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JP2002219444A - Purifying equipment of contaminated soil containing volatile organic compound - Google Patents

Purifying equipment of contaminated soil containing volatile organic compound

Info

Publication number
JP2002219444A
JP2002219444A JP2001014536A JP2001014536A JP2002219444A JP 2002219444 A JP2002219444 A JP 2002219444A JP 2001014536 A JP2001014536 A JP 2001014536A JP 2001014536 A JP2001014536 A JP 2001014536A JP 2002219444 A JP2002219444 A JP 2002219444A
Authority
JP
Japan
Prior art keywords
dust
volatile organic
heating
soil
heated
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.)
Pending
Application number
JP2001014536A
Other languages
Japanese (ja)
Inventor
Kazuhiro Yamada
和寛 山田
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.)
Nikko Co Ltd
Nikko KK
Original Assignee
Nikko Co Ltd
Nikko KK
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 Nikko Co Ltd, Nikko KK filed Critical Nikko Co Ltd
Priority to JP2001014536A priority Critical patent/JP2002219444A/en
Publication of JP2002219444A publication Critical patent/JP2002219444A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a purifying equipment of a contaminated soil where the contaminated soil containing a volatile organic compound is preferably treated by heating and purifying. SOLUTION: The contaminated soil containing the volatile organic compound is heated by a heating rotary kiln 1 to volatilize and separate or decompose the volatile organic compound and a dust in an exhaust gas discharged from the rotary kiln 1 is captured by an inertial dust separator 9 and a bag filter 10. A heavily condensed volatile organic compound is contained in this captured dust, which is supplied to a dust heating equipment 8 where the dust is heated to perform purification processing by volatilizing and separating or decomposing the volatile organic compound. A heated soil or a heated dust discharged from the kiln 1 or a dust heating equipment 18 is supplied to a soil water-cooling equipment 26 where water is flushed over the soil or the dust to cool it, thereby facilitating handling.

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、油分などの揮発性
有機化合物を含んだ汚染土壌を加熱して浄化処理する装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for heating and purifying contaminated soil containing volatile organic compounds such as oil.

【0002】[0002]

【従来の技術】近年、産業活動に伴って各事業所の敷地
内やその周辺地域の土壌が油等の揮発性有機化合物の廃
液によって汚染され、その土壌の地下を流れる地下水に
まで汚染が及んでいるといったことが取り沙汰されて問
題となっている。このように汚染された土壌を処理する
ために、その土壌を掘削して加熱用ロータリーキルンへ
投入し、土壌を揮発性有機化合物の沸点温度以上、例え
ば、揮発性有機化合物が灯油であれば沸点180〜30
0℃、重油であれば沸点350℃以上に加熱して土壌に
しみ込んでいる揮発性有機化合物を揮発分離または分解
させて土壌の浄化処理を行っている。
2. Description of the Related Art In recent years, soil in the premises of each business site and the surrounding area has been contaminated with waste liquid of volatile organic compounds such as oil due to industrial activities, and contaminated groundwater flowing under the soil. It has been a problem that it has been talked about. In order to treat the soil contaminated in this way, the soil is excavated and put into a rotary kiln for heating, and the soil is heated to the boiling point of the volatile organic compound or higher, for example, if the volatile organic compound is kerosene, the boiling point is 180. ~ 30
At 0 ° C., in the case of heavy oil, the boiling point is heated to 350 ° C. or higher, and volatile organic compounds permeating the soil are volatilized and separated or decomposed to purify the soil.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記装
置にて汚染土壌を加熱浄化したときに揮発性有機化合物
濃度を測定したところ、揮発性有機化合物濃度500P
PMの汚染土壌の加熱に際し、慣性集塵機にて捕捉した
ダストが1000PPM、またバグフィルターにて捕捉
したダストが3000PPMの高濃度となっており、ロ
ータリーキルンの排ガスに同伴して飛散するダスト分に
揮発性有機化合物が多く付着していることが判明した。
However, when the volatile organic compound concentration was measured when the contaminated soil was heated and purified by the above apparatus, the volatile organic compound concentration was 500 P.
When the PM contaminated soil is heated, the dust trapped by the inertial dust collector has a high concentration of 1000 PPM, and the dust trapped by the bag filter has a high concentration of 3000 PPM. It turned out that many organic compounds were attached.

【0004】本発明は上記の点に鑑み、揮発性有機化合
物を含む汚染土壌を好適に加熱浄化処理する汚染土壌の
浄化装置を提供することを課題とする。
[0004] In view of the above, an object of the present invention is to provide an apparatus for purifying contaminated soil containing a volatile organic compound by suitably heating and purifying the contaminated soil.

【0005】[0005]

【課題を解決するための手段】本発明は上記の課題を解
決するために、請求項1記載の揮発性有機化合物を含む
汚染土壌の浄化装置にあっては、揮発性有機化合物を含
む汚染土壌を加熱処理するバーナを備えた加熱用ロータ
リーキルンと、該加熱用ロータリーキルンから導出され
る排ガス中のダストを捕捉する集塵機とを少なくとも備
えるとともに、集塵機にて捕捉したダストを加熱してダ
スト中の揮発性有機化合物を加熱浄化処理するダスト加
熱手段を配設したことを特徴としている。
According to the present invention, there is provided an apparatus for purifying contaminated soil containing a volatile organic compound according to the present invention. A heating rotary kiln having a burner for heat treatment, and at least a dust collector for capturing dust in the exhaust gas derived from the heating rotary kiln, and heating the dust captured by the dust collector to remove volatile matter in the dust. Dust heating means for heating and purifying organic compounds is provided.

【0006】また、請求項2記載の揮発性有機化合物を
含む汚染土壌の浄化装置にあっては、揮発性有機化合物
を含む汚染土壌を加熱処理するバーナを備えた加熱用ロ
ータリーキルンと、該加熱用ロータリーキルンから導出
される排ガス中のダストを捕捉する集塵機とを少なくと
も備えるとともに、集塵機にて捕捉したダストを加熱用
ロータリーキルン内に投入して加熱土壌と混合させてダ
スト中の揮発性有機化合物を加熱浄化処理させるように
したことを特徴としている。
According to a second aspect of the present invention, there is provided an apparatus for purifying contaminated soil containing volatile organic compounds, wherein the heating rotary kiln includes a burner for heat-treating the contaminated soil containing volatile organic compounds; At least a dust collector that captures dust in exhaust gas derived from the rotary kiln is provided.The dust captured by the dust collector is put into a heating rotary kiln and mixed with heated soil to heat and purify volatile organic compounds in the dust. It is characterized by being processed.

【0007】また、請求項3記載の揮発性有機化合物を
含む汚染土壌の浄化装置にあっては、前記加熱用ロータ
リーキルンから排出される加熱土壌と集塵機にて捕捉し
て加熱浄化処理したダストに水を噴射して冷却する土壌
水冷手段を配設したことを特徴としている。
Further, in the apparatus for purifying contaminated soil containing a volatile organic compound according to claim 3, the heated soil discharged from the heating rotary kiln and the dust which has been captured by a dust collector and heated and purified are treated with water. It is characterized in that soil water cooling means for injecting and cooling water is provided.

【0008】[0008]

【発明の実施の形態】本発明の請求項1記載の揮発性有
機化合物を含む汚染土壌の浄化装置によれば、揮発性有
機化合物を含む汚染土壌を加熱用ロータリーキルンに供
給してバーナの熱風にて加熱して揮発性有機化合物を揮
発分離または分解させる。そして、ロータリーキルンの
排ガスに同伴して飛散する高濃度の揮発性有機化合物を
含むダストを下流の集塵機によって捕捉し、この捕捉し
たダストをダスト加熱装置に供給して加熱し、揮発性有
機化合物を揮発分離または分解し、ダストに付着する揮
発性有機化合物を浄化処理するのである。
According to the apparatus for purifying contaminated soil containing a volatile organic compound according to the first aspect of the present invention, the contaminated soil containing a volatile organic compound is supplied to a heating rotary kiln to generate hot air from a burner. To evaporate or separate volatile organic compounds. The dust containing high concentrations of volatile organic compounds scattered along with the exhaust gas from the rotary kiln is captured by a downstream dust collector, and the captured dust is supplied to a dust heating device and heated to volatilize the volatile organic compounds. It separates or decomposes and purifies volatile organic compounds attached to dust.

【0009】このように、高濃度の揮発性有機化合物を
含むダストを加熱して浄化処理するので、ダストを含め
た土壌がより効果的に浄化され、汚染土壌の浄化に好適
な装置となる。
As described above, since the dust containing a high concentration of volatile organic compounds is heated and purified, the soil including the dust is more effectively purified, and the apparatus is suitable for purifying the contaminated soil.

【0010】また、本発明の請求項2記載の揮発性有機
化合物を含む汚染土壌の浄化装置によれば、揮発性有機
化合物を含む汚染土壌を加熱用ロータリーキルンに供給
してバーナの熱風にて加熱し、揮発性有機化合物を揮発
分離または分解させる。そして、そして、ロータリーキ
ルンの排ガスに同伴して飛散する高濃度の揮発性有機化
合物を含むダストを下流の集塵機によって捕捉し、この
捕捉したダストをロータリーキルン内に投入して高温雰
囲気に晒すと共に加熱土壌と混合させてダストを加熱
し、ダスト中の揮発性有機化合物を揮発分離または分解
させる。
According to the apparatus for purifying contaminated soil containing a volatile organic compound according to claim 2 of the present invention, the contaminated soil containing the volatile organic compound is supplied to a rotary kiln for heating and heated by hot air from a burner. Then, volatile organic compounds are volatilized or separated. Then, dust containing high concentration of volatile organic compounds scattered along with the exhaust gas of the rotary kiln is captured by a downstream dust collector, and the captured dust is thrown into the rotary kiln, exposed to a high-temperature atmosphere and heated soil. The dust is heated by mixing, and volatile organic compounds in the dust are volatilized or separated.

【0011】このように、高濃度の揮発性有機化合物を
含むダストをロータリーキルンにて投入して高温雰囲気
に晒しながら加熱土壌と混合して浄化処理するので、別
途の加熱装置が不要となって低コストにてダスト中の揮
発性有機化合物を浄化でき、汚染土壌の浄化に好適な装
置となる。
As described above, dust containing a high concentration of volatile organic compounds is injected by a rotary kiln and mixed with the heated soil while being exposed to a high-temperature atmosphere for purification treatment. It is possible to purify volatile organic compounds in dust at a low cost, and the device is suitable for purifying contaminated soil.

【0012】また、本発明の請求項3記載の揮発性有機
化合物を含む汚染土壌の浄化装置によれば、加熱用ロー
タリーキルンから排出される加熱土壌と集塵機にて捕捉
して加熱浄化処理したダストを土壌水冷手段に供給し、
水を噴射して土壌温度を低下させると共に含水率を上昇
させている。これによって、土壌は取り扱いやすい状態
となり、コンベヤ等によって工場内の所定の堆積場所等
に難なく搬送することが可能となる。
Further, according to the apparatus for purifying contaminated soil containing a volatile organic compound according to claim 3 of the present invention, the heated soil discharged from the heating rotary kiln and the dust that has been heat-purified by being captured by a dust collector are collected. Supply to the soil water cooling means,
Water is sprayed to lower the soil temperature and raise the water content. As a result, the soil is in an easy-to-handle state, and can be transported by a conveyor or the like to a predetermined accumulation place in a factory without difficulty.

【0013】[0013]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0014】図1中の1は、油等の揮発性有機化合物に
よって汚染された土壌を掘削したものを加熱するロータ
リーキルンであって、内部に多数の掻上げ羽根を周設し
た円筒状のドラム2を回転自在に傾斜支持し、駆動装置
(図示せず)により所定の速度で回転させている。前記
ドラム2の一端には投入ホッパ3を、他端には排出ホッ
パ4を配設しており、投入ホッパ3側の配置した投入コ
ンベヤ5によって汚染土壌をドラム2内に投入し、掻上
げ羽根で掻上げながらドラム2内を転動流下させる間
に、排出ホッパ4側に配設したバーナ6から供給する熱
風によって汚染土壌を加熱して土壌中に含まれる揮発性
有機化合物を揮発分離または分解し、浄化された土壌を
排出ホッパ4の排出口7から排出するようにしている。
1 is a rotary kiln for heating excavated soil contaminated with volatile organic compounds such as oil. The rotary kiln has a cylindrical drum 2 having a number of scraping blades provided therein. Is rotatably inclined and supported at a predetermined speed by a driving device (not shown). A charging hopper 3 is disposed at one end of the drum 2 and a discharge hopper 4 is disposed at the other end. Contaminated soil is charged into the drum 2 by a charging conveyor 5 disposed on the side of the charging hopper 3, and a scraping blade is provided. The contaminated soil is heated by the hot air supplied from the burner 6 disposed on the discharge hopper 4 side while volatilizing and flowing down in the drum 2 while being scraped up, thereby volatilizing or separating volatile organic compounds contained in the soil. Then, the purified soil is discharged from the discharge port 7 of the discharge hopper 4.

【0015】ロータリーキルン1の投入ホッパ3上部に
は排ガスを導出する排気ダクト8を連結しており、該排
気ダクト8はその途中に排ガス中のダスト分を除去する
慣性集塵機9やバグフィルタ10等の集塵機を介在させ
ると共に、その下流に排ガスを吸引する排風機11を介
在させて脱臭炉12の入口側に連結している。
An exhaust duct 8 for discharging exhaust gas is connected to the upper part of the input hopper 3 of the rotary kiln 1. The exhaust duct 8 includes an inertial dust collector 9 and a bag filter 10 for removing dust in the exhaust gas. A dust collector is interposed, and an exhaust fan 11 that sucks exhaust gas is interposed downstream of the dust collector and connected to the inlet side of the deodorizing furnace 12.

【0016】脱臭炉12には炉内温度を所定値に維持す
るためのバーナ13を備えており、炉内に導入される排
ガスを高温雰囲気に晒すことによって排ガス中の揮発性
有機化合物を燃焼分解するようにしている。なお、脱臭
炉12は揮発性有機化合物が完全に燃焼分解できるよう
に、炉内温度を例えば、略750℃以上の高温を維持す
るようにバーナ13の燃焼量をコントロールすると共
に、排ガスが炉内を通過するのに少なくとも1乃至2秒
以上かかる程度の炉長さを確保することが好ましい。
The deodorizing furnace 12 is provided with a burner 13 for maintaining the furnace temperature at a predetermined value, and burns and decomposes volatile organic compounds in the exhaust gas by exposing the exhaust gas introduced into the furnace to a high-temperature atmosphere. I am trying to do it. The deodorizing furnace 12 controls the combustion amount of the burner 13 so that the volatile organic compounds can be completely burned and decomposed, and maintains the furnace temperature at, for example, a high temperature of about 750 ° C. or more. It is preferable to secure a furnace length such that it takes at least 1 to 2 seconds or more to pass through.

【0017】前記脱臭炉12から排出される排ガスは高
温であり、この排ガス熱を有効に利用するために、脱臭
炉12の出口側には熱交換器14を配設している。そし
て、熱交換器14には脱臭炉12のバーナ13に燃焼用
空気を供給するファン15の供給ダクト17を連結して
いる。熱交換器14を通過した脱臭炉12の排ガスは煙
突17より大気中に放出される。
The exhaust gas discharged from the deodorizing furnace 12 has a high temperature, and a heat exchanger 14 is provided at the outlet side of the deodorizing furnace 12 in order to effectively use the exhaust gas heat. The heat exchanger 14 is connected to a supply duct 17 of a fan 15 for supplying combustion air to the burner 13 of the deodorizing furnace 12. Exhaust gas from the deodorizing furnace 12 that has passed through the heat exchanger 14 is released into the atmosphere from a chimney 17.

【0018】また、慣性集塵機9及びバグフィルタ10
にて回収されるダストは適宜な搬送手段によってダスト
加熱装置18に供給される。ダスト加熱装置18はダス
ト中の揮発性有機化合物を加熱して揮発分離または分解
するもので、例えば、図1で示すような、ケーシング1
9内にスクリュー羽根20を周設した軸体21を貫通さ
せて両端部を回転自在に軸支し、駆動装置(図示せず)
にて所定速度で回転させると共に、ケーシング19の一
端に供給口22を、他端に排出口23を備え、かつ、ケ
ーシング19の周囲には電気ヒータ24を取り付けて加
熱保温できる構造としている。また、ケーシング19内
にてダスト加熱時に揮発するガスを抜き取る抜き取り口
25を備え、抜き取ったガスを排気ダクト8に導出させ
るようにしている。なお、前記電気ヒータ24に代えて
脱臭炉12から排出される高温の排ガスを利用しケーシ
ング19を加熱するようにしても良い。
The inertial dust collector 9 and the bag filter 10
The dust collected at is supplied to the dust heating device 18 by an appropriate transport means. The dust heating device 18 heats a volatile organic compound in dust to volatilize and separate or decompose the dust. For example, as shown in FIG.
A shaft 21 having a screw blade 20 provided therethrough penetrates through the shaft 9 to rotatably support both ends thereof, and a driving device (not shown)
, The casing 19 is provided with a supply port 22 at one end and a discharge port 23 at the other end, and an electric heater 24 is attached around the casing 19 so that the casing 19 can be heated and kept warm. In addition, the casing 19 is provided with an extraction port 25 for extracting a gas volatilized when the dust is heated, and the extracted gas is led to the exhaust duct 8. The casing 19 may be heated by using high-temperature exhaust gas discharged from the deodorizing furnace 12 instead of the electric heater 24.

【0019】加熱用ロータリーキルン1やダスト加熱装
置18から排出される土壌やダストは高温かつ乾燥して
いるために取り扱いにくいので、土壌水冷装置26に供
給して水を浴びせ、湿潤、冷却させて取り扱いやすいよ
うにする。この土壌水冷装置26は、例えば図1に示す
ように、ケーシング27内に撹拌羽根28を適宜間隔で
取り付けた軸体29を貫通させて両端部を回転自在に軸
支し、駆動装置(図示せず)にて所定速度で回転させる
ようにすると共に、ケーシング27の一端に土壌の供給
口30を、他端に排出口31を備えている。また、ケー
シング27には水噴射ノズル32を取り付け、図示しな
い水供給源から供給される水を加熱土壌に向けて噴射し
て加熱土壌を湿潤、冷却させるようにしており、水を浴
びた土壌は温度が低下すると共に埃が出にくい程度に含
水率を高めて取り扱いやすい状態となる。
Since the soil and dust discharged from the heating rotary kiln 1 and the dust heating device 18 are difficult to handle because they are hot and dry, they are supplied to the soil water cooling device 26 to be immersed in water, wet, cooled and handled. Make it easy. As shown in FIG. 1, for example, the soil water cooling device 26 has a shaft body 29 in which a stirring blade 28 is attached at an appropriate interval in a casing 27, and rotatably supports both ends thereof. ), The casing 27 is provided with a soil supply port 30 at one end and a discharge port 31 at the other end. Further, a water injection nozzle 32 is attached to the casing 27, and water supplied from a water supply source (not shown) is injected toward the heated soil to wet and cool the heated soil. As the temperature decreases, the moisture content is increased to such an extent that dust is less likely to come out, and the state becomes easy to handle.

【0020】しかして、上記装置にて揮発性有機化合物
を含んだ汚染土壌を処理するときには、先ず、投入コン
ベヤ5によって加熱用ロータリーキルン1の投入ホッパ
3側から揮発性有機化合物を含んだ汚染土壌をドラム2
内へ供給し、汚染土壌がドラム2内を転動流下する間に
バーナ6の熱風と接触させて揮発性有機化合物の沸点以
上に加熱し、汚染土壌中の揮発性有機化合物を揮発分離
または分解させる。
When treating the contaminated soil containing a volatile organic compound by the above-mentioned apparatus, first, the conveyed soil from the charging hopper 3 of the heating rotary kiln 1 is removed by the charging conveyor 5. Drum 2
While the contaminated soil is tumbling down the drum 2, the contaminated soil is brought into contact with the hot air of the burner 6 and heated to a temperature higher than the boiling point of the volatile organic compound to volatilize or separate the volatile organic compound in the contaminated soil. Let it.

【0021】ロータリーキルン1内にて排気される排ガ
スは下流の慣性集塵機9、バグフィルタ10に導かれて
ダスト分を捕捉された後、脱臭炉12へと導入され、脱
臭炉12内の高温ガスと接触してガス中の揮発性有機化
合物が完全に燃焼され、臭気やダイオキシン等も分解さ
れて無害となり、熱交換器14を通過して煙突17より
大気中に放出される。
Exhaust gas exhausted in the rotary kiln 1 is guided to a downstream inertial dust collector 9 and a bag filter 10 to capture dust, and then introduced into a deodorizing furnace 12, where high-temperature gas in the deodorizing furnace 12 is removed. Upon contact, the volatile organic compounds in the gas are completely burned, and odors and dioxins are also decomposed and rendered harmless, and pass through the heat exchanger 14 and are released into the atmosphere from the chimney 17.

【0022】また、ファン15から供給する燃焼用空気
は熱交換器14を通過する間に熱交換されて空気温度が
高められ、脱臭炉12のバーナ13に供給されて燃焼用
空気として使用される。
The combustion air supplied from the fan 15 exchanges heat while passing through the heat exchanger 14 to increase the air temperature, and is supplied to the burner 13 of the deodorizing furnace 12 to be used as combustion air. .

【0023】慣性集塵機9やバグフィルタ10にて回収
されたダストには高濃度の揮発性有機化合物が含まれて
おり、これを浄化処理するために、適宜の搬送手段によ
ってダスト加熱装置18に供給される。揮発性有機化合
物を含むダストは、ダスト加熱装置18の供給口22か
ら供給されてスクリュー21にて移送される間に、電気
ヒータ24によって揮発性有機化合物の沸点以上に加熱
されて排出口23より排出される。この加熱によってダ
スト中に含まれる揮発性有機化合物の多くは揮発分離ま
たは分解されると共に、揮発したガスは排気ダクト8を
経由して脱臭炉12に導かれて燃焼分解される。
The dust collected by the inertial dust collector 9 and the bag filter 10 contains a high concentration of volatile organic compounds, and is supplied to the dust heating device 18 by an appropriate conveying means in order to purify the volatile organic compounds. Is done. While the dust containing the volatile organic compound is supplied from the supply port 22 of the dust heating device 18 and transferred by the screw 21, the dust is heated to a temperature equal to or higher than the boiling point of the volatile organic compound by the electric heater 24 and is discharged from the discharge port 23. Is discharged. By this heating, most of the volatile organic compounds contained in the dust are volatilized and separated or decomposed, and the volatilized gas is led to the deodorizing furnace 12 via the exhaust duct 8 and burned and decomposed.

【0024】ロータリーキルン1から排出される加熱土
壌と、ダスト加熱装置18から排出されるダストは、土
壌水冷装置26へと導かれ、撹拌羽根28によって混合
されながら水噴射ノズル31から噴射する水を浴びて湿
潤、冷却されて温度が低下すると共に含水率を高めて取
り扱いやすい状態となる。
The heated soil discharged from the rotary kiln 1 and the dust discharged from the dust heating device 18 are guided to a soil water cooling device 26, and are bathed with water jetted from a water jet nozzle 31 while being mixed by a stirring blade 28. As a result, the temperature is lowered by being wet and cooled, and the water content is increased, so that the state becomes easy to handle.

【0025】このように、慣性集塵機9やバグフィルタ
10にて捕捉した高濃度の揮発性有機化合物を含むダス
トを加熱装置18にて加熱し、ダスト中の揮発性有機化
合物を揮発分離または分解して浄化処理するので、ダス
トを含めた土壌がより効果的に浄化される。
As described above, the dust containing a high concentration of volatile organic compounds captured by the inertial dust collector 9 and the bag filter 10 is heated by the heating device 18 to volatilize and separate or decompose the volatile organic compounds in the dust. The soil, including dust, is more effectively purified.

【0026】また、図2はダスト加熱手段として、熱交
換器を採用した他の実施例を示している。なお、図2に
おいて図1と同一符号は同一構成要素を示し、その説明
は省略する。
FIG. 2 shows another embodiment employing a heat exchanger as the dust heating means. 2, the same reference numerals as those in FIG. 1 denote the same components, and a description thereof will be omitted.

【0027】図中の33はダストを加熱するための熱供
給源であるバーナであって、該バーナは燃焼室34内に
火炎を形成して熱風を供給し、燃焼室34の出口に配設
した熱交換器35を通過させて煙突17へと排気するよ
うにしている。また、慣性集塵機9及びバグフィルタ1
0にて捕捉されたダストは、圧送ブロア36によりダク
ト37を介して熱交換器35へと送り込まれて加熱さ
れ、ダストに含まれる揮発性有機化合物を揮発分離また
は分解させる。そして熱交換器35を通過した加熱ダス
トはサイクロン集塵機38にて捕捉され、ロータリーキ
ルン1から排出される土壌と共に土壌水冷装置26へと
送り込まれて冷却される。また、サイクロン集塵機38
を通過した排気エアーは慣性集塵機9の手前の排気ダク
ト8へと回収される。
Reference numeral 33 in the drawing denotes a burner which is a heat supply source for heating the dust. The burner forms a flame in the combustion chamber 34 to supply hot air, and is disposed at the outlet of the combustion chamber 34. The heat is passed through the heat exchanger 35 and exhausted to the chimney 17. In addition, the inertial dust collector 9 and the bag filter 1
The dust captured at 0 is sent to the heat exchanger 35 via the duct 37 by the pressure blower 36 and heated, and volatilizes or separates or decomposes volatile organic compounds contained in the dust. The heated dust that has passed through the heat exchanger 35 is captured by the cyclone dust collector 38 and sent to the soil water cooling device 26 together with the soil discharged from the rotary kiln 1 to be cooled. In addition, cyclone dust collector 38
The exhaust air that has passed through is collected by the exhaust duct 8 in front of the inertial dust collector 9.

【0028】また、図3は慣性集塵機9やバグフィルタ
10にて捕捉した高濃度の揮発性有機化合物を含むダス
トをロータリーキルン1に投入して加熱浄化処理する装
置の実施例を示している。なお、図3において図1と同
一符号は同一構成要素を示し、その説明は省略する。
FIG. 3 shows an embodiment of an apparatus in which dust containing high-concentration volatile organic compounds captured by the inertial dust collector 9 or the bag filter 10 is charged into the rotary kiln 1 and subjected to heat purification treatment. In FIG. 3, the same reference numerals as those in FIG. 1 denote the same components, and a description thereof will be omitted.

【0029】図2中の39は、ロータリーキルン1の排
出ホッパ4を貫通して取り付けたダスト投入シュートで
あって、シュート排出端をドラム2の排出側付近に臨ま
せている。そして、慣性集塵機9やバグフィルタ10に
て捕捉した高濃度の揮発性有機化合物を含むダストをダ
スト投入シュート32を介してドラム2内投入し、ドラ
ム2内の高温雰囲気に晒すと共に高温に加熱した土壌と
混ぜ合わせることによってダストに含まれる揮発性有機
化合物を揮発分離または分解させるようにしている。
In FIG. 2, reference numeral 39 denotes a dust input chute which is attached through the discharge hopper 4 of the rotary kiln 1, and has a chute discharge end facing the discharge side of the drum 2. Then, dust containing a high-concentration volatile organic compound captured by the inertial dust collector 9 or the bag filter 10 was charged into the drum 2 via the dust charging chute 32, and was exposed to a high-temperature atmosphere in the drum 2 and heated to a high temperature. By mixing with soil, volatile organic compounds contained in dust are volatilized and separated or decomposed.

【0030】このように、慣性集塵機9やバグフィルタ
10にて捕捉した高濃度の揮発性有機化合物を含むダス
トをロータリーキルン1にて加熱するようにすれば、別
途の加熱装置が不要となり、低コストにてダストの浄化
処理を行える。
As described above, if the dust containing a high concentration of volatile organic compounds captured by the inertial dust collector 9 or the bag filter 10 is heated by the rotary kiln 1, no separate heating device is required, and the cost is reduced. Can be used to purify the dust.

【0031】[0031]

【発明の効果】以上のように本発明の請求項1記載の揮
発性有機化合物を含む汚染土壌の浄化装置によれば、揮
発性有機化合物を含む汚染土壌を加熱処理するバーナを
備えた加熱用ロータリーキルンと、該加熱用ロータリー
キルンから導出される排ガス中のダストを捕捉する集塵
機とを少なくとも備えるとともに、集塵機にて捕捉した
ダストを加熱してダスト中の揮発性有機化合物を加熱浄
化処理するダスト加熱手段を配設したので、高濃度の揮
発性有機化合物を含むダストを加熱して浄化処理でき、
ダストを含めた土壌がより効果的に浄化され、浄化装置
として好適な装置となる。
As described above, according to the apparatus for purifying contaminated soil containing volatile organic compounds according to the first aspect of the present invention, a heating apparatus provided with a burner for heat-treating contaminated soil containing volatile organic compounds is provided. Dust heating means comprising at least a rotary kiln and a dust collector for capturing dust in exhaust gas derived from the heating rotary kiln, and heating and purifying volatile organic compounds in the dust by heating the dust captured by the dust collector. , So that dust containing high concentrations of volatile organic compounds can be heated and purified,
The soil including dust is more effectively purified, and the device is suitable as a purification device.

【0032】また、請求項2記載の揮発性有機化合物を
含む汚染土壌の浄化装置によれば、揮発性有機化合物を
含む汚染土壌を加熱処理するバーナを備えた加熱用ロー
タリーキルンと、該加熱用ロータリーキルンから導出さ
れる排ガス中のダストを捕捉する集塵機とを少なくとも
備えるとともに、集塵機にて捕捉したダストを加熱用ロ
ータリーキルン内に投入して加熱土壌と混合させてダス
ト中の揮発性有機化合物を加熱浄化処理させるようにし
たので、低コストにて高濃度の揮発性有機化合物を含む
ダストを浄化処理でき、浄化装置として更に好適な装置
となる。
Further, according to the apparatus for purifying contaminated soil containing volatile organic compounds according to claim 2, a rotary kiln for heating provided with a burner for heat-treating contaminated soil containing volatile organic compounds, and the rotary kiln for heating And a dust collector that captures dust in the exhaust gas derived from the exhaust gas, and throws the dust captured by the dust collector into a heating rotary kiln and mixes it with the heated soil to heat and purify volatile organic compounds in the dust. As a result, dust containing a high concentration of volatile organic compounds can be purified at low cost, and the apparatus is more suitable as a purification apparatus.

【0033】また、請求項3記載の揮発性有機化合物を
含む汚染土壌の浄化装置によれば、前記加熱用ロータリ
ーキルンから排出される加熱土壌と集塵機にて捕捉して
加熱浄化処理したダストに水を噴射して冷却する土壌水
冷手段を配設したので、浄化処理した土壌は温度も低く
て埃も出ずに取り扱いやすい状態となり、コンベヤ等に
よって工場内の所定の堆積場所等に難なく搬送すること
も可能となる。
According to the apparatus for purifying contaminated soil containing a volatile organic compound according to the third aspect of the present invention, water is collected into the heated soil discharged from the heating rotary kiln and the dust which has been heated and purified by being collected by a dust collector. Soil water cooling means for cooling by spraying is provided, so the purified soil is low in temperature and easy to handle without dust, and it can be transported to a predetermined deposition site in a factory without difficulty by a conveyor etc. It becomes possible.

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

【図1】本発明に係る揮発性有機化合物を含む汚染土壌
の浄化装置の一実施例を示す概略説明図である。
FIG. 1 is a schematic explanatory view showing one embodiment of an apparatus for purifying contaminated soil containing a volatile organic compound according to the present invention.

【図2】本発明に係る揮発性有機化合物を含む汚染土壌
の浄化装置の他の実施例を示す概略説明図である。
FIG. 2 is a schematic explanatory view showing another embodiment of the apparatus for purifying contaminated soil containing a volatile organic compound according to the present invention.

【図3】本発明に係る揮発性有機化合物を含む汚染土壌
の浄化装置の他の実施例を示す概略説明図である。
FIG. 3 is a schematic explanatory view showing another embodiment of the apparatus for purifying contaminated soil containing a volatile organic compound according to the present invention.

【符号の説明】[Explanation of symbols]

1…加熱用ロータリーキルン 2…ドラム 6…バーナ 9…慣性集塵機 10…バグフィルタ 12…脱臭炉 18…ダスト加熱装置(ダスト加熱手段) 30…土壌水冷装置(土壌水冷手段) 32…水噴射ノズル 33…バーナ 35…熱交換器(ダスト加熱手段) 36…排気ダクト 38…サイクロン集塵機 39…ダスト投入
シュート
DESCRIPTION OF SYMBOLS 1 ... Rotary kiln for heating 2 ... Drum 6 ... Burner 9 ... Inertial dust collector 10 ... Bag filter 12 ... Deodorizing furnace 18 ... Dust heating apparatus (dust heating means) 30 ... Soil water cooling apparatus (soil water cooling means) 32 ... Water injection nozzle 33 ... Burner 35 heat exchanger (dust heating means) 36 exhaust duct 38 cyclone dust collector 39 dust chute

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】揮発性有機化合物を含む汚染土壌を加熱処
理するバーナを備えた加熱用ロータリーキルンと、該加
熱用ロータリーキルンから導出される排ガス中のダスト
を捕捉する集塵機とを少なくとも備えるとともに、集塵
機にて捕捉したダストを加熱してダスト中の揮発性有機
化合物を加熱浄化処理するダスト加熱手段を配設したこ
とを特徴とする揮発性有機化合物を含む汚染土壌の浄化
装置。
1. A heating rotary kiln provided with a burner for heat-treating contaminated soil containing volatile organic compounds, a dust collector for capturing dust in exhaust gas derived from the heating rotary kiln, and at least a dust collector An apparatus for purifying contaminated soil containing volatile organic compounds, comprising dust heating means for heating dust captured by heating to purify volatile organic compounds in the dust.
【請求項2】揮発性有機化合物を含む汚染土壌を加熱処
理するバーナを備えた加熱用ロータリーキルンと、該加
熱用ロータリーキルンから導出される排ガス中のダスト
を捕捉する集塵機とを少なくとも備えるとともに、集塵
機にて捕捉したダストを加熱用ロータリーキルン内に投
入して加熱土壌と混合させてダスト中の揮発性有機化合
物を加熱浄化処理させるようにしたことを特徴とする揮
発性有機化合物を含む汚染土壌の浄化装置。
2. A dust collector comprising at least a heating rotary kiln provided with a burner for heat-treating contaminated soil containing volatile organic compounds, and a dust collector for trapping dust in exhaust gas derived from the heating rotary kiln. The apparatus for purifying contaminated soil containing volatile organic compounds, wherein the trapped dust is put into a heating rotary kiln and mixed with the heated soil to heat and purify volatile organic compounds in the dust. .
【請求項3】前記加熱用ロータリーキルンから排出され
る加熱土壌と集塵機にて捕捉して加熱浄化処理したダス
トに水を噴射して冷却する土壌水冷手段を配設したこと
を特徴とする請求項1又は2記載の揮発性有機化合物を
含む汚染土壌の浄化装置。
3. A soil water cooling means for injecting water into the heated soil discharged from the heating rotary kiln and capturing and purifying the heated soil by a dust collector and cooling the dust is provided. Or a device for purifying contaminated soil containing the volatile organic compound according to item 2.
JP2001014536A 2001-01-23 2001-01-23 Purifying equipment of contaminated soil containing volatile organic compound Pending JP2002219444A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001014536A JP2002219444A (en) 2001-01-23 2001-01-23 Purifying equipment of contaminated soil containing volatile organic compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001014536A JP2002219444A (en) 2001-01-23 2001-01-23 Purifying equipment of contaminated soil containing volatile organic compound

Publications (1)

Publication Number Publication Date
JP2002219444A true JP2002219444A (en) 2002-08-06

Family

ID=18881221

Family Applications (1)

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

Country Link
JP (1) JP2002219444A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054706A (en) * 2005-08-23 2007-03-08 Nippon Road Co Ltd:The Heating and cleaning apparatus of contaminated soil
KR100847058B1 (en) 2007-12-10 2008-07-18 하상안 Polluted Soil Purification System
KR100916612B1 (en) * 2007-09-06 2009-09-14 한국건설기술연구원 Contaminated earth and sand purification device for heat washing combined use
JP2009226379A (en) * 2008-03-25 2009-10-08 Toshiba Corp Treatment method for contaminated soil
KR101104410B1 (en) * 2009-03-20 2012-01-16 주식회사 대일이앤씨 Purification Soil Chiller
KR101104406B1 (en) 2009-03-20 2012-01-16 주식회사 대일이앤씨 Thermal desorption device for purification of contaminated soil with predrying function
CN106140802A (en) * 2016-07-07 2016-11-23 华中科技大学 A kind of synchronous mode organic polluted soil microwave remediation device
CN108202080A (en) * 2018-02-27 2018-06-26 广东环境保护工程职业学院 A kind of soil Thermal desorption prosthetic appliance and method
CN108746181A (en) * 2018-08-22 2018-11-06 苏州三体智能科技有限公司 A kind of soil remediation equipment and its working method
CN108817062A (en) * 2018-06-28 2018-11-16 上海环境工程设计研究院有限公司 Indirect thermal desorption device for organic polluted soil showering

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04501378A (en) * 1988-10-29 1992-03-12 オー ウント カー オーレンスタイン ウント コツペル アクチエンゲゼルシヤフト Method and apparatus for treating contaminated soil
JPH05192648A (en) * 1991-07-22 1993-08-03 Linde Ag Method for decontaminating contaminated soil
JPH09501863A (en) * 1993-06-04 1997-02-25 フレセニウス ウムヴェルテヒニク ゲエムベハ Contaminated soil purification device and method
JP2000288527A (en) * 1999-04-05 2000-10-17 Tokuyama Corp Waste treatment method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04501378A (en) * 1988-10-29 1992-03-12 オー ウント カー オーレンスタイン ウント コツペル アクチエンゲゼルシヤフト Method and apparatus for treating contaminated soil
JPH05192648A (en) * 1991-07-22 1993-08-03 Linde Ag Method for decontaminating contaminated soil
JPH09501863A (en) * 1993-06-04 1997-02-25 フレセニウス ウムヴェルテヒニク ゲエムベハ Contaminated soil purification device and method
JP2000288527A (en) * 1999-04-05 2000-10-17 Tokuyama Corp Waste treatment method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007054706A (en) * 2005-08-23 2007-03-08 Nippon Road Co Ltd:The Heating and cleaning apparatus of contaminated soil
KR100916612B1 (en) * 2007-09-06 2009-09-14 한국건설기술연구원 Contaminated earth and sand purification device for heat washing combined use
KR100847058B1 (en) 2007-12-10 2008-07-18 하상안 Polluted Soil Purification System
JP2009226379A (en) * 2008-03-25 2009-10-08 Toshiba Corp Treatment method for contaminated soil
KR101104410B1 (en) * 2009-03-20 2012-01-16 주식회사 대일이앤씨 Purification Soil Chiller
KR101104406B1 (en) 2009-03-20 2012-01-16 주식회사 대일이앤씨 Thermal desorption device for purification of contaminated soil with predrying function
CN106140802A (en) * 2016-07-07 2016-11-23 华中科技大学 A kind of synchronous mode organic polluted soil microwave remediation device
CN108202080A (en) * 2018-02-27 2018-06-26 广东环境保护工程职业学院 A kind of soil Thermal desorption prosthetic appliance and method
CN108817062A (en) * 2018-06-28 2018-11-16 上海环境工程设计研究院有限公司 Indirect thermal desorption device for organic polluted soil showering
CN108746181A (en) * 2018-08-22 2018-11-06 苏州三体智能科技有限公司 A kind of soil remediation equipment and its working method

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