JP2001233621A - Method of vitrifying treatment with treated ash and molded product - Google Patents

Method of vitrifying treatment with treated ash and molded product

Info

Publication number
JP2001233621A
JP2001233621A JP2000045367A JP2000045367A JP2001233621A JP 2001233621 A JP2001233621 A JP 2001233621A JP 2000045367 A JP2000045367 A JP 2000045367A JP 2000045367 A JP2000045367 A JP 2000045367A JP 2001233621 A JP2001233621 A JP 2001233621A
Authority
JP
Japan
Prior art keywords
ash
treated
glass
halogen
treating agent
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
JP2000045367A
Other languages
Japanese (ja)
Inventor
Yoshiyuki Kashiwagi
佳行 柏木
Nobuyuki Yoshioka
信行 吉岡
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
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 Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP2000045367A priority Critical patent/JP2001233621A/en
Publication of JP2001233621A publication Critical patent/JP2001233621A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/005Melting in furnaces; Furnaces so far as specially adapted for glass manufacture of glass-forming waste materials
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping

Abstract

PROBLEM TO BE SOLVED: To solve a problem that when treated ash remained after the incineration treatment of wastes and having toxic materials of halogen-containing substance (especially chlorine-containing substance) is used as a resource through melting and vitrification, there is a danger of deposition of toxic materials during the heat treatment when the treated ash is molten and vitrified. SOLUTION: The treated ash having halogen-containing substances and a treating agent for dechlorination which contains glass components, are charged into a heat treatment furnace 1, and they are heat-treated. This can perform simultaneously dechlorination and vitrification to obtain glass products.

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、ガラス成分を含む
灰類に、ガラス成分を含む脱塩素用の処理剤を添加して
加熱し、灰類に含まれているハロゲン系物質を分解析出
して処理剤と接触反応させ、無害な塩化物を生成するこ
とで分解ガスと処理灰類の無害化を行うとともに、ガラ
ス化処理する方法と、これを溶融して成形したガラス成
形品に関し、特に、灰類をガラス化して有効利用を図る
技術に関する。
BACKGROUND OF THE INVENTION The present invention relates to a method of adding a dechlorinating agent containing a glass component to ash containing a glass component and heating the ash to decompose and precipitate a halogen-based substance contained in the ash. In addition to detoxifying the decomposed gas and treated ash by producing a harmless chloride by contact reaction with the treating agent, a vitrification method and a glass molded product obtained by melting and molding the same, particularly And technology for vitrifying ash for effective use.

【0002】[0002]

【従来の技術】各種廃棄物の焼却処理で発生する焼却
灰、排気ガスと一緒に運ばれる各種集塵機で補足された
飛灰、各種汚泥の脱水焼却された汚泥焼却灰、乾燥した
汚泥、更には汚染した土壌など要無害化処理対象物は膨
大な量がある。
2. Description of the Related Art Incineration ash generated in the incineration of various wastes, fly ash supplemented by various dust collectors carried with exhaust gas, sludge incineration ash obtained by dehydration and incineration of various sludges, dry sludge, There is a huge amount of detoxified objects such as contaminated soil.

【0003】これらの灰類は、有害なハロゲン系の有機
化合物(ダイオキシン類、塩化水素など)を含有してお
り、単に埋め立て処分するだけでは、ダイオキシン類の
溶出による環境汚染の問題が発生する。そこで、処理灰
類を安全に処理し、且つリサイクル利用の可能な技術の
開発が望まれ各種の処理方法が提案されている。
[0003] These ashes contain harmful halogen-based organic compounds (dioxins, hydrogen chloride, etc.), and simply disposing of them in a landfill poses a problem of environmental pollution due to elution of dioxins. Therefore, it is desired to develop a technology that can safely treat the treated ash and that can be recycled, and various treatment methods have been proposed.

【0004】例えば、アルミ残灰等にガラスカレット粉
末をバインダとして造粒し、焼成・固化してコンクリー
ト用骨材として利用する方法(特開平11−31495
0)、又は焼却灰をスラグ化し、スラグガラスの粉砕物
から建材として有効利用可能な発泡材を得る方法(特開
平11−171661)、あるいは、環境汚染防止の観
点から焼却灰を再焼成してガラス状焼成物を得、焼却灰
に含有する重金属やハロゲン化有機物をガラス質中に封
じ込めて水中に溶出しないようにする方法(特開平10
−21215)等で提案されている。
For example, a method in which glass cullet powder is granulated on aluminum residual ash or the like as a binder, fired and solidified, and used as an aggregate for concrete (JP-A-11-31495)
0) or a method of converting incinerated ash into slag and obtaining a foam material that can be effectively used as a building material from pulverized slag glass (JP-A-11-171661), or re-burning incinerated ash from the viewpoint of environmental pollution prevention A method of obtaining a glass-like fired product and encapsulating heavy metals and halogenated organic substances contained in the incineration ash in vitreous so as not to elute into water (Japanese Patent Laid-Open No.
-21215).

【0005】また、本願の出願人も、焼却灰、飛灰、汚
泥焼却灰等の処理灰をガラス化する場合、これらの処理
灰に含有するダイオキシン類等の有害物質を無害化処理
する方法(特開平11−19616)、およびこの無害
化した処理灰をガラス化し、これを粉体化して建設用素
材として有効利用を可能とした処理方法(特開平11−
1145435)を提案している。
[0005] In addition, the applicant of the present application also discloses a method of detoxifying harmful substances such as dioxins contained in treated ash such as incinerated ash, fly ash and sludge incinerated ash. JP-A-11-19616) and a processing method in which the harmless treated ash is vitrified and powdered to enable effective utilization as a construction material (JP-A-11-19616).
1145435).

【0006】[0006]

【発明が解決しようとする課題】焼却灰をガラス化して
資源として有効利用を図る場合、処理灰中には有害なハ
ロゲン系有機化合物が含有されており、これを加熱溶融
する際に処理灰から塩素系ガスが発生し、ダイオキシン
類発生の原因となる。即ち、上記のコンクリート骨材を
得る場合、又は発泡材を得る場合、あるいは重金属やハ
ロゲン化有機物をガラス質中に封じ込める場合のいずれ
の場合でも、成形過程の溶融加熱時に有害な塩素系ガス
が発生する恐れがあるが、その無害化対策が取られてい
ない。
When vitrifying incinerated ash for effective use as a resource, the treated ash contains harmful halogenated organic compounds. Chlorine gas is generated, which causes dioxins. That is, harmful chlorine-based gas is generated during melting and heating in the molding process, either when obtaining the above-mentioned concrete aggregate, when obtaining a foamed material, or when encapsulating heavy metals or halogenated organic substances in glass. However, no detoxification measures have been taken.

【0007】これに対し、本願の出願人が先に提案した
ものは、処理灰とアルカリ物質からなる脱塩素剤とを混
合して加熱し、加熱時に発生する有害な塩化水素と脱塩
素剤とを接触反応させて無害な塩化物に置換生成するこ
とで無害な処理灰を得ること、およびこの無害化された
処理灰を溶解して冷却固化してガラス化し、これを粉体
化して有効利用を図るもので、加熱溶融時の処理灰から
有害な塩素系ガスを除去する環境上好ましい処理方法で
ある。
[0007] On the other hand, the one proposed by the applicant of the present application is to mix a treated ash and a dechlorinating agent composed of an alkali substance and heat them, and to remove harmful hydrogen chloride and dechlorinating agent generated during heating. To make harmless treated ash by contacting and reacting with harmless chloride, and dissolving this harmless treated ash, solidifying it by cooling, vitrifying it, and powdering it for effective use This is an environmentally preferable treatment method for removing harmful chlorine-based gas from treated ash during heating and melting.

【0008】しかし、この処理方法は、処理灰をガラス
化し、更にこのガラス化物を粉体化して利用するもので
あるが、その後の調査研究により、脱塩素用に使用する
処理剤には、本来ガラス組成成分が多く含んでいること
が判り、この処理剤により、被処理灰類を容易にガラス
化できることを見出した。
[0008] However, this treatment method is to vitrify the treated ash and further use this vitrified material as a powder. However, according to a subsequent investigation and research, the treatment agent used for dechlorination is originally not used. It was found that many glass composition components were contained, and it was found that the ash to be treated could be easily vitrified by this treating agent.

【0009】本発明の目的は、この被処理灰類によるガ
ラス化処理方法と、処理灰からガラス化成形品を得る技
術を提供するにある。
An object of the present invention is to provide a vitrification method using the ash to be treated and a technique for obtaining a vitrified molded product from the treated ash.

【0010】[0010]

【課題を解決するための手段】本発明は、処理灰(焼却
灰、飛灰、汚泥焼却灰)、乾燥汚泥、汚染土壌類(以
下、被処理灰類と称す)には、ガラス組成成分がある程
度含まれており、且つ本発明者らが先に提案した処理灰
類の脱塩素処理およびそのガラス化処理(特開平11−
19616、特開平11−114535)、又はバグフ
ィルタに噴霧して排ガスの清浄化を行う脱塩素用の処理
剤にも、ガラス組成成分が多く含まれていることに着目
し、この処理剤を利用して被処理灰類をガラス化処理す
る方法を提案するものである。
SUMMARY OF THE INVENTION According to the present invention, a glass composition component is contained in treated ash (incinerated ash, fly ash, sludge incinerated ash), dried sludge, and contaminated soils (hereinafter referred to as ash to be treated). Dechlorination of treated ash which is contained to some extent and which has been previously proposed by the present inventors and vitrification thereof (Japanese Unexamined Patent Publication No.
19616, JP-A-11-114535), or the use of this treating agent by focusing on the fact that the treating agent for dechlorination for purifying exhaust gas by spraying onto a bag filter also contains a large amount of glass composition components. And a method of vitrifying the ash to be treated.

【0011】即ち、(1)処理剤として、加熱により被
処理物から分解析出する有害成分と反応して無害な塩化
物を生成するアルカリ金属、アルカリ金属化合物、アル
カリ土類化合物、アルカリ土類金属化合物に含まれるア
ルカリ物質を使用すること、(a)アルカリ金属化合物
の処理剤には、炭酸水素ナトリウム、炭酸ナトリウム、
セスキ炭酸ナトリウム、天然ソーダ、炭酸カリウム、炭
酸水素カリウム、炭酸ナトリウム、水酸化ナトリウム、
水酸化カリウムが含まれ、(b)アルカリ土類金属化合
物には、石灰(CaO)、消石灰(CaCOH2)、炭
酸カルシウム(CaCO3)、ドロマイト(CaCO3
MgCO3)が含まれ、(2)被処理灰類には、(a)
アルカリ金属(Li,Na,K,Rb,Cs,Fr)お
よび(b)アルカリ土類金属(Ca,Sr,Ba,R
a)がある程度含まれていること、(3)一方、ソーダ
ガラスの主成分は、Na2O・CaO・5SiO2(天然
ソーダ)を中心とした組成をもち、主な成分範囲(重量
%)は、SiO2:65〜75,Na2O:10〜20,
CaO:5=15,その他:Al23,MgO,Fe2
3であること、即ち、被処理灰類の無害化処理に使用
するアルカリ物質は、本来ガラス組成成分を多く含んで
いることに着目し、処理剤の添加量をガラス組成に調整
(制御)して添加することで、処理後の被処理灰類を容
易にガラス化できることを見出した。
(1) As a treating agent, an alkali metal, an alkali metal compound, an alkaline earth compound, an alkaline earth compound, which reacts with a harmful component decomposed and precipitated from an object to be treated by heating to form a harmless chloride The use of an alkali substance contained in the metal compound, (a) the treating agent for the alkali metal compound includes sodium hydrogen carbonate, sodium carbonate,
Sodium sesquicarbonate, natural soda, potassium carbonate, potassium bicarbonate, sodium carbonate, sodium hydroxide,
Potassium hydroxide is contained, and (b) alkaline earth metal compounds include lime (CaO), slaked lime (CaCOH 2 ), calcium carbonate (CaCO 3 ), dolomite (CaCO 3.
MgCO 3 ), and (2) ash to be treated includes (a)
Alkali metals (Li, Na, K, Rb, Cs, Fr) and (b) alkaline earth metals (Ca, Sr, Ba, R
(3) On the other hand, the main component of the soda glass has a composition centered on Na 2 O.CaO.5SiO 2 (natural soda), and the main component range (% by weight) is, SiO 2: 65~75, Na 2 O: 10~20,
CaO: 5 = 15, other: Al 2 O 3 , MgO, Fe 2
Focusing on the fact that it is O 3 , that is, the alkali substance used for the detoxification treatment of the ash to be treated inherently contains a large amount of glass composition components, the amount of the treatment agent is adjusted to the glass composition (control). It was found that the ash to be treated after the treatment can be easily vitrified by the addition.

【0012】本発明はこれらの知見に基づいてなされた
もので、上記の課題を解決するための手段は、ハロゲン
系物質を含む被処理灰類と、ガラス成分を含むアルカリ
物質からなる処理剤とを混合して外部加熱手段による加
熱処理炉で加熱し、被処理灰類から分解析出したハロゲ
ン系物質と処理剤とを接触反応させて無害な塩化物を生
成することで分解ガスの無害化と被処理灰類の無害化お
よびガラス化を行うことを特徴とするガラス化処理方法
とするものである。
The present invention has been made based on these findings, and means for solving the above-mentioned problems include a treatment ash containing a halogen-based substance and a treatment agent comprising an alkali substance containing a glass component. Is mixed and heated in a heat treatment furnace by external heating means, and the halogen-based substance decomposed and precipitated from the ash to be treated is brought into contact with the treating agent to produce harmless chlorides, thereby rendering the harmless gas harmless. And detoxification and vitrification of the ash to be treated.

【0013】また、ハロゲン系物質を含む被処理灰類
と、ガラス成分を含むアルカリ物質からなる処理剤とを
混合して外部加熱手段による加熱処理炉で加熱し、被処
理灰類から分解析出したハロゲン系物質と処理剤とを接
触反応させて無害な塩化物を生成することで分解ガスの
無害化と被処理灰類の無害化を行うとともに、ソーダガ
ラスの主成分であるSi,Na,Caの添加量を制御す
ることでガラス化する。
Further, the ash to be treated containing a halogen-based substance and a treating agent comprising an alkali substance containing a glass component are mixed and heated in a heating furnace by an external heating means to decompose and precipitate from the ash to be treated. The harmless chloride is generated by contacting the treated halogen-based substance with the treating agent, thereby detoxifying the decomposed gas and the ash to be treated, and at the same time, the main components of soda glass, Si, Na, Vitrification is achieved by controlling the amount of Ca added.

【0014】被処理灰類は各種あり、また処理方法によ
りその成分は千差万別であることから、事前に、これら
の被処理灰類の成分を分析調査し、不足するSi,C
a,Na量に応じて添加量を調整(制御)する。
There are various types of ash to be treated, and the components vary widely depending on the treatment method. Therefore, the components of these ash to be treated are analyzed and investigated in advance, and the deficient Si, C
The amount of addition is adjusted (controlled) according to the amounts of a and Na.

【0015】そして、ソーダガラスの主成分の添加量
(重量%)は、好ましくは、SiO2が65〜75,N
aO2が10〜20,CaOが5〜15の成分比とす
る。
[0015] Then, the amount of the main component of soda glass (wt%), preferably, SiO 2 is 65 to 75, N
aO 2 is 10-20 and CaO is 5-15 component ratio.

【0016】本発明に使用されるアルカリ物質の処理剤
は、本願の出願人が先に提案して開示した特開平11−
19616号、特開平11−114535号に記載の処
理剤、即ち、加熱により被処理物から分解析出する有害
物質と反応して無害な塩化物を生成するアルカリ金属、
アルカリ金属化合物、アルカリ土類化合物、アルカリ土
類金属化合物に含まれる物質の中から少なくとも1種類
を選択、又は2種以上を混合したものを使用する。
The treating agent for an alkaline substance used in the present invention is disclosed in Japanese Patent Application Laid-Open No.
19616, JP-A-11-114535, a treatment agent, that is, an alkali metal which reacts with a harmful substance which is decomposed and precipitated from an object to be treated by heating to form a harmless chloride,
At least one kind is selected from alkali metal compounds, alkaline earth compounds, and substances contained in alkaline earth metal compounds, or a mixture of two or more kinds is used.

【0017】この中のアルカリ金属化合物は、炭酸水素
ナトリウム、炭酸ナトリウム、セスキ炭酸ナトリウム、
天然ソーダ、炭酸カリウム、炭酸水素カリウム、炭酸ナ
トリウムカリウム、水酸化ナトリウム、水酸化カリウム
から選択した単体、複数種の混合を含む。
The alkali metal compounds therein include sodium hydrogen carbonate, sodium carbonate, sodium sesquicarbonate,
Including simple soda selected from natural soda, potassium carbonate, potassium bicarbonate, sodium potassium carbonate, sodium hydroxide, potassium hydroxide, and a mixture of plural kinds.

【0018】また、上記(a)炭酸水素ナトリウムは、
別称、酸性炭酸ナトリウム、重炭酸ナトリウム、重炭酸
ソーダ。
Also, the above-mentioned (a) sodium hydrogen carbonate
Also known as acidic sodium carbonate, sodium bicarbonate, and sodium bicarbonate.

【0019】(b)炭酸ナトリウムは、別称、炭酸ソー
ダ、ソーダ、ソーダ灰、洗濯ソーダ、結晶ソーダ。
(B) Sodium carbonate is another name such as sodium carbonate, soda, soda ash, washing soda, and crystal soda.

【0020】(c)セスキ炭酸ナトリウムは、別称、二
炭酸一水素ナトリウム、三二炭酸水素ナトリウム、ナト
リウムセスキカーボネート、(d)天然ソーダは、別
称、トロナと称される。
(C) Sodium sesquicarbonate is another name, sodium monohydrogen dicarbonate, sodium tricarbonate, sodium sesquicarbonate. (D) Natural soda is another name, trona.

【0021】上記の加熱処理炉での外部加熱手段による
加熱温度は、被処理灰類からハロゲン系物質が分解析出
する温度で、且つ塩化物の融点以下の500℃〜800
℃が望ましい。
The heating temperature by the external heating means in the above-mentioned heat treatment furnace is a temperature at which the halogen-based substance is decomposed and precipitated from the ash to be treated and is 500 ° C. to 800 ° C. which is lower than the melting point of chloride.
C is desirable.

【0022】本発明でガラス化処理する被処理灰類は、
焼却灰、飛灰、汚泥焼却灰、乾燥汚泥、汚染土壌類のい
ずれか、又はこれらの混合物であればよい。
The ash to be treated to be vitrified in the present invention is:
Any of incineration ash, fly ash, sludge incineration ash, dry sludge, contaminated soil, or a mixture thereof may be used.

【0023】また、本発明によるガラス成形品は、ハロ
ゲン系物質を含む被処理灰類と、アルカリ物質からなる
処理剤とを混合して外部加熱手段による加熱処理炉で加
熱し、被処理灰類から分解析出したハロゲン系物質と処
理剤とを接触反応させて無害な塩化物を生成することで
分解ガスの無害化と被処理灰類の無害化を行うとともに
溶融ガラスを得、該溶融ガラスを取り出し、所定の形状
(板、ブロック、容器)に形成又はカレットに加工、発
泡材の原料として利用可能とする。
Further, the glass molded article according to the present invention is obtained by mixing ash to be treated containing a halogen-based substance and a treating agent comprising an alkali substance and heating the mixture in a heat treatment furnace by an external heating means. A halogen-based substance decomposed and precipitated from the material and a treating agent are contact-reacted to form harmless chlorides, thereby detoxifying the decomposed gas and detoxifying the ash to be treated, and obtaining a molten glass. Is taken out and formed into a predetermined shape (plate, block, container) or processed into a cullet, so that it can be used as a raw material of a foam material.

【0024】[0024]

【発明の実施の形態】以下、本発明の実施の形態を図面
によって説明する。本発明はガラス成分を含む処理灰
(焼却灰、飛灰、汚泥焼却灰等)、汚泥乾燥類、汚染土
壌類、(汚染海岸砂、工場、農地等)の一般土地等から
の処理物(以下、被処理灰類と称す)からハロゲン系物
質(塩素、臭素、沃素、フッ素、アスタチン類)、特
に、塩素を除去して無害化し、これをガラス化処理する
方法と、ガラス成形品(板材、ブロック材、ビン類、各
種容器等)又はカレットに加工した成形品を得るにあ
る。
Embodiments of the present invention will be described below with reference to the drawings. The present invention relates to treated ash (incinerated ash, fly ash, sludge incinerated ash, etc.) containing glass components, dried sludge, contaminated soils, and contaminated lands (contaminated coastal sands, factories, agricultural lands, etc.) from general land and the like (hereinafter, referred to as ash) And ash to be treated), by removing halogen-based substances (chlorine, bromine, iodine, fluorine, and astatins), particularly chlorine, to render them harmless and vitrifying them. Block material, bottles, various containers, etc.) or cullet.

【0025】図1はこの被処理灰類をガラス化処理する
方法を説明するための概念図で、1は加熱処理炉を示
し、該加熱処理炉1は、回転自在の回転円筒体1aと、
この回転円筒体1aの外周にガスダクトを形成して熱ガ
スの導入によって回転円筒体1aおよび回転円筒体1a
内の被処理物としての被処理灰類を外部から加熱する加
熱ジャケット1bとからなる。なおこの外部加熱手段
は、電気加熱手段(誘導加熱、抵抗加熱、マイクロ波加
熱)としてもよい。
FIG. 1 is a conceptual diagram for explaining a method of vitrifying the ash to be treated. Reference numeral 1 denotes a heat treatment furnace. The heat treatment furnace 1 includes a rotatable rotary cylindrical body 1a,
A gas duct is formed around the outer periphery of the rotating cylinder 1a, and the rotating cylinder 1a and the rotating cylinder 1a are formed by introducing hot gas.
And a heating jacket 1b for externally heating ash to be treated as an object to be treated therein. The external heating means may be an electric heating means (induction heating, resistance heating, microwave heating).

【0026】2は供給側ダクトで、被処理灰類と脱塩素
用の処理剤とを混合した混合物を加熱処理炉1の回転円
筒体1a内に導入する。3は排出側ダクトで、加熱処理
炉1で加熱処理した被処理灰類でガラス化したものを排
出する。
Reference numeral 2 denotes a supply duct, which introduces a mixture obtained by mixing the ash to be treated and the treating agent for dechlorination into the rotating cylindrical body 1a of the heat treatment furnace 1. Reference numeral 3 denotes a discharge-side duct which discharges vitrified ash that has been heat-treated in the heat treatment furnace 1.

【0027】回転円筒体1aは、鉄系の金属部材からな
り、図示は省略してあるが、内部に送り羽根を有し、一
端の供給口側は供給側ダクト2に、他端の排出口側は排
出側ダクト3に連通するとともに、支持ローラで回転自
在に支持され、且つ回転駆動手段で回転駆動されるよう
に構成されている。そして、回転円筒体1aの回転によ
って被処理灰類と処理剤の混合物は、供給口側から排出
口側に撹拌しながら移送されるようになっている。
The rotary cylinder 1a is made of an iron-based metal member, and although not shown, has a feed blade therein, and has a supply port at one end connected to the supply duct 2 and a discharge port at the other end. The side communicates with the discharge side duct 3, is rotatably supported by a support roller, and is configured to be rotationally driven by rotational driving means. The mixture of the ash to be treated and the treatment agent is transferred from the supply port side to the discharge port side while being stirred by the rotation of the rotary cylindrical body 1a.

【0028】また、加熱ジャケット1bと、供給側およ
び排出側ダクト2および3は固定され、回転円筒体1a
との回転接触部にはメカニカルシールが施されており、
回転接触部からのガス漏れを防止している。
The heating jacket 1b and the supply-side and discharge-side ducts 2 and 3 are fixed, and the rotating cylindrical body 1a
A mechanical seal is applied to the rotating contact part with
Gas leakage from the rotating contact part is prevented.

【0029】4は熱ガス発生手段で、LNG、LPG又
は石油等の燃料を燃焼して熱ガスを発生させ、加熱ジャ
ケット1b内に導入する。
Reference numeral 4 denotes a hot gas generating means for generating a hot gas by burning a fuel such as LNG, LPG or petroleum, and introducing the hot gas into the heating jacket 1b.

【0030】5は分解ガス処理手段で、ガス燃焼炉、排
ガス冷却手段、バグフィルタ等の清浄化手段を有し、加
熱処理炉1で加熱処理中に発生した分解ガスを導入して
燃焼し、燃焼後のガスを冷却し、バグフィルタで清浄化
して排出する。
Reference numeral 5 denotes a decomposed gas treatment means, which has a gas combustion furnace, an exhaust gas cooling means, a purifying means such as a bag filter, etc., and introduces the decomposed gas generated during the heat treatment in the heat treatment furnace 1 and burns it. The gas after combustion is cooled, cleaned with a bag filter and discharged.

【0031】6はガラス成形手段で、加熱処理炉1で加
熱処理され、有害成分が除去された被処理灰類でガラス
化したものを受け、これを成形する。7は固化手段で、
ガラス成形手段6で成形したガラス成形品を徐冷して固
化する。8は固化成形品回収手段で、固化手段7で固化
した成形品7aをコンベア等で移送し回収する。
Numeral 6 denotes a glass forming means for receiving vitrified ash which has been subjected to heat treatment in the heat treatment furnace 1 and from which harmful components have been removed, and forms it. 7 is a solidifying means,
The glass molded product formed by the glass forming means 6 is gradually cooled and solidified. Numeral 8 denotes a solidified molded product collecting means for transferring and collecting the molded product 7a solidified by the solidifying means 7 by a conveyor or the like.

【0032】なお、外部加熱手段が電気加熱とした場合
は、加熱ジャケット1bおよび熱ガス発生手段4は必要
としない。
When the external heating means is electric heating, the heating jacket 1b and the hot gas generating means 4 are not required.

【0033】次に被処理灰類のガラス化処理の一連の処
理方法について説明する。まず、熱ガス発生手段4でL
NG等の燃料を燃焼して熱ガスを発生させ、加熱ジャケ
ット1bに導入するとともに、回転円筒体1aを回転駆
動する。
Next, a series of treatment methods for vitrifying the ash to be treated will be described. First, the hot gas generating means 4
A fuel such as NG is burned to generate a hot gas, which is introduced into the heating jacket 1b and drives the rotary cylinder 1a to rotate.

【0034】次に、供給側ダクト2を介してハロゲン系
物質を含む被処理灰類と処理剤(例えば、炭酸水素ナト
リウム)を十分混合した混合物を供給側ダクト2を介し
て加熱処理炉1に供給する。処理剤は、通常粉体を使用
するが、勿論その形態は任意である。
Next, a mixture obtained by sufficiently mixing the ash containing a halogen-based substance and a treating agent (for example, sodium hydrogen carbonate) through the supply duct 2 is supplied to the heating furnace 1 through the supply duct 2. Supply. As the treatment agent, a powder is usually used, but the form is of course arbitrary.

【0035】投入される被処理灰類は、都市ゴミ焼却灰
や廃棄物焼却プラントから排出される飛灰等によってガ
ラス成分関係の含有量は異なるが、後者の飛灰における
ガラス成分関係の含有量(g/Kg)は、特公平6−3
8863号によれば、Ca:80〜100,K:30〜
45,Na:10〜30,SiO2:250〜500と
なっている。
The ash to be treated has a different glass component-related content due to municipal garbage incineration ash or fly ash discharged from a waste incineration plant, but the glass component-related content in the latter fly ash. (G / Kg) is 6-3
No. 8863, Ca: 80-100, K: 30-
45, Na: 10~30, SiO 2 : and has a 250 to 500.

【0036】一方、ソーダガラスの成分(重量%)は、
上記のようにSiO2:65〜75,Na2O:10〜2
0,CaO:5〜15,その他:Al23,MgO,F
23であることから、Si,Naを中心に成分調整す
ることでガラスを生成することができる。
On the other hand, the components (% by weight) of soda glass
SiO 2 as described above: 65~75, Na 2 O: 10~2
0, CaO: 5 to 15, other: Al 2 O 3 , MgO, F
Since it is e 2 O 3 , a glass can be produced by adjusting the components mainly with Si and Na.

【0037】即ち、焼却飛灰のガラス関係成分(g/K
g)が、Caが80〜100,Kが30〜45,Naが
10〜30,SiO2が250〜500である場合には
例えば、その中間値とガラス成分比から、ガラス成分の
不足する量を表1のように求めることができる。そし
て、表1から不足するSi,Naを追加し、アルカリ物
質の処理剤を添加する。
That is, glass-related components (g / K) of incinerated fly ash
The amount g) is, Ca is 80 to 100, K is 30-45, Na 10 to 30, for example in the case SiO 2 is 250 to 500, from the intermediate value and a glass component ratio, the lack of the glass component Can be obtained as shown in Table 1. Then, the insufficient Si and Na from Table 1 are added, and a treating agent for an alkaline substance is added.

【0038】[0038]

【表1】 [Table 1]

【0039】また、都市ゴミ焼却灰におけるガラス成分
関係のものは、特開平11−347515号にその一例
が示されているように、Ca:23.2,Si:8.
0,K:4.0,Na:3.5各重量%である。(バグ
フィルタにてCaを噴霧して排ガスを浄化していること
から、Ca分が多い傾向にある。) このように被処理灰類によってガラス成分関係が異なる
ので、追加成分と量とをあらかじめ灰の種類ごと調査し
て定めておく必要がある。
As for glass-related components in municipal incineration ash, as shown in JP-A-11-347515, Ca: 23.2, Si: 8.
0, K: 4.0, and Na: 3.5, respectively. (Since the exhaust gas is purified by spraying Ca with a bag filter, the Ca content tends to be large.) As described above, the glass component relationship differs depending on the ash to be treated. It is necessary to investigate and determine each type of ash.

【0040】被処理灰類におけるガラス成分は、一般的
にはNa2Oが不足しており、これを補うために、脱塩
素用の処理剤として使用した炭酸水素ナトリウム(Na
HCO3)とか、炭酸ナトリウム(Na2CO3)、(別
称、ソーダ灰)、セスキ炭酸ナトリウム(別称、天然ソ
ーダ)を添加混合する。
The glass component of the ash to be treated generally lacks Na 2 O. To compensate for this, sodium bicarbonate (Na) used as a treating agent for dechlorination was used.
HCO 3 ), sodium carbonate (Na 2 CO 3 ), (also called soda ash), and sodium sesquicarbonate (also called natural soda) are added and mixed.

【0041】上記の加熱処理炉1での加熱処理は、被処
理灰類から有害成分、特に、塩素系ガス(塩化水素)が
分解析出する温度と時間を事前に調査して、被処理灰類
固有の性質を把握し、調査結果を基に塩素系ガスが十分
析出する温度と時間(500℃〜800℃、好ましくは
600℃、1時間程度)で処理する。
In the heat treatment in the heat treatment furnace 1, the temperature and time at which harmful components, especially chlorine-based gas (hydrogen chloride), are decomposed and precipitated from the ash to be treated are investigated in advance, and the ash to be treated is The properties specific to the class are grasped, and the treatment is performed at a temperature and time (500 ° C. to 800 ° C., preferably 600 ° C., about 1 hour) at which the chlorine-based gas is sufficiently precipitated based on the investigation results.

【0042】なお、温度と時間は、加熱処理炉の状態
(大きさ、加熱手段など炉に依存する条件)、処理量、
処理時間、処理温度などにも関係するので、データを蓄
積しておく必要がある。
The temperature and time are determined by the condition of the heating furnace (conditions depending on the furnace such as the size and heating means), the amount of treatment,
Since it is related to the processing time, the processing temperature, and the like, it is necessary to accumulate data.

【0043】加熱処理炉での加熱処理は、図2(A)の
模式図に示すように、乾燥・脱塩素・ガラス化を一つの
加熱処理炉10で行うようにしてもよいし、又は図2
(B)のように乾燥・脱塩素炉11とガラス化処理炉1
2とを上下に配設し、乾燥・脱塩素炉11で脱塩素処理
した被処理灰類を、連通ダクト13を介してガラス化処
理炉12に導入し、ここで溶融ガラス化するようにして
もよく、被処理灰類の性状により選択する。
The heat treatment in the heat treatment furnace may be such that drying, dechlorination, and vitrification are performed in one heat treatment furnace 10, as shown in the schematic diagram of FIG. 2
Drying / dechlorination furnace 11 and vitrification furnace 1 as shown in FIG.
2 are disposed vertically, and the ash to be treated, which has been dechlorinated in the drying / dechlorination furnace 11, is introduced into the vitrification furnace 12 through the communication duct 13, where it is melted and vitrified. The choice is made according to the properties of the ash to be treated.

【0044】なお、これら加熱炉10,11,12は、
図1の加熱処理炉1と同じ構成の炉を使用できる。即
ち、内部に処理物の搬送と撹拌を行う回転送り羽根を備
えた回転円筒体と、外部加熱手段を備えた構成とする。
The heating furnaces 10, 11, and 12 are
A furnace having the same configuration as the heat treatment furnace 1 in FIG. 1 can be used. That is, a configuration is provided in which a rotating cylindrical body provided with rotating feed blades for carrying and stirring the processed material therein, and an external heating means are provided.

【0045】図1の加熱処理炉1での加熱処理は、「燃
焼、焼却」ではなく、低酸素雰囲気中での「蒸し焼き、
熱分解」での処理で、加熱により被処理灰類から分解析
出した有害な塩素系ガスとアルカリ物質からなる処理剤
と効果的に反応させ、有害な塩素系ガスを無害な塩類に
置換生成させる。
The heat treatment in the heat treatment furnace 1 shown in FIG. 1 is not "combustion and incineration" but "steaming,
In the `` pyrolysis '' treatment, the harmful chlorine-based gas decomposed and precipitated from the ash to be treated by heating is effectively reacted with a treating agent consisting of an alkaline substance, and the harmful chlorine-based gas is replaced with harmless salts. Let it.

【0046】即ち、処理剤として炭酸水素ナトリウム
(NaHCO3)を使用した場合、加熱処理炉1内にお
いて塩化水素(HCl)が発生すると、直ちに接触反応
して(NaHCO3)+(HCl)→(NaCl)+
(H2O)+(CO2)となり、無害な塩化ナトリウム
(NaCl)に置換生成され、分解ガス中の有害な塩化
水素が無くなり、分解ガスの無害化と、有害成分析出後
の処理灰類の無害化が同時に行われる。
That is, when sodium hydrogencarbonate (NaHCO 3 ) is used as a treating agent, when hydrogen chloride (HCl) is generated in the heat treatment furnace 1, a contact reaction occurs immediately and (NaHCO 3 ) + (HCl) → (HCl). NaCl) +
(H 2 O) + (CO 2 ), which is replaced and produced by harmless sodium chloride (NaCl), harmful hydrogen chloride in the decomposed gas is eliminated, and the decomposed gas is rendered harmless and treated ash after deposition of harmful components. Detoxification is performed at the same time.

【0047】上記のように加熱処理炉1内に脱塩素用の
処理剤を添加したことにより、無害な塩化物(NaC
l)が存在するが、この塩化物の融点は801℃であ
り、加熱処理炉での外部加熱手段による加熱温度を80
0℃以下としておけば、融解などによる塩素の析出とい
った問題は生じない。
By adding the treatment agent for dechlorination into the heat treatment furnace 1 as described above, harmless chlorides (NaC
l) is present, but the melting point of this chloride is 801 ° C., and the heating temperature of the heat treatment furnace by external heating means is 80 ° C.
If the temperature is set to 0 ° C. or lower, a problem such as precipitation of chlorine due to melting does not occur.

【0048】加熱処理炉1で得られた溶融ガラスは、ガ
ラス成形手段6に導入し、ここで所定の形状(板、ブロ
ック、容器等)に成形し(又はカレットを得)、固化手
段7で徐冷しつつ固形して成形品7aを得、固化成形品
回収手段8で回収する。
The molten glass obtained in the heat treatment furnace 1 is introduced into a glass forming means 6, where it is formed into a predetermined shape (plate, block, container, etc.) (or cullet is obtained) and solidified by a solidifying means 7. The molded product 7a is solidified while being gradually cooled, and is collected by the solidified molded product collecting means 8.

【0049】従って、無害化した被処理灰類と、無害化
処理用の処理剤と同成分のアルカリ物質とを溶解するこ
とでガラス成形品を得ることができ、被処理灰類の有効
再利用ができる。また溶融ガラスは、特開平11−17
1661のように発泡材の原料としても利用可能であ
る。
Accordingly, a glass molded article can be obtained by dissolving the detoxified ash to be treated and an alkali substance of the same component as the detoxifying treatment agent, and effectively reusing the ash to be treated. Can be. Further, the molten glass is disclosed in
It can also be used as a raw material of a foaming material like 1661.

【0050】一方、加熱処理炉1での加熱処理時に発生
した分解ガスは、処理剤との接触反応によって無害化さ
れ、有毒な塩素系ガス(塩化水素、塩素ガス)を含んで
いないが、更に安全を図るために、分解ガス処理手段5
に送り込み、ここで燃焼処理し、燃焼後のガスは冷却
(温水化して回収)され、バグフィルタを介して排出す
る。なお、加熱処理炉1を加熱した後の熱ガスは、熱交
換器等により排熱を利用した後、この分解ガス処理手段
5に送り燃焼処理した後排出すると熱エネルギーの有効
利用が図れる。
On the other hand, the decomposition gas generated during the heat treatment in the heat treatment furnace 1 is rendered harmless by the contact reaction with the treating agent and does not contain toxic chlorine-based gases (hydrogen chloride, chlorine gas). In order to ensure safety, the decomposition gas processing means 5
, Where it is subjected to combustion treatment, and the gas after combustion is cooled (recovered by warming) and discharged through a bag filter. The heat gas after heating the heat treatment furnace 1 uses exhaust heat by a heat exchanger or the like, and then is sent to the decomposed gas processing means 5 to be burned and then discharged, so that thermal energy can be effectively used.

【0051】[0051]

【発明の効果】以上のように本発明は、ハロゲン系物質
で汚染されているガラス成分を含む被処理灰類(焼却
灰、飛灰、汚泥焼却灰、汚泥乾燥類、汚染土壌類)の被
処理物と、アルカリ物質からなる脱塩素用の処理剤とを
混合して加熱処理して脱塩素処理を行うとともに、処理
剤に含まれているガラス成分でガラス化処理するように
したので、次の効果を奏する。 (1)ハロゲン系物質で汚染されているガラス成分を含
む、被処理灰類は、焼却灰、飛灰、汚泥焼却灰、乾燥汚
泥、汚染土壌類などの被処理物を無害化する際に使用す
るアルカリ物質を、脱塩素による塩化物形成と、ガラス
形成に必要な成分量となるように添加することで、被処
理物の無害化、発生ガスの無害化、と合わせて被処理灰
類をガラス化できる。 (2)ガラス化した被処理物中には、有害なダイオキシ
ン類は含まないので多目的に有効利用できる。
As described above, the present invention relates to the treatment of ash to be treated (incinerated ash, fly ash, sludge incinerated ash, sludge dried, contaminated soils) containing glass components contaminated with halogen-based substances. The treated product and the treatment agent for dechlorination consisting of an alkali substance were mixed and heated to perform the dechlorination treatment, and the glass component contained in the treatment agent was vitrified. Has the effect of (1) Ashes to be treated, including glass components contaminated with halogen-based substances, are used to detoxify incineration ash, fly ash, sludge incineration ash, dry sludge, contaminated soil, etc. The ash to be treated is added together with the alkali substance to be added, so that the amount of components required for the formation of chloride by dechlorination and the formation of glass will be detoxified and the generated gas detoxified. Can be vitrified. (2) The harmful dioxins are not contained in the vitrified material to be processed, so that it can be effectively used for multiple purposes.

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

【図1】本発明の実施の形態の概念図FIG. 1 is a conceptual diagram of an embodiment of the present invention.

【図2】本発明の実施の形態の模式図FIG. 2 is a schematic diagram of an embodiment of the present invention.

【符号の説明】 1…加熱処理炉 1a…回転円筒体 1b…加熱ジャケット 2…供給側ダクト 3…排出側ダクト 4…熱ガス発生手段 5…分解ガス処理手段 6…ガラス成形手段 7…固化手段 8…固化成形品回収手段[Description of Signs] 1 ... Heat treatment furnace 1a ... Rotating cylindrical body 1b ... Heating jacket 2 ... Supply side duct 3 ... Discharge side duct 4 ... Hot gas generation means 5 ... Decomposition gas treatment means 6 ... Glass forming means 7 ... Solidification means 8 ... means for collecting solidified molded products

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C03B 1/00 B09B 3/00 304K Fターム(参考) 2E191 BB01 BC01 BC02 BD01 BD11 4D004 AA36 AA37 AA41 AB06 BA10 CA14 CA15 CA24 CA29 CA34 CC11 CC13 DA02 DA03 DA06 DA10 4G014 AA00 AC00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C03B 1/00 B09B 3/00 304K F term (Reference) 2E191 BB01 BC01 BC02 BD01 BD11 4D004 AA36 AA37 AA41 AB06 BA10 CA14 CA15 CA24 CA29 CA34 CC11 CC13 DA02 DA03 DA06 DA10 4G014 AA00 AC00

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 ハロゲン系物質を含む被処理灰類と、ガ
ラス成分を含むアルカリ物質からなる処理剤とを混合し
て外部加熱手段による加熱処理炉で加熱し、被処理灰類
から分解析出したハロゲン系物質と処理剤とを接触反応
させて無害な塩化物を生成することで分解ガスの無害化
と被処理灰類の無害化およびガラス化を行うことを特徴
とする処理灰類によるガラス化処理方法。
An ash to be treated containing a halogen-based substance and a treating agent comprising an alkali substance containing a glass component are mixed and heated in a heat treatment furnace by an external heating means to decompose and precipitate from the ash to be treated. Glass with treated ash characterized by detoxifying decomposed gas, detoxifying ash to be treated and vitrifying by producing a harmless chloride by contacting the treated halogen-based material with a treating agent Treatment method.
【請求項2】 ハロゲン系物質を含む被処理物と、ガラ
ス成分を含むアルカリ物質からなる処理剤とを混合して
外部加熱手段による加熱処理炉で加熱し、被処理灰類か
ら分解析出したハロゲン系物質と処理剤とを接触反応さ
せて無害な塩化物を生成することで分解ガスの無害化と
被処理灰類の無害化を行うとともに、ソーダガラスの主
成分であるSi,Na,Caの添加量を制御することで
ガラス化することを特徴とする処理灰類によるガラス化
処理方法。
2. An object to be treated containing a halogen-based substance and a treating agent made of an alkaline substance containing a glass component are mixed and heated in a heat treatment furnace by an external heating means to be decomposed and precipitated from the ash to be treated. By causing a harmless chloride by contacting a halogen-based substance with a treating agent to detoxify decomposed gas and detoxifying ash to be treated, Si, Na, and Ca, which are main components of soda glass, A vitrification method using treated ash, characterized in that vitrification is performed by controlling the amount of ash added.
【請求項3】 ソーダガラスの主成分の添加量(重量
%)は、SiO2が65〜75、Na2Oが10〜20、
CaOが5〜15の成分比としたことを特徴とする請求
項2記載の処理灰類によるガラス化処理方法。
3. The addition amount (% by weight) of the main component of soda glass is 65 to 75 for SiO 2 , 10 to 20 for Na 2 O,
The vitrification method using treated ash according to claim 2, wherein the CaO has a component ratio of 5 to 15.
【請求項4】 アルカリ物質は、加熱により被処理灰類
から分解析出するハロゲン系物質と反応して無害な塩化
物を生成するアルカリ金属、アルカリ金属化合物、アル
カリ土類化合物、アルカリ土類金属化合物に含まれる物
質の中から少なくとも1種類を選択、又は2種以上を混
合したものであることを特徴とする請求項1又は2記載
の処理灰類によるガラス化処理方法。
4. An alkali material, an alkali metal, an alkali metal compound, an alkaline earth compound, an alkaline earth metal, which reacts with a halogen-based material decomposed and precipitated from ash to be treated by heating to form a harmless chloride. 3. The vitrification method using treated ash according to claim 1 or 2, wherein at least one kind is selected from substances contained in the compound, or two or more kinds are mixed.
【請求項5】 外部加熱手段による加熱温度は、500
℃〜800℃としたことを特徴とする請求項1又は2記
載の処理灰類によるガラス化処理方法。
5. The heating temperature of the external heating means is 500
The vitrification method using the treated ash according to claim 1 or 2, wherein the temperature is set to be from 800C to 800C.
【請求項6】 被処理灰類は、焼却灰、飛灰、汚泥焼却
灰、乾燥汚泥、汚染土壌類のいずれか、又は混合物であ
ることを特徴とする請求項1又は2記載の処理灰類によ
るガラス化処理方法。
6. The treated ash according to claim 1, wherein the ash to be treated is any one of incineration ash, fly ash, sludge incineration ash, dry sludge, and contaminated soils, or a mixture thereof. Vitrification treatment method.
【請求項7】 ハロゲン系物質を含む被処理灰類と、ア
ルカリ物質からなる処理剤とを混合して外部加熱手段に
よる加熱処理炉で加熱し、被処理灰類から分解析出した
ハロゲン系物質と処理剤とを接触反応させて無害な塩化
物を生成することで分解ガスの無害化と被処理灰類の無
害化を行うとともに溶融ガラスを得、該溶融ガラスを所
定の形状に成形して成形品としたことを特徴とする処理
灰類によるガラス成形品。
7. A ash to be treated containing a halogen-based substance and a treating agent comprising an alkali substance are mixed and heated in a heat treatment furnace by an external heating means, and the ash to be treated is decomposed and precipitated from the ash to be treated. And the treating agent are contact-reacted to produce harmless chlorides, thereby detoxifying the decomposed gas and detoxifying the ash to be treated and obtaining molten glass, and forming the molten glass into a predetermined shape. A glass molded product made from treated ash, which is a molded product.
JP2000045367A 2000-02-23 2000-02-23 Method of vitrifying treatment with treated ash and molded product Pending JP2001233621A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000045367A JP2001233621A (en) 2000-02-23 2000-02-23 Method of vitrifying treatment with treated ash and molded product

Publications (1)

Publication Number Publication Date
JP2001233621A true JP2001233621A (en) 2001-08-28

Family

ID=18567963

Family Applications (1)

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

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007296412A (en) * 2006-02-27 2007-11-15 Okutama Kogyo Co Ltd Fly ash treatment method
CN108500026A (en) * 2017-02-24 2018-09-07 永续发展股份有限公司 Waste vitrification treatment method and apparatus using cycle and plasma

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007296412A (en) * 2006-02-27 2007-11-15 Okutama Kogyo Co Ltd Fly ash treatment method
CN108500026A (en) * 2017-02-24 2018-09-07 永续发展股份有限公司 Waste vitrification treatment method and apparatus using cycle and plasma

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