JP3526012B2 - Toxic substance separation and removal equipment - Google Patents

Toxic substance separation and removal equipment

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Publication number
JP3526012B2
JP3526012B2 JP09635799A JP9635799A JP3526012B2 JP 3526012 B2 JP3526012 B2 JP 3526012B2 JP 09635799 A JP09635799 A JP 09635799A JP 9635799 A JP9635799 A JP 9635799A JP 3526012 B2 JP3526012 B2 JP 3526012B2
Authority
JP
Japan
Prior art keywords
container
harmful substance
vacuum pump
harmful substances
harmful
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.)
Expired - Fee Related
Application number
JP09635799A
Other languages
Japanese (ja)
Other versions
JP2000288526A (en
Inventor
徹巳 日笠山
博 久保
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Obayashi Corp
Original Assignee
Obayashi Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Obayashi Corp filed Critical Obayashi Corp
Priority to JP09635799A priority Critical patent/JP3526012B2/en
Publication of JP2000288526A publication Critical patent/JP2000288526A/en
Application granted granted Critical
Publication of JP3526012B2 publication Critical patent/JP3526012B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

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、産業廃
棄物、汚泥等に含まれている油や有機塩素化合物といっ
たさまざまな有害物質を該汚染土壌等から分離除去する
装置に関する。
TECHNICAL FIELD The present invention relates to an apparatus for separating and removing various harmful substances such as oil and organic chlorine compounds contained in contaminated soil, industrial waste, sludge and the like from the contaminated soil and the like.

【0002】[0002]

【従来の技術】工場跡地等で基礎工事を行う場合、燃料
油や機械油が掘削土に混じって搬出されることがある。
かかる油汚染土をそのまま放置すると、該土に混入して
いる油分が揮発して周囲に拡散し、周辺住民の生活に支
障を来すとともに、雨水によって土粒子から遊離した場
合には、地下水等に混入して水質を汚濁させる原因とも
なる。そのため、かかる油汚染土については、例えば焼
却によって油分を除去し環境への拡散を防止する必要が
ある。
2. Description of the Related Art Fuel oil and machine oil are sometimes mixed with excavated soil and carried out when foundation work is performed on a site of a factory.
If such oil-contaminated soil is left as it is, the oil content mixed in the soil volatilizes and diffuses to the surroundings, hindering the lives of neighboring residents, and when it is released from soil particles by rainwater, groundwater, etc. It can also cause contamination of water quality. Therefore, for such oil-contaminated soil, it is necessary to remove the oil content by incineration, for example, to prevent its diffusion into the environment.

【0003】また、工場跡地の土壌がトリクロロエチレ
ンやテトラクロロエチレンといった有機塩素化合物で汚
染されていることがあり、かかる汚染物質の拡散防止に
ついても十分な対策が必要となる。
Further, the soil at the site of the factory may be contaminated with organic chlorine compounds such as trichlorethylene and tetrachloroethylene, and sufficient measures must be taken to prevent the diffusion of such pollutants.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、汚染土
壌、汚泥、産業廃棄物等を焼却処理する場合、焼却時に
かなりのエネルギーを必要とすることや土壌特性が変化
してしまうことは言うに及ばず、混入物あるいは焼却温
度によってはダイオキシンなどの有害副産物が発生する
懸念もあるという問題を生じていた。
However, it goes without saying that when incinerating contaminated soil, sludge, industrial waste, etc., considerable energy is required during incineration and soil characteristics change. However, there has been a problem that harmful by-products such as dioxins may be generated depending on contaminants or incineration temperature.

【0005】一方、汚染土壌等に生石灰を添加して含有
水と反応させ、そのときの発生熱で汚染物質を揮発させ
る方法もあるが、やはり土壌特性が変化してしまうとい
う問題のほか、発熱に時間がかかって効率的な有害物質
の揮発除去が困難であるという問題や、気化した有害物
質が大気に拡散することがないように作業空間全体を気
密空間とし、その上で該気密空間内の空気をすべて浄化
処理しなければならないなどの問題を生じていた。
On the other hand, there is also a method in which quick lime is added to contaminated soil or the like to react with the contained water, and the pollutants are volatilized by the heat generated at that time, but in addition to the problem that the soil characteristics change, heat generation It is difficult to efficiently remove toxic substances by volatilization, and the entire working space is made an airtight space so that the vaporized toxic substances do not diffuse into the atmosphere. There was a problem that all the air in the room had to be purified.

【0006】また、掘削された汚染土を水などで洗浄す
る方法もあるが、かかる方法では、洗浄水の循環設備や
浄化設備が必要になることはもちろん、処理された土が
スラリー状になっているため、これを脱水処理する手間
が増えるという問題を生じていた。
There is also a method of washing the excavated contaminated soil with water or the like. However, such a method requires not only circulation equipment for cleaning water and purification equipment, but also treated soil in the form of slurry. Therefore, there has been a problem that the labor for dehydration treatment is increased.

【0007】本発明は、上述した事情を考慮してなされ
たもので、有害副産物を発生させたり後処理に手間をか
けたりすることなく、さまざまな有害物質を汚染土壌等
から効率的に分離除去することが可能な有害物質の分離
除去装置を提供することを目的とする。
The present invention has been made in consideration of the above-mentioned circumstances, and efficiently separates and removes various harmful substances from contaminated soil etc. without generating harmful by-products and troublesome post-treatment. It is an object of the present invention to provide a separation / removal device for harmful substances that can be used.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係る有害物質の分離除去装置は請求項1に
記載したように、有害物質を含んだ対象物が収容される
気密性の収容体と、該収容体内の気密空間に連通された
排気管と、該排気管を介して前記収容体内の気体を引き
抜いて気圧を低下させることにより前記有害物質を前記
対象物内から揮発させるとともに揮発した有害物質を前
記収容体の外部に排出する真空ポンプと、該真空ポンプ
の上流側若しくは下流側に接続され前記収容体から排出
された有害物質を捕集する捕集機器と、前記収容体内を
加熱する加熱手段とを備え、前記収容体を水平軸線廻り
に回動自在に構成するとともに該収容内の内面に攪拌翼
を突設してなり、前記収容体の周面に対象物投入口を設
けたものである。
In order to achieve the above object, the device for separating and removing harmful substances according to the present invention has an airtightness in which an object containing a harmful substance is accommodated as described in claim 1. A container, an exhaust pipe communicated with an airtight space in the container, and a gas in the container is drawn out through the exhaust pipe to reduce the atmospheric pressure to volatilize the harmful substance from the inside of the object. A vacuum pump for discharging the volatilized harmful substance to the outside of the container, a collection device connected to the upstream side or the downstream side of the vacuum pump for collecting the harmful substance discharged from the container, and the inside of the container A heating means for heating the container, the container is configured to be rotatable about a horizontal axis, and a stirring blade is projectingly provided on an inner surface of the container, and an object inlet is provided on a peripheral surface of the container. Is provided.

【0009】また、本発明に係る有害物質の分離除去装
置は請求項2に記載したように、有害物質を含んだ対象
物が収容される気密性の収容体と、該収容体内の気密空
間に連通された排気管と、該排気管を介して前記収容体
内の気体を引き抜いて気圧を低下させることにより前記
有害物質を前記対象物内から揮発させるとともに揮発し
た有害物質を前記収容体の外部に排出する真空ポンプ
と、該真空ポンプの上流側若しくは下流側に接続され前
記収容体から排出された有害物質を捕集する捕集機器
と、前記収容体内を加熱する加熱手段とを備え、前記収
容体を水平軸線廻りに回動自在に構成するとともに該収
容内の内面に攪拌翼を突設してなり、前記加熱手段を前
記攪拌翼に設けたものである。
Further, as described in claim 2, the apparatus for separating and removing harmful substances according to the present invention comprises an airtight container for accommodating an object containing a harmful substance and an airtight space inside the container. An exhaust pipe communicated with the container, and the gas inside the container is drawn out through the exhaust pipe to reduce the atmospheric pressure so that the harmful substance is volatilized from the inside of the object and the harmful substance volatilized to the outside of the container. The housing includes a vacuum pump for discharging, a collecting device connected to an upstream side or a downstream side of the vacuum pump for collecting harmful substances discharged from the container, and a heating unit for heating the inside of the container. A body is configured to be rotatable about a horizontal axis, a stirring blade is projectingly provided on an inner surface of the housing, and the heating means is provided on the stirring blade.

【0010】[0010]

【0011】本発明に係る有害物質の分離除去装置にお
いては、まず、気密性の収容体内に有害物質を含んだ対
象物を投入して密封する。次に、気密性の収容体内の気
密空間に連通された排気管を介して該収容体内の空気を
真空ポンプで引き抜いて空気圧を低下させる。
In the device for separating and removing harmful substances according to the present invention, first, an object containing a harmful substance is put into an airtight container and sealed. Next, the air in the housing is reduced by a vacuum pump through the exhaust pipe communicating with the airtight space in the airtight housing to reduce the air pressure.

【0012】このようにすると、収容体内では、空気圧
低下に伴う有害物質の沸点降下が生じて対象物内の有害
物質が揮発するので、これを収容体の外部に排出し、さ
らに捕集機器で回収する。
In this way, the boiling point of the harmful substance is lowered in the container due to the decrease in the air pressure, and the harmful substance in the object is volatilized. Therefore, the harmful substance is discharged to the outside of the container and further collected by the collecting device. to recover.

【0013】ここで、真空ポンプによる空気の引抜きを
行うにあたり、空気の引抜きと同時に若しくはその前
に、加熱手段によって収容体内を加熱するとともに、収
容体を水平軸線廻りに回動させる。
Here, when the air is extracted by the vacuum pump, at the same time as or before the air is extracted, the inside of the container is heated by the heating means and the container is rotated around the horizontal axis.

【0014】このようにすると、収容体内の温度上昇に
よって有害物質の蒸気圧が大きくなり、真空度をあまり
高くせずとも有害物質を揮発回収することが可能とな
る。また、収容体の回動操作によって、該収容体内の対
象物が攪拌翼で攪拌されることとなり、上述した揮発作
用が促進されるとともに、対象物内に混入している有害
物質を均一に揮発させることも可能となる。ここで、加
熱手段をどのように構成するかは任意であり、例えば電
磁波を照射して加熱する、ゴミ焼却炉等の余剰熱を温風
の形で気密空間内に送り込む、電熱手段等の発熱体を収
容体に設置する、収容体に温水を通すなどの方法が考え
られる。
In this way, the vapor pressure of the harmful substance increases due to the temperature rise in the container, and it becomes possible to volatilize and recover the harmful substance without raising the vacuum degree too much. Further, by rotating the container, the object inside the container is agitated by the stirring blades, which promotes the above-mentioned volatilization action and evenly volatilizes the harmful substances mixed in the object. It is also possible to do. Here, how to configure the heating means is arbitrary, for example, irradiating with electromagnetic waves to heat, surplus heat of a dust incinerator or the like is sent into the airtight space in the form of warm air, heat generation of electric heating means, etc. It is possible to install the body in the container or pass warm water through the container.

【0015】なお、空気が抜かれた後についても、気密
空間内の気体、すなわち揮発した有害物質を抜いて減圧
状態を維持することにより、対象物内の有害物質を引き
続き揮発させる。
Even after the air is removed, the gas in the airtight space, that is, the volatilized harmful substance is removed to maintain the reduced pressure state, so that the harmful substance in the object is continuously volatilized.

【0016】有害物質が含まれている対象物としては、
主として汚染土であるが、これ以外にもスラグ、焼却
灰、汚泥、コンクリート廃材、プラスチック廃材、廃棄
木材等も含まれる。
As the object containing the harmful substance,
Although it is mainly contaminated soil, it also includes slag, incineration ash, sludge, concrete waste, plastic waste, waste wood, etc.

【0017】有害物質としては、油類や、トリクロロエ
タン、トリクロロエチレン、テトラクロロエチレン、P
CBなどの有機塩素化合物、あるいはベンゼン、トルエ
ン、ナフタレン、フェノールなどの芳香族炭化水素のほ
か、減圧下、特に、数mmHg以下のほぼ真空といえる
状態で沸点が常温以下に下がるすべての物質が包摂され
る。したがって、水銀等の重金属も本発明でいうところ
の有害物質に含まれる。
As harmful substances, oils, trichloroethane, trichloroethylene, tetrachloroethylene, P
Includes organochlorine compounds such as CB, and aromatic hydrocarbons such as benzene, toluene, naphthalene, and phenol, as well as all substances that have a boiling point below room temperature under reduced pressure, especially at a vacuum of several mmHg or less. To be done. Therefore, heavy metals such as mercury are also included in the harmful substances in the present invention.

【0018】気密空間内の気圧は、該空間内の温度にお
ける有害物質の蒸気圧以下となるように設定するのが望
ましい。この程度まで気圧を下げれば、対象物内に含ま
れる有害物質は直ちに揮発する。なお、必ずしも有害物
質の蒸気圧を下回る必要はなく、若干効率は落ちるもの
の、該蒸気圧に近い気圧であればかなりの揮発作用を期
待できる。
The air pressure in the airtight space is preferably set to be equal to or lower than the vapor pressure of harmful substances at the temperature in the space. If the atmospheric pressure is lowered to this extent, the harmful substances contained in the target object will immediately volatilize. The vapor pressure of the harmful substance does not necessarily have to be lower than the vapor pressure, and although the efficiency is slightly lowered, a considerable volatilization action can be expected if the pressure is close to the vapor pressure.

【0019】ここで、収容体内に対象物を収容するため
の対象物投入口については、これをどのように構成して
もよいが、かかる対象物投入口を収容体の周面に設ける
ようにしたならば、該対象物投入口が下を向くように収
容体を水平軸線廻りに回動させることにより、対象物投
入口を対象物排出口として兼用することが可能となる。
Here, the object insertion port for accommodating the object in the container may have any structure, but the object insertion port is provided on the peripheral surface of the container. Then, by rotating the container about the horizontal axis so that the object input port faces downward, the object input port can also be used as the object discharge port.

【0020】また、加熱手段の構成や配置は任意である
が、これを攪拌翼に設けるようにしたならば、対象物と
接触する面積が十分に確保され、該対象物の加熱を効率
的に行うことが可能となる。
Although the heating means may be arbitrarily configured and arranged, if the heating means is provided on the stirring blade, a sufficient area for contacting the object can be secured and the object can be efficiently heated. It becomes possible to do.

【0021】[0021]

【発明の実施の形態】以下、本発明に係る有害物質の分
離除去装置の実施の形態について、添付図面を参照して
説明する。なお、従来技術と実質的に同一の部品等につ
いては同一の符号を付してその説明を省略する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of a device for separating and removing harmful substances according to the present invention will be described below with reference to the accompanying drawings. It should be noted that parts and the like which are substantially the same as those of the conventional technique are designated by the same reference numerals and the description thereof is omitted.

【0022】図1は、本実施形態に係る有害物質の分離
除去装置を示した全体図、図2は同じく全体斜視図であ
る。これらの図でわかるように、本実施形態に係る有害
物質の分離除去装置1は、重油、軽油、灯油、ガソリン
等の油分、トリクロロエチレン、テトラクロロエチレン
などの有機塩素化合物といった有害物質を含んだ対象物
としての汚染土2が収容される気密性の収容体3と、該
収容体内の気密空間に連通された排気管4と、該排気管
に気液分離タンク5を介して接続された真空ポンプ6
と、該真空ポンプの下流側に接続された捕集機器7とか
ら概ね構成してある。
FIG. 1 is an overall view showing a device for separating and removing harmful substances according to this embodiment, and FIG. 2 is an overall perspective view of the same. As can be seen from these figures, the hazardous substance separation / removal device 1 according to the present embodiment is an object containing hazardous substances such as heavy oil, light oil, kerosene, oil components such as gasoline, and organic chlorine compounds such as trichlorethylene and tetrachloroethylene. The airtight container 3 in which the polluted soil 2 is contained, the exhaust pipe 4 communicating with the airtight space in the container, and the vacuum pump 6 connected to the exhaust pipe via the gas-liquid separation tank 5.
And a collecting device 7 connected to the downstream side of the vacuum pump.

【0023】真空ポンプ6は、排気管4を介して収容体
3内の気体を引き抜いて収容体3内の気圧を下げること
により、収容体3内の気圧低下に伴う有害物質の沸点降
下作用で汚染土2内の有害物質を揮発させ、さらに、揮
発した有害物質を収容体3の外部に排出するようになっ
ている。
The vacuum pump 6 draws out the gas in the container 3 through the exhaust pipe 4 and lowers the atmospheric pressure in the container 3, so that the boiling point of the harmful substance is lowered as the atmospheric pressure in the container 3 decreases. The harmful substances in the polluted soil 2 are volatilized, and the volatilized harmful substances are discharged to the outside of the container 3.

【0024】気液分離タンク5には気圧計10を取り付
けてあり、連通する収容体3内の気圧を計測できるよう
になっているとともに、該タンクの底面近傍には排水弁
12を設けてあり、該排水弁を開くことにより、気液分
離タンク5に溜まった有害物質や、汚染土2内から蒸発
してきた水分を抜くことができるようになっている。
A barometer 10 is attached to the gas-liquid separation tank 5 so that the atmospheric pressure in the communicating container 3 can be measured, and a drain valve 12 is provided near the bottom surface of the tank. By opening the drain valve, it is possible to remove harmful substances accumulated in the gas-liquid separation tank 5 and water evaporated from the contaminated soil 2.

【0025】捕集機器7は、活性炭吸着塔で構成してあ
り、真空ポンプ6から排出された気体から有害物質であ
る揮発分を吸着するとともに、該揮発分が除去された空
気等を排気口15から放出するようになっている。捕集
機器7内に充填する吸着剤としては、活性炭以外にも、
シリカ・アルミナ系吸着剤、モレキュラーシービングカ
ーボン等の合成吸着剤、ゼオライト、活性白土とも呼ば
れる酸性白土などから、有害物質の吸着特性に応じて適
宜選択すればよい。
The collecting device 7 is composed of an activated carbon adsorption tower, adsorbs volatile components, which are harmful substances, from the gas discharged from the vacuum pump 6, and exhausts the air from which the volatile components have been removed. It is designed to release from 15. As the adsorbent to be filled in the collection device 7, other than activated carbon,
It may be appropriately selected from silica / alumina-based adsorbents, synthetic adsorbents such as molecular sieving carbon, zeolite, and acid clay also called activated clay, depending on the adsorption property of harmful substances.

【0026】一方、気密性の収容体3はほぼ円筒状をな
し、鉄骨等で組み立てた架台21の内側上方に横向きに
配置してある。
On the other hand, the airtight container 3 has a substantially cylindrical shape, and is disposed laterally above the inside of the gantry 21 assembled from a steel frame or the like.

【0027】ここで、収容体3の両端周縁には図3(a)
でよくわかるようにガイド溝22を設けてあり、該ガイ
ド溝に架台21に取り付けられた荷重受け23のローラ
24を嵌め込むことで、収容体3を図1の矢印で示すよ
うに水平軸線廻りに回動自在に支持するとともに、収容
体3の一端(図1では右端)に設けられたプーリ25と
架台21に取り付けられた駆動モータ26の回転軸27
との間にベルト28を掛けることで、収容体3を水平軸
線廻りに回動させることができるようになっている。な
お、上述した排気管4は、収容体3に取り付けられたプ
ーリ25の中心近傍を貫通するように取り付けてあり、
収容体3内の気密状態が維持されるようにして該収容体
の内部空間に連通させてある。
Here, as shown in FIG.
The guide groove 22 is provided so that the container 3 can be rotated around the horizontal axis as shown by the arrow in FIG. 1 by fitting the roller 24 of the load receiver 23 attached to the pedestal 21 into the guide groove. And a rotary shaft 27 of a drive motor 26 attached to the frame 21 while being rotatably supported by the housing 25 and provided at one end (right end in FIG. 1) of the housing 3.
The housing 28 can be rotated about the horizontal axis by hanging the belt 28 between the housing 3 and the belt 28. The exhaust pipe 4 described above is attached so as to penetrate near the center of the pulley 25 attached to the container 3,
The container 3 is communicated with the internal space of the container so that the airtight state of the container 3 is maintained.

【0028】荷重受け23は、収容体3を水平軸線廻り
に回動自在となるように安定支持できるよう適宜設置す
るものとし、本実施形態ではその一例として、120゜
間隔で計三箇所設置してある。
The load receivers 23 are appropriately installed so that the containing body 3 can be stably supported so as to be rotatable about a horizontal axis, and in this embodiment, as an example thereof, three places are installed at 120 ° intervals. There is.

【0029】収容体3の周面には、対象物投入口として
の土砂投入口29を設けてあり、該土砂投入口を介して
内部の中空空間に汚染土2を投入することができるとと
もに、収容体3を上下反転させれば、該土砂投入口から
処理を終えた土を排出し、収容体3の下方に引出し自在
に配置された処理土受け槽30に落とすことができるよ
うになっている。すなわち、土砂投入口29は、対象物
排出口である土砂排出口としても機能する。
On the peripheral surface of the container 3, a earth and sand inlet 29 is provided as an object inlet, through which the contaminated soil 2 can be injected into the hollow space inside. When the container 3 is turned upside down, the treated soil can be discharged from the earth and sand inlet and dropped into the treated soil receiving tank 30 arranged below the container 3 so as to be freely drawn out. There is. That is, the earth and sand inlet 29 also functions as an earth and sand outlet that is an object outlet.

【0030】収容体3は、内部を真空若しくはそれに近
い状態まで減圧しても破損することがないよう、適当な
肉厚の鋼製容器で形成するとともに、水平軸線廻りの回
転がスムーズに行われるよう、必要に応じて図1に示す
ようなバランサー31を取り付け、重量の偏りを防止し
ておくのがよい。
The container 3 is formed of a steel container having an appropriate thickness so that the container 3 will not be damaged even if the inside pressure is reduced to a vacuum or a state close thereto, and the container 3 is smoothly rotated about the horizontal axis. As described above, it is preferable to attach a balancer 31 as shown in FIG. 1 as needed to prevent the weight from being biased.

【0031】収容体3の内面には、図3(b)でよくわか
るように攪拌翼32を突設してあり、収容体3の回動操
作とともに攪拌翼32が回ることで、収容された汚染土
2を攪拌することができるようになっている。また、攪
拌翼32の断面内には、加熱手段としての電熱ヒータ3
3を埋設してあり、図示しない電源に接続してあるとと
もに、収容体3内の温度を計測するための温度センサ3
5を該収容体の内面に取り付けてある。
As can be seen clearly in FIG. 3 (b), a stirring blade 32 is provided on the inner surface of the container 3, and the stirring blade 32 is rotated by the rotation of the container 3 so that the container 3 is accommodated. The polluted soil 2 can be stirred. Further, in the cross section of the stirring blade 32, the electric heater 3 as a heating means is provided.
3 is embedded and connected to a power source (not shown), and a temperature sensor 3 for measuring the temperature inside the container 3.
5 is attached to the inner surface of the container.

【0032】一方、架台21には駆動モータ26や電熱
ヒータ33に接続された電源を制御する制御盤34を取
り付けてあり、該制御盤は、図4のブロック図に示すよ
うに、駆動モータ26の回転状態を該駆動モータに内蔵
されたエンコーダ37で監視しつつ収容体3が所望の回
転モードや回転速度で回転するよう、駆動モータ26を
駆動制御するとともに、収容体3内の温度を温度センサ
35で監視しつつ該収容体内の温度が所望の温度に維持
されるよう、電源36を制御して電熱ヒータ33への通
電状態や通電量などを調整することができるようになっ
ている。収容体3の回転モードとしては、例えば一方向
にのみの連続若しくは断続回転、正逆両方向の切換回
転、所望角度範囲内での揺動回転などが考えられる。
On the other hand, a control board 34 for controlling the power source connected to the drive motor 26 and the electric heater 33 is attached to the pedestal 21, and the control board 34, as shown in the block diagram of FIG. While monitoring the rotation state of the drive motor by the encoder 37 built in the drive motor, the drive motor 26 is driven and controlled so that the container 3 rotates in a desired rotation mode or rotation speed, and the temperature inside the container 3 is controlled by the temperature. The power source 36 can be controlled to adjust the energization state and the energization amount to the electrothermal heater 33 so that the temperature inside the container can be maintained at a desired temperature while being monitored by the sensor 35. As the rotation mode of the container 3, for example, continuous or intermittent rotation in only one direction, switching rotation in both forward and reverse directions, swinging rotation within a desired angle range, and the like can be considered.

【0033】分離除去装置1を用いて汚染土2内から有
害物質を分離除去するには、まず、図6(a)に示すよう
に収容体3の土砂投入口29から汚染土2を投入して密
封し、しかる後に真空ポンプ6を作動させて収容体3内
の空気を引き抜き、該収容体内の空気圧を下げる。
In order to separate and remove harmful substances from the contaminated soil 2 using the separation / removal device 1, first, as shown in FIG. 6 (a), the contaminated soil 2 is charged from the earth / sand input port 29 of the container 3. Then, the vacuum pump 6 is actuated to draw out the air in the container 3 to reduce the air pressure in the container.

【0034】空気圧を下げる程度としては、収容体3内
の空気圧が該収容体内の温度における有害物質の蒸気圧
以下となるように真空ポンプ6を作動させるのが望まし
い。具体的には、有害物質が灯油である場合には、その
蒸気圧曲線は概ね図5のようになるので、気温が25゜
C程度であるならば、60mmHg程度以下に下げれば
よい。なお、同図には、参考までに水やエチルアルコー
ルの蒸気圧曲線も描いてあり、同図から、水蒸気に先行
して揮発油分が回収できることがわかる。
As for the degree of lowering the air pressure, it is desirable to operate the vacuum pump 6 so that the air pressure in the container 3 becomes equal to or lower than the vapor pressure of harmful substances at the temperature in the container. Specifically, when the harmful substance is kerosene, its vapor pressure curve becomes as shown in FIG. 5, and therefore, if the temperature is about 25 ° C., it may be lowered to about 60 mmHg or less. For reference, the vapor pressure curves of water and ethyl alcohol are also drawn in the figure, and it can be seen from the figure that the volatile oil content can be recovered prior to the steam.

【0035】このように収容体3内の空気圧を下げる
と、該収容体内では、空気圧低下に伴う有害物質の沸点
降下が生じて汚染土2内の有害物質が直ちに揮発するの
で、これを真空ポンプ6で収容体3から吸引する。そし
て、吸引された揮発分を、気液分離タンク5で液体若し
くは液体に含まれる形で回収するとともに、残りの揮発
分を捕集機器7にて吸着回収し、浄化空気を排気口15
から排出する。一方、気液分離タンク5内に溜まった有
害物質を含む溶液については、排水浄化設備や廃棄物処
理施設に送って適宜処理する。
When the air pressure in the container 3 is reduced in this way, the boiling point of the harmful substance is lowered in the container due to the decrease in the air pressure, and the harmful substance in the polluted soil 2 is immediately volatilized. At 6, suction is performed from the container 3. Then, the sucked volatile matter is collected in the gas-liquid separation tank 5 in the form of liquid or contained in the liquid, and the remaining volatile matter is adsorbed and collected by the collecting device 7, and the purified air is discharged through the exhaust port 15
Discharge from. On the other hand, the solution containing the harmful substance accumulated in the gas-liquid separation tank 5 is sent to a waste water purification facility or a waste treatment facility for appropriate treatment.

【0036】ここで、真空ポンプ6による空気の引抜き
を行うにあたり、空気の引抜きと同時に若しくはその前
に、電熱ヒータ33で収容体3内を加熱するとともに、
図6(b)に示すように駆動モータ26で収容体3を水平
軸線廻りに回動させる。
Here, when air is extracted by the vacuum pump 6, the inside of the container 3 is heated by the electric heater 33 at the same time as or before the air is extracted, and
As shown in FIG. 6 (b), the drive motor 26 rotates the container 3 about the horizontal axis.

【0037】このようにすると、収容体3内の温度上昇
によって有害物質の蒸気圧が大きくなり、真空度をあま
り高くせずとも有害物質を揮発回収することが可能とな
る。また、収容体3の回動操作に伴って該収容体内に収
容された汚染土2が攪拌翼32で攪拌されるため、上述
した揮発作用が促進されるとともに、汚染土2内に混入
している有害物質を均一に揮発させることも可能とな
る。
In this way, the vapor pressure of the harmful substance increases due to the temperature rise in the container 3, and it is possible to volatilize and recover the harmful substance without raising the vacuum degree too much. Further, since the contaminated soil 2 contained in the container 3 is stirred by the stirring blade 32 as the container 3 is rotated, the above-mentioned volatilization action is promoted and the contaminated soil 2 is mixed into the contaminated soil 2. It is also possible to volatilize existing harmful substances uniformly.

【0038】なお、空気が抜かれた後も、収容体3内の
揮発分を真空ポンプ6で抜いて減圧状態を維持すること
により、汚染土2内の有害物質を引き続き揮発させる。
Even after the air is evacuated, the volatile matter in the container 3 is evacuated by the vacuum pump 6 to maintain the reduced pressure state, so that the harmful substances in the contaminated soil 2 are continuously volatilized.

【0039】真空ポンプ6を作動させる時間について
は、どの程度まで有害物質を除去したいかによって適宜
調節する。また、いったん所定の気圧まで下げた後にお
いては、真空ポンプ6を断続運転あるいは出力を弱めて
運転し、収容体3内で揮発した有害物質による圧力上昇
の分だけ圧力が下がるようにすれば足りる。
The time for operating the vacuum pump 6 is appropriately adjusted depending on how much harmful substance is desired to be removed. Further, after the pressure is once lowered to a predetermined atmospheric pressure, it is sufficient to intermittently operate the vacuum pump 6 or operate with the output weakened so that the pressure is reduced by an amount corresponding to the pressure increase due to the harmful substances volatilized in the container 3. .

【0040】汚染土2内の有害物質が所望の程度まで分
離除去されたならば、真空ポンプ6を停止するととも
に、図6(c)に示すように土砂投入口29が下を向くよ
うに収容体3を水平軸線廻りに回動させ、しかる後に処
理された土を土砂投入口29から処理土受け槽30に落
下させる。処理済みの土は、例えば盛土材料として使用
すればよい。
When the harmful substances in the contaminated soil 2 are separated and removed to a desired degree, the vacuum pump 6 is stopped and the earth and sand inlet 29 is housed so as to face downward as shown in FIG. 6 (c). The body 3 is rotated about the horizontal axis, and then the treated soil is dropped into the treated soil receiving tank 30 through the earth and sand inlet 29. The treated soil may be used as an embankment material, for example.

【0041】なお、捕集機器7の排気口15近傍に検知
センサを設置することによって該排気口15からの揮発
分の含有量を監視し、計測値が一定値を越えたときに
は、捕集機器7内の活性炭の吸着能力が低下したと判断
し、捕集機器7内の活性炭を加熱する等の方法によって
吸着能力を回復させるようにするのがよい。
By installing a detection sensor in the vicinity of the exhaust port 15 of the collection device 7, the content of volatile components from the exhaust port 15 is monitored, and when the measured value exceeds a certain value, the collection device 7 is collected. It is preferable to determine that the adsorption capacity of the activated carbon in 7 has decreased and recover the adsorption ability by heating the activated carbon in the collection device 7 or the like.

【0042】以上説明したように、本実施形態に係る有
害物質の分離除去装置によれば、気圧低下に伴う有害物
質の沸点降下により、汚染土2に含まれる有害物質を直
ちに揮発させて収容体3の外側に排出することができ
る。
As described above, according to the hazardous substance separating / removing apparatus of this embodiment, the harmful substance contained in the polluted soil 2 is immediately volatilized due to the drop in the boiling point of the hazardous substance due to the decrease in atmospheric pressure. 3 can be discharged to the outside.

【0043】そのため、多大な焼却エネルギーを費やす
ることなく、また焼却時にダイオキシン等の有害副産物
を発生させることなく、さらには気化した有害物質が外
部に拡散することを懸念することもなく、短時間に有害
物質を汚染土2から分離除去することが可能となる。し
かも、処理された土は、生石灰処理や焼却処理されたわ
けではないので、土壌特性に変化はなく、また、水処理
されたわけではないので脱水の必要もない。したがっ
て、処理土を盛土材などにそのまま転用することが可能
となる。
Therefore, a large amount of incineration energy is not consumed, harmful by-products such as dioxins are not generated during incineration, and there is no concern that vaporized harmful substances diffuse to the outside. It is possible to separate and remove harmful substances from the polluted soil 2 in a time. Moreover, since the treated soil has not been treated with quick lime or incinerated, the soil characteristics have not changed, and since it has not been treated with water, there is no need for dehydration. Therefore, the treated soil can be diverted to the embankment material as it is.

【0044】また、有害物質を気体状態で回収できるの
で、液体状態で回収する場合に比べて後処理が容易とな
るという作用効果も奏する。
Further, since the harmful substance can be recovered in the gas state, there is an effect that the post-treatment becomes easier as compared with the case of recovering in the liquid state.

【0045】また、本実施形態に係る有害物質の分離除
去装置1によれば、収容体3の内面に攪拌翼32を突設
し、収容体3の回動操作に伴って攪拌翼32で汚染土2
を攪拌するようにしたので、沸点降下による有害物質の
揮発作用が促進されるとともに、汚染土2内に混入して
いる有害物質を均一に揮発させることも可能となる。
Further, according to the device 1 for separating and removing harmful substances according to the present embodiment, the stirring blade 32 is provided so as to project from the inner surface of the container 3, and the stirring blade 32 contaminates as the container 3 rotates. Sat 2
Since the stirring is performed, the volatilization action of the harmful substance due to the boiling point drop is promoted, and the harmful substance mixed in the contaminated soil 2 can be evenly volatilized.

【0046】また、本実施形態に係る有害物質の分離除
去装置1によれば、電熱ヒータ33で汚染土2を加熱す
るようにしたので、収容体3内の温度上昇によって有害
物質の蒸気圧が大きくなり、真空度をあまり高くせずと
も有害物質を揮発回収することが可能となる。なお、上
述した攪拌翼32による攪拌作用によって収容体3内を
均一に加熱することができるという相乗効果も期待でき
る。
In addition, according to the harmful substance separation / removal apparatus 1 of the present embodiment, since the contaminated soil 2 is heated by the electric heater 33, the vapor pressure of the harmful substance increases due to the temperature rise in the container 3. It becomes large, and it becomes possible to volatilize and recover harmful substances without increasing the degree of vacuum. A synergistic effect that the inside of the container 3 can be heated uniformly by the stirring action of the stirring blade 32 described above can be expected.

【0047】また、本実施形態に係る有害物質の分離除
去装置によれば、収容体3の周面に対象物投入口である
土砂投入口29を設けるようにしたので、土砂投入口2
9が下を向くように収容体3を水平軸線廻りに回動させ
ることにより、土砂投入口29を対象物排出口である土
砂排出口として兼用することができるとともに、処理済
みの土をスムーズに排出することも可能となる。
Further, according to the harmful substance separating / removing apparatus of the present embodiment, since the earth and sand inlet 29, which is an object inlet, is provided on the peripheral surface of the container 3, the earth and sand inlet 2
By rotating the container 3 around the horizontal axis so that 9 faces downward, the earth and sand inlet 29 can be used also as an earth and sand outlet that is an object outlet, and the treated soil can be smoothed. It can also be discharged.

【0048】また、本実施形態に係る有害物質の分離除
去装置によれば、加熱手段である電熱ヒータ33を攪拌
翼32に設けるようにしたので、汚染土2と接触する面
積が十分に確保され、該汚染土の加熱を効率的に行うこ
とが可能となる。
Further, in the device for separating and removing harmful substances according to the present embodiment, since the electric heater 33 as a heating means is provided on the stirring blade 32, a sufficient area for contacting the contaminated soil 2 is secured. Therefore, it becomes possible to efficiently heat the contaminated soil.

【0049】本実施形態では、有害物質を分離除去する
対象物を汚染土2としたが、本発明の対象物はかかる汚
染土2に限定されるものではなく、これに代えて、スラ
グ、焼却灰、汚泥、コンクリート廃材、プラスチック廃
材、廃棄木材等を対象物としてもよい。
In the present embodiment, the polluted soil 2 is used as the object for separating and removing harmful substances, but the object of the present invention is not limited to the polluted soil 2, and instead of this, slag or incineration is used. The object may be ash, sludge, concrete waste material, plastic waste material, waste wood, or the like.

【0050】また、本実施形態では、有害物質である揮
発分を活性炭の吸着によって回収するようにしたが、こ
れに代えて、例えば揮発分を溶剤に溶け込ませる形で回
収するようにしてもよい。
Further, in the present embodiment, the volatile matter, which is a harmful substance, is collected by adsorption of activated carbon, but instead of this, for example, the volatile matter may be collected in the form of being dissolved in a solvent. .

【0051】また、本実施形態では、収容体3と真空ポ
ンプ6との間に気液分離タンク5を設置して液化回収を
行うようにしたが、これを省略し、捕集機器7でのみ有
害物質の回収を行うようにしてもよい。
Further, in this embodiment, the gas-liquid separation tank 5 is installed between the container 3 and the vacuum pump 6 to perform the liquefaction recovery, but this is omitted and only the collecting device 7 is used. Harmful substances may be collected.

【0052】また、本実施形態では、気液分離タンク
5、真空ポンプ6、捕集機器7の順で収容体3に接続し
たが、まず、気液分離タンク5は、真空ポンプ6がいわ
ゆるドライタイプのものであればこれを省略してもよい
し、真空ポンプ6と捕集機器7との順序を入れ替えても
よい。
Further, in the present embodiment, the gas-liquid separation tank 5, the vacuum pump 6, and the collection device 7 are connected to the container 3 in this order. First, in the gas-liquid separation tank 5, the vacuum pump 6 is a so-called dry type. If it is of a type, this may be omitted, or the order of the vacuum pump 6 and the collection device 7 may be exchanged.

【0053】また、本実施形態では、加熱手段である電
熱ヒータ33を攪拌翼32に埋設するようにしたが、か
かる配置構成以外に、収容体3の本体に埋設する、収容
体3の内面に貼着する、収容体3の回転中心付近に配置
するなどさまざまな形態が考えられる。
Further, in the present embodiment, the electric heater 33, which is a heating means, is embedded in the stirring blade 32. However, in addition to this arrangement, the inner surface of the container 3 embedded in the main body of the container 3 is not provided. Various forms are conceivable such as sticking or arranging near the rotation center of the container 3.

【0054】また、本実施形態では特に言及しなかった
が、必要に応じて、収容体3内に圧力センサを設置した
り、攪拌状況等を確認するための覗き窓を設けたり、有
害物質の揮発状況を確認するための気体抽出口を設ける
ことが考えられる。
Although not particularly mentioned in the present embodiment, a pressure sensor is installed in the container 3, a peep window for checking the agitation status, etc. is provided, and harmful substances It is conceivable to provide a gas extraction port to check the volatilization status.

【0055】また、本実施形態では特に言及しなかった
が、場合によっては、気液分離タンク5の上流側に液化
装置を設けて排気管4内の揮発分を速やかに液化させ、
気液分離タンク5での回収効率を高めるようにしてもよ
い。
Although not particularly mentioned in this embodiment, in some cases, a liquefying device is provided on the upstream side of the gas-liquid separation tank 5 to quickly liquefy the volatile components in the exhaust pipe 4,
The recovery efficiency in the gas-liquid separation tank 5 may be increased.

【0056】また、本実施形態では特に言及しなかった
が、有害物質を含んだ汚染土2を収容体3内に密封する
際、該汚染土に所定の気化促進剤を添加するようにして
もよい。
Although not particularly mentioned in the present embodiment, when the contaminated soil 2 containing a harmful substance is sealed in the container 3, a predetermined vaporization accelerator may be added to the contaminated soil. Good.

【0057】このようにすると、収容体3内では、気化
促進剤の作用によって有害物質が揮発しやすい状態とな
るので、減圧操作を行っても気化しない有害物質であっ
ても、これをすみやかに揮発させて汚染土2から分離除
去することが可能となる。なお、かかる気化促進剤は、
汚染土2を投入した後、収容体3の内部に連通接続され
た注入口(図示せず)を介してに該汚染土に添加するよ
うにしてもよい。
In this way, the harmful substance is likely to volatilize in the container 3 due to the action of the vaporization accelerator, so that even if the harmful substance is not vaporized even when the depressurizing operation is performed, it is promptly removed. It becomes possible to volatilize and separate and remove from the contaminated soil 2. Incidentally, such a vaporization accelerator,
After the contaminated soil 2 is charged, it may be added to the contaminated soil through an inlet (not shown) connected to the inside of the container 3 so as to communicate therewith.

【0058】気化促進剤の具体例としては、酸性溶液を
加えることによって青酸ガスとして揮発するシアン、同
じく酸性溶液を加えるとともに酸化剤を加えて酸化還元
電位を高くすることによってアルシンガスとして揮発す
る砒素、塩酸を加えることによって非常に気化しやすく
なる水銀などが含まれ、シアンの場合、酸性溶液が気化
促進剤となり、砒素の場合、酸性溶液及び酸化剤が気化
促進剤となり、水銀の場合、塩酸が気化促進剤となる。
なお、本実施形態で対象とした油等の有害物質であれ
ば、気化促進剤を添加せずとも減圧操作のみでスムーズ
に気化させることができるが、かかる減圧操作に加えて
気化促進剤を添加すれば、有害物質の除去効率を著しく
高めることができることは言うまでもない。
Specific examples of the vaporization accelerator include cyanide which is volatilized as a hydrocyanic acid gas by adding an acidic solution, and arsenic which is volatilized as an arsine gas by adding an acidic solution and an oxidizing agent to increase the redox potential. It contains mercury, etc., which is very easily vaporized by adding hydrochloric acid.In the case of cyan, the acidic solution serves as a vaporization accelerator, in the case of arsenic, the acidic solution and the oxidizing agent serve as a vaporization accelerator, and in the case of mercury, hydrochloric acid It becomes a vaporization accelerator.
In addition, if it is a harmful substance such as oil targeted in the present embodiment, it can be smoothly vaporized only by depressurizing operation without adding the vaporization accelerator, but in addition to the depressurizing operation, the vaporization accelerator is added. Needless to say, if this is done, the efficiency of removing harmful substances can be significantly increased.

【0059】[0059]

【発明の効果】以上述べたように、本発明に係る有害物
質の分離除去装置によれば、真空吸引による有害物質の
沸点降下により、対象物に含まれる有害物質を直ちに揮
発させて収容体の外側に排出することができる。そのた
め、多大な焼却エネルギーを費やすることなく、また焼
却時にダイオキシン等の有害副産物を発生させることな
く、短時間に有害物質を対象物から分離除去することが
可能となる。しかも、処理された土は、生石灰処理や焼
却処理されたわけではないので、土壌特性に変化はな
く、また、水処理されたわけではないので脱水の必要も
ない。したがって、処理土を盛土材などにそのまま転用
することが可能となる。
As described above, according to the apparatus for separating and removing harmful substances according to the present invention, the boiling point of the harmful substance is lowered by vacuum suction, so that the harmful substance contained in the object is immediately volatilized, and Can be discharged to the outside. Therefore, it becomes possible to separate and remove the harmful substances from the target in a short time without spending a large amount of incineration energy and without generating harmful by-products such as dioxins during the incineration. Moreover, since the treated soil has not been treated with quick lime or incinerated, the soil characteristics have not changed, and since it has not been treated with water, there is no need for dehydration. Therefore, the treated soil can be diverted to the embankment material as it is.

【0060】また、収容体内面に突設された攪拌翼によ
って、真空吸引による揮発作用が促進されるとともに、
対象物内に混入している有害物質を均一に揮発させるこ
とも可能となるとともに、収容体内を加熱手段で加熱す
ることによって、収容体内の温度上昇によって有害物質
の蒸気圧が大きくなり、真空度をあまり高くせずとも有
害物質を揮発回収することも可能となる。
Further, the agitating blades provided on the inner surface of the housing promote the volatilization by vacuum suction, and
It is possible to evenly volatilize harmful substances mixed in the object, and by heating the inside of the container with heating means, the vapor pressure of the harmful substances increases due to the temperature rise inside the container, and the degree of vacuum is increased. It is also possible to volatilize and recover harmful substances without raising the temperature too much.

【0061】また、請求項1に係る有害物質の分離除去
装置によれば、対象物投入口が下を向くように収容体を
水平軸線廻りに回動させることにより、対象物投入口を
対象物排出口として兼用することが可能となるという効
果も奏する。
Further, according to the hazardous substance separating / removing apparatus of the first aspect, the object input port is rotated by rotating the container about the horizontal axis so that the object input port faces downward. There is also an effect that it can also be used as a discharge port.

【0062】また、請求項2に係る有害物質の分離除去
装置によれば、対象物と接触する面積が十分に確保さ
れ、該対象物の加熱を効率的に行うことが可能となると
いう効果も奏する。
Further, according to the apparatus for separating and removing harmful substances according to the second aspect, the area in contact with the object can be sufficiently secured, and the object can be efficiently heated. Play.

【0063】[0063]

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

【図1】本実施形態に係る有害物質の分離除去装置の全
体図。
FIG. 1 is an overall view of a device for separating and removing harmful substances according to the present embodiment.

【図2】本実施形態に係る有害物質の分離除去装置の全
体斜視図。
FIG. 2 is an overall perspective view of a harmful substance separation / removal device according to the present embodiment.

【図3】本実施形態に係る有害物質の分離除去装置の図
であり、(a)は図1のA―A線方向から見た側面図、(b)
は図1のB―B線に沿う断面図。
FIG. 3 is a diagram of a device for separating and removing harmful substances according to the present embodiment, in which (a) is a side view as seen from the direction of the line AA in FIG. 1, (b).
2 is a sectional view taken along the line BB of FIG.

【図4】制御盤34とその周辺機器との電気接続関係を
示したブロック図。
FIG. 4 is a block diagram showing an electrical connection relationship between a control panel 34 and its peripheral devices.

【図5】本実施形態に係る有害物質の分離除去装置の作
用を示すグラフ。
FIG. 5 is a graph showing the operation of the harmful substance separation / removal device according to the present embodiment.

【図6】本実施形態に係る有害物質の分離除去装置の作
用を示す斜視図。
FIG. 6 is a perspective view showing the operation of the harmful substance separation / removal device according to the embodiment.

【符号の説明】[Explanation of symbols]

1 分離除去装置 2 汚染土(対象物) 3 収容体 4 排気管 5 気液分離タンク 6 真空ポンプ 7 捕集機器 29 対象物投入口 32 攪拌翼 33 電熱ヒータ(加熱手段) 1 Separation and removal device 2 Contaminated soil (target) 3 housing 4 exhaust pipe 5 Gas-liquid separation tank 6 vacuum pump 7 Collection equipment 29 Object input port 32 stirring blades 33 Electric heater (heating means)

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B09C 1/00 - 1/10 B09B 3/00 - 5/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields investigated (Int.Cl. 7 , DB name) B09C 1/00-1/10 B09B 3/00-5/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 有害物質を含んだ対象物が収容される気
密性の収容体と、該収容体内の気密空間に連通された排
気管と、該排気管を介して前記収容体内の気体を引き抜
いて気圧を低下させることにより前記有害物質を前記対
象物内から揮発させるとともに揮発した有害物質を前記
収容体の外部に排出する真空ポンプと、該真空ポンプの
上流側若しくは下流側に接続され前記収容体から排出さ
れた有害物質を捕集する捕集機器と、前記収容体内を加
熱する加熱手段とを備え、前記収容体を水平軸線廻りに
回動自在に構成するとともに該収容内の内面に攪拌翼を
突設してなり、前記収容体の周面に対象物投入口を設け
たことを特徴とする有害物質の分離除去装置。
1. An airtight container for accommodating an object containing a harmful substance, an exhaust pipe communicating with an airtight space inside the container, and a gas in the container extracted through the exhaust pipe. A vacuum pump that volatilizes the harmful substance from the inside of the object by lowering the atmospheric pressure and discharges the volatilized harmful substance to the outside of the container, and the vacuum pump connected to the upstream side or the downstream side of the vacuum pump. It comprises a collecting device for collecting harmful substances discharged from the body, and a heating means for heating the inside of the container, and the container is configured to be rotatable about a horizontal axis and agitated on the inner surface of the container. A device for separating and removing harmful substances, characterized in that the blade is provided in a protruding manner, and an object inlet is provided on the peripheral surface of the container.
【請求項2】 有害物質を含んだ対象物が収容される気
密性の収容体と、該収容体内の気密空間に連通された排
気管と、該排気管を介して前記収容体内の気体を引き抜
いて気圧を低下させることにより前記有害物質を前記対
象物内から揮発させるとともに揮発した有害物質を前記
収容体の外部に排出する真空ポンプと、該真空ポンプの
上流側若しくは下流側に接続され前記収容体から排出さ
れた有害物質を捕集する捕集機器と、前記収容体内を加
熱する加熱手段とを備え、前記収容体を水平軸線廻りに
回動自在に構成するとともに該収容内の内面に攪拌翼を
突設してなり、前記加熱手段を前記攪拌翼に設けたこと
を特徴とする有害物質の分離除去装置。
2. An airtight container for accommodating an object containing a harmful substance, an exhaust pipe communicating with an airtight space inside the container, and a gas in the container extracted through the exhaust pipe. A vacuum pump that volatilizes the harmful substance from the inside of the object by lowering the atmospheric pressure and discharges the volatilized harmful substance to the outside of the container, and the vacuum pump connected to the upstream side or the downstream side of the vacuum pump. It comprises a collecting device for collecting harmful substances discharged from the body, and a heating means for heating the inside of the container, and the container is configured to be rotatable about a horizontal axis and agitated on the inner surface of the container. An apparatus for separating and removing harmful substances, characterized in that the blade is provided in a protruding manner, and the heating means is provided on the stirring blade.
JP09635799A 1999-04-02 1999-04-02 Toxic substance separation and removal equipment Expired - Fee Related JP3526012B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09635799A JP3526012B2 (en) 1999-04-02 1999-04-02 Toxic substance separation and removal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09635799A JP3526012B2 (en) 1999-04-02 1999-04-02 Toxic substance separation and removal equipment

Publications (2)

Publication Number Publication Date
JP2000288526A JP2000288526A (en) 2000-10-17
JP3526012B2 true JP3526012B2 (en) 2004-05-10

Family

ID=14162754

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3526012B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100960554B1 (en) * 2008-03-28 2010-06-03 재단법인서울대학교산학협력재단 Washing Machine Of Contaminants By Using Charged Micro Bubbles
JP2012217977A (en) * 2011-04-14 2012-11-12 Kansai Electric Power Co Inc:The Food waste processor
CN108273842A (en) * 2018-05-02 2018-07-13 北京高能时代环境技术股份有限公司 A kind of soil remediation thermal desorption heating device
CN111438173A (en) * 2019-12-21 2020-07-24 江苏地质矿产设计研究院 Device for treating organic pollutant soil

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