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JP4009883B2 - Method and apparatus for separating and removing harmful substances - Google Patents
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JP4009883B2 - Method and apparatus for separating and removing harmful substances - Google Patents

Method and apparatus for separating and removing harmful substances Download PDF

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Publication number
JP4009883B2
JP4009883B2 JP20377797A JP20377797A JP4009883B2 JP 4009883 B2 JP4009883 B2 JP 4009883B2 JP 20377797 A JP20377797 A JP 20377797A JP 20377797 A JP20377797 A JP 20377797A JP 4009883 B2 JP4009883 B2 JP 4009883B2
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container
harmful
substance
harmful substances
harmful substance
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JPH1128446A (en
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清茂 西林
博 久保
徹巳 日笠山
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Obayashi Corp
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Obayashi Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、汚染土壌、産業廃棄物等に含まれているシアンや砒素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方法及び装置に関する。
【0002】
【従来の技術】
工場跡地等で基礎工事を行う場合、シアンや砒素といった物質が掘削土に混じって搬出されることがある。かかる掘削土をそのまま放置すると、シアン等が地下水等を経由して環境に拡散し、生態系に大きな影響を及ぼすおそれがある。
【0003】
そのため、かかる物質は、水銀、カドミウム、有機隣、鉛、六価クロム、PCBなどとともに、環境への拡散を厳重に監視すべき有害物質として扱われ、一般廃棄物とは区別して管理型若しくは遮断型の廃棄物処分場に処分する、所定の薬剤で不溶化処理を行う、通電によって回収するといったさまざまな措置を講じなければならない。
【0004】
【発明が解決しようとする課題】
しかしながら、最近では、環境保護の観点から廃棄物処分場の確保がかなり困難な状況になってきており、廃棄処分すべき処分場が見当たらないという問題を生じていた。
【0005】
一方、不溶化処理は、処理された土が新たな産業廃棄物となる場合があり、その場合には上述したと同様、処分場確保の点で問題が生じるし、通電回収による方法では、一定の通電期間を要し、電気的に中性の有害物質であればそもそも回収が困難である。いずれにしろ、シアンや砒素といった有害物質を汚染土壌等から効率的に分離除去する方法はいまだ確立されていないのが現状である。
【0006】
本発明は、上述した事情を考慮してなされたもので、シアンや砒素いった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方法及び装置を提供することを目的とする。
【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方法は請求項1に記載したように、有害物質を含んだ対象物を気密空間内に密封するとともに該対象物に所定の気化促進剤を添加し、次いで、前記気密空間内の気圧を下げて前記有害物質の沸点降下を生じさせることにより前記対象物内から前記有害物質を揮発させるとともに、揮発した有害物質を前記気密空間の外部に排出する有害物質の分離除去方法であって、有害物質がシアンで気化促進剤が酸性溶液、又は有害物質が砒素で気化促進剤が酸性溶液及び酸化剤であるものである。
【0008】
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接続され所定の気化促進剤が貯留された貯留タンクと、前記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、前記真空ポンプは、気圧低下による前記有害物質の沸点降下によって前記気化促進剤が添加された前記対象物内から前記有害物質を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ようになっている有害物質の分離除去装置であって、有害物質がシアンで気化促進剤が酸性溶液、又は有害物質が砒素で気化促進剤が酸性溶液及び酸化剤であるものである。
【0009】
また、本発明に係る有害物質の分離除去装置は、前記収容体を剛体容器で構成したものである。
【0010】
また、本発明に係る有害物質の分離除去装置は、前記収容体をシートで構成し、該シートを前記対象物を収容した状態で袋状に密封自在に構成したものである。
【0011】
本発明に係る有害物質の分離除去方法においては、有害物質を含んだ対象物を気密空間内に密封するとともに該対象物に気化促進剤を添加し、しかる後に気密空間内の空気を抜いて空気圧を下げる。このようにすると、気密空間内では、気化促進剤の作用によって有害物質が気化しやすい状態となるとともに空気圧低下に伴う有害物質の沸点降下が生じるので、対象物内からは有害物質が揮発する。したがって、これを気密空間の外部に排出することにより、対象物内に含まれる有害物質が分離除去される。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。
【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。
【0013】
本発明において有害物質とは、減圧しても常温では気化しないが気化促進剤を加えることによって、減圧下、特に数mmHg以下のほぼ真空といえる状態で気化が促進される物質のうち、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、又は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が該当する。ここで、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る。
【0015】
気密空間をどのように形成するかは任意であり、例えば気密性収容体の内部空間を気密空間とし、該気密性収容体の内部に掘削土砂等の対象物を投入するようにしてもよいし、実際に汚染された地盤を対象物とするならば、その汚染領域を取り囲むようにして地中壁を形成するとともに、その上部を気密シートで覆って気密空間を形成してもよい。
【0016】
気密空間内の気圧は、気化促進剤を添加した状態での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気化促進剤の作用と相まって直ちに揮発する。なお、必ずしも上述した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。
【0017】
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とともに、貯留タンクに貯留された気化促進剤を収容体内に送り込んで対象物内に添加する。次に、排気管を介して収容体内の空気を真空ポンプで抜き、空気圧を下げる。
【0018】
このようにすると、気密空間内では、気化促進剤の作用によって有害物質が気化しやすい状態となるとともに空気圧低下に伴う有害物質の沸点降下が生じるので、対象物内からは有害物質が揮発する。したがって、これを気密空間の外部に排出し、さらに捕集機器で捕集する。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。
【0019】
有害物質、それが含まれている対象物並びに気圧に関する説明については、上述したとほぼ同様であるのでここでは省略する。
【0020】
気密性の収容体としては、内部の真空状態を実質的に維持できるものであれば、外部からの大気圧に耐える構造にするかどうかは任意であるが、対象物に大気圧が作用すると該対象物からの有害物質の揮発が妨げられることが懸念される場合には、前記収容体を剛体容器で構成しておくと、対象物に大気圧が作用しないので、有害物質は、対象物内からスムーズに揮発する。
【0021】
一方、対象物に大気圧が作用しても有害物質の揮発が妨げられるおそれがない場合、例えば、対象物が礫や砂利を多く含んだ汚染土である場合には、前記収容体をシートで構成し、該シートを前記対象物を収容した状態で袋状に密封自在に構成しておくと、本発明による揮発作用に加圧作用が加わり、より効率的な分離除去が可能となる。また、収容体がシートであるため、保管や運搬の際にたたんでおくことができるという作用効果も得られる。
【0022】
なお、気密性シートの使用の際にはこれを拡げて対象物を載せた後、対象物を包み込むようにして袋状に密封し、しかる後に収容体内の空気を上述したように引き抜いて有害物質を揮発除去すればよい。気密性シートとしては、ナイロン、ビニロン、ポリエステルターポリンなどの材料から任意に選択することができる。
【0023】
【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方法及び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。
【0024】
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斜視図である。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、有害物質であるシアン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供給管17を介して連通接続され気化促進剤である酸性溶液が貯留された貯留タンク5と、収容体3に貫通配置された排気管4と、該排気管に気液分離タンク6を介して接続された真空ポンプ7と、該真空ポンプの下流側に接続された捕集機器8とからなり、真空ポンプ7は、酸性溶液の添加によって収容体3内でシアンから変化したシアン化水素酸を、排気管4を介して該収容体内の気体を引き抜いて気圧を下げることにより、収容体3内の気圧低下に伴う沸点降下作用で青酸ガスとして揮発させ、さらに揮発した青酸ガスを収容体3の外部に排出するようになっている。
【0025】
気密性の収容体3は、ナイロン、ビニロン、ポリエステルターポリンなどの材料で形成された気密性シート11を、後述するように汚染土2を収容した状態で袋状に包み込んだ後、接着、溶着等の方法で密封して構成するのがよい。
【0026】
排気管4は、例えば硬質塩化ビニルで形成することが可能であり、多数の孔16が形成されたその先端部分を収容体3の底部に設置されたサンドマット9内に埋設してある。そして、該マット内を通過してきた収容体3内の空気や汚染土2内からの青酸ガスを孔16から吸入するようになっている。
【0027】
すなわち、サンドマット9は、孔16を汚染土2で目詰まりさせることなく空気や青酸ガスをスムーズに排出させるためのいわば通気体としての役目を果たすとともに、汚染土2の重量や該土に含まれる礫等の突起物によって気密性シート11が破れたりしないようにする保護層としての役目も果たす。
【0028】
気液分離タンク6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ドレインコック12を設けてあり、バルブ13を閉じた状態で該コックを開くことにより、汚染土2内から蒸発して気液分離タンク6に溜まった水を抜くことができるようになっている。なお、かかる水に汚染土2から揮発した青酸ガスが溶けている場合には、気密状態を維持しながら引き抜いて処理する。
【0029】
捕集機器8は、真空ポンプ7から排出された気体から有害物質である青酸ガスを捕集回収するための機器であり、その内部には、青酸ガスを吸着するための活性炭を充填してある。なお、微量の青酸ガスが捕集機器8内で吸着されずに排気口から大気に放出される事態が考えられるが、かかる場合には、捕集機器8の排気口を加熱燃焼炉に接続し、該燃焼炉にて青酸ガスを燃焼させて窒素、二酸化炭素及び水に分解し、無毒化を図るようにするのがよい。
【0030】
本実施形態に係る有害物質の分離除去装置1を現場にて製造するには、まず、図2(a)に示すように気密性のシート11を地面上に拡げ、その上にサンドマット9を敷き均すとともに該マット内に排気管4の先端部分を埋設する。
【0031】
次に、同図(b)に示すようにサンドマット9の上に汚染土2を盛るとともに、該汚染土内に供給管17の先端を埋設する。
【0032】
次に、気密性のシート11の縁部を持ち上げてサンドマット9及び汚染土2を袋状に包み込む。そして、それらの縁部を重ね合わせて溶着、接着等の方法によって接合密封し、同図(c)に示すような、内部に気密空間が形成された収容体3とする。
【0033】
最後に、供給管17に貯留タンク5を接続するとともに、排気管4に気液分離タンク6、真空ポンプ7及び捕集機器8を図1に示したように順次接続する。
【0034】
このようにして組み立てられた分離除去装置1を用いて汚染土2内からシアンを分離除去するには、まず、貯留タンク5内の酸性溶液を収容体3内に送り込み、汚染土2のpHを低下させる。このようにすると、汚染土2内のシアンは、酸性環境下でシアン化水素酸に変化し、青酸ガスとして気化しやすくなる。
【0035】
かかる状態で、真空ポンプ7を作動させて収容体3内の空気を抜き、該収容体内の空気圧を下げる。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シアン化水素酸の蒸気圧以下となるように真空ポンプ7を作動させるのが望ましい。ここで、シアン化水素酸の蒸気圧曲線が概ね図3のようになるとするならば、気温が10゜Cのときには、収容体内の気圧を例えば100mmHg程度以下に下げればよい。また、さらに数mmHgまで下げてやれば、土粒子内部や土粒子間の細かい空隙に存在して離脱しにくい状態のものも、これを短時間に効率よく揮発させることができる。なお、同図には、参考までに灯油、水、エチルアルコールの蒸気圧曲線も併せて示した。
【0036】
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、空気圧低下に伴うシアン化水素酸の沸点降下が生じて汚染土2内のシアン化水素酸が直ちに青酸ガスとして揮発するので、これを真空ポンプ7で収容体3から吸引して捕集機器8に送り、該捕集機器にて青酸ガスを吸着させて回収する。
【0037】
なお、空気が抜かれた後についても、気密空間内の気体、すなわち揮発した青酸ガスを抜いて減圧状態を維持することにより、汚染土2内のシアンを引き続き揮発させる。
【0038】
真空ポンプ7を作動させる時間については、どの程度までシアンを除去したいかによって適宜調節する。また、いったん所定の空気圧まで下げた後においては、真空ポンプ7を断続運転あるいは出力を弱めて運転し、収容体3内で揮発した青酸ガス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。
【0039】
汚染土2内のシアンが所望の程度まで分離除去されたならば、真空ポンプ7 を停止して気密性シート11を開き、該シート内から処理された土を取り出す。処理済みの土は、例えば盛土材料として使用すればよい。
【0040】
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方法及び装置によれば、酸性溶液の添加によってシアンをシアン化水素酸に変化させて気化しやすくし、かかる状態で気圧を下げてシアン化水素酸の沸点を降下させることにより、シアンを青酸ガスとして汚染土2内から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。
【0041】
そのため、きわめて毒性の強いシアンを汚染土から効率的に分離除去することが可能となり、汚染土を処分するための廃棄物処分場を設置する必要がなくなる。また、処理した後に脱水が必要となる水洗浄とは異なり、処理された土をすぐに再利用することができる。
【0042】
また、収容体3内の気圧が該収容体内の温度におけるシアン化水素酸の蒸気圧以下となるように真空ポンプ7を作動させるようにしたので、汚染土2内に含まれるシアンは、青酸ガスの形で直ちに揮発し、短時間に汚染土内のシアン含有量を低下させることができる。
【0043】
また、収容体3を気密性シート11で構成したので、該シートを介して大気圧が汚染土2に作用する。そのため、汚染土2に含まれているシアンは、気化促進剤及び減圧による揮発作用に大気圧による加圧作用が加わり、収容体3外部への排出が促進され、より効率的な分離除去が可能となる。また、収容体3がシート11であるため、保管や運搬の際にたたんでおくことができるという作用効果も得られる。
【0044】
また、収容体3の底部に保護層としてのサンドマット9を設けたので、汚染土2の重量が大きかったり該汚染土に突起物が含まれていたとしても、それが原因で収容体3が損傷を受けることはない。そのため、収容体3の転用が可能となる。
【0045】
また、サンドマット9内に排気管4を埋設するようにしたので、該管に形成された孔16が汚染土2で塞がれて空気やシアンの排出が妨げられるおそれがなくなるとともに、汚染土2の広い範囲からシアンを揮発させることも可能となる。
【0046】
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としたが、本発明の対象物はかかる汚染土に限定されるものではなく、汚染土以外にも、スラグ、焼却灰、汚泥、コンクリート廃材、プラスチック廃材、廃棄木材等を対象物としてもよい。
【0047】
また、本実施形態では、有害物質をシアンとしたが、本発明でいうところの有害物質はかかる物質に限定されるものではなく、例えば砒素に対しても適用することができる。かかる構成においては、砒素が含まれている汚染土等の対象物に酸性溶液及び酸化剤を気化促進剤として添加すれば、砒素がアルシンガスの形で気化しやすい状態となるので、上述の実施形態と同様にして気密空間内の気圧を下げれば、対象物から砒素を揮発させて分離除去することが可能である。また、水銀が含まれている汚染土に対しては、塩酸を加えることで該水銀を気化しやすくすることができる。
【0048】
また、本実施形態では、収容体内に気化促進剤を送り込むようにしたが、収容体内に密封する前に予め汚染土に添加混合するようにしてもよい。
【0049】
また、本実施形態では、減圧しても常温では気化しないが気化促進剤を加えることによって気化が促進される物質を対象としたが、気化促進剤を使用せずとも減圧下で揮発させることができる有害物質に対しても本発明を適用することができる。かかる構成によれば、有害物質の気化が速まるため、分離除去効率が著しく改善される。
【0050】
また、本実施形態では、気密性のシート11を用いて収容体3を構成したが、かかる構成に代えて図4(a)に示すように、剛性の高い、例えば鋼製の容器21を収容体とし、かかる容器21の内部を汚染土2を収容するための気密空間とするとともに、該容器21に排気管22を介して図1と同様の気液分離タンク6、真空ポンプ7及び捕集機器8を順次接続するようにしてもよい。
【0051】
かかる構成によれば、対象物である汚染土2に大気圧が作用すると有害物質の揮発が妨げられることが懸念される場合において、有害物質を対象物内からスムーズに揮発させることが可能となる。なお、この場合、同図(b)に示すように有孔の排気管23を用いてもよい。
【0052】
また、本実施形態では、収容体3を用いて気密空間を形成するようにしたが、実際に汚染された地盤を対象物とするならば、図5に示すように、地盤31内の汚染領域32を取り囲むようにして地中壁33を形成しその上部を気密シート若しくは剛性板34で覆って気密空間を形成するとともに、地中壁33に排気管35を貫通させて、気液分離タンク6、真空ポンプ7及び捕集機器8を順次接続するようにしてもよい。なお、地中壁33の下端については、必要に応じて適宜気密処理を行う。
【0053】
また、本実施形態では、気液分離タンク6、真空ポンプ7、捕集機器8の順で収容体3に接続したが、まず、気液分離タンクは、真空ポンプ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、真空ポンプと捕集機器との順序を入れ替えてもよい。
【0054】
また、本実施形態では、保護層としてサンドマットを採用したが、これに代えて、合板を気密性シートの上に載せて保護層としてもよいし、アスファルトやコンクリートで構成してもよい。一方、気密性シート自体に強度を持たせるようにすれば、あるいは対象物の重量等による破損のおそれがないのであれば、かかる保護層を省略してもよい。
【0055】
また、本実施形態では、通気体としてサンドマット9を採用したが、かかる通気体は、一定の上載圧が作用しても内部に空気や青酸ガスの通路が確保されるのであればどのようなものでもよく、例えば、砂や砂利を敷き均す代わりに、高分子系材料で形成された立体網目状マットを使用してもよい。また、敷き均された砂や砂利内に硬質塩化ビニル等で形成した有孔管を埋設して通気性をさらに向上させるようにしてもよい。
【0056】
なお、かかる通気体は、例えば、排気管の先端を分岐することによって対象物の広い範囲からシアンを排出することができるのであれば、あるいは、汚染土2が礫、砂利等を多く含んだ通気性の高いものであれば、これを省略してもよい。
【0057】
【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方法によれば、シアン等の有害物質を対象物から効率的に分離除去することが可能となり、該対象物を処分するための廃棄物処分場を設置する必要がなくなるとともに、水洗浄等の方法とは異なり、処理された土をすぐに再利用することも可能となる。
【0058】
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、シアン等の有害物質を対象物から効率的に分離除去することが可能となり、該対象物を処分するための廃棄物処分場を設置する必要がなくなるとともに、水洗浄等の方法とは異なり、処理された土をすぐに再利用することも可能となる。
【0059】
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、請求項2の効果に加えて、対象物に大気圧が作用すると有害物質の揮発が妨げられることが懸念される場合において、有害物質を対象物内からスムーズに揮発させることが可能となるという効果も奏する。
【0060】
また、請求項4に係る本発明の有害物質の分離除去装置によれば、請求項2の効果に加えて、有害物質は、気化促進剤による気化作用及び減圧による揮発作用に加えて大気圧の加圧作用によって収容体外部への排出が促進され、より効率的な分離除去が可能となる。また、保管や運搬の際に収容体をたたんでおくことができるという作用効果も得られる。
【0061】
【図面の簡単な説明】
【図1】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。
【図2】本実施形態に係る有害物質の分離除去装置を現場にて製作する手順を示した施工手順図。
【図3】本実施形態に係る有害物質の分離除去装置及び方法の作用を説明したグラフ。
【図4】変形例に係る有害物質の分離除去装置を示した断面図。
【図5】変形例に係る有害物質の分離除去方法を示した断面図。
【符号の説明】
1 有害物質の分離除去装置
2 汚染土(対象物)
3 収容体
4、22、23、35 排気管
7 真空ポンプ
8 捕集機器
9 サンドマット(通気体、保護層)
11、34 気密性のシート
21 鋼製容器(収容体)
33 地中壁(気密空間)
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method and apparatus for separating and removing various harmful substances such as cyan and arsenic contained in contaminated soil and industrial waste from the contaminated soil.
[0002]
[Prior art]
When foundation works are carried out at a factory site, substances such as cyan and arsenic may be carried in excavated soil. If such excavated soil is left as it is, cyanide and the like may diffuse into the environment via groundwater and the like, which may have a significant impact on the ecosystem.
[0003]
For this reason, such substances are treated as hazardous substances that should be closely monitored for diffusion to the environment together with mercury, cadmium, organic neighbors, lead, hexavalent chromium, PCB, etc., and are controlled or blocked separately from general waste. Various measures must be taken, such as disposal at a type waste disposal site, insolubilization with a predetermined chemical, and recovery by energization.
[0004]
[Problems to be solved by the invention]
However, recently, it has become quite difficult to secure a waste disposal site from the viewpoint of environmental protection, and there has been a problem that there is no disposal site to be disposed of.
[0005]
On the other hand, insolubilization treatment, the treated soil may become a new industrial waste. In that case, as described above, a problem arises in terms of securing a disposal site. An energization period is required, and if it is an electrically neutral harmful substance, it is difficult to recover in the first place. In any case, a method for efficiently separating and removing harmful substances such as cyan and arsenic from contaminated soil has not yet been established.
[0006]
The present invention has been made in view of the above-described circumstances, and provides a method and apparatus for separating and removing harmful substances capable of efficiently separating and removing harmful substances such as cyan and arsenic from contaminated soil and the like. With the goal.
[0007]
[Means for Solving the Problems]
In order to achieve the above object, according to the method for separating and removing harmful substances according to the present invention, the object containing the harmful substances is sealed in an airtight space and predetermined vaporization promotion is performed on the object. And then volatilizing the harmful substance from within the object by lowering the atmospheric pressure in the hermetic space to cause a boiling point drop of the harmful substance, and removing the volatilized harmful substance from the outside of the hermetic space. In this method, the harmful substance is cyan and the vaporization accelerator is an acidic solution, or the harmful substance is arsenic and the vaporization accelerator is an acidic solution and an oxidizing agent.
[0008]
In addition, the hazardous substance separation / removal device according to the present invention is connected to an airtight container in which an object containing a hazardous substance is accommodated and an airtight space in the container, as described in claim 2. A storage tank in which a predetermined vaporization accelerator is stored; an exhaust pipe communicated with an airtight space in the container; a vacuum pump that draws out gas in the container through the exhaust pipe and lowers the atmospheric pressure; A collecting device connected to an upstream side or a downstream side of a vacuum pump for collecting harmful substances discharged from the container, wherein the vacuum pump is the vaporization accelerator by lowering the boiling point of the harmful substances due to a decrease in atmospheric pressure. A device for separating and removing harmful substances, which volatilizes the harmful substances from the object to which is added, and discharges the volatilized harmful substances to the outside of the container, wherein the harmful substances are cyan. Accelerator is of the acid solution, or toxic substances vaporized accelerator arsenic is an acidic solution and oxidizing agent.
[0009]
Moreover, the harmful substance separation / removal device according to the present invention is such that the container is formed of a rigid container.
[0010]
Moreover, the harmful substance separation / removal device according to the present invention is configured such that the container is configured by a sheet, and the sheet is configured to be sealed in a bag shape in a state where the object is stored.
[0011]
In the method for separating and removing toxic substances according to the present invention, the object containing the toxic substances is sealed in the airtight space, and a vaporization accelerator is added to the object. Lower. In this manner, in the airtight space, the harmful substance is easily vaporized by the action of the vaporization accelerator, and the boiling point of the harmful substance is lowered due to the decrease in air pressure. Therefore, the harmful substance is volatilized from within the object. Therefore, by discharging this to the outside of the airtight space, harmful substances contained in the object are separated and removed. Even after the air is removed, the gas in the airtight space, that is, the volatilized harmful substance is removed and the reduced pressure state is maintained, so that the harmful substance in the object is continuously volatilized.
[0012]
Objects that contain toxic substances are mainly contaminated soil, but slag, incinerated ash, sludge, concrete waste, plastic waste, waste wood, etc. are also included.
[0013]
The harmful substance in the present invention is an acidic solution among substances whose vaporization is promoted under a reduced pressure, particularly in a state of almost vacuum of several mmHg or less, by adding a vaporization accelerator, even if the pressure is reduced, but does not vaporize at room temperature. Cyanide that volatilizes as a cyanide gas by adding, or arsenic that volatilizes as an arsine gas by adding an acidic solution and adding an oxidizing agent to increase the oxidation-reduction potential. Here, in the case of cyan, an acidic solution is a vaporization accelerator, and in the case of arsenic, an acidic solution and an oxidizing agent are vaporization accelerators.
[0015]
How to form the airtight space is arbitrary. For example, the internal space of the airtight container may be an airtight space, and an object such as excavated earth and sand may be put into the airtight container. If the soil is actually contaminated, the underground wall may be formed so as to surround the contaminated area, and the airtight space may be formed by covering the upper part with an airtight sheet.
[0016]
The air pressure in the airtight space is desirably set to be equal to or lower than the vapor pressure of the harmful substance at the temperature in the space with the vaporization accelerator added. If the atmospheric pressure is lowered to this level, harmful substances contained in the object volatilize immediately in combination with the action of the vaporization accelerator. It is not always necessary to lower the vapor pressure of the harmful substance described above, and although the efficiency is slightly reduced, a considerable volatilization effect can be expected if the pressure is close to the vapor pressure.
[0017]
In the hazardous substance separation / removal device according to the present invention, first, an object containing the harmful substance is charged and sealed in an airtight container, and a vaporization accelerator stored in a storage tank is sent into the container. Add in the object. Next, the air in the container is evacuated by a vacuum pump through the exhaust pipe, and the air pressure is lowered.
[0018]
In this manner, in the airtight space, the harmful substance is easily vaporized by the action of the vaporization accelerator, and the boiling point of the harmful substance is lowered due to the decrease in air pressure. Therefore, the harmful substance is volatilized from within the object. Therefore, this is discharged to the outside of the airtight space and further collected by a collecting device. Even after the air is removed, the gas in the airtight space, that is, the volatilized harmful substance is removed and the reduced pressure state is maintained, so that the harmful substance in the object is continuously volatilized.
[0019]
The explanation regarding the harmful substance, the object containing it, and the atmospheric pressure is the same as described above, and is omitted here.
[0020]
As an airtight container, any structure that can withstand the atmospheric pressure from the outside can be used as long as the internal vacuum state can be substantially maintained. If there is a concern that the volatilization of harmful substances from the object will be hindered, if the container is configured with a rigid container, atmospheric pressure will not act on the object. Volatilizes smoothly.
[0021]
On the other hand, if there is no risk that volatilization of harmful substances will be prevented even if atmospheric pressure acts on the object, for example, if the object is contaminated soil containing a lot of gravel and gravel, the container is covered with a sheet. If configured, and the sheet is configured to be sealed in a bag shape in a state in which the object is accommodated, a pressurizing action is added to the volatilizing action according to the present invention, and more efficient separation and removal are possible. In addition, since the container is a sheet, the effect of being able to be folded during storage and transportation is also obtained.
[0022]
In addition, when using the airtight sheet, after expanding it and placing the object, it is sealed in a bag shape so as to wrap the object, and then the air inside the container is drawn out as described above and harmful substances May be removed by volatilization. The airtight sheet can be arbitrarily selected from materials such as nylon, vinylon, and polyester tarpaulin.
[0023]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of a method and apparatus for separating and removing harmful substances according to the present invention will be described below with reference to the accompanying drawings.
[0024]
FIG. 1 is an overall perspective view showing a hazardous substance separation and removal apparatus according to this embodiment. As can be seen in the figure, the hazardous substance separation / removal device 1 according to the present embodiment includes an airtight container 3 in which contaminated soil 2 as an object containing cyan, which is a harmful substance, is accommodated, and the accommodation. A storage tank 5 that is connected to an airtight space in the body through a supply pipe 17 and stores an acidic solution that is a vaporization accelerator, an exhaust pipe 4 that is disposed through the container 3, and gas-liquid separation in the exhaust pipe It consists of a vacuum pump 7 connected via a tank 6 and a collecting device 8 connected downstream of the vacuum pump. The vacuum pump 7 changed from cyan in the container 3 by the addition of an acidic solution. Hydrocyanic acid is volatilized as a hydrocyanic acid gas by lowering the atmospheric pressure by pulling out the gas in the container through the exhaust pipe 4 and lowering the atmospheric pressure in the container 3, and further containing the volatilized hydrocyanic acid gas Drain outside the body 3 It has become the jar.
[0025]
The airtight container 3 is formed by wrapping an airtight sheet 11 formed of a material such as nylon, vinylon, polyester tarpaulin or the like in a bag shape in a state of containing contaminated soil 2 as will be described later, followed by adhesion, welding, or the like. It is good to seal and constitute by this method.
[0026]
The exhaust pipe 4 can be made of, for example, hard vinyl chloride, and the tip portion where a large number of holes 16 are formed is embedded in a sand mat 9 installed at the bottom of the container 3. The air inside the container 3 that has passed through the mat and the hydrocyanic acid gas from the contaminated soil 2 are sucked from the holes 16.
[0027]
That is, the sand mat 9 serves as a so-called vent for smoothly discharging air and hydrocyanic acid gas without clogging the holes 16 with the contaminated soil 2, and is contained in the weight of the contaminated soil 2 and the soil. It also serves as a protective layer that prevents the airtight sheet 11 from being broken by protrusions such as gravel.
[0028]
The gas-liquid separation tank 6 is provided with a barometer 10 so that the pressure inside the communicating container 3 can be measured. A drain cock 12 is provided near the bottom of the tank, and a valve 13 is provided. By opening the cock in a closed state, the water evaporated from the contaminated soil 2 and accumulated in the gas-liquid separation tank 6 can be drained. In addition, when the hydrocyanic acid gas volatilized from the contaminated soil 2 is dissolved in such water, the water is extracted while being maintained in an airtight state.
[0029]
The collection device 8 is a device for collecting and recovering hydrocyanic acid gas, which is a harmful substance, from the gas discharged from the vacuum pump 7, and the inside thereof is filled with activated carbon for adsorbing the hydrocyanic acid gas. . Although a small amount of hydrocyanic acid gas may be released from the exhaust port to the atmosphere without being adsorbed in the collection device 8, in such a case, the exhaust port of the collection device 8 is connected to a heating combustion furnace. In the combustion furnace, it is preferable to burn the hydrocyanic acid gas and decompose it into nitrogen, carbon dioxide and water to make it non-toxic.
[0030]
In order to manufacture the harmful substance separation and removal apparatus 1 according to the present embodiment on site, first, as shown in FIG. 2 (a), an airtight sheet 11 is spread on the ground, and a sand mat 9 is placed thereon. In addition, the tip of the exhaust pipe 4 is embedded in the mat.
[0031]
Next, as shown in FIG. 4B, the contaminated soil 2 is piled on the sand mat 9, and the tip of the supply pipe 17 is embedded in the contaminated soil.
[0032]
Next, the edge of the airtight sheet 11 is lifted to wrap the sand mat 9 and the contaminated soil 2 in a bag shape. Then, the edges 3 are overlapped and bonded and sealed by a method such as welding or adhesion to form a container 3 having an airtight space formed therein as shown in FIG.
[0033]
Finally, the storage tank 5 is connected to the supply pipe 17, and the gas-liquid separation tank 6, the vacuum pump 7, and the collecting device 8 are sequentially connected to the exhaust pipe 4 as shown in FIG.
[0034]
In order to separate and remove cyan from the contaminated soil 2 using the separation and removal apparatus 1 assembled in this way, first, the acidic solution in the storage tank 5 is sent into the container 3 to adjust the pH of the contaminated soil 2. Reduce. In this way, cyan in the contaminated soil 2 changes to hydrocyanic acid in an acidic environment, and is easily vaporized as a cyanide gas.
[0035]
In this state, the vacuum pump 7 is operated to evacuate the air in the container 3 to lower the air pressure in the container. In order to lower the air pressure, it is desirable to operate the vacuum pump 7 so that the air pressure in the container 3 is lower than the vapor pressure of hydrocyanic acid at the temperature in the container. Here, assuming that the vapor pressure curve of hydrocyanic acid is approximately as shown in FIG. 3, when the temperature is 10 ° C., the atmospheric pressure in the container may be lowered to about 100 mmHg or less. Further, if it is further lowered to several mmHg, it is possible to efficiently volatilize even those in the state where they are present in the interior of the soil particles or in the fine voids between the soil particles and are not easily separated. In the figure, the vapor pressure curves of kerosene, water, and ethyl alcohol are also shown for reference.
[0036]
When the air pressure in the container 3 is lowered in this way, the boiling point of hydrocyanic acid drops due to the decrease in air pressure in the container, and hydrocyanic acid in the contaminated soil 2 immediately volatilizes as hydrocyanic acid gas. 7 is sucked from the container 3 and sent to the collecting device 8, and the cyanating gas is adsorbed and collected by the collecting device.
[0037]
Even after the air is removed, the cyanide in the contaminated soil 2 is continuously volatilized by removing the gas in the airtight space, that is, the volatilized cyanate gas, and maintaining the reduced pressure state.
[0038]
The time for operating the vacuum pump 7 is appropriately adjusted depending on how much cyan is desired to be removed. Once the air pressure is lowered to a predetermined level, it is sufficient to operate the vacuum pump 7 intermittently or with reduced output so that the pressure is reduced by the pressure increase due to the hydrocyanic acid gas volatilized in the container 3. .
[0039]
When the cyan in the contaminated soil 2 is separated and removed to a desired degree, the vacuum pump 7 is stopped, the airtight sheet 11 is opened, and the treated soil is taken out from the sheet. The treated soil may be used as an embankment material, for example.
[0040]
As described above, according to the method and apparatus for separating and removing harmful substances according to the present embodiment, cyanide is easily changed to hydrocyanic acid by the addition of an acidic solution, and in this state, hydrocyanic acid is reduced by reducing the atmospheric pressure. By lowering the boiling point of, cyanide can be immediately volatilized from the contaminated soil 2 as cyanuric acid gas and discharged to the outside of the container 3.
[0041]
This makes it possible to efficiently separate and remove extremely toxic cyan from the contaminated soil, eliminating the need for a waste disposal site for disposing of the contaminated soil. Moreover, unlike the water washing which requires dehydration after the treatment, the treated soil can be reused immediately.
[0042]
Further, since the vacuum pump 7 is operated so that the atmospheric pressure in the container 3 is equal to or lower than the vapor pressure of hydrocyanic acid at the temperature in the container, cyan contained in the contaminated soil 2 is in the form of cyanide gas. It can be volatilized immediately and the cyan content in the contaminated soil can be reduced in a short time.
[0043]
Further, since the container 3 is composed of the airtight sheet 11, the atmospheric pressure acts on the contaminated soil 2 through the sheet. Therefore, the cyanide contained in the contaminated soil 2 is added to the volatilization action caused by the vaporization accelerator and the reduced pressure, and the pressurization action due to the atmospheric pressure is added, the discharge to the outside of the container 3 is promoted, and more efficient separation and removal is possible It becomes. Moreover, since the container 3 is the sheet | seat 11, the effect that it can be folded in the case of storage or conveyance is also acquired.
[0044]
Moreover, since the sand mat 9 as a protective layer is provided at the bottom of the container 3, even if the weight of the contaminated soil 2 is large or the contaminated soil includes protrusions, the container 3 is There is no damage. Therefore, the container 3 can be diverted.
[0045]
Further, since the exhaust pipe 4 is embedded in the sand mat 9, there is no possibility that the holes 16 formed in the pipe are blocked with the contaminated soil 2 to prevent the discharge of air and cyan, and the contaminated soil. Cyan can be volatilized from a wide range of 2.
[0046]
In the present embodiment, the object for separating and removing harmful substances is contaminated soil, but the object of the present invention is not limited to such contaminated soil, in addition to contaminated soil, slag, incinerated ash, sludge, Concrete waste, plastic waste, waste wood, etc. may be the target.
[0047]
In the present embodiment, the harmful substance is cyan. However, the harmful substance referred to in the present invention is not limited to such a substance, and can be applied to, for example, arsenic. In such a configuration, if an acidic solution and an oxidizing agent are added as a vaporization accelerator to an object such as contaminated soil containing arsenic, arsenic is easily vaporized in the form of arsine gas. If the air pressure in the hermetic space is lowered in the same manner as described above, arsenic can be volatilized and removed from the object. Further, mercury can be easily evaporated by adding hydrochloric acid to contaminated soil containing mercury.
[0048]
Moreover, in this embodiment, although the vaporization promoter is sent into the container, it may be added to and mixed with the contaminated soil in advance before sealing the container.
[0049]
Further, in the present embodiment, a substance that does not vaporize at room temperature even under reduced pressure but is accelerated by adding a vaporization accelerator is targeted, but may be volatilized under reduced pressure without using a vaporization accelerator. The present invention can also be applied to possible harmful substances. According to such a configuration, since the vaporization of harmful substances is accelerated, the separation and removal efficiency is remarkably improved.
[0050]
Further, in this embodiment, the container 3 is configured using the airtight sheet 11, but instead of such a configuration, as shown in FIG. 4A, a container 21 made of, for example, steel, having high rigidity is accommodated. The inside of the container 21 is an airtight space for containing the contaminated soil 2, and the gas-liquid separation tank 6, the vacuum pump 7 and the collection device similar to those shown in FIG. You may make it connect the apparatus 8 sequentially.
[0051]
According to such a configuration, when it is feared that volatilization of the harmful substance is hindered when atmospheric pressure acts on the contaminated soil 2 as the target object, the harmful substance can be volatilized smoothly from within the target object. . In this case, a perforated exhaust pipe 23 may be used as shown in FIG.
[0052]
In the present embodiment, the airtight space is formed using the container 3. However, if the actually contaminated ground is an object, the contaminated area in the ground 31 is shown in FIG. An underground wall 33 is formed so as to surround 32, and an upper part thereof is covered with an airtight sheet or a rigid plate 34 to form an airtight space, and an exhaust pipe 35 is passed through the underground wall 33, so that the gas-liquid separation tank 6 The vacuum pump 7 and the collecting device 8 may be sequentially connected. In addition, about the lower end of the underground wall 33, an airtight process is performed suitably as needed.
[0053]
In this embodiment, the gas-liquid separation tank 6, the vacuum pump 7, and the collecting device 8 are connected to the container 3 in this order. First, the gas-liquid separation tank may be a so-called dry type vacuum pump. For example, this may be omitted, and the order of the vacuum pump and the collection device may be changed.
[0054]
In the present embodiment, a sand mat is used as the protective layer, but instead, a plywood may be placed on the airtight sheet to form the protective layer, or may be made of asphalt or concrete. On the other hand, if the airtight sheet itself is given strength, or if there is no risk of damage due to the weight of the object, the protective layer may be omitted.
[0055]
Further, in the present embodiment, the sand mat 9 is adopted as a ventilation body. However, such a ventilation body can be any type as long as a passage for air or hydrocyanic acid gas is secured inside even if a constant overpressure is applied. For example, instead of spreading sand and gravel, a three-dimensional mesh mat formed of a polymer material may be used. In addition, a perforated pipe made of hard vinyl chloride or the like may be embedded in the leveled sand or gravel to further improve the air permeability.
[0056]
In addition, such a ventilation body, for example, can discharge cyan from a wide range of the object by branching the tip of the exhaust pipe or the ventilation soil 2 contains a lot of gravel, gravel, etc. This may be omitted if it has high properties.
[0057]
【The invention's effect】
As described above, according to the method for separating and removing harmful substances of the present invention according to claim 1, it becomes possible to efficiently separate and remove harmful substances such as cyan from the object, and dispose of the object. Therefore, unlike the methods such as water washing, the treated soil can be reused immediately.
[0058]
Moreover, according to the hazardous substance separation / removal apparatus of the present invention according to claim 2, it becomes possible to efficiently separate and remove harmful substances such as cyan from the object, and waste for disposing of the object. There is no need to install a disposal site, and unlike the methods such as water washing, the treated soil can be reused immediately.
[0059]
Further, according to the hazardous substance separation and removal apparatus of the present invention according to claim 3, in addition to the effect of claim 2, there is a concern that the volatilization of harmful substances may be hindered when atmospheric pressure acts on the object. In this case, it is possible to smoothly volatilize harmful substances from the inside of the object.
[0060]
According to the harmful substance separation / removal device of the present invention according to claim 4, in addition to the effect of claim 2, the harmful substance has an atmospheric pressure in addition to the vaporization action by the vaporization accelerator and the volatilization action by the reduced pressure. Discharge to the outside of the container is promoted by the pressurizing action, and more efficient separation and removal are possible. Moreover, the effect that the container can be folded in the case of storage and conveyance is also acquired.
[0061]
[Brief description of the drawings]
FIG. 1 is an overall perspective view of a hazardous substance separation and removal apparatus according to an embodiment of the present invention.
FIG. 2 is a construction procedure diagram showing a procedure for producing a hazardous substance separation / removal device according to the present embodiment on site;
FIG. 3 is a graph illustrating the operation of the hazardous substance separation and removal apparatus and method according to the present embodiment.
FIG. 4 is a cross-sectional view showing a hazardous substance separation and removal apparatus according to a modification.
FIG. 5 is a sectional view showing a method for separating and removing harmful substances according to a modification.
[Explanation of symbols]
1 Separation and removal equipment for hazardous substances 2 Contaminated soil (object)
3 Container 4, 22, 23, 35 Exhaust pipe 7 Vacuum pump 8 Collection device 9 Sandmat (vent, protective layer)
11, 34 Airtight sheet 21 Steel container (container)
33 Underground wall (airtight space)

Claims (4)

有害物質を含んだ対象物を気密空間内に密封するとともに該対象物に所定の気化促進剤を添加し、次いで、前記気密空間内の気圧を下げて前記有害物質の沸点降下を生じさせることにより前記対象物内から前記有害物質を揮発させるとともに、揮発した有害物質を前記気密空間の外部に排出する有害物質の分離除去方法であって、有害物質がシアンで気化促進剤が酸性溶液、又は有害物質が砒素で気化促進剤が酸性溶液及び酸化剤であることを特徴とする有害物質の分離除去方法。  By sealing an object containing a toxic substance in an airtight space and adding a predetermined vaporization accelerator to the object, and then lowering the atmospheric pressure in the airtight space to cause a boiling point drop of the toxic substance A method for separating and removing a harmful substance that volatilizes the harmful substance from the object and discharges the volatilized harmful substance to the outside of the airtight space, wherein the harmful substance is cyan and the vaporization accelerator is an acidic solution or harmful A method for separating and removing harmful substances, wherein the substance is arsenic and the vaporization accelerator is an acidic solution and an oxidizing agent. 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接続され所定の気化促進剤が貯留された貯留タンクと、前記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、前記真空ポンプは、気圧低下による前記有害物質の沸点降下によって前記気化促進剤が添加された前記対象物内から前記有害物質を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ようになっている有害物質の分離除去装置であって、有害物質がシアンで気化促進剤が酸性溶液、又は有害物質が砒素で気化促進剤が酸性溶液及び酸化剤であることを特徴とする有害物質の分離除去装置。  An airtight container that contains an object containing a harmful substance, a storage tank that is connected to an airtight space in the container and stores a predetermined vaporization accelerator, and an airtight space in the container. An exhaust pipe, a vacuum pump that draws out the gas in the container through the exhaust pipe and lowers the atmospheric pressure, and is connected to an upstream side or a downstream side of the vacuum pump to capture harmful substances discharged from the container. The vacuum pump is configured to volatilize the harmful substance and volatilize the harmful substance from the object to which the vaporization accelerator is added by lowering the boiling point of the harmful substance due to a decrease in atmospheric pressure. A device for separating and removing harmful substances to be discharged to the outside of the container, wherein the harmful substances are cyan and the vaporization accelerator is an acidic solution, or the harmful substances are arsenic and the vaporization accelerator is an acidic solution and an acid. Separation apparatus for removing harmful substances, which is a drug. 前記収容体を剛体容器で構成した請求項2記載の分離除去装置。  The separation / removal device according to claim 2, wherein the container is formed of a rigid container. 前記収容体をシートで構成し、該シートを前記対象物を収容した状態で袋状に密封自在に構成した請求項2記載の分離除去装置。  The separation / removal device according to claim 2, wherein the container is constituted by a sheet, and the sheet is configured to be sealed in a bag shape in a state where the object is accommodated.
JP20377797A 1997-07-14 1997-07-14 Method and apparatus for separating and removing harmful substances Expired - Fee Related JP4009883B2 (en)

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