JPS6038079A - Method and equipment for high temperature melting treatment of waste material - Google Patents

Method and equipment for high temperature melting treatment of waste material

Info

Publication number
JPS6038079A
JPS6038079A JP58147067A JP14706783A JPS6038079A JP S6038079 A JPS6038079 A JP S6038079A JP 58147067 A JP58147067 A JP 58147067A JP 14706783 A JP14706783 A JP 14706783A JP S6038079 A JPS6038079 A JP S6038079A
Authority
JP
Japan
Prior art keywords
exhaust gas
quicklime
incineration residue
waste
temperature melting
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
JP58147067A
Other languages
Japanese (ja)
Inventor
Hiroshi Fujiyama
藤山 博
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.)
Kawasaki Heavy Industries Ltd
Kawasaki Motors Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Kawasaki Jukogyo 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 Kawasaki Heavy Industries Ltd, Kawasaki Jukogyo KK filed Critical Kawasaki Heavy Industries Ltd
Priority to JP58147067A priority Critical patent/JPS6038079A/en
Publication of JPS6038079A publication Critical patent/JPS6038079A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce an energy consumption amount, by using a used reactant used in a noxious gas removing apparatus for purifying exhaust gas as the m.p. falling agent of the incineration residue in a high temp. furnace. CONSTITUTION:Hight temp. exhaust gas generated from an incinerator 11 is cooled after introduced into an exhaust gas boiler 12 and discharged to a noxious gas removing apparatus 14 while minute ash floated in the exhaust gas is collected by an electric dust collector 13. Quick lime 17 is separately charged into this apparatus 14 and the reaction product formed to the outer skin part of quick lime 17 by the passage of the exhaust gas is charged into a separator 15 along with quick lime 17 to separate the surface reaction product from quick lime. On the other hand, the incineration residue from the incinerator 11 or incineration ash from the exhaust gas boiler 2 is preliminarily charged in a high temp. melting furnace 16 and, when quick lime 17 from the separator 17 is charged in said furnace 16, the m.p. of the molten substance therein is fallen and the melting of the incineration residue is enabled in reduced quantity of electricity or a reduced oil amount.

Description

【発明の詳細な説明】 (a)産業上の利用分野 本発明は廃棄物の高温溶融処理方法およびその設備に関
し、詳しくは1.高VIJL溶融炉における焼却残渣の
溶融を容易にした高温溶融処理方法およびその設備に関
する。これは、焼却残渣を溶融スラグ化してその減容化
、安定化を図る際、残渣溶融に使用されるエネルギ消費
量を低減させる分野で利用されるものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a method for high-temperature melting treatment of waste and its equipment, and in detail 1. The present invention relates to a high-temperature melting method and equipment for facilitating the melting of incineration residue in a high VIJL melting furnace. This is used in the field of reducing the amount of energy consumed for melting the residue when incineration residue is turned into molten slag to reduce and stabilize its volume.

(b)従来技術 都市ゴミなどの廃棄物を焼却する焼却設備は、その1例
として第1図に示すような、焼却炉1、焼却排ガスによ
る熱回収ボイラ2、排ガス中の微小焼却灰を捕集する電
気集塵機3、排ガス中の有害ガスを除去する有害ガス除
去装置4や、焼却炉1から排出される焼却残渣および熱
回収ボイラ2内で沈降した焼却灰を溶融する高温溶融炉
5などからなり、焼却炉1から排出される排ガスならび
に焼却残渣の処理が1つの設備内で円滑に行なわれるよ
うになっている。そして、高温溶融炉5ば焼却残渣の廃
棄またはその利用を図るために、それを溶融して減容化
、安定化させる機能を有する。
(b) Prior art An example of an incinerator for incinerating waste such as municipal garbage is shown in Figure 1, which includes an incinerator 1, a heat recovery boiler 2 using incineration exhaust gas, and a heat recovery boiler 2 that captures minute incineration ash in the exhaust gas. from an electrostatic precipitator 3 that collects the dust, a harmful gas removal device 4 that removes harmful gases from exhaust gas, and a high-temperature melting furnace 5 that melts incineration residue discharged from the incinerator 1 and incinerated ash that has settled in the heat recovery boiler 2. Thus, the exhaust gas discharged from the incinerator 1 and the incineration residue can be smoothly processed within one facility. The high-temperature melting furnace 5 has the function of melting, reducing and stabilizing the incineration residue in order to dispose of it or utilize it.

焼却残渣は灰分の外に未燃物、金属や陶磁器などの不燃
物が混在していて、その溶融温度は一般に1500℃程
度である。したがって、高温溶融炉5に投入される常温
または100℃前後の焼却残渣を溶融するために、電気
抵抗法、油バーす法、マイクロ波法などにより電気また
は油などのエネルギを多量に消費している。このエネル
ギは焼却残渣の処理にのみ使用されるので、できるだけ
少ない方が良く、それを実現する方策として、焼却残渣
の溶融温度降下作用を有する生石灰が、高温溶融炉5に
別途投入されたりしている。ところが、この生石灰の投
入量は焼却残渣のほぼ30%重量比にも及ぶ。一方、有
害ガス除去装置においては、排ガス中の硫黄分や塩素分
を除去するために、やはり生石灰が利用されている。そ
の結果、廃棄物の処理に当たっては、大量の生石灰が消
費されることになり、また、有害ガス除去装置で生成さ
れた反応生成物や高温溶融炉で得られた溶融スラグの量
が増大してその投棄量が増え、その改善が強く要望され
ている。
In addition to ash, incineration residue contains unburnt materials such as metals and ceramics, and its melting temperature is generally about 1500°C. Therefore, in order to melt the incineration residue at room temperature or around 100°C, which is fed into the high-temperature melting furnace 5, a large amount of energy such as electricity or oil is consumed by the electrical resistance method, oil bar method, microwave method, etc. There is. Since this energy is used only for processing the incineration residue, it is better to use as little as possible, and as a measure to achieve this, quicklime, which has the effect of lowering the melting temperature of the incineration residue, is separately charged into the high-temperature melting furnace 5. There is. However, the amount of quicklime added reaches approximately 30% by weight of the incineration residue. On the other hand, in harmful gas removal devices, quicklime is still used to remove sulfur and chlorine from exhaust gas. As a result, a large amount of quicklime is consumed in waste treatment, and the amount of reaction products generated by harmful gas removal equipment and molten slag obtained from high-temperature melting furnaces increases. The amount of waste being discarded is increasing, and there is a strong demand for improvement.

(C)発明の目的 本発明は上述の問題を解消するためになされたもので、
1つの廃棄物処理設備で使用される高温溶融炉における
焼却残渣の融点降下剤である生石灰と有害ガス除去装置
における有害ガス除去剤である生石灰との使用量の低減
を図り、加えて、高温溶融炉からの溶融スラグ量と有害
ガス除去装置から排出される反応生成物量の総計を少な
くすることができる廃棄物の高温溶融処理方法およびそ
の設備を提供することを目的とする。
(C) Purpose of the invention The present invention has been made to solve the above-mentioned problems.
We aim to reduce the amount of quicklime used as a melting point depressant for incineration residue in the high-temperature melting furnace used in one waste treatment facility, and the amount of quicklime used as a harmful gas removal agent in the harmful gas removal equipment. It is an object of the present invention to provide a method for high-temperature melting treatment of waste and its equipment, which can reduce the total amount of molten slag from a furnace and the amount of reaction products discharged from a harmful gas removal device.

((])発明の構成 本発明の構成を第2図に基づいて説明すると、第1の発
明は、廃棄物を焼却した後の焼却残渣を1、高温溶融固
化処理する廃棄物処理設備において、焼却炉11からの
排ガスを浄化するために乾式の有害ガス除去装置14で
反応剤として使用された生石灰17を高温溶融炉16に
投入し、焼却残渣の融点降下剤として利用する廃棄物の
高温溶融処理方法である。
(()) Structure of the Invention The structure of the present invention will be explained based on FIG. The quicklime 17 used as a reactant in the dry harmful gas removal device 14 to purify the exhaust gas from the incinerator 11 is charged into the high-temperature melting furnace 16, and the waste is melted at high temperature to be used as a melting point depressant for the incineration residue. This is a processing method.

第2の発明は、廃棄物を焼却した後の焼却残渣を、高温
溶融固化処理する廃棄物処理設備において、焼却炉11
からの排ガスを浄化するために反応剤として生石灰17
が投入される乾式の有害ガス除去装置14と、焼却残渣
を溶融させる高温溶融炉16との間に、生石灰17の有
害ガス除去装置14における反応生成物から残存生石灰
を取り出す分l1lt機15が設けられている廃棄物の
高温溶融処理設備である。
The second invention is a waste treatment facility that processes incineration residue after incinerating waste at a high temperature by melting and solidifying the incinerator 11.
Quicklime 17 as a reactant to purify exhaust gas from
A 11lt machine 15 is provided between the dry harmful gas removal device 14 into which the waste is charged and the high-temperature melting furnace 16 which melts the incineration residue. This is a high-temperature melting treatment facility for waste.

(e)実施例 以下、本発明をその実施例を示す図面を参照しながら説
明する。
(e) Examples Hereinafter, the present invention will be explained with reference to drawings showing examples thereof.

第2図は廃棄物処理設備10の全体配置図で、11は都
市ゴミなどの廃棄物を焼却する焼却炉、12ば焼却炉1
1からの排ガスを利用して熱回収を行なう排ガスボイラ
、j3は排ガスボイラ12を流過した排ガス中の微小な
灰分を捕集する電気集塵機、14は排ガスを大気に放出
するに先立ち排ガス中の硫黄分や塩素分などを生石灰を
利用して除去するための乾式の有害ガス除去装置、15
は有害ガス除去装置14で反応して得られた反応生成物
から生石灰を回収するための分離機で、例えば、ボール
ミルである。有害ガス除去装置14に投入される生石灰
は粒状であり、反応生成物である例えば硫酸カルシウム
はその生石灰の表面に生成され、その内部には生石灰が
未反応のまま残存しているので、この分離機15はそれ
を機械的に回収する機能を有している。16は高温溶融
炉で、焼却炉1からの焼却残渣および排ガスボイラ12
内で沈降した焼却灰が投入され、それらを溶融して溶融
スラグを生成するものである。なお、この高温溶融炉1
6における焼却残渣など、の溶融温度を低めるための融
点降下剤として、分離機15からの生石灰が投入される
Figure 2 is an overall layout diagram of the waste treatment equipment 10, where 11 is an incinerator for incinerating waste such as municipal garbage, and 12 is an incinerator 1.
j3 is an electrostatic precipitator that collects minute ash in the exhaust gas that has passed through the exhaust gas boiler 12; Dry harmful gas removal device for removing sulfur, chlorine, etc. using quicklime, 15
is a separator for recovering quicklime from the reaction product obtained by the reaction in the harmful gas removal device 14, and is, for example, a ball mill. The quicklime fed into the harmful gas removal device 14 is granular, and reaction products such as calcium sulfate are generated on the surface of the quicklime, and the quicklime remains unreacted inside, so this separation is difficult. The machine 15 has a function of mechanically collecting it. 16 is a high-temperature melting furnace, which contains incineration residue from the incinerator 1 and an exhaust gas boiler 12;
Incineration ash that has settled inside the reactor is input and melted to produce molten slag. In addition, this high-temperature melting furnace 1
Quicklime from the separator 15 is fed as a melting point depressant to lower the melting temperature of the incineration residue etc. in the separator 15.

このよ・うな構成の廃棄物処理設備によれば、次のよう
にして焼却炉から発生する排ガスならびに焼却残渣を処
理することができ、また、それらの廃棄における有害成
分の除去および減容化・安定化を、少量の反応剤および
エネルギで実現することができる。
According to the waste treatment equipment configured as described above, it is possible to treat the exhaust gas and incineration residue generated from the incinerator in the following manner, and also to remove harmful components and reduce the volume when disposing of them. Stabilization can be achieved with small amounts of reactants and energy.

まず、焼却炉11から発生した排ガスは高温の熱エネル
ギを有するので、それが排ガスボイラ12に導入されて
熱回収が図られる。そこを流過して降温した排ガスは電
気集塵機j3でその中に浮遊する微小な灰分が捕集され
、有害ガス除去装置14に導出される。有害ガス除去装
置】4には、排ガスが流過する図示しない1対のルーへ
内に生石灰17が別途投入されているので、排ガスがそ
の間隙を流過する間に反応して硫酸カルシウムや塩化カ
ルシウムが反応生成物として生成され、排ガス中の硫黄
分や塩素分が除去されて大気に放出される。これらの反
応生成物は粒状の生石灰の主として外皮部に生成されて
いるので、これが分離機15に投入され、例えばスティ
ールポールなどと共に回転されて、表面の反応生成物が
生石灰の周囲より粉砕または剥離されて元の反応剤と同
様の生石灰が分離される。反応生成物はほぼ粉状となり
、篩分けられると、小粒化した生石灰が得られる。一方
、焼却炉11からの焼却残渣および/または排ガスボイ
ラ12からの焼却灰が高温溶融炉16に投入されている
ので、その中に分l1lltta15からの生石灰が供
給される。焼却残渣の融点はゴミ質によっても異なるが
、通常1500℃程度であり、生石灰17が投入される
と、電導度の高い生石灰により溶融物の粘性が低下して
その融点が例えば1300℃程度に降下する。その結果
、焼却残渣の溶融が少ない電気量や油量で可能となり、
焼却残渣の溶融スラグ化を容易に行なうことができる。
First, since the exhaust gas generated from the incinerator 11 has high-temperature thermal energy, it is introduced into the exhaust gas boiler 12 to recover heat. The exhaust gas that has passed there and cooled down has minute ash particles floating therein collected by the electrostatic precipitator j3, and is led out to the harmful gas removal device 14. [Harmful gas removal device] In 4, quicklime 17 is separately put into a pair of louis (not shown) through which the exhaust gas flows, so as the exhaust gas flows through the gaps, it reacts and produces calcium sulfate and chloride. Calcium is produced as a reaction product, which removes sulfur and chlorine from the exhaust gas and releases it into the atmosphere. These reaction products are mainly produced in the outer skin of the granular quicklime, so this is fed into the separator 15 and rotated with a steel pole, for example, so that the reaction products on the surface are crushed or peeled off from the periphery of the quicklime. Quicklime, which is similar to the original reactant, is separated. The reaction product is almost powder-like, and when sieved, quicklime with small particles is obtained. On the other hand, since the incineration residue from the incinerator 11 and/or the incineration ash from the exhaust gas boiler 12 are charged into the high-temperature melting furnace 16, the quicklime from the portion 11lltta 15 is supplied therein. The melting point of incineration residue varies depending on the type of garbage, but is usually around 1,500°C, and when quicklime 17 is added, the viscosity of the molten material decreases due to the quicklime with high conductivity, and the melting point drops to, for example, around 1,300°C. do. As a result, incineration residue can be melted with less electricity and oil,
Incineration residue can be easily converted into molten slag.

なお、高温溶融炉16へは生石灰17が投入されるので
、高温溶融炉16で発生するガスには未燃物の燃焼によ
る微量の一酸化炭素などが含まれる外は大半が空気や水
蒸気であり、有害ガス成分が多量に含まれることはない
。その結果ざこのガスが例えば排ガスボイラ12の低温
側に供給され、やはり熱回収されるが、有害ガス除去装
置14において投入されている生石灰に反応生成物を当
初以上に生成させて、分離機15における生石灰の分離
回収量を減少させるといったことは生じない。
In addition, since quicklime 17 is charged into the high-temperature melting furnace 16, the gas generated in the high-temperature melting furnace 16 is mostly air and water vapor, except for a small amount of carbon monoxide caused by the combustion of unburned materials. , does not contain large amounts of harmful gas components. As a result, the gas is supplied to the low-temperature side of the exhaust gas boiler 12, for example, and the heat is recovered, but the reaction product is generated in the quicklime charged in the harmful gas removal device 14 more than before, and the separator 15 There is no reduction in the amount of quicklime separated and recovered.

分離機15で分離された硫酸カルシウムや塩化カルシウ
ムは固体または粉体状態で投棄され、高温溶融炉16で
得られた溶融スラグは埋め立て地などに投棄されたり、
他の産業用副資材として利用される。
Calcium sulfate and calcium chloride separated in the separator 15 are dumped in solid or powdered form, and the molten slag obtained in the high-temperature melting furnace 16 is dumped in a landfill or the like.
Used as an auxiliary material for other industries.

とごろで、高温溶融炉16には少なくともカルシウム分
が供給されると、上述した効果を発揮させることができ
るのであるが、有害ガス除去装置14からの生石灰を包
含した反応生成物を直接供給してもよい。しかし、その
場合には、高温溶融炉1Gにおて反応生成物中の硫黄や
塩素分が再び気化して有害ガスが発生することになるの
で、高温溶融炉16に苛性ソーダなどを用いる湿式ガス
処理装置、生石灰を用いる乾式ガス処理装置、または消
石灰を用いる半乾式のガス処理装置などを付設する必要
がある。その場合には前述した分離機15が不要となる
が、高温溶融炉16におけるガス処理のために新たな反
応剤を供給する必要があり、本発明ではこのような反応
剤ならびに他の融点降下剤を使用するといったことは回
避され、有害ガス除去装置14に供給された生石灰のみ
でもって一連の処理を行なわせることができ、廃棄物処
理における有害ガスの除去および焼却残渣の溶融のため
のランニングコストの低減を可能にすることができる。
However, if at least calcium is supplied to the high-temperature melting furnace 16, the above-mentioned effect can be achieved, but if the reaction product containing quicklime from the harmful gas removal device 14 is directly supplied. It's okay. However, in that case, the sulfur and chlorine content in the reaction product will vaporize again in the high-temperature melting furnace 1G and harmful gases will be generated, so wet gas treatment using caustic soda or the like is used in the high-temperature melting furnace 16. It is necessary to install a dry gas treatment device using quicklime, or a semi-dry gas treatment device using slaked lime. In that case, the separator 15 described above becomes unnecessary, but it is necessary to supply a new reactant for gas treatment in the high temperature melting furnace 16, and in the present invention, such a reactant as well as other melting point depressants are used. It is possible to perform a series of treatments using only the quicklime supplied to the hazardous gas removal device 14, thereby reducing the running costs for removing hazardous gas and melting incineration residue in waste treatment. It is possible to reduce the

(f)発明の効果 本発明は以上詳細に説明したように、第1の発明におい
て、排ガスを浄化する有害ガス除去装置で使用された使
用済みの反応剤を、高温溶融炉における焼却残渣の融点
降下剤として利用するようにしたので、有害ガス除去装
置から投棄される使用済み反応剤量が少なくなり、その
投棄量を減少させることができる。そして、投棄される
ことなく回収された残存する反応剤で焼却残渣の溶融温
度の低下を図ることができるので、高温溶融炉における
電気または油などのエネルギ消費量の低減を可能にする
ことができる。また、第2の発明の構成によれば、有害
ガス除去装置からの反応生成物から生石灰を容易に回収
して高温溶融炉に供給できるので、上述の発明と同様の
効果を得るための設備の実現を図ることができる。
(f) Effects of the Invention As explained in detail above, in the first invention, the used reactant used in a harmful gas removal device for purifying exhaust gas is melted in a high-temperature melting furnace at the melting point of the incineration residue. Since the reactant is used as a depressant, the amount of used reactant discarded from the harmful gas removal device is reduced, and the amount of discarded reactant can be reduced. The remaining reactant recovered without being dumped can lower the melting temperature of the incineration residue, making it possible to reduce energy consumption such as electricity or oil in the high-temperature melting furnace. . Furthermore, according to the configuration of the second invention, quicklime can be easily recovered from the reaction product from the harmful gas removal device and supplied to the high-temperature melting furnace. It is possible to achieve this goal.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の廃棄物処理設備の配置図、第2図は本発
明の廃棄物の高温溶融処理設備を含む廃棄物処理設備の
配置図である。 10−・廃棄物処理設備、11−・−焼却炉、14・−
有害ガス除去装置、15・−分l1llt機、16−高
温溶融炉、17−・−生石灰 特許出願人 川崎重工業株式会社
FIG. 1 is a layout diagram of conventional waste treatment equipment, and FIG. 2 is a layout diagram of waste treatment equipment including the waste high temperature melting treatment equipment of the present invention. 10-・Waste treatment equipment, 11-・-Incinerator, 14・-
Harmful gas removal equipment, 15-minute 11llt machine, 16-high temperature melting furnace, 17--quicklime patent applicant Kawasaki Heavy Industries, Ltd.

Claims (3)

【特許請求の範囲】[Claims] (1) 廃棄物を焼却した後の焼却残渣を、高温溶融固
化処理する廃棄物処理設備において、焼却炉からの排ガ
スを浄化するために乾式の有害ガス除去装置で反応剤と
して使用された生石灰を高温溶融炉に投入し、焼却残渣
の融点降下剤として利用することを特徴とする廃棄物の
高温溶融処理方法。
(1) In a waste treatment facility that processes the incineration residue after incinerating waste at a high temperature, the quicklime used as a reaction agent in a dry harmful gas removal device is used to purify the exhaust gas from the incinerator. A high-temperature melting treatment method for waste, which is characterized by charging waste into a high-temperature melting furnace and using it as a melting point depressant for incineration residue.
(2) 廃棄物を焼却した後の焼却残渣を、高温溶融固
化処理する廃棄物処理設備において、焼却炉からの排ガ
スを浄化するために反応剤として生石灰が投入される乾
式の有害ガス除去装置と、焼却残渣を溶融させる高温溶
融炉との間に、前記生石灰の有害ガス除去装置における
反応生成物から残存生石灰を取り出す分離機を設けたこ
とを特徴とする廃棄物の高温溶融処理設備。
(2) In a waste treatment facility that processes the incineration residue after incinerating waste at high temperatures, it is a dry type harmful gas removal device in which quicklime is added as a reactant to purify the exhaust gas from the incinerator. A high-temperature melting treatment facility for waste, characterized in that a separator is provided between a high-temperature melting furnace for melting incineration residue and a separator for extracting residual quicklime from the reaction product in the quicklime noxious gas removal device.
(3) 前記分離機は、ボールミルであることを特徴と
する特許請求の範囲第2項記載の廃棄物の高温溶融処理
設備。
(3) The high-temperature melting treatment equipment for waste according to claim 2, wherein the separator is a ball mill.
JP58147067A 1983-08-10 1983-08-10 Method and equipment for high temperature melting treatment of waste material Pending JPS6038079A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58147067A JPS6038079A (en) 1983-08-10 1983-08-10 Method and equipment for high temperature melting treatment of waste material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58147067A JPS6038079A (en) 1983-08-10 1983-08-10 Method and equipment for high temperature melting treatment of waste material

Publications (1)

Publication Number Publication Date
JPS6038079A true JPS6038079A (en) 1985-02-27

Family

ID=15421730

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58147067A Pending JPS6038079A (en) 1983-08-10 1983-08-10 Method and equipment for high temperature melting treatment of waste material

Country Status (1)

Country Link
JP (1) JPS6038079A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62245015A (en) * 1986-04-16 1987-10-26 Hitachi Zosen Corp Slag tap combustion method
JPH04313615A (en) * 1991-04-12 1992-11-05 Kobe Steel Ltd Method for adjusting basicity of incineration ash in incineration ash-melting furnace
JP2016148669A (en) * 2016-03-01 2016-08-18 日本碍子株式会社 Treatment method of radioactive cesium contaminant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62245015A (en) * 1986-04-16 1987-10-26 Hitachi Zosen Corp Slag tap combustion method
JPH04313615A (en) * 1991-04-12 1992-11-05 Kobe Steel Ltd Method for adjusting basicity of incineration ash in incineration ash-melting furnace
JP2016148669A (en) * 2016-03-01 2016-08-18 日本碍子株式会社 Treatment method of radioactive cesium contaminant

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