JPH05112835A - Manufacture of sintered ore - Google Patents
Manufacture of sintered oreInfo
- Publication number
- JPH05112835A JPH05112835A JP12215791A JP12215791A JPH05112835A JP H05112835 A JPH05112835 A JP H05112835A JP 12215791 A JP12215791 A JP 12215791A JP 12215791 A JP12215791 A JP 12215791A JP H05112835 A JPH05112835 A JP H05112835A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- pallet
- sintering
- cylindrical
- ore
- 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.)
- Pending
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は焼結鉱の製造方法に係
り、詳しくは、焼結鉱は一般にドラムミキサで造粒され
た後、ベルトコンベア、給鉱ホッパ等を経由し、装入シ
ュ−トを介して焼結機のパレット上に装入する焼結鉱の
製造方法に係る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing sinter, and more specifically, the sinter is generally granulated by a drum mixer and then charged through a belt conveyor, a feed hopper, etc. The present invention relates to a method for producing a sinter that is charged on a pallet of a sinter machine via a grate.
【0002】[0002]
【従来の技術】焼結鉱を造粒する方法としては、例えば
特公昭43−6256号公報により提案された方法があ
る。この方法は例えばボ−ルミル、ロッドミルその他の
潤式磨砕機にて原料の摩砕、水分の調整、混練を行なっ
た後、竪型、円筒型等の造粒機により生ペレットを造粒
するものである。2. Description of the Related Art As a method for granulating sinter, there is, for example, the method proposed in Japanese Patent Publication No. 43-6256. This method is, for example, a method in which raw materials are ground with a ball mill, rod mill or other moisturizing grinder, water content is adjusted, and kneading is performed, and then raw pellets are granulated with a vertical or cylindrical granulator. Is.
【0003】この方法によれば他の原料とドラムミキサ
で混合造粒することができるが、この際に凝似粒子に崩
壊を生じ、単にドラムミキサを経由した原料粒子と同様
な程度のものしか得ることができない。また、この粒子
は輸送途中でも崩壊を生じ造粒後のベルト乗り継ぎ部や
給鉱ホッパ内で凝似粒子が崩壊するという問題があっ
た。According to this method, other raw materials can be mixed and granulated by the drum mixer, but at this time, the similar particles are disintegrated, and only particles having the same degree as the raw material particles passed through the drum mixer can be obtained. I can't. In addition, there is a problem that the particles collapse during the transportation, and the similar particles collapse in the belt transfer section and the feed hopper after granulation.
【0004】しかし、造粒後の凝似粒子が搬送過程で崩
壊することはある程度仕方がないものと考えられ、その
対策としてB、Cジャンクションの落差減等による崩壊
量を抑える対策以外にほとんど考慮されていない。However, it is considered that it is unavoidable that colloidal particles after granulation collapse in the course of transportation, and as a countermeasure therefor, most of them are considered in addition to the measures for suppressing the amount of collapse due to the reduction of the B and C junction heads. It has not been.
【0005】[0005]
【発明が解決しようとする課題】本発明は上記問題の解
決を目的とし、具体的には、ドラムフィ−ダ−から原料
切出しを受け、その直下に設けた造粒機により装入直前
に造粒し、崩壊等を生じないようにした焼結鉱の製造方
法を提案することを目的とする。SUMMARY OF THE INVENTION The present invention is intended to solve the above problems. Specifically, the raw material is cut out from a drum feeder and granulated by a granulator provided immediately below the granulator immediately before charging. However, it is an object of the present invention to propose a method for producing a sintered ore that does not cause collapse or the like.
【0006】[0006]
【課題を解決するための手段】すなわち、本発明は焼結
鉱を製造する際に、焼結機の給鉱シュ−ト上に多数の円
筒状若しくは半割円筒状の構造物を並列に配置すると共
に、この構造物に円振動を与える振動造粒機を設け、次
いで、前記焼結機の給鉱ホッパから切出される焼結原料
に加振力3〜10g(gは重力の加速度)を与えて凝似
粒子化を図ると共に、この凝似粒子化を直接若しくはシ
ュ−トを介してパレット上に装入することを特徴とす
る。That is, according to the present invention, when manufacturing a sintered ore, a large number of cylindrical or half-cylindrical structures are arranged in parallel on a feed ore sew of a sintering machine. At the same time, a vibrating granulator that gives circular vibration to this structure is provided, and then a vibrating force of 3 to 10 g (g is the acceleration of gravity) is applied to the sintering raw material cut out from the feed hopper of the sintering machine. It is characterized in that the particles are given to make them into similar particles, and that the similar particles are directly or via a shoe charged on a pallet.
【0007】[0007]
【作用】以下、図面により本発明を詳しく説明すると、
次の通りである。The present invention will be described in detail below with reference to the drawings.
It is as follows.
【0008】図1は本発明を実施する際に用いられる全
体のフロ−を示す配置図であり、図2は給鉱部の概要の
説明図であり、図3は排出端から造粒原料を排出する状
況の説明図であり、図4(a)、(b)ならびに(c)
はそれぞれ図2の造粒機の実施例の一例を示す斜視図で
ある。符号1は鉄鉱石、2は石灰石、3はミルスケ−
ル、4は転炉滓、5は電気炉滓、6は副原滓、7は返
鉱、8は生石灰、9は原料、10は粉コ−クス、11は
配合原料、12は1次ミキサ−、13は2次ミキサ−、
14は装入原料、15は焼結機、16はパレット、17
は給鉱装置、18はホッパ−、19はドラムフィ−ダ
−、20は造粒機、20aはスロ−ピングシュ−ト、2
0bは振動機、20cはカットオフゲ−ト、21は原料
層、22はウィンドボックス、23は排風支管、24は
排出ダクト、25はメインブロア−、30は微粉鉄鉱石
槽、35は焼結原料、36は床敷鉱を示す。FIG. 1 is a layout view showing an entire flow used when carrying out the present invention, FIG. 2 is an explanatory view of an outline of a mining section, and FIG. 3 is a view showing a granulation raw material from a discharge end. It is explanatory drawing of the situation which discharges, FIG.4 (a), (b) and (c)
FIG. 3 is a perspective view showing an example of the embodiment of the granulator of FIG. 2 respectively. Reference numeral 1 is iron ore, 2 is limestone, and 3 is a mill scale.
4, 4 converter slag, 5 electric furnace slag, 6 secondary raw slag, 7 return ore, 8 quicklime, 9 raw material, 10 raw coke, 11 compounded raw material, 12 primary mixer -, 13 are secondary mixers,
14 is a charging raw material, 15 is a sintering machine, 16 is a pallet, 17
Is a ore feeder, 18 is a hopper, 19 is a drum feeder, 20 is a granulator, 20a is a sloping shoe, 2
0b is a vibrator, 20c is a cut-off gate, 21 is a raw material layer, 22 is a wind box, 23 is an exhaust air branch pipe, 24 is an exhaust duct, 25 is a main blower, 30 is a fine iron ore tank, and 35 is a sintering raw material. , 36 indicates a bed ore.
【0009】焼結鉱は、鉄鉱石、石灰石などの原料と熱
源である粉コ−クスとをドラムミキサ−で混合し、水分
を加えて造粒した原料をDL式焼結機(パレット)上に
装入して原料層を形成し、点火炉で点火し下向きに空気
を吸引した状態で粉コ−クスの燃焼を徐々に上層から下
層に導きながら焼成して製造される。In the sinter, a raw material such as iron ore and limestone is mixed with a powder coke which is a heat source in a drum mixer, and water is added to granulate the raw material, which is placed on a DL type sintering machine (pallet). It is manufactured by charging to form a raw material layer, igniting in an ignition furnace and sucking air downward while gradually guiding combustion of powder coke from the upper layer to the lower layer.
【0010】上記焼結鉱製造プロセスにおける原料の混
合造粒工程は、図1に示すように、鉄鉱石1、石灰石
2、ミルスケ−ル3、転炉滓4、電気炉滓5、副原滓
6、返鉱7(なおバインダ−としての生石灰8を配合す
る場合もある。)よりなる原料9に、熱源としての粉コ
−クス10を加えた配合原料11を、1次及び2次ドラ
ムミキサ−12及び13で混合造粒して焼結機装入原料
14を得るものである。The raw material mixing and granulating step in the above sinter production process is, as shown in FIG. 1, iron ore 1, limestone 2, mill scale 3, converter slag 4, electric furnace slag 5, auxiliary raw slag. 6, a raw material 9 composed of return ore 7 (which may also be mixed with quick lime 8 as a binder) and a powdered coke 10 as a heat source are added to a mixed raw material 11 for a primary and secondary drum mixer. 12 and 13 are mixed and granulated to obtain a sintering machine charging raw material 14.
【0011】この装入原料14のDL焼結機15のパレ
ット16への供給は、給鉱装置17のホッパ−18から
ドラムフィ−ダ−19或はベルトフィ−ダ−(図示せ
ず)を介して落下供給される装入原料14を造粒機20
を介して焼結機パレット16上に連続的に供給し、パレ
ット16上に所定層厚の原料層21を連続的に形成する
ものである。原料層21は、パレット16下に設けられ
たウィンドボックス22群、排風支管23群、排ガス排
出ダクト24、メインブロア−25で下向きに空気が吸
引されつつ、原料供給装置17の下流の点火炉26で点
火し、原料層21中の粉コ−クスの燃焼を徐々に上層か
ら下層に導かれ焼成される。The charging raw material 14 is supplied to the pallet 16 of the DL sintering machine 15 from the hopper 18 of the ore feeder 17 through a drum feeder 19 or a belt feeder (not shown). The charging raw material 14 supplied by dropping is granulated by the granulator 20.
The raw material layer 21 having a predetermined thickness is continuously formed on the pallet 16 by continuously supplying the raw material layer 21 onto the pallet 16 via the sintering machine. The raw material layer 21 is an ignition furnace downstream of the raw material supply device 17 while air is sucked downward by a wind box 22 group, an exhaust air branch pipe 23 group, an exhaust gas exhaust duct 24, and a main blower 25 provided under the pallet 16. It is ignited at 26, and the combustion of the powder coke in the raw material layer 21 is gradually guided from the upper layer to the lower layer and fired.
【0012】また、図2に示すように造粒機20はドラ
ムフィ−ダ−19からの原料切出しを受け、その直下の
造粒機20を作動させ造粒を図るようにしたものであ
る。この造粒機20は円筒状又は半割円筒状のものから
構成されており、その排出端から排出される造粒済原料
は図3の矢印のように各造粒部分から集中する。Further, as shown in FIG. 2, the granulating machine 20 receives the raw material cut out from the drum feeder 19 and operates the granulating machine 20 immediately below to cut out the granulating material. The granulating machine 20 is composed of a cylindrical or half-cylindrical one, and the granulated raw material discharged from the discharge end thereof is concentrated from each granulating portion as shown by the arrow in FIG.
【0013】従って、その排出端にスロ−ピングシュ−
ト20aを配すことにより矢印のように拡幅を図ること
ができ、もってパレット上に幅方向変差を少なくした状
態で塔載することができる。Therefore, the sloping shoe is attached to the discharge end.
By arranging the toe 20a, the width can be widened as indicated by the arrow, and thus the pallet can be mounted on the pallet in a state in which the variation in the width direction is reduced.
【0014】この造粒機20の基本原理は例えば円筒状
の造粒機20(シュ−ト)に振動機20b(加振器)を
接続し、振動加速度を与えることにより、ゲ−トから切
出される原料の粒状化を得るものである。The basic principle of the granulator 20 is that, for example, a vibrator 20b (vibrator) is connected to a cylindrical granulator 20 (shoot) and a vibration acceleration is applied to the granulator 20 to disconnect it from the gate. This is what gives the granulation of the raw material delivered.
【0015】ここで原料はシュ−ト内で円振動を与えら
れる結果、粗粒にはその表面に微粒子の付着するいわゆ
る核造粒が図られ、また、粗粒が少なくともバインダ−
の利用により粒子成長が達成される。この処理を施した
原料は直ちにパレット16上へ装入される結果、通気性
を良好にし、生産性を向上させることが可能となる。Here, as a result of the circular vibration of the raw material being imparted to the inside of the shoot, so-called nuclear granulation in which the fine particles adhere to the surface of the coarse particles is achieved, and the coarse particles are at least the binder.
Grain growth is achieved by utilizing The raw material that has been subjected to this treatment is immediately loaded onto the pallet 16, and as a result, it is possible to improve the air permeability and improve the productivity.
【0016】円筒状造粒機20(シュ−ト)とは図4の
(a)では円筒の一部を欠き、一方を原料受入れ側とし
て構成されている。また、図4の(b)は円筒の一部を
欠いたものの一方に一体型受入れ部を形成した例を示
し、図4の(c)は一部の切欠きを残し、他の排出側は
円筒とした例である。With the cylindrical granulator 20 (shoot), a part of the cylinder is cut off in FIG. 4 (a), and one side is configured as a raw material receiving side. Further, FIG. 4 (b) shows an example in which an integral type receiving portion is formed on one side of a cylinder which is partially lacking, and FIG. 4 (c) shows a part of the notch on the other discharge side. This is an example of a cylinder.
【0017】図4の(a)ならびに(b)においては、
原料の排出状態が観察できるが、付着等を生じると切欠
き部から原料が漏れる恐れがあり、図4の(c)では観
察部を原料入側の一部にとどめ、他を円筒とし漏れ防止
を図ったものである。なお、左右方向への振動、円振動
であれば原料は円筒内壁に沿う運動を行ない、切欠き部
を有していても飛外すことはない。In FIGS. 4A and 4B,
Although the discharged state of the raw material can be observed, the raw material may leak from the notch if adhesion or the like occurs. In Fig. 4 (c), the observation part is limited to a part of the raw material inlet side and the other part is a cylinder to prevent leakage. Is intended. If the material vibrates in the left-right direction or circular vibration, the raw material moves along the inner wall of the cylinder and does not fly off even if it has a notch.
【0018】なお、造粒機20はパレット16巾方向と
一体物であっても、分割タイプであってもよいが、この
場合、造粒機と造粒機の間の原料が少なくなるため、こ
れを防止するため造粒機下に補助シュ−トとした方がよ
い。振動造粒機と同じく、加振力(加速度は3〜10
g)の領域が良いと思われる。この理由は加振力を大き
く加えることにより、造粒粒子強度の向上を図ることが
できるが、あまり強いと途中でその加振による崩壊があ
るのでこの範囲とした。The granulator 20 may be integrated with the width direction of the pallet 16 or may be of a divided type. In this case, however, the amount of raw materials between the granulators is reduced, In order to prevent this, it is better to use an auxiliary shoe under the granulator. Excitation force (acceleration is 3-10
The area of g) seems to be good. The reason for this is that the strength of the granulated particles can be improved by applying a large excitation force, but if it is too strong, it will collapse due to the excitation in the middle, so this range was made.
【0019】なお、ここで造粒される粒子は、そのまま
パレット16に装入されるため、その粒子が焼結層をそ
のまま形成することから通気性が良く、もって焼結性を
高め得るものである。Since the particles granulated here are charged into the pallet 16 as they are, the particles form a sintered layer as they are, so that the air permeability is good and the sinterability can be improved. is there.
【0020】[0020]
【実施例】図1ならびに図3に示すような装置を用いて
凝似粒子を調整した。比較のため従来法と対比した結果
を表1に示す。EXAMPLE The mimetic particles were prepared using an apparatus as shown in FIGS. Table 1 shows the results of comparison with the conventional method for comparison.
【0021】[0021]
【表1】 [Table 1]
【0022】[0022]
【発明の効果】以上詳しく説明したように、本発明は焼
結鉱を製造する際に、焼結機の給鉱シュ−ト上に多数の
円筒状若しくは半割円筒状の構造物を並列に配置すると
共に、この構造物に円振動を与える振動造粒機を設け、
次いで、前記焼結機の給鉱ホッパから切出される焼結原
料に加振力3〜10g(gは重力の加速度)を与えて凝
似粒子化を図ると共に、この凝似粒子化を直接若しくは
シュ−トを介してパレット上に装入することを特徴とす
る。As described above in detail, according to the present invention, when a sintered ore is manufactured, a large number of cylindrical or half-cylindrical structures are arranged in parallel on a feed ore shoot of a sintering machine. Along with the arrangement, a vibration granulator that gives circular vibration to this structure is installed,
Then, a vibrating force of 3 to 10 g (g is the acceleration of gravity) is applied to the sintering raw material cut out from the ore feeding hopper of the sintering machine to make the particles similar to each other, and the similar particles are directly or directly generated. It is characterized in that it is loaded on a pallet via a shoot.
【0023】従って、本発明によれば焼結機給鉱部で造
粒し、しかも、高速に造粒できる振動造粒機により直接
パレットに装入するようにしたため、通気性が良好で焼
結性を高めることができる。Therefore, according to the present invention, since the granulation is carried out in the ore feeding section of the sintering machine and the pellets are directly charged into the pallet by the vibrating granulator capable of high speed granulation, the air permeability is good and the sintering is carried out. You can improve your sex.
【図1】本発明を実施する際に用いられる全体のフロ−
を示す配置図である。FIG. 1 is an overall flow chart used in carrying out the present invention.
FIG.
【図2】給鉱部の概要の説明図である。FIG. 2 is an explanatory diagram of an outline of a mining section.
【図3】排出端から造粒原料を排出する状況の説明図で
ある。FIG. 3 is an explanatory diagram of a situation in which a granulation raw material is discharged from a discharge end.
【図4】(a)、(b)ならびに(c)はそれぞれ図2
の造粒機の実施例の一例を示す斜視図である。4 (a), (b) and (c) are respectively FIG.
It is a perspective view which shows an example of the Example of the granulator of this.
1 鉄鉱石 2 石灰石 3 ミルスケ−ル 4 転炉滓 5 電気炉滓 6 副原滓 7 返鉱 8 生石灰 9 原料 10 粉コ−クス 11 配合原料 12 1次ミキサ− 13 2次ミキサ− 14 装入原料 15 焼結機 16 パレット 17 給鉱装置 18 給鉱ホッパ− 19 ドラムフィ−ダ− 20 造粒機 20a スロ−ピングシュ−ト 20b 振動機 20c カットオフゲ−ト 21 原料層 22 ウィンドボックス 23 排風支官 24 排出ダクト 25 メインブロア− 30 微粉鉄鉱石槽 35 焼結原料 36 床敷鉱 DESCRIPTION OF SYMBOLS 1 Iron ore 2 Limestone 3 Mill scale 4 Converter slag 5 Electric furnace slag 6 Sub-raw slag 7 Return mine 8 Quick lime 9 Raw material 10 Powder coke 11 Blend raw material 12 Primary mixer 13 Secondary mixer 14 Raw material 15 Sintering machine 16 Pallet 17 Mining device 18 Mining hopper 19 Drum feeder 20 Granulator 20a Sloping shot 20b Vibratory machine 20c Cutoff gate 21 Raw material layer 22 Windbox 23 Exhaust air blower 24 Discharge Duct 25 Main blower 30 Fine iron ore tank 35 Sintering raw material 36 Floor ore
【手続補正書】[Procedure amendment]
【提出日】平成4年10月12日[Submission date] October 12, 1992
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】図面の簡単な説明[Name of item to be corrected] Brief description of the drawing
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図面の簡単な説明】[Brief description of drawings]
【図1】 本発明を実施する際に用いられる全体のフロ
ーを示す配置図である。FIG. 1 is a layout diagram showing an overall flow used when implementing the present invention.
【図2】 給鉱部の概要の説明図である。FIG. 2 is an explanatory diagram of an outline of a mining section.
【図3】 排出端から造粒原料を排出する状況の説明図
である。FIG. 3 is an explanatory diagram of a situation where a granulation raw material is discharged from a discharge end.
【図4】 図2の造粒機の実施例の一例を示す斜視図で
ある。FIG. 4 is a perspective view showing an example of an embodiment of the granulator of FIG.
【図5】 図2の他の実施例の一例を示す斜視図であ
る。5 is a perspective view showing an example of another embodiment of FIG. 2. FIG.
【図6】 図2の他の実施例の一例を示す斜視図であ
る。FIG. 6 is a perspective view showing an example of another embodiment of FIG.
【符号の説明】 1 鉄鉱石 2 石灰石 3 ミルスケール 4 転炉滓 5 電気炉滓 6 副原滓 7 返鉱 8 生石灰 9 原料 10 粉コークス 11 配合原料 12 1次ミキサー 13 2次ミキサー 14 装入原料 15 焼結機 16 パレット 17 給鉱装置 18 給鉱ホッパー 19 ドラムフィーダー 20 造粒機 20a スローピングシュート 20b 振動機 20c カットオフゲート 21 原料層 22 ウインドボックス 23 排風支官 24 排出ダクト 25 メインブロアー 30 微粉鉄鉱石槽 35 焼結原料 36 床敷鉱[Explanation of symbols] 1 iron ore 2 limestone 3 mil scale 4 converter slag 5 electric furnace slag 6 auxiliary raw slag 7 reclaimed lime 8 quicklime 9 raw material 10 powder coke 11 blended raw material 12 primary mixer 13 secondary mixer 14 charging raw material 15 Sintering machine 16 Pallet 17 Mining equipment 18 Mining hopper 19 Drum feeder 20 Granulator 20a Sloping chute 20b Vibratory machine 20c Cut-off gate 21 Raw material layer 22 Windbox 23 Exhaust support 24 Exhaust duct 25 Main blower 30 Fine powder Iron ore tank 35 Sintering raw material 36 Floor mat
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】全図[Correction target item name] All drawings
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図1】 [Figure 1]
【図2】 [Fig. 2]
【図3】 [Figure 3]
【図4】 [Figure 4]
【図5】 [Figure 5]
【図6】 [Figure 6]
Claims (1)
ュ−ト上に多数の円筒状若しくは半割円筒状の構造物を
並列に配置すると共に、この構造物に円振動を与える振
動造粒機を設け、次いで、前記焼結機の給鉱ホッパから
切出される焼結原料に加振力3〜10g(gは重力の加
速度)を与えて凝似粒子化を図ると共に、この凝似粒子
化を直接若しくはシュ−トを介してパレット上に装入す
ることを特徴とする焼結鉱の製造方法。1. When manufacturing a sintered ore, a large number of cylindrical or half-cylindrical structures are arranged in parallel on a feed ore shoot of a sintering machine, and circular vibration is applied to the structures. And a vibrating granulator for giving a vibrating granulator, and then applying a vibrating force of 3 to 10 g (g is the acceleration of gravity) to the sintering raw material cut out from the feed hopper of the sintering machine to achieve similar particles. A method for producing a sintered ore, which comprises charging the similar particles directly or via a shoe onto a pallet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12215791A JPH05112835A (en) | 1991-04-24 | 1991-04-24 | Manufacture of sintered ore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12215791A JPH05112835A (en) | 1991-04-24 | 1991-04-24 | Manufacture of sintered ore |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05112835A true JPH05112835A (en) | 1993-05-07 |
Family
ID=14829012
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12215791A Pending JPH05112835A (en) | 1991-04-24 | 1991-04-24 | Manufacture of sintered ore |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05112835A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100544434B1 (en) * | 2001-06-05 | 2006-01-24 | 주식회사 포스코 | Charging Apparatus for Sinter Mix |
KR100554136B1 (en) * | 2001-12-24 | 2006-02-20 | 주식회사 포스코 | Apparatus for providing the blending material for the sintering process |
KR101372633B1 (en) * | 2007-09-07 | 2014-03-11 | 주식회사 포스코 | Chute for charging electric furnace |
-
1991
- 1991-04-24 JP JP12215791A patent/JPH05112835A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100544434B1 (en) * | 2001-06-05 | 2006-01-24 | 주식회사 포스코 | Charging Apparatus for Sinter Mix |
KR100554136B1 (en) * | 2001-12-24 | 2006-02-20 | 주식회사 포스코 | Apparatus for providing the blending material for the sintering process |
KR101372633B1 (en) * | 2007-09-07 | 2014-03-11 | 주식회사 포스코 | Chute for charging electric furnace |
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