JP3537280B2 - Waste molten slag treatment method - Google Patents

Waste molten slag treatment method

Info

Publication number
JP3537280B2
JP3537280B2 JP480497A JP480497A JP3537280B2 JP 3537280 B2 JP3537280 B2 JP 3537280B2 JP 480497 A JP480497 A JP 480497A JP 480497 A JP480497 A JP 480497A JP 3537280 B2 JP3537280 B2 JP 3537280B2
Authority
JP
Japan
Prior art keywords
slag
waste
elution
air
heavy metals
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.)
Expired - Fee Related
Application number
JP480497A
Other languages
Japanese (ja)
Other versions
JPH10192814A (en
Inventor
信義 西原
秀実 小佐野
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP480497A priority Critical patent/JP3537280B2/en
Publication of JPH10192814A publication Critical patent/JPH10192814A/en
Application granted granted Critical
Publication of JP3537280B2 publication Critical patent/JP3537280B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

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、都市ごみ、産業廃
棄物、汚泥などの廃棄物を直接溶融してスラグを製造す
る方法、及び廃棄物を一旦焼却して灰とした後に溶融し
てスラグを製造する方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for producing slag by directly melting waste such as municipal waste, industrial waste, and sludge, and a method for once incinerating waste to form ash and then melting the slag. And a method for producing the same.

【0002】[0002]

【従来の技術】現状は、大半の廃棄物は焼却方式で処理
されているが、焼却方式では焼却灰の処分場を必要とす
る等の欠点がある。特に大都市圏では焼却灰の処分場の
確保が困難であり、廃棄物を直接溶融する方法または、
廃棄物の焼却灰を溶融して減容化、さらには再資源化が
可能な方式で処理する必要性が高まっている。しかも、
廃棄物を溶融したスラグを再資源化するためには、天然
の砂や砕石並の物理性状(強度、粒度分布)を有してい
ること、及び化学性状を有していることが必要である。
特に化学性状としては、スラグ中の重金属が溶出しない
ことが安全性の観点から必要である。
2. Description of the Related Art At present, most waste is treated by an incineration method. However, the incineration method has a drawback that a disposal site for incinerated ash is required. In particular, in the metropolitan area, it is difficult to secure a disposal site for incinerated ash.
There is an increasing need to dissolve incinerated ash from waste in a manner that allows volume reduction and further recycling. Moreover,
In order to recycle slag from molten waste, it is necessary to have physical properties (strength, particle size distribution) comparable to natural sand and crushed stone, and to have chemical properties .
In particular, as for chemical properties, it is necessary from the viewpoint of safety that heavy metals in the slag are not eluted.

【0003】そこで、スラグの性状を改善する方法とし
ては、特公平8−29312号公報に、廃棄物を溶融し
た後、溶融炉雰囲気圧力の沸騰温度よりも2〜50℃低
い範囲で±10℃に維持され、かつ、pH8.0〜1
3.0に調整された熱水中に融液を流下・冷却してスラ
グを得ることを特徴とするスラグの製造方法が開示され
ている。
[0003] To improve the properties of slag, Japanese Patent Publication No. 8-29312 discloses a method of melting refuse and then adding ± 10 ° C in a range of 2 to 50 ° C lower than the boiling temperature of the atmosphere pressure in the melting furnace after melting the waste. , And pH 8.0-1
A slag production method is disclosed in which a slag is obtained by flowing and cooling a melt in hot water adjusted to 3.0.

【0004】[0004]

【発明が解決しようとする課題】上記の特公平8−29
312号公報の方法は、天然砂並の高強度で、表面に凹
凸を有し、土木建築資材等として適正粒度分布を有した
品質の安定したスラグを得ることができるスラグの製造
方法を提供することを目的としている。すなわち、天然
の砂に近い物理性状を有するスラグを得ることを目的と
しており、重金属の溶出特性等の化学性状に関しては記
載されていない。埋め立てや海洋投棄が主な処分方法で
ある焼却灰等より、再資源化を目的とするスラグは重金
属の溶出特性等の化学性状に関して厳しい管理が必要で
ある。本発明は、重金属が溶出しない天然砂並の化学的
に安定したスラグを得ることのできるスラグの製造方法
を提供することを目的とする。
Problems to be Solved by the Invention
The method disclosed in Japanese Patent No. 312 provides a method for producing slag capable of obtaining stable slag of high quality, which is as strong as natural sand, has irregularities on the surface, and has an appropriate particle size distribution as a material for civil engineering and construction. It is intended to be. That is, the purpose is to obtain a slag having a physical property close to that of natural sand, and there is no description about chemical properties such as elution characteristics of heavy metals. Slags intended for recycling require strict control over chemical properties such as the elution characteristics of heavy metals rather than incineration ash, which is the main disposal method for landfills and ocean dumping. An object of the present invention is to provide a method for producing slag that can obtain chemically stable slag equivalent to natural sand from which heavy metals do not elute.

【0005】[0005]

【課題を解決するための手段】現状の溶融方式におい
て、定常操業時に製造したスラグからの重金属の溶出は
みられず、安定した製品が得られるが、立ち上げ時等の
炉体温度の低い非定常操業時に、平成6年度環境庁告示
25号の基準内であるが微量検出されることがある。課
題を解決するための本発明の特徴手段は、廃棄物を溶融
した後、冷却して固化したスラグを、溶出防止ピット中
で、30日以上の定期的な攪拌、または強制送風を行っ
てスラグ中の重金属を溶性の酸化鉛および炭酸鉛と
し、かつスラグ中の珪酸SiO2 の三次元的網目構造に
組み込ませることにより、スラグからの重金属の溶出を
防止することにある。
In the current melting method, no heavy metal is eluted from the slag produced during normal operation, and a stable product can be obtained. During normal operation, trace amounts may be detected within the standards of the Environmental Agency Notification No. 25 of 1994. The characteristic means of the present invention for solving the problem is that, after melting the waste, the slag cooled and solidified is periodically stirred or blasted for 30 days or more in the elution prevention pit to perform slag blasting. It is an object of the present invention to prevent heavy metals from being eluted from slag by making the heavy metals therein hardly soluble lead oxide and lead carbonate and incorporating them into a three-dimensional network structure of silicate SiO 2 in slag.

【0006】通常、溶融処理後のスラグは貯留ホッパに
3日〜1週間程度の短期間貯留した後、まとめて出荷ま
たは廃棄する。本発明は、貯留ホッパの替わりに溶出防
止ピットを設けスラグを空気中に一定期間以上晒して、
スラグ中の重金属を難溶性の物質に変えることにより重
金属の溶出を防止する。例えば、鉛化合物が空気中で酸
化及び炭酸化され、難溶性の酸化鉛PbO及び炭酸鉛P
bCO3 となり、さらにスラグ中の珪酸SiO2 の三次
元的網目構造に組み込まれることにより溶出は防止され
る。従って、本発明の方法で製造したスラグは、土木資
材等に使用した場合、重金属が溶出することなく安全に
使用することができる。
Normally, the slag after the melting treatment is stored in a storage hopper for a short period of about 3 days to 1 week, and then shipped or discarded collectively. The present invention provides an elution prevention pit instead of a storage hopper and exposes the slag to the air for a certain period of time,
The heavy metal in the slag is converted into a hardly soluble substance to prevent the elution of the heavy metal. For example, lead compounds are oxidized and carbonated in the air, and lead oxide PbO and lead carbonate P are hardly soluble.
It becomes bCO 3 and is further incorporated into the three-dimensional network structure of silicate SiO 2 in the slag, thereby preventing elution. Therefore, when the slag produced by the method of the present invention is used for civil engineering materials and the like, heavy metals can be safely used without elution of heavy metals.

【0007】[0007]

【実施例】【Example】

(実施例1)廃棄物を溶融処理する実施例として、コー
クスを用いて廃棄物を直接溶融処理する場合を図1に示
す。図1において、溶融炉1の炉上部から、廃棄物及
び、副原料としてコークスおよび石灰石が溶融炉1に装
入される。廃棄物としては都市ごみを処理した。溶融炉
1の下部周辺に設けられた羽口2から空気および酸素が
供給される。廃棄物の処理量は560kg/h、コーク
スおよび石灰石は廃棄物の約6%、空気は520Nm3
/h、酸素は30Nm3 /hである。溶融炉に装入され
た廃棄物およびコークス等は炉内で充填層を形成し、炉
下部の羽口2から吹き込まれた空気および酸素により、
コークスおよび廃棄物の一部が燃焼する。該燃焼ガスは
溶融炉内を炉底部から上昇し、燃焼ガスの顕熱により廃
棄物を予熱、乾燥、熱分解する。廃棄物の乾燥、熱分解
の過程で発生した水蒸気、熱分解ガスおよび微細なダス
トはガス排出管4から排出される。
(Example 1) As an example in which waste is melted, FIG. 1 shows a case in which waste is directly melted using coke. In FIG. 1, waste and coke and limestone as auxiliary materials are charged into the melting furnace 1 from the furnace upper part of the melting furnace 1. Municipal waste was disposed of as waste. Air and oxygen are supplied from a tuyere 2 provided around the lower part of the melting furnace 1. Waste treatment amount is 560 kg / h, coke and limestone are about 6% of waste, and air is 520 Nm 3
/ H and oxygen are 30 Nm 3 / h. The waste, coke, and the like charged into the melting furnace form a packed bed in the furnace, and the air and oxygen blown from the tuyere 2 at the lower part of the furnace form
Some of the coke and waste will burn. The combustion gas rises in the melting furnace from the bottom of the furnace, and the waste is preheated, dried and thermally decomposed by the sensible heat of the combustion gas. Steam, pyrolysis gas and fine dust generated in the process of drying and pyrolysis of waste are discharged from the gas discharge pipe 4.

【0008】一方、廃棄物の灰分および非燃焼物とコー
クス、石灰は高温に加熱され炉底部へと下りていき、羽
口から吹き込まれた空気および酸素でコークスが燃焼
し、灰分および非燃焼物は1300℃から1450℃に
加熱され溶融状態となって、スラグ排出孔3から炉外へ
排出される。石灰石はスラグの塩基度、すなわちスラグ
中の石灰分CaOと珪酸分SiO2 の比率を0.5以上
とし、溶融状態のスラグの流動性の調整のために添加す
る。スラグ排出口から排出された溶融状態のスラグは水
砕設備5に投入され、砂状の細かい粒子となる。また、
溶融状態のスラグ中には溶融メタルが含まれているが、
メタルもスラグと同様に細かい粒子状となる。
On the other hand, ash and non-combustible waste, coke and lime of waste are heated to a high temperature and descend to the furnace bottom, where coke burns with air and oxygen blown from tuyeres, and ash and non-combustible Is heated from 1300 ° C. to 1450 ° C. to be in a molten state and discharged from the slag discharge hole 3 to the outside of the furnace. Limestone slag basicity, namely the lime CaO and the ratio of the silicic acid content of SiO 2 in the slag is 0.5 or more, is added in order to adjust the fluidity of the slag in the molten state. The molten slag discharged from the slag discharge port is charged into the granulation equipment 5 and becomes fine sand-like particles. Also,
Slag in the molten state contains molten metal,
Metal also becomes fine particles like slag.

【0009】粒子状のスラグとメタルは掻き上げ装置6
によって排出され、湿式磁選機7へ供給されてスラグと
メタルに分離され、スラグは磁選時の付着水のある状態
で溶出防止ピット8に供給される。溶出防止ピット8に
おいてスラグを2〜3mの高さまで積み上げた状態で空
気に晒した。本実施例の場合、実施時期は冬期で雰囲気
温度5〜15℃で行い、溶出防止ピットでの処理期間は
3ケ月とし、処理期間中は均一に酸化、炭酸化できるよ
う0.5ケ月毎にスラグを攪拌した。処理後のスラグは
インターロッキングブロック等のコンクリート2次製品
の骨材や土木資材などとして利用する。
The slag and metal in the form of particles are scraped by a scraping device 6
, And is supplied to the wet magnetic separator 7 to be separated into slag and metal. The slag is supplied to the elution preventing pit 8 in a state where water adheres during magnetic separation. In the elution prevention pit 8, the slag was exposed to air while being piled up to a height of 2 to 3 m. In the case of this embodiment, the operation is performed at an ambient temperature of 5 to 15 ° C. in winter, and the treatment period in the elution prevention pit is 3 months. During the treatment period, every 0.5 months so as to uniformly oxidize and carbonate. The slag was stirred. The slag after the treatment is used as an aggregate or a civil engineering material of a secondary concrete product such as an interlocking block.

【0010】図2に実施例を示す。本実施例におけるス
ラグ1の性状は通常操業時で、処理前の鉛の溶出濃度は
0.005mg/リットル以下、すなわち定量下限以下
で、鉛の溶出はみられなかった。図2に示すスラグ2
は、溶融炉の立ち上げ時のスラグであり、処理前のスラ
グの鉛の溶出濃度が0.008mg/リットルである。
溶出防止ピットで3ケ月間空気に晒した後の鉛の溶出濃
度は0.005mg/リットル以下、すなわち定量下限
以下となり、鉛の溶出はみられなかった。
FIG. 2 shows an embodiment. The properties of the slag 1 in this example were during normal operation, and the lead elution concentration before the treatment was 0.005 mg / liter or less, that is, the lower limit of quantification was less than that, and no lead was eluted. Slag 2 shown in FIG.
Is slag at the time of starting the melting furnace, and the slag before treatment has a lead elution concentration of 0.008 mg / liter.
The lead elution concentration after exposure to air for 3 months at the elution prevention pit was 0.005 mg / liter or less, that is, the determination limit or less, and no lead elution was observed.

【0011】スラグを空気に晒すにあたり、スラグ中の
重金属を難溶性の酸化物及び炭酸塩に変え、スラグ中の
珪酸SiO2 の三次元的網目構造に一定期間以上必要で
ある。図2に示すスラグ3は、夏期の雰囲気温度(25
〜35℃)が高く反応の促進されやすい状態で同様の処
理を行ったスラグであり、30日で溶出が防止できたこ
とから、最低30日以上空気に晒す必要がある。
When exposing the slag to air, it is necessary to convert heavy metals in the slag into sparingly soluble oxides and carbonates to form a three-dimensional network structure of silicate SiO 2 in the slag for a certain period or more. The slag 3 shown in FIG.
This is a slag that has been subjected to the same treatment in a state where the reaction is easily accelerated and the elution was prevented in 30 days. Therefore, the slag must be exposed to air for at least 30 days.

【0012】なお、溶出防止ピット8においてスラグの
積み上げ高さを1m以下にした状態で攪拌を行わずに空
気に晒した結果同様の効果が得られた。よって、溶出防
止ピット8は、設置面積に制限がありスラグの積み高さ
が1mを越える場合は攪拌操作を加えながら空気に晒す
ことで均一に酸化、炭酸化し、設置面積を広くとること
ができスラグの積み高さが1m以下に抑えられる場合は
攪拌操作なしに空気にスラグを晒すことで、重金属の溶
出を防止できる。
The same effect was obtained as a result of exposing the slag in the elution prevention pit 8 to air without stirring while keeping the slag pile height at 1 m or less. Therefore, the dissolution prevention pit 8 has a limited installation area, and when the pile height of the slag exceeds 1 m, it can be uniformly oxidized and carbonated by exposing it to air while adding a stirring operation, so that the installation area can be widened. When the pile height of the slag can be suppressed to 1 m or less, the elution of heavy metals can be prevented by exposing the slag to air without a stirring operation.

【0013】(実施例2)スラグを空気に晒す方法とし
て、実施例1の溶出防止ピット8に送風配管を追加設置
した場合の実施例を示す。本実施例におけるスラグは、
実施例1と同じロットのスラグを用いた。送風配管付き
溶出防止ピット8′にスラグを2〜3mの高さまで積み
上げた状態にし、攪拌は行わず0.5Nm3 /hで送風
することで強制的に空気に晒した。本実施例の場合、実
施時期は冬期で雰囲気温度5〜15℃で行い、溶出防止
ピットでの処理期間は3ケ月とし実施例1と条件をあわ
せた。
(Embodiment 2) As an example of a method of exposing slag to air, an embodiment in which a ventilation pipe is additionally installed in the elution prevention pit 8 of Embodiment 1 will be described. The slag in this embodiment is:
The same lot of slag as in Example 1 was used. The slag was piled up to a height of 2 to 3 m in the elution prevention pit 8 ′ with a ventilation pipe, and was forced to be exposed to air by blowing at 0.5 Nm 3 / h without stirring. In the case of the present embodiment, the operation was performed in winter at an ambient temperature of 5 to 15 ° C., and the treatment period in the elution prevention pit was set to three months, and the conditions were the same as those in Example 1.

【0014】図2に示すスラグ4は、送風配管付き溶出
防止ピットで空気に晒したスラグである。実施例1と同
様に処理前の溶出濃度が0.008mg/リットルのス
ラグは、送風配管付き溶出防止ピットで3ケ月間空気に
晒した後の鉛の溶出濃度が0.005mg/リットル以
下、すなわち定量下限以下となり、鉛の溶出はみられな
くなった。実施例1と同様、スラグを1m以上積み上げ
ることができ、溶出防止ピット8′の設置面積は小さく
できる。
The slag 4 shown in FIG. 2 is slag that has been exposed to air in an elution prevention pit with a ventilation pipe. In the same manner as in Example 1, the slag having an elution concentration of 0.008 mg / liter before treatment has a lead elution concentration of 0.005 mg / liter or less after being exposed to air for 3 months in an elution prevention pit with a ventilation pipe, that is, It was below the lower limit of quantification, and no elution of lead was observed. As in the first embodiment, the slag can be stacked by 1 m or more, and the installation area of the elution prevention pit 8 'can be reduced.

【0015】なお、溶出試験方法及び分析方法は平成6
年環境庁告示第25号にしたがって行った。また、鉛以
外の重金属としては、砒素、水銀、カドミウム、六価ク
ロム、セレンに関しても分析したが、処理前及び後とも
に定量下限以下であり、溶出はみられなかった。さら
に、処理の前後でスラグの物理性状を比較したが差異は
なく、コンクリート2次製品の骨材、土木資材として有
効利用した場合、支障はなかった。
The dissolution test method and analysis method are described in 1994
In accordance with the Notification of the Environment Agency No.25. In addition, arsenic, mercury, cadmium, hexavalent chromium, and selenium were also analyzed as heavy metals other than lead, but before and after the treatment, the quantification was below the lower limit of quantification, and no elution was observed. Furthermore, the physical properties of the slag were compared before and after the treatment, but there was no difference, and there was no problem when the slag was effectively used as an aggregate or a civil engineering material for secondary concrete products.

【0016】[0016]

【発明の効果】本発明によって、以下の効果を実現する
ことができる。 (1)廃棄物を溶融したスラグを空気中に一定期間以上
晒すことによって、スラグからの重金属などの溶出を防
止することが可能である。重金属の溶出を防止すること
によって、スラグの再資源化を図ることができる。 (2)また、実施例に示すごとく、処理期間中に攪拌、
空気吹き付け等の操作を加えれば、スラグはより均一に
酸化、炭酸化され、空気に晒す設備の設置面積を小さく
することができる。 (3)空気中に長期間晒したスラグは、物理性状が悪化
することはなく、コンクリート2次製品の骨材、土木資
材として有効利用する場合、支障はない。 (4)廃棄物のスラグを再資源化することにより、スラ
グの処分場が不要となるだけでなく、天然砂の採掘によ
る自然破壊を防止することができる。
According to the present invention, the following effects can be realized. (1) It is possible to prevent the elution of heavy metals and the like from the slag by exposing the slag obtained by melting the waste to air for a certain period or more. By preventing the elution of heavy metals, slag can be recycled. (2) Also, as shown in the examples, stirring during the treatment period,
If an operation such as air blowing is added, the slag is more uniformly oxidized and carbonated, and the installation area of the equipment exposed to the air can be reduced. (3) The physical properties of slag exposed to air for a long period of time do not deteriorate, and there is no hindrance when slag is effectively used as aggregate or civil engineering material for secondary concrete products. (4) Recycling waste slag not only eliminates the need for a slag disposal site, but also prevents natural destruction due to mining of natural sand.

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

【図1】本発明の実施例を示すブロック図である。FIG. 1 is a block diagram showing an embodiment of the present invention.

【図2】本発明の実施例を示す図である。FIG. 2 is a diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 溶融炉 2 羽口 3 スラグ排出孔 4 ガス排出管 5 水砕設備 6 掻き上げ装置 7 磁選機 8 溶出防止ピット 8′送風機付き溶出防止ピット 1 melting furnace 2 tuyere 3 Slag discharge hole 4 Gas exhaust pipe 5 Granulation equipment 6 Raising device 7 Magnetic separator 8 Elution prevention pit Elution prevention pit with 8 'blower

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 B09B 5/00 C04B 5/02 C04B 18/04 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) B09B 3/00 B09B 5/00 C04B 5/02 C04B 18/04

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 廃棄物を溶融した後、冷却して固化した
スラグを、溶出防止ピット中で、30日以上の定期的な
攪拌、または強制送風を行ってスラグ中の重金属を
性の酸化鉛および炭酸鉛とし、かつスラグ中の珪酸Si
2 の三次元的網目構造に組み込ませることにより、ス
ラグからの重金属の溶出を防止することを特徴とする廃
棄物溶融スラグの処理方法。
1. After melting the waste, the solidified slag that has cooled and solidified is subjected to regular stirring or forced air blowing for 30 days or more in a dissolution prevention pit to hardly dissolve heavy metals in the slag. /> Silicated silicate in slag as lead oxide and lead carbonate
A method for treating waste molten slag, wherein the metal is incorporated into a three-dimensional network structure of O 2 to prevent the elution of heavy metals from the slag.
JP480497A 1997-01-14 1997-01-14 Waste molten slag treatment method Expired - Fee Related JP3537280B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP480497A JP3537280B2 (en) 1997-01-14 1997-01-14 Waste molten slag treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP480497A JP3537280B2 (en) 1997-01-14 1997-01-14 Waste molten slag treatment method

Publications (2)

Publication Number Publication Date
JPH10192814A JPH10192814A (en) 1998-07-28
JP3537280B2 true JP3537280B2 (en) 2004-06-14

Family

ID=11593960

Family Applications (1)

Application Number Title Priority Date Filing Date
JP480497A Expired - Fee Related JP3537280B2 (en) 1997-01-14 1997-01-14 Waste molten slag treatment method

Country Status (1)

Country Link
JP (1) JP3537280B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100433344B1 (en) * 2000-12-06 2004-05-27 주식회사 포스코 Apparatus of separating pure slag granulation in blast furnace

Also Published As

Publication number Publication date
JPH10192814A (en) 1998-07-28

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