JP2001254114A - Rotary hearth furnace - Google Patents

Rotary hearth furnace

Info

Publication number
JP2001254114A
JP2001254114A JP2000065793A JP2000065793A JP2001254114A JP 2001254114 A JP2001254114 A JP 2001254114A JP 2000065793 A JP2000065793 A JP 2000065793A JP 2000065793 A JP2000065793 A JP 2000065793A JP 2001254114 A JP2001254114 A JP 2001254114A
Authority
JP
Japan
Prior art keywords
furnace
rotary hearth
pellets
rotary
bed
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
JP2000065793A
Other languages
Japanese (ja)
Inventor
Koji Matsui
宏司 松井
Seiji Nonoyama
誠二 野々山
Toshihiko Nishikawa
年彦 西川
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP2000065793A priority Critical patent/JP2001254114A/en
Publication of JP2001254114A publication Critical patent/JP2001254114A/en
Pending legal-status Critical Current

Links

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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)
  • Manufacture Of Iron (AREA)
  • Tunnel Furnaces (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a rotary hearth furnace, in which the service life of the rotary hearth is extended, and the maintenance is easily performed and the cost needed to this maintenance is reduced. SOLUTION: In this rotary hearth furnace in which pellet 8 obtained by mixing and granulating metal oxide and reducing agent, is charged on the rotary hearth 3 in the furnace and carried in the furnace by rotating this rotary hearth, and heated to a high temperature to reduce the metal oxide into the metal, dolomite grain 7 having 5-40 mm outer diameter is laid on the rotary hearth and the pellet is charged on the laid dolomite grain.

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】本発明は製鋼廃棄物等の金属
酸化物を還元処理し回収するための回転炉床の構造に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rotary hearth structure for reducing and recovering metal oxides such as steelmaking waste.

【0002】[0002]

【従来の技術】従来からインメテコ法と称されている金
属還元処理方法は、特公昭64ー5233,特開平8ー
337827等の特許公報により知られているように、
粉状の金属酸化物(酸化鉄,酸化ニッケル等)と還元剤
(石炭,コークス等)を結合材とともに混合し造粒する
ことにより直径10〜30mm程度のペレットを形成
し、該ペレットを回転炉床炉に装入して高温度に加熱す
ることにより、金属を還元し回収しようとするものであ
る。
2. Description of the Related Art The metal reduction treatment method conventionally called the inmeteco method is disclosed in Japanese Patent Publications Nos. 64-5233 and 8-3337827.
A powdery metal oxide (iron oxide, nickel oxide, etc.) and a reducing agent (coal, coke, etc.) are mixed with a binder and granulated to form pellets having a diameter of about 10 to 30 mm. It is intended to reduce and recover metals by charging them into a floor furnace and heating them to a high temperature.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記金属還
元処理においては従来から回転床炉が使用されている
が、加熱により溶融したペレットが回転床を構成する耐
火物に溶着することがあるので、その耐火物を除去する
メンテナンス作業に大きな労力を必要とするものであっ
た。また、回転床には従来から熱膨張吸収用のスリット
が形成されているが、そのスリットにペレットが落下す
ると、リジッドな耐火物の場合に次の昇温時に膨張を吸
収できなくなり、耐火物を破損させることがあった。さ
らには、炉床耐火物がペレット排出用のスクリューコン
ベヤとの間にペレットが挟まると炉床耐火物が摩耗し易
いという問題があった。このため、従来では回転床の耐
火物の寿命は短く,メンテナンスが容易でなく、高いコ
ストが掛かる状況であった。そこで本発明は、上記課題
を解決し、回転床の寿命を延ばし,メンテナンスを容易
ならしめ、そのコストを軽減しようとするものである。
By the way, in the metal reduction treatment, a rotary bed furnace has been conventionally used. However, since the pellets melted by heating may be welded to a refractory constituting the rotary bed, Maintenance work for removing the refractory required a great deal of labor. In addition, a slit for absorbing thermal expansion is conventionally formed in the rotating bed, but if pellets fall into the slit, it will not be able to absorb the expansion at the next temperature rise in the case of a rigid refractory, and the refractory May cause damage. Further, there is a problem that the hearth refractory is liable to be worn when the pellet is sandwiched between the hearth refractory and a screw conveyor for discharging the pellet. For this reason, in the past, the life of the refractory on the rotating bed was short, maintenance was not easy, and high cost was required. Therefore, the present invention is to solve the above-mentioned problems, prolong the life of the rotating bed, facilitate maintenance, and reduce the cost.

【0004】[0004]

【課題を解決するための手段】そのために本発明は、金
属酸化物と還元剤とを混合し造粒してなるペレットを炉
内の回転床上に装入し、該回転床を回転させることによ
り該ペレットを炉内搬送し高温度に加熱することにより
金属を還元するのに使用する回転床炉であって、回転床
上に外径5〜40mmのドロマイト粒を敷設し、その上
にペレットが載置されるようにしたことを特徴とする。
For this purpose, the present invention provides a method in which a pellet formed by mixing and granulating a metal oxide and a reducing agent is charged on a rotating bed in a furnace, and the rotating bed is rotated. A rotary bed furnace used to reduce the metal by transporting the pellets in a furnace and heating the pellets to a high temperature. Dolomite grains having an outer diameter of 5 to 40 mm are laid on the rotary bed, and the pellets are placed thereon. It is characterized by being arranged.

【0005】[0005]

【発明の実施の形態】次に本発明に係る回転床炉の実施
の形態を説明する。この回転床炉は、図1の水平断面平
面図、および、図2のA−A線断面図に示したように、
平面円形の炉体1が形成され、該炉体内底部に車輪2が
固設され、該車輪2上に環状の回転床3が支持され、動
力源(図示せず)の駆動によって該回転床3が該炉体内
で矢印aの方向に低速回転するよう構成されている。
Next, an embodiment of a rotary hearth furnace according to the present invention will be described. As shown in the horizontal sectional plan view of FIG. 1 and the sectional view taken along line AA of FIG.
A furnace body 1 having a circular plane shape is formed, wheels 2 are fixed to the bottom of the furnace body, and an annular rotating floor 3 is supported on the wheels 2. The rotating floor 3 is driven by a power source (not shown). Are configured to rotate at a low speed in the direction of arrow a in the furnace.

【0006】この回転床3は、耐火レンガをもって構築
され、その上面の外周縁と内周縁に夫々凸堤4,5を形
成することにより深さ50mm程の窪部6を形成し、該
窪部中に外径5〜40mmのドロマイト粒7を敷設して
なる。このドロマイト粒7は、SiO,CaO,MgO
を主成分とするドロマイト(クカイ石)を焼成したレン
ガ質のもので、安価で入手が容易であるとともに、化学
的に安定していて耐熱性が高い等の特質を持つ。
The rotary floor 3 is constructed of fire-resistant bricks, and convex ridges 4 and 5 are formed on an outer peripheral edge and an inner peripheral edge of an upper surface thereof to form a concave portion 6 having a depth of about 50 mm. Dolomite grains 7 having an outer diameter of 5 to 40 mm are laid therein. The dolomite grains 7 are made of SiO, CaO, MgO.
It is a brick made of dolomite (kukai stone) whose main component is calcined. It is inexpensive and easily available, and has characteristics such as being chemically stable and having high heat resistance.

【0007】8はこの回転床炉にて還元処理する金属酸
化物のペレットであって、製鋼ダストあるいは廃車粉砕
チップのような粉粒状体を石炭,コークス,木炭等の炭
素系還元剤、およびベントナイト等の無機結合材と混合
し造粒することにより外径10〜30mmのペレット状
に形成されている。
Reference numeral 8 denotes pellets of metal oxide to be reduced in the rotary bed furnace. The pellets are used to reduce powdery or granular materials such as steelmaking dust or waste car pulverized chips to a carbon-based reducing agent such as coal, coke or charcoal, and bentonite. It is formed into a pellet having an outer diameter of 10 to 30 mm by mixing and granulating with an inorganic binder such as.

【0008】9は炉体1の天井壁に開設されたペレット
装入口、10は炉体の側壁に設けられたバーナ、11は
燃焼ガス排出口、12は回転床3上に架すように設けら
れたスクリューコンベア、13は該スクリューコンベア
の一端に設けられたペレット抽出口である。そして、炉
体1内は矢印aに示した回転床3の回転方向に従い加熱
帯と還元帯が形成されている。そしてペレット8は、装
入口9から投入され回転床3上に敷設されたドロマイト
粒7上に載置されて、回転床3が回転するに従い加熱帯
にて1000℃程度の高温度に加熱され、還元帯にて還
元性に保たれた雰囲気ガスの基で該ペレット中の金属酸
化物が炭素系還元剤との接触により還元され金属化す
る。そして、スクリューコンベア12にて抽出口13に
掻き寄せられ炉外に排出される。
Reference numeral 9 denotes a pellet loading opening formed on the ceiling wall of the furnace body 1, 10 a burner provided on the side wall of the furnace body, 11 a combustion gas discharge port, and 12 provided so as to span the rotary bed 3. The screw conveyor 13 provided is a pellet extraction port provided at one end of the screw conveyor. A heating zone and a reduction zone are formed in the furnace body 1 according to the rotation direction of the rotary bed 3 indicated by the arrow a. Then, the pellets 8 are loaded from the charging port 9 and placed on the dolomite grains 7 laid on the rotating bed 3, and are heated to a high temperature of about 1000 ° C. in a heating zone as the rotating bed 3 rotates, The metal oxide in the pellets is reduced and metallized by contact with a carbon-based reducing agent under the atmosphere gas kept reducible in the reduction zone. Then, it is scraped to the extraction port 13 by the screw conveyor 12 and discharged out of the furnace.

【0009】この回転床3では、ペレット8が加熱によ
って溶融しても、回転床3上に敷設された前記ドロマイ
ト粒7間に浸入するだけであるので、回転床3を構成す
る炉床耐火物自体に溶着することなく、また、熱膨張吸
収用のスリットにペレットが落下して炉床を破損させる
ようなおそれもなくなり、メンテナンスが容易になる。
また、ドロマイト粒7がペレット8に付着して高炉や精
錬炉にそのまま搬入されたとしても、SiO,CaO,
MgOを主成分とするものであるので、何ら悪影響を及
ぼすことがない。
In the rotary bed 3, even if the pellets 8 are melted by heating, they only penetrate between the dolomite grains 7 laid on the rotary bed 3. Without welding to itself, there is no danger that the pellets will fall on the slits for absorbing thermal expansion and damage the hearth, making maintenance easier.
Further, even if the dolomite grains 7 adhere to the pellets 8 and are directly carried into a blast furnace or a smelting furnace, SiO, CaO,
Since it is mainly composed of MgO, there is no adverse effect.

【0010】また、図3に示したように、ペレット8が
スクリューコンベア12にて抽出口11に掻き寄せられ
る際に、該ペレットが該スクリューコンベアによって圧
下されてもその下に敷設されたドロマイト粒7が自在に
動き得ることによって、ペレット8が食い込んでスクリ
ューコンベア12の回転を妨害したり回転床自体を摩耗
させたりするおそれがない。なお、回転床上に敷設する
ドロマイト粒の大きさとしては外径5〜40mmである
ことが望ましく、概略この範囲であることで、ドロマイ
ト粒が自在に動き得て上記作用がなされるとともに、熱
膨張,収縮を吸収し得るようになる。
As shown in FIG. 3, when the pellets 8 are scraped by the screw conveyor 12 to the extraction port 11, even if the pellets are pressed down by the screw conveyor, the dolomite granules laid under the pellets are crushed. Since the 7 can move freely, there is no danger that the pellets 8 will bite and hinder the rotation of the screw conveyor 12 or wear the rotating bed itself. The size of the dolomite particles to be laid on the rotating bed is desirably 5 to 40 mm in outer diameter. When the size is approximately in this range, the dolomite particles can move freely, and the above-described action is performed. , To be able to absorb shrinkage.

【0011】[0011]

【発明の効果】このように本発明は、金属酸化物と還元
剤とを混合し造粒してなるペレットを炉内の回転床上に
装入し、該回転床を回転させることにより該ペレットを
炉内搬送し高温度に加熱することにより金属を還元する
のに使用する回転床炉であって、回転床上に外径5〜4
0mmのドロマイト粒を敷設し、その上にペレットが載
置されるようにしたので、回転床の寿命を延ばし,メン
テナンスを容易ならしめ、そのコストを軽減させるなど
有益な効果がある。
As described above, according to the present invention, a pellet obtained by mixing and granulating a metal oxide and a reducing agent is charged on a rotary bed in a furnace, and the pellet is rotated by rotating the rotary bed. A rotary bed furnace used to reduce metal by being transported in a furnace and heated to a high temperature, and having an outer diameter of 5 to 4 on a rotary bed.
Since the dolomite grains of 0 mm are laid and the pellets are placed thereon, there are beneficial effects such as extending the life of the rotating bed, facilitating maintenance, and reducing the cost.

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

【図1】本発明の回転床炉の実施の形態を示す水平断面
平面図。
FIG. 1 is a horizontal sectional plan view showing an embodiment of a rotary bed furnace of the present invention.

【図2】図1の回転床炉のA−A線断面図。FIG. 2 is a sectional view taken along the line AA of the rotary bed furnace of FIG.

【図3】図1の回転床炉のB−B線断面図。FIG. 3 is a cross-sectional view of the rotary bed furnace of FIG. 1 taken along line BB.

【符号の説明】[Explanation of symbols]

1 炉体 3 回転床 4,5 凸堤 6 窪部 7 ドロマイト粒 8 ペレット DESCRIPTION OF SYMBOLS 1 Furnace body 3 Rotating floor 4, 5 Convex ridge 6 Depression 7 Dolomite grain 8 Pellet

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 金属酸化物と還元剤とを混合し造粒して
なるペレットを炉内の回転床上に装入し、該回転床を回
転させることにより該ペレットを炉内搬送し高温度に加
熱することにより金属を還元するのに使用する回転床炉
であって、回転床上に外径5〜40mmのドロマイト粒
を敷設し、その上にペレットが載置されるようにしたこ
とを特徴とする回転床炉。
1. A pellet formed by mixing and granulating a metal oxide and a reducing agent is loaded on a rotary bed in a furnace, and the rotary bed is rotated to convey the pellets in the furnace to a high temperature. A rotary bed furnace used for reducing a metal by heating, wherein dolomite grains having an outer diameter of 5 to 40 mm are laid on the rotary bed, and pellets are placed thereon. Rotary hearth furnace.
JP2000065793A 2000-03-09 2000-03-09 Rotary hearth furnace Pending JP2001254114A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000065793A JP2001254114A (en) 2000-03-09 2000-03-09 Rotary hearth furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000065793A JP2001254114A (en) 2000-03-09 2000-03-09 Rotary hearth furnace

Publications (1)

Publication Number Publication Date
JP2001254114A true JP2001254114A (en) 2001-09-18

Family

ID=18585261

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000065793A Pending JP2001254114A (en) 2000-03-09 2000-03-09 Rotary hearth furnace

Country Status (1)

Country Link
JP (1) JP2001254114A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007113929A1 (en) * 2006-04-04 2007-10-11 Nippon Steel Corporation Hearth carriage connection structure for rotary hearth furnace
WO2007113928A1 (en) * 2006-04-03 2007-10-11 Nippon Steel Corporation Hearth structure of rotary hearth furnace
WO2010030148A2 (en) * 2008-09-12 2010-03-18 주식회사 원진 A reduction and fusing method and reduction and fusing device for a metal oxide using a hermetically sealed crucible
CN103388980A (en) * 2012-05-07 2013-11-13 北京低碳清洁能源研究所 Drying furnace or pyrolyzing furnace with rotary material bed
JP2017036473A (en) * 2015-08-10 2017-02-16 住友金属鉱山株式会社 Process for smelting nickel oxide ore

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007113928A1 (en) * 2006-04-03 2007-10-11 Nippon Steel Corporation Hearth structure of rotary hearth furnace
US8057736B2 (en) 2006-04-03 2011-11-15 Nippon Steel Corporation Hearth structure of rotary furnace hearth
KR101093786B1 (en) 2006-04-03 2011-12-19 신닛떼쯔 엔지니어링 가부시끼가이샤 Hearth structure of rotary hearth furnace
WO2007113929A1 (en) * 2006-04-04 2007-10-11 Nippon Steel Corporation Hearth carriage connection structure for rotary hearth furnace
US8021602B2 (en) 2006-04-04 2011-09-20 Nippon Steel Corporation Hearth carriage coupling structure of rotary furnace hearth
KR101073115B1 (en) 2006-04-04 2011-10-13 신닛떼쯔 엔지니어링 가부시끼가이샤 Hearth carriage connection structure for rotary hearth furnace
CN101438117B (en) * 2006-04-04 2012-08-22 新日本制铁株式会社 Hearth carriage connection structure of rotary hearth furnace
WO2010030148A2 (en) * 2008-09-12 2010-03-18 주식회사 원진 A reduction and fusing method and reduction and fusing device for a metal oxide using a hermetically sealed crucible
WO2010030148A3 (en) * 2008-09-12 2010-07-15 주식회사 원진 A reduction and fusing method and reduction and fusing device for a metal oxide using a hermetically sealed crucible
CN103388980A (en) * 2012-05-07 2013-11-13 北京低碳清洁能源研究所 Drying furnace or pyrolyzing furnace with rotary material bed
JP2017036473A (en) * 2015-08-10 2017-02-16 住友金属鉱山株式会社 Process for smelting nickel oxide ore

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