JPH0892616A - Operation of coke packed bed type smelting reduction furnace - Google Patents

Operation of coke packed bed type smelting reduction furnace

Info

Publication number
JPH0892616A
JPH0892616A JP22679394A JP22679394A JPH0892616A JP H0892616 A JPH0892616 A JP H0892616A JP 22679394 A JP22679394 A JP 22679394A JP 22679394 A JP22679394 A JP 22679394A JP H0892616 A JPH0892616 A JP H0892616A
Authority
JP
Japan
Prior art keywords
furnace
charging pipe
pressure
coke
hopper
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.)
Granted
Application number
JP22679394A
Other languages
Japanese (ja)
Other versions
JP3273104B2 (en
Inventor
Tsuneya Hasegawa
恒也 長谷川
Yoichi Watanabe
洋一 渡辺
Kiyosuke Niko
精祐 児子
Takashi Ushijima
崇 牛島
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP22679394A priority Critical patent/JP3273104B2/en
Publication of JPH0892616A publication Critical patent/JPH0892616A/en
Application granted granted Critical
Publication of JP3273104B2 publication Critical patent/JP3273104B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE: To provide an operating method for assuring the long-time stable operation of a smelting reduction furnace by preventing the blow-by of in- furnace gases to the charging pipe hopper of the furnace, thereby preventing the deterioration of a sealing valve disposed in the charging pipe hopper. CONSTITUTION: The pressure P0 in the furnace 2 and the pressure PH in the charging pipe hopper 4 are respectively measured by pressure gages 6, 7 and the pressure difference ΔP therebetween is calculated and is compared with a pressure difference set value ΔP0 . The amt. of the gaseous N2 from a gaseous N2 supply source 8 into the charging pipe hopper 4 is controlled by automatically controlling a shut off valve 11 in such a manner that ΔP>=ΔP0 is attained. The caption number 3 denotes the charging pipe of coke 12 and the caption number 5 denotes the sealing valve to shut off the pressure in the furnace 2 and the atm.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は炉頂部にコークス装入用
の装入管を備えたコークス充填層型溶融還元炉の操業方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for operating a coke packed bed type smelting reduction furnace having a charging tube for charging coke at the top of the furnace.

【0002】[0002]

【従来の技術】一般に、コークス充填層型溶融還元炉に
おいては炉頂装入装置を介して炉内に装入される原料は
コークスのみであり、炉内温度が高くなると炉頂部にお
いては700から1000℃にも達する。本発明者等が
開示した特開平5−271734号公報の溶融還元炉
は、炉頂装入装置等の機器の保護のために、図1に示す
ように炉頂部から炉内2に突出させた装入管3を配設
し、装入管3の内部を常にコークス12で満たすように
構成し、コークス12のマテリアルシールによって炉内
2の高温ガスが炉頂装入装置、特に、装入管直上のホツ
パ4(以下装入管ホツパという)まで流れ込むのを防止
している。
2. Description of the Related Art Generally, in a coke packed bed type smelting reduction furnace, the only raw material to be charged into the furnace through a furnace top charging device is coke, and when the temperature in the furnace rises, the temperature from the top to 700 It reaches 1000 ° C. The smelting reduction furnace disclosed in Japanese Patent Application Laid-Open No. H5-271734 disclosed by the present inventors has been made to project from the furnace top into the furnace 2 as shown in FIG. 1 in order to protect the equipment such as the furnace top charging device. The charging pipe 3 is provided, and the inside of the charging pipe 3 is always filled with the coke 12. The high temperature gas in the furnace 2 is prevented by the material seal of the coke 12 from the furnace top charging device, especially the charging pipe. It is prevented from flowing into the hopper 4 directly above (hereinafter referred to as the charging pipe hopper).

【0003】図2は、図1の装入管ホツパ4に設けられ
たシール弁5の詳細説明図であり、高圧の炉内と大気と
の圧力遮断を行なっているが、特にシール弁5のシール
ゴム13の耐熱度が低いためシール弁5の保護が重要と
なる。なお、15は弁座、点線部分は弁体14が開の状
態を示す。
FIG. 2 is a detailed explanatory view of the seal valve 5 provided in the charging pipe hopper 4 of FIG. 1, and performs pressure shutoff between the high-pressure furnace and the atmosphere. Since the heat resistance of the seal rubber 13 is low, it is important to protect the seal valve 5. In addition, 15 shows a valve seat, and a dotted line shows a state in which the valve body 14 is open.

【0004】[0004]

【発明が解決しようとする課題】装入管に充満されたコ
ークスのマテリアルシールのみによって炉内の高温上昇
ガスが装入管ホツパへ流入するのを防止しようとする、
上述のような技術手段は次のような問題があった。
In order to prevent the high temperature rising gas in the furnace from flowing into the charging pipe hopper only by the material seal of the coke filled in the charging pipe,
The technical means as described above has the following problems.

【0005】1.コークスによるマテリアルシールは完
全ではなく、コークス粒の間隙を通って若干のガスの上
昇が存在する。 2.装入されたコークスが装入管内を降下する間にコー
クス中の水分が蒸発するので、特に炉内温度低下を目的
として炉内に散水する操業においては多量の蒸気が上記
ガスと供に上昇する。 3.炉内のコークス消費量が異常に速くなる場合には、
ガスの上昇が顕著となり、甚しい場合には装入管内のコ
ークスが空となり、炉内ガスが直接、装入管ホツパに流
れ込む。
1. The coke material seal is not perfect and there is some gas rise through the coke grain gap. 2. Since the water in the coke evaporates while the charged coke descends in the charging pipe, a large amount of steam rises together with the above gas especially in the operation of spraying water into the furnace for the purpose of lowering the temperature inside the furnace. . 3. If the coke consumption in the furnace becomes abnormally fast,
When the gas rises remarkably and the coke in the charging pipe becomes empty in the worst case, the gas in the furnace directly flows into the charging pipe hopper.

【0006】すなわち、上記のような問題点があるため
に、装入管ホツパ内が高温雰囲気になってシール弁のシ
ールゴムが損傷したり、蒸気の上昇によってシールゴム
にダストが付着し易くなり、この結果シール弁の漏れが
発生し、操業を不可能としていた。本発明は、上述した
問題を解決して炉内ガスが上昇して装入管ホツパ内に流
入するのを防止するコークス充填層型溶融還元炉の操業
方法を提供することを課題とするものである。
That is, because of the above problems, the inside of the charging pipe hopper is in a high temperature atmosphere and the seal rubber of the seal valve is damaged, or dust rises easily on the seal rubber due to the rise of steam. As a result, the seal valve leaked, making operation impossible. An object of the present invention is to provide a method for operating a coke packed bed smelting reduction furnace which solves the above-mentioned problems and prevents the gas in the furnace from rising and flowing into the charging pipe hopper. is there.

【0007】[0007]

【課題を解決するための手段】本発明は上述の問題を解
決するもので、コークスを装入管を介して炉頂から炉内
に装入するコークス充填層型溶融還元炉の操業方法に適
用され、次の方法を採った。すなわち、該装入管直上の
装入管ホッパ内の圧力(PH )および炉頂部の炉内の圧
力(PO )を連続的に測定してそれらの圧力差(ΔP=
H −PO )を演算し、予め設定した圧力差設定値をΔ
O (正数)としたとき、ΔP≧ΔPOとなるように該
装入管ホッパ内に不活性ガスを自動的に吹込むことを特
徴とするコークス充填層型溶融還元炉の操業方法であ
る。
The present invention solves the above problems and is applied to a method for operating a coke packed bed type smelting reduction furnace in which coke is charged into the furnace from the furnace top through a charging pipe. The following method was adopted. That is, the pressure (P H ) in the charging pipe hopper directly above the charging pipe and the pressure (P O ) in the furnace at the top of the furnace are continuously measured and their pressure difference (ΔP =
P H -P O) is calculated, and the pressure difference setting value Δ which is set in advance
A method for operating a coke packed bed smelting reduction furnace, characterized in that an inert gas is automatically blown into the charging pipe hopper so that ΔP ≧ ΔP O when P O (a positive number). is there.

【0008】[0008]

【作用】本発明の作用を図1により説明する。コークス
充填層型溶融還元炉1の炉頂部の炉内に突出して配設さ
れた装入管3直上の装入管ホッパ4内に、N2 ガス等の
不活性ガスを、N2 ガス供給源8、N2 ガス吹込配管
9、流量調節弁10、遮断弁11を介して連続して吹込
み、装入管ホッパ4内圧力を炉内2の圧力よりも高めに
保持するようにしたので、装入管ホッパ4内に吹込まれ
たN2 ガスが、装入管3を介して炉内2に流れ込むよう
になり、炉内ガスの上昇を防止することができる。
The operation of the present invention will be described with reference to FIG. The coke packed layer type smelting reduction furnace instrumentation pipe hopper 4 directly above instrumentation pipe 3 arranged to protrude to one of the furnace top portion of the furnace, an inert gas such as N 2 gas, N 2 gas supply source 8, the N 2 gas blowing pipe 9, the flow rate adjusting valve 10, and the shutoff valve 11 are continuously blown to keep the pressure inside the charging pipe hopper 4 higher than the pressure inside the furnace 2. The N 2 gas blown into the charging pipe hopper 4 flows into the furnace 2 via the charging pipe 3 and the rise of the furnace gas can be prevented.

【0009】また、何等かの異常によって、装入管3内
のコークスが空になり炉内2と装入管ホッパ4とが直接
連通されたとしても、圧力バランスにより、炉内ガスが
急激に装入管ホッパ4内に上昇することを防止すること
ができる。この結果、装入管ホッパ4の上部に配設した
シール弁5が高温にさらされることはなく、また、炉内
ガスとともに上昇してくる蒸気も遮断できるので、シー
ル弁5のシールゴムの損傷やシール弁5へのダスト付着
が防止でき、シール弁5のシール漏れをなくすることが
できる。
Even if the coke in the charging pipe 3 is emptied due to some abnormality and the furnace 2 and the charging pipe hopper 4 are directly communicated with each other, the pressure balance causes the gas in the furnace to rapidly rise. It is possible to prevent the rise into the charging pipe hopper 4. As a result, the seal valve 5 arranged above the charging pipe hopper 4 is not exposed to high temperatures, and the steam rising with the gas in the furnace can be blocked, so that the seal rubber of the seal valve 5 is not damaged or damaged. It is possible to prevent dust from adhering to the seal valve 5 and eliminate the seal leakage of the seal valve 5.

【0010】[0010]

【実施例】図1は本発明を好適に実施できる装置並びに
その制御フローの説明図である。炉内2と装入管ホッパ
4内には各々内部圧力を測定する圧力計6、7が設置さ
れそれぞれの圧力が連続的に測定される。装入管ホッパ
4には、N2 ガス等の不活性ガスの供給源8から配管さ
れた吹込配管9を接続し、吹込配管9の経路中に流量調
節弁10と遠隔操作できる遮断弁11が配設されてい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an explanatory view of an apparatus and its control flow in which the present invention can be suitably implemented. Inside the furnace 2 and the charging pipe hopper 4, pressure gauges 6 and 7 for measuring the internal pressure are installed, and the respective pressures are continuously measured. The charging pipe hopper 4 is connected to a blow pipe 9 connected from a supply source 8 of an inert gas such as N 2 gas, and a flow control valve 10 and a shut-off valve 11 which can be remotely operated are provided in a path of the blow pipe 9. It is arranged.

【0011】コークス充填層型溶融還元炉の操業におい
ては、炉内圧力計6で測定された炉内圧力PO と、装入
管ホッパ内圧力計で測定された装入管ホッパ内圧力PH
との圧力差ΔPを演算し、この圧力差ΔPと予め設定さ
れた圧力差設定値ΔPO との差を演算し、この結果に応
じて遮断弁11を開閉することによって、装入管ホッパ
内圧力PH を炉内圧力PO より若干高めに保持する。す
なわち、ΔP<ΔPO のときは、遮断弁11を開として
2 ガスを装入管ホッパ4内に吹込み、装入管ホッパ4
内の圧力を上昇させる。そして、ΔP≧ΔPO の状態に
なったら遮断弁11を閉としてN2 ガスの吹込を停止す
る。
[0011] In the operation of the coke packed layer type smelting reduction furnace, the furnace pressure is determined by the furnace pressure gauge 6 P O and, measured in instrumentation pipe hopper manometer the instrumentation pipe hopper pressure P H
By calculating the pressure difference ΔP between the pressure difference ΔP and the pressure difference setting value ΔP O set in advance and opening / closing the shutoff valve 11 according to the result. The pressure P H is kept slightly higher than the furnace pressure P O. That is, when ΔP <ΔP O , the shut-off valve 11 is opened and N 2 gas is blown into the charging pipe hopper 4 to make the charging pipe hopper 4
Increase the pressure inside. When ΔP ≧ ΔP O, the shutoff valve 11 is closed to stop blowing N 2 gas.

【0012】実操業においては、装入管ホッパ4内に吹
込まれたN2 ガスは装入管内に充満されたコークスの間
隙を通って炉内2に排出されるため遮断弁11はほぼ連
続して開状態となるが、装入管ホッパ4内の圧力が上昇
し過ぎるのを防止するためにΔPとΔPO との比較によ
る遮断弁11の開閉を行うべきである。また吹込みN 2
ガス量をできるだけ少量に押えるために流量調節弁10
を調整する。
In the actual operation, the blowing into the charging pipe hopper 4 is performed.
Embedded N2 Gas is in the charging coke while it is in the coke
Since it is discharged into the furnace 2 through the gap, the shut-off valve 11 is almost continuous.
The pressure in the charging pipe hopper 4 rises although it continues to open.
ΔP and ΔP to prevent overshootingO By comparison with
The shutoff valve 11 should be opened and closed. Also blow N 2 
Flow control valve 10 to keep the amount of gas as small as possible
Adjust.

【0013】本実施例においては、溶融還元炉の炉内容
積140m3 、出銑量140ton/day、炉頂(炉
頂部での炉内)圧力0.5kg/cm2 ・G、装入管ホ
ッパ内圧力と炉内圧力との差圧設定値ΔPO =0.1k
g/cm2 である。従来技術においては、操業3ケ月で
シール弁のシール漏れが発生し、その都度シールゴムの
交換を行なっていたが、本発明によれば、装入管ホッパ
内へのガスや蒸気の上昇は皆無となり、シール弁の損傷
もなくなり、シールゴムを交換することなく1年以上の
操業が可能となった。
In this embodiment, the internal volume of the smelting reduction furnace is 140 m 3 , the amount of tapping is 140 ton / day, the pressure at the top of the furnace (in the furnace at the top of the furnace) is 0.5 kg / cm 2 · G, and the charging pipe hopper is used. Differential pressure setting value between internal pressure and furnace pressure ΔP O = 0.1k
It is g / cm 2 . In the prior art, a seal leak occurred in the seal valve after three months of operation, and the seal rubber was replaced each time, but according to the present invention, there is no rise of gas or steam into the charging pipe hopper. , The seal valve is no longer damaged, and it has been possible to operate for over a year without replacing the seal rubber.

【0014】[0014]

【発明の効果】本発明によれば、コークス充填層型溶融
還元炉の長期安定操業が可能となり、生産性の向上並び
に設備維持管理費の節減に優れた効果を奏する。
According to the present invention, the coke packed bed type smelting reduction furnace can be stably operated for a long period of time, and it is excellent in improving productivity and reducing facility maintenance costs.

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

【図1】図1は本発明を好適に実施できる装置並びにそ
の制御フローの説明図である。
FIG. 1 is an explanatory diagram of an apparatus that can preferably implement the present invention and a control flow thereof.

【図2】図2は図1のシール弁の詳細説明図である。FIG. 2 is a detailed explanatory diagram of the seal valve of FIG.

【符号の説明】[Explanation of symbols]

1 溶融還元炉 2 炉内 3 装入管 4 装入管ホッパ 5 シール弁 6 炉内圧力計 7 装入管ホッパ圧力計 8 N2 ガス供給源 9 N2 ガス吹込配管 10 流量調節弁 11 遮断弁 12 コークス 13 シールゴム 14 弁体 15 弁座 PO …炉内圧力 PH …装入管ホッパ内圧力 ΔP…圧力差 ΔPO …圧力差設定値1 Smelting Reduction Furnace 2 Furnace 3 Charging Pipe 4 Charging Pipe Hopper 5 Seal Valve 6 Furnace Pressure Gauge 7 Charging Pipe Hopper Pressure Gauge 8 N 2 Gas Supply Source 9 N 2 Gas Injection Piping 10 Flow Control Valve 11 Shutoff Valve 12 coke 13 seal rubber 14 valve body 15 valve seat P O ... inner pressure P H ... instrumentation pipe hopper pressure [Delta] P ... pressure difference [Delta] P O ... pressure difference setpoint

───────────────────────────────────────────────────── フロントページの続き (72)発明者 児子 精祐 千葉市中央区川崎町1番地 川崎製鉄株式 会社千葉製鉄所内 (72)発明者 牛島 崇 千葉市中央区川崎町1番地 川崎製鉄株式 会社千葉製鉄所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Seisuke Kouko 1 Kawasaki-cho, Chuo-ku, Chiba-shi Inside the Kawasaki Steel Co., Ltd. (72) Inventor Takashi Ushijima 1 Kawasaki-cho, Chuo-ku, Chiba Kawasaki Steel Co., Ltd. Chiba Inside the steel mill

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 コークスを装入管を介して炉頂から炉内
に装入するコークス充填層型溶融還元炉の操業方法にお
いて、該装入管直上の装入管ホッパ内の圧力(PH )お
よび炉頂部の炉内の圧力(PO )を連続的に測定してそ
れらの圧力差(ΔP=PH −PO )を演算し、予め設定
した圧力差設定値をΔPO (正数)としたとき、ΔP≧
ΔPO となるように該装入管ホッパ内に不活性ガスを自
動的に吹込むことを特徴とするコークス充填層型溶融還
元炉の操業方法。
1. A method of operating a coke packed bed type smelting reduction furnace in which coke is charged into the furnace from the furnace top through a charging pipe, the pressure (P H in the charging pipe hopper immediately above the charging pipe. ) And the pressure (P O ) in the furnace at the top of the furnace are continuously measured, and the pressure difference (ΔP = P H −P O ) between them is calculated, and the preset pressure difference set value is ΔP O (a positive number). ), ΔP ≧
A method for operating a coke packed bed type smelting reduction furnace, characterized in that an inert gas is automatically blown into the charging pipe hopper so as to obtain ΔP O.
JP22679394A 1994-09-21 1994-09-21 Operation method of coke packed bed type smelting reduction furnace Expired - Fee Related JP3273104B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22679394A JP3273104B2 (en) 1994-09-21 1994-09-21 Operation method of coke packed bed type smelting reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22679394A JP3273104B2 (en) 1994-09-21 1994-09-21 Operation method of coke packed bed type smelting reduction furnace

Publications (2)

Publication Number Publication Date
JPH0892616A true JPH0892616A (en) 1996-04-09
JP3273104B2 JP3273104B2 (en) 2002-04-08

Family

ID=16850710

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22679394A Expired - Fee Related JP3273104B2 (en) 1994-09-21 1994-09-21 Operation method of coke packed bed type smelting reduction furnace

Country Status (1)

Country Link
JP (1) JP3273104B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030038922A (en) * 2001-11-07 2003-05-17 주식회사 포스코 Cokes input control apparatus in blast furnace
KR100398408B1 (en) * 1999-12-28 2003-09-19 주식회사 포스코 Apparatus for controlling pressure in hopper of blast furnace
KR100793578B1 (en) * 2001-12-20 2008-01-14 주식회사 포스코 Apparatus for press controlling of hopper of blast furnace
KR100805052B1 (en) * 2001-11-06 2008-02-20 주식회사 포스코 Apparatus for controlling pressure of hopper in blast furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100398408B1 (en) * 1999-12-28 2003-09-19 주식회사 포스코 Apparatus for controlling pressure in hopper of blast furnace
KR100805052B1 (en) * 2001-11-06 2008-02-20 주식회사 포스코 Apparatus for controlling pressure of hopper in blast furnace
KR20030038922A (en) * 2001-11-07 2003-05-17 주식회사 포스코 Cokes input control apparatus in blast furnace
KR100793578B1 (en) * 2001-12-20 2008-01-14 주식회사 포스코 Apparatus for press controlling of hopper of blast furnace

Also Published As

Publication number Publication date
JP3273104B2 (en) 2002-04-08

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