JPS589940A - Controlling method for internal pressure of preheating furnace in sintering machine - Google Patents

Controlling method for internal pressure of preheating furnace in sintering machine

Info

Publication number
JPS589940A
JPS589940A JP10780381A JP10780381A JPS589940A JP S589940 A JPS589940 A JP S589940A JP 10780381 A JP10780381 A JP 10780381A JP 10780381 A JP10780381 A JP 10780381A JP S589940 A JPS589940 A JP S589940A
Authority
JP
Japan
Prior art keywords
furnace
pressure
ignition
preheating
internal pressure
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
JP10780381A
Other languages
Japanese (ja)
Other versions
JPS60419B2 (en
Inventor
Akikazu Suzawa
須沢 昭和
Yoshio Nakagawa
中川 美男
Yozo Hosoya
細谷 陽三
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 JP10780381A priority Critical patent/JPS60419B2/en
Publication of JPS589940A publication Critical patent/JPS589940A/en
Publication of JPS60419B2 publication Critical patent/JPS60419B2/en
Expired legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To manufacture a high quality product inexpensively and efficiently with a sintering furnace provided with preheating furnaces before and behind the igniting furnace by regulating the internal pressure of each of the preheating furnaces to a suitable plus range and keeping it higher than the internal pressure of the igniting furnace. CONSTITUTION:The internal pressure of a preheating furnace 5 is detected with a pressure detecting terminal 10, and the detected value is fed back to a controller 12. The controller 12 regulates the opening of a valve 13 and/or the opening of a damper 16 so as to regulate the detected value of the internal pressure of the furnace 5 to +0.5- +2.0mm.H2O. The internal pressure of an igniting furnace 6 is detected with a pressure detecting terminal 11, and the detected value is fed back to the controller 12. The controller 12 regulates the opening of a valve 14 and/or the opening of a damper 17 so as to make the detected value of the internal pressure of the furnaces 0-3mm.H2O higher than that of the furnace 6 at all times.

Description

【発明の詳細な説明】 本ji@は鋳#IIKおける予熱炉の炉内圧力制御方法
に関する%O″eある。
DETAILED DESCRIPTION OF THE INVENTION This article relates to a method for controlling the pressure inside a preheating furnace in casting #IIK.

ドワイトaイド式焼@ * K xる焼結鉱の製造方法
において1点火炉の豪毅に保熱炉【設け1点火畿0鋳曽
″′ド上層を保熱1なツら焼結する技術はI会知、で、
ある、又1点火≧中保熱炉の操業において、−結構O冷
却−から排出す◆#IIガX!1IiIIj熱ガスを点
火r中保熱デ内へ導入しつつ綿、−yる技II%知られ
ている。
Dwight a-type sintering @ * K is I Aichi, and
In some cases, when 1 ignition ≧ medium heat retention furnace is operated, - quite a bit of O cooling - is discharged ◆ #II gas! 1IiIIj The technique of heating the cotton while introducing hot gas into the heat retention device during ignition is known.

そして、li来の焼結鉱製造方法において1点火炉や保
熱炉の炉内圧力制御は重要であって、轟皇看KLる研究
が盛んに行われている0例えは点火炉については特公昭
55−9444号公報に焼結機の冷却器から排出する高
温排ガスを点火炉内へ導入し、炉内圧力を常にプラス圧
に保持するという技術が開示されてお夛、又特開昭55
−28306号公報には点火炉内に燃焼用空気とは別に
炉内圧調整用がx、 2供給し炉内圧を所定のマイナス
圧に制御するという技術が開示されておプ、又以前から
点火炉炉内圧は大気圧近傍に細持すべ書であるという研
究報、告があって、これらの知見及び夷H4業t/cシ
ける経験を基にして点火炉の、炉内圧力を考察してみ1
%炉内圧の最適値は焼結原料や配合、割合1wa結機の
操業条件等に工って変化するものでやる限ル単@には求
められず、又解決すべき技術課題も多いと太見る。
In the modern sintered ore production method, controlling the pressure inside the ignition furnace and heat retention furnace is important, and much research is being conducted on the ignition furnace. Publication No. 55-9444 discloses a technique in which high-temperature exhaust gas discharged from the cooler of the sintering machine is introduced into the ignition furnace to maintain the pressure inside the furnace at positive pressure at all times.
Publication No. 28306 discloses a technology in which air for adjusting the furnace internal pressure is supplied into the ignition furnace in addition to the combustion air to control the furnace internal pressure to a predetermined negative pressure. There are research reports and reports that the pressure inside the furnace should be kept close to atmospheric pressure, and based on these findings and the experience of the H4 industry, we considered the pressure inside the ignition furnace. Mi1
The optimum value of the furnace pressure (%) cannot be determined in a simple manner as it varies depending on the sintering raw materials, composition, operating conditions of the 1wa sintering machine, etc., and there are many technical issues to be solved. look.

又、保熱炉の炉内圧制fjlK関して#−i特企昭50
−20926号公報、Ks炉内にlI&xk吹き込み炉
内圧力を水柱−3u〜水柱+3mオでのI!囲内に制御
しつつ点火直lIO鉤結鉱【加熱し焼結を行うという技
術が開示場れている。
Also, regarding the internal pressure control fjlK of a heat retention furnace,
Publication No. 20926, Ks furnace is injected with lI & A technology has been disclosed that heats and sinters the ignition while controlling the temperature within the range.

この1うに911来O鉤結横の操業Kt11−いては点
火炉中保熱炉Ota*条件についての提案はなされてい
るが1点火炉の前段における焼結原料の加熱や予熱に関
しては注Sネれていなかった。
Since 1991, a proposal has been made regarding the operation of the sintering furnace Ota* in the ignition furnace. It wasn't.

ところが最近に1にって例えば特企昭54−24682
号公報に霧水されているように1点火炉の前段に予熱炉
を設けて点火前において原料表層部を予熱した後点火し
、焼結するという技術が発明され実機化が進められてい
る。この技術は点火前にパレット上の原料上層部に乾燥
、予熱帯會設けるという点でドワイトロイド式―結機に
する焼結鉱製造方法の欠点會鱗決し、I11結鉱Os質
向上。
However, recently, for example, special plan 1972-24682
As described in the above publication, a technology has been invented, in which a preheating furnace is provided in front of the ignition furnace to preheat the surface layer of the raw material before ignition, and then ignited and sintered, and is being put into practical use. This technology eliminates the shortcomings of the Dwight Lloyd method of producing sintered ore in that it requires a drying and preheating chamber on the upper layer of the raw material on the pallet before ignition, and improves the quality of I11 ore.

焼結時開の短縮、燃料部減勢の効果が得られるtのであ
る。
The effect of shortening the open time during sintering and reducing energy in the fuel section can be obtained.

しかしながら1点火炉の前段に設ける予熱炉は従来の保
熱炉とは設置位置が異なるばかシではなく機#XRが全
<Xな夛、又点火炉とt構造及び機能がJ%なるがゆえ
に予熱炉の操tKIi来の保熱炉中点火炉の操業技術【
利用す為ことはできず、°又。
However, the preheating furnace installed before the ignition furnace is not installed in a different position from the conventional heat retention furnace, but because the machine #XR is all < Preheating furnace operation tKIi's operating technology for heat retention furnace and ignition furnace [
It is not possible to use it.

予熱炉は点火炉の前段望ましくは隣接して設置するので
予熱炉単独の操業条件ばかりでなく予熱デの操業が点火
炉に影響【与え、逆に点火炉の炉内圧力KJC9予熱炉
の炉内圧力が影響管受けるこtから、予熱炉tいかに操
業するかということは蟲業者Kflせられた技術的課題
であった。
Since the preheating furnace is installed upstream of the ignition furnace, preferably adjacent to it, not only the operating conditions of the preheating furnace alone but also the operation of the preheating device affect the ignition furnace. Since the pressure is affected by the influence tube, how to operate the preheating furnace was a technical problem faced by manufacturers.

本発明はこのような状況に鑑みてなされたものであ夛1
点火炉の前段に予熱炉1設けた焼結機において、予熱炉
の炉内圧力を十o、s〜+2・0■HsOの範囲内とす
ると共に点火炉の炉内圧力!、63m*1(,0以下の
範囲内で高く維持することt−善黴とするものである。
The present invention was made in view of this situation.
In a sintering machine with a preheating furnace 1 installed upstream of the ignition furnace, the pressure inside the preheating furnace is set within the range of 100, s to +2.0 ■HsO, and the pressure inside the ignition furnace is kept within the range of , 63m*1 (, 0 or less) is considered to be a good mold.

以下図面に基づき本発明【説明する。The present invention will be explained below based on the drawings.

第1図は本発明に係ろ焼結機【例示する概略図でToシ
、第211は本発明の実施例を示す説明園である。
Fig. 1 is a schematic diagram illustrating a sintering machine according to the present invention, and Fig. 211 is an explanatory diagram showing an embodiment of the present invention.

本発明に係る焼結機は j[1図に示す1うに、   
′原料フィーダー1から焼結原料を焼結機2のルット3
土へ連続的に切多出し、ヌプロ季ット4vt低速で一転
せしめ、)臂レット3上の鉤結原料表層郁を予熱炉5か
ら熱風を吹き付けて予熱し、予熱された原料表面へ点火
炉6にて火炎管噴射し□門□科中に配合した黴ノ臂−令
ントのコークス□粉ramせしめ下方から第2図に示す
ウィンドーツクスフ1介して吸気し紳鉱部11に至るま
での間にノ臂レット3上O鉤結原料【金層にわたって焼
結□せしめ連続的に@給鉱tlI4造する装置であって
、この装置自体は例えばlII#金昭54−24682
号公報K14示ネれておL ドヮイトロイド式鋳結機0
改JL!1′として会知Oものである。
The sintering machine according to the present invention has the following features:
'The sintering raw material is transferred from the raw material feeder 1 to the lut 3 of the sintering machine 2.
Continuously cut the material into the soil, turn it around at a low speed of Nupro 4V, preheat the surface layer of the hooked raw material on the armlet 3 by blowing hot air from the preheating furnace 5, and transfer it to the surface of the preheated raw material in the ignition furnace. At step 6, a flame tube is injected into the mold and the coke powder mixed in the □ gate □ section. This is a device that sinters over the gold layer and continuously produces @ feed ore tlI4, and this device itself is made of, for example, II # Kinsho 54-24682.
Publication K14 Indicated L Deutroid type casting machine 0
Kai JL! 1' is a knowledgeable thing.

本発明は点火炉6とこれKII緩して前段に設置した予
熱炉5の炉内圧力を点火炉6の炉内圧力とO関係t*g
t、て最適に制御する方法でToL予熱炉5の炉内圧力
f + 0−5− +2−OM Hs00範囲内とする
と共に点火炉の炉内圧カj13.以下の範囲内で高く細
持することにある。
In the present invention, the pressure inside the ignition furnace 6 and the preheating furnace 5 installed at the front stage of the ignition furnace 6 are determined by the relationship t*g
t, the furnace pressure of the ToL preheating furnace 5 is controlled to be within the range of f + 0-5- +2-OM Hs00 by an optimal control method, and the furnace pressure of the ignition furnace is controlled to be within the range of f + 0-5- +2-OM Hs00. The goal is to maintain it within the following range.

予熱炉sの炉内圧カ會十0・5〜+2;OwxQ範■と
するのは1点大前の′−結原料−均一に予熱するために
必1I11に値であり 、 + 0.5 m )!*O
,1FcillO場合には点火炉6内の炉内圧ガO影蕃
を受けて与熱炉5内の圧力変動が大とな)、又点火ゾロ
内の大炎が予熱炉5内へ流れるという問題が生じ1点火
ゾロと予熱炉5とt仕切る仕切1118の下端が溶横し
、更には予熱炉内が大気圧1〕も圧力が低くなった場合
はノ臂しット両ナイド及び予熱ipsom面下部から冷
風管機い込み原料表層の均一な予熱が不可能になル予熱
機能を低減する危険性が大−〈な□る。三方炉内圧力が
+2−Ow Hg0k超えると予熱炉内からの熱風吹出
しが着しくなat険な状態とな)、更には予熱炉から点
火炉内へ予熱空気が入り込むので点火炉における正常の
点火かで番なくなるという問題が生じる。
The internal pressure of the preheating furnace is 0.5 to +2; OwxQ range is 1 point large - the crystallizing material - the value must be 1I11 for uniform preheating, + 0.5 m )! *O
, 1 Fcell O, there is a problem that the pressure fluctuation in the heating furnace 5 is large due to the influence of the pressure inside the ignition furnace 6), and the large flame in the ignition furnace flows into the preheating furnace 5. If the lower end of the partition 1118 that separates the preheating furnace 5 from the 1st ignition melts, and the pressure in the preheating furnace becomes lower than the atmospheric pressure 1], the lower end of the partition 1118 that separates the preheating furnace 5 and This makes it impossible to uniformly preheat the surface layer of the raw material fed into the cold air pipe machine, and there is a great risk that the preheating function will be reduced. If the pressure inside the three-way furnace exceeds +2-OwHg0k, the hot air from inside the preheating furnace will not blow out properly (a dangerous situation will occur), and furthermore, preheated air will enter the ignition furnace from the preheating furnace, preventing normal ignition in the ignition furnace. A problem arises in which the number of keys is lost.

一方、予熱炉の炉内圧を点火炉O炉内圧L9も常に0■
HIO以上で3−Om HmO以下の値だけ高目に設定
するのは、予熱炉の炉内圧が点火tso炉内圧力りり低
くなると点火炉における火炎が予熱炉側へ流れるため前
述のように仕切壁が溶損するという問題があるはか2点
火炉Kkける火炎が原料表面に流れて均一な点火がms
にな〕その結果点大強度を低下させ焼結鉱の成品歩留を
悪化させ。
On the other hand, the furnace internal pressure of the preheating furnace and the ignition furnace O furnace internal pressure L9 are always 0.
The reason why the value is set higher than HIO and less than 3-Om HmO is because when the pressure inside the preheating furnace gets too low, the flame in the ignition furnace flows toward the preheating furnace. There is a problem of melting and damage in the two-ignition furnace.
As a result, the strength of the sintered ore is greatly reduced and the product yield of the sintered ore is deteriorated.

エネルギー原単位中落下強度、低slR元粉化指数等成
品の品質を悪化させる 又、炉内圧力差が3 mm H*Oを超えると逆に点火
炉Kk叶る火炎が予熱炉と反対匈即ちΔレットの進行方
向に吹嘗飛ばされるので、この場合を原料表層へO均一
な点火ができなくなり成品歩留やエネルイー原単位及び
成品品質が悪化する−1層ち、予熱デと点火炉の炉内圧
力差は0〜31UH10の範囲で予熱炉oyJが常に高
くなるように操業すると予熱炉と点火炉との炉内圧力の
バランスが優れ、予熱炉の機能が正常Km持でき、点火
炉においても火炎が流れたL吹會飛ばされたりすること
がなく火炎が安定しておp均一な着火が可能である。
In addition, if the pressure difference in the furnace exceeds 3 mm H*O, the flame of the ignition furnace will be opposite to that of the preheating furnace. In this case, uniform ignition to the surface layer of the raw material becomes impossible, and the product yield, energy consumption rate, and product quality deteriorate. If the preheating furnace oyJ is operated so that the internal pressure difference is in the range of 0 to 31UH10 and the preheating furnace oyJ is always high, the internal pressure between the preheating furnace and the ignition furnace will be well balanced, the preheating furnace can function normally for Km, and even the ignition furnace will The flame is not blown away and the flame is stable and uniform ignition is possible.

次に本発明に係る予熱炉及び点火炉の炉内圧制御方法k
g211に基づいて脱明する。
Next, a method k for controlling the internal pressure of a preheating furnace and an ignition furnace according to the present invention.
Delight based on g211.

第2図に示すように予熱炉5内に拡圧カ樟出端10を設
け1点火炉6内にも圧カ検出端lit設け、8E力検出
端10,11は制御装置12へその圧力検出値會入力せ
しめる工うに構成してお)。
As shown in FIG. 2, a pressure expansion force outlet end 10 is provided in the preheating furnace 5, and a pressure detection end lit is also provided in the ignition furnace 6, and the 8E force detection ends 10 and 11 are connected to the control device 12 to detect the pressure. )

制御装置12からは予熱炉5内と点火炉6内へ熱風11
込むための枝管9人及び9Bにそれぞれ設けた熱風流量
調整用弁13及び弁14へ弁の開閉指令を発するように
なっており、更にはウィンドゼツクス7.7と吸気用メ
インダクト15と【接続するウィンドレグ15A、15
B[設置した流量調整用ダンパー16及び17にダンノ
ー開閉指令を発するようになっている。図中、9は熱風
吹込用本管である。
Hot air 11 is sent from the control device 12 into the preheating furnace 5 and into the ignition furnace 6.
It is designed to issue valve opening/closing commands to the hot air flow rate adjustment valves 13 and 14 provided in branch pipes 9 and 9B, respectively. [Wind leg 15A, 15 to connect
B [Dunno opening/closing commands are issued to the installed flow rate adjustment dampers 16 and 17. In the figure, 9 is a main pipe for blowing hot air.

本発明に係る制御装ft12は予熱炉5内の炉内圧力値
が+0.5〜+2.0龍H,Oの範囲内にあるかどうか
の判定を行い、炉内圧力がこOSS内に入っている場合
は弁13及びダンパー160開閉指令は発しない。次に
点火炉6内の圧力と予熱炉5内の圧力と會比較し予熱炉
50方が点火炉6エ夛も炉内圧が3mH10以内の範囲
内で高い値【維持しているかどうかt判定する。この判
定の結果、範囲内にあれば弁14及びダンパー17の開
閉指令は発しない、しかしながら予熱炉5の炉内圧が点
火炉6内の圧力よj3mHsOtjllえて高い場合、
又は予熱炉HOP内圧が点火炉6内の圧力よやも低い場
合には点火炉6内に熱風管吹き込む枝管9Bに設けた弁
14又はクインドレグダン/臂−170mfm令を尭し
点火P6内の炉内圧を調整することKLp予熱炉5と点
火炉6とO炉内圧差を所定の値、即ち予熱rsO方が0
〜3鰭石0以内の範囲内で雷に高い値となるようKM持
せしめる0点火炉6内の圧力は大気圧に出来るだけ近い
値とする。−bXmm″′Cあp、望オしくは大気圧プ
ラス・マイナスl■H,OO範囲内と・するのが有利で
あるため1点火炉60炉内圧調斃が望ましくない範囲と
なる仁とが予!lネれる場合には次の15な麩置會とる
The control device ft12 according to the present invention determines whether the furnace pressure value in the preheating furnace 5 is within the range of +0.5 to +2.0 H,O, and determines whether the furnace pressure value is within the range of +0.5 to +2.0. If so, the valve 13 and damper 160 opening/closing commands are not issued. Next, the pressure in the ignition furnace 6 is compared with the pressure in the preheating furnace 5, and the pressure in the preheating furnace 50 and the pressure in the ignition furnace 6 are higher within the range of 3 mH10. . If the result of this determination is within the range, the opening/closing command for the valve 14 and damper 17 will not be issued. However, if the pressure inside the preheating furnace 5 is higher than the pressure inside the ignition furnace 6,
Or, if the internal pressure of the preheating furnace HOP is lower than the pressure inside the ignition furnace 6, the valve 14 or the valve 14 installed on the branch pipe 9B that blows the hot air into the ignition furnace 6 or the quintile/arm-170mfm can be used to close the furnace inside the ignition P6. Adjusting the internal pressure The difference in internal pressure between the KLp preheating furnace 5, the ignition furnace 6, and the O furnace is set to a predetermined value, that is, the preheating rsO is 0.
The pressure in the 0 ignition furnace 6, which maintains KM to a high value within the range of 0 to 3, is set to a value as close to atmospheric pressure as possible. -b If I am able to attend, I will hold the next 15 meeting.

蕗ち、制御装置12内に点火炉炉内圧力の望tしい値と
して大気圧プラスマイナス1.oIIwHloの値を予
め入力しておき1点火炉6内圧力の調整が必l!になっ
た際調整後の圧力が前記予、め入力してシ〈値から外れ
ることが予lIされる場合には点火炉の炉内圧力管その
ままとして予熱炉S内の圧力を制御する。予熱炉5内の
圧力、igt*a弁13又線Iンパー16の開度を調整
し圧力検出端lOによる炉内圧力機出値をフィードバッ
クさせることにより前記弁1 ’3又はダンパー16の
いずれか又は両方の開度を調整するととによp炉内圧力
が+α5〜+20−H,Oの範囲内で所定の値に制御す
る。又。
The desired value of the pressure inside the ignition furnace is set in the control device 12 as atmospheric pressure plus or minus 1. It is necessary to input the value of oIIwHlo in advance and adjust the pressure inside the ignition furnace 6! If it is predicted that the adjusted pressure will deviate from the pre-input value, the pressure in the preheating furnace S is controlled using the furnace pressure pipe of the ignition furnace as is. By adjusting the pressure in the preheating furnace 5, the opening degree of the igt*a valve 13 or the line I damper 16, and feeding back the pressure output value in the furnace by the pressure detection terminal lO, either the valve 1'3 or the damper 16 can be adjusted. Alternatively, by adjusting both opening degrees, the pressure inside the furnace is controlled to a predetermined value within the range of +α5 to +20−H,O. or.

点火炉6内の圧力調整を可能な範囲内で行った後残シの
圧力制御を予熱炉5で行ってもよい。
After the pressure in the ignition furnace 6 has been adjusted within a possible range, the pressure of the residue may be controlled in the preheating furnace 5.

圧力検出端10による予熱炉5内の圧力検出値が+0,
5〜+20■H鵞0の範囲内から外れた場合はただちに
弁13又はダン”−16の開度を111111し所定の
炉内圧力になるように制御し、制御後は点火炉6内の圧
力と予熱炉5内の圧力上の差が前記所定の範囲内にある
かどうかを判定し、予熱炉炉内圧制御による点火炉の炉
内圧が正常であるかどうかを確認し、正常の範囲から外
れ九場合には点火炉6の炉内圧を前記のとおり制御する
The pressure detected in the preheating furnace 5 by the pressure detection end 10 is +0,
If the value falls outside the range of 5 to +20■H 0, immediately control the opening of valve 13 or Dan''-16 to maintain the predetermined pressure in the furnace, and after controlling the pressure in the ignition furnace 6. It is determined whether the difference in the pressure between In the case of 9, the pressure inside the ignition furnace 6 is controlled as described above.

実施例 点火炉の前段に点火炉と隣接し九予熱炉を設けたドワイ
トロイド式焼結機によp、予熱炉には250℃の熱風管
導入して点火前の焼結原料表層【予熱しその後点火L−
felt給鉱′に#造した。この時予熱炉の炉内圧力は
一〇・5〜3・OmaHloの範囲。
Example: A Dwight Lloyd type sintering machine is used, which has a preheating furnace installed in the front stage of the ignition furnace and adjacent to the ignition furnace. Then ignition L-
# was made in the felt feed. At this time, the pressure inside the preheating furnace is in the range of 10.5 to 3.OmaHlo.

点火炉の炉内圧力は−2,0〜1・5 w H20の範
囲内でそれぞれ8段階K O−5w HsO*IIみで
変化させて成品歩留、燃料原単位、m給鉱の品質、生産
比を比較した。そO結果を第1表にまとめて示した。
The internal pressure of the ignition furnace was varied in 8 steps within the range of -2.0 to 1.5 w H20, respectively, to determine product yield, fuel consumption, quality of feed ore, The production ratio was compared. The results are summarized in Table 1.

菖1表に示す1うに成品歩留、原料中に配合した粉)−
クスのコークス原単位1点火炉における00G原単位、
得られた焼結鉱の落下強度及び低iIR元粉化指数、生
意比は、予熱炉炉内圧力が0・5〜2・0■H虐00@
@で〔予熱炉炉内圧カ一点火炉炉内圧力〕が0〜3 w
r )Is 00範囲にある実施例1〜実施例4が嵐好
な値を示し次。しかしながら予熱炉炉内圧力がO−5m
 HtO未満でかつ予熱炉1ヤ点火炉07Fが炉内圧の
高い比較例1.2は共に本発明の実施例に比験していず
れも劣る結果となってお〕、又、予熱炉炉内圧力が2・
□wHsOkm、1かつ〔予熱炉炉内圧カ一点火炉炉内
圧力〕が3 M 1110 vt超えた比較例3.4は
本発@C)lil施例に比験していずれも劣るばかルで
なく前記比較例1.21りも劣る結果となった。比較例
3,4は共に本発明の前記JIIJI!要件【欠くのみ
ならず本発1!jlKIKる点火炉O適正炉内圧範8を
外れていることが悪影響を1埋しているものと考えられ
る。
1 Sea urchin product yield shown in Table 1, powder mixed in raw materials) -
00G basic unit in one ignition furnace,
The drop strength, low iIR original powdering index, and raw material ratio of the obtained sintered ore were determined when the pressure inside the preheating furnace was 0.5 to 2.0 ■ H 00@
At @, [preheating furnace furnace pressure] is 0 to 3 w
r) Examples 1 to 4 in the Is 00 range showed excellent values. However, the pressure inside the preheating furnace is O-5m.
Comparative Examples 1 and 2, in which the pressure in the preheating furnace 1 and the ignition furnace 07F were lower than HtO, had inferior results compared to the examples of the present invention. 2・
Comparative example 3.4 in which wHsOkm was 1 and [preheating furnace internal pressure] exceeded 3 M 1110 vt was not inferior in any way compared to the present @ C) lil example, but was as above. The results were also inferior to Comparative Example 1.21. Comparative Examples 3 and 4 are both JIIJI! of the present invention! Requirements [Not only lacking, but also essential! It is thought that the fact that the ignition furnace O is out of the appropriate furnace internal pressure range is one of the negative effects.

以上述べた15に本発明によれば点火炉の前段に予熱炉
を設けたドワイトロイド弐鉤結機に1つて焼結鉱t−製
造するに際し、良品質の製品を安価にかつ能率的にIR
造できるというHIFな効果【奏するものである。
According to the above-mentioned 15, according to the present invention, when manufacturing sintered ore using a Dwight Lloyd sintering machine equipped with a preheating furnace at the front stage of the ignition furnace, a high quality product can be produced at low cost and efficiently using IR.
It has the HIF effect of being able to create.

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

wXIIllは本発明に係る焼結機を例示する概略図。 @2図は本発明の実施例を示す説明図である。 2・・・焼結機S 5・・・予熱炉、6・・・点火炉。 9人、トド・・枝管、10.11・・・圧力検出端。 12・・・制御装置、13.14・・・弁、1$A、1
5B・・・ウィンドレグ、16.17・・・ダンパー。 代理人 弁理士  秋 沢 政 光 信   2   名
wXIIll is a schematic diagram illustrating a sintering machine according to the present invention. @2 Figure is an explanatory diagram showing an embodiment of the present invention. 2... Sintering machine S 5... Preheating furnace, 6... Ignition furnace. 9 people, sea lion...branch pipe, 10.11...pressure detection end. 12...Control device, 13.14...Valve, 1$A, 1
5B... Wind leg, 16.17... Damper. Agent Patent Attorney Masanobu Akizawa 2 people

Claims (1)

【特許請求の範囲】[Claims] (1)点火炉O前段に予熱デ【設けた焼結機において、
予熱炉の炉内圧力k + 0−5〜+ 2−OmH,O
のll1l内とすゐと共に点火PIDf’内圧力A j
l 3 wm 40以下ctHts内で高(IIIk持
することt41黴とする焼結@における予II&炉の炉
内圧力制御方法。
(1) In the sintering machine equipped with a preheating device in the front stage of the ignition furnace O,
Furnace pressure of preheating furnace k + 0-5 ~ + 2-OmH,O
Ignition PIDf' internal pressure A j
l 3 wm 40 or less ctHts to maintain high (IIIk) t41 mold during sintering @preliminary & furnace pressure control method.
JP10780381A 1981-07-10 1981-07-10 Furnace pressure control method for preheating furnace in sintering machine Expired JPS60419B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10780381A JPS60419B2 (en) 1981-07-10 1981-07-10 Furnace pressure control method for preheating furnace in sintering machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10780381A JPS60419B2 (en) 1981-07-10 1981-07-10 Furnace pressure control method for preheating furnace in sintering machine

Publications (2)

Publication Number Publication Date
JPS589940A true JPS589940A (en) 1983-01-20
JPS60419B2 JPS60419B2 (en) 1985-01-08

Family

ID=14468423

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10780381A Expired JPS60419B2 (en) 1981-07-10 1981-07-10 Furnace pressure control method for preheating furnace in sintering machine

Country Status (1)

Country Link
JP (1) JPS60419B2 (en)

Also Published As

Publication number Publication date
JPS60419B2 (en) 1985-01-08

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