JPS59170212A - Production of reduced iron briquette - Google Patents

Production of reduced iron briquette

Info

Publication number
JPS59170212A
JPS59170212A JP4363083A JP4363083A JPS59170212A JP S59170212 A JPS59170212 A JP S59170212A JP 4363083 A JP4363083 A JP 4363083A JP 4363083 A JP4363083 A JP 4363083A JP S59170212 A JPS59170212 A JP S59170212A
Authority
JP
Japan
Prior art keywords
reduced iron
feeder
briquettes
carbonaceous material
sponge
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
JP4363083A
Other languages
Japanese (ja)
Inventor
Kunio Hachisuga
蜂須賀 邦夫
Michio Kabaru
香春 陸夫
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
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP4363083A priority Critical patent/JPS59170212A/en
Publication of JPS59170212A publication Critical patent/JPS59170212A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/0086Conditioning, transformation of reduced iron ores

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To produce reduced iron briquettes without generation of combustible gas and reoxidation of reduced iron by supplying high temp. sponge-like reduced iron and fine carbonaceous material having respectively specific grain size distributions to a feeder of a compression modling device and molding the materials with forming rolls. CONSTITUTION:Reduced iron like sponge having a high temp. of >=650 deg.C and >=80% 3-30mm. and <=20% -3mm. discharged from a reduction furnace is fed via a container 1 and a storage bin 3 to a compression molding device 2 and is fed forcibly by a screw feeder 4 to forming roll 5. On the other hand, a fine carbonaceous material having 50-90% 0.075-2.0mm. grain size and <=2% moisture content is supplied via a hopper 11 of a carbonaceous material feeder 10, a constant feeder 12, a screw conveyor 13 and a chute 14 to the feeder 4. The reduced iron added with the carbonaceous material is formed by the rolls 5 to a chained reduced iron briquette of the high temp. which is then separated with a separating machine 6. The separated briquettes are dropped into a cooling water tank 8, and are transferred by a vibrating conveyor 7, from which the briquettes are conveyed by a discharging conveyor 9.

Description

【発明の詳細な説明】 本発明は、微細炭材k ’11rs加した高温還元鉄を
圧縮成形して製造される加炭還元鉄ブリケットの製造方
法の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for producing carburized reduced iron briquettes, which are produced by compression molding high-temperature reduced iron to which fine carbon material k'11rs has been added.

従来、熱間或は冷間のスポンジ状の還元鉄を・圧縮成形
装置で圧縮成形して、ブリケット化し還元鉄サイズを大
きくすると共に還元鉄の比表面積と気孔率を減少させ、
輸送効率を高めると共に化学的安定、再酸化防止を計る
ことは知られている。
Conventionally, hot or cold sponge-like reduced iron is compression molded using a compression molding machine to form briquettes to increase the size of the reduced iron and reduce the specific surface area and porosity of the reduced iron.
It is known to improve transport efficiency, provide chemical stability, and prevent re-oxidation.

例えば第1図は、還元炉から熱間排出される高温(65
−0℃以上)の還元鉄に対して採用された公知の熱間還
元鉄の圧縮成形装置を示す。
For example, Figure 1 shows the high temperature (65
1 shows a known compression molding apparatus for hot reduced iron, which is used for reduced iron at a temperature of −0° C. or higher.

還元炉(図示せず)から熱間排出されたスポンジ状の還
元鉄は一旦、コンテナlに装入されて、圧縮成形装置2
に送られる。なおコンテナ1は密閉型になっており、上
記還元鉄の保温と再ば化防止とが可能となっている。上
記コンテナlは圧縮成形装置2の上部に設けられた貯蔵
ビン3に直結芒れて、上記還元鉄が大気にさらされるこ
となく貯蔵ビン3円に投入される。この貯蔵ビン3と成
形ロール5との間には強制圧送式の例えばスクリュ一式
のフィーダー4があり、上記還元鉄がこのフィーダー4
により成形ロール5に強制的に圧送される。
Sponge-like reduced iron hotly discharged from a reduction furnace (not shown) is once charged into a container 1, and then transferred to a compression molding device 2.
sent to. Note that the container 1 is of a closed type, making it possible to keep the reduced iron warm and prevent it from re-fertilizing. The container 1 is directly connected to a storage bin 3 provided on the top of the compression molding apparatus 2, and the reduced iron is charged into the storage bin 3 without being exposed to the atmosphere. Between the storage bin 3 and the forming roll 5, there is a forced feed type feeder 4, for example, a set of screws, and the reduced iron is fed to this feeder 4.
The material is forcibly fed to the forming rolls 5.

そし、て圧縮成形装置2の下部には、分離機6゜振動コ
ンベアーマを有する冷却水槽8が設けられ・成形ロール
5刀為らの高温のチェーン状還元鉄ブリケットを分離機
6で分離し、冷却水槽8へ落下し、水中冷却しつつ振動
コンベアー7で移送し・水槽8炉ら常温以上の偏置で排
出する。排出された還元鉄ブリケットは搬送コンベアー
9で搬送され、例えば山積貯蔵される。
A cooling water tank 8 having a separator 6° vibrating conveyor arm is provided at the bottom of the compression molding apparatus 2.The separator 6 separates the high temperature chain-shaped reduced iron briquettes from the five forming rolls. It falls into a cooling water tank 8, is cooled in water and transferred by a vibrating conveyor 7, and is discharged from a water tank 8 furnace at a temperature above room temperature. The discharged reduced iron briquettes are transported by a transport conveyor 9 and stored, for example, in a pile.

そして各種UJ製鋼炉の溶解鉄源として使用される○ なお上記熱間圧w成形では、圧縮成形−4A置2の成形
ロール5からの還元鉄ブリケットは600℃以上の’=
温であシ、この顕熱km効利用するために、成形ロール
5直下で製品コンテナ(図示せすりに装入して上記各種
の製鋼炉へ搬送供給1′る場合もめる。
And used as a source of molten iron in various UJ steelmaking furnaces.
In order to take advantage of this sensible heat, the product may be charged into a product container (not shown) directly below the forming rolls 5 and transported and supplied to the above-mentioned various steelmaking furnaces.

ところで上記・還元鉄ブリケットを各種の製鋼炉で溶解
処理し、所定の鋼種の溶鋼を得ようとする際、上記還元
鉄ブリケット中の炭素含有量が不足する場合、コークス
粉、カーボンブラック等の微細炭材を上記還元鉄に添加
して圧縮成形する安価で・かつ〃l炭量調節自在なカロ
炭方法か・特開昭53−12’712号公報に提案され
ている。具体的には第1図の圧縮成形装置2のフィーダ
ー4に炭材ケ供給)る炭材供給装置10を併設しフィー
ダー4に、コークス等の微粉末をホツノ< −11。
By the way, when the above-mentioned reduced iron briquettes are melted in various steelmaking furnaces to obtain molten steel of a specified steel type, if the carbon content in the above-mentioned reduced iron briquettes is insufficient, fine particles such as coke powder and carbon black may be used. An inexpensive Karo-char method in which a carbonaceous material is added to the above-mentioned reduced iron and compression molded is proposed in JP-A-53-12-712, which is capable of controlling the amount of coal. Specifically, a carbon material supply device 10 is attached to the feeder 4 of the compression molding apparatus 2 shown in FIG.

コンスタントフィーダー12.スクリューコンベアー1
′、り、シュート14を介し供給するものである。
Constant feeder 12. screw conveyor 1
', is supplied through the chute 14.

ところが上記特開昭53−1’2’712号公報には使
用炭材の粒度についての記載かない。′−1,た将開昭
51−’14435号公報のスクラップ鉄、鋼に炭材欠
除7J[I L、て冷間圧縮成形する方法では、0.0
1鰭〜2.8 mのコークス粉を使用することか記載3
れているにとどまる。
However, JP-A-53-1'2'712 does not describe the particle size of the carbon material used. '-1, In the method of cold compression molding of scrap iron and steel, 7J [IL, 0.0
It is stated that coke powder of 1 fin to 2.8 m should be used.3
It remains as it is.

本弁明は、第1図の加炭還元鉄ブリケットの製造プロセ
スにおいて、特に650℃以上の高温。
This defense is based on the manufacturing process of the carburized reduced iron briquettes shown in FIG. 1, especially at a high temperature of 650°C or higher.

スポンジ状の3〜30ni80%以上−3關以下20%
以−トの還元鉄に炭材を添加する場合に、上記炭材の粒
度、水分埴か、加炭還元鉄ブリケットの品質製造プロセ
スの安全上の問題の有無を決定するという調査結果iI
Cもとづきなされたもので、本発明は炭材を際加し、上
記高温スポンジ状の還元鉄を圧縮成形する方法において
、■炭材添加による還元鉄ブリケットの蛸度2強度低下
を最少にすると共に■炭イ珂水分と高温スポンジ状還元
鉄との反応による可燃性カスの発生及びそれにともなう
発熱、還元鉄の書叡化を有効に防止した還元鉄ブリ扮ッ
トの製造方法を提供するものである。
Spongy 3~30ni 80% or more - 3cm or less 20%
When adding carbonaceous material to the above-mentioned reduced iron, it is determined whether there is a safety problem in the particle size of the carbonaceous material, moisture content, or the quality manufacturing process of carburized reduced iron briquettes II.
The present invention is based on the method of compression molding the above-mentioned high-temperature sponge-like reduced iron by adding a carbonaceous material to the method. ■The present invention provides a method for producing reduced iron briquettes that effectively prevents the generation of flammable scum due to the reaction between charcoal water and high-temperature sponge-like reduced iron, the resulting heat generation, and the formation of reduced iron. be.

本発明の要旨は次V通りである。The gist of the present invention is as follows.

スポンジ状の還元鉄を圧1に6fit形装置のフィダー
に供給するときに、微細な炭材勿炭材供給装置りCより
上記フィーダーに供給して上記還元鉄VC添加したのち
、この還元鉄を圧縮成型装置の成型ロールにより成形す
る還元鉄ブリケットの製造方法しこおいて、650℃以
上の高温、スポンジ状の3〜30 rrvn 80%以
上−3岨20%以下の還元鉄に、粒度0.0 ’i’ 
5+rtm〜2.0ttun、 50〜90%で、かつ
含有水分2%以下の炭材を添加することを特徴とする還
元鉄ブリケットの製造方法。
When feeding sponge-like reduced iron to the feeder of a 6-fit type device at pressure 1, the fine carbonaceous material is fed to the feeder from the carbonaceous material feeding device C, and after the above reduced iron VC is added, this reduced iron is A method for producing reduced iron briquettes formed by a forming roll of a compression molding device is carried out at a high temperature of 650° C. or higher, into a spongy reduced iron having a particle size of 0.8 to 30 80% to 20% or less. 0 'i'
5+rtm to 2.0ttun, 50 to 90%, and a method for producing reduced iron briquettes, characterized by adding carbonaceous material having a moisture content of 2% or less.

以下、本発明の還元鉄ブリケットの製造方法について説
明する。
Hereinafter, the method for producing reduced iron briquettes of the present invention will be explained.

コークス、カーボンブラック、黒鉛等の炭材は還元鉄に
比して低督度であり、この炭材を尚温スポンジ状の還元
鉄に添加すると圧縮成形時、炭材の還元鉄同離間作用が
作用し還元鉄ブリケットの密度亜ひ強直が・炭材非添加
ブリケットに比軟して低下する。
Carbonaceous materials such as coke, carbon black, and graphite have a lower temperature than reduced iron, and when these carbonaceous materials are added to reduced iron in the form of a still-temperature sponge, during compression molding, the carbonaceous materials have a reduced iron separation effect. As a result, the density of reduced iron briquettes is lower than that of briquettes without carbonaceous additives.

還元鉄ブリケットの密度低下は、第2図に示すように高
温還元鉄ブリケットを水中に罰冷却し、常温以上で大気
中に取り出し大気中で冷却する冷却工程(第1図のプロ
セスの冷却工程)における再版化の増大の大きな原因に
なると共に、還元鉄ブリケットの溶解処理工程せでの連
撮、貯蔵時(例えば海上輸送、大気開放下での貯蔵時)
の再酸化の増大の犬さな原因となシ、還元エネルギーの
多大な浪費となる。
The density reduction of reduced iron briquettes can be achieved by cooling the high-temperature reduced iron briquettes in water as shown in Figure 2, then taking them out into the atmosphere at room temperature or higher and cooling them in the atmosphere (the cooling process of the process in Figure 1). This is a major cause of the increase in reprinting in the industry, as well as continuous shooting during the melting process of reduced iron briquettes, and during storage (e.g., shipping by sea, storage in open air).
This causes a significant increase in reoxidation, resulting in a significant waste of reduction energy.

また還元鉄ブリケットの強度低下は、このブリケットの
浴解処理工程葦での逢i過程での粉発生を助長し溶解処
理工程での歩留低下の原因となったり或は溶解工程での
発生集展ダストの増大及び飛散ダストによる耐火物、例
えば電気炉蓋の横部等の溶解プロセスの経済性をそこな
わせしめる。
In addition, the decrease in strength of reduced iron briquettes may promote the generation of powder during the melting process of the briquettes in the bath melting process, causing a decrease in yield during the melting process, or may cause the generation of powder during the melting process. The increase in spread dust and the scattered dust impair the economic efficiency of the process of melting refractories, such as the sides of electric furnace lids.

そこで本発明者等は咋加戻材の粒度及び粒度構成と還元
鉄ブリケットの密度2強度との関係について程々検討、
調査し・還元鉄に冷加する炭材粒度栴成によって、上記
晶度、シ虫度低下を極少に出来ること7見い出し1乙。
Therefore, the present inventors conducted extensive research on the relationship between the particle size and particle size structure of the rejuvenating material and the density 2 strength of reduced iron briquettes.
The above-mentioned decrease in crystallinity and graininess can be minimized by investigating and reducing the grain size of carbon material by cooling it into reduced iron. 7. Heading 1 B.

即ち、0.0’75mm以下の炭材微粒子は微細であシ
、■湿分存在下での大気中に放置した際、大気中の湿分
を容易′に、吸収すると共に■成形時スポンジ状還元鉄
と還元鉄間に存在し、これら還元鉄相互の粘着効果を抑
制する。一方・2・01m以上の炭材粗粒子は、粗大で
あシ、■成形時還元鉄内に均−分載せず、還元鉄ブリケ
ット内部に偏析して存在すると共に■成形特還元鉄相互
の粘着効果を抑制して犬さな楕度1強度低下を引き起す
In other words, carbonaceous particles with a diameter of 0.0'75 mm or less are fine, and when left in the atmosphere in the presence of moisture, they easily absorb moisture from the atmosphere and become spongy during molding. It exists between reduced irons and suppresses the mutual adhesion effect of these reduced irons. On the other hand, carbonaceous coarse particles with a diameter of 2.01 m or more are coarse, and are not placed evenly on the reduced iron during molding, and are segregated inside the reduced iron briquette, and also adhere to each other during forming. Suppresses the effect and causes a decrease in dog ellipticity 1 strength.

このように0.075mm以下及び2−0 +lI#1
以上の炭材は還元鉄ブリケットの強度、密度面で好筐し
くないことが明ら刀)となったので本発明者等は0.0
75+1il11〜2・O咽粒度の存在割合と還元鉄ブ
リケントの密度並びに強度の関恍ン調肴した結釆、第3
図遍ひに第4図に示す如く、C1,O、’75 +Ir
111〜2.0IIIIn150〜90yoの炭材を採
用した時に還元鉄ブリケットの密度差ひ強度を蚊も筒く
維持できること〃・判明した。そこで本発明では、炭材
の粒度構成を0.075翫〜2−0 +nm + 50
〜90%に限定するものである。
In this way, 0.075mm or less and 2-0 +lI#1
It is clear that the above carbon materials are not suitable for reduced iron briquettes in terms of strength and density.
75+1il11~2・O ratio of pharyngeal grain size and density and strength of reduced iron briquent, 3rd
As shown in Figure 4, C1, O, '75 +Ir
It has been found that when a carbon material of 111-2.0IIIn150-90yo is used, the density difference strength of reduced iron briquettes can be maintained even against mosquitoes. Therefore, in the present invention, the particle size structure of the carbon material is set to 0.075 to 2-0 + nm + 50
It is limited to ~90%.

m 3v及び第2図から明らかなように本発明の如< 
00 ’75wn〜2.O+++m 、 50〜90%
の炭材を用いぬことにより密度低下を最少にして、前記
還元エネルギーの浪費を極少におさえることができる。
As is clear from m 3v and FIG.
00'75wn~2. O+++m, 50-90%
By not using carbonaceous materials, the decrease in density can be minimized and the waste of the reduction energy can be minimized.

lた第4図から明らかなように強度低下を極少にして前
記搬送歩留低下或は前記溶解プロセスの経済性低下を極
小におさえることができる。
As is clear from FIG. 4, it is possible to minimize the decrease in strength, thereby minimizing the decrease in the conveyance yield or the economic efficiency of the melting process.

ところで炭材中の水分は、]記の如く高温スポンジ状還
元鉄と容易V(反応し水素、メタン等の発生及び還元鉄
、P+ば化の原因となる。
By the way, the moisture in the carbonaceous material easily reacts with the high-temperature spongy reduced iron as described below, causing the generation of hydrogen, methane, etc., and the formation of reduced iron and P+.

H20+C→CO+H2・ ・ ・・ ・ ・ ・(1
)2H20+2C→2CO十〇H4−・−(21H20
+Fe+FeO+)12・・・・・・(3)なお(11
、(21式中(1)’Cば・SI温スポンジ状還元鉄中
の言有炭素並びに遊離炭素及び炭材中の炭素である。
H20+C→CO+H2・・・・・・・(1
)2H20+2C→2CO10H4-・-(21H20
+Fe+FeO+)12...(3) Note that (11
, (in formula 21, (1)'C is the stated carbon in the warm spongy reduced iron, the free carbon, and the carbon in the carbonaceous material.

圧縮成形装置の周辺算囲気は大気であシ、この装置内で
発生した水累、−酸化炭素、メタンは周辺界囲気のを気
を吸い込んで、装置内での異常燃焼、異常爆発の原因と
なると共に炭材水分は、高温スポンジ状還元鉄と反応し
再版化の原因となり先に述べた還元エイ・ルギーの浪費
を結果的に招く。
The ambient air around the compression molding equipment is the atmosphere, and water accumulation, carbon oxide, and methane generated within this equipment can be sucked into the surrounding air and cause abnormal combustion or explosions within the equipment. At the same time, the moisture content of the carbonaceous material reacts with the high-temperature sponge-like reduced iron, causing reprinting and resulting in the waste of reduced iron as mentioned above.

そこで本発明者等は、炭材中の水分と含、有水分による
高温スポンジ状還元鉄の書酸化性及び反応に伴なう発生
ガスとの関係を第1図の加炭成形プロセスで調査したと
ころ・第5図に示す如く炭材中水分2%會現に著しく異
なり、炭材中水分を2Z以下にすることが前bピ加炭成
形プロセスの経済上、安全上、効果的であることが明ら
かとなった。
Therefore, the present inventors investigated the relationship between the water content in the carbon material, the oxidation property of high-temperature sponge-like reduced iron due to water content, and the gas generated during the reaction using the carburization process shown in Figure 1. However, as shown in Figure 5, the moisture content in the carbonaceous material is significantly different from the 2% condition, and it is found that reducing the moisture content in the carbonaceous material to 2Z or less is effective from the economic and safety standpoints of the carburization process. It became clear.

ヤこで本兜明では、炭材水分を2.7.以下に駆足する
ものである。
At Yakode Honkamei, the charcoal material moisture content is 2.7. The following is a quick guide.

なお第3〜5図から炭材隙7JLl叢は、3%葡越え) ると還元鉄ブリケットの密度2強度及び圧縮成形時の再
酸化並ひ16反比、ガス発生量が著しく劣化並びに増加
する傾向にあり、加炭量は3′X;以内にととめるのか
奸才し、いとともわかる。更になお第3゜4図の結果は
、炭材銘柄、コークス粉、炭材中水分:lO%一定、筒
温還元鉄粒度指成;’700℃。
Furthermore, from Figures 3 to 5, when the carbon gap 7JLl mass exceeds 3%), the density 2 strength of reduced iron briquettes, the reoxidation during compression molding, and the 16 inverse ratio, the gas generation rate tends to significantly deteriorate and increase. It is clear that the amount of carburization can be kept within 3'X. Furthermore, the results shown in Figure 3-4 are carbon material brand, coke powder, moisture content in carbon material: constant 1O%, cylinder temperature reduced iron particle size specification: '700°C.

3〜301111n 90%  3+閘10%、圧縮欣
形、並びIs加炭条件;第1図のプロセスで圧縮成形条
件一定。
3 to 301111n 90% 3+lock 10%, compression cylindrical shape, arrangement Is carburization conditions; Compression molding conditions constant in the process shown in FIG.

加炭条件は加炭鴬一定の諸条件下で得たものであゐ0 壕だ第5図の結果は、第3,4図(D実施条件で炭材粒
度条件i0.0 ’75nbn−20+質+ 70%に
固だしたものである。また炭材銘柄ケカーホンブラソク
、黒鉛V’−に史しても第3,4.5図と同様な結果と
なった。
The carburizing conditions are those obtained under certain conditions. The results were also the same as those shown in Figures 3 and 4.5 for the carbonaceous materials Kekahon Blasok and graphite V'-.

実施例 3 T/H(1)製造能力を視し炭材供給装置r備えた
第1図の圧縮成形装置に2いて’700℃の3〜30■
 90%、−311ag以下10%の高温スポンジ状還
元鉄に炭材71%硝加して加炭還元鉄ブリケット(サイ
ズ40CC)を製造すljmして炭材として粒度構成0
.0’75n而〜2.0?#172%、水分1.3%の
粉コークスを用いて製造した。
Example 3 T/H (1) In view of manufacturing capacity, the compression molding apparatus shown in Fig. 1 equipped with a carbonaceous material supply device was heated at 700°C for 3 to 30 seconds.
Carbonized reduced iron briquettes (size 40CC) are produced by adding 71% carbon material to high-temperature sponge-like reduced iron of 90%, -311ag or less and 10%.
.. 0'75n~2.0? It was produced using coke powder with #172% and moisture content of 1.3%.

その結果を第1衣に示す。The results are shown in Figure 1.

比較例 実施例における実施条件の内、炭材として粒度構成0.
0 ’i’ 5 mm〜2.0 +rm 20%、水分
35%の粉コークスを用いて製造した結果ケ第1表に併
記した0 第1表
Comparative Example Among the implementation conditions in the example, the particle size structure is 0.
0 'i' 5 mm ~ 2.0 +rm Results of manufacturing using coke powder with 20% and 35% moisture 0 Table 1

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

第1図は還元鉄の圧縮成形装置例の説明図、第2〜5図
は本発明法の説明図で、第3及び4図は炭材粒度構成と
還元鉄ブリケットの密度及び強度(タンブラ−試験法に
おける一3711111粉元生率%」との関係図、第2
図は還元鉄ブリケットの密度と再酸化との関係図、第5
図は炭材中の水分?圧縮成形時の鴇酸化2反応元生ガス
量との関係図である1、 1・・・・ ・・コンテナ 2・・ ・・・・・圧縮成形装置 3・・・・ ・・貯蔵ヒン 4・・・・・・・フィダー 5 ・・・・ ・・成形ロール 6・・・ ・・・・分離機 7・  ・・  ・・振動コンヘアー 8・・ ・・・・・冷却水幅 9・・・・・・・搬送コンヘアー 10  ・・・・・炭材供給装置 11・・・・ ・ホッパー 12・・・・・ ・コンスタントフィーダー13・・・
・・・スクリューコンベアー14  ・ ・・ ・ ・
シュート 化 願 人 新日本製鐵株式公社
Fig. 1 is an explanatory diagram of an example of compression molding equipment for reduced iron, Figs. 2 to 5 are explanatory diagrams of the method of the present invention, and Figs. Relationship diagram with “13711111 Flour Original Viability %” in the test method, 2nd
Figure 5 shows the relationship between the density of reduced iron briquettes and reoxidation.
Is the diagram moisture in the charcoal material? 1. Container 2. Compression molding device 3. Storage hinge 4. ... Feeder 5 ... Forming roll 6 ... Separator 7 ... Vibrating conhair 8 ... ... Cooling water width 9 ... ... Conveyor conveyor 10 ... Carbon material supply device 11 ... - Hopper 12 ... - Constant feeder 13 ...
・・・Screw conveyor 14 ・ ・ ・ ・
Request for chute Nippon Steel Corporation

Claims (1)

【特許請求の範囲】[Claims] スポンジ状の還元鉄を圧縮成形装置のフィダーに供給す
るときに、微細な炭材を炭材供給装置により上記フィー
ダーに供給して上記還元鉄に添加したのち、この還元鉄
を圧縮成型装置の成型ロールにより成形する還元鉄ブリ
ケットの製造方法において、650℃以上の筒温、スポ
ンジ状の3〜30mJn8o%以上−3咽20%以下の
還元鉄に、粒[0、O75+rui〜20jmn 、 
5 o〜90%で、かつ含南水分2′A)以下の炭桐を
添加することを特徴とする還元鉄ブリケットの製造方法
When feeding sponge-like reduced iron to the feeder of a compression molding device, fine carbonaceous material is supplied to the feeder by the carbon material supply device and added to the reduced iron, and then this reduced iron is molded into the compression molding device. In the method for producing reduced iron briquettes formed by rolls, the cylinder temperature is 650°C or higher, and the sponge-like reduced iron of 3 to 30 mJn8o% or more - 30mJn 20% or less is mixed with grains [0, O75 + rui ~ 20jmn,
5. A method for producing reduced iron briquettes, characterized by adding charcoal paulownia with a content of 90% to 90% and a moisture content of 2'A) or less.
JP4363083A 1983-03-16 1983-03-16 Production of reduced iron briquette Pending JPS59170212A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4363083A JPS59170212A (en) 1983-03-16 1983-03-16 Production of reduced iron briquette

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4363083A JPS59170212A (en) 1983-03-16 1983-03-16 Production of reduced iron briquette

Publications (1)

Publication Number Publication Date
JPS59170212A true JPS59170212A (en) 1984-09-26

Family

ID=12669173

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4363083A Pending JPS59170212A (en) 1983-03-16 1983-03-16 Production of reduced iron briquette

Country Status (1)

Country Link
JP (1) JPS59170212A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006004350A1 (en) * 2004-06-30 2006-01-12 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
WO2006006820A1 (en) * 2004-07-12 2006-01-19 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
WO2006009371A1 (en) * 2004-07-16 2006-01-26 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same.
KR101036640B1 (en) * 2004-07-12 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036643B1 (en) * 2004-07-30 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted iron of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036646B1 (en) * 2004-07-16 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036638B1 (en) * 2004-07-12 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036639B1 (en) * 2004-07-16 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted iron of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006004350A1 (en) * 2004-06-30 2006-01-12 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
WO2006006820A1 (en) * 2004-07-12 2006-01-19 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
AU2005263068B2 (en) * 2004-07-12 2008-10-30 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
US7588717B2 (en) 2004-07-12 2009-09-15 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same
KR101036640B1 (en) * 2004-07-12 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036638B1 (en) * 2004-07-12 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
WO2006009371A1 (en) * 2004-07-16 2006-01-26 Posco Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same.
KR101036645B1 (en) * 2004-07-16 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036646B1 (en) * 2004-07-16 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036639B1 (en) * 2004-07-16 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted iron of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same
KR101036643B1 (en) * 2004-07-30 2011-05-24 주식회사 포스코 An apparatus for manufacturing compacted iron of reduced materials comprising fine direct reduced irons and an apparatus for manufacturing molten irons using the same

Similar Documents

Publication Publication Date Title
TW562860B (en) Method for producing reduced iron
WO2006046606A1 (en) Process for producing molten iron and apparatus therefor
US5730775A (en) Method for rapid reduction of iron oxide in a rotary hearth furnace
US5885521A (en) Apparatus for rapid reduction of iron oxide in a rotary hearth furnace
WO2012002338A1 (en) Process for producing molten steel using particulate metallic iron
US3244507A (en) Method of indurating ore particles
US8277536B2 (en) Process for producing molten iron and apparatus for producing molten iron
US8101007B2 (en) Method for reduction treatment of electric furnace dust
JPS59170212A (en) Production of reduced iron briquette
JP3304872B2 (en) Method and apparatus for rapid reduction of iron oxide in rotary hearth heating furnace
RU2278167C2 (en) Method for production of iron metal
US6451085B1 (en) Method for producing reduced iron
US20160237514A1 (en) Method for manufacturing iron nuggets
JP4976701B2 (en) Molten iron manufacturing method and molten iron manufacturing apparatus
TW486559B (en) Method and apparatus for charging raw and carbonaceous materials into a moving hearth furnace
JP4893347B2 (en) Operation method of mobile hearth furnace
JP2014227582A (en) Method for producing agglomerated raw material for blast furnace
US891705A (en) Method of treating ore.
US3144413A (en) Calcium carbide manufacture
JPS63128127A (en) Manufacture of sintered ore
KR101677409B1 (en) Method and equipment for hot compacting iron recycling by-product emitted from coal-based iron making process
JP4935384B2 (en) Method for producing reduced metal
JPS59170213A (en) Production of reduced iron briquette
KR20160063433A (en) Manufacturing method of reduced iron, the manufacturing apparatus thereof and the reduced ion using the same
TW202239974A (en) Operating method for reducing furnace