高圧力
条件下において処理する超臨界処理法がある。あるい
は、処理対象物に水素供与体、アルカリ、溶媒を添加し
た後に、窒素雰囲気下で、350度程度に加熱処理する
アルカリ触媒分解法がある。
For example, dioxins in a solid substance are
There are a melting treatment method in which the melting is performed under a high temperature condition of 200 degrees or more, and a supercritical treatment method in which the treatment is performed under a high temperature and high pressure condition of 370 degrees or more and 22 MPa or more. Alternatively, there is an alkali-catalyzed decomposition method in which a hydrogen donor, an alkali, and a solvent are added to an object to be treated, and then heat treatment is performed at about 350 ° C. in a nitrogen atmosphere.

【0004】[0004]

【発明が解決しようとする課題】しかし、疎水性有機物
に汚染された土壌は、汚染物質が固相に強く吸着してい
るために浄化が困難であり、bioremediationなどの処理
を行なっても土壌中の汚染物濃度が変化しなくなるなど
限界があった。さらに、浄化を行なうためには上述した
土壌の焼却等の処理コストが高い方式しかなく、現実的
でなかった。
However, soil contaminated with hydrophobic organic matter is difficult to purify because the contaminants are strongly adsorbed on the solid phase, and even if bioremediation or other treatments are performed, the soil is not contaminated. There was a limit such that the contaminant concentration in the sample no longer changed. Further, there is only a method that requires a high treatment cost such as the above-described incineration of soil to perform purification, which is not practical.

【0005】本発明は上記した課題を解決するものであ
り、疎水性有機物を、常温、常圧の下で少ないエネルギ
ーによって固相から脱着することができる汚染土壌、ス
ラリー等の浄化方法を提供することを目的とする。
The present invention solves the above-mentioned problems, and provides a method for purifying contaminated soil, slurry, and the like which can desorb a hydrophobic organic substance from a solid phase under normal temperature and normal pressure with little energy. The purpose is to:

【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
に、本発明の汚染土壌、スラリー等の浄化方法は、反応
槽に貯留した固液混相の処理対象物に、疎水性有機物に
対する吸着能を有する球状樹脂を添加し、槽内の水面付
近に浮遊する球状樹脂を槽底部へ巡廻させて槽内で球状
樹脂を循環しながら、槽内に配置した超音波発信体から
処理対象物へ固相に振動抽出作用を及ぼす超音波を照射
し、振動抽出作用によって疎水性有機物を固相から液相
に移行させて脱着し、界面活性剤と疎水性有機物との結
合によって固相に対する疎水性有機物の再吸着を防止す
るとともに、脱着した疎水性有機物を球状樹脂に吸着す
るものである。
In order to solve the above-mentioned problems, a method for purifying contaminated soil and slurry according to the present invention is characterized in that a solid-liquid mixed phase object to be treated stored in a reaction tank has an adsorption capacity for hydrophobic organic substances. Is added, and the spherical resin floating near the water surface in the tank is circulated to the bottom of the tank to circulate the spherical resin in the tank, and from the ultrasonic transmitter disposed in the tank to the object to be treated. The solid phase is irradiated with ultrasonic waves that exerts vibration extraction action, the hydrophobic organic substance is transferred from the solid phase to the liquid phase by the vibration extraction action and desorbed, and the hydrophobic property to the solid phase is bonded by the combination of the surfactant and the hydrophobic organic substance. This prevents the re-adsorption of organic substances and adsorbs the desorbed hydrophobic organic substances to the spherical resin.

【0007】上記した構成により、処理対象物に含まれ
たダイオキシン類等の疎水性有機物は、固相の土壌粒子
表層に吸着し、あるいは途上粒子微細間隙内孔に付着
し、あるいは土壌粒子中に含まれる有機物と複雑に絡み
あって存在する。
[0007] With the above structure, hydrophobic organic substances such as dioxins contained in the object to be treated are adsorbed on the surface layer of the solid phase soil particles, adhere to the pores in the fine gaps of the developing particles, or are contained in the soil particles. It exists in a complex entanglement with the organic matter contained.

【0008】土壌粒子表層に吸着した疎水性有機物は液
相と接していれば平衡状態を保つように土壌から脱着す
る。このため、液相の疎水性有機物を球状樹脂によって
吸着し、液相の疎水性有機物濃度を減じることにより、
平衡を保つように土壌から疎水性有機物が脱着し、土壌
中の汚染物濃度が低下して処理対象物の浄化が進行す
る。球状樹脂は槽内を流動することにより、疎水性有機
物との接触頻度が高まり、吸着効率が向上する。
The hydrophobic organic matter adsorbed on the surface layer of the soil particles is desorbed from the soil so as to maintain an equilibrium state when in contact with the liquid phase. Therefore, the hydrophobic organic substance in the liquid phase is adsorbed by the spherical resin and the concentration of the hydrophobic organic substance in the liquid phase is reduced,
Hydrophobic organic substances are desorbed from the soil so as to maintain the equilibrium, the concentration of contaminants in the soil is reduced, and purification of the object to be treated proceeds. By flowing the spherical resin in the tank, the frequency of contact with the hydrophobic organic substance is increased, and the adsorption efficiency is improved.

【0009】しかし、途上粒子微細間隙内孔に付着し、
あるいは土壌粒子中に含まれる有機物と複雑に絡みあっ
て存在する疎水性有機物は、非常に強く土壌粒子に吸着
されており、液相中へ殆ど移行しない形態となって存在
している。
[0009] However, the particles adhere to the pores of the fine particles in the process,
Alternatively, the hydrophobic organic matter present in a complex entanglement with the organic matter contained in the soil particles is very strongly adsorbed to the soil particles and exists in a form that hardly migrates into the liquid phase.

【0010】このため、処理対象物の固相に作用する超
音波を照射し、その振動エネルギーによって疎水性有機
物を液相ヘ移行しやすい形態に変化させて固相から液相
に移行させる。この振動抽出作用によって抽出した疎水
性有機物は再び固相に再吸着し易いが、界面活性剤が疎
水性有機物と結合することによって、固相に対する疎水
性有機物の再吸着を防止し、疎水性有機物を液相に留め
る。この液相の疎水性有機物を球状樹脂によって吸着
し、液相の疎水性有機物濃度を減じ、土壌から疎水性有
機物が脱着することを促進し、処理対象物の浄化を行な
う。
[0010] For this purpose, an ultrasonic wave is applied to the solid phase of the object to be treated, and the vibrational energy is used to change the hydrophobic organic substance into a form that can easily move to the liquid phase, thereby causing the hydrophobic organic substance to move from the solid phase to the liquid phase. The hydrophobic organic substance extracted by the vibration extraction action is easily re-adsorbed to the solid phase again, but the surfactant is bonded to the hydrophobic organic substance, thereby preventing the hydrophobic organic substance from being re-adsorbed to the solid phase, and In the liquid phase. The hydrophobic organic substance in the liquid phase is adsorbed by the spherical resin, the concentration of the hydrophobic organic substance in the liquid phase is reduced, the desorption of the hydrophobic organic substance from the soil is promoted, and the object to be treated is purified.

【0011】スラリーの浄化が終了したら、球状粒子は
オーバーフロー水と共に槽外へ取り出す。球状樹脂は水
に浮くので容易に回収できる。回収効率を上げるため反
応槽内に水を入れてもよい。取り出した球状樹脂はトル
エン等の溶剤で洗浄して再生し再利用する。溶剤中に溶
け込んだ疎水性有機物は別途処理をする。処理済みのス
ラリーは底部より引き抜いて脱水等の処理を施す。
After the purification of the slurry is completed, the spherical particles are taken out of the tank together with the overflow water. Since the spherical resin floats on water, it can be easily collected. Water may be introduced into the reaction tank to increase the recovery efficiency. The removed spherical resin is washed with a solvent such as toluene, regenerated and reused. The hydrophobic organic substance dissolved in the solvent is separately treated. The treated slurry is pulled out from the bottom and subjected to a treatment such as dehydration.

【0012】振動抽出作用を及ぼす超音波は、処理対象
物の物性、例えば疎水性有機物の種類や組成、汚泥や土
壌の性状によって異なり、あるいは反応槽の形状によっ
て異なるので、経験則として予め求める。
The ultrasonic wave exerting the vibration extracting action depends on the physical properties of the object to be treated, for example, the type and composition of the hydrophobic organic substance, the properties of sludge and soil, or the shape of the reaction tank, and is determined in advance as an empirical rule.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施形態を図面に
基づいて説明する。図1において、反応槽1に貯留する
処理対象物2は、産業廃棄物等の最終処分場における埋
立地浸出水、汚染土壌、スラリー等であり、ダイオキシ
ン類、PCB類、芳香族炭化水素等の疎水性有機物を含
んでいる。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, an object 2 to be treated stored in a reaction tank 1 is leachate from a landfill at a final disposal site for industrial waste, contaminated soil, slurry, and the like, such as dioxins, PCBs, and aromatic hydrocarbons. Contains hydrophobic organics.

【0014】反応槽1には、固液混相の処理対象物2を
供給する供給系3と、界面活性剤を投入する薬剤供給系
4と、疎水性有機物に対する吸着能を有する球状樹脂
(XAD2)aを投入する吸着剤供給系5とを接続して
おり、槽上部と槽底部を連通して循環系6を設け、循環
系6から分岐して処理スラリーを取り出す排出系7を設
けており、循環系6の上部にオーバーフロー用のバルブ
8を設けている。球状樹脂(XAD2)は、巨大網状構
造をもった合成吸着剤であって、硬くて、かつ不溶性で
あって多孔性ポリマーの球状樹脂である。その物性を表
1に示す。
A reaction tank 1 has a supply system 3 for supplying a solid-liquid mixed-phase object 2 to be treated, a drug supply system 4 for supplying a surfactant, and a spherical resin (XAD2) having an adsorbing ability for hydrophobic organic substances. a circulating system 6 is connected to the tank top and the tank bottom, and a discharge system 7 is provided for branching out of the circulating system 6 to take out the processing slurry. An overflow valve 8 is provided above the circulation system 6. The spherical resin (XAD2) is a synthetic adsorbent having a huge network structure, and is a hard, insoluble, porous polymer spherical resin. The physical properties are shown in Table 1.

【0015】[0015]

【表1】 反応槽1の内部には、超音波発信体9(ホーン)を設け
ており、超音波発信体9は導波管10を通して超音波発
振器11に接続している。超音波発振器11は処理対象
物2の固相に振動抽出作用を及ぼす超音波振動を発振す
るものである。超音波発信体9は電圧を受けて発振する
セラミック等の振動子を使用することもできる。
[Table 1] An ultrasonic transmitter 9 (horn) is provided inside the reaction tank 1, and the ultrasonic transmitter 9 is connected to an ultrasonic oscillator 11 through a waveguide 10. The ultrasonic oscillator 11 oscillates ultrasonic vibration which exerts a vibration extracting action on the solid phase of the processing object 2. The ultrasonic transmitter 9 may use a vibrator made of ceramic or the like that oscillates upon receiving a voltage.

【0016】超音波発信体9から発信する超音波、つま
り振動抽出作用を及ぼす超音波の周波数は、処理対象物
2の物性、例えば疎水性有機物の種類や組成、汚泥や土
壌の性状によって異なり、あるいは反応槽1の形状によ
って異なるので、経験則として予め求める。
The frequency of the ultrasonic wave transmitted from the ultrasonic transmitter 9, that is, the frequency of the ultrasonic wave exerting the vibration extracting action, varies depending on the physical properties of the object 2 to be treated, for example, the type and composition of the hydrophobic organic substance, and the properties of the sludge and the soil. Alternatively, since it depends on the shape of the reaction tank 1, it is determined in advance as an empirical rule.

【0017】以下、上記した構成における作用を説明す
る。供給系3から反応槽1へ処理対象物2を供給し、所
定量の処理対象物2を反応槽1に貯留する。薬剤供給系
4から所定量の界面活性剤、例えばLAS(アルキルベ
ンゼンスルフォン酸ナトリウム)を、CMC濃度(臨界
ミセル濃度)以上に保たれるように添加し、吸着剤供給
系5から適当量の球状樹脂aを投入する。循環系6を通
して槽内の水面付近に浮遊する球状樹脂aを処理対象物
2とともに槽底部に巡廻し、処理対象物2およぼ球状樹
脂aを槽内で循環流動させる。
The operation of the above configuration will be described below. The processing object 2 is supplied from the supply system 3 to the reaction tank 1, and a predetermined amount of the processing object 2 is stored in the reaction tank 1. A predetermined amount of a surfactant, for example, LAS (sodium alkylbenzene sulfonate) is added from the drug supply system 4 so as to maintain the CMC concentration (critical micelle concentration) or higher, and an appropriate amount of spherical resin is added from the adsorbent supply system 5. Input a. The spherical resin a floating near the water surface in the tank is circulated together with the processing object 2 to the bottom of the tank through the circulation system 6, and the processing object 2 and the spherical resin a are circulated and flow in the tank.

【0018】処理対象物2に含まれたダイオキシン類等
の疎水性有機物は、固相の土壌粒子表層に吸着し、ある
いは途上粒子微細間隙内孔に付着し、あるいは土壌粒子
中に含まれる有機物と複雑に絡みあって存在する。
Hydrophobic organic substances such as dioxins contained in the processing object 2 are adsorbed on the surface layer of the solid phase soil particles, adhere to the pores in the fine gaps of the developing particles, or are separated from the organic substances contained in the soil particles. It exists in a complex entanglement.

【0019】土壌粒子表層に吸着した疎水性有機物は液
相と接していれば平衡状態を保つように土壌から脱着す
る。このため、液相の疎水性有機物を球状樹脂aによっ
て吸着し、液相の疎水性有機物濃度を減じることによ
り、平衡を保つように土壌から疎水性有機物が脱着し、
土壌中の汚染物濃度が低下して処理対象物2の浄化が進
行する。このとき、球状樹脂aが槽内を流動することに
より、疎水性有機物との接触頻度が高まり、吸着効率が
向上する。
The hydrophobic organic matter adsorbed on the surface layer of the soil particles is desorbed from the soil so as to maintain an equilibrium state when in contact with the liquid phase. For this reason, the hydrophobic organic substance in the liquid phase is adsorbed by the spherical resin a, and the hydrophobic organic substance is desorbed from the soil so as to maintain an equilibrium by reducing the concentration of the hydrophobic organic substance in the liquid phase,
The concentration of the contaminants in the soil decreases, and the purification of the treatment target 2 proceeds. At this time, since the spherical resin a flows in the tank, the frequency of contact with the hydrophobic organic substance increases, and the adsorption efficiency improves.

【0020】しかし、途上粒子微細間隙内孔に付着し、
あるいは土壌粒子中に含まれる有機物と複雑に絡みあっ
て存在する疎水性有機物は、液相に接するだけでは、そ
の低い溶解度のために脱着することが困難である。
However, the particles adhere to the pores of the fine particles on the way,
Alternatively, it is difficult to desorb a hydrophobic organic substance existing in a complex entanglement with an organic substance contained in soil particles due to its low solubility only by contacting with a liquid phase.

【0021】このため、超音波発振器11で発振する超
音波を導波管10を通して超音波発信体9から処理対象
物2へ照射し、その振動エネルギーによって疎水性有機
物を固相から液相に移行させる。この振動抽出作用によ
って抽出した疎水性有機物は再び固相に再吸着し易い
が、界面活性剤が疎水性有機物と結合することによっ
て、固相に対する疎水性有機物の再吸着を防止し、疎水
性有機物を液相に留める。一方、液相に移行した疎水性
有機物を球状樹脂aによって吸着し、液相の疎水性有機
物濃度を減じ、土壌から疎水性有機物が脱着することを
促進し、処理対象物2の浄化を行なう。
For this reason, the ultrasonic wave oscillated by the ultrasonic oscillator 11 is irradiated through the waveguide 10 from the ultrasonic wave transmitter 9 onto the object 2 to be processed, and the vibration energy transfers the hydrophobic organic substance from the solid phase to the liquid phase. Let it. The hydrophobic organic substance extracted by the vibration extraction action is easily re-adsorbed to the solid phase again, but the surfactant is bonded to the hydrophobic organic substance, thereby preventing the hydrophobic organic substance from being re-adsorbed to the solid phase, and In the liquid phase. On the other hand, the hydrophobic organic substance transferred to the liquid phase is adsorbed by the spherical resin a, the concentration of the hydrophobic organic substance in the liquid phase is reduced, the desorption of the hydrophobic organic substance from the soil is promoted, and the treatment object 2 is purified.

【0022】球状樹脂aはバルブ8を開栓してオーバー
フロー水と共に槽外へ取り出す。球状樹脂は水に浮くの
で、容易に回収できる。回収効率を上げるため反応槽内
に水を入れてもよい。取り出した球状樹脂はトルエン等
の溶剤で疎水性有機物を抽出・洗浄し、再利用する。
The spherical resin a is taken out of the tank together with overflow water by opening the valve 8. Since the spherical resin floats on water, it can be easily collected. Water may be introduced into the reaction tank to increase the recovery efficiency. The extracted spherical resin is used for extracting and washing hydrophobic organic substances with a solvent such as toluene, and then reusing it.

【0023】以下に、上述した構成の実証試験について
説明する。図2は水相と土壌の2相モデルの概念図であ
る。土壌に吸着している汚染物には比較的に弱い力で土
壌に吸着して早く水相へ移行するものと、強力に吸着し
て殆ど水中へ移行しないものとがある。弱い吸着物の割
合をFで示し、強い吸着物の割合を1−Fで示してお
り、Fが大きい程に土壌浄化は容易となる。
Hereinafter, a verification test of the above configuration will be described. FIG. 2 is a conceptual diagram of a two-phase model of an aqueous phase and a soil. The contaminants adsorbed on the soil include those that are adsorbed on the soil with relatively weak force and move to the aqueous phase quickly, and those that are strongly adsorbed and hardly move into water. The ratio of the weak adsorbate is indicated by F, and the ratio of the strong adsorbate is indicated by 1-F. The larger the F, the easier the soil purification.

【0024】[0024]

【数1】 この2相モデル方程式は、土壌中の初期汚染物量S0
x時間後にどの程度(Sx)になるかを示したモデル式
である。図3は上記のモデル方程式のグラフ図であり、
弱い吸着物の割合Fが大きい程に汚染物がたくさん落ち
るので最終的な(Sx)は小さくなり、早い脱着の定数
k1が大きい程に汚染物が早く落ちるのでカーブの傾き
は急になる。
(Equation 1) This two-phase model equation is a model equation that indicates how much (Sx) the initial contaminant amount S 0 in the soil will be after x hours. FIG. 3 is a graph of the above model equation.
The larger the ratio F of the weak adsorbate, the more contaminants fall, so that the final (Sx) becomes smaller, and the larger the constant k1 of fast desorption, the faster the contaminants fall, so that the slope of the curve becomes steeper.

【0025】図4は、ある汚染土壌を水中で反転攪拌し
て汚染物を洗い流した2相モデルの結果を示すものであ
り、ナフタリンは68%、フェナントレンは46%、ピ
レンは42%が早く水中へ移行している。
FIG. 4 shows the results of a two-phase model in which a contaminated soil was inverted and stirred in water to wash away contaminants. Naphthalene was 68%, phenanthrene was 46%, and pyrene was 42%, and water was earlier. Has transitioned to

【0026】図5は、同じ汚染土壌を界面活性剤の存在
下で超音波処理した後に反転攪拌した2相モデルの結果
を示すものであり、ナフタリンは93%、フェナントレ
ンは94%、ピレンは90%が早く水中へ移行してお
り、浄化効率が確実に上がっていることを示している。
FIG. 5 shows the results of a two-phase model in which the same contaminated soil was subjected to ultrasonic treatment in the presence of a surfactant and then inverted and stirred. Naphthalene was 93%, phenanthrene was 94%, and pyrene was 90%. % Migrated into the water early, indicating that the purification efficiency has definitely increased.

【0027】図6は、図5に示した処理を行なった後の
弱い吸着物の割合Fを示しており、他の物質に関して
も、界面活性剤の存在下で超音波処理することが有効で
あることが伺える。
FIG. 6 shows the ratio F of the weakly adsorbed substance after the treatment shown in FIG. 5, and it is effective to carry out ultrasonic treatment in the presence of a surfactant for other substances. I can tell you something.

【0028】[0028]

【発明の効果】以上述べたように本発明によれば、処理
対象物に球状樹脂と界面活性剤を添加して超音波を照射
することにより、処理対象物から疎水性有機物を脱着す
るとともに、脱着した疎水性有機物を界面活性剤で液相
に留めながら球状樹脂で吸着して、処理対象物から疎水
性有機物を分離して浄化することができる。したがっ
て、ダイオキシン類、農薬等の疎水性有機物を、常温、
常圧の下で少ないエネルギーによって固相から脱着し、
汚染土壌、スラリー等の浄化を行なえる。
As described above, according to the present invention, a hydrophobic organic substance is desorbed from a processing object by adding a spherical resin and a surfactant to the processing object and irradiating with ultrasonic waves. The desorbed hydrophobic organic substance is adsorbed by the spherical resin while remaining in a liquid phase with a surfactant, and the hydrophobic organic substance can be separated from the object to be treated and purified. Therefore, hydrophobic organic substances such as dioxins, pesticides, etc.
Desorbs from the solid phase with little energy under normal pressure,
It can purify contaminated soil and slurry.

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

【図1】本発明の実施形態における浄化装置の模式図で
ある。
FIG. 1 is a schematic diagram of a purification device according to an embodiment of the present invention.

【図2】水相と土壌の2相モデルの概念図である。FIG. 2 is a conceptual diagram of a two-phase model of an aqueous phase and a soil.

【図3】モデル方程式のグラフ図である。FIG. 3 is a graph of a model equation.

【図4】ある汚染土壌を水中で反転攪拌した2相モデル
の結果を示すグラフ図である。
FIG. 4 is a graph showing the result of a two-phase model in which a certain contaminated soil is inverted and stirred in water.

【図5】同汚染土壌を界面活性剤の存在下で反転攪拌す
るとともに超音波処理した2相モデルの結果を示すグラ
フ図である。
FIG. 5 is a graph showing the results of a two-phase model obtained by subjecting the contaminated soil to reverse stirring and ultrasonic treatment in the presence of a surfactant.

【図6】図5に示した処理を行なった後の弱い吸着物の
割合Fを示すグラフ図である。
6 is a graph showing a ratio F of a weak adsorbate after performing the processing shown in FIG. 5;

【符号の説明】[Explanation of symbols]

1 反応槽 2 処理対象物 3 供給系 4 薬剤供給系 5 吸着剤供給系 6 循環系 7 排出系 8 バルブ 9 超音波発信体 10 導波管 11 超音波発振器 a 球状樹脂 DESCRIPTION OF SYMBOLS 1 Reaction tank 2 Processing object 3 Supply system 4 Drug supply system 5 Adsorbent supply system 6 Circulation system 7 Discharge system 8 Valve 9 Ultrasonic wave transmitter 10 Waveguide 11 Ultrasonic oscillator a Spherical resin

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中河 浩一 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 Fターム(参考) 4D004 AA41 AB06 AB07 CA12 CA15 CA40 CA44 CA47 CA50 CB01 CB42 CB44 CC05 CC17 4D037 AA11 AB14 BA26 BB08 CA01 4D059 AA18 BH01 BH08 BK22 CA23 DB40  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Koichi Nakagawa 2-47, Shishitsuhigashi, 1-chome, Namiwa-ku, Osaka-shi, Osaka F-term (reference) 4D004 AA41 AB06 AB07 CA12 CA15 CA40 CA44 CA47 CA50 CB01 CB42 CB44 CC05 CC17 4D037 AA11 AB14 BA26 BB08 CA01 4D059 AA18 BH01 BH08 BK22 CA23 DB40

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 反応槽に貯留した固液混相の処理対象物
に、疎水性有機物に対する吸着能を有する球状樹脂を添
加し、槽内の水面付近に浮遊する球状樹脂を槽底部へ巡
廻させて槽内で球状樹脂を循環しながら、槽内に配置し
た超音波発信体から処理対象物へ固相に振動抽出作用を
及ぼす超音波を照射し、振動抽出作用によって疎水性有
機物を固相から液相に移行させて脱着し、界面活性剤と
疎水性有機物との結合によって固相に対する疎水性有機
物の再吸着を防止するとともに、脱着した疎水性有機物
を球状樹脂に吸着することを特徴とする汚染土壌、スラ
リー等の浄化方法。
1. A spherical resin having an ability to adsorb hydrophobic organic substances is added to a solid-liquid mixed phase treatment object stored in a reaction tank, and the spherical resin floating near the water surface in the tank is circulated to the bottom of the tank. While circulating the spherical resin in the tank, the solid phase is irradiated with ultrasonic waves from the ultrasonic wave transmitter placed in the tank to the object to be processed, and the hydrophobic organic substance is removed from the solid phase by the vibration extraction action. Desorbs by transferring to the liquid phase, preventing re-adsorption of the hydrophobic organic substance to the solid phase by bonding the surfactant and the hydrophobic organic substance, and adsorbing the desorbed hydrophobic organic substance to the spherical resin. A method for purifying contaminated soil and slurry.
JP2000159279A 2000-05-30 2000-05-30 Purification method for contaminated soil, slurry, etc. Expired - Fee Related JP3703366B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000159279A JP3703366B2 (en) 2000-05-30 2000-05-30 Purification method for contaminated soil, slurry, etc.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000159279A JP3703366B2 (en) 2000-05-30 2000-05-30 Purification method for contaminated soil, slurry, etc.

Publications (2)

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JP3703366B2 JP3703366B2 (en) 2005-10-05

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Country Link
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CN104646408A (en) * 2014-10-16 2015-05-27 中山大学 Device and method for separating polymers in soil
CN107188382A (en) * 2017-06-14 2017-09-22 山西省环境科学研究院 A kind of method in situ for removing polycyclic aromatic hydrocarbons in sediments
CN109264946A (en) * 2018-11-28 2019-01-25 知合环境(北京)有限责任公司 A kind of method of step depth separation oily sludge
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Publication number Priority date Publication date Assignee Title
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007209914A (en) * 2006-02-10 2007-08-23 Honda Electronic Co Ltd Cleaning system for volatile organic compound-contaminated soil and its cleaning method
JP4654134B2 (en) * 2006-02-10 2011-03-16 本多電子株式会社 Purification system for soil contaminated with volatile organic compounds and purification method thereof
CN104646408A (en) * 2014-10-16 2015-05-27 中山大学 Device and method for separating polymers in soil
CN107188382A (en) * 2017-06-14 2017-09-22 山西省环境科学研究院 A kind of method in situ for removing polycyclic aromatic hydrocarbons in sediments
CN107188382B (en) * 2017-06-14 2024-04-16 山西省环境科学研究院 Method for removing polycyclic aromatic hydrocarbon in sediment in situ
CN109264946A (en) * 2018-11-28 2019-01-25 知合环境(北京)有限责任公司 A kind of method of step depth separation oily sludge
CN115405054A (en) * 2022-09-09 2022-11-29 北京建筑大学 Green roof system of matrix normal position restoration

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