JP2527519B2 - Molten slag crystallization furnace - Google Patents
Molten slag crystallization furnaceInfo
- Publication number
- JP2527519B2 JP2527519B2 JP4326798A JP32679892A JP2527519B2 JP 2527519 B2 JP2527519 B2 JP 2527519B2 JP 4326798 A JP4326798 A JP 4326798A JP 32679892 A JP32679892 A JP 32679892A JP 2527519 B2 JP2527519 B2 JP 2527519B2
- Authority
- JP
- Japan
- Prior art keywords
- zone
- crystallization
- molten slag
- furnace
- temperature
- 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
- 239000002893 slag Substances 0.000 title claims description 39
- 238000002425 crystallisation Methods 0.000 title claims description 37
- 230000008025 crystallization Effects 0.000 title claims description 37
- 238000001816 cooling Methods 0.000 claims description 20
- 230000000630 rising effect Effects 0.000 claims description 10
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000010801 sewage sludge Substances 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B5/00—Treatment of metallurgical slag ; Artificial stone from molten metallurgical slag
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Tunnel Furnaces (AREA)
- Processing Of Solid Wastes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、下水汚泥等の溶融スラ
グから結晶化物を製造するために用いられる溶融スラグ
結晶化炉に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a molten slag crystallization furnace used for producing a crystallized product from molten slag such as sewage sludge.
【0002】[0002]
【従来の技術】下水汚泥等の溶融スラグを結晶化させる
ことにより強度に優れた骨材等を製造することは従来か
ら知られている。ところが、従来の溶融スラグ結晶化炉
は結晶化容器をローラチェーンによって一定速度で駆動
する方式や、結晶化容器を搭載した台車をチェーンによ
って一定速度で引っ張る方式のものであったため、結晶
化容器の移動速度は最初から最後まで一律であった。2. Description of the Related Art It has been conventionally known to produce aggregate having excellent strength by crystallizing molten slag such as sewage sludge. However, the conventional molten slag crystallization furnace has a method of driving the crystallization container at a constant speed with a roller chain, or a method of pulling a trolley equipped with the crystallization container with a chain at a constant speed. The speed of movement was uniform from start to finish.
【0003】一方、結晶化をうまく行わせるためには結
晶化温度(ヒートカーブ)を溶融スラグの組成変動等に
対応させてコントロールすることが必要であり、また実
用的には1300〜1500℃の高温のスラグによってチェーン
等が劣化しないように配慮する必要がある。しかし上記
した従来の溶融スラグ結晶化炉では、結晶化容器の移動
速度が一定であるためにヒートカーブの調整は専らバー
ナーによる加熱や冷却風の供給によって行われるのみで
あり、適正なヒートカーブの調整は困難であった。更に
従来の溶融スラグ結晶化炉では、結晶化容器を駆動する
チェーン等が熱劣化することを避けられなかった。On the other hand, in order to successfully perform crystallization, it is necessary to control the crystallization temperature (heat curve) in correspondence with the composition variation of the molten slag, and practically, it is 1300 to 1500 ° C. It is necessary to consider that the chain etc. will not deteriorate due to high temperature slag. However, in the above-mentioned conventional molten slag crystallization furnace, since the moving speed of the crystallization container is constant, the adjustment of the heat curve is performed only by heating with a burner or supply of cooling air, and an appropriate heat curve is obtained. Adjustment was difficult. Further, in the conventional molten slag crystallization furnace, it is unavoidable that the chain or the like that drives the crystallization container is thermally deteriorated.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、溶融スラグの組成変動等に対応させ
てヒートカーブを幅広く調整することができ、また高温
のスラグによる機械設備の劣化の少ない耐熱性に優れた
溶融スラグ結晶化炉を提供するために完成されたもので
ある。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art and enables the heat curve to be adjusted widely in accordance with the composition variation of molten slag, and the mechanical equipment of high temperature slag can be used. It was completed in order to provide a molten slag crystallization furnace with little deterioration and excellent heat resistance.
【0005】[0005]
【課題を解決するための手段】上記の課題を解決するた
めになされた本発明は、結晶化容器を所定温度まで昇温
する昇温帯と、溶融スラグを受け入れ結晶化させる恒温
帯と、その後の溶融スラグを冷却する冷却帯とに内部が
区分された炉体と、前記炉体の昇温帯、恒温帯、冷却帯
中の結晶化容器を各帯毎にそれぞれ特立させて異なる速
度で搬送可能な搬送機とを備えたことを特徴とするもの
である。The present invention, which has been made to solve the above-mentioned problems, provides a temperature rising zone for raising the temperature of a crystallization vessel to a predetermined temperature, a constant temperature zone for receiving and crystallizing molten slag, and a subsequent temperature zone. The furnace body whose inside is divided into the cooling zone for cooling the molten slag, the temperature rising zone of the furnace body, the constant temperature zone, and the crystallization container in the cooling zone can be specialized for each zone and transported at different speeds. It is characterized in that it is provided with a different carrier.
【0006】[0006]
【作用】本発明の溶融スラグ結晶化炉によれば、スラグ
溶融炉から溶融スラグを受ける結晶化容器を、各帯毎に
設けられた搬送機によって炉体の各帯で異なる速度で移
動させることができるので、単にバーナーによる加熱や
冷却風の供給に頼らざるを得なかった従来の装置に比較
して、ヒートカーブの調整可能な範囲を拡大することが
できる。このため、溶融スラグの組成変動等に対応して
適切なヒートカーブを設定することができる。According to the molten slag crystallization furnace of the present invention, the crystallization container that receives the molten slag from the slag melting furnace is moved at different speeds in each zone of the furnace body by the carrier provided in each zone. Therefore, it is possible to expand the adjustable range of the heat curve as compared with the conventional device that has to rely solely on heating by a burner or supply of cooling air. Therefore, it is possible to set an appropriate heat curve corresponding to the composition variation of the molten slag.
【0007】[0007]
【実施例】以下に本発明を図示の実施例によって更に詳
細に説明する。図1において、1は下水汚泥等を溶融し
てスラグ化するスラグ溶融炉、2はその下方に形成され
たトンネル状の炉体である。この炉体2はスラグ溶融炉
1の前後に延びるように設置されている。炉体2の内部
はいくつかの遮蔽板3によって複数ゾーンに区画されて
おり、実施例では入口側から順に昇温帯4、調節帯5、
恒温帯6、調節帯7、冷却帯8となっている。ここで調
節帯5、7は前後いずれの帯にも変化させることができ
るゾーンであるが、必須のものではない。The present invention will be described below in more detail with reference to the illustrated embodiments. In FIG. 1, 1 is a slag melting furnace that melts sewage sludge and the like to form slag, and 2 is a tunnel-shaped furnace body formed below the slag melting furnace. The furnace body 2 is installed so as to extend in front of and behind the slag melting furnace 1. The inside of the furnace body 2 is divided into a plurality of zones by some shield plates 3. In the embodiment, the temperature rising zone 4, the adjusting zone 5,
There are a constant temperature zone 6, a control zone 7, and a cooling zone 8. Here, the adjustment bands 5 and 7 are zones that can be changed to any of the front and rear bands, but they are not essential.
【0008】炉体2の内部のこれらの各ゾーンには、独
立して駆動される搬送機9が敷設されている。実施例で
は搬送機9はローラユニットであり、昇温帯4、調節帯
5、恒温帯6、調節帯7、冷却帯8の各帯ごとに独立し
て異なる速度で駆動することができるようになってい
る。そしてローラとしては各種セラミック製品の高温焼
成に用いられている耐熱性に優れたセラミックローラが
取り付けられ、炉外からローラを駆動する機構を採用し
ている。In each of these zones inside the furnace body 2, an independently driven carrier 9 is laid. In the embodiment, the conveyor 9 is a roller unit, and each of the temperature rising zone 4, the adjusting zone 5, the constant temperature zone 6, the adjusting zone 7 and the cooling zone 8 can be independently driven at different speeds. ing. As the roller, a ceramic roller having excellent heat resistance used for high temperature firing of various ceramic products is attached, and a mechanism for driving the roller from outside the furnace is adopted.
【0009】10はこれら搬送機9によって炉体2内を移
動する結晶化容器であり、セッター11の上に載せられて
入口側から供給され、出口側から取り出される。なお、
炉体の入口と出口にはそれぞれ可動遮蔽板12、13が設け
られており、結晶化容器10の出し入れの際だけに開閉さ
れる。Reference numeral 10 denotes a crystallization container which is moved in the furnace body 2 by these conveyors 9, is placed on the setter 11, is supplied from the inlet side, and is taken out from the outlet side. In addition,
Movable shield plates 12 and 13 are provided at the entrance and exit of the furnace body, and are opened and closed only when the crystallization container 10 is taken in and out.
【0010】また図1の下段に示したように、恒温帯6
及びその前後の調節帯5、7のゾーンにはローラの上下
に燃焼バーナ14が設けられて炉内温度を制御しており、
また冷却帯8にはローラの上下に冷却ノズル15が設けら
れて炉内を冷却している。更に炉帯2の上部には昇温帯
排気ファン16と冷却帯排気ファン17とが設けられてお
り、恒温帯6で発生した高温のガスを入口側に移動させ
ながら結晶化容器10を加熱し、昇温帯排気ファン16によ
り外部へ排出できるようになっている。Further, as shown in the lower part of FIG.
In addition, combustion burners 14 are provided above and below the rollers in the zones of the adjustment zones 5 and 7 before and after the zone to control the temperature inside the furnace.
Further, cooling nozzles 15 are provided above and below the rollers in the cooling zone 8 to cool the inside of the furnace. Further, a heating zone exhaust fan 16 and a cooling zone exhaust fan 17 are provided above the furnace zone 2 to heat the crystallization vessel 10 while moving the high temperature gas generated in the constant temperature zone 6 to the inlet side, It can be discharged to the outside by the temperature rising zone exhaust fan 16.
【0011】このように構成された本発明の溶融スラグ
結晶化炉は、炉体2の入口側から結晶化容器10を炉内に
入れ、搬送機9によって昇温帯4を移動させる間に結晶
化容器10の予熱を行う。そして結晶化容器10が恒温帯6
に達したときにスラグ溶融炉1から溶融したスラグを結
晶化容器10の内部に注入する。その後、結晶化容器10は
搬送機9によって恒温帯6内を移動し、更に冷却帯8を
通過する間にスラグを結晶化させる。In the molten slag crystallization furnace of the present invention thus constructed, the crystallization vessel 10 is put into the furnace from the inlet side of the furnace body 2, and the carrier 9 moves the temperature rising zone 4 for crystallization. Preheat container 10. And the crystallization container 10 has a constant temperature zone 6
When the temperature reaches, the molten slag is poured into the crystallization container 10 from the slag melting furnace 1. After that, the crystallization container 10 is moved in the constant temperature zone 6 by the carrier 9 and crystallizes the slag while passing through the cooling zone 8.
【0012】前記したように、結晶化の工程ではスラグ
の組成変動等に対応させてヒートカーブを適切に設定す
る必要があるが、本発明の溶融スラグ結晶化炉では結晶
化容器10を各帯ごとに独立して異なる速度で駆動するこ
とができる。このため、図2に示すように恒温帯6内に
おける結晶化容器10の移動速度を変化させることによっ
て、スラグの温度保持時間を変えることができる。ま
た、図3に示すように冷却帯8の搬送機9の速度を変え
ることによって、スラグの冷却速度を変えることもでき
る。更に実施例のように調節帯5、7を設けておけば、
これを恒温帯6や冷却帯8に変化させることによっても
ヒートカーブを調節することができる。従って本発明に
よれば、スラグの組成変動等に対応させてヒートカーブ
を適切に設定することが可能となる。As described above, in the crystallization process, it is necessary to appropriately set the heat curve in correspondence with the composition variation of the slag, but in the molten slag crystallization furnace of the present invention, the crystallization container 10 is provided in each zone. Each can be driven independently at different speeds. Therefore, as shown in FIG. 2, the temperature holding time of the slag can be changed by changing the moving speed of the crystallization container 10 in the constant temperature zone 6. Further, as shown in FIG. 3, the cooling speed of the slag can be changed by changing the speed of the carrier 9 of the cooling zone 8. Further, if the adjustment bands 5 and 7 are provided as in the embodiment,
The heat curve can also be adjusted by changing this to the constant temperature zone 6 or the cooling zone 8. Therefore, according to the present invention, it becomes possible to appropriately set the heat curve in correspondence with the composition variation of the slag and the like.
【0013】[0013]
【発明の効果】以上に説明したように、本発明の溶融ス
ラグ結晶化炉によれば溶融スラグの組成変動等に対応さ
せてヒートカーブを幅広く調整することができ、溶融ス
ラグの結晶化を十分に行わせることができる。また実施
例のように搬送機としてローラユニットを使用し、結晶
化容器を耐熱性に優れたセラミックローラで移動させる
ことにより、高温のスラグによる機械設備の劣化を防止
することができる。As described above, according to the molten slag crystallization furnace of the present invention, the heat curve can be widely adjusted in accordance with the composition variation of the molten slag, and the crystallization of the molten slag is sufficiently performed. Can be done. In addition, by using a roller unit as a carrier and moving the crystallization container with a ceramic roller having excellent heat resistance as in the embodiment, deterioration of mechanical equipment due to high temperature slag can be prevented.
【図1】本発明の実施例を説明する断面図である。FIG. 1 is a sectional view illustrating an embodiment of the present invention.
【図2】恒温帯の搬送機の速度を変えることによるヒー
トカーブの変化を示すグラフである。FIG. 2 is a graph showing a change in a heat curve by changing the speed of a carrier in a constant temperature zone.
【図3】冷却帯の搬送機の速度を変えることによるヒー
トカーブの変化を示すグラフである。FIG. 3 is a graph showing a change in a heat curve by changing a speed of a carrier in a cooling zone.
2 炉体 4 昇温帯 6 恒温帯 8 冷却帯 9 搬送機 10 結晶化容器 2 furnace body 4 temperature rising zone 6 constant temperature zone 8 cooling zone 9 carrier 10 crystallization vessel
Claims (2)
帯と、溶融スラグを受け入れ結晶化させる恒温帯と、そ
の後の溶融スラグを冷却する冷却帯とに内部が区分され
た炉体と、前記炉体の昇温帯、恒温帯、冷却帯中の結晶
化容器を各帯毎にそれぞれ特立させて異なる速度で搬送
可能な搬送機とを備えたことを特徴とする溶融スラグ結
晶化炉。1. A furnace body whose inside is divided into a temperature rising zone for raising the temperature of the crystallization container to a predetermined temperature, a constant temperature zone for receiving and crystallizing the molten slag, and a cooling zone for cooling the molten slag thereafter. A molten slag crystallization furnace, characterized in that the crystallization containers in the temperature rising zone, the constant temperature zone, and the cooling zone of the furnace body are individually provided for each zone and can be transported at different speeds.
も1か所に、前後いずれの帯にも変化させることが可能
な調節帯を設けた請求項1記載の溶融スラグ結晶化炉。2. The molten slag crystallization furnace according to claim 1, wherein a control zone capable of changing to any of the front and back zones is provided at least at one place between the temperature rising zone, the constant temperature zone and the cooling zone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4326798A JP2527519B2 (en) | 1992-12-07 | 1992-12-07 | Molten slag crystallization furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4326798A JP2527519B2 (en) | 1992-12-07 | 1992-12-07 | Molten slag crystallization furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06171991A JPH06171991A (en) | 1994-06-21 |
JP2527519B2 true JP2527519B2 (en) | 1996-08-28 |
Family
ID=18191828
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4326798A Expired - Fee Related JP2527519B2 (en) | 1992-12-07 | 1992-12-07 | Molten slag crystallization furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2527519B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3271528B2 (en) * | 1996-10-04 | 2002-04-02 | 日本鋼管株式会社 | Slag aggregate production equipment |
CN103971924B (en) * | 2014-05-07 | 2016-05-25 | 黟县越驰科技电子有限公司 | Magnetic crystallization furnace |
JP2016013952A (en) * | 2014-07-02 | 2016-01-28 | 中部リサイクル株式会社 | Manufacturing apparatus for crystalline molten slag |
-
1992
- 1992-12-07 JP JP4326798A patent/JP2527519B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH06171991A (en) | 1994-06-21 |
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Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19960419 |
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