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JPS6014802B2 - Quality control method of reduced iron in floating reduction process - Google Patents
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JPS6014802B2 - 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
JPS6014802B2
JPS6014802B2 JP8381778A JP8381778A JPS6014802B2 JP S6014802 B2 JPS6014802 B2 JP S6014802B2 JP 8381778 A JP8381778 A JP 8381778A JP 8381778 A JP8381778 A JP 8381778A JP S6014802 B2 JPS6014802 B2 JP S6014802B2
Authority
JP
Japan
Prior art keywords
exhaust gas
reduced iron
iron ore
floating
iron
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
JP8381778A
Other languages
Japanese (ja)
Other versions
JPS5511160A (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 JP8381778A priority Critical patent/JPS6014802B2/en
Publication of JPS5511160A publication Critical patent/JPS5511160A/en
Publication of JPS6014802B2 publication Critical patent/JPS6014802B2/en
Expired legal-status Critical Current

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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 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の還元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
二酸化炭素あるいは水蒸気と炭素粒体とを反応させて一
酸化炭素や水素濃度の高い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
スが注目をあぴている。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、更に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、
還元鉄の品質を一定に保持することができなくなるおそ
れがある。
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 such as carbon oxide or hydrogen, a reducing atmosphere with a high concentration of carbon monoxide or hydrogen is created by reacting carbon particles or carbon particles with carbon dioxide or water vapor generated by this reduction reaction. The floating reduction process is attracting attention because of its ability to generate and increase reduction efficiency as much as possible. However, in the floating reduction process, in order to always produce reduced iron of constant quality,
■ Sufficient reducing gas is generated within the floating layer, ■
It is necessary to satisfy one condition that the iron oxide is sufficiently reduced in the floating layer, but ■ consumption due to coke formation and further gasification of the pulverized coal that generates the floating layer, The above two conditions cannot be satisfied due to changes in operating conditions such as changes in composition due to differences in powdered coal types, changes in reduction difficulty due to differences in raw material ores, etc.
There is a possibility that the quality of reduced iron cannot be maintained constant.

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別に供給し
得る様にし、プロセス排ガス中の成分を分析し、該分析
値をもとに鉄鉱石量と炭材量の供孫舎比率を排ガス中の
成分が一定となるよう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 a floating reduction process in which iron ore is introduced into a floating layer of carbon formed by any one or some of the carbonaceous materials, the carbonaceous material and iron ore can be supplied separately, and the process exhaust gas is This system is characterized by analyzing the components in the exhaust gas and controlling the ratio of the amount of iron ore and the amount of carbonaceous materials based on the analyzed values so that the components in the exhaust gas remain constant.

以下本発明の実施例を図面を参照しつつ説明する。Embodiments of the present invention will be described below with reference to the drawings.

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総合管4が取付けられており、反
応塔下面には、チャ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。
A process gas whose pressure is increased by a blower 2 and heated by a heater 3 is fed into the reaction tower 1 at the lower side of the reaction tower 1 in which a suspended layer of pulverized coal or the like is formed inside. A supply pipe 4 is attached, and a separator 7 is installed at the bottom of the reaction tower, which separates fluidized particles such as char or coke from reduced iron, and allows fluidized particles 5 and reduced iron 6 to be taken out separately. It is provided.

反応塔1の上部には、プロセス排ガス排出管8が設けら
れており、該プロセス排ガス排出管8の中途部にはダス
ト除去及び銭熱利用のためのベンチュリースクラバー兼
クーラー9及びプロセス排ガスの成分を分析する成分分
析計10が取付けられている。
A process exhaust gas discharge pipe 8 is provided in the upper part of the reaction tower 1, and a venturi scrubber/cooler 9 for dust removal and heat utilization and a venturi scrubber/cooler 9 for dust removal and heat utilization are installed in the middle of the process exhaust gas discharge pipe 8. A component analyzer 10 for analysis is attached.

反応塔1の上部には、途中から二股に分れたシュート1
1が取付けられており、該シュート11の二股部の一方
にはスクリューフイーダー12が、又他方にはスクリュ
ーフィーダ−13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 12 is attached to one of the bifurcated portions of the chute 11, and a screw feeder 13 is attached to the other.

更にスクリューフイーダー12上には鉄鉱石ホツパー1
4が、スクリューフイーダー13上には徴粉炭ホッパー
15が夫々配設されている。スクリューフィーダー12
,13の駆動用モーター16,17は比率設定器18,
19に連接されており、該比率設定器18,19は、何
れも前記成分分析計101こインターロックされている
Furthermore, an iron ore hopper 1 is placed on the screw feeder 12.
4, fine coal hoppers 15 are disposed on the screw feeders 13, respectively. Screw feeder 12
, 13 drive motors 16, 17 are ratio setters 18,
The ratio setters 18 and 19 are both interlocked with the component analyzer 101.

運転に際しては予め実験等によりプロセス排ガス中の一
酸化炭素あるいは水素又はそれらの合計濃度が何%の時
は鉄鉱石の重量と徴粉炭の重量との比率ご:鯵譲雲をど
の位にするかを求めておき、これを比率設定器18,1
9に夫々設定しておく。昇圧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13から徴粉炭を、又スクリ
ューフィーダー12から鉄鉱石を反応塔1内に供給すれ
ば、反応塔1内には微粉炭等の浮遊層が形成され、鉄鉱
石は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、還元鉄は取出されるが、流動粒子は反応塔1
に送られ再使用される。
Before operation, determine in advance through experiments, etc., what percentage of carbon monoxide, hydrogen, or their total concentration is in the process exhaust gas, the ratio of the weight of iron ore to the weight of fine coal, and the ratio of the weight of iron ore to the weight of pulverized coal. is calculated in advance, and this is set in the ratio setter 18, 1.
Set each to 9. If pressurized and heated process gas is supplied into the reaction tower 1 from the process gas supply pipe 4, fine coal is supplied from the screw feeder 13, and iron ore is supplied from the screw feeder 12 into the reaction tower 1. A suspended layer of pulverized coal, etc. is formed inside the iron ore, and the iron ore is reduced by the process gas to become reduced iron, which enters the separator 7 from the reaction tower 1, where the reduced iron and fluidized particles are separated and reduced iron is produced. is taken out, but the fluidized particles are removed from the reaction column 1.
sent to and reused.

一方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、プロセス排ガス排出管8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9でダストの除去及び顕熱の回収が行われ、該プ
ロセス排ガスの一部は成分分析計101こ送られる一方
大部分は再び昇圧、加熱されプロセスガスとして前記プ
ロセスガス供給管4より反応塔1に循環供給される。成
分分析計10で分析されるガス成分が例えば一酸化炭素
の場合、プロセス排ガス中の一酸化炭素が所定の値より
多い時には、プロセス排ガスの還元の度合いが大きすぎ
る。
On the other hand, 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 exhaust gas exhaust pipe 8 as a process exhaust gas, and is passed through the venturi scrubber. Dust is removed and sensible heat is recovered in a cooler 9, and a portion of the process exhaust gas is sent to a component analyzer 101, while the majority is pressurized and heated again and reacts as a process gas through the process gas supply pipe 4. It is circulated and fed to the column 1. For example, when the gas component analyzed by the component analyzer 10 is carbon monoxide, when the amount of carbon monoxide in the process exhaust gas is more than a predetermined value, the degree of reduction of the process exhaust gas is too large.

従ってこの場合にはご=叢霧雲の値を大きくするよう、
すなわち鉄鉱石の量を増すか徴粉炭の量を減らすよう、
比率設定器18,19からの信号を受けてスクリュ−フ
ィーダ−12,13の供聯合量が変り、プロセス排ガス
の還元度が調整される。又一酸化炭素が所定の値より少
ない時には、プロセス排ガスが充分還元されていないの
で、この場合にはごの値が小さくなるよう徴粉炭の量を
増すか、あるいは鉄鉱石の量を減少するよう、スクリュ
ーフィーダ−12,13の供給量の調整が行われる。プ
ロセス排ガス中の二酸化炭素を分析する場合には、二酸
化炭素が所定の値より大きい時ごを減少するようにし、
二酸化炭素が所定の値より小さい時ごを増加するように
制御すればよい。
Therefore, in this case, increase the value of the cloud,
In other words, increase the amount of iron ore or reduce the amount of pulverized coal.
In response to signals from the ratio setters 18 and 19, the combined amount of the screw feeders 12 and 13 is changed, and the degree of reduction of the process exhaust gas is adjusted. Also, when carbon monoxide is less than a predetermined value, the process exhaust gas has not been reduced sufficiently, so in this case, the amount of pulverized coal should be increased or the amount of iron ore should be decreased so that the carbon monoxide value becomes smaller. The supply amount of the screw feeders 12 and 13 is adjusted. When analyzing carbon dioxide in process exhaust gas, reduce the times when carbon dioxide is higher than a predetermined value,
Control may be performed to increase the number of times when carbon dioxide is lower than a predetermined value.

なお本発明の実施例においては、ガス中の分析する成分
を一酸化炭素あるいは二酸化炭素とする場合について説
明したが、水素若しくは水蒸気を単独に分析しても実施
できること、一酸化炭素、二酸化炭素、水素、水蒸気を
任意に組合せても実施できること、精度の高い制御を行
うには成分分析計と比率設定器との間にコンピューター
を設置すればよいこと、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。
In the examples of the present invention, the case where the component to be analyzed in the gas is carbon monoxide or carbon dioxide has been explained, but it is also possible to analyze hydrogen or water vapor alone. It can be carried out using any combination of hydrogen and water vapor, and in order to perform highly accurate control, it is sufficient to install a computer between the component analyzer and the ratio setting device, within the scope of 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]

図は本発明の実施例の説明図である。 図中1は反応塔、4はプロセスガス供給管、6は還元鉄
、8はプロセス排ガス排出管、1川ま成分分析計、12
,13はスクリューフィーダー、18,19は比率設定
器を示す。
The figure is an explanatory diagram of an embodiment of the present invention. In the figure, 1 is a reaction tower, 4 is a process gas supply pipe, 6 is reduced iron, 8 is a process exhaust gas discharge pipe, 1 is a river component analyzer, 12
, 13 are screw feeders, and 18 and 19 are ratio setters.

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別に供給し得る様にし、プロセス排
ガス中の成分を分析し、該分析値をもとに鉄鉱石量と炭
材量の供給比率を排ガス中の成分が一定となるよう制御
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,
We made it possible to supply carbonaceous materials and iron ore separately, analyzed the components in the process exhaust gas, and based on the analysis values, adjusted the supply ratio of the amount of iron ore and the amount of carbonaceous materials so that the components in the exhaust gas remained constant. A method for controlling the quality of reduced iron.
JP8381778A 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process Expired JPS6014802B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8381778A JPS6014802B2 (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
JP8381778A JPS6014802B2 (en) 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process

Publications (2)

Publication Number Publication Date
JPS5511160A JPS5511160A (en) 1980-01-25
JPS6014802B2 true JPS6014802B2 (en) 1985-04-16

Family

ID=13813226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8381778A Expired JPS6014802B2 (en) 1978-07-10 1978-07-10 Quality control method of reduced iron in floating reduction process

Country Status (1)

Country Link
JP (1) JPS6014802B2 (en)

Also Published As

Publication number Publication date
JPS5511160A (en) 1980-01-25

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