JP2000354841A - Solidification of incineration ash - Google Patents
Solidification of incineration ashInfo
- Publication number
- JP2000354841A JP2000354841A JP11167688A JP16768899A JP2000354841A JP 2000354841 A JP2000354841 A JP 2000354841A JP 11167688 A JP11167688 A JP 11167688A JP 16768899 A JP16768899 A JP 16768899A JP 2000354841 A JP2000354841 A JP 2000354841A
- Authority
- JP
- Japan
- Prior art keywords
- ash
- incinerated ash
- temperature
- slag
- sintering
- 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
Links
Landscapes
- Processing Of Solid Wastes (AREA)
- Fire-Extinguishing Compositions (AREA)
Abstract
(57)【要約】
【課題】 焼却灰に加圧を行いながら放電プラズ焼結処
理を施すことにより、灰中に含有されるダイオキシンの
分解、有害揮発物質(塩素、NOx、SOx、水銀等)
濃度の低減、及び重金属(Cr6+、Pb、Cu、Zn、
Cd、Hg)の溶出防止、分離除去が可能である焼却灰
の固化処理方法。
【解決手段】 (1)焼却灰を黒鉛型(ダイ)に充頃し
た後に圧力を2.94×108Paまで加圧し、ダイオ
キシンおよび揮発性物質を除去するため、プラズマの温
度を850℃前後まで一気に昇温し、850℃前後の温
度で5分程度保持する。(2)この焼却灰を焼結減容ス
ラグにするため、圧力を5.88×108Paまで加圧
し、さらに温度を1,100℃まで昇温し、この条件で
10分程度焼結処理を行う。(3)焼結処理後の焼却灰
の体積は約1/10以下に減容され、有毒揮発物質の除
去された固化成型スラグになる。(4)得られた固化成
型スラグに防水性、補強効果のあるコーティング液を塗
布する。
(57) [Summary] [PROBLEMS] Decomposition of dioxin contained in ash and harmful volatile substances (chlorine, NOx, SOx, mercury, etc.) by subjecting incinerated ash to discharge plasma sintering while applying pressure
Reduction of concentration and heavy metals (Cr 6+ , Pb, Cu, Zn,
A method for solidifying incinerated ash that can prevent elution of Cd and Hg) and can separate and remove the same. SOLUTION: (1) After filling incinerated ash into a graphite mold (die), the pressure is increased to 2.94 × 10 8 Pa to remove dioxins and volatile substances, and the plasma temperature is set to around 850 ° C. The temperature is raised at a stretch until the temperature is maintained at about 850 ° C. for about 5 minutes. (2) In order to convert the incinerated ash into slag with reduced sintering volume, the pressure was increased to 5.88 × 10 8 Pa, and the temperature was further increased to 1,100 ° C., and sintering was performed for about 10 minutes under these conditions. I do. (3) The volume of the incinerated ash after the sintering process is reduced to about 1/10 or less, and it becomes a solidified molded slag from which toxic volatile substances have been removed. (4) A coating liquid having a waterproof property and a reinforcing effect is applied to the obtained solidified molded slag.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、都市ゴミおよび放
射性ゴミなどの廃棄物の焼却によって生じる灰の最終処
分のための固化成型処理方法に関するものである。特
に、本発明は、焼却灰に放電プラズマ焼却処理を施すこ
とにより、焼却灰の体容積を約1/10以下に滅容化す
るこができ、しかも近年着目されているダイオキシンの
分解、NOx,SOx,水銀等の有毒揮発性物質濃度の
低減化を行い、地球環境保護・修復に寄与することがで
きる方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solidification molding method for final disposal of ash generated by incineration of waste such as municipal waste and radioactive waste. In particular, the present invention can reduce the body volume of incinerated ash to about 1/10 or less by subjecting the incinerated ash to discharge plasma incineration, and furthermore, has recently focused on decomposition of dioxin, NOx, The present invention relates to a method capable of reducing the concentration of toxic volatile substances such as SOx and mercury and contributing to protection and restoration of the global environment.
【0002】又、特に、本発明においては、放電プラズ
マ焼結温度を制御することにより、灰中に含有される重
金属の封じ込め、或いは溶融の選択が可能となる。さら
に本発明は、最終処分スラグを固化成型するまでの工程
が簡単であり、又スラグの固化成型後に表面にコーティ
ング処理を施すことにより、より安全な固化成型スラグ
を得ることができる方法に関するものである。In particular, in the present invention, by controlling the discharge plasma sintering temperature, it becomes possible to select the containment or melting of heavy metals contained in the ash. Furthermore, the present invention relates to a method in which the process up to solidifying and molding the final disposal slag is simple, and a more secure solidified molded slag can be obtained by applying a coating treatment to the surface after solidifying and molding the slag. is there.
【0003】[0003]
【従来の技術】従来のゴミの焼却灰の処理方法は、最終
処分地である埋立地に焼却灰と薬剤を混練して廃棄する
方法、あるいはセメントと飛灰を機械的に混練して廃棄
する方法、さらには高温で灰を溶かし、溶融スラグとし
てから埋立地に廃棄する方法があるが、一般的には焼却
灰に薬剤を混ぜて安定なキレート化合物にして廃棄、処
分する方式が主流である。2. Description of the Related Art Conventional refuse incineration ash treatment methods include a method in which incineration ash and a chemical are mixed and discarded in a landfill, which is a final disposal site, or a method in which cement and fly ash are mechanically kneaded and discarded. There is a method, and furthermore, a method of dissolving the ash at high temperature and disposing it as a molten slag and disposing it in a landfill, but in general the method of mixing and burning incinerated ash to make a stable chelate compound and disposing and disposing of it .
【0004】しかし、一部の埋立地においては遮水設
備、浸出水集水設備、灰貯蓄構造物等の欠陥、不備によ
り焼却灰からの有毒成分物質の溶出が問題化されてい
る。また、溶融固化法において溶融スラグと重金属を分
離し、処分する方法は工程そのものが複雑であり経済的
にも問題がある。However, in some landfills, leaching of toxic component substances from incinerated ash has been problematic due to defects and inadequacy of water shielding facilities, leachate water collecting facilities, ash storage structures and the like. In addition, the method of separating and disposing of molten slag and heavy metal in the melt-solidification method has a complicated process itself and is economically problematic.
【0005】更に、従来は、焼却灰埋立地に直接焼却灰
を廃棄処分するという方法が一般的であり、一部には埋
立地の構造物の不備等の理由によりそこから有毒物質成
分が漏洩していることが公表されている。しかし、各地
方自治体の立場上、まだ全部が明るみにされず、焼却灰
からの漏洩物質成分の種類および化学分析値は秘密事項
にされているのが現状である。一部の都道府県において
は焼却灰のコンクリート固化が行われているが、焼却灰
とコンクリートを一緒に固めるため、多量のコンクリー
トを必要とし、減量処理が不十分であった(最大コンク
リート50に対して焼却灰50程度)。また、従来の放
電プラズマ溶融法にしても、最終処分の安定スラグにす
るまでの工程が複雑であり、それに要する設備費がかな
り高い。Further, conventionally, a method of directly disposing of incineration ash in an incineration ash landfill is generally used, and in some cases, toxic substance components leak from the incineration ash because of inadequate structure of the landfill. It is publicly announced that However, from the standpoint of each local government, the whole has not yet been clarified, and at present, the types and chemical analysis values of the leaked substance components from incinerated ash are kept secret. In some prefectures, concrete of incinerated ash is solidified. However, in order to solidify incinerated ash and concrete together, a large amount of concrete was required, and the weight reduction treatment was insufficient (up to 50 concrete). About 50 incineration ash). In addition, even with the conventional discharge plasma melting method, the steps required to obtain a stable slag for final disposal are complicated, and the equipment cost required for this is considerably high.
【0006】[0006]
【発明が解決しようとする課題】そこで、本発明におい
ては、環境保全および公害防止のために、最終処分スラ
グをより安全で取り扱いが容易な固化成型体を得るため
のものである。SUMMARY OF THE INVENTION Therefore, in the present invention, in order to protect the environment and prevent pollution, it is an object of the present invention to obtain a solid molded product which is safer and easier to handle the final disposal slag.
【0007】[0007]
【課題を解決するための手段】そこで、本発明において
は、焼却灰に放電プラズマ焼却処理を施すことにより、
焼却灰自体に瞬間的に数1,000〜10,000℃の
局所的高温状態(放電柱=放電プラズマ)を得ることが
できる(焼却灰平均の温度は温度モニター検出器で表示
される)。この現象により、焼却灰中に含有されている
ダイオキシン類の分解、揮発性有毒物質の低減および除
去が瞬時に行え、さらに減容された安定なスラグに処理
できる。Therefore, in the present invention, the incineration ash is subjected to a discharge plasma incineration treatment,
A local high temperature of several thousand to 10,000 ° C. (discharge column = discharge plasma) can be instantaneously obtained in the incineration ash itself (the average temperature of the incineration ash is indicated by a temperature monitor detector). By this phenomenon, the decomposition of dioxins contained in the incineration ash, the reduction and removal of volatile toxic substances can be performed instantaneously, and the slag can be further processed into a reduced volume stable slag.
【0008】従来からある放電プラズマ溶融法は焼却灰
に圧力が加わらず、昇温の方法も間接加熱に近い。した
がって、焼却灰が減容化された安定なスラグに分別され
るまでには複雑な処理工程と多くの設備が必要である。In the conventional discharge plasma melting method, no pressure is applied to the incinerated ash, and the method of raising the temperature is similar to indirect heating. Therefore, complicated processing steps and many facilities are required before incinerated ash is separated into stable slag with reduced volume.
【0009】本発明においては、放電プラズマ焼結処理
温度を溶融点以下に調整して焼却灰を処理し、得られた
固化成型スラグに耐浸水性及び補強コーティング材を塗
布することにより、より安全、かつ取り扱い容易な減容
固化スラグが得られる。また、本発明においては、放電
プラズマ焼結処理温度を融点以上に調整して焼却灰を処
理することにより、得られたスラグ中の大部分の重金属
を取り除くことができる。In the present invention, the incineration ash is treated by adjusting the discharge plasma sintering treatment temperature to a melting point or lower, and the obtained solidified molded slag is coated with a water-resistant and reinforcing coating material, thereby providing a more secure. A volume-reduced solidified slag which is easy to handle is obtained. In the present invention, most of heavy metals in the obtained slag can be removed by treating the incinerated ash by adjusting the discharge plasma sintering treatment temperature to the melting point or higher.
【0010】さらに、本発明の固化処理方法を可燃性放
射性廃棄物の焼却灰処理の固化成型に用いることによ
り、焼却灰の減容化と放射性核種のスラグ内封じ込みが
より簡便になる。Furthermore, by using the solidification method of the present invention for solidification molding of incineration ash treatment of combustible radioactive waste, volume reduction of incineration ash and enclosing of radionuclides in slag become easier.
【0011】[0011]
【発明の実施の形態】(1)固化成型しようとする焼却
灰を黒鉛型(ダイ)に充頃し、真空引きした後に圧力を
2.94×108Paまで加圧する。ダイオキシンおよ
び揮発性物質を除去するため、プラズマの温度を850
℃前後まで一気に昇温する。850℃前後の温度で5分
程度保持する。その際には、焼却灰局部の温度は1,0
00℃以上になっている。次に、 (2)この焼却灰を焼結減容スラグにするため、圧力を
5.88×108Paまで加圧し、さらに温度を1,1
00℃まで昇温し、この条件で10分程度焼結処理を行
う。又、焼却灰中の重金属を除去するためには放電プラ
ズマ焼結処理温度を1,300〜1,400℃で15分
程度保持する。DESCRIPTION OF THE PREFERRED EMBODIMENTS (1) The incinerated ash to be solidified and formed is filled in a graphite die, and after evacuation, the pressure is increased to 2.94 × 10 8 Pa. The plasma temperature is set at 850 to remove dioxins and volatiles.
The temperature is raised to about ℃ at a stretch. The temperature is kept at about 850 ° C. for about 5 minutes. In that case, the temperature of the incinerated ash local part was 1,0
It is over 00 ° C. Next, (2) in order to convert the incinerated ash into slag with reduced sintering volume, the pressure was increased to 5.88 × 10 8 Pa, and the temperature was further increased to 1.1.
The temperature is raised to 00 ° C., and sintering is performed under these conditions for about 10 minutes. Further, in order to remove heavy metals in the incineration ash, the discharge plasma sintering temperature is maintained at 1,300 to 1,400 ° C. for about 15 minutes.
【0012】(3)焼結処理後の焼却灰の体積は約1/
10以下に減容され、有毒揮発物質の除去された固化成
型スラグになる。 (4)得られた固化成型スラグに防水性、補強効果のあ
るコーティング液を塗布する。かかるコーティング材と
しては、エポキシ樹脂、ポリチオール等のエポキシ系樹
脂が使用される。(3) The volume of the incinerated ash after sintering is about 1 /
The solidified molded slag is reduced in volume to 10 or less and toxic volatile substances are removed. (4) A coating liquid having a waterproof property and a reinforcing effect is applied to the obtained solidified molded slag. As the coating material, an epoxy resin such as an epoxy resin and polythiol is used.
【0013】本発明で行われる放電プラズマ焼結(SP
S)の原理は、図1に示されるように、圧粉体試料に直
流パルス電圧をON−OFF繰り返し印加すると、圧粉
体間で1000〜10000℃の局所高温状態(放電プ
ラズマ)が生じる。したがって、粉体粒子表面では気化
と熔融現象を引き起こし、粒子間接触部ではネックとい
うくびれた部分ができ、溶着状態となる。The spark plasma sintering (SP) performed in the present invention
The principle of S) is that, as shown in FIG. 1, when a DC pulse voltage is repeatedly applied ON-OFF to a green compact sample, a local high temperature state (discharge plasma) of 1000 to 10000 ° C. is generated between the green compacts. Therefore, vaporization and melting phenomena are caused on the surface of the powder particles, and a constricted portion called a neck is formed at the contact portion between the particles, so that a welding state is obtained.
【0014】又、図2は放電プラズマ焼結装置の模式図
で、上下電極にON−OFFのパルス電圧を印加し、さ
らに上下パンチに数トン〜数十トンの圧力を加圧する。
型の内部においては図1に示すような放電プラズマが焼
結固化しようとする粉体間で発生し、極めて短期間で焼
結固化が行われる。FIG. 2 is a schematic view of a discharge plasma sintering apparatus, in which an ON-OFF pulse voltage is applied to upper and lower electrodes, and a pressure of several to several tens tons is further applied to the upper and lower punches.
Inside the mold, a discharge plasma as shown in FIG. 1 is generated between the powders to be sintered and solidified, and the sintering and solidification are performed in a very short time.
【0015】[0015]
【実施例】第1工程(焼却灰中に含有されるダイオキシ
ン類、揮発性有毒物質の除去)一般家庭から排出される
都市ゴミを焼却装置で燃焼させ、その残査である焼却灰
に放電プラズマ焼結処理を施す。[Example] First step (removal of dioxins and volatile toxic substances contained in incinerated ash) Municipal garbage discharged from ordinary households is burned in an incinerator, and the residual incineration ash is discharged by plasma discharge. Sintering is performed.
【0016】焼却灰を黒鉛型(ダイ)に充頃し、真空引
きした後に圧力を2.94×108Paまで加圧した。
ダイオキシンおよび揮発性物質を除去するため、プラズ
マの温度を850℃前後まで昇温させ、850℃前後の
温度で5分程度保持した。その際の焼却灰局部の温度は
1,000℃以上になった。The incinerated ash was charged into a graphite mold (die), evacuated, and then pressurized to 2.94 × 10 8 Pa.
In order to remove dioxins and volatile substances, the temperature of the plasma was raised to about 850 ° C. and maintained at about 850 ° C. for about 5 minutes. At that time, the temperature of the local incineration ash became 1,000 ° C. or higher.
【0017】ダイオキシン、および揮発性有毒物質であ
る塩素、NOx、SOxの濃度を日常生活にさしつかえ
ない濃度(ダイオキシン濃度については0.005ng
−TEQ/g、NOx,SOxについては50ppm程
度)まで低減するために、850℃前後の温度領域で5
分間程度保持することが必要であった。The concentrations of dioxin and volatile toxic substances, chlorine, NOx and SOx, are inconsistent with daily life (the concentration of dioxin is 0.005 ng
−TEQ / g, about 50 ppm for NOx and SOx) in a temperature range around 850 ° C.
It was necessary to hold for about a minute.
【0018】第2工程(焼却灰の減容固化) 第1工程で処理した焼却灰を減容するため、黒鉛型中で
圧力を5.88×108paまで加圧し、さらに焼結反
応を起こさせるため温度を1,100℃まで昇温し、こ
の温度で10分程度保持した。Second step (solidification and reduction of incineration ash) In order to reduce the volume of the incineration ash treated in the first step, the pressure is increased to 5.88 × 10 8 pa in a graphite mold, and the sintering reaction is further performed. To raise the temperature, the temperature was raised to 1,100 ° C., and the temperature was maintained for about 10 minutes.
【0019】焼却灰の減容結果は、次のとおりであっ
た。 放電プラズマ焼結処理前の焼却灰の体積:75cm3 放電プラズマ焼結処理後のスラグの体積:7.0cm3
(直径:3.0cm×高さ:1.0cmの円筒ペレッ
ト) 又、得られた減容固化成型スラグ中の有害金属濃度に関
する、エネルギー分散型X線検出器を用いての測定結果
は、検出限界以下であった。The results of volume reduction of the incinerated ash were as follows. Volume of incineration ash before spark plasma sintering: 75 cm 3 Volume of slag after spark plasma sintering: 7.0 cm 3
(Diameter: 3.0 cm x height: 1.0 cm, cylindrical pellet) In addition, the measurement result of the harmful metal concentration in the obtained volume-reduced solidified molded slag using an energy dispersive X-ray detector is detected. It was below the limit.
【0020】第3工程(固化成型スラグの表面処理) 約1/10以下に減容され固化スラグの防水および補強
のため、得られた固化成型体の表面に表面処理材を塗布
した。Third step (Surface treatment of solidified molded slag) A surface treatment material was applied to the surface of the solidified molded body to reduce the volume to about 1/10 or less and to waterproof and reinforce the solidified molded slag.
【0021】(焼却灰固化成型スラグの分析値)ダイオ
キシンに関しては、他の実験データより900℃程度の
加熱によって日常生活にさしつかえない濃度に低減され
る。現在のところ、厚生省が決めている焼却灰の規制値
は無く、参考値として0.0lng−TEQ/gという
目安の値が示されている。今回の放電プラズマ焼結法で
固化される焼結温度は、局所で1,000〜10,00
0℃程度、焼結体外部測定温度で1,100℃なのでこ
れらの一般データ値よりもさらにダイオキシンの濃度が
低減されている。(Analytical value of incinerated ash-solidified molded slag) Dioxin can be reduced to a concentration that can be used in daily life by heating at about 900 ° C. according to other experimental data. At present, there is no regulation value of incineration ash set by the Ministry of Health and Welfare, and a reference value of 0.0 lng-TEQ / g is shown as a reference value. The sintering temperature solidified by the current spark plasma sintering method is 1,000-10,000 locally.
Since the temperature is about 0 ° C. and 1,100 ° C. at the temperature outside the sintered body, the dioxin concentration is further reduced from these general data values.
【0022】又、揮発性有毒物質に関しても、放電プラ
ズマ焼結温度範囲においては、SOx,NOxの値は3
0ppm以下になるという既成値が一般的に公表されて
いる。Regarding volatile toxic substances, the values of SOx and NOx are 3 in the discharge plasma sintering temperature range.
A pre-established value of 0 ppm or less is generally published.
【0023】更に又、無機物の分析においては、エネル
ギー分散型X線分析装置(EDX)およびX線回折装置
を用いて測定した結果、有害金属等は検出されなかっ
た。In the analysis of inorganic substances, no harmful metals were detected as a result of measurement using an energy dispersive X-ray analyzer (EDX) and an X-ray diffractometer.
【0024】[0024]
【発明の効果】本発明によれば、放電プラズマ焼結処理
を焼却灰に施し、さらに得られた固化成型スラグに防水
性、補強効果のある表面処理を施すことにより、固化成
型スラグの容積は処理前の焼却灰の嵩に比較して約1/
10に減容できる。さらに、高温で焼却灰を処理できる
ため、ダイオキシンおよび揮発性有毒物質の低減除去が
できる有効な焼却灰の固化処理方法である。According to the present invention, the volume of the solidified molded slag can be reduced by subjecting the incinerated ash to spark plasma sintering and subjecting the obtained solidified molded slag to a surface treatment having a waterproof and reinforcing effect. About 1 / compared to the volume of incinerated ash before treatment
Volume can be reduced to 10. Further, since the incineration ash can be treated at a high temperature, it is an effective incineration ash solidification method capable of reducing and removing dioxins and volatile toxic substances.
【図1】 放電プラズマ焼結の原理を示す図である。FIG. 1 is a diagram showing the principle of spark plasma sintering.
【図2】 放電プラズマ焼結装置の構造を示す図であ
る。FIG. 2 is a diagram showing a structure of a spark plasma sintering apparatus.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 三田村 久吉 茨城県那珂郡東海村白方字白根2番地の4 日本原子力研究所東海研究所内 (72)発明者 前田 敏克 茨城県那珂郡東海村白方字白根2番地の4 日本原子力研究所東海研究所内 Fターム(参考) 2E191 BA12 BD01 BD11 BD18 4D004 AA36 AB03 AB07 AB10 CA03 CA14 CA30 CA44 CA45 CA50 DA02 DA06 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Hisakichi Mitamura 2-4, Shirane, Shirakata, Tokai-mura, Naka-gun, Ibaraki Pref. 2-4 Shirane F-term in the Japan Atomic Energy Research Institute Tokai Research Laboratory (reference) 2E191 BA12 BD01 BD11 BD18 4D004 AA36 AB03 AB07 AB10 CA03 CA14 CA30 CA44 CA45 CA50 DA02 DA06
Claims (2)
を行いながら放電プラズ焼却処理を施すことにより、灰
中に含有されるダイオキシンの分解、有害揮発物質(塩
素、NOx、SOx、水銀等)濃度の低減及び重金属
(Cr6+、Pb、Cu、Zn、Cd、Hg)の溶出防
止、分離除去が可能である焼却灰の固化処理方法。An incineration ash is subjected to a discharge plasm incineration process while being pressurized from several tons to 20 tons to decompose dioxins contained in the ash and to remove harmful volatile substances (chlorine, NOx, SOx, mercury). Etc.) A method for solidifying incineration ash that can reduce the concentration, prevent elution of heavy metals (Cr 6+ , Pb, Cu, Zn, Cd, Hg), and separate and remove them.
とにより、より低温、短時間で焼却灰の固化成型を行う
ことができ、最終処分灰の減容(元の容積の1/10以
下)を促進するこができ、さらに固化成型体に防水性、
表面保護用のコーテング材を塗布することによりスラグ
の廃棄および再利用がより安全、簡便にでき、地球環境
保護・環境修復に適合した焼却灰の固化処理方法。2. By subjecting the incinerated ash to a discharge plasma sintering treatment, the incinerated ash can be solidified and molded at a lower temperature and in a shorter time, and the volume of the final ashes (1/10 or less of the original volume) can be reduced. ) Can be promoted, and the solidified molded body is waterproof,
A method for solidifying incinerated ash that is safer and easier to dispose and reuse slag by applying a coating material for surface protection, and that is suitable for global environmental protection and environmental restoration.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11167688A JP2000354841A (en) | 1999-06-15 | 1999-06-15 | Solidification of incineration ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11167688A JP2000354841A (en) | 1999-06-15 | 1999-06-15 | Solidification of incineration ash |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000354841A true JP2000354841A (en) | 2000-12-26 |
Family
ID=15854398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11167688A Pending JP2000354841A (en) | 1999-06-15 | 1999-06-15 | Solidification of incineration ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000354841A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3359016B2 (en) | 2000-02-18 | 2002-12-24 | 三菱重工業株式会社 | Ash and soil detoxification method and detoxification equipment |
| KR100497188B1 (en) * | 2002-09-03 | 2005-06-23 | 재단법인 포항산업과학연구원 | Detoxification method of dioxins in incineration ashes using slag |
| JP2007131496A (en) * | 2005-11-11 | 2007-05-31 | Chugoku Electric Power Co Inc:The | Method for producing coal ash sintered body using coal ash powder as raw material |
| CN109675910A (en) * | 2019-01-17 | 2019-04-26 | 北京工大环能科技有限公司 | A kind of processing method for heavy metals such as dioxin in flying dust and mercury |
-
1999
- 1999-06-15 JP JP11167688A patent/JP2000354841A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3359016B2 (en) | 2000-02-18 | 2002-12-24 | 三菱重工業株式会社 | Ash and soil detoxification method and detoxification equipment |
| KR100497188B1 (en) * | 2002-09-03 | 2005-06-23 | 재단법인 포항산업과학연구원 | Detoxification method of dioxins in incineration ashes using slag |
| JP2007131496A (en) * | 2005-11-11 | 2007-05-31 | Chugoku Electric Power Co Inc:The | Method for producing coal ash sintered body using coal ash powder as raw material |
| CN109675910A (en) * | 2019-01-17 | 2019-04-26 | 北京工大环能科技有限公司 | A kind of processing method for heavy metals such as dioxin in flying dust and mercury |
| CN109675910B (en) * | 2019-01-17 | 2021-01-05 | 北京工大环能科技有限公司 | Treatment method for heavy metals such as dioxin, mercury and the like in fly ash |
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