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JPS6014803B2 - Quality control method of reduced iron in floating reduction process - Google Patents
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JPS6014803B2 - Quality control method of reduced iron in floating reduction process - Google Patents

Quality control method of reduced iron in floating reduction process

Info

Publication number
JPS6014803B2
JPS6014803B2 JP8381878A JP8381878A JPS6014803B2 JP S6014803 B2 JPS6014803 B2 JP S6014803B2 JP 8381878 A JP8381878 A JP 8381878A JP 8381878 A JP8381878 A JP 8381878A JP S6014803 B2 JPS6014803 B2 JP S6014803B2
Authority
JP
Japan
Prior art keywords
reduced iron
iron
floating
reduction process
reduction
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
Application number
JP8381878A
Other languages
Japanese (ja)
Other versions
JPS5511161A (en
Inventor
信 清水
幸長 片橋
徹男 堀江
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries 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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP8381878A priority Critical patent/JPS6014803B2/en
Publication of JPS5511161A publication Critical patent/JPS5511161A/en
Publication of JPS6014803B2 publication Critical patent/JPS6014803B2/en
Expired legal-status Critical Current

Links

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  • Manufacture Of Iron (AREA)

Description

【発明の詳細な説明】 本発明は浮遊式還元プロセスにおいて還元鉄の品質すな
わち金属化率又は還元率等を一定の状態に保持する制御
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control method for maintaining the quality of reduced iron, that is, the metallization rate or reduction rate, etc., in a constant state in a floating reduction process.

近年、塔内に加熱雰囲気を形成し、この雰囲気中に炭素
粒体ないし粉体を導入して炭素の浮遊層を形成し、該浮
遊層内に酸化鉄原材料を通過させて該浮遊層の一酸化炭
素あるいは水素などによる還元性ガス雰囲気により前記
酸化鉄原材料を還元しつつ、この還元反応によって生成
される二酸化炭素や水蒸気と炭素粒体とを反応させて一
酸化炭素や水素の還元性雰囲気を生成させ、還元効率を
可及的に高めることのできる浮遊式還元プロセスが注目
をあびている。
In recent years, a heated atmosphere is formed in the tower, carbon particles or powder are introduced into this atmosphere to form a carbon floating layer, and an iron oxide raw material is passed through the floating layer to form a part of the floating layer. While reducing the iron oxide raw material in a reducing gas atmosphere of carbon oxide or hydrogen, the carbon particles and carbon particles generated by this reduction reaction are reacted to create a reducing atmosphere of carbon monoxide and hydrogen. A floating reduction process that can generate hydrogen and increase the reduction efficiency as much as possible is attracting attention.

しかるに浮遊式還元プロセスにおいては、常に一定品質
の還元鉄を生産するためには、■ 浮遊層内で充分な還
元ガスの発生があること、■ 浮遊層内で酸化鉄が充分
還元されていること、の一つの条件を満足することが必
要であるが、■ 浮遊層を生成する徴粉炭がコークス化
しガス化することによる消耗、@ 徴粉炭種類の相違に
よる組成の変化、■ 原料鉱石の相違による該原料鉱石
の還元難易度の変化、等の操業条件の変化により、前記
二つの条件を満足することができず、還元鉄の金属化率
又は還元率を一定に保持することができなくなるおそれ
がある。
However, in the floating reduction process, in order to always produce reduced iron of a constant quality, it is necessary to: ■ ensure that sufficient reducing gas is generated within the floating layer, and ■ ensure that iron oxide is sufficiently reduced within the suspended layer. It is necessary to satisfy one of the following conditions: ■ Depletion due to coke and gasification of the fine coal that forms the floating layer, @ Changes in composition due to differences in the type of fine coal, ■ Due to differences in raw material ores. Due to changes in operating conditions such as changes in the difficulty of reduction of the raw material ore, the above two conditions may not be satisfied and the metallization rate or reduction rate of reduced iron may not be able to be maintained constant. be.

本発明は、操業条件が変化してもこれに追従し、生産さ
れる還元鉄の金属化率又は還元率を一定に保持すること
を目的としてなしたもので、徴粉炭、チャー、コークス
等の炭村のうちの任意のひとつ若しくはいくつかで形成
される炭素の浮遊層に鉄鉱石を投入して還元する浮遊式
還元プロセスにおいて、炭材及び鉄鉱石を個々に供給し
得る様にし、製品として取出された還元鉄の酸素量若し
くは還元率あるいは金属化率又な比重のごとき還元鉄特
性を検出し、該還元鉄特性が一定となるよう鉄鉱石と炭
材の供給比率を制御することを特徴とするものである。
The present invention was made for the purpose of keeping the metallization rate or reduction rate of the produced reduced iron constant even if the operating conditions change. In the floating reduction process, in which iron ore is introduced into a floating layer of carbon formed in one or more of the coal villages, carbonaceous material and iron ore can be supplied individually, and as a product. It is characterized by detecting the reduced iron characteristics such as the amount of oxygen, reduction rate, metallization rate, or specific gravity of the extracted reduced iron, and controlling the supply ratio of iron ore and carbonaceous material so that the reduced iron characteristics are constant. That is.

以下本発明の実施例を図面を参照しつつ説明する。内部
に徴粉炭等による浮遊層を形成するようにした反応塔1
の下部側方には、送風機2によって昇圧され加熱器3に
よって加熱されたプロセスガスを該反応塔1内に送給す
るプロセスガス供V給管4が取付けられており、反応塔
1下面には、チヤーやコークスのごとき流動粒子と還元
鉄とを分離し流動粒子5と還元鉄6とを分けて取出し得
るようにした分離機7が設けられている。
Embodiments of the present invention will be described below with reference to the drawings. Reaction tower 1 in which a suspended layer of pulverized coal, etc. is formed inside.
A process gas supply V supply pipe 4 is attached to the lower side of the reaction tower 1 for feeding the process gas, which has been pressurized by the blower 2 and heated by the heater 3, into the reaction tower 1. A separator 7 is provided which separates fluid particles such as char or coke from reduced iron, and allows fluid particles 5 and reduced iron 6 to be taken out separately.

又還元鉄6の取出し経路8には還元鉄6内の酸素の分析
計9が取付けられている。反応塔1の上部には、プロセ
ス排ガス排出管10が設けられており、該プロセス排ガ
ス排出管10の中途部にはダスト除去及び薄霞熱利用の
ためのベンチュリースクラバー兼クーラー11が接続さ
れている。
Further, an analyzer 9 for oxygen in the reduced iron 6 is attached to the extraction route 8 for the reduced iron 6. A process exhaust gas discharge pipe 10 is provided at the top of the reaction tower 1, and a venturi scrubber/cooler 11 is connected to the midway part of the process exhaust gas discharge pipe 10 for dust removal and thin haze heat utilization. .

反応塔1の上部には、途中から二股に分れたシュート1
2が取付けられており、該シュ−ト12の二股部の一方
にはスクリューフイーダー13が、又他方にはスクリュ
ーフイーダー14が取付けられている。
At the top of the reaction tower 1, there is a chute 1 that splits into two from the middle.
A screw feeder 13 is attached to one of the bifurcated portions of the chute 12, and a screw feeder 14 is attached to the other.

更にスクリューフィーダー13上には鉄鉱石ホツパー1
5が、スクリューフイーダー14上には徴粉炭ホッパー
16が夫々配設されている。スクリューフィーダー13
,14の駆動用モーター17,18は、比率設定器19
,20に連接されており、該比率設定器19,20は、
何れも分析計9にインターロックされている。
Furthermore, an iron ore hopper 1 is placed on the screw feeder 13.
A fine coal hopper 16 is disposed on the screw feeder 14, respectively. Screw feeder 13
, 14 drive motors 17, 18 are connected to a ratio setting device 19.
, 20, and the ratio setters 19, 20 are connected to
Both are interlocked with analyzer 9.

運転に際しては、予め実験により分離機7より取出され
た還元鉄6中の酸素が何%の時は鉄鉱石の重量と徴粉炭
の重量との比率ご=霧鯵雲をどの位にするかを求めてお
き、これを比率設定器19,20に夫々設定しておく。
During operation, it is determined in advance by experiment what percentage of oxygen is in the reduced iron 6 taken out from the separator 7, and what percentage of the weight of the iron ore and the weight of the powdered coal should be. This is determined in advance and set in the ratio setters 19 and 20, respectively.

昇庄され加熱されたプロセスガスをプロセスガス供給管
4から反応塔1内に供給すると共にスクリューフィーダ
ー14から徴粉炭を、又スクリューフイーダー13から
鉄鉱石を、夫々反応塔1内に供V給すれば、反応塔1内
には徴粉炭等の浮遊層が形成され、鉄鉱石プロセスガス
により還元されて還元鉄となり、反応塔1から分離機7
に入り、ここで還元鉄と流動粒子とが分離され、還元鉄
6は取出し経路8を通って外部に取出され、流動粒子5
は反応塔1に送られ再使用される。プロセスガスは鉄鉱
石を還元することにより酸化されるが、徴粉炭の浮遊層
中を上昇する間に再び還元されて還元ガスとなり、プロ
セスガス排出管10中へプロセス排ガスとして排出され
、ベンチュリースクラバー兼クーラー11でダストの除
去及び顕彰熱の回収が行われ、しかる後昇圧、加熱され
プロセスガスとしてプロセスガス供給管4より反応繁1
に循環供聯合される。
The heated and elevated process gas is supplied into the reaction tower 1 from the process gas supply pipe 4, and pulverized coal is supplied from the screw feeder 14, and iron ore is supplied from the screw feeder 13 into the reaction tower 1, respectively. As a result, a suspended layer of powdered coal is formed in the reaction tower 1, which is reduced by the iron ore process gas to become reduced iron, which is then transferred from the reaction tower 1 to the separator 7.
The reduced iron and the fluidized particles are separated here, and the reduced iron 6 is taken out to the outside through the extraction path 8, and the fluidized particles 5
is sent to reaction column 1 and reused. The process gas is oxidized by reducing the iron ore, but as it rises through the floating layer of pulverized coal, it is reduced again and becomes a reducing gas, which is discharged into the process gas discharge pipe 10 as process exhaust gas, which serves as a venturi scrubber. The dust is removed and the residual heat is recovered in the cooler 11, and then the pressure is increased, the heat is heated, and the process gas is supplied to the process gas supply pipe 4 for reaction.
are combined in circulation.

取出し経路8を通る還元鉄はその一部が分析計9にサン
プリングされ、化学分析されて還元鉄中の酸素量が検出
される。
A portion of the reduced iron passing through the extraction path 8 is sampled by an analyzer 9 and chemically analyzed to detect the amount of oxygen in the reduced iron.

分析された酸素の量が所定の値より大きい時は還元鉄の
還元の度合いが不充分である。
When the amount of oxygen analyzed is greater than a predetermined value, the degree of reduction of reduced iron is insufficient.

従ってこの場合にはご=鯵鱗雲の値を4・ごくするよう
、すなわち徴粉炭の量を増すか鉄鉱石の量を減少するよ
う、比率設定器20,19からの信号を受けてスクリュ
ーフィーダー14,13の供給量が変り、還元鉄の酸素
量が一定となるよう制御される。又分析計9で分析され
た酸素量が所定の値より少ない時は還元鉄の還元が充分
すぎるから、この場合にはどの値が大きくなるよう鉄鉱
石の量を増すかあるいは徴粉炭の量を減少するよう、ス
クリューフイーダー13,14の供給量の調整やが行わ
れる。なお本発明の実施例においては、還元鉄中の酸素
を分析する場合について説明したが、還元率や金属化率
や比重等還元鉄特性を把握できるものなら、いかなるも
のによっても金属化率又は還元率を一定に保持するよう
な制御を行い得ること、分析計と比率設定器との間にコ
ンピューターを設置すれば、精度の高い制御を行い得る
こと、その他本発明の要旨を逸脱しない範囲内で種々変
更を加え得ること、等は勿論である。
Therefore, in this case, the screw feeder 14 receives signals from the ratio setters 20 and 19 to reduce the value of 4.0, that is, to increase the amount of powdered coal or decrease the amount of iron ore. , 13 is changed, and the amount of oxygen in the reduced iron is controlled to be constant. Also, when the amount of oxygen analyzed by the analyzer 9 is less than the predetermined value, the reduction of reduced iron is sufficient, so in this case, it is necessary to increase the amount of iron ore or the amount of powdered coal to increase the value. The supply amount of the screw feeders 13 and 14 is adjusted so as to decrease the amount. In the embodiments of the present invention, the case where oxygen in reduced iron is analyzed has been explained, but any method can be used to analyze reduced iron characteristics such as reduction rate, metallization rate, specific gravity, etc. It is possible to perform control to keep the ratio constant, and if a computer is installed between the analyzer and the ratio setting device, highly accurate control can be performed, and other aspects that do not depart from the gist of the present invention. Of course, various changes may be made.

本発明の浮遊式還元プロセスにおける還元鉄の品質制御
方法は、上述のごとき構成であるから、還元鉄の金属化
率又は還元率を一定の状態に制御できるという効果を奏
し得る。
Since the method for controlling the quality of reduced iron in a floating reduction process of the present invention has the above-described configuration, it can produce the effect that the metallization rate or reduction rate of reduced iron can be controlled to a constant state.

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

図面は本発明の説明図である。 図中1は反応塔、4はプロセスガス供給管、6は還元鉄
、7は分離機、8は取出し経路、9は分析計、13,1
4はスクリューフィーダー、19,2川ま比率設定器を
示す。
The drawings are explanatory diagrams of the present invention. In the figure, 1 is a reaction tower, 4 is a process gas supply pipe, 6 is reduced iron, 7 is a separator, 8 is an extraction route, 9 is an analyzer, 13,1
4 shows a screw feeder, 19.2 shows a ratio setting device.

Claims (1)

【特許請求の範囲】[Claims] 1 微粉炭、チヤー、コークス等の炭材のうちの任意の
ひとつ若しくはいくつかで形成される炭素の浮遊層に鉄
鉱石を投入して還元する浮遊式還元プロセスにおいて、
炭材及び鉄鉱石を個々に供給し得る様にし、製品として
取出された還元鉄の酸素量若しくは還元率あるいは金属
化率又は比重のごとき還元鉄特性を検出し、該還元鉄特
性が一定となるよう鉄鉱石と炭材の供給比率を制御する
ことを特徴とする還元鉄の品質制御方法。
1. In a floating reduction process in which iron ore is introduced into a carbon floating layer formed by any one or some of carbon materials such as pulverized coal, char, and coke,
Carbon material and iron ore can be supplied individually, and reduced iron characteristics such as oxygen content, reduction rate, metallization rate, or specific gravity of reduced iron extracted as a product are detected, and the reduced iron characteristics are kept constant. A method for controlling the quality of reduced iron, characterized by controlling the supply ratio of iron ore and carbonaceous material.
JP8381878A 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process Expired JPS6014803B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8381878A JPS6014803B2 (en) 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8381878A JPS6014803B2 (en) 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process

Publications (2)

Publication Number Publication Date
JPS5511161A JPS5511161A (en) 1980-01-25
JPS6014803B2 true JPS6014803B2 (en) 1985-04-16

Family

ID=13813256

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8381878A Expired JPS6014803B2 (en) 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process

Country Status (1)

Country Link
JP (1) JPS6014803B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103143448B (en) * 2013-04-03 2014-05-07 张京三 Method for extracting float coal, ferrous sulfide and kaoline from gangue through flotation

Also Published As

Publication number Publication date
JPS5511161A (en) 1980-01-25

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