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JP3878390B2 - In-furnace deposit removal method for rotary kiln reduction furnace - Google Patents

In-furnace deposit removal method for rotary kiln reduction furnace Download PDF

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Publication number
JP3878390B2
JP3878390B2 JP2000091928A JP2000091928A JP3878390B2 JP 3878390 B2 JP3878390 B2 JP 3878390B2 JP 2000091928 A JP2000091928 A JP 2000091928A JP 2000091928 A JP2000091928 A JP 2000091928A JP 3878390 B2 JP3878390 B2 JP 3878390B2
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JP
Japan
Prior art keywords
rotary kiln
furnace
metal oxide
reducing
reduction furnace
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
JP2000091928A
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Japanese (ja)
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JP2001279312A (en
Inventor
泰永 遠藤
浩 小出
茂 森下
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
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries Ltd
Sumitomo Metal Industries 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 Sumitomo Heavy Industries Ltd, Sumitomo Metal Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP2000091928A priority Critical patent/JP3878390B2/en
Publication of JP2001279312A publication Critical patent/JP2001279312A/en
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Publication of JP3878390B2 publication Critical patent/JP3878390B2/en
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  • Manufacture And Refinement Of Metals (AREA)
  • Manufacture Of Iron (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Description

【0001】
【発明が属する技術分野】
本発明は、ロータリーキルン式還元炉の炉内付着物除去方法に関する。
【0002】
【従来の技術】
金属酸化物含有原料は、還元剤や成分調整剤などとともにロータリーキルン式還元炉に投入され、バーナーからロータリーキルン内へ放射された火炎によって加熱されつつ、撹拌されて、還元される。
【0003】
しかし、炉内温度によっては、被処理物の軟化半溶融物がロータリーキルンの内壁に付着し始め、時間経過とともに付着物の厚さが増大し、堰を形成してしまい、ついには原料やスラグが下流へ向かって移動できなくなる。このように付着物が所定の厚さ以上となった場合あるいは付着物が成長し原料の流れを阻害したり、ロータリーキルンの処理能力が低下してきた場合に、従来は、ロータリーキルン式還元炉を停止し、炉内温度を下げた後に、人力あるいは重機械などの手段により、炉内付着物を機械的に除去し、再度運転を始めていた。
【0004】
また、実開平6−2099号、特開2000−18830号には、ハンマーやスクリュー部材などを用いて、運転中に機械的にロータリーキルン内部の付着物を除去する方法が開示されているが、炉内温度が1200℃を越えるような高温のロータリーキルンには、熱的な耐久性の観点からこのような機械的な付着物除去装置を適用することは不可能である。
【0005】
なお、本明細書において、「金属酸化物」の語には、酸化鉄のみならず、Cu、Ti、Cr、Ni等の非鉄金属の酸化物も含まれる。
【0006】
【発明が解決しようとする課題】
上記従来技術においては、ロータリーキルン式還元炉の降温・再昇温による休止時間が長く、ロータリーキルンの稼働率を低下させ、かつ、付着物除去作業は付着物落下などが起こる可能性のある危険な作業であり、また昇降温による耐火物の損傷などの問題がある。
【0007】
この問題点に鑑みて、鋭意研究開発し本発明に至ったものであり、本発明の目的は、ロータリーキルン式還元炉を昇降温することなく、比較的短時間のうちに炉内付着物を除去する新しい方法を提供する事にある。
【0008】
【課題を解決するための手段】
上記目的は、請求項1に記載のロータリーキルン式還元炉の炉内付着物除去方法、すなわち、金属酸化物含有原料を炭素質固体還元剤を用いて還元するロータリーキルン式還元炉において、半溶融物がロータリーキルンの内壁に付着し、付着物が所定の厚さ以上となった場合に、金属酸化物含有原料の投入を中止し、還元剤のみを投入して炉内の還元雰囲気を維持した状態で運転する、具体的にはロータリーキルン排ガス中の酸素濃度を0〜1%、一酸化炭素濃度が1〜5%になるよう空気量を調整することにより、ロータリーキルンの炉内付着物を溶融・除去することができる。
【0009】
【作用】
金属酸化物含有原料の投入を中止し、還元剤のみを投入するとともに空気供給量を減らした状態で運転すると、付着物を構成している金属酸化物が、投入した還元剤と装入空気を減じた効果による還元雰囲気との相剰効果により、還元・溶融され、これにより、付着物全体が徐々に溶融・除去される。
【0010】
【発明の実施の形態】
以下、添付図面を参照して、本発明の実施形態について説明する。
【0011】
図1は、本発明の実施形態のロータリーキルンの正面断面を示す概略図である。
【0012】
ロータリーキルン1は円筒形状であり、外面は外皮鋼板101によって被われ、その内側には耐火レンガ102が内張りされている。上流開口端110(図1において左端)が、被処理物及び排ガスを放出する下流開口端120よりもわずかに高く、中心軸105がほぼ水平となるように配置してある。
【0013】
上流開口端110はフロントウォール103によって閉鎖されているが、重油バーナー130がフロントウォール103を貫通してあり、重油バーナー130の火炎135をロータリーキルン1の内部に放射している。また、フロントウォール103には、金属酸化物含有原料等投入ホッパー106のほかに還元剤投入ホッパー107が取り付けられている。さらに、フロントウォール103には空気吹き込み口108が取り付けられており、調整弁109によって、ロータリーキルン内への空気導入量を調整することができる。
【0014】
ロータリーキルン1は中心軸105のまわりに回転しており、金属酸化物含有原料等2は撹拌されながら、上流から下流へ向かって徐々に移動しつつ加熱され、金属酸化物は還元され、下流開口端120へ向かって移動し、ついに下流開口端120の下部から落下する。
【0015】
しかしながら、ロータリーキルン1の内壁に付着する付着物の厚さが所定値以上となると、被処理物の下流への移動が妨げられてしまう。
【0016】
【実施例】
本実施例においては、金属酸化物として酸化鉄含有ダストを用い、直径4.2m、長さ14mのロータリーキルンを用い、付着物の厚さが600mmに達した時に、上記通常運転を停止し、付着物除去運転に切り替える。酸化鉄含有原料等投入ホッパー106を閉じ、酸化鉄含有原料等の投入を停止し、一方、還元剤投入ホッパーを開いて、10mmアンダーの粒度の石炭を約1ton/hで連続投入した。炉内温度は1300℃以上とし、通常運転時よりも50℃程度高めとした。また、ロータリーキルン1への空気吹き込み量を減らして、ロータリーキルン内が酸化雰囲気にならないように保つ。付着物除去運転を続けると、付着物を構成している鉄含有酸化物が還元・溶融されるため、付着物全体が徐々に除去されて、約24時間で、付着物の厚さは100mm程度に低減された。この程度の厚さの付着物であれば、通常運転を行う上で障害とならない。
【0017】
【発明の効果】
本発明に係る炉内付着物除去方法によれば、比較的短時間のうちに付着物を除去し、運転を再開でき、ロータリーキルン式還元炉の休止期間を短縮し、炉の稼動率を向上できる。また、炉の昇降温による耐火物が損傷防止され、付着物の人か重機による除去作業が解消されるという効果が得られる。
【図面の簡単な説明】
【図1】本発明の実施形態のロータリーキルンの正面断面を示す概略図である。
【符号の説明】
1 ロータリーキルン
101 外皮鋼板
102 耐火レンガ
103 フロントウォール
105 中心軸
106 金属酸化物含有原料等投入ポッパー
107 還元剤投入ホッパー
110 上流開口端
120 下流開口端
130 重油バーナー
3 還元物
[0001]
[Technical field to which the invention belongs]
The present invention relates to a method for removing deposits in a rotary kiln type reduction furnace.
[0002]
[Prior art]
The metal oxide-containing raw material is put into a rotary kiln type reduction furnace together with a reducing agent, a component adjusting agent, and the like, and is stirred and reduced while being heated by a flame emitted from a burner into the rotary kiln.
[0003]
However, depending on the temperature in the furnace, the softened semi-melt of the object to be processed begins to adhere to the inner wall of the rotary kiln, and the thickness of the object increases with time, forming a weir. Cannot move downstream. Thus, when the deposit becomes thicker than the prescribed thickness, or when the deposit grows and obstructs the flow of raw materials, or the processing capacity of the rotary kiln has declined, the rotary kiln reduction furnace has been conventionally stopped. After the furnace temperature was lowered, the deposits in the furnace were mechanically removed by means of human power or heavy machinery, and the operation was started again.
[0004]
Japanese Utility Model Laid-Open No. 6-2099 and Japanese Patent Laid-Open No. 2000-18830 disclose a method of mechanically removing deposits inside the rotary kiln during operation using a hammer or a screw member. It is impossible to apply such a mechanical deposit removing device to a high temperature rotary kiln with an internal temperature exceeding 1200 ° C. from the viewpoint of thermal durability.
[0005]
In the present specification, the term “metal oxide” includes not only iron oxide but also oxides of non-ferrous metals such as Cu, Ti, Cr, and Ni.
[0006]
[Problems to be solved by the invention]
In the above-mentioned prior art, the downtime due to the temperature reduction / reheating of the rotary kiln type reduction furnace is long, the operation rate of the rotary kiln is lowered, and the deposit removal work is a dangerous work that may cause deposit fall etc. In addition, there are problems such as damage to refractories due to temperature rise and fall.
[0007]
In view of this problem, the present invention has been intensively researched and developed, and the object of the present invention is to remove the deposits in the furnace within a relatively short time without raising or lowering the temperature of the rotary kiln type reduction furnace. Is to provide a new way to do.
[0008]
[Means for Solving the Problems]
The above object is achieved by the method for removing deposits in a rotary kiln type reduction furnace according to claim 1, that is, in a rotary kiln type reduction furnace in which a metal oxide-containing raw material is reduced using a carbonaceous solid reducing agent. When it adheres to the inner wall of the rotary kiln and the deposit exceeds the specified thickness, it stops operation of the metal oxide-containing raw material and operates with the reducing atmosphere in the furnace maintained by introducing only the reducing agent. Specifically, by adjusting the amount of air so that the oxygen concentration in the rotary kiln exhaust gas is 0 to 1% and the carbon monoxide concentration is 1 to 5%, the deposits in the furnace of the rotary kiln are melted and removed. Can do.
[0009]
[Action]
If the metal oxide-containing raw material is stopped and the operation is performed with only the reducing agent and the air supply amount reduced, the metal oxide constituting the adhering substance will reduce the charged reducing agent and the charged air. Due to the coherent effect with the reducing atmosphere due to the reduced effect, it is reduced and melted, whereby the entire deposit is gradually melted and removed.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the accompanying drawings.
[0011]
FIG. 1 is a schematic view showing a front cross section of a rotary kiln according to an embodiment of the present invention.
[0012]
The rotary kiln 1 has a cylindrical shape, the outer surface is covered with a skin steel plate 101, and a refractory brick 102 is lined on the inner side. The upstream opening end 110 (left end in FIG. 1) is slightly higher than the downstream opening end 120 that discharges the object to be processed and the exhaust gas, and the central axis 105 is arranged to be substantially horizontal.
[0013]
Although the upstream opening end 110 is closed by the front wall 103, a heavy oil burner 130 passes through the front wall 103 and radiates a flame 135 of the heavy oil burner 130 into the rotary kiln 1. In addition to the metal oxide-containing raw material charging hopper 106, a reducing agent charging hopper 107 is attached to the front wall 103. Further, an air blowing port 108 is attached to the front wall 103, and the amount of air introduced into the rotary kiln can be adjusted by the adjustment valve 109.
[0014]
The rotary kiln 1 is rotated around the central axis 105, and the metal oxide-containing raw material 2 is heated while being gradually moved from upstream to downstream while being stirred, the metal oxide is reduced, and the downstream opening end It moves toward 120 and finally falls from the lower part of the downstream opening end 120.
[0015]
However, when the thickness of the deposit adhered to the inner wall of the rotary kiln 1 exceeds a predetermined value, the downstream movement of the workpiece is hindered.
[0016]
【Example】
In this example, iron oxide-containing dust was used as the metal oxide, a rotary kiln having a diameter of 4.2 m and a length of 14 m was used, and when the thickness of the deposit reached 600 mm, the above normal operation was stopped and attached. Switch to kimono removal operation. The iron oxide-containing raw material charging hopper 106 was closed, and the iron oxide-containing raw material charging was stopped. On the other hand, the reducing agent charging hopper was opened, and coal having a particle size under 10 mm was continuously charged at about 1 ton / h. The furnace temperature was set to 1300 ° C or higher, and about 50 ° C higher than that during normal operation. Further, the amount of air blown into the rotary kiln 1 is reduced to keep the rotary kiln from becoming an oxidizing atmosphere. If the deposit removal operation is continued, the iron-containing oxide constituting the deposit is reduced and melted, so the entire deposit is gradually removed, and the thickness of the deposit is about 100 mm in about 24 hours. Reduced to If the deposit has such a thickness, it does not become an obstacle to normal operation.
[0017]
【The invention's effect】
According to the in-furnace deposit removal method according to the present invention, deposits can be removed in a relatively short time, the operation can be resumed, the downtime of the rotary kiln reduction furnace can be shortened, and the operation rate of the furnace can be improved. . Further, the refractory due to the temperature rise and fall of the furnace is prevented from being damaged, and the effect of removing the deposit by a person or heavy equipment is obtained.
[Brief description of the drawings]
FIG. 1 is a schematic view showing a front cross section of a rotary kiln according to an embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Rotary kiln 101 Hull steel plate 102 Refractory brick 103 Front wall 105 Center shaft 106 Metal oxide containing raw material introduction popper 107 Reducing agent introduction hopper 110 Upstream opening end 120 Downstream opening end 130 Heavy oil burner 3 Reduced product

Claims (2)

金属酸化物含有原料を炭素質固体還元剤を用いて還元するロータリーキルン式還元炉において、半溶融物がロータリーキルンの内壁に付着し、付着物が所定の厚さ以上となった場合に、金属酸化物含有原料の投入を中止し、還元剤のみを投入するとともに空気供給量を減らして炉内の還元雰囲気を維持した状態で運転するロータリーキルン式還元炉の炉内付着物を溶融除去する方法。In a rotary kiln type reduction furnace that reduces a metal oxide-containing raw material using a carbonaceous solid reducing agent, when a semi-molten material adheres to the inner wall of the rotary kiln and the deposit exceeds a predetermined thickness, the metal oxide how to stop the introduction of containing raw material is melted removed furnace deposits rotary kiln reducing furnace to operate in a state of to reduce the air supply to maintain a reducing atmosphere in the furnace while introducing only the reducing agent. 金属酸化物含有原料を炭素質固体還元剤を用いて還元するロータリーキルン式還元炉において、半溶融物がロータリーキルンの内壁に付着し、付着物が所定の厚さ以上となった場合に、金属酸化物含有原料の投入を中止し、還元剤のみを投入するとともに空気供給量を減らしてロータリーキルン式還元炉排ガス中の酸素濃度を0〜1%、一酸化炭素濃度が1〜5%になるように炉内の還元雰囲気を維持した状態で運転するロータリーキルン式還元炉の炉内付着物を溶融除去する方法。In a rotary kiln type reduction furnace that reduces a metal oxide-containing raw material using a carbonaceous solid reducing agent, when a semi-molten material adheres to the inner wall of the rotary kiln and the deposit exceeds a predetermined thickness, the metal oxide Furnace so that oxygen content in the rotary kiln type reduction furnace exhaust gas is reduced to 0 to 1% and carbon monoxide concentration to 1 to 5% by stopping the introduction of the contained raw materials and reducing only the reducing agent and reducing the air supply amount. A method of melting and removing deposits in a rotary kiln type reduction furnace that operates in a state in which the reducing atmosphere is maintained.
JP2000091928A 2000-03-29 2000-03-29 In-furnace deposit removal method for rotary kiln reduction furnace Expired - Fee Related JP3878390B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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JP3878390B2 true JP3878390B2 (en) 2007-02-07

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JP4820777B2 (en) * 2007-06-04 2011-11-24 住友重機械工業株式会社 Reduction processing apparatus and reduction processing method
US10100378B2 (en) * 2013-12-19 2018-10-16 Tata Steel Nederland Technology B.V. Method to operate a smelt cyclone

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