JP2000061443A - Device for separating and removing harmful material - Google Patents

Device for separating and removing harmful material

Info

Publication number
JP2000061443A
JP2000061443A JP10231781A JP23178198A JP2000061443A JP 2000061443 A JP2000061443 A JP 2000061443A JP 10231781 A JP10231781 A JP 10231781A JP 23178198 A JP23178198 A JP 23178198A JP 2000061443 A JP2000061443 A JP 2000061443A
Authority
JP
Japan
Prior art keywords
container
vacuum pump
harmful
harmful substances
contaminated soil
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
JP10231781A
Other languages
Japanese (ja)
Other versions
JP3555738B2 (en
Inventor
Kazuo Toge
和男 峠
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 JP23178198A priority Critical patent/JP3555738B2/en
Publication of JP2000061443A publication Critical patent/JP2000061443A/en
Application granted granted Critical
Publication of JP3555738B2 publication Critical patent/JP3555738B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To efficiently separate and remove various harmful materials from contaminated soil, etc. SOLUTION: This device 1 for separating and removing a harmful material is composed of an airtight storage 3 for the contaminated soil 2 as an object contg. the harmful material, an exhaust pipe 4 communicating with the airtight storage 3, a vacuum pump 6 connected to the exhaust pipe 4 through a gas-liq. separation tank 5 and a collecting device 7 connected to the downstream side of the vacuum pump 6. The gas in the storage 3 is evacuated by the vacuum pump 6 through the exhaust pipe 4 to lower the gas pressure in the storage 3. Consequently, the harmful material in the contaminated soil 2 is volatilized by the b.p. depression action of the harmful material due to the pressure lowering in the storage 3, and further the volatilized harmful material is discharged outside the storage 3.

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 However, it has been difficult to efficiently remove the harmful substances by volatilization.

【0006】本発明は、上述した事情を考慮してなされ
たもので、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 view of the above circumstances, and an object thereof is to provide a device for separating and removing harmful substances from which various harmful substances can be efficiently separated and removed from contaminated soil or the like. And

【0007】[0007]

【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を備えたものであ
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 that discharges the volatilized harmful substance to the outside of the containing body, and a collecting device that is connected to the upstream side or the downstream side of the vacuum pump and collects the harmful substance discharged from the containing body Is.

【0008】また、本発明に係る有害物質の分離除去装
置は、前記収容体内に攪拌手段を設置したものである。
Further, the harmful substance separating / removing apparatus according to the present invention has a stirring means installed in the container.

【0009】また、本発明に係る有害物質の分離除去装
置は、前記収容体内を加熱する加熱手段を備えたもので
ある。
The toxic substance separating / removing apparatus according to the present invention includes a heating means for heating the inside of the container.

【0010】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 hazardous substance separating / removing apparatus according to the present invention, first, an object containing a hazardous 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.

【0011】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。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。
In this way, the boiling point of the harmful substance is lowered in the container due to the decrease of 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. Even after the air is removed, the gas in the airtight space, that is, the vaporized harmful substance is removed to maintain the reduced pressure state, so that the harmful substance in the object is continuously vaporized.

【0012】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。
[0012] 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.

【0013】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 the 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.

【0014】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。
It is desirable that the air pressure in the airtight space is 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.

【0015】ここで、前記収容体内に攪拌手段を設置し
た場合においては、該攪拌手段で収容体内に収容された
対象物を攪拌させる。このようにすると、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。
Here, when the stirring means is installed in the container, the stirring means stirs the object contained in the container. By doing so, it is possible to promote the above-mentioned volatilization action and to evenly volatilize the harmful substances mixed in the object.

【0016】また、前記収容体内を加熱する加熱手段を
備えた場合においては、該加熱手段で収容体内を加熱す
る。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。
When a heating means for heating the inside of the container is provided, the inside of the container is heated by the heating means. By doing so, 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.

【0017】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。
The configuration of the heating means is arbitrary, and for example, it is heated by irradiating electromagnetic waves, the surplus heat of a refuse incinerator or the like is fed into the airtight space in the form of warm air, and the heat generation of electric heating means or the like. It is possible to install the body in the container or pass warm water through the container.

【0018】[0018]

【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 will be omitted.

【0019】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である。同図でわかるように、
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とからなり、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。
FIG. 1 is an overall view showing a device for separating and removing harmful substances according to this embodiment. As you can see in the figure,
The hazardous substance separation / removal device 1 according to the present embodiment includes heavy oil,
Light oil, kerosene, oil such as gasoline, trichlorethylene,
An airtight container 3 in which a polluted soil 2 containing a harmful substance such as an organic chlorine compound such as tetrachloroethylene is contained, an exhaust pipe 4 communicating with the airtight space in the container, and an exhaust pipe It is composed of a vacuum pump 6 connected via a gas-liquid separation tank 5 and a collection device 7 connected to the downstream side of the vacuum pump.
The gas in the container 3 is drawn out through the air to lower the atmospheric pressure in the container 3, and the harmful substance in the polluted soil 2 is volatilized by the boiling point lowering action of the harmful substance accompanying the pressure decrease in the container 3, Further, the volatilized harmful substance is discharged to the outside of the container 3.

【0020】気密性の収容体3は、どのような材質で構
成してもよいが、例えば鋼製の容器で構成しておけば、
対象物である汚染土2に大気圧が作用して揮発が妨げら
れるのを未然に防止することができる。
The airtight container 3 may be made of any material. For example, if it is made of a steel container,
It is possible to prevent the polluted soil 2 which is the object from being affected by atmospheric pressure and obstructing volatilization.

【0021】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 air pressure inside the communicating container 3 can be measured, and a drain valve 12 is provided near the bottom 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.

【0022】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.

【0023】一方、収容体3には、駆動モータ21で昇
降自在に回転駆動される攪拌機構22を取り付けてあ
り、かかる駆動モータ21及び攪拌機構22は、駆動モ
ータ21で攪拌機構22を昇降あるいは回転させること
によってその攪拌翼23で汚染土2を攪拌する攪拌手段
として作用する。
On the other hand, an agitating mechanism 22 which is rotatably driven by a drive motor 21 is attached to the container 3, and the drive motor 21 and the agitating mechanism 22 raise or lower the agitating mechanism 22 by the drive motor 21. By rotating, the stirring blade 23 acts as a stirring means for stirring the contaminated soil 2.

【0024】また、収容体3の壁断面内には通水管24
を埋設してあり、該通水管にはボイラー25を接続して
ある。すなわち、通水管24及びボイラー25は、ボイ
ラー25から供給される温水を通水管24に通して収容
体3内部を加熱するとともに、加熱によって温度が下が
った冷水を再びボイラー25に循環させることで収容体
3内部を加熱する加熱手段として作用する。
A water pipe 24 is provided in the wall cross section of the container 3.
And a boiler 25 is connected to the water pipe. That is, the water pipe 24 and the boiler 25 heat the hot water supplied from the boiler 25 through the water pipe 24 to heat the inside of the container 3, and the cold water whose temperature has been lowered by heating is circulated to the boiler 25 again to be housed. It acts as a heating means for heating the inside of the body 3.

【0025】なお、気液分離タンク5の上流側には、液
化装置26及び該液化装置に冷水を供給するとともに熱
交換で暖められた温水を冷却して再び液化装置26に循
環させる冷却装置27を設けてあり、かかる液化装置2
6及び冷却装置27は、排気管4内の揮発分を液化させ
る液化手段として作用する。
On the upstream side of the gas-liquid separation tank 5, a liquefying device 26 and a cooling device 27 for supplying cold water to the liquefying device and cooling the hot water warmed by heat exchange and circulating it to the liquefying device 26 again. Liquefaction device 2
6 and the cooling device 27 act as a liquefying means for liquefying the volatile components in the exhaust pipe 4.

【0026】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、収容体3の投入口2
8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 by using the separation / removal device 1, first, the charging port 2 of the container 3
The polluted soil 2 is charged from 8 and sealed, and then the vacuum pump 6 is operated to draw out the air in the container 3 to lower the air pressure in the container.

【0027】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2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 is as shown in FIG. 2, so that 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.

【0028】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、液化装置26で液化した分を気液分離タンク5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 lowered in this way, the boiling point of the harmful substance drops due to the decrease in the air pressure in the container, and the harmful substance in the contaminated soil 2 is immediately volatilized. At 6, suction is performed from the container 3. Then, the liquefied component in the liquefaction device 26 is collected in the gas-liquid separation tank 5, the remaining volatile components are adsorbed and collected in the collection device 7, and the purified air is discharged from the exhaust port 15. 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.

【0029】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 components in the container 3 are 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.

【0030】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 substances are 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. .

【0031】また、真空ポンプ6による揮発吸引を行っ
ている間、攪拌機構22を駆動モータ21で適宜駆動し
て汚染土2を攪拌するとともに、ボイラー25を作動さ
せて温水を収容体3の通水管24に供給し汚染土2を加
熱する。
While the vacuum pump 6 is performing the volatilization suction, the stirring mechanism 22 is appropriately driven by the drive motor 21 to stir the contaminated soil 2, and the boiler 25 is operated to let the hot water pass through the container 3. The contaminated soil 2 is heated by supplying it to the water pipe 24.

【0032】このようにすると、汚染土2からの有害物
質の揮発作用が促進されるとともに、汚染土2からの均
一な揮発が期待できる。
In this way, the volatilization action of the harmful substances from the polluted soil 2 is promoted, and the uniform volatilization from the polluted soil 2 can be expected.

【0033】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を停止し、処理され
た土を排出口29から取り出す。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 have been separated and removed to a desired degree, the vacuum pump 6 is stopped and the treated soil is taken out from the discharge port 29. The treated soil may be used as an embankment material, for example.

【0034】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 near 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 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.

【0035】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 separation / removal device 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.

【0036】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, it becomes possible to separate and remove harmful substances from the contaminated soil 2 in a short time without spending a large amount of incineration energy and without generating harmful by-products such as dioxins during incineration. Moreover, the treated soil was not treated with quicklime or incineration, so
There is no change in soil properties and no need for dehydration as it has not been water treated. Therefore, the treated soil can be diverted to the embankment material as it is.

【0037】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内の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を作動させるようにしたので、汚染土2内に含まれ
る有害物質は直ちに揮発し、短時間に汚染土2内の有害
物質含有量を低下させることができる。
Further, according to the harmful substance separation / removal apparatus 1 of this embodiment, the vacuum pump 6 is operated so that the atmospheric pressure in the container 3 becomes equal to or lower than the vapor pressure of the harmful substance at the temperature in the container. Therefore, the harmful substance contained in the polluted soil 2 is immediately volatilized, and the harmful substance content in the polluted soil 2 can be reduced in a short time.

【0038】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内に攪拌機構22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 hazardous substance separating / removing apparatus 1 of the present embodiment, the contaminated soil 2 is agitated in the container 3 by the agitating mechanism 22, so that the volatilizing action of the hazardous substance due to the lowering of the boiling point can be achieved. While being promoted, it is possible to evenly volatilize harmful substances mixed in the contaminated soil 2.

【0039】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、ボイラー25からの温水を収容体3
内の通水管24に通すことで汚染土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、上述の攪拌
機構22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。
Further, according to the hazardous substance separating / removing apparatus 1 according to the present embodiment, the warm water from the boiler 25 is stored in the container 3.
Since the contaminated soil 2 is heated by passing it through the water passage pipe 24 inside, the vapor pressure of the harmful substance increases due to the temperature rise in the container 3, and the harmful substance is volatilized and recovered without raising the vacuum degree too much. It becomes possible to do. In addition, a synergistic effect that the inside of the container 3 can be uniformly heated by the stirring mechanism 22 described above can be expected.

【0040】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 object for separating and removing harmful substances is the contaminated soil 2. However, the object of the present invention is not limited to the contaminated 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.

【0041】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. .

【0042】また、本実施形態では、収容体3と真空ポ
ンプ6との間に液化装置26及び気液分離タンク5を設
置して冷却液化による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 the present embodiment, the liquefying device 26 and the gas-liquid separation tank 5 are installed between the container 3 and the vacuum pump 6 to collect by cooling and liquefying, but this is omitted. The harmful substances may be collected only by the collecting device 7.

【0043】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 collecting device 7 are connected to the container 3 in this order. First, in the gas-liquid separation tank 5, the vacuum pump 6 is so-called dry. 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.

【0044】また、本実施形態では、揮発作用の促進等
を目的として、攪拌手段である駆動モータ21及び攪拌
機構22並びに加熱手段である通水管24及びボイラー
25を設置したが、真空ポンプ6だけで有害物質を効率
よく回収することができるのであれば、これらのいずれ
かあるいは両方を省略してもよい。
Further, in this embodiment, the drive motor 21 and the stirring mechanism 22, which are stirring means, and the water pipe 24 and the boiler 25, which are heating means, are installed for the purpose of accelerating the volatilization action, but only the vacuum pump 6 is provided. Either or both of these may be omitted as long as the harmful substances can be efficiently collected in.

【0045】また、本実施形態では、通水管24を収容
体3の壁断面にのみ埋設するようにしたが、収容体3内
を加熱することができるのであれば、どのように通水管
24を埋設してもよく、例えば、攪拌機構22のシャフ
ト部分や攪拌翼23にも埋設するようにすれば、加熱効
率の向上を図ることが可能となる。
Further, in the present embodiment, the water pipe 24 is embedded only in the wall cross section of the container 3, but if the inside of the container 3 can be heated, how can the water pipe 24 be formed. It may be embedded. For example, if it is embedded also in the shaft portion of the stirring mechanism 22 and the stirring blades 23, the heating efficiency can be improved.

【0046】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.

【0047】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、
図3に示すように密封後であっても収容体3の内部に連
通接続された注入口30を介して汚染土2に添加するよ
うにしてもよい。
In this way, since the harmful substance is easily volatilized in the container 3 by the action of the vaporization accelerator, even if the harmful substance is not vaporized even when the depressurizing operation is performed, the harmful substance is promptly removed. It becomes possible to volatilize and separate and remove from the contaminated soil 2. Incidentally, such a vaporization accelerator,
As shown in FIG. 3, even after sealing, it may be added to the contaminated soil 2 through the injection port 30 that is connected and communicated with the inside of the container 3.

【0048】かかる具体例としては、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。
As a specific example, cyanide which is volatilized as a cyanide gas by adding an acidic solution, and arsenic and hydrochloric acid which is volatilized as an arsine gas by adding an oxidizing solution and an oxidizing agent to increase the redox potential are added. In the case of cyanide, the acidic solution serves as a vaporization promoter, in the case of arsenic, the acidic solution and the oxidizing agent serve as a vaporization promoter, and in the case of mercury, hydrochloric acid is a vaporization promoter. Becomes In addition, if it is a harmful substance such as oil targeted in this embodiment,
It is possible to smoothly vaporize only by the depressurization operation without adding the vaporization accelerator, but it goes without saying that if the vaporization accelerator is added in addition to the depressurization operation, the efficiency of removing harmful substances can be significantly increased.

【0049】[0049]

【発明の効果】以上述べたように、請求項1に係る本発
明の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 of the present invention according to claim 1, the boiling point of the harmful substances is lowered by vacuum suction, and the harmful substances contained in the object are immediately volatilized. Can be discharged to the outside of the container. 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.

【0050】また、請求項2に係る本発明の有害物質の
分離除去装置によれば、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いう効果も奏する。
Further, according to the apparatus for separating and removing harmful substances of the present invention according to claim 2, the volatilization action by vacuum suction is promoted and the harmful substances mixed in the object are uniformly vaporized. There is also an effect that it becomes possible.

【0051】また、請求項3に係る本発明の有害物質の
分離除去装置によれば、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という効
果も奏する。
Further, according to the apparatus for separating and removing harmful substances of the present invention according to claim 3, the vapor pressure of the harmful substances increases due to the temperature rise in the containing body, and the harmful substances are volatilized without raising the vacuum degree too much. There is also an effect that it becomes possible to collect.

【0052】[0052]

【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作
用を示すグラフ。
FIG. 2 is a graph showing the operation of the harmful substance separation / removal device according to the present embodiment.

【図3】変形例に係る有害物質の分離除去装置の全体
図。
FIG. 3 is an overall view of a device for separating and removing harmful substances according to a modification.

【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 21 駆動モータ(攪拌手段) 22 攪拌機構(攪拌手段) 24 通水管(加熱手段) 25 ボイラー(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 21 Drive motor (stirring means) 22 Stirring mechanism (stirring means) 24 Water pipe (heating means) 25 boiler (heating means)

Claims (3)

【特許請求の範囲】[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を備えたことを特徴
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. A device for separating and removing harmful substances, comprising: a collecting device for collecting the harmful substances discharged from the body.
【請求項2】 前記収容体内に攪拌手段を設置した請求
項1記載の分離除去装置。
2. The separation / removal device according to claim 1, wherein stirring means is installed in the container.
【請求項3】 前記収容体内を加熱する加熱手段を備え
た請求項1記載の分離除去装置。
3. The separation / removal device according to claim 1, further comprising heating means for heating the inside of the container.
JP23178198A 1998-08-18 1998-08-18 Apparatus and method for separating and removing harmful substances Expired - Fee Related JP3555738B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23178198A JP3555738B2 (en) 1998-08-18 1998-08-18 Apparatus and method for separating and removing harmful substances

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23178198A JP3555738B2 (en) 1998-08-18 1998-08-18 Apparatus and method for separating and removing harmful substances

Publications (2)

Publication Number Publication Date
JP2000061443A true JP2000061443A (en) 2000-02-29
JP3555738B2 JP3555738B2 (en) 2004-08-18

Family

ID=16928940

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Country Status (1)

Country Link
JP (1) JP3555738B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011218312A (en) * 2010-04-12 2011-11-04 Miike Iron Works Co Ltd Recycling plant for fishery waste
CN105057336A (en) * 2015-08-14 2015-11-18 无锡乐华自动化科技有限公司 Non-destructive repair method of contaminated soil
CN105057335A (en) * 2015-08-14 2015-11-18 无锡乐华自动化科技有限公司 Contaminated soil remediation method
CN105170615A (en) * 2015-08-26 2015-12-23 苏州宏奇锐自动化有限公司 Equipment for removing soil pollutants
CN105170635A (en) * 2015-08-26 2015-12-23 苏州宏奇锐自动化有限公司 Automation system for repairing contaminated soil
CN106607442A (en) * 2015-10-26 2017-05-03 镇江中焱数控设备有限公司 Garbage collection device
CN110002703A (en) * 2019-05-08 2019-07-12 义乌市婉聚电子有限公司 A kind of soil heavy metals removal device based on agricultural
CN113070334A (en) * 2021-04-12 2021-07-06 张月 Solar ex-situ remediation system and method based on green energy pollution site remediation

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011218312A (en) * 2010-04-12 2011-11-04 Miike Iron Works Co Ltd Recycling plant for fishery waste
CN105057336A (en) * 2015-08-14 2015-11-18 无锡乐华自动化科技有限公司 Non-destructive repair method of contaminated soil
CN105057335A (en) * 2015-08-14 2015-11-18 无锡乐华自动化科技有限公司 Contaminated soil remediation method
CN105170615A (en) * 2015-08-26 2015-12-23 苏州宏奇锐自动化有限公司 Equipment for removing soil pollutants
CN105170635A (en) * 2015-08-26 2015-12-23 苏州宏奇锐自动化有限公司 Automation system for repairing contaminated soil
CN106607442A (en) * 2015-10-26 2017-05-03 镇江中焱数控设备有限公司 Garbage collection device
CN110002703A (en) * 2019-05-08 2019-07-12 义乌市婉聚电子有限公司 A kind of soil heavy metals removal device based on agricultural
CN113070334A (en) * 2021-04-12 2021-07-06 张月 Solar ex-situ remediation system and method based on green energy pollution site remediation

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