JPH0829312B2 - Method for producing slag by melting waste - Google Patents
Method for producing slag by melting wasteInfo
- Publication number
- JPH0829312B2 JPH0829312B2 JP12509391A JP12509391A JPH0829312B2 JP H0829312 B2 JPH0829312 B2 JP H0829312B2 JP 12509391 A JP12509391 A JP 12509391A JP 12509391 A JP12509391 A JP 12509391A JP H0829312 B2 JPH0829312 B2 JP H0829312B2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- hot water
- waste
- temperature
- cooling
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】Detailed Description of the Invention
【0001】[0001]
【産業上の利用分野】本発明は、建設汚泥(シールド掘
削工法、杭打ち工法等による工事で排出される泥土)、
上下水道汚泥、都市ゴミ焼却灰、シュレッダーダスト焼
却灰、食品・紙パルプ工場からの汚泥、石炭灰等の廃棄
物を溶融処理して、高強度で表面に凹凸のあるスラグを
製造する方法に関するものである。本発明の方法により
製造されたスラグは、土工事材(サンドドレーン材、サ
ンドコンパクション材、埋戻材等)、舗装材(路盤材、
歩道材等)、コンクリート骨材、壁材、園芸材、ろ過
材、建材等に利用することができる。[Field of Industrial Application] The present invention relates to construction sludge (mud discharged from construction work by shield excavation method, pile driving method, etc.),
Method for producing high-strength and rugged slag by melting and processing waste such as water and sewage sludge, municipal waste incineration ash, shredder dust incineration ash, sludge from food / pulp and pulp mill, coal ash, etc. Is. The slag produced by the method of the present invention is used for earthwork materials (sand drain materials, sand compaction materials, backfill materials, etc.), pavement materials (roadbed materials,
It can be used for sidewalk materials, etc.), concrete aggregates, wall materials, gardening materials, filtration materials, building materials, etc.
【0002】[0002]
【従来の技術】近年、廃棄物処分地確保が困難となって
おり、廃棄物の安定化、減容化のみならず、再資源化が
求められている。従来、水冷によるスラグ製造方法とし
て廃棄物に必要に応じて、融点降下の目的でCaO源材
等を加えて、1300〜1600℃の温度で溶融し、溶
融炉雰囲気圧力の沸騰温度よりも0〜80℃低い範囲
で、成行きの温度(昼夜、スラグ量等で温度が変化)で
水中へ流下させてスラグを製造する方法が知られてい
る。また、液pH調整を実施しておらず、液pHは、通
常6.0〜9.0で、殆どの場合、pH7.0〜8.0
であった。したがって高強度で、表面に凹凸があり、品
質の安定したスラグの製造が困難であった。2. Description of the Related Art In recent years, it has become difficult to secure a waste disposal site, and not only stabilization and volume reduction of waste but also recycling is required. Conventionally, as a slag manufacturing method by water cooling, if necessary, a CaO source material or the like is added to the waste for the purpose of lowering the melting point, melted at a temperature of 1300 to 1600 ° C, and is 0 to more than the boiling temperature of the melting furnace atmosphere pressure. There is known a method of producing slag by flowing it down into water at a temperature of the end (temperature changes depending on the amount of slag, etc., day and night) in a range lower by 80 ° C. Further, the liquid pH is not adjusted, and the liquid pH is usually 6.0 to 9.0, and in most cases, the pH is 7.0 to 8.0.
Met. Therefore, it was difficult to manufacture a slag having high strength, unevenness on the surface, and stable quality.
【0003】また、特開昭63−20099号公報に
は、溶融炉から落下する溶融スラグを冷却手段及び加振
手段を備えた受容器に受け、間接的に冷却して粒状の固
化体とし、連続的に取り出す下水汚泥溶融スラグの処理
方法が記載されている。In Japanese Patent Laid-Open No. 63-20099, a molten slag falling from a melting furnace is received by a receiver equipped with a cooling means and a vibrating means, and indirectly cooled to form a granular solidified body. A treatment method for sewage sludge molten slag that is continuously taken out is described.
【0004】[0004]
【発明が解決しようとする課題】上記の特開昭63−2
0099号公報記載の方法においては、80〜350℃
の高い温度でスラグを冷却しており、本発明と温度範囲
の一部が共通するが、間接水冷又は間接空冷を行うもの
であるので、冷却部面積が小さく、廃棄物溶融による大
量の融液を、同一温度で安定的に冷却し、かつ、搬送す
るのは困難である。また、間接冷却であるから、液pH
の制御によりスラグを水熱処理することができない。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
In the method described in Japanese Patent Publication No.
The slag is cooled at a high temperature, and part of the temperature range is common with the present invention, but since it is used for indirect water cooling or indirect air cooling, the cooling part area is small, and a large amount of melt due to waste melting It is difficult to stably cool and convey the same at the same temperature. In addition, since it is indirect cooling, the liquid pH
Therefore, the slag cannot be hydrothermally treated.
【0005】また、上記の従来技術では、次の4つを満
足する水冷スラグが得られない。 (1) 天然砂並みの高強度スラグ、 (2) 表面に凹凸を有したスラグ、 (3) 土木建築資材等としての適正粒度分布を有した
スラグ、 (4) 品質の安定したスラグ、本発明者らは、上記の
(1)〜(4)を満足するスラグを得るために、種々研
究した結果、溶融炉雰囲気圧力の沸騰温度よりも2〜5
0℃低い範囲で±10℃に維持され、かつ、液pHが
8.0〜13.0の熱水中に流下させて冷却すること
で、(1)〜(4)を満足するスラグを得ることができ
ることを知見した。さらに、破砕後のスラグを融液冷却
用の熱水と同性状の熱水中で処理することにより、スラ
グ表面の凹凸を大きくすることができることを知見し
た。本発明は、上記の知見に基づいてなされたもので、
高強度で表面に凹凸を有する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するものであ
る。Further, in the above-mentioned conventional technique, a water-cooled slag satisfying the following four conditions cannot be obtained. (1) High-strength slag equivalent to natural sand, (2) Slag having irregularities on the surface, (3) Slag having an appropriate particle size distribution as a civil engineering building material, (4) Slag of stable quality, the present invention In order to obtain the slag satisfying the above (1) to (4), the inventors conducted various studies and found that the slag was 2 to 5% higher than the boiling temperature of the melting furnace atmosphere pressure.
A slag satisfying (1) to (4) is obtained by maintaining the temperature at ± 10 ° C in the low range of 0 ° C and allowing it to flow down into hot water having a liquid pH of 8.0 to 13.0 for cooling. I found that I can do it. Furthermore, it was found that the unevenness of the slag surface can be increased by treating the crushed slag in hot water having the same properties as the hot water for cooling the melt. The present invention was made based on the above findings,
It is an object of the present invention to provide a slag manufacturing method capable of obtaining a slag having high strength and unevenness on the surface.
【0006】[0006]
【課題を解決するための手段及び作用】上記の目的を達
成するために、請求項1の廃棄物溶融によるスラグの製
造方法は、図1に示すように、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、pH8.0〜13.0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
ことを特徴としている。10は溶融炉、12は水冷装
置、14は熱水容器、16は破砕機、18はポンプであ
る。図1において、溶融炉雰囲気圧力の沸騰温度よりも
2〜50℃、望ましくは5〜20℃低い範囲で±10
℃、望ましくは±5℃に維持された循環熱水中に融液を
流下させて冷却することにより、スラグが製造される。
そして、破砕機16により破砕することにより製品とな
る。循環熱水の温度は、例えば、熱水容器14内の熱水
温度を検出し冷水供給量を調節することにより制御され
る。In order to achieve the above object, a method for producing slag by melting waste according to a first aspect of the present invention is as follows: As shown in FIG. It is maintained at ± 10 ° C within the range of 2 to 50 ° C lower than the boiling temperature of the atmospheric pressure , and the pH is adjusted to 8.0 to 13.0.
In hot water that is integer, the melt flowing down and cooling to is characterized by obtaining a slag. 10 is a melting furnace, 12 is a water cooling device, 14 is a hot water container, 16 is a crusher, and 18 is a pump. In FIG. 1, within the range of 2 to 50 ° C., preferably 5 to 20 ° C. lower than the boiling temperature of the melting furnace atmosphere pressure, ± 10
The slag is produced by causing the melt to flow down into the circulating hot water maintained at ℃, preferably ± 5 ℃ and cooling.
And it becomes a product by crushing with the crusher 16. The temperature of the circulating hot water is controlled, for example, by detecting the hot water temperature in the hot water container 14 and adjusting the cold water supply amount.
【0007】熱水のpH調整は、循環系、例えば熱水容
器14にpH調整材を添加することによりなされ、pH
8.0〜13.0、望ましくはpH9.0〜12.0に
調整される。また、請求項2の方法は、請求項1の方法
において、廃棄物にCaO源材、Fe2O3源材、Si
O2源材からなる群より選ばれた添加材を加えて組成調
整した後、溶融するものである。さらに、請求項3の方
法は、請求項1又は2の方法において、図2に示すよう
に、スラグを破砕した後、破砕物を融液冷却用の熱水と
同じ性状の熱水中で0.5〜20時間処理するものであ
る。図2は、破砕機16で破砕したスラグを、水熱処理
容器20内の融液冷却用の熱水中、又は融液冷却用の熱
水と同性状の熱水中で処理することにより、品質の向上
したスラグを製造する方法を示している。22は固液分
離機、24はポンプである。The pH of the hot water is adjusted by adding a pH adjuster to the circulating system, for example, the hot water container 14,
The pH is adjusted to 8.0 to 13.0, preferably 9.0 to 12.0. The method according to claim 2 is the method according to claim 1 , wherein the waste is CaO source material, Fe 2 O 3 source material, and Si.
The composition is adjusted by adding an additive material selected from the group consisting of O 2 source materials, and then melted . Furthermore, in the method of claim 3, in the method of claim 1 or 2 , as shown in FIG. 2, after crushing the slag, the crushed material is heated in hot water having the same properties as hot water for cooling the melt. .5~20 hours to Monodea
It 2 shows that the slag crushed by the crusher 16 is treated in hot water for cooling the melt in the hydrothermal treatment container 20 or in hot water having the same properties as the hot water for cooling the melt, thereby improving the quality. 3 shows a method for producing the improved slag. 22 is a solid-liquid separator and 24 is a pump.
【0008】溶融炉雰囲気圧力は、通常は常圧の場合が
多いが、石炭ガス化炉等では雰囲気圧力は加圧状態とな
る。常圧状態の場合は、熱水温度は50〜98℃、望ま
しくは80〜95℃で±10℃、望ましくは±5℃に維
持されるが、加圧状態の場合は、熱水温度は水の沸騰温
度よりも2〜50℃、望ましくは5〜20℃低い範囲で
±10℃、望ましくは±5℃に維持される。石炭ガス化
炉のような高圧下では、水冷装置12からのスラグの取
出しは、水冷装置底部からの取出しとなる。[0008] The atmospheric pressure of the melting furnace is usually normal pressure in most cases, but the atmospheric pressure is increased in a coal gasification furnace or the like. In the normal pressure state, the hot water temperature is maintained at 50 to 98 ° C., preferably 80 to 95 ° C., ± 10 ° C., preferably ± 5 ° C., but in the pressurized state, the hot water temperature is water. It is maintained at ± 10 ° C, preferably ± 5 ° C in the range of 2 to 50 ° C, preferably 5 to 20 ° C lower than the boiling temperature of. Under high pressure such as in a coal gasifier, slag is taken out from the water cooling device 12 from the bottom of the water cooling device.
【0009】溶融炉10としては、電気、ガス、油、石
炭、コークス、可燃性ゴミ、廃材等を熱源とした電気
炉、表面溶融炉、旋回溶融炉、コークスベッド溶融炉等
が用いられる。水冷装置12としては、容器内に熱水を
充満させてポンプ18で循環しながら温度、及び/又は
液pHをコントロールするもの等が用いられる。破砕機
16としては、回転数を調整することで粒度調整が容易
なハンマーミル等の衝撃式破砕機が用いられる。水熱処
理容器20としては、外部ジャケットを熱水循環により
保温し、スラグを底部より抜き出す型式、又はコンベア
で上部より抜き出す型式のもの等が用いられる。As the melting furnace 10, an electric furnace using electricity, gas, oil, coal, coke, combustible dust, waste materials, etc. as a heat source, a surface melting furnace, a swirling melting furnace, a coke bed melting furnace and the like are used. As the water cooling device 12, a device for controlling the temperature and / or the liquid pH while the container is filled with hot water and circulated by the pump 18 is used. As the crusher 16, an impact crusher such as a hammer mill whose particle size can be easily adjusted by adjusting the rotation speed is used. As the hydrothermal treatment vessel 20, a type in which an outer jacket is kept warm by circulating hot water and slag is extracted from the bottom or a conveyor is extracted from the top is used.
【0010】熱水pH調整材としては、アルカリ性の廃
棄物、石灰、水酸化鉄、カセイソーダ等が用いられる。
また、酸性側に調整する場合は、硫酸、塩酸等が用いら
れる。組成調整用のCaO源材としては、石灰、貝殻、
高炉スラグ、コンクリート片、石灰系下水汚泥等が用い
られ、Fe2O3源材としては、鉄鉱石、鉄鋼汚泥、酸
化鉄等が用いられ、SiO2源材としては、ケイ砂、ケ
イ石、砕石、使用済み鋳物砂、残土等が用いられる。冷
却水(熱水)の温度が、溶融炉雰囲気圧力の沸騰温度よ
りも50℃を越えて低い場合、例えば常圧下において、
冷却水温が、50℃未満であると粒径が大きく、表面に
凹凸のある高強度スラグが得られず、98℃を越える
と、発生スチームが溶融炉に悪影響を及ぼす。さらに、
液pHが8.0〜13.0あれば、スラグが水熱処理さ
れ、表面にケイ酸カルシウム水和物等が生成するなどに
より、スラグの強度が大となり、表面の凹凸か大きくな
る。液pHが8.0未満であると水熱処理効果が不十分
となり、液pHが13.0を越えるとアルカリ残存量が
多くなるなどの問題がある。また、水熱処理時間が0.
5時間未満であると水熱処理効果が不十分であり、20
時間を越えると水熱処理容器が大きくなって経済性に問
題がある。さらに、破砕後に水熱処理すれば、すべての
表面が水熱処理されるのでスラグ品質がより向上する。
また、水温が±10℃よりも変動が大きくなれば、スラ
グ品質が変動する。すなわち、低い側になれば、粒径が
小さくなり、強度が低下し、高い側となれば、粒径が大
きくなり、かつ、強度が大きくなる。As the hot water pH adjusting material, alkaline waste, lime, iron hydroxide, caustic soda and the like are used.
When adjusting to the acidic side, sulfuric acid, hydrochloric acid or the like is used. As the CaO source material for composition adjustment, lime, seashell,
Blast furnace slag, concrete pieces, lime sludge or the like is used as the Fe 2 O 3 source material, iron ore, steel sludge, iron oxide or the like is used as the SiO 2 source material, silica sand, quartzite, Crushed stone, used foundry sand, residual soil, etc. are used. When the temperature of the cooling water (hot water) is lower than the boiling temperature of the melting furnace atmosphere pressure by more than 50 ° C., for example, under normal pressure,
If the cooling water temperature is less than 50 ° C., the particle size is large, and high strength slag having irregularities on the surface cannot be obtained. If it exceeds 98 ° C., the generated steam adversely affects the melting furnace. further,
When the pH of the liquid is 8.0 to 13.0, the slag is hydrothermally treated, and calcium silicate hydrate or the like is generated on the surface, so that the strength of the slag becomes large and the unevenness of the surface becomes large. If the liquid pH is less than 8.0, the hydrothermal treatment effect will be insufficient, and if the liquid pH exceeds 13.0, there will be a problem that the amount of residual alkali increases. Further, the hydrothermal treatment time is 0.
If it is less than 5 hours, the effect of hydrothermal treatment is insufficient, and 20
If the time is exceeded, the hydrothermal treatment container becomes large and there is a problem in economic efficiency. Furthermore, if hydrothermal treatment is carried out after crushing, all surfaces are hydrothermally treated, so that the quality of slag is further improved.
If the water temperature fluctuates more than ± 10 ° C, the slag quality fluctuates. That is, on the lower side, the particle size becomes smaller and the strength decreases, and on the higher side, the particle size becomes larger and the strength increases.
【0011】廃棄物にCaO源材を加えて、溶流点を1
350℃以下とし、1400℃〜1600℃で溶融する
とスラグ量の変化、昼と夜との外気温変化等による炉の
放熱量などの変化によって、融液の流動性変化が小さく
なり、融液状態で安定して熱水中に流下し、高品質で、
かつ、品質の安定したスラグが得られる。破砕機16の
回転数を調整すると、スラグの粒度が異なるので、各用
途による適正粒度とするために、回転数を変えて破砕す
るか、異なる回転数によるスラグを混合するなどの方法
が用いられる。なお、溶流点とは、JIS M 880
1(石炭類の試験方法)に準拠し、3角錐 (2.7×
2.7×3.0×8Hmm)を製作した後、電気炉に入
れ、5℃/分で昇温し、三角錐の高さが幅のほぼ1/6
になった時の温度を言う。A CaO source material was added to the waste to adjust the melting point to 1
When the temperature is 350 ° C. or less and melts at 1400 ° C. to 1600 ° C., the change in melt flowability becomes small due to changes in the amount of slag, heat radiation of the furnace due to changes in outside temperature between day and night, etc. Stable in the hot water, high quality,
Moreover, slag with stable quality can be obtained. When the rotation speed of the crusher 16 is adjusted, the particle size of the slag is different. Therefore, in order to obtain an appropriate particle size for each application, a method such as crushing by changing the rotation speed or mixing slags with different rotation speeds is used. . The melting point is JIS M 880.
3 pyramid (2.7 x
(2.7 × 3.0 × 8 H mm) was placed in an electric furnace and heated at 5 ° C./min so that the height of the triangular pyramid was about 1/6 of the width.
Say the temperature when it became.
【0012】[0012]
【実施例】以下、本発明の実施例について説明する。圧
壊強度は、木屋式硬度計を用い、3mmの球形粒子が破
壊する強度である。 実施例1 建設汚泥100部に鉄鉱石20部を加えて原料調整をし
た。この混合物の溶流点は1300℃で、旋回溶融炉を
用いて1450℃で溶融し、冷却用の熱水の水温、液p
H(Ca(OH)2で調整)を1時間サイクルで変化さ
せ、種々の水冷条件下で黒色のスラグを製造した。回転
数2500rpmで破砕したスラグ製造時の水温pHと
圧壊強度との関係は図3に示すとおり、水温が高いほど
大きくなり、かつ、pHが8.0よりも10.0の方が
大きくなっていた。なお、比較のため天然砕砂(硬質砂
岩)の圧壊強度を測定したところ、19kg/3mmφ
であり、水温が約600℃以上で天然砕砂以上の強度を
有するスラグとなった。また、製造時の水温と2500
rpmの回転数で破砕した後の5mm以上スラグの割合
の関係を図4に示す。図4に示すとおり、水温が高いほ
ど多くなり、かつ、液pHが8.0よりも10.0の方
が多くなっており、5mm以上の粒子が有効なテラゾタ
イルのような美観材骨材への適用が図れる。Embodiments of the present invention will be described below. The crush strength is the strength with which spherical particles of 3 mm are broken using a Kiya type hardness meter. Example 1 20 parts of iron ore was added to 100 parts of construction sludge to prepare raw materials. The melting point of this mixture is 1300 ° C., it is melted at 1450 ° C. using a swirling melting furnace, and the temperature of the hot water for cooling, liquid p
H (adjusted with Ca (OH) 2 ) was changed in 1 hour cycle to produce black slag under various water cooling conditions. As shown in FIG. 3, the relationship between the water temperature pH and the crush strength at the time of manufacturing slag crushed at a rotation speed of 2500 rpm becomes larger as the water temperature becomes higher, and the pH becomes 10.0 rather than 8.0. It was For comparison, the crush strength of crushed natural sand (hard sandstone) was measured to be 19 kg / 3 mmφ.
Thus, the slag having a water temperature of about 600 ° C. or higher and a strength higher than that of natural crushed sand was obtained. Also, the water temperature during production and 2500
FIG. 4 shows the relationship of the ratio of slag of 5 mm or more after crushing at the rotation speed of rpm. As shown in FIG. 4, the higher the water temperature, the more the liquid pH is 10.0 rather than 8.0, and the particles with a diameter of 5 mm or more are effective as terazotile-like aesthetic aggregates. Can be applied.
【0013】実施例2 乾燥した建設汚泥のみを原料とし、旋回溶融炉を用いて
1550℃で溶融し、種々の水冷条件下でスラグを製造
し、破砕機の回転数を3500rpmとして破砕した。
得られたスラグを用い、水セメント比50%、フロー値
190±5mmでボルトランドセメントによるモルタル
を作成し、5φ×10cmの型枠に流し込み20℃で1
日養生後に脱形し、さらに、6日養生して圧縮強度を測
定した。製造時の熱水のpH、温度とモルタルの7日養
生圧縮強度との関係を図5に示す。図5から、水温が高
いほどモルタル強度は高く、かつ、液pHが8.0〜1
3.0で最大となっていることがわかる。なお、pH調
整において、アルカリ性側はCa(OH)2を用いて行
い、酸性側はH2SO4を用いて行った。Example 2 Only dried construction sludge was used as a raw material and melted at 1550 ° C. in a swirling melting furnace to produce slag under various water cooling conditions, and the crusher was crushed at 3500 rpm.
Using the obtained slag, a mortar made of boltland cement with a water-cement ratio of 50% and a flow value of 190 ± 5 mm is prepared, poured into a 5φ × 10 cm mold and at 1 ° C. at 20 ° C.
It was demolded after daily curing and further cured for 6 days to measure the compressive strength. The relationship between the pH and temperature of hot water during production and the 7-day curing compressive strength of mortar is shown in FIG. From FIG. 5, the higher the water temperature, the higher the mortar strength, and the liquid pH is 8.0-1.
It can be seen that the maximum is 3.0. In the pH adjustment, Ca (OH) 2 was used on the alkaline side and H 2 SO 4 was used on the acidic side.
【0014】実施例3 建設汚泥100部に鉄鉱石20部を加えて原料調整し
た。この混合物を旋回溶融炉を用いて1450℃で溶融
し、温度90℃、pH10.0の熱水中に投下してスラ
グとした。このスラグを破砕機の回転数を3500rp
mとして破砕した。得られたスラグは黒色で、JIS
A 5004(コンクリート砕砂)を満足する粒度分布
を有していた。このスラグを冷却用熱水(温度90℃、
pH10.0)下で2時間処理した。圧壊強度は23k
g/3mmφであり、モルタルの7日強度(圧縮)は4
70kg/cm2であり、天然砕砂によるモルタルの7
日強度(圧縮)420kg/cm2よりも約10%高い
値を示し、破砕後に水熱処理することで、スラグ単体な
らびにモルタルはより高強度となった。Example 3 A raw material was prepared by adding 20 parts of iron ore to 100 parts of construction sludge. This mixture was melted at 1450 ° C. using a swirling melting furnace and dropped into hot water having a temperature of 90 ° C. and a pH of 10.0 to obtain slag. The rotation speed of this slag crusher is 3500 rp
It was crushed as m. The slag obtained is black and conforms to JIS
It had a particle size distribution satisfying A 5004 (crushed concrete sand). This slag is cooled with hot water (temperature 90 ° C,
It was treated under pH 10.0) for 2 hours. Crush strength is 23k
g / 3mmφ, mortar's 7-day strength (compression) is 4
70 kg / cm 2 of natural crushed sand mortar
It showed a value 10% higher than the daily strength (compression) of 420 kg / cm 2 , and the hydrothermal treatment after crushing made the slag simple substance and the mortar even stronger.
【0015】[0015]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) 高強度で表面に凹凸のあるスラグが得られ、天
然砕砂、砂代替として土木建築資材等として再資源化を
図ることができる。 (2) 得られたスラグを破砕する場合は、破砕機の回
転数を小さくすることにより、粒径5mm以上の高強度
スラグが多く得られ、かつ、色が黒色であるので、テラ
ゾタイルのような付加価値の高い美観材の骨材へ適用す
ることができる。Since the present invention is configured as described above, it has the following effects. (1) A slag with high strength and uneven surface can be obtained, which can be recycled as a natural crushed sand, a civil engineering building material, etc. as a substitute for sand. (2) When crushing the obtained slag, by reducing the rotation speed of the crusher, a large amount of high-strength slag with a particle size of 5 mm or more is obtained, and the color is black, so that it is similar to terrazotile. It can be applied to aesthetic aggregates with high added value.
【図1】本発明の廃棄物溶融によるスラグの製造方法の
一実施例を示す工程図である。FIG. 1 is a process drawing showing an embodiment of a method for producing slag by melting waste according to the present invention.
【図2】本発明の方法の他の実施例を示す工程図であ
る。FIG. 2 is a process drawing showing another embodiment of the method of the present invention.
【図3】熱水の水温とスラグ圧壊強度との関係を示すグ
ラフである。FIG. 3 is a graph showing the relationship between hot water temperature and slag crush strength.
【図4】熱水の水温とスラグ破砕後の粒径5mm以上ス
ラグ割合との関係を示すグラフである。FIG. 4 is a graph showing a relationship between a water temperature of hot water and a slag ratio of a particle size of 5 mm or more after crushing slag.
【図5】熱水のpHと7日養生後のスラグ圧縮強度との
関係を示すグラフである。FIG. 5 is a graph showing the relationship between the pH of hot water and the slag compressive strength after curing for 7 days.
【符号の説明】 10 溶融炉 12 水冷装置 14 熱水容器 16 破砕機 18 ポンプ 20 水熱処理容器 22 固液分離機 24 ポンプ[Explanation of Codes] 10 Melting Furnace 12 Water Cooling Device 14 Hot Water Container 16 Crusher 18 Pump 20 Hydrothermal Treatment Container 22 Solid-Liquid Separator 24 Pump
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C04B 5/00 C 5/06 // C04B 18/10 Z 18/16 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C04B 5/00 C 5/06 // C04B 18/10 Z 18/16
Claims (3)
の沸騰温度よりも2〜50℃低い範囲で±10℃に維持
され、かつ、pH8.0〜13.0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
る廃棄物溶融によるスラグの製造方法。1. Hot water after melting the waste, maintained at ± 10 ° C. within a range of 2 to 50 ° C. lower than the boiling temperature of the melting furnace atmosphere pressure , and adjusted to pH 8.0 to 13.0. A method for producing slag by melting waste, characterized in that slag is obtained by flowing down and cooling a melt inside.
SiO2源材からなる群より選ばれた添加材を加えて組
成調整した後、溶融する請求項1記載の廃棄物溶融によ
るスラグの製造方法。2. A waste material comprising CaO source material, Fe 2 O 3 source material,
After the composition prepared by adding an additive material selected from the group consisting of SiO 2 source material, manufacturing method of the slag by waste melting 請 Motomeko 1, wherein you melt.
用の熱水と同じ性状の熱水中で0.5〜20時間処理す
る請求項1又は2記載の廃棄物溶融によるスラグの製造
方法。3. After crushing the slag, the crushed material is treated in hot water having the same properties as the hot water for cooling the melt for 0.5 to 20 hours.
That請 Motomeko 1 or 2 method for producing a slag by waste melt according.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12509391A JPH0829312B2 (en) | 1991-04-26 | 1991-04-26 | Method for producing slag by melting waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12509391A JPH0829312B2 (en) | 1991-04-26 | 1991-04-26 | Method for producing slag by melting waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04326975A JPH04326975A (en) | 1992-11-16 |
| JPH0829312B2 true JPH0829312B2 (en) | 1996-03-27 |
Family
ID=14901676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12509391A Expired - Fee Related JPH0829312B2 (en) | 1991-04-26 | 1991-04-26 | Method for producing slag by melting waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0829312B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010017293A (en) * | 1999-08-10 | 2001-03-05 | 이구택 | A Method for Preparing Water-Granulated Slag Having Low Density |
| JP4514363B2 (en) * | 2001-05-25 | 2010-07-28 | メタウォーター株式会社 | Molten solidified product of incinerated ash, method and apparatus for melting and solidifying, and method of using molten solidified product |
| JP5367280B2 (en) * | 2008-03-04 | 2013-12-11 | 一般財団法人電力中央研究所 | Foam material manufacturing system and manufacturing method |
| JP6431744B2 (en) * | 2014-10-22 | 2018-11-28 | 株式会社大林組 | Method for producing herbicidal material |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63205189A (en) * | 1987-02-19 | 1988-08-24 | Daido Steel Co Ltd | Method for solidifying molten slag |
-
1991
- 1991-04-26 JP JP12509391A patent/JPH0829312B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04326975A (en) | 1992-11-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4700348B2 (en) | Two-component wet cement, method for producing and using the same | |
| US8535435B2 (en) | Method of fabrication of construction materials from industrial solid waste | |
| EP0542330B1 (en) | Porous granulated steel slag composition and use of such a steel slag composition as aggregate or cement replacement in building materials, road building materials and embankment materials | |
| AU2012278447B2 (en) | Method for manufacturing light-weight construction material using waste product and light-weight construction material manufactured thereby | |
| AU2020306874B2 (en) | Method for producing a carbonate bonded, compacted article | |
| JP3188200B2 (en) | Manufacturing method of artificial lightweight aggregate | |
| EP0188371A2 (en) | Artificial lightweight aggregate | |
| US5676750A (en) | Process of treatment and environment-friendly utilization of asbestos-cement products | |
| JPH0829312B2 (en) | Method for producing slag by melting waste | |
| JP3288649B2 (en) | Solidification and stabilization of waste and fly ash | |
| JP3840371B2 (en) | Steelmaking slag and sand-washed sludge treatment method | |
| KR100489207B1 (en) | Method for preparing ascon | |
| Chakravarty et al. | Strategies for solid waste management in SAIL steel plants | |
| JP2007261880A (en) | Manufacturing method of sintered product | |
| EP4577505A1 (en) | A carbonated composite | |
| TWI740176B (en) | Manufacturing method of cement modifier and functional cement material containing the cement modifier | |
| JP2007260503A (en) | Method for producing fired product | |
| JP4447494B2 (en) | Manufacturing method of sintered product | |
| JPH06134438A (en) | Treatment method of waste asbestos material and manufacturing method of ceramic products using waste asbestos material | |
| EP2093033A2 (en) | Method for treating catalyzed hydraulic mixtures containing industrial slags and aggregates for making non polluting articles and the articles made thereby | |
| JP4160467B2 (en) | Artificial aggregate manufacturing method and artificial aggregate manufactured by the method | |
| CN1830874A (en) | Method for producing steam-pressing silicate products by waste concrete | |
| JP3657703B2 (en) | Method for producing hydrated cured product | |
| CN107673685A (en) | The method that environment-friendly baking-free bricks are made using stainless steel waste residue | |
| JP4579063B2 (en) | Method for producing conglomerate-like artificial rock |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |