JP2002155309A - Ejecting device in movable furnace hearth type heat treatment furnace and its operation method - Google Patents

Ejecting device in movable furnace hearth type heat treatment furnace and its operation method

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Publication number
JP2002155309A
JP2002155309A JP2000348210A JP2000348210A JP2002155309A JP 2002155309 A JP2002155309 A JP 2002155309A JP 2000348210 A JP2000348210 A JP 2000348210A JP 2000348210 A JP2000348210 A JP 2000348210A JP 2002155309 A JP2002155309 A JP 2002155309A
Authority
JP
Japan
Prior art keywords
heat treatment
hearth type
moving hearth
type heat
treatment furnace
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
JP2000348210A
Other languages
Japanese (ja)
Other versions
JP3583067B2 (en
Inventor
Takao Umeki
隆夫 梅木
Masahiko Tetsumoto
理彦 鉄本
Toshikatsu Uchida
利克 内田
Sumuto Hashimoto
澄人 橋本
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP2000348210A priority Critical patent/JP3583067B2/en
Priority to US09/916,588 priority patent/US6669756B2/en
Priority to EP01118269A priority patent/EP1178276A3/en
Priority to CA002354465A priority patent/CA2354465A1/en
Publication of JP2002155309A publication Critical patent/JP2002155309A/en
Application granted granted Critical
Publication of JP3583067B2 publication Critical patent/JP3583067B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Tunnel Furnaces (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an ejecting device in a movable furnace hearth type reduction furnace with which a material to be heat-treated can continuously be ejected in a fixed amount without obstructing the operation in the movable furnace hearth type reduction furnace and a facility on the downstream side therefrom and without reoxidizing the material to be heat-treated in the reduction furnace. SOLUTION: The material to be heat-treated ejected from an ejecting hole 11 of the movable furnace hearth type reduction furnace 1, is ejected into a screen sizer 3, and the material to be heat-treated from which a large lump foreign material is removed with this screen sizer 3 is discharged into a receiving recessed position 71a in a receiving pan 71 arranged in a casing 5 with a hopper through a seal leg 4 into which reoxidization preventing gas is blown from a gas blowing nozzle 6, the material to be heat-treated piled on the upper surface of this receiving recessed position 71a, is ejected into the casing 5 with the hopper from both end parts in the longitudinal direction of the receiving pan 71 by swinging a scraper 72 and also, supplied into the facility at the downstream side from a lower ejecting hole 52 in the casing 5 with the hopper.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、移動炉床式熱処理
炉の排出装置およびその操業方法に関する。より詳しく
は、移動炉床式熱処理炉、および下流側設備の操業が妨
げられることがなく、再酸化性の恐れが高い還元鉄を、
排出する場合においても還元鉄を再酸化させることがな
く、定量的、かつ連続的に排出することができ、しかも
構成部品の損耗を少なくすることを可能ならしめるよう
にした移動炉床式熱処理炉の排出装置およびその操業方
法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a discharge apparatus for a moving hearth type heat treatment furnace and a method for operating the same. In more detail, the moving hearth-type heat treatment furnace, and reduced iron that does not hinder the operation of the downstream equipment and has a high risk of reoxidation,
A moving hearth type heat treatment furnace capable of quantitatively and continuously discharging reduced iron without reoxidizing reduced iron even when discharging, and reducing wear of components. And a method of operating the same.

【0002】[0002]

【従来の技術】周知のとおり、近年、鉄鉱石、または製
鉄所のダスト、その他の廃棄物、石炭等を成分とする原
料を還元することによって、還元鉄または金属鉄を製造
する移動炉床式熱処理炉が広く利用されるようになって
きている。還元鉄または金属鉄を製造する移動炉床式熱
処理炉は、その移動炉床上で原料を還元、または還元後
に、さらなる加熱により鉄とスラグを溶融分離させる。
そして、排出口から排出された再酸化性の高い還元鉄ま
たは再酸化の問題のない金属鉄(以下、被熱処理物とい
う。)、炭素質粉、スラグ混合物を炉外に排出するため
の排出装置を備えているが、このような移動炉床式熱処
理炉の排出装置には種々の形態のものが知られている。
2. Description of the Related Art As is well known, in recent years, a moving hearth type in which reduced iron or metallic iron is produced by reducing raw materials containing iron ore, dust from ironworks, other waste, coal, etc. as components. Heat treatment furnaces are becoming widely used. In a moving hearth type heat treatment furnace for producing reduced iron or metallic iron, the raw material is reduced on the moving hearth, or after the reduction, the iron and slag are melted and separated by further heating.
A discharge device for discharging a mixture of reduced iron having high reoxidation property or metallic iron having no reoxidation problem (hereinafter referred to as a heat treatment target), a carbonaceous powder, and a slag mixture discharged from the discharge port. However, various types of discharge devices of such a moving hearth type heat treatment furnace are known.

【0003】先ず、従来例1に係る移動炉床式熱処理炉
の排出装置は、この移動炉床式熱処理炉の被熱処理物の
排出口と下流側設備との間に配設されるシュートと、こ
のシュートに配設され、移動炉床式からの高温ガスの流
出を阻止する2段構え、またはそれ以上の段数の周知の
構成になる高温開閉弁とから構成されている。つまり、
高温開閉弁相互の開閉操作により、移動炉床式熱処理炉
からの高温ガスの流出を阻止しながら、被熱処理物を炉
外に排出すると共に、排出された被熱処理物を下流側設
備に供給する構成になるものである。
First, a discharge device of a moving hearth type heat treatment furnace according to Conventional Example 1 includes a chute disposed between a discharge port of a heat treatment target of the moving hearth type heat treatment furnace and downstream equipment; The chute is provided with a two-stage or high-temperature on-off valve having a well-known configuration having more stages than that for preventing the outflow of high-temperature gas from the moving hearth type. That is,
By opening and closing the high-temperature on-off valves, the heat-treated material is discharged outside the furnace while the flow of the high-temperature gas from the moving hearth-type heat treatment furnace is prevented, and the discharged heat-treated material is supplied to downstream equipment. It is a configuration.

【0004】従来例2に係る移動炉床式熱処理炉の物排
出装置は、この移動炉床式熱処理炉の被熱処理物を排出
する排出口と取外し式密閉容器との間に配設されるシュ
ートと、このシュートの途中に配設される周知の構成に
なる高温開閉弁とから構成されてなるものである。
The object discharge device of the moving hearth type heat treatment furnace according to the prior art 2 is a chute disposed between the discharge port for discharging the heat treatment target of the moving hearth type heat treatment furnace and the detachable closed container. And a high-temperature on-off valve having a well-known configuration disposed in the middle of the chute.

【0005】従来例3に係る移動炉床式熱処理炉の排出
装置は、この移動炉床式熱処理炉の被熱処理物を排出す
る排出口に一端側が接続されたシュートの他端側に、振
動フィーダー、スクリュコンベヤ、またはパンコンベヤ
等の定量排出機器が配設されてなる構成になるものであ
る。
[0005] The discharge device of the moving hearth type heat treatment furnace according to the prior art 3 comprises a vibrating feeder connected to the other end of a chute having one end connected to a discharge port for discharging a heat treatment target of the moving hearth type heat treatment furnace. , A screw conveyor, a pan conveyor or the like.

【0006】[0006]

【発明が解決しようとする課題】上記従来例1に係る移
動炉床式熱処理炉の排出装置では、移動炉床式熱処理炉
の排出口から排出される被熱処理物は最高1000℃も
の高温であるのに加えて、粉体(炭素質粉)も排出され
るため、高温開閉弁に閉塞、固着等のトラブルが発生し
易く、安定操業の継続が困難である。また、高温開閉弁
による被熱処理物の排出は断続的であり、特に下流側に
溶解炉が設置されている場合には連続溶解ができず、還
元鉄または金属鉄の生産性の向上が望めないという解決
すべき課題があった。
In the discharge apparatus of the moving hearth type heat treatment furnace according to the above prior art example 1, the object to be heat treated discharged from the discharge port of the moving hearth type heat treatment furnace has a high temperature as high as 1000 ° C. at the maximum. In addition, since powder (carbonaceous powder) is also discharged, troubles such as blockage and sticking of the high-temperature on-off valve are likely to occur, and it is difficult to continue stable operation. In addition, the discharge of the material to be heat-treated by the high-temperature on-off valve is intermittent, especially when a melting furnace is installed on the downstream side, continuous melting cannot be performed, and improvement in productivity of reduced iron or metallic iron cannot be expected. There was a problem to be solved.

【0007】上記従来例2に係る移動炉床式熱処理炉の
排出装置では、高温開閉弁について上記従来例1の場合
と同様の問題があるのに加えて、移動炉床式熱処理炉と
取外し式密閉容器との間に配設されるシュートとを完全
に密閉構成にすることが困難であり、特に移動炉床式熱
処理炉を負圧で操業する場合、移動炉床式熱処理炉内に
空気が流入する危険性が大である。つまり、移動炉床式
熱処理炉内に空気が流入すると、還元された還元鉄が再
酸化して製品価値が低下すると共に、酸化時の熱により
還元鉄が溶融して融着したり、炭素質粉が燃焼する等の
問題が生じて排出困難となり、さらに製品価値が低下す
ることになる。
[0007] In the discharge apparatus of the moving hearth type heat treatment furnace according to the second conventional example, the high temperature on-off valve has the same problems as those of the first prior art example. It is difficult to make the chute disposed between the closed vessel and the closed vessel completely closed.Especially, when the moving hearth type heat treatment furnace is operated at a negative pressure, air flows into the moving hearth type heat treatment furnace. The risk of inflow is great. In other words, when air flows into the moving hearth type heat treatment furnace, the reduced reduced iron is re-oxidized and the product value is reduced, and the reduced iron is melted and fused by the heat of the oxidation, Problems such as burning of the powder occur, making it difficult to discharge, and further reducing the product value.

【0008】上記従来例3に係る移動炉床式熱処理炉の
排出装置では、被熱処理物を定量的に排出することがで
きるという利点があるものの、振動フィーダー、スクリ
ュコンベヤ、またはパンコンベヤ等に、耐高温性、気密
性に関する問題があり、上記従来例2の場合と同様に、
還元鉄が再酸化して製品価値が低下すると共に、酸化時
の熱により還元鉄が溶融して還元鉄同志が融着したり、
炭素質粉が燃焼する等の問題が生じる。また、振動フィ
ーダー、スクリュコンベヤ、パンコンベヤ等のうち、最
も気密性が優れているのはスクリュコンベヤであるが、
スクリュコンベヤでは、構造上、スクリュシャフトが高
温の被熱処理物に直接接触するため、耐熱性の問題に加
えて、摩耗による消耗が激しくメンテナンスコストが嵩
むという解決すべき課題があった。
[0008] The discharge device of the moving hearth type heat treatment furnace according to the prior art 3 has the advantage that the heat treatment target can be discharged quantitatively, but the vibration feeder, the screw conveyer, the pan conveyer, etc. There are problems related to high temperature resistance and airtightness.
The reduced iron is re-oxidized and the product value is reduced, and the reduced iron is melted by the heat of the oxidation and the reduced iron is fused together.
Problems such as burning of the carbonaceous powder occur. Of the vibratory feeder, screw conveyor, pan conveyor, etc., the one with the best airtightness is the screw conveyor,
In the screw conveyor, there is a problem to be solved in that the screw shaft is in direct contact with a high-temperature heat-treated material due to its structure, and in addition to the problem of heat resistance, wear due to abrasion is severe and maintenance cost is increased.

【0009】従って、本発明の目的は、移動炉床式熱処
理炉、および下流側設備の操業が妨げられることがな
く、再酸化性の恐れが高い還元鉄を、排出する場合にお
いても還元鉄を再酸化させることがなく、定量的、かつ
連続的に排出することができ、しかも構成部品の損耗を
少なくすることを可能ならしめる移動炉床式熱処理炉の
排出装置および移動炉床式熱処理炉の操業方法を提供す
ることである。なお、本発明は、還元鉄または金属鉄を
対象として限定するものではなく、非鉄金属等を含有す
る熱処理された金属含有物を対象とするものである。
Therefore, an object of the present invention is to reduce the reduced iron even when discharging the reduced iron having a high possibility of reoxidation without hindering the operation of the moving hearth type heat treatment furnace and the downstream equipment. A discharge apparatus for a moving hearth type heat treatment furnace and a moving hearth type heat treatment furnace which can be discharged quantitatively and continuously without reoxidation and which can reduce the wear of components. It is to provide an operation method. The present invention is not limited to reduced iron or metallic iron, but is directed to a heat-treated metal-containing material containing a non-ferrous metal or the like.

【0010】[0010]

【課題を解決するための手段】本発明は、上記実情に鑑
みてなされたもので、従って上記課題を解決するため
に、本発明の請求項1に係る移動炉床式熱処理炉の排出
装置が採用した手段の特徴とするところは、移動炉床式
熱処理炉から被熱処理物を下流側設備に排出する移動炉
床式熱処理炉の排出装置であって、ケーシング内に、前
記移動炉床式熱処理炉から排出された被熱処理物を受入
れて一時的に保持する受入れ凹所を備えた凹状保持部材
と、前記受入れ凹所の面に沿うように往復動して、この
受入れ凹所内に保持されている被熱処理物を前記ケーシ
ング内に排出するスクレーパーとを設けたところにあ
る。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned circumstances, and in order to solve the above-mentioned problems, a discharge apparatus for a moving hearth type heat treatment furnace according to claim 1 of the present invention is provided. The feature of the adopted means is a discharge device of a moving hearth type heat treatment furnace for discharging an object to be heat-treated from a moving hearth type heat treatment furnace to downstream equipment, wherein the moving hearth type heat treatment furnace is provided in a casing. A concave holding member having a receiving recess for receiving and temporarily holding the object to be heat-treated discharged from the furnace, and reciprocating along the surface of the receiving recess to be held in the receiving recess. And a scraper for discharging the object to be heat-treated into the casing.

【0011】本発明の請求項2に係る移動炉床式熱処理
炉の排出装置が採用した手段の特徴とするところは、請
求項1に記載に移動炉床式熱処理炉の排出装置におい
て、前記移動炉床式熱処理炉と前記凹状保持部材との間
に、前記移動炉床式熱処理炉から排出された被熱処理物
を前記凹状保持部材の受入れ凹所に導くシ−ルレグを配
設したところにある。
According to a second aspect of the present invention, there is provided a discharge apparatus for a moving hearth type heat treatment furnace, wherein the discharging apparatus for a moving hearth type heat treatment furnace is characterized in that, A seal leg is provided between the hearth type heat treatment furnace and the concave holding member for guiding a heat-treated material discharged from the moving hearth type heat treatment furnace to a receiving recess of the concave holding member. .

【0012】本発明の請求項3に係る移動炉床式熱処理
炉の排出装置が採用した手段の特徴とするところは、請
求項2に記載に移動炉床式熱処理炉の排出装置におい
て、前記ケーシング内に再酸化防止ガスを吹込むガス吹
込みノズルを、前記シールレグに連通させたところにあ
る。
[0012] The discharging apparatus of the moving hearth type heat treatment furnace according to claim 3 of the present invention is characterized in that the means employed in the discharging apparatus of the moving hearth type heat treatment furnace according to claim 2 is the casing. A gas blowing nozzle for blowing a re-oxidation preventing gas into the inside is connected to the seal leg.

【0013】本発明の請求項4に係る移動炉床式熱処理
炉の排出装置が採用した手段の特徴とするところは、請
求項3に記載の移動炉床式熱処理炉の排出装置におい
て、前記移動炉床式熱処理炉と前記シ−ルレグとの間
に、被熱処理物中の異物を選別して系外に排出するスク
リーンサイザーを配設したところにある。
According to a fourth aspect of the present invention, there is provided a discharge apparatus for a moving hearth type heat treatment furnace according to a fourth aspect of the present invention. A screen sizer is disposed between the hearth type heat treatment furnace and the seal leg to select foreign matter in the heat treatment target and discharge the foreign matter to the outside of the system.

【0014】本発明の請求項5に係る移動炉床式熱処理
炉の操業方法が採用した手段の特徴とするところは、移
動炉床式熱処理炉から被熱処理物を下流側設備に排出す
る移動炉床式熱処理炉の操業方法であって、前記移動炉
床式熱処理炉から排出された被熱処理物をケーシング内
に設けた凹状保持部材の受入れ凹所に受入れると共に一
時的に保持し、前記受入れ凹所の面に沿うようにスクレ
ーパーを往復動させて、前記受入れ凹所内に保持されて
いる被熱処理物を前記ケーシング内に排出するところに
ある。
According to a fifth aspect of the present invention, there is provided a method for operating a moving hearth type heat treatment furnace, wherein the moving hearth type heat treatment furnace discharges a heat-treated material from the moving hearth type heat treatment furnace to downstream equipment. A method of operating a floor type heat treatment furnace, comprising: receiving a heat-treated object discharged from the moving hearth type heat treatment furnace in a receiving recess of a concave holding member provided in a casing; The scraper is reciprocated along the plane of the place to discharge the object to be heat-treated held in the receiving recess into the casing.

【0015】本発明の請求項6に係る移動炉床式熱処理
炉の操業方法が採用した手段の特徴とするところは、請
求項5に記載の移動炉床式熱処理炉の操業方法におい
て、前記ケーシング内に、少なくとも被熱処理物の再酸
化を防止する再酸化防止ガスを吹込むところにある。
A feature of the means adopted by the method for operating a moving hearth type heat treatment furnace according to claim 6 of the present invention is that in the method for operating a moving hearth type heat treating furnace according to claim 5, At least, a re-oxidation preventing gas for preventing re-oxidation of the object to be heat-treated is blown therein.

【0016】本発明の請求項7に係る移動炉床式熱処理
炉の操業方法が採用した手段の特徴とするろころは、請
求項5または6のうちの何れか一つの項に記載の移動炉
床式熱処理炉の操業方法において、前記移動炉床式熱処
理炉から排出された被熱処理物を、前記シ−ルレグ中を
通して前記凹状保持部材の受入れ凹所に受入れるところ
にある。
According to a seventh aspect of the present invention, there is provided a moving furnace according to any one of the fifth and sixth aspects of the present invention, wherein the roller is characterized by a means adopted by the operating method of the moving hearth type heat treatment furnace. In the method for operating a floor type heat treatment furnace, the object to be heat treated discharged from the moving hearth type heat treatment furnace is received in the receiving recess of the concave holding member through the seal leg.

【0017】本発明の請求項8に係る移動炉床式熱処理
炉の操業方法が採用した手段の特徴とするろころは、請
求項7に記載の移動炉床式熱処理炉の操業方法におい
て、前記ケーシング内に吹込む再酸化防止ガスの吹込み
量を、前記被熱処理物の表面温度により制御するところ
にある。
According to the eighth aspect of the present invention, there is provided a method for operating a moving hearth type heat treatment furnace according to claim 7, wherein the roller is characterized by a means adopted by the method for operating a moving hearth type heat treatment furnace. The amount of the reoxidation preventing gas blown into the casing is controlled by the surface temperature of the object to be heat treated.

【0018】本発明の請求項9に係る移動炉床式熱処理
炉の操業方法が採用した手段の特徴とするろころは、請
求項5乃至8のうちの何れか一つの項に記載の移動炉床
式熱処理炉の操業方法において、前記スクレーパーの単
位時間当たりの往復動数を調整することにより被熱処理
物の排出量を制御するところにある。
According to a ninth aspect of the present invention, there is provided a roller equipped with the method of operating the moving hearth type heat treatment furnace according to any one of the fifth to eighth aspects. In the operation method of the floor-type heat treatment furnace, the discharge amount of the heat treatment target is controlled by adjusting the number of reciprocations of the scraper per unit time.

【0019】[0019]

【発明の実施の形態】以下、本発明の移動炉床式熱処理
炉の操業方法を実施する実施の形態に係る移動炉床式熱
処理炉としての移動炉床式還元炉の排出装置を、その模
式的全体斜視図の図1と、そのホッパー付ケーシングの
模式的縦断断面図の図2と、そのスクレーパーの作動説
明図の図3とを順次参照しながら説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a discharge apparatus of a moving hearth type reduction furnace as a moving hearth type heat treating furnace according to an embodiment for carrying out a method of operating a moving hearth type heat treating furnace of the present invention will be described. FIG. 1 of the overall perspective view of the target, FIG. 2 of a schematic longitudinal sectional view of the casing with the hopper, and FIG. 3 of the operation explanatory view of the scraper will be described in order.

【0020】先ず、図1に示す符号1は、垂直軸心を回
転中心として回転する円形状の、図示しない炉床を有す
る移動炉床式還元炉である。この移動炉床式還元炉1の
外周部側面には、図示しない投入装置により炉床上に投
入された原料を、この炉床が垂直軸心を回転中心として
1回転する間に熱処理されたもの、つまり還元された被
熱処理物(再酸化性の高い還元鉄または再酸化の問題の
ない金属鉄)または炭素質粉、スラグ混合物を排出する
排出口11が設けられており、前記被熱処理はこの排出
口11から、後述する構成になる排出装置2に排出され
るように構成されている。なお、図示省略しているが、
前記排出口11から前記排出装置2には、気密可能な筒
状の排出シュートが連通している。
First, reference numeral 1 shown in FIG. 1 is a moving hearth type reduction furnace having a circular hearth, not shown, which rotates around a vertical axis. On the outer peripheral side surface of the moving hearth-type reduction furnace 1, a raw material charged on the hearth by a charging device (not shown) is heat-treated while the hearth makes one rotation around a vertical axis, That is, a discharge port 11 for discharging the reduced heat-treated material (reduced iron having high reoxidation property or metallic iron having no reoxidation problem), carbonaceous powder, and slag mixture is provided. It is configured to be discharged from the outlet 11 to a discharge device 2 having a configuration described later. Although not shown,
An airtight cylindrical discharge chute communicates with the discharge device 2 from the discharge port 11.

【0021】前記排出装置2は、前記排出口11から排
出された被熱処理物の中から、例えば耐火物、ペレット
が付着し合った塊状物、剥離した炉床、原料装入時の異
物等の種々の異物を系外に排出する、複数本の回転ロー
ル31が平行に配設されると共に、図示しない気密ケー
シング内に収容されてなる、ローラスクリーンとも呼ば
れるスクリーンサイザー3を備えている。このスクリー
ンサイザー3により異物が除去された被熱処理物を下方
に導くマテリアルシール機能を有する筒状のシ−ルレグ
4を備えると共に、このシ−ルレグ4の下端が、再酸化
し易い還元鉄の場合には再酸化を防止する再酸化防止ガ
ス、例えば窒素ガス等の不活性ガス、または酸化性ガス
を含まない排ガス等を吹込む複数(この例では2本であ
る。)のガス吹込みノズル6(図2参照。)を備えると
共に、後述する構成、かつ機能を有する定量排出装置7
を有し、下部にホッパー部51を備えたホッパー付ケー
シング5に気密可能に貫通している。
The discharge device 2 includes, for example, refractories, lumps having pellets adhered thereto, exfoliated hearths, and foreign matter when charging raw materials, among the heat-treated materials discharged from the discharge port 11. A plurality of rotating rolls 31 for discharging various foreign substances out of the system are provided in parallel with each other, and include a screen sizer 3 called a roller screen, which is housed in an airtight casing (not shown). A cylindrical seal leg 4 having a material sealing function for guiding a heat-treated material from which foreign matters have been removed by the screen sizer 3 downward, and a lower end of the seal leg 4 is made of reduced iron which is easily reoxidized. Is a plurality (two in this example) of gas injection nozzles 6 for blowing a reoxidation preventing gas for preventing reoxidation, for example, an inert gas such as a nitrogen gas, or an exhaust gas containing no oxidizing gas. (See FIG. 2), and a fixed-quantity discharge device 7 having a configuration and a function to be described later.
And penetrates airtightly through a hopper-equipped casing 5 having a hopper section 51 at the bottom.

【0022】なお、前記シールレグ4の形状は円筒状で
あるが、マテリアルシール機能を有していればこの形状
に限定されるものではなく、例えば角筒状であっても良
い。また、前記ガス吹込みノズル6は、図2に示すよう
に、前記シ−ルレグ4の前記ホッパー付ケーシング5内
に突出する部位に連通させてあるが、この構成に限るも
のではなく、このシ−ルレグ4の前記ホッパー付ケーシ
ング5外であっても良い。つまり、前記シ−ルレグ4へ
の前記ガス吹込みノズル6の連通位置は、前記移動炉床
式還元炉1の炉内圧保持メインテナンス性等を考慮して
決定すれば良いものである。
Although the shape of the seal leg 4 is cylindrical, it is not limited to this shape as long as it has a material sealing function. For example, the shape may be a rectangular tube. As shown in FIG. 2, the gas injection nozzle 6 communicates with a portion of the seal leg 4 projecting into the casing 5 with the hopper. However, the present invention is not limited to this configuration. -It may be outside the casing 5 with the hopper of the leg leg 4. In other words, the communication position of the gas injection nozzle 6 to the seal leg 4 may be determined in consideration of the maintenance performance of the moving hearth type reduction furnace 1 in the furnace pressure and the like.

【0023】前記定量排出装置7は、図1乃至3に示す
ように構成されている。即ち、上側に受入れ凹所71a
が形成されるように平板が湾曲形成され、前記シ−ルレ
グ4から排出される被熱処理物を受入れて一時的に保持
する凹状保持部材である受けパン71を備えている。ま
た、この受けパン71の湾曲面に沿うように往復動、つ
まりスイングされ、前記受けパン71に受入れられてい
る被熱処理物を、その両側外方に排出する機能を有する
横長平板状のスクレーパー72を備えている。前記スク
レーパー72の端部のそれぞれには、上端が前記ホッパ
ー付ケーシング5の端面を貫通する回動軸74に固着さ
れたスイングアーム73の下端が固着されており、前記
回動軸74は回動軸作動シリンダー75のロッドの伸縮
作動により回動されるように構成されている。勿論、前
記受けパン71の幅方向の端部は、前記ホッパー付ケー
シング5の内壁、または平行、かつ垂直な2枚の壁板に
固着され、この受けパン71の幅方向に被熱処理物が零
れ落ちることがないように配慮されている。
The quantitative discharge device 7 is configured as shown in FIGS. That is, the receiving recess 71a
And a receiving pan 71 which is a concave holding member for receiving and temporarily holding the object to be heat-treated discharged from the seal leg 4. Also, a horizontally long flat scraper 72 having a function of reciprocating, that is, swinging along the curved surface of the receiving pan 71 and discharging the object to be heat-treated received in the receiving pan 71 outward on both sides thereof. It has. At each end of the scraper 72, a lower end of a swing arm 73 whose upper end is fixed to a rotating shaft 74 that penetrates the end surface of the casing 5 with the hopper is fixed, and the rotating shaft 74 rotates. It is configured to be rotated by the expansion and contraction operation of the rod of the shaft operation cylinder 75. Of course, the end in the width direction of the receiving pan 71 is fixed to the inner wall of the casing 5 with the hopper or two parallel and vertical wall plates, and the object to be heat-treated spills in the width direction of the receiving pan 71. Care is taken not to fall.

【0024】なお、前記回動軸作動シリンダー75は、
油圧、空圧、電動駆動等の何れの駆動源によるものであ
っても良い。また、前記回動軸74の先端部にピニオン
を外嵌すると共に、前記回動軸作動シリンダー75のロ
ッドの先端に、前記ピニオンに噛合するラックを取付
け、このラックを往復動させることにより、前記回動軸
74を回動させて前記スクレーパー72をスイングさる
構成にしても、前記回動軸作動シリンダー75と同等の
機能を発揮させることができるから、上記スイング構成
に限定されるものではない。
Incidentally, the rotating shaft operating cylinder 75 includes:
It may be driven by any drive source such as hydraulic, pneumatic, and electric drive. In addition, a pinion is externally fitted to the tip of the rotating shaft 74, and a rack that meshes with the pinion is attached to the tip of the rod of the rotating shaft operating cylinder 75, and the rack is reciprocated, whereby the rack is reciprocated. Even if the scraper 72 is swung by rotating the rotating shaft 74, the same function as the rotating shaft operating cylinder 75 can be exerted, and the present invention is not limited to the swing configuration.

【0025】前記スクレーパー72は、上記のとおり、
被熱処理物を前記受けパン71の両側外方に排出する機
能を有しているので、被熱処理物または異物等のサイズ
がシールレグ4を通過し得る範囲の大きさである場合に
は、大塊の被熱処理物であっても、前記排出装置2のみ
により問題なく排出することが可能であるため、必ずし
も前記スクリーンサイザー3を設ける必要がないもので
ある。但し、特に排出口11から高頻度で大塊の被熱処
理物が排出される場合は、スクリーンサイザー3を設け
ることにより大塊の被熱処理物を除去することができる
ので、スクレーパー72を円滑にスイング作動させるこ
とが可能になるという効果が生じる。
The scraper 72 is, as described above,
Since it has a function of discharging the object to be heat-treated to the outside of both sides of the receiving pan 71, if the size of the object to be heat-treated or a foreign substance is large enough to pass through the seal leg 4, the large mass It is not necessary to necessarily provide the screen sizer 3 because the heat treatment target can be discharged without any problem only by the discharge device 2. However, especially when a large lump of the heat-treated substance is discharged from the discharge port 11 at a high frequency, the large lump of the heat-treated substance can be removed by providing the screen sizer 3, so that the scraper 72 can be smoothly swung. This has the effect that it can be activated.

【0026】そして、前記ホッパー付ケーシング5のホ
ッパー部51の下部排出口52から定量ずつ排出された
被熱処理物は、図示しない下流側設備に送られるように
構成されている。ところで、前記スクレーパー72のス
イング作動を停止させることにより、受けパン71やシ
ールレグ4またはホッパー部51中に被熱処理物を滞留
させることができるので、例えば下流設備や上流の移動
炉床式還元炉が緊急停止したとしても、ある程度のバッ
ファー機能を発揮することができる。
The heat-treated material discharged from the lower discharge port 52 of the hopper section 51 of the hopper-equipped casing 5 is sent to a downstream facility (not shown). By stopping the swing operation of the scraper 72, the heat treatment target can be retained in the receiving pan 71, the seal leg 4, or the hopper portion 51. Even if an emergency stop is performed, a certain buffer function can be exhibited.

【0027】以下、上記構成になる移動炉床式還元炉1
の排出装置2の作用態様を説明すると、炉床上において
熱処理された被熱処理物を排出口11から排出するに際
しては、先ず移動炉床式還元炉1からの高熱ガスの流出
を防止し、被熱処理物の再酸化を防止するために、ガス
吹込ノズル6からホッパー付きケーシング5内に窒素ガ
ス等の不活性ガスや酸化性ガスを含まない排ガス等の再
酸化防止ガスが吹込まれると共に、排出口11から被熱
処理物の排出が開始される。再酸化防止ガスの吹込量
は、被熱処理物の温度の高低によって加減制御、つま
り、被熱処理物の温度が高温であれば大量の再酸化防止
ガスが吹込まれる一方、被熱処理物の温度が低温であれ
ば少量の再酸化防止ガスが吹込まれる。
Hereinafter, the moving hearth type reduction furnace 1 having the above-described structure will be described.
When the operation of the discharge device 2 is described, when the heat-treated material that has been heat-treated on the hearth is discharged from the discharge port 11, first, the outflow of high-temperature gas from the moving hearth-type reduction furnace 1 is prevented, and the heat-treatment is performed. In order to prevent re-oxidation of the material, a re-oxidation preventing gas such as an inert gas such as a nitrogen gas or an exhaust gas not containing an oxidizing gas is blown into the casing 5 with a hopper from the gas injection nozzle 6 and a discharge port. From 11, the discharge of the heat treatment target is started. The blowing amount of the reoxidation preventing gas is controlled by the level of the temperature of the object to be heat treated.In other words, if the temperature of the object to be heat treated is high, a large amount of the antioxidant gas is blown, while the temperature of the object to be heat treated is If the temperature is low, a small amount of antioxidant gas is blown.

【0028】前記排出口12から排出された被熱処理物
は、スクリーンサイザー3により大塊の異物が除去さ
れ、所定以下の粒径の被熱処理物だけが再酸化防止ガス
が吹き込まれている筒状のシ−ルレグ4内に移動し、マ
テリアルシール機能により移動炉床式還元炉1からのガ
スの流出を防止し、そして外気等の酸化性ガスを含む下
流側ガスの流入を防止しながら、このシ−ルレグ4内を
下降してホッパー付ケーシング5内の受けパン71の受
入れ凹所71aの上面に落下し、安息角に応じて受入れ
凹所71aの上面に堆積して一時的に保持される。
The heat-treated material discharged from the discharge port 12 is removed by the screen sizer 3 to remove a large amount of foreign matter. Of the moving hearth-type reduction furnace 1 by the material sealing function, and the inflow of the downstream gas including the oxidizing gas such as the outside air. It descends in the seal leg 4, falls on the upper surface of the receiving recess 71a of the receiving pan 71 in the casing 5 with a hopper, and accumulates on the upper surface of the receiving recess 71a according to the angle of repose and is temporarily held. .

【0029】ところで、本実施の形態では、上記のとお
り、被熱処理物が再酸化し易い還元鉄等である場合に
は、ガス吹込ノズル6から窒素ガス等の不活性ガスや酸
化性ガスを含まない排ガス等の再酸化防止ガスが吹込ま
れるが、例えばこれら窒素ガスなどの不活性ガスや酸化
性ガスを含まない排ガス等の代わりに還元性ガスである
炭化水素系ガス、例えば天然ガスを吹込むことができ
る。ガス吹込ノズル6から天然ガスを吹込むことによっ
て、シ−ルレグ4やホッパー付ケーシング5内の被熱処
理物のうち、高温の還元鉄の再酸化による金属化率の低
下を防止することが可能になると共に、還元鉄や金属鉄
の温度が高温であるほど吸熱反応である分解反応が促進
されるから、自己制御的、かつ簡易的に還元鉄や金属鉄
の表面温度を制御することができ、さらに分解反応によ
り還元鉄や金属鉄の表面付近にカーボンが生じるので、
これら還元鉄や金属鉄同志の固着をより効果的に防止す
ることが可能になるという効果が生じる。
In the present embodiment, as described above, when the heat treatment target is reduced iron or the like which is easily reoxidized, the gas injection nozzle 6 contains an inert gas such as nitrogen gas or an oxidizing gas. A reoxidation preventing gas such as exhaust gas is blown, but a hydrocarbon-based gas that is a reducing gas, such as natural gas, is blown instead of an inert gas such as nitrogen gas or an exhaust gas containing no oxidizing gas. Can be included. By injecting natural gas from the gas injection nozzle 6, it is possible to prevent a reduction in the metallization rate due to the reoxidation of high-temperature reduced iron among the heat-treated materials in the seal leg 4 and the casing 5 with the hopper. At the same time, the higher the temperature of reduced iron or metallic iron, the more the endothermic decomposition reaction is promoted, so that the surface temperature of reduced iron or metallic iron can be controlled in a self-regulating and simple manner, In addition, carbon is generated near the surface of reduced iron and metallic iron by the decomposition reaction,
There is an effect that it is possible to more effectively prevent the reduced iron and metallic iron from sticking together.

【0030】また、移動炉床式還元炉1から異常に高温
の被熱処理物が排出された場合、受けパン71の受入れ
凹所71aの上面に堆積する被熱処理物の表面温度、ま
たはスクリーンサイザー3、シールレグ4、およびスク
レーパー72、またはそれら相互を結合するシュート等
の鉄皮の表面温度の高低に応じて、ガス吹込みノズル6
からの再酸化防止ガスの吹込み量を制御して緊急冷却す
ることにより、被熱処理物の再酸化を防止することがで
きる。
When an abnormally high temperature heat-treated material is discharged from the moving hearth type reduction furnace 1, the surface temperature of the heat-treated material deposited on the upper surface of the receiving recess 71a of the receiving pan 71 or the screen sizer 3 The gas injection nozzle 6 according to the level of the surface temperature of the shell such as the seal leg 4, the scraper 72, or the chute connecting them, or the like.
By performing the emergency cooling by controlling the amount of the reoxidation preventing gas to be blown, the reoxidation of the heat treatment target can be prevented.

【0031】また、移動炉床式還元炉1から異常に高温
の被熱処理物が排出された場合や高温の被熱処理物が排
出装置2内に長時間滞留する場合には、上記のような再
酸化防止ガスの吹込みによる被熱処理物の冷却、再酸化
防止に加えて、スクリーンサイザー3、シールレグ4、
およびスクレーパー72等に粉状炭素質材または石灰系
物質を供給することにより、被熱処理物である還元鉄や
金属鉄同志の固着を防止することができる。
When an abnormally high-temperature heat-treated material is discharged from the moving hearth-type reduction furnace 1 or when the high-temperature heat-treated material stays in the discharge device 2 for a long time, the above-mentioned reheating is performed. In addition to cooling the object to be heat treated and preventing re-oxidation by blowing the antioxidant gas, the screen sizer 3, the seal leg 4,
By supplying the powdery carbonaceous material or the lime-based material to the scraper 72 and the like, it is possible to prevent reduced iron or metallic iron, which is a heat treatment target, from sticking together.

【0032】次いで、スクレーパー72の回動速度を制
御して、前記受けパン71の上に一時的に保持されてい
る被熱処理物を、この受けパン71の長手方向の両端部
からホッパー付ケーシング5内に排出する。その場合、
スクレーパー72の回動速度を、シールレグ4、または
受けパン71の受入れ凹所71aの上面における被熱処
理物の堆積レベルにより制御してもよいし、その堆積重
量、またはその重量変化によって制御しても構わないも
のである。このようにしてホッパー付ケーシング5内に
排出された被熱処理物は、このホッパー付ケーシング5
のホッパー部51を滑落または転がり落ちて下部排出口
52から下流側設備に供給され、下流側設備において然
るべき処理が施されることとなる。
Next, by controlling the rotation speed of the scraper 72, the heat-treated object temporarily held on the receiving pan 71 is removed from both ends of the receiving pan 71 in the longitudinal direction. Drain into. In that case,
The rotation speed of the scraper 72 may be controlled by the accumulation level of the heat treatment target on the seal leg 4 or the upper surface of the receiving recess 71a of the receiving pan 71, or may be controlled by the accumulation weight or the change in the weight. It doesn't matter. The object to be heat-treated discharged into the casing 5 with the hopper in this manner is the casing 5 with the hopper.
The hopper portion 51 slides down or rolls down and is supplied from the lower discharge port 52 to the downstream equipment, so that appropriate processing is performed in the downstream equipment.

【0033】なお、受けパン71の受入れ凹所71aの
上面における被熱処理物の堆積レベルの測定方法につい
ては、特に制限がないけれども、非接触式で被熱処理物
の堆積レベルを測定する構成にすることが好ましい。例
えば、シールレグ4、またはホッパー付ケーシング5の
外壁面に非接触式のガンマ線レベル計を付設することが
考えられる。また、ロードセルやマイクロ波、静電容量
式の測定装置等の採用も考えられる。
The method of measuring the deposition level of the object to be heat-treated on the upper surface of the receiving recess 71a of the receiving pan 71 is not particularly limited, but is configured to measure the deposition level of the object to be heat-treated in a non-contact manner. Is preferred. For example, it is conceivable to provide a non-contact gamma ray level meter on the outer surface of the seal leg 4 or the casing 5 with the hopper. It is also conceivable to employ a load cell, a microwave, a capacitance type measuring device, or the like.

【0034】以上詳述したように、本実施の形態に係る
移動炉床式還元炉1の排出装置2によれば、受けパン7
1とスクレーパー72とは、極めて簡単な構造であるた
め、耐高温性の素材だけで構成することができる。ま
た、受けパン71とスクレーパー72やスクリーンサイ
ザー3の回転ロール31を2重筒状の水冷構成にするこ
とにより耐熱性を向上させて、排出される還元鉄、炭素
質粉とスラグとの混合物の温度条件に対応することもで
きる。さらに、前記回動軸74および図示しない駆動部
は、図1,2から良く理解されるように、被熱処理物に
接触するようなことがない。
As described in detail above, according to the discharge device 2 of the moving hearth type reduction furnace 1 according to the present embodiment, the receiving pan 7
Since 1 and the scraper 72 have a very simple structure, they can be composed only of a high temperature resistant material. The heat resistance is improved by forming the receiving pan 71, the scraper 72 and the rotating roll 31 of the screen sizer 3 into a double cylindrical water-cooled structure, so that the mixture of the discharged reduced iron, the carbonaceous powder and the slag is formed. It can also respond to temperature conditions. Further, the rotating shaft 74 and the driving unit (not shown) do not come into contact with the object to be heat treated, as is well understood from FIGS.

【0035】従って、本実施の形態に係る移動炉床式還
元炉1の排出装置2は、上記従来例1や2に係る移動炉
床式還元炉の排出装置と異なり、高温開閉弁を備えてい
ないからトラブルの発生が少なく、安定操業の継続が容
易である。また、高温開閉弁によらず、スクレーパー7
2の回動により排出する構成であって、被熱処理物を連
続的に排出することができるから、例え下流側に溶解炉
が設置されている場合であっても、還元鉄または金属鉄
を連続溶解することができ、鉄製品の生産性の向上に大
いに寄与することができる。
Therefore, the discharge device 2 of the mobile hearth type reduction furnace 1 according to the present embodiment is different from the discharge device of the mobile hearth type reduction furnace according to the prior arts 1 and 2 in that it has a high-temperature open / close valve. Since there is no trouble, there is little trouble, and stable operation can be easily continued. Also, regardless of the high-temperature on-off valve, the scraper 7
Since the object to be heat-treated can be continuously discharged, the reduced iron or metallic iron can be continuously discharged even if a melting furnace is installed on the downstream side. It can be dissolved and can greatly contribute to the improvement of productivity of iron products.

【0036】また、本実施の形態に係る移動炉床式還元
炉1の排出装置2は、上記従来例2、3に係る移動炉床
式還元炉の排出装置と異なり、シールレグ4におけるマ
テリアルシール機能と、再酸化防止ガスとにより移動炉
床式還元炉1内への外気等の酸化性ガスの流入を遮断す
ることができ、例え移動炉床式還元炉1を負圧で操業す
る場合でも、移動炉床式還元炉1内に酸化性ガスが流入
するような恐れが少ないから、還元された還元鉄の酸化
による製品価値の低下、酸化時の熱による還元鉄の溶融
に起因する融着や、炭素質粉の燃焼による問題が生じる
ような恐れを少なくすることができる。
The discharge device 2 of the movable hearth type reduction furnace 1 according to the present embodiment is different from the discharge device of the mobile hearth type reduction furnace according to the conventional examples 2 and 3 in that the material sealing function in the seal leg 4 is provided. And the reoxidation preventing gas, it is possible to cut off the flow of oxidizing gas such as outside air into the moving hearth type reducing furnace 1. Even when the moving hearth type reducing furnace 1 is operated at a negative pressure, Since there is little possibility that an oxidizing gas flows into the moving hearth-type reduction furnace 1, a reduction in the product value due to oxidation of the reduced reduced iron, fusion due to melting of the reduced iron due to heat during the oxidation, In addition, it is possible to reduce the risk that a problem due to the burning of the carbonaceous powder occurs.

【0037】上記従来例3に係る移動炉床式還元炉の排
出装置では、振動フィーダー、スクリュコンベヤ、また
はパンコンベヤ等に耐高温性、気密性に問題があった
が、本実施の形態に係る移動炉床式還元炉1の排出装置
2は、上記のとおり、受けパン71とスクレーパー72
やスクリーンサイザー3の回転ロール31を2重筒状の
水冷等の冷却手段を備えた構成にすることにより耐熱性
を向上させて、排出される被熱処理物の温度条件に対応
することができるのに加えて、前記回動軸74は被熱処
理物の排出中に、この被熱処理物に接触するようなこと
がない。
In the discharge device of the moving hearth type reduction furnace according to the conventional example 3, the vibration feeder, the screw conveyor, the pan conveyor and the like had problems in high temperature resistance and airtightness. As described above, the discharge device 2 of the moving hearth type reduction furnace 1 includes the receiving pan 71 and the scraper 72.
In addition, the heat resistance can be improved by providing the rotating roll 31 of the screen sizer 3 with a cooling means such as water cooling in a double cylindrical shape, so that it is possible to cope with the temperature conditions of the discharged heat treatment target. In addition, the rotating shaft 74 does not come into contact with the object to be heat-treated while the object is being discharged.

【0038】さらに、スクレーパー72は、従来例3に
係る排出装置のスクリュコンベヤのスクリュシャフトの
場合と同様に、被熱処理物に直接接触するが、板状であ
ってスクリュシャフトに比較して遙にその構造が簡単で
あり、しかも接触圧も低く摩耗量も少ないから、耐熱性
の問題や摩耗による消耗が少なく、排出装置2のメンテ
ナンスコストに関して有利になるという優れた経済効果
がある。
Further, the scraper 72 is in direct contact with the object to be heat-treated, as in the case of the screw shaft of the screw conveyor of the discharging device according to the conventional example 3, but it is plate-shaped and is far more than the screw shaft. Since the structure is simple, the contact pressure is low, and the amount of wear is small, the problem of heat resistance and wear due to wear are small, and there is an excellent economic effect that the maintenance cost of the discharge device 2 is advantageous.

【0039】なお、以上では、被熱処理物として、再酸
化性の高い還元鉄または再酸化の問題のない金属鉄、炭
素質粉、スラグ混合物等を排出する移動炉床式還元炉1
を例として説明した。しかしながら、再酸化性が高い高
温還元鉄の排出だけでなく、再酸化性が比較的低い金属
鉄や実質的に再酸化の問題がない高純度の金属鉄または
非鉄金属等を含有する熱処理された金属含有物の排出に
対しても、本発明の技術的思想を適用することができる
ので、上記実施の形態によって、本発明の技術的思想の
適用範囲が限定されるものではなく、また本発明の技術
的思想を逸脱しない範囲内における設計変更等は自由自
在である。
In the above, the moving hearth-type reduction furnace 1 for discharging reduced iron having a high reoxidation property or metallic iron, carbonaceous powder, slag mixture or the like having no reoxidation problem as the heat treatment target.
Has been described as an example. However, not only high-temperature reducible high-temperature reduced iron emission but also heat treatment containing relatively low-reoxidation metallic iron or high-purity metallic iron or non-ferrous metal having substantially no reoxidation problem was performed. Since the technical idea of the present invention can be applied to the discharge of metal-containing materials, the scope of the technical idea of the present invention is not limited by the above-described embodiment. The design can be freely changed without departing from the technical concept of the present invention.

【0040】[0040]

【発明の効果】以上詳述したように、本発明の請求項1
乃至4に係る移動炉床式熱処理炉の排出装置、本発明の
請求項5乃至9に係る移動炉床式熱処理炉の操業方法に
よれば、従来例1または2に係る移動炉床式熱処理炉の
排出装置のように、高温開閉弁を備えていないから、安
定操業の継続が可能になる。また、被熱処理物の排出は
スクレーパーの往復動により行われるため、高温開閉弁
の場合よりも断続間隔が短く、より連続に近い状態で下
流側の溶解炉に供給することができるから、従来例1ま
たは2に係る移動炉床式熱処理炉の排出装置の場合より
も、安定操業の継続が可能であるから還元鉄または金属
鉄の生産性が優れている。
As described in detail above, claim 1 of the present invention
According to the moving hearth type heat treatment furnace discharge apparatus according to any one of claims 1 to 4, the moving hearth type heat treatment furnace according to the first or second conventional example, Unlike the discharge device of the above, since it does not have a high-temperature on-off valve, stable operation can be continued. Further, since the discharge of the heat-treating object is performed by reciprocating movement of the scraper, the intermittent interval is shorter than in the case of the high-temperature on-off valve, and it can be supplied to the downstream melting furnace in a more continuous state. Since the stable operation can be continued, the productivity of reduced iron or metallic iron is superior to the case of the discharge apparatus of the moving hearth type heat treatment furnace according to 1 or 2.

【0041】また、シールレグによるマテリアルシール
機能と、排出装置内への再酸化防止ガスの吹込みにより
移動炉床式熱処理炉内への空気の流入を遮断する構成
で、上記従来例2に係る移動炉床式熱処理炉の排出装置
にように、移動炉床式熱処理炉と取外し式密閉容器との
間にシュートが配設されてなる構成でなく、例え移動炉
床式熱処理炉を負圧で操業する場合であっても、移動炉
床式熱処理炉内に外気等の酸化性ガスが流入する恐れが
少なくなるから、還元鉄が再酸化することがなく、酸化
時の熱により還元鉄が溶融して融着したり、炭素質粉が
燃焼する等の問題が生じることがないから、品質が優れ
た製品を製造することができる。
Further, the material according to the second conventional example has a material sealing function by a seal leg and a structure in which air is prevented from flowing into the moving hearth type heat treatment furnace by blowing reoxidation preventing gas into the discharging device. Unlike a discharge device of a hearth-type heat treatment furnace, a chute is provided between the moving hearth-type heat treatment furnace and the detachable closed vessel, but the mobile hearth-type heat treatment furnace operates at a negative pressure. Even in the case where the oxidizing gas such as outside air flows into the moving hearth type heat treatment furnace, the reduced iron does not re-oxidize, Thus, there is no problem such as fusing or burning of the carbonaceous powder, so that it is possible to manufacture a product having excellent quality.

【0042】また、スクレーパーが、従来例3に係る排
出装置のスクリュコンベヤのスクリュシャフトと同様に
被熱処理物に直接接触するが、板状であってスクリュシ
ャフトに比較して遙にその構造が簡単であり、しかも接
触圧も低く摩耗量も少ないから、従来例3に係る排出装
置のスクリュコンベヤに比較して、メンテナンスコスト
が遙に安価になるという優れた経済効果がある。
The scraper is in direct contact with the object to be heat-treated in the same manner as the screw shaft of the screw conveyor of the discharging device according to the prior art 3, but the plate shape is much simpler than that of the screw shaft. In addition, since the contact pressure is low and the amount of wear is small, there is an excellent economic effect that the maintenance cost is much lower than that of the screw conveyor of the discharging device according to the conventional example 3.

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

【図1】本発明の移動炉床式還元炉の操業方法を実施す
る実施の形態に係る移動炉床式還元炉の排出装置の模式
的全体斜視図である。
FIG. 1 is a schematic overall perspective view of a discharge device of a moving hearth type reduction furnace according to an embodiment for carrying out a method for operating a moving hearth type reducing furnace of the present invention.

【図2】本発明の実施の形態に係る移動炉床式還元炉の
排出装置のホッパー付ケーシングの模式的縦断断面図で
ある。
FIG. 2 is a schematic longitudinal sectional view of a casing with a hopper of the discharge device of the moving hearth-type reduction furnace according to the embodiment of the present invention.

【図3】本発明の実施の形態に係る移動炉床式還元炉の
排出装置のスクレーパーの作動説明図である。
FIG. 3 is an operation explanatory view of a scraper of the discharge device of the moving hearth type reduction furnace according to the embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…移動炉床式還元炉,11排出口 2…排出装置 3…スクリーンサイザー,31…回転ロール 4…シールレグ 5…ホッパー付ケーシング,51…ホッパー部,52…
下部排出口 6…不活性ガス吹込ノズル 7…定量排出装置,71…受けパン,71a…受入れ凹
所,72…スクレーパー,73…スイングアーム,74
…回動軸,75…回動軸作動シリンダー
DESCRIPTION OF SYMBOLS 1 ... Moving hearth type reduction furnace, 11 discharge ports 2 ... Discharge device 3 ... Screen sizer, 31 ... Rotating roll 4 ... Seal leg 5 ... Casing with hopper, 51 ... Hopper part, 52 ...
Lower discharge port 6 ... Inert gas injection nozzle 7 ... Quantitative discharge device, 71 ... Receiving pan, 71a ... Receiving recess, 72 ... Scraper, 73 ... Swing arm, 74
... Rotating shaft, 75 ... Rotating shaft operating cylinder

───────────────────────────────────────────────────── フロントページの続き (72)発明者 内田 利克 大阪府大阪市中央区備後町4丁目1番3号 株式会社神戸製鋼所大阪支社内 (72)発明者 橋本 澄人 大阪府大阪市中央区備後町4丁目1番3号 株式会社神戸製鋼所大阪支社内 Fターム(参考) 4K012 DE02 4K050 AA07 BA01 CA09 CF12 CG22 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Toshikatsu Uchida 4-3-1 Bingocho, Chuo-ku, Osaka-shi, Osaka Kobe Steel, Ltd. Osaka branch office (72) Inventor Sumito Hashimoto Chuo-ku, Osaka-shi, Osaka 4-1-3 Bingo-cho Kobe Steel, Ltd. Osaka Branch Office F-term (reference) 4K012 DE02 4K050 AA07 BA01 CA09 CF12 CG22

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 移動炉床式熱処理炉から被熱処理物を下
流側設備に排出する移動炉床式熱処理炉の排出装置であ
って、ケーシング内に、前記移動炉床式熱処理炉から排
出された被熱処理物を受入れて一時的に保持する受入れ
凹所を備えた凹状保持部材と、前記受入れ凹所の面に沿
うように往復動して、この受入れ凹所内に保持されてい
る被熱処理物を前記ケーシング内に排出するスクレーパ
ーとを設けたことを特徴とする移動炉床式熱処理炉の排
出装置。
1. A discharge device of a moving hearth type heat treatment furnace for discharging an object to be heat-treated from a moving hearth type heat treatment furnace to downstream equipment, wherein the discharge device is discharged from the moving hearth type heat treatment furnace into a casing. A concave holding member having a receiving recess for receiving and temporarily holding the object to be heat-treated, and reciprocating along the surface of the receiving recess to move the object to be heat-treated held in the receiving recess. A discharge device for a moving hearth type heat treatment furnace, further comprising a scraper for discharging into the casing.
【請求項2】 前記移動炉床式熱処理炉と前記凹状保持
部材との間に、前記移動炉床式熱処理炉から排出された
被熱処理物を前記凹状保持部材の受入れ凹所に導くシ−
ルレグを配設したことを特徴とする請求項1に記載に移
動炉床式熱処理炉の排出装置。
2. A sheet guide between the moving hearth type heat treatment furnace and the concave holding member, the heat treatment object discharged from the moving hearth type heat treating furnace being guided to a receiving recess of the concave holding member.
The discharge device of a moving hearth type heat treatment furnace according to claim 1, wherein a leleg is provided.
【請求項3】 前記ケーシング内に再酸化防止ガスを吹
込むガス吹込みノズルを、前記シールレグに連通させた
ことを特徴とする請求項2に記載に移動炉床式熱処理炉
の排出装置。
3. A discharge apparatus for a moving hearth type heat treatment furnace according to claim 2, wherein a gas injection nozzle for injecting a re-oxidation preventing gas into said casing is communicated with said seal leg.
【請求項4】 前記移動炉床式熱処理炉と前記シ−ルレ
グとの間に、被熱処理物中の異物を選別して系外に排出
するスクリーンサイザーを配設したことを特徴とする請
求項3に記載の移動炉床式熱処理炉の排出装置。
4. A screen sizer is disposed between the moving hearth type heat treatment furnace and the seal leg, for selecting foreign matter in the object to be heat treated and discharging it to the outside of the system. 4. The discharge device of the moving hearth type heat treatment furnace according to 3.
【請求項5】 移動炉床式熱処理炉から被熱処理物を下
流側設備に排出する移動炉床式熱処理炉の操業方法であ
って、前記移動炉床式熱処理炉から排出された被熱処理
物をケーシング内に設けた凹状保持部材の受入れ凹所に
受入れると共に一時的に保持し、前記受入れ凹所の面に
沿うようにスクレーパーを往復動させて、前記受入れ凹
所内に保持されている被熱処理物を前記ケーシング内に
排出することを特徴とする移動炉床式熱処理炉の操業方
法。
5. A method of operating a moving hearth type heat treatment furnace for discharging a heat treatment target from a moving hearth type heat treatment furnace to downstream equipment, comprising: The heat-treating object held in the receiving recess by reciprocating the scraper along the surface of the receiving recess while receiving and temporarily holding the recess in the receiving recess of the concave holding member provided in the casing. The method for operating a moving hearth type heat treatment furnace, comprising discharging the waste gas into the casing.
【請求項6】 前記ケーシング内に、少なくとも被熱処
理物の再酸化を防止する再酸化防止ガスを吹込むことを
特徴とする請求項5に記載の移動炉床式熱処理炉の操業
方法。
6. The method for operating a moving hearth type heat treatment furnace according to claim 5, wherein a reoxidation preventing gas for preventing at least reoxidation of the heat treatment target is blown into the casing.
【請求項7】 前記移動炉床式熱処理炉から排出された
被熱処理物を、前記シ−ルレグ中を通して前記凹状保持
部材の受入れ凹所に受入れることを特徴とする請求項5
または6のうちの何れか一つの項に記載の移動炉床式熱
処理炉の操業方法。
7. The heat treatment object discharged from the moving hearth type heat treatment furnace is received in the receiving recess of the concave holding member through the seal leg.
Or the operation method of the moving hearth type heat treatment furnace according to any one of the above items 6.
【請求項8】 前記ケーシング内に吹込む再酸化防止ガ
スの吹込み量を、前記被熱処理物の表面温度により制御
することを特徴とする請求項7に記載の移動炉床式熱処
理炉の操業方法。
8. The operation of the moving hearth type heat treatment furnace according to claim 7, wherein the amount of the reoxidation preventing gas blown into the casing is controlled by the surface temperature of the heat treatment target. Method.
【請求項9】 前記スクレーパーの単位時間当たりの往
復動数を調整することにより被熱処理物の排出量を制御
することを特徴とする請求項5乃至8のうちの何れか一
つの項に記載の移動炉床式熱処理炉の操業方法。
9. The apparatus according to claim 5, wherein the amount of the heat-treated material discharged is controlled by adjusting the number of reciprocating movements of the scraper per unit time. Operating method of moving hearth type heat treatment furnace.
JP2000348210A 2000-07-31 2000-11-15 Discharge device of moving hearth type heat treatment furnace and method of operating the same Expired - Lifetime JP3583067B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2000348210A JP3583067B2 (en) 2000-11-15 2000-11-15 Discharge device of moving hearth type heat treatment furnace and method of operating the same
US09/916,588 US6669756B2 (en) 2000-07-31 2001-07-30 Discharge apparatus for movable hearth type heat-treatment furnace, its operation method, and method and apparatus for manufacturing molten iron using the same
EP01118269A EP1178276A3 (en) 2000-07-31 2001-07-30 Discharge apparatus for movable hearth type heat-treatment furnace, its operation method, and method and apparatus for manufacturing molten iron using the same
CA002354465A CA2354465A1 (en) 2000-07-31 2001-07-31 Discharge apparatus for movable hearth type heat-treatment furnace, its operation method, and method and apparatus for manufacturing molten iron using the same

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011246758A (en) * 2010-05-26 2011-12-08 Kobe Steel Ltd Device for storing reduced iron
JP2012102929A (en) * 2010-11-09 2012-05-31 Sumitomo Heavy Ind Ltd Solid fuel feeding apparatus
KR101298710B1 (en) * 2011-09-29 2013-08-21 현대제철 주식회사 Treating apparatus for waste gas in sintering machine
KR101455346B1 (en) 2012-09-27 2014-10-27 현대제철 주식회사 Modular discharging devices of activated carbon

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011246758A (en) * 2010-05-26 2011-12-08 Kobe Steel Ltd Device for storing reduced iron
JP2012102929A (en) * 2010-11-09 2012-05-31 Sumitomo Heavy Ind Ltd Solid fuel feeding apparatus
KR101298710B1 (en) * 2011-09-29 2013-08-21 현대제철 주식회사 Treating apparatus for waste gas in sintering machine
KR101455346B1 (en) 2012-09-27 2014-10-27 현대제철 주식회사 Modular discharging devices of activated carbon

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