JP2000320813A - Melting furnace exhaust gas treatment method - Google Patents

Melting furnace exhaust gas treatment method

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Publication number
JP2000320813A
JP2000320813A JP11126807A JP12680799A JP2000320813A JP 2000320813 A JP2000320813 A JP 2000320813A JP 11126807 A JP11126807 A JP 11126807A JP 12680799 A JP12680799 A JP 12680799A JP 2000320813 A JP2000320813 A JP 2000320813A
Authority
JP
Japan
Prior art keywords
exhaust gas
melting furnace
gas
incineration
combustion chamber
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
JP11126807A
Other languages
Japanese (ja)
Inventor
Tetsuya Usuki
徹也 薄木
Masaaki Nishino
雅明 西野
Naoyuki Isozaki
直之 磯崎
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP11126807A priority Critical patent/JP2000320813A/en
Publication of JP2000320813A publication Critical patent/JP2000320813A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【課題】 専用の排ガス処理設備を設ける必要がなく、
かつ溶融炉から排出される排ガスのエネルギーを回収す
ることができる溶融炉排ガスの処理方法を提供するこ
と。 【解決手段】 ごみ焼却施設に設けられた焼却残渣溶融
炉の排ガスの処理方法であって、還元性雰囲気で操業す
る溶融炉30で焼却残渣を溶融処理した際に発生する排
ガスをごみ焼却炉10の2次燃焼室14の入口部へ導入
する。
(57) [Abstract] [Problem] There is no need to provide a dedicated exhaust gas treatment facility.
To provide a method for treating exhaust gas of a melting furnace capable of recovering energy of the exhaust gas discharged from the melting furnace. SOLUTION: This is a method for treating exhaust gas from an incineration residue melting furnace provided in a refuse incineration facility, wherein the exhaust gas generated when the incineration residue is melt-processed in a melting furnace 30 operated in a reducing atmosphere is used as a waste incinerator. To the inlet of the secondary combustion chamber 14.

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、ごみ焼却残渣を還
元性雰囲気で操業する溶融炉で溶融処理した際に発生す
る排ガスの処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating exhaust gas generated when a refuse incineration residue is melt-processed in a melting furnace operated in a reducing atmosphere.

【0002】[0002]

【従来の技術】都市ごみの大部分はごみ焼却施設で焼却
処理された後、埋め立て処分されている。しかし、この
焼却に伴って発生する焼却残渣のうち、特に飛灰の処分
に際しては、さらに、その中に含まれる重金属を安定化
する処理を施さなければ埋め立て処分をすることができ
ない。又、焼却灰についても、埋立地の確保が困難にな
るにしたがって、その減容化と安定化が必要な状況にな
ってきた。
2. Description of the Related Art Most municipal solid waste is incinerated in a refuse incineration facility and then disposed of in landfill. However, among the incineration residues generated by the incineration, especially in the disposal of fly ash, landfill disposal cannot be performed unless a treatment for stabilizing heavy metals contained therein is further performed. Also, as incineration ash becomes more difficult to secure in landfills, it has become necessary to reduce its volume and stabilize it.

【0003】このため、焼却残渣の処理については、減
容化と重金属の安定化が同時に行われる溶融法による処
理が行われるようになってきた。焼却残渣の溶融処理は
種々の方法で行われているが、溶融法によっては、焼却
残渣中の未燃分などの分解によって生成したCOガス,
2 ガスなどにより、炉内が還元性雰囲気に保持され
る。この結果、COガス,H2 ガスがそれぞれ数十%に
も及ぶ濃度で含まれている排ガスが溶融炉から排出され
る。
[0003] For this reason, the treatment of incineration residues has been carried out by a melting method in which volume reduction and stabilization of heavy metals are simultaneously performed. Melting treatment of incineration residues is performed by various methods. However, depending on the melting method, CO gas generated by decomposition of unburned matter in the incineration residues,
The inside of the furnace is kept in a reducing atmosphere by H 2 gas or the like. As a result, the exhaust gas containing the CO gas and the H 2 gas at concentrations of several tens of percent each is discharged from the melting furnace.

【0004】従来、焼却残渣の溶融炉を有するごみ焼却
施設において、ごみの焼却処理とその焼却残渣の溶融処
理は、例えば、特開平7−77318号公報に示された
方法によって行われている。特開平7−77318号公
報に示された方法においては、焼却炉でごみを燃焼させ
た際に排出される焼却灰と焼却炉から発生するごみ焼却
排ガスを集塵処理した際に捕集される飛灰が溶融炉へ送
られ、焼却残渣(焼却灰と飛灰)の溶融処理が行われ
る。この際、溶融炉から排出された排ガスに空気を加え
て可燃性ガスを燃焼させ、次いで集塵処理をした後、大
気放散している。
Conventionally, in a refuse incineration facility having a melting furnace for incineration residues, incineration of the refuse and melting of the incineration residues are carried out, for example, by the method disclosed in JP-A-7-77318. In the method disclosed in Japanese Patent Application Laid-Open No. 7-77318, incineration ash discharged when burning refuse in an incinerator and refuse incineration exhaust gas generated from the incinerator are collected during dust collection processing. Fly ash is sent to the melting furnace, where the incineration residue (incinerated ash and fly ash) is melted. At this time, air is added to the exhaust gas discharged from the melting furnace to burn flammable gas, and then, after a dust collection process, it is released to the atmosphere.

【0005】[0005]

【発明が解決しようとする課題】還元性雰囲気の溶融炉
から発生する排ガスはCOガス,H2 ガスなどの可燃性
ガスを多量に含むものであるが、上記従来技術において
は、その可燃性ガスを燃焼させてしまうので、排ガスが
有するエネルギーが廃棄されている。しかも、その排ガ
スを大気放出するためには、燃焼装置及び集塵機などよ
りなる専用の排ガス処理設備を設けなければならず、溶
融炉の建設に要する設備費が嵩むと共に、溶融炉の操業
管理が煩雑になっている。
Exhaust gas generated from a melting furnace in a reducing atmosphere contains a large amount of flammable gas such as CO gas and H 2 gas. As a result, the energy of the exhaust gas is discarded. Moreover, in order to release the exhaust gas to the atmosphere, a dedicated exhaust gas treatment facility consisting of a combustion device and a dust collector must be provided, which increases the equipment costs required for the construction of the melting furnace and complicates the operation management of the melting furnace. It has become.

【0006】本発明は、上記の課題を解決するためにな
されたものであり、専用の排ガス処理設備を設ける必要
がなく、かつ溶融炉から排出される排ガスのエネルギー
を回収することができる溶融炉排ガスの処理方法を提供
することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and does not require the provision of a dedicated exhaust gas treatment facility, and can recover the energy of the exhaust gas discharged from the melting furnace. An object of the present invention is to provide a method for treating exhaust gas.

【0007】[0007]

【課題を解決するための手段】上記の課題は次の発明に
より解決される。
The above object is achieved by the following invention.

【0008】第一の発明は、ごみ焼却施設に設けられた
焼却残渣溶融炉の排ガスの処理方法において、還元性雰
囲気で操業する溶融炉で焼却残渣を溶融処理した際に発
生する排ガスを、ごみ焼却炉内へ導入することを特徴と
する溶融炉排ガスの処理方法である。
[0008] The first invention is a method of treating exhaust gas from an incineration residue melting furnace provided in a refuse incineration facility, wherein the exhaust gas generated when the incineration residue is melt-processed in a melting furnace operated in a reducing atmosphere is treated as waste. This is a method for treating exhaust gas from a melting furnace, which is introduced into an incinerator.

【0009】この発明によれば、COガス,H2 ガスな
どの可燃性ガスが多量に含まれている溶融炉排ガスをご
み焼却炉内へ導入し、ごみ焼却排ガスと混合して燃焼さ
せるので、その燃焼熱を回収することができる。
According to the present invention, the waste gas from the melting furnace, which contains a large amount of combustible gas such as CO gas and H 2 gas, is introduced into the waste incinerator, and is mixed with the waste gas and burned. The heat of combustion can be recovered.

【0010】第二の発明は、焼却残渣を溶融処理した際
に発生する排ガスを焼却炉の2次燃焼室の入口部へ導入
することを特徴とする第一の発明の溶融炉排ガスの処理
方法である。
According to a second aspect of the present invention, there is provided a method for treating exhaust gas of a melting furnace according to the first aspect, wherein exhaust gas generated when the incineration residue is melted is introduced into an inlet of a secondary combustion chamber of an incinerator. It is.

【0011】この発明によれば、溶融炉排ガスを2次燃
焼が行われる前の箇所である2次燃焼室の入口部へ導入
するので、焼却排ガス中のNOX とCOガス,H2 ガス
との反応によって還元されるNOX の量が増加し、排ガ
ス中のNOX の濃度が低減される。
According to this invention, since the introduction into the inlet portion of the secondary combustion chamber is a portion before the melting furnace exhaust gases secondary combustion takes place, NO X and CO gas in incineration flue gas, and H 2 gas the reaction amount of the NO X to be reduced is increased by a, the concentration of the NO X in the exhaust gas is reduced.

【0012】[0012]

【発明の実施の形態】図1は本発明による溶融炉排ガス
の処理方法に係る実施の形態の一例を示す図である。こ
こで、10は焼却炉、40は都市ごみを示す。焼却炉の
燃焼室11には、搬送機能を有するストーカ12が設け
られている。14は燃焼室の上部に設けられ、燃焼室の
各所で発生した焼却排ガスの混合を促進させるための中
間天井である。そして、15は焼却炉の上部に設けられ
た2次燃焼室、16はボイラ、ガスクーラーなどのガス
冷却設備、17は酸性ガス除去装置及び集塵機よりなる
排ガス処理設備である。又、25は焼却残渣の貯槽、3
0は焼却残渣を溶融処理する溶融炉である。
FIG. 1 is a diagram showing an example of an embodiment of a method for treating exhaust gas from a melting furnace according to the present invention. Here, 10 indicates an incinerator and 40 indicates municipal waste. A stoker 12 having a transfer function is provided in a combustion chamber 11 of the incinerator. Reference numeral 14 denotes an intermediate ceiling provided at an upper portion of the combustion chamber for promoting mixing of incineration exhaust gas generated at various points in the combustion chamber. Reference numeral 15 denotes a secondary combustion chamber provided at an upper part of the incinerator, 16 denotes gas cooling equipment such as a boiler and a gas cooler, and 17 denotes an exhaust gas treatment equipment including an acid gas removing device and a dust collector. 25 is a storage tank for incineration residues, 3
Numeral 0 denotes a melting furnace for melting the incineration residue.

【0013】焼却炉10へ投入されたごみ40はストー
カ12の上を搬送されながら、乾燥、燃焼、後燃焼の各
過程を経て灰化され、焼却灰となって排出される。焼却
灰は焼却残渣貯槽25へ送られる。又、ストーカ12上
の各所で発生したごみ焼却排ガスはその組成がそれぞれ
異なるが、これらの排ガスは2次燃焼室の入口部である
ガス混合部14へ流れてきた段階で混合され、2次燃焼
室15へ流入する。ガス混合部14(2次燃焼室入口
部)にはガス吹き込みノズル18が設けられており、溶
融炉30で発生した排ガスの吹き込みが行われる。この
溶融炉排ガスは、その組成の一例を示せば、表1のごと
くであり、COガス,H2 ガスなどの可燃性ガスを多量
に含んでいる。
The refuse 40 put into the incinerator 10 is ashed through drying, burning and post-combustion processes while being conveyed on the stoker 12, and is discharged as incinerated ash. The incineration ash is sent to the incineration residue storage tank 25. Further, although the incineration exhaust gas generated at various places on the stoker 12 has different compositions, these exhaust gases are mixed at the stage where they flow into the gas mixing section 14 which is the inlet of the secondary combustion chamber, and are subjected to the secondary combustion. It flows into the chamber 15. A gas injection nozzle 18 is provided in the gas mixing section 14 (the inlet of the secondary combustion chamber), and the exhaust gas generated in the melting furnace 30 is injected. An example of the composition of this melting furnace exhaust gas is as shown in Table 1, and contains a large amount of combustible gas such as CO gas and H 2 gas.

【0014】[0014]

【表1】 [Table 1]

【0015】このため、この溶融炉排ガスの吹き込みに
よって、ガス混合部14においては、CO,H2 などの
還元性ガスの量が増加し、燃焼室11で生成したNOX
が減少する。次いで、ガス吹き込みノズル18より下流
側の2次燃焼室15に設けられた空気吹き込みノズル1
9から2次燃焼用空気の吹き込みが行われ、排ガスの完
全燃焼が行われる。なお、上記のガス吹き込み及び2次
燃焼用空気の吹き込み方法については、後述する。
For this reason, the amount of reducing gas such as CO and H 2 increases in the gas mixing section 14 due to the blowing of the melting furnace exhaust gas, and the NO x generated in the combustion chamber 11 is increased.
Decrease. Next, the air blowing nozzle 1 provided in the secondary combustion chamber 15 downstream of the gas blowing nozzle 18
From 9 on, secondary combustion air is blown, and complete combustion of exhaust gas is performed. The method of blowing the gas and the secondary combustion air will be described later.

【0016】2次燃焼室15から排出した排ガスは、ガ
ス冷却設備16へ送られ、熱回収される。熱回収された
焼却排ガスは、排ガス処理設備17へ送られ、塩化水素
などの酸性ガスの除去処理と除塵処理がなされた後、煙
突から放散される。排ガス処理設備17の除塵処理の際
に捕集された飛灰は、焼却残渣貯槽25へ送られる。焼
却残渣貯槽25に集められた焼却残渣(焼却灰と飛灰)
は、溶融炉30へ装入されて溶融処理され、溶融スラグ
となって排出される。
The exhaust gas discharged from the secondary combustion chamber 15 is sent to a gas cooling facility 16 where heat is recovered. The heat-recovered incineration exhaust gas is sent to an exhaust gas treatment facility 17 where it is subjected to a treatment for removing acidic gas such as hydrogen chloride and a dust removal treatment, and then emitted from a chimney. Fly ash collected during the dust removal processing of the exhaust gas treatment equipment 17 is sent to the incineration residue storage tank 25. Incineration residue (incineration ash and fly ash) collected in the incineration residue storage tank 25
Is charged into the melting furnace 30 and subjected to a melting process, and is discharged as a molten slag.

【0017】溶融炉30は密閉タイプの電気抵抗式の炉
であって、焼却残渣の溶融物中に浸漬された電極31の
間の通電によって、電気抵抗熱を発生させ、装入された
焼却残渣を溶融する炉である。この炉による溶融処理に
おいては、焼却残渣の加熱・溶融中に、焼却残渣中の未
燃焼分などの分解によってCO,HX などの可燃性ガス
(還元性ガス)が生成し、炉内が還元性雰囲気になる。
この溶融炉排ガスは、上述のように、焼却炉へ送られ
る。
The melting furnace 30 is a closed-type electric resistance type furnace, which generates electric resistance heat by energizing between the electrodes 31 immersed in the melted incineration residue, and the charged incineration residue. Is a furnace that melts. In the melt-processing by the furnace during the heating and melting of incineration residue, CO by decomposition of such unburnt incineration residue, combustible gas (reducing gas) is produced, such as H X, the furnace reduction It becomes a sexual atmosphere.
This melting furnace exhaust gas is sent to the incinerator as described above.

【0018】上記のようにして行われるごみの焼却とそ
の焼却残渣の溶融処理において、溶融炉30で発生した
排ガスは、その全量が焼却炉のガス混合部14へ吹き込
まれる。又、焼却炉の2次燃焼室15へは空気が吹き込
まれるが、2次燃焼室15の出口には温度計20及び酸
素濃度計21が設けられており、これらの測定値に基づ
いて、空気吹き込みノズル19から吹き込まれる2次燃
焼用空気の流量が制御される。そのために、制御装置2
2、2次燃焼用空気の流量調節ダンパー23、2次燃焼
用送風機24が設けられており、2次燃焼室15から排
出される焼却排ガスの温度及び酸素濃度が所定値になる
ように調節される。
In the incineration of the refuse and the melting treatment of the incineration residue performed as described above, the entire amount of the exhaust gas generated in the melting furnace 30 is blown into the gas mixing section 14 of the incinerator. Although air is blown into the secondary combustion chamber 15 of the incinerator, a thermometer 20 and an oxygen concentration meter 21 are provided at the outlet of the secondary combustion chamber 15, and based on these measured values, the air is measured. The flow rate of the secondary combustion air blown from the blowing nozzle 19 is controlled. Therefore, the control device 2
2, a secondary combustion air flow control damper 23 and a secondary combustion blower 24 are provided, and the temperature and oxygen concentration of the incineration exhaust gas discharged from the secondary combustion chamber 15 are adjusted to predetermined values. You.

【0019】上記のように、溶融炉排ガスを焼却炉10
へ導入すれば、溶融炉専用の燃焼装置及び集塵機などの
排ガス処理設備を設ける必要がなくなる。このため、燃
焼装置の失火に対する監視作業などの付帯設備に関わる
作業がなくなり、溶融炉の操業が容易になる。
As described above, the exhaust gas from the melting furnace is discharged from the incinerator 10
In this case, there is no need to provide a combustion device dedicated to the melting furnace and an exhaust gas treatment facility such as a dust collector. For this reason, work related to the auxiliary equipment such as monitoring work for misfire of the combustion device is eliminated, and the operation of the melting furnace is facilitated.

【0020】なお、この実施の形態においては、溶融炉
排ガスが焼却炉のガス混合部14へ導入されているが、
溶融炉排ガスが焼却炉の何れの箇所に導入されても、2
次燃焼室15へ流入した段階で燃焼し、その燃焼熱はガ
ス冷却設備16で回収される。このため、エネルギー回
収だけの観点からすれば、溶融炉排ガスの導入箇所は限
定されない。しかし、燃焼室11で生成したNOX を減
少させようとする場合には、溶融炉排ガスをガス混合部
14へ導入して還元性ガスの量を増加させることが必要
である。
In this embodiment, the melting furnace exhaust gas is introduced into the gas mixing section 14 of the incinerator.
No matter where the exhaust gas from the melting furnace is introduced into the incinerator,
The fuel burns at the stage where it flows into the next combustion chamber 15, and the heat of combustion is recovered by the gas cooling facility 16. For this reason, from the viewpoint of energy recovery only, there is no limitation on the location where the melting furnace exhaust gas is introduced. However, when attempting to reduce the NO X generated in the combustion chamber 11, it is necessary to the melting furnace exhaust gases increase the amount of introduced into the gas mixing portion 14 a reducing gas.

【0021】[0021]

【発明の効果】本発明によれば、還元性雰囲気で操業す
る溶融炉の排ガスをごみ焼却炉内へ導入するので、溶融
炉排ガス中のCOガス,H2 ガスなどの可燃性ガスが2
次燃焼室で燃焼し、その燃焼熱が回収される。さらに、
溶融炉専用の排ガス処理設備を設ける必要がなく、溶融
炉の操業が容易になると共に、ごみ焼却施設の建設費が
軽減される。
According to the present invention, since the exhaust gas of a melting furnace operated in a reducing atmosphere is introduced into a refuse incinerator, the flammable gas such as CO gas and H 2 gas in the exhaust gas of the melting furnace is reduced to 2 %.
Combustion occurs in the next combustion chamber, and the heat of combustion is recovered. further,
It is not necessary to provide an exhaust gas treatment facility dedicated to the melting furnace, so that the operation of the melting furnace becomes easy and the construction cost of the waste incineration facility is reduced.

【0022】特に、溶融炉の排ガスを焼却炉内のガス混
合部へ導入した場合には、ガス混合部におけるCO,H
2 などのガスが増加し、排ガス中のNOX の濃度が低減
される。
In particular, when the exhaust gas from the melting furnace is introduced into the gas mixing section in the incinerator, CO, H in the gas mixing section is reduced.
Gas such increases 2, the concentration of the NO X in the exhaust gas is reduced.

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

【図1】本発明による溶融炉排ガスの処理方法に係る実
施の形態の一例を示す図である。
FIG. 1 is a diagram showing an example of an embodiment according to a method for treating exhaust gas from a melting furnace according to the present invention.

【符号の説明】[Explanation of symbols]

10 焼却炉 11 燃焼室 12 ストーカ 13 中間天井 14 ガス混合部 15 2次燃焼室 16 ガス冷却設備 17 排ガス処理設備 18 ガス吹き込みノズル 19 空気吹き込みノズル 20 温度計 21 酸素濃度計 22 制御装置 23 2次燃焼用空気の流量調節ダンパー 24 2次燃焼用送風機 25 焼却残渣の貯槽 30 電気抵抗式溶融炉 40 都市ごみ Reference Signs List 10 incinerator 11 combustion chamber 12 stoker 13 intermediate ceiling 14 gas mixing section 15 secondary combustion chamber 16 gas cooling equipment 17 exhaust gas treatment equipment 18 gas injection nozzle 19 air injection nozzle 20 thermometer 21 oxygen concentration meter 22 control device 23 secondary combustion Air flow control damper for secondary use 24 Blower for secondary combustion 25 Storage tank for incineration residue 30 Electric melting furnace 40 Municipal solid waste

───────────────────────────────────────────────────── フロントページの続き (72)発明者 磯崎 直之 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 Fターム(参考) 3K061 AA23 AB03 AC01 AC03 BA05 CA11 DA12 DA17 3K065 AB03 AC01 AC03 BA05 HA01 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Naoyuki Isozaki 1-2-1, Marunouchi, Chiyoda-ku, Tokyo F-term (reference) 3K061 AA23 AB03 AC01 AC03 BA05 CA11 DA12 DA17 3K065 AB03 AC01 AC03 BA05 HA01

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ごみ焼却施設に設けられた焼却残渣溶融
炉の排ガスの処理方法において、還元性雰囲気で操業す
る溶融炉で焼却残渣を溶融処理した際に発生する排ガス
をごみ焼却炉内へ導入することを特徴とする溶融炉排ガ
スの処理方法。
1. A method for treating exhaust gas from an incineration residue melting furnace provided in a refuse incineration facility, wherein the exhaust gas generated when the incineration residue is melt-processed in a melting furnace operated in a reducing atmosphere is introduced into the refuse incineration furnace. A method for treating exhaust gas from a melting furnace.
【請求項2】 焼却残渣を溶融処理した際に発生する排
ガスを焼却炉の2次燃焼室の入口部へ導入することを特
徴とする請求項1に記載の溶融炉排ガスの処理方法。
2. The method according to claim 1, wherein the exhaust gas generated when the incineration residue is melted is introduced into an inlet of a secondary combustion chamber of the incinerator.
JP11126807A 1999-05-07 1999-05-07 Melting furnace exhaust gas treatment method Pending JP2000320813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11126807A JP2000320813A (en) 1999-05-07 1999-05-07 Melting furnace exhaust gas treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11126807A JP2000320813A (en) 1999-05-07 1999-05-07 Melting furnace exhaust gas treatment method

Publications (1)

Publication Number Publication Date
JP2000320813A true JP2000320813A (en) 2000-11-24

Family

ID=14944456

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11126807A Pending JP2000320813A (en) 1999-05-07 1999-05-07 Melting furnace exhaust gas treatment method

Country Status (1)

Country Link
JP (1) JP2000320813A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007127355A (en) * 2005-11-04 2007-05-24 Takuma Co Ltd Rubbish incinerating/melting method and device therefor
JP2023525198A (en) * 2020-03-03 2023-06-15 グレンツェバッハ ビーエスエイチ ゲーエムベーハー Integrated plant for waste incineration and rock wool production and method for operating this plant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007127355A (en) * 2005-11-04 2007-05-24 Takuma Co Ltd Rubbish incinerating/melting method and device therefor
JP2023525198A (en) * 2020-03-03 2023-06-15 グレンツェバッハ ビーエスエイチ ゲーエムベーハー Integrated plant for waste incineration and rock wool production and method for operating this plant
JP7585567B2 (en) 2020-03-03 2024-11-19 グレンツェバッハ ビーエスエイチ ゲーエムベーハー Integrated plant for waste incineration and rock wool production and method for operating said plant

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