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JPS6124074B2 - - Google Patents
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JPS6124074B2 - - Google Patents

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Publication number
JPS6124074B2
JPS6124074B2 JP57039702A JP3970282A JPS6124074B2 JP S6124074 B2 JPS6124074 B2 JP S6124074B2 JP 57039702 A JP57039702 A JP 57039702A JP 3970282 A JP3970282 A JP 3970282A JP S6124074 B2 JPS6124074 B2 JP S6124074B2
Authority
JP
Japan
Prior art keywords
temperature
incineration ash
waste incineration
melting
mold
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
Application number
JP57039702A
Other languages
Japanese (ja)
Other versions
JPS58156388A (en
Inventor
Kazuo Okada
Akitoshi Yamada
Takao Myazaki
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP57039702A priority Critical patent/JPS58156388A/en
Publication of JPS58156388A publication Critical patent/JPS58156388A/en
Publication of JPS6124074B2 publication Critical patent/JPS6124074B2/ja
Granted legal-status Critical Current

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  • Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は下水汚泥焼却灰や都市ごみ焼却灰等の
廃棄物焼却灰を原料とする結晶化物の製造法に関
するものである。 従来、各地の下水処理場やごみ処理場から発生
する下水汚泥やごみは、そのまま埋立投棄すると
衛生上あるいは悪臭公害上問題があるので大部分
は焼却処理され、焼却灰として埋立投棄されてい
るが、埋立用地の確保が難しくなつてきているう
えに焼却灰からの重金属等の溶出その他埋立処分
にともなう二次公害が大きな社会問題となつてお
り、さらに省資源、省エネルギーの観点からも廃
棄物焼却灰を溶融して有効利用することが検討さ
れている。廃棄物焼却灰を溶融成形して骨材等に
有効利用しようとする試みとしては、特公昭55−
24010号公報に示されるように溶融物を水封ボツ
クス中に落下させて水中で固化させて小塊状の固
化物を得る方法があるが、この方法によつて得ら
れる成形物は強度が弱いうえに形状がまちまちで
あるという間題点を有しており、また特公昭56−
11877号公報に示されるように、水冷した鋳型中
に溶融物を投入固化させることにより大塊状の固
化物を得る方法は、骨材とするために破砕装置が
必要であるうえに破砕面から重金属類が溶出する
等の問題点を有するものであつた。 本発明は前記のような問題点を解決して機械的
強度および化学的安定性に優れ、しかも、用途に
合致した製品形状に最初から成形された高強度の
結晶化物を容易に量産できる廃棄物焼却灰を原料
とする結晶化物の製造法を目的として完成された
もので、SiO225〜45%(重量%、以下同じ)、
Al2O35〜15%、Fe2O35〜25%、CaO20〜40%、
MgO1〜5%、P2O51〜10%を主な組成とし、か
つ、(CaO+MgO)/SiO2比が0.8〜1.2の廃棄物
焼却灰を1350〜1500℃で溶融した溶融物を表面温
度が300〜600℃に保持された型中に投入して成形
し、次に該成形物を1020〜1180℃の温度に30分以
上保持して結晶化することを特徴とするものであ
る。 本発明において原料として使用する廃棄物焼却
灰は、下水汚泥焼却灰あるいは都市ごみ焼却灰等
であつて、これらの廃棄物焼却灰中には、
SiO2、Al2O3、Fe2O3、CaO、MgO、P2O5が主と
して含まれる外にK2O、Na2O等が含まれてお
り、それらの含有量は焼却灰の種類等により若干
異なる。このような廃棄物焼却灰の溶融特性すな
わち溶融温度に対する粘度の関係をみると、一般
のガラスの成形加工に適した粘度域に対応する成
形温度域は一般のガラスに比較して極端に狭く、
いわゆる「足の短かいガラス」の性質を有してお
り、また、例えば1350℃以上の溶融温度域におけ
る粘度は一般のガラスに比較してかなり低いこと
から溶融したのち流し込み成形するのに適してい
るが、このような組成の廃棄物焼却灰を溶融成形
後さらに結晶化するには、SiO225〜45%(重量
%、以下同じ)好ましくは30〜40%、Al2O35〜
15%好ましくは5〜10%、Fe2O35〜25%好まし
くは5〜15%、CaO20〜40%好ましくは30〜35
%、MgO1〜5%好ましくは2〜5%、P2O51〜
10%好ましくは2〜10%、その他よりなり、か
つ、(CaO+MgO)/SiO2比が0.8〜1.2好ましく
は0.9〜1.1の範囲内であることが重要であり、こ
のために焼却機より得られた前記廃棄物焼却灰は
これを分析し、組成範囲が前記特定組成範囲内に
ないときは、前記の組成範囲に入るように調整す
る。なお、組成調整に際しては、安価な粘土、シ
ラス、ベンガラ、石炭、ドロマイト、骨灰等を用
いることが好ましい。このようにして、組成調整
された廃棄物焼却灰は溶融炉中において1350〜
1500℃程度で溶融した後に該溶融物を用途に応じ
たキヤビテイ部の表面温度すなわち型の表面温度
が300〜600℃好ましくは400〜500℃に保持された
型中に投入して成形し、引き続いてその成形物を
溶融炉排ガス等によつて1020〜1180℃好ましくは
1050〜1150℃の温度範囲内の所定温度に保持され
た結晶化炉中に30分以上好ましくは40〜90分保持
するか、前記温度範囲内をゆつくりとした昇降温
速度で昇降温させてその温度範囲内に30分以上好
ましくは40〜90分保持してこの成形物中に結晶核
の形成およびその結晶核を中心として結晶成長を
起こさせ、成形物全体を結晶化すればよい。な
お、本発明においてSiO2を25〜45%とするの
は、SiO2が25%未満ではガラス形成骨格として
のSiO2が不足して高強度の結晶化物が得られな
いからであり、45%を越えると溶融温度が上昇し
て前記溶融温度では粘度が高くなつて流し込み成
形に適しないうえ結晶化にも悪影響を及ぼすから
であり、また、Al2O3を5〜15%とするのは、
Al2O3が5%未満では高強度の結晶化物が得られ
ず、15%を越えると溶融温度が高くなりすぎるか
らであり、さらに、Fe2O3を5〜25%とするのは
Fe2O3は融剤としてばかりでなく核形成剤として
も重要な成分であり、その量が5%未満では融剤
としての効果がうすくて溶融温度が低下しないう
えに結晶核の形成も不充分であり、25%を越える
と強度を著しく低下させるからである。また、
CaOを20〜40%とするのはCaOが20%未満では溶
融物の粘度が増加するとともに結晶化に悪影響が
あるうえ強度が低下し、40%を越えると化学的安
定性を著しく低下させるからであり、さらに、
MgOを1〜5%とするのは、MgOはCaOに代わ
る組成調整剤として用いられて化学的安定性を増
す効果があるにも拘らずその含有量が1%未満で
はその効果がなく、5%を越える量を入れても効
果は変らないからであり、また、P2O5を1〜10
%とするのはP2O5は核形成剤として最も重要な
成分であつて、その量が1%未満では1020〜1180
℃の温度範囲では結晶核が形成されず、10%を越
えると成形段階での失透現象が表われるからであ
る。さらにまた、(CaO+MgO)/SiO2比を0.8
〜1.2とすることは溶融温度の低下のために重要
であるうえに溶融物の結晶化のためにも重要であ
つて、この混合比が0.8未満あるいは1.2を越える
と、溶融温度が上昇して溶融炉の炉材の侵蝕や溶
融コストの増加が起るので好ましくない。次に、
廃棄物焼却灰の溶融温度を1350〜1500℃と限定し
たのは、前記組成範囲に調整された廃棄物焼却灰
の溶融物は溶融温度が高くなると急激に粘性が低
下するいわゆる「足の短かいガラス」の性質を有
することから、1350℃未満では連続的に移動する
型中に連続的に溶融物を投入するのに必要な粘度
101ポイズ以下好ましくは101/2ポイズ以下の粘
度が得られないため成形物が互いに連結し個々の
独立した成形体になりにくいうえに成形物の離型
が悪くなり、また、実プラントにおいて1500℃を
越える溶融温度を維持することは設備上からもエ
ネルギーコスト面からもロスが大きいので、上限
を1500℃とし、さらに、成形後引き続いて結晶化
を行う場合において、1020〜1180℃の温度で熱処
理するには溶融温度を1350〜1500℃の温度範囲に
保持することが熱エネルギーの有効利用の点より
最もよい。次に、溶融物を投入する型の表面温度
を300〜600℃に保持するのは、鋳鉄や黒鉛等の型
の材質や形状によつて異なるが、300℃未満では
成形物が急冷されてクラツクが入るおそれがあ
り、600℃を越えると成形物の型への焼付きが起
きて難型しにくくなるおそれがあるためである。
また、結晶化温度を1020〜1180℃と限定したの
は、前記組成に調整された廃棄物焼却灰は1020℃
未満では結晶成長が起りにくく、1180℃を越える
と結晶化物の再融解等により安定した結晶成長が
妨げられるからである。なお、結晶化に際して
は、それぞれ特定温度範囲内の一定温度に所定時
間保持するのが均一な結晶核の形成および結晶成
長をさせるうえでより好ましいが、前述のとおり
それぞれの特定温度範囲内で所定時間かけてゆつ
くりと降温あるいは昇温してもほぼ同等の結果が
得られる。また、結晶化時間を30分以上としたの
は、30分未満の保持時間では結晶化を完全に行な
うことができないので、高強度の結晶化物が得ら
れないためである。なお、溶融物を投入する型は
黒鉛やボロンナイトライド等の漏れ性が悪くて滑
性の良い材質で製作するか、鋳鉄等で製作した金
型の表面に黒鉛やボロンナイトライド等の離型剤
をコーテイングすることが望ましく、また、型の
キヤビテイ部形状は製造される結晶化物の用途に
応じそのまま使用できるように製品形状と対応し
たものであればよく、特に、セメントモルタルと
混練してセメント製品を製作する場合の骨材とし
て使用する場合には表面に凹凸や凹凸条をつける
ことが好ましいためキヤビテイ部の型面に凹凸を
形成しておくことが好ましい。 このようにして得られる結晶化物は高強度であ
るばかりでなく、表面が平滑な光沢面であつて取
扱が容易であり、しかも、骨材、板、柱等最終的
に利用される製品形状のものとして最初から成形
されるから、破砕、切断、加工といつた後処理の
ための手間が不要なうえに加工面から重金属類が
溶出するおそれもない。 本発明は前記説明から明らかなように、特定組
成範囲の廃棄物焼却灰を特定の溶融条件で溶融し
たのち型に投入して成形し、さらに、特定の結晶
化条件下で処理することによつて機械的強度およ
び化学的安定性に優れた結晶化物を容易に得るこ
とができるものであつて、このような優れた特性
を持つ結晶化物はセメントと混練して使用される
重量骨材、道路の埋め戻し、舗装等に使用される
砕石、歩道や床面等に敷設されるタイル、建物の
壁面、柱等に使用される外壁材等の建材その他用
途は極めて広く、また、結晶化は溶融炉排ガスを
有効利用することもできるから、安価に得られる
うえに省エネルギー的にも優れ、さらに、従来埋
立処分されてきた廃棄物焼却灰の埋立処分地や二
次公害の心配をなくすることもできる等種々の利
点がある。 実施例 各所の下水処理場の廃棄物焼却灰を下記表に記
載する化学組成および組成比率に組成調整し、そ
れぞれの溶融特性に従つて1380〜1480℃の温度に
維持された溶融炉内において5時間で溶融し、そ
の溶融物を400℃に保持された無端コンベア上に
連続して設置された黒鉛製の型中に投入して成形
し、次いで、溶融炉排ガスを用いて1050〜1150℃
の温度に維持された結晶炉内で40分保持して結晶
化させた結晶化物No.1〜No.12を表中に本発明例
として記載した。次に、本発明の数値限定範囲外
の組成および熱処理条件で得られた結晶化物
No.13〜No.20を表中に参考例として記載し、
また、廃棄物焼却灰を原料とする結晶化物の強
度、化学的安定性等を鉱滓スラグ、ガラスと対比
するため、これらを表中参考例として鉱滓スラ
グをNo.21にガラスをNo.22、No.23として記載し
た。これらの各種の結晶化物等について圧縮強
度、曲げ強度、硬度、硫酸ナトリウム安定性試験
について比較測定した10個の試料の平均値は表の
とおりであつた。この結果から明らかなように、
本発明によつて得られた結晶化物は参考例によつ
て得られた結晶化物等に比べて機械的強度および
化学的安定性に優れていることが確認された。
The present invention relates to a method for producing a crystallized product using waste incineration ash such as sewage sludge incineration ash and municipal waste incineration ash as a raw material. Traditionally, most of the sewage sludge and garbage generated from sewage treatment plants and garbage treatment plants in various places have been incinerated and disposed of as incinerated ash in landfills, as dumping them in landfills poses hygiene and odor pollution problems. , it is becoming difficult to secure land for landfills, and the secondary pollution associated with landfill disposal, such as the elution of heavy metals from incinerated ash, has become a major social problem.In addition, waste incineration is becoming more and more important from the viewpoint of resource and energy conservation. Consideration is being given to melting the ash and making effective use of it. An attempt was made to melt and mold waste incineration ash to effectively use it as aggregate, etc.
As shown in Publication No. 24010, there is a method of dropping a molten material into a water-sealed box and solidifying it in water to obtain a solidified material in the form of small lumps, but the molded product obtained by this method is weak in strength and It has the problem that its shape varies, and it also has the problem that the
As shown in Publication No. 11877, the method of obtaining a large lump of solidified material by pouring the molten material into a water-cooled mold and solidifying it requires a crushing device to make aggregate, and also removes heavy metals from the crushed surface. This method had problems such as the elution of certain substances. The present invention solves the above-mentioned problems by creating a waste material that has excellent mechanical strength and chemical stability, and which can be easily mass-produced into high-strength crystallized products that are formed from the beginning into a product shape that matches the intended use. It was completed for the purpose of producing a crystallized product using incineration ash as a raw material, and contains 25 to 45% SiO 2 (weight%, same hereinafter),
Al2O3 5-15 %, Fe2O3 5-25 %, CaO20-40%,
The surface temperature of the molten material obtained by melting waste incineration ash at 1350 to 1500°C with a main composition of 1 to 5% MgO and 1 to 10% P 2 O 5 and a (CaO + MgO) / SiO 2 ratio of 0.8 to 1.2 It is characterized in that it is poured into a mold held at 300 to 600°C and molded, and then the molded product is held at a temperature of 1020 to 1180°C for 30 minutes or more to crystallize. The waste incineration ash used as a raw material in the present invention is sewage sludge incineration ash or municipal waste incineration ash, etc., and these waste incineration ash contain:
In addition to mainly containing SiO 2 , Al 2 O 3 , Fe 2 O 3 , CaO, MgO, and P 2 O 5 , it also contains K 2 O, Na 2 O, etc., and their content varies depending on the type of incineration ash. It varies slightly depending on the situation. Looking at the melting characteristics of waste incineration ash, that is, the relationship between viscosity and melting temperature, the forming temperature range corresponding to the viscosity range suitable for forming ordinary glass is extremely narrow compared to ordinary glass.
It has the properties of so-called "short-legged glass," and its viscosity in the melting temperature range of 1,350°C or higher is considerably lower than that of ordinary glass, making it suitable for pouring after melting. However, in order to further crystallize waste incineration ash having such a composition after melting and forming, SiO 2 25 to 45% (weight %, the same hereinafter) is preferably 30 to 40%, Al 2 O 3 5 to 5%.
15% preferably 5-10%, Fe2O3 5-25 % preferably 5-15%, CaO20-40% preferably 30-35
%, MgO 1-5% preferably 2-5%, P 2 O 5 1-5%
It is important that the (CaO+MgO)/ SiO2 ratio is in the range of 0.8 to 1.2, preferably 0.9 to 1.1, and for this reason, the The waste incineration ash is analyzed, and if the composition range is not within the specific composition range, it is adjusted to fall within the composition range. In addition, when adjusting the composition, it is preferable to use inexpensive clay, whitebait, red iron, coal, dolomite, bone ash, etc. In this way, the composition-adjusted waste incineration ash is heated to 1350~
After melting at about 1500℃, the molten material is poured into a mold whose cavity part surface temperature, that is, the surface temperature of the mold, is maintained at 300 to 600℃, preferably 400 to 500℃, depending on the application, and then molded. The molded product is heated to 1020-1180℃ preferably by melting furnace exhaust gas etc.
Either by keeping it in a crystallization furnace maintained at a predetermined temperature within the temperature range of 1050 to 1150°C for 30 minutes or more, preferably 40 to 90 minutes, or by raising and lowering the temperature within the temperature range at a slow rate. The entire molded product may be crystallized by maintaining the molded product within the temperature range for 30 minutes or more, preferably 40 to 90 minutes, to cause formation of crystal nuclei in the molded product and crystal growth centered on the crystal nuclei. In the present invention, SiO 2 is set to 25 to 45% because if SiO 2 is less than 25%, SiO 2 as a glass-forming skeleton is insufficient and a high-strength crystallized product cannot be obtained. If the Al 2 O 3 content is 5 to 15%, the melting temperature will rise and the viscosity will become high at the above melting temperature, making it unsuitable for casting and having a negative effect on crystallization. ,
If Al 2 O 3 is less than 5%, a high-strength crystallized product cannot be obtained, and if it exceeds 15%, the melting temperature becomes too high. Furthermore, setting Fe 2 O 3 to 5 to 25% is
Fe 2 O 3 is an important component not only as a fluxing agent but also as a nucleating agent; if its amount is less than 5%, its effect as a fluxing agent is weak, the melting temperature does not decrease, and crystal nuclei are not formed. This is because if it exceeds 25%, the strength will be significantly reduced. Also,
The reason why CaO is set at 20 to 40% is because if CaO is less than 20%, the viscosity of the melt will increase, it will have a negative effect on crystallization, and the strength will decrease, and if it exceeds 40%, it will significantly reduce the chemical stability. And furthermore,
The reason why MgO is set at 1 to 5% is that although MgO is used as a composition adjusting agent in place of CaO and has the effect of increasing chemical stability, it has no effect if the content is less than 1%. This is because the effect does not change even if the amount exceeds 1 % to 10 % .
% is because P 2 O 5 is the most important component as a nucleating agent, and if its amount is less than 1%, it will be 1020 to 1180.
This is because crystal nuclei are not formed in the temperature range of 0.degree. C., and if the temperature exceeds 10%, devitrification occurs during the molding stage. Furthermore, the (CaO + MgO)/SiO 2 ratio is 0.8
~1.2 is important not only for lowering the melting temperature but also for crystallizing the melt; if this mixing ratio is less than 0.8 or exceeds 1.2, the melting temperature will increase. This is undesirable because it corrodes the furnace material of the melting furnace and increases melting costs. next,
The reason why we limited the melting temperature of waste incineration ash to 1,350 to 1,500℃ is because the molten waste incineration ash adjusted to the above composition range has a so-called "short-legged structure" in which the viscosity decreases rapidly as the melting temperature increases. Because it has the properties of "glass", the viscosity required to continuously introduce the melt into a continuously moving mold at temperatures below 1350℃
Since it is not possible to obtain a viscosity of 10 1 poise or less, preferably 10 1/2 poise or less, the molded products are connected to each other and are difficult to form into individual, independent molded products, and the molding becomes difficult to release from the mold. Maintaining a melting temperature over 1500°C involves a large loss in terms of both equipment and energy costs, so the upper limit is set at 1500°C, and furthermore, when crystallizing is performed subsequently after molding, a temperature of 1020 to 1180°C is required. For heat treatment, it is best to maintain the melting temperature within the range of 1350 to 1500°C in terms of effective use of thermal energy. Next, the surface temperature of the mold into which the molten material is poured must be maintained at 300 to 600°C, depending on the material and shape of the mold, such as cast iron or graphite, but if it is below 300°C, the molded product will cool rapidly and crack This is because if the temperature exceeds 600°C, the molded product may seize to the mold and become difficult to mold.
In addition, the crystallization temperature was limited to 1020 to 1180°C because the waste incineration ash adjusted to the above composition was heated to 1020°C.
If the temperature is less than 1180°C, crystal growth is difficult to occur, and if it exceeds 1180°C, stable crystal growth will be hindered due to remelting of crystallized substances. In addition, during crystallization, it is more preferable to maintain a constant temperature within each specific temperature range for a predetermined period of time in order to form uniform crystal nuclei and crystal growth. Almost the same results can be obtained even if the temperature is gradually lowered or increased over time. Further, the reason why the crystallization time is set to 30 minutes or more is because crystallization cannot be completed completely with a holding time of less than 30 minutes, and a high-strength crystallized product cannot be obtained. The mold into which the molten material is introduced should be made of a material with good leakage and good slipperiness, such as graphite or boron nitride, or the surface of the mold should be made of cast iron, etc., with a release material such as graphite or boron nitride. In addition, the shape of the cavity of the mold may be compatible with the shape of the product so that it can be used as it is depending on the purpose of the crystallized product being manufactured. When used as an aggregate for manufacturing products, it is preferable to form irregularities or irregularities on the surface, so it is preferable to form irregularities on the mold surface of the cavity part. The crystallized product obtained in this way not only has high strength but also has a smooth and glossy surface, making it easy to handle. Since it is formed from the beginning, there is no need for post-processing such as crushing, cutting, and processing, and there is no risk of heavy metals leaching from the processed surface. As is clear from the above description, the present invention is achieved by melting waste incineration ash having a specific composition range under specific melting conditions, putting it into a mold and shaping it, and further treating it under specific crystallization conditions. Crystallized products with excellent mechanical strength and chemical stability can be easily obtained by using these materials. Crushed stone used for backfilling and paving, tiles laid on sidewalks and floors, building materials such as exterior wall materials used for building walls and columns, and other uses are extremely wide. Furnace exhaust gas can be used effectively, so it can be obtained at low cost and has excellent energy savings.Furthermore, it eliminates the need for landfills and secondary pollution of waste incineration ash, which has traditionally been disposed of in landfills. There are various advantages such as: Example Waste incineration ash from sewage treatment plants in various places was adjusted to the chemical composition and composition ratio listed in the table below, and melted in a melting furnace maintained at a temperature of 1380 to 1480°C according to the respective melting characteristics. The molten material is poured into graphite molds continuously installed on an endless conveyor kept at 400°C and molded, and then heated to a temperature of 1050 to 1150°C using melting furnace exhaust gas.
Crystallized products No. 1 to No. 12, which were crystallized by being held for 40 minutes in a crystallization furnace maintained at a temperature of , are listed as examples of the present invention in the table. Next, crystallized products obtained with compositions and heat treatment conditions outside the numerically limited range of the present invention
No.13 to No.20 are listed as reference examples in the table,
In addition, in order to compare the strength, chemical stability, etc. of crystallized products made from waste incineration ash with those of slag and glass, these are used as reference examples in the table: slag is No. 21, glass is No. 22, It was listed as No.23. The average values of 10 samples comparatively measured for compressive strength, bending strength, hardness, and sodium sulfate stability test for these various crystallized products were as shown in the table. As is clear from this result,
It was confirmed that the crystallized product obtained by the present invention has superior mechanical strength and chemical stability compared to the crystallized product obtained by the reference example.

【表】 なお、表中において、微少硬度はビツカース硬
度(ロード1Kg)を、硫酸ナトリウム安定性試験
はJIS A−1122骨材の安定性試験方法による5回
繰返しの減量率(%)を示す。
[Table] In the table, the microhardness indicates the Bitkers hardness (load 1 kg), and the sodium sulfate stability test indicates the weight loss rate (%) of 5 repetitions according to the JIS A-1122 aggregate stability test method.

Claims (1)

【特許請求の範囲】[Claims] 1 SiO225〜45%(重量%、以下同じ)、Al2O35
〜15%、Fe2O35〜25%、CaO20〜40%、MgO1〜
5%、P2O51〜10%を主な組成とし、かつ、
(CaO+MgO)/SiO2比が0.8〜1.2の廃棄物焼却
灰を1350〜1500℃で溶融した溶融物を表面温度が
300〜600℃に保持された型中に投入して成形し、
次に該成形物を1020〜1180℃の温度に30分以上保
持して結晶化することを特徴とする廃棄物焼却灰
を原料とする結晶化物の製造法。
1 SiO 2 25-45% (weight%, same below), Al 2 O 3 5
~15%, Fe2O3 5~25%, CaO20~ 40 %, MgO1~
5%, P 2 O 5 1-10% as the main composition, and
(CaO + MgO) / SiO 2 ratio is 0.8 to 1.2 waste incineration ash is melted at 1350 to 1500℃.
It is poured into a mold kept at 300-600℃ and molded.
1. A method for producing a crystallized product using waste incineration ash as a raw material, characterized in that the molded product is then held at a temperature of 1020 to 1180° C. for 30 minutes or more to crystallize it.
JP57039702A 1982-03-12 1982-03-12 Method for making crystallized matter from incineration ash of waste matter as raw material Granted JPS58156388A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57039702A JPS58156388A (en) 1982-03-12 1982-03-12 Method for making crystallized matter from incineration ash of waste matter as raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57039702A JPS58156388A (en) 1982-03-12 1982-03-12 Method for making crystallized matter from incineration ash of waste matter as raw material

Publications (2)

Publication Number Publication Date
JPS58156388A JPS58156388A (en) 1983-09-17
JPS6124074B2 true JPS6124074B2 (en) 1986-06-09

Family

ID=12560338

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Application Number Title Priority Date Filing Date
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Country Link
JP (1) JPS58156388A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04354575A (en) * 1991-06-03 1992-12-08 Daido Steel Co Ltd Method for adjusting viscosity of molten slag
DK0556409T3 (en) * 1991-09-06 1996-11-25 Kobe Steel Ltd Melt slag slag container, and method and apparatus for making hard aggregates from waste using the vessel
FR2712214B1 (en) * 1993-11-10 1996-01-19 Emc Services Waste crystallization process.
JPH09253767A (en) * 1996-03-27 1997-09-30 Oomi:Kk Simple mold for press and manufacturing method thereof
JP3271528B2 (en) * 1996-10-04 2002-04-02 日本鋼管株式会社 Slag aggregate production equipment

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Publication number Publication date
JPS58156388A (en) 1983-09-17

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