JP2003181437A - Method for thermally decontaminating soil polluted with dioxins - Google Patents
Method for thermally decontaminating soil polluted with dioxinsInfo
- Publication number
- JP2003181437A JP2003181437A JP2001383872A JP2001383872A JP2003181437A JP 2003181437 A JP2003181437 A JP 2003181437A JP 2001383872 A JP2001383872 A JP 2001383872A JP 2001383872 A JP2001383872 A JP 2001383872A JP 2003181437 A JP2003181437 A JP 2003181437A
- Authority
- JP
- Japan
- Prior art keywords
- dxn
- polluted
- dioxins
- soil
- 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.)
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- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、焼却炉解体廃棄
物やこれを含むダイオキシン類汚染土壌の浄化方法に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying incinerator demolition waste and dioxin-contaminated soil containing it.
【0002】[0002]
【従来の技術】昨今、ごみ焼却処分場周辺ではダイオキ
シン類(以下DXNと略記する)のような難水溶性有機
塩素化合物による土壌汚染が社会問題化し、焼却処分場
周辺土壌のDXN汚染がいくつか見付かっている。ま
た、ごみ焼却事業の広域化に伴い、老朽化した焼却設備
の解体が進められているが、焼却炉解体の際にDXNに
汚染された廃棄物が発生する。これら廃棄物またはこれ
を含む汚染土壌は掘削後保管されるケースが多いが、保
管に伴う汚染土壌の飛散などの二次汚染が生じる恐れが
ある。2. Description of the Related Art Recently, soil pollution due to poorly water-soluble organic chlorine compounds such as dioxins (hereinafter abbreviated as DXN) has become a social problem in the vicinity of a refuse incinerator, and DXN contamination in the soil around the incinerator is some. Found. In addition, with the spread of waste incineration business, the dismantling of aging incinerators is in progress, but when the incinerator is dismantled, DXN-contaminated waste is generated. These wastes or contaminated soil containing them are often stored after excavation, but secondary contamination such as scattering of contaminated soil may occur during storage.
【0003】[0003]
【発明が解決しようとする課題】この発明の課題は、上
記のような実状に鑑み、汚染土壌や廃棄物の保管に伴う
飛散などの二次汚染の恐れのないDXN汚染土壌の浄化
方法を提供することにある。SUMMARY OF THE INVENTION In view of the above situation, an object of the present invention is to provide a method for purifying DXN-contaminated soil which is free from the risk of secondary pollution such as scattering due to storage of contaminated soil or waste. To do.
【0004】[0004]
【課題を解決するための手段】この発明によるDXN汚
染土壌の浄化方法は、DXN汚染物を温度250〜70
0℃で加熱することを特徴とする方法である。A method for cleaning DXN-contaminated soil according to the present invention is a method for treating DXN-contaminated soil at a temperature of 250 to 70.
The method is characterized by heating at 0 ° C.
【0005】この方法に適用されるDXN汚染物は例え
ば焼却炉解体廃棄物またはこれを含む汚染土壌である。DXN pollutants applied to this method are, for example, incinerator demolition waste or contaminated soil containing it.
【0006】加熱温度は好ましくは400〜550℃で
ある。The heating temperature is preferably 400 to 550 ° C.
【0007】加熱雰囲気は、好ましくは空気雰囲気であ
る。The heating atmosphere is preferably an air atmosphere.
【0008】従来、DXNの分解には800℃以上の高
温が必要とされてきた。また、低温での分解には酸素欠
乏状態を維持することが反応の安定性のために必要とさ
れている。これらの原因として焼却炉飛灰中には数%の
重金属類が混在しており、それら重金属類の触媒作用に
よりDXNが再合成されることが挙げられる。しかし、
土壌中に存在する重金属量は飛灰量と比較して少なく、
DXN再合成の度合いも少ないことが考えられるため、
空気雰囲気での低温加熱処理を採用した。塩素化の程度
の低いDXNは300〜400℃で大部分が揮発するこ
とから二次燃焼などによるDXN分解を行えばよく、塩
素化の程度の高いものは脱塩素化反応や酸化反応により
分解される。そのため、低温度域での分解は装置材質の
高度化を必要としない、空気雰囲気は窒素ガス発生装置
などの付帯設備を必要としないなどの利点を有する。Conventionally, the decomposition of DXN has required a high temperature of 800 ° C. or higher. Further, maintaining the oxygen deficient state is required for decomposition at low temperature for the stability of the reaction. The cause of these is that several% of heavy metals are mixed in the fly ash of the incinerator, and DXN is resynthesized by the catalytic action of these heavy metals. But,
The amount of heavy metals present in soil is small compared to the amount of fly ash,
Since the degree of DXN resynthesis may be low,
Low temperature heat treatment in air atmosphere was adopted. DXN with a low degree of chlorination is mostly volatilized at 300 to 400 ° C, so DXN decomposition by secondary combustion or the like may be performed, and DXN with a high degree of chlorination is decomposed by a dechlorination reaction or an oxidation reaction. It Therefore, the decomposition in the low temperature range has advantages that the equipment material is not required to be sophisticated, and the air atmosphere does not require auxiliary equipment such as a nitrogen gas generator.
【0009】[0009]
【発明の実施の形態】つぎに、この発明を実施例により
具体的に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Next, the present invention will be specifically described with reference to Examples.
【0010】実施例1
DXN汚染土壌20gを入れた直径40mmのSUS管
を水平型管状炉により1時間加熱処理した。処理中はS
US管を1.7rpmで回転させ、窒素ガスを0.5N
m3 /h通気した。加熱処理温度は250、400、
550および700℃とした。所定時間後、処理土壌を
急冷し、DXN含有量を測定した。温度250℃での処
理では、処理前に土壌に含まれていたDXNの15%を
除去することができた。温度400、550および70
0℃では99%以上のDXNを除去することができた。
これらの結果を表1にまとめて示す。Example 1 A 40 mm diameter SUS tube containing 20 g of DXN-contaminated soil was heat-treated in a horizontal tubular furnace for 1 hour. S during processing
Rotate the US tube at 1.7 rpm and add 0.5N nitrogen gas.
Aerated with m 3 / h. The heat treatment temperature is 250, 400,
550 and 700 ° C. After a predetermined time, the treated soil was rapidly cooled and the DXN content was measured. The treatment at a temperature of 250 ° C. was able to remove 15% of DXN contained in the soil before the treatment. Temperatures 400, 550 and 70
At 0 ° C, 99% or more of DXN could be removed.
These results are summarized in Table 1.
【0011】[0011]
【表1】 [Table 1]
【0012】2) 窒素ガスを、これを同じ流量で供給
する空気に置き代えた以外、実施例1と同様の操作を行
った。2) The same operation as in Example 1 was performed except that the nitrogen gas was replaced with air supplied at the same flow rate.
【0013】その結果、温度250℃での処理では、処
理前に土壌に含まれていたDXNの20%を除去するこ
とができた。温度400℃の処理では90%のDXNを
除去することができた。温度550および700℃では
99.9%以上のDXNを除去することができた。これ
らの結果を表2にまとめて示す。As a result, 20% of DXN contained in the soil before the treatment could be removed by the treatment at the temperature of 250 ° C. The treatment at a temperature of 400 ° C. was able to remove 90% of DXN. At the temperatures of 550 and 700 ° C., 99.9% or more of DXN could be removed. The results are summarized in Table 2.
【0014】[0014]
【表2】 [Table 2]
【0015】実施例3
この発明による低温加熱法によるダイオキシン類汚染土
壌の浄化方法の例を図1に示す。Example 3 FIG. 1 shows an example of a method for cleaning dioxins-contaminated soil by the low temperature heating method according to the present invention.
【0016】DXN汚染土壌はスクリーン(1) で処理さ
れた後、間接加熱キルン(2) に投入され、250〜70
0℃、好ましくは400〜550℃の温度で回転下に加
熱処理される。間接加熱キルン(2) の熱源は電気、蒸
気、化石燃料、熱媒体等である。発生した排ガスはつい
で二次燃焼炉(3) へ送られ、ここで800〜1000℃
で加熱され、ガス中の有機分、DXN等が完全燃焼され
る。次いで処理ガスは空気または水の注入により冷却さ
れた後、高温集塵器(4) へ送られる。ここへ消石灰が投
入され、300〜500℃で排ガス中のダストや有害物
が除去される。次いで、同ガスは脱硝触媒装置(8) に通
されて脱硝処理された後、熱交換器(5) で熱回収される
と共に排ガス中の水分が凝縮される。処理ガスは誘引通
風機(6) を経て煙突(7) から系外へ放出される。高温集
塵器(4) から出た灰分、ダスト等はダスト搬送装置(10)
で所定場所で送られる。間接加熱キルン(2) から出た浄
化土壌は冷却フィーダ(9) で所定置場へ送られる。After the DXN-contaminated soil is treated with the screen (1), it is thrown into the indirect heating kiln (2) to obtain 250-70.
It is heat-treated under rotation at a temperature of 0 ° C., preferably 400 to 550 ° C. The heat source of the indirect heating kiln (2) is electricity, steam, fossil fuel, heat medium, etc. The generated exhaust gas is then sent to the secondary combustion furnace (3), where it is 800-1000 ℃.
The gas is heated by, and the organic components, DXN, etc. in the gas are completely burned. Then, the treated gas is cooled by injecting air or water and then sent to the high temperature dust collector (4). Slaked lime is put in here, and dust and harmful substances in the exhaust gas are removed at 300 to 500 ° C. Next, the same gas is passed through a denitration catalyst device (8) and subjected to denitration treatment, after which heat is recovered in the heat exchanger (5) and water in the exhaust gas is condensed. The treated gas is discharged to the outside of the system from the chimney (7) through the induced draft fan (6). Dust transfer device (10) for ash, dust, etc. from the high temperature dust collector (4)
Will be sent in place. The purified soil discharged from the indirect heating kiln (2) is sent to the designated storage site by the cooling feeder (9).
【0017】[0017]
【発明の効果】DXN汚染物を窒素雰囲気または好まし
くは空気雰囲気で加熱処理することにより、DXN汚染
物からDXNを除去することができる。このとき処理温
度は高いほど好ましいが、空気雰囲気の場合DXN(T
EQ)除去率が90%以上必要なら400℃以上での処
理、99.6%以上必要なら550℃以上での処理、ま
た窒素雰囲気の場合DXN(TEQ)除去率が99%以
上必要なら400℃以上での処理、99.9%以上必要
なら550℃以上での処理を行うのが好ましい。INDUSTRIAL APPLICABILITY DXN can be removed from DXN contaminants by heat-treating the DXN contaminants in a nitrogen atmosphere or preferably an air atmosphere. At this time, the higher the processing temperature, the more preferable, but in the case of an air atmosphere, DXN (T
If the removal rate of EQ) is 90% or more, the treatment is 400 ° C or more, if it is 99.6% or more, the treatment is 550 ° C or more, and in the case of a nitrogen atmosphere, 400 ° C if the DXN (TEQ) removal rate is 99% or more. It is preferable to perform the above treatment, and if necessary 99.9% or more, the treatment at 550 ° C. or more.
【0018】この発明によれば、こうして、汚染土壌や
廃棄物の保管に伴う飛散などの二次汚染の恐れのないD
XN汚染土壌の浄化方法が提供される。According to the present invention, there is thus no risk of secondary pollution such as scattering due to storage of contaminated soil or waste.
A method for cleaning XN-contaminated soil is provided.
【図1】 この発明による低温加熱法によるダイオキシ
ン類汚染土壌の浄化方法の例を示すフローシートであ
る。FIG. 1 is a flow sheet showing an example of a method for cleaning dioxins-contaminated soil by the low temperature heating method according to the present invention.
(1) :スクリーン (2) :間接加熱キルン (3) :二次燃焼炉 (4) :高温集塵器 (5) :熱交換器 (6) :誘引通風機 (7) :煙突 (8) :脱硝触媒装置 (9) :冷却フィーダ (10):ダスト搬送装置 (1): Screen (2): Indirect heating kiln (3): Secondary combustion furnace (4): High temperature dust collector (5): Heat exchanger (6): Induction fan (7): Chimney (8): DeNOx catalyst device (9): Cooling feeder (10): Dust carrier
───────────────────────────────────────────────────── フロントページの続き (72)発明者 浜野 修史 大阪市住之江区南港北1丁目7番89号 日 立造船株式会社内 (72)発明者 梅村 省三 大阪市住之江区南港北1丁目7番89号 日 立造船株式会社内 Fターム(参考) 2E191 BA12 BB00 BB01 BD11 4D004 AA21 AA41 AB07 CA22 CA36 CC02 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Osamu Hamano 1-89 Minami Kohoku 1-89, Suminoe-ku, Osaka Standing Shipbuilding Co., Ltd. (72) Inventor Shozo Umemura 1-89 Minami Kohoku 1-89, Suminoe-ku, Osaka Standing Shipbuilding Co., Ltd. F-term (reference) 2E191 BA12 BB00 BB01 BD11 4D004 AA21 AA41 AB07 CA22 CA36 CC02
Claims (4)
00℃で加熱することを特徴とする加熱法によるダイオ
キシン類汚染土壌の浄化方法。1. Dioxin contaminants at a temperature of 250 to 7
A method for cleaning dioxin-contaminated soil by a heating method, which comprises heating at 00 ° C.
物またはこれを含む汚染土壌である請求項1記載の浄化
方法。2. The purification method according to claim 1, wherein the dioxin pollutant is incinerator demolition waste or contaminated soil containing the same.
項1または2記載の浄化方法。3. The purification method according to claim 1, wherein the heating temperature is 400 to 550 ° C.
〜3のいずれかに記載の浄化方法。4. The heating atmosphere is an air atmosphere.
~ The purification method according to any one of 3 to 3.
Priority Applications (1)
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JP2001383872A JP2003181437A (en) | 2001-12-18 | 2001-12-18 | Method for thermally decontaminating soil polluted with dioxins |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2001383872A JP2003181437A (en) | 2001-12-18 | 2001-12-18 | Method for thermally decontaminating soil polluted with dioxins |
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Publication Number | Publication Date |
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JP2003181437A true JP2003181437A (en) | 2003-07-02 |
Family
ID=27593748
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JP2001383872A Pending JP2003181437A (en) | 2001-12-18 | 2001-12-18 | Method for thermally decontaminating soil polluted with dioxins |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006263649A (en) * | 2005-03-25 | 2006-10-05 | Hitachi Zosen Corp | Organic halogen compound decomposition |
-
2001
- 2001-12-18 JP JP2001383872A patent/JP2003181437A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006263649A (en) * | 2005-03-25 | 2006-10-05 | Hitachi Zosen Corp | Organic halogen compound decomposition |
JP4639890B2 (en) * | 2005-03-25 | 2011-02-23 | 日立造船株式会社 | Decomposition method of organic halogen compounds |
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