JP5494512B2 - Method of charging sintered raw materials - Google Patents

Method of charging sintered raw materials Download PDF

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JP5494512B2
JP5494512B2 JP2011019949A JP2011019949A JP5494512B2 JP 5494512 B2 JP5494512 B2 JP 5494512B2 JP 2011019949 A JP2011019949 A JP 2011019949A JP 2011019949 A JP2011019949 A JP 2011019949A JP 5494512 B2 JP5494512 B2 JP 5494512B2
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淳治 長田
健一 八ケ代
和之 品川
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Nippon Steel Corp
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Description

本発明は、ドワイトロイド(DL)式焼結機で製造される焼結鉱の品質や生産性を向上させるための焼結原料の装入方法に関する。 The present invention relates to a method for charging a sintered raw material for improving the quality and productivity of a sintered ore produced by a Dwytroid (DL) type sintering machine.

粉鉱石等の鉄鉱石、粉コークス等の凝結材、及び生石灰等の石灰類を、焼結原料に用いて焼結鉱を製造する方法としては、焼結原料の一部又は全部を適切な粒径の造粒物に造粒して焼結パレット(以下、単にパレットともいう)に装入した後、この焼結原料の表層に点火し、パレット下方に向けて空気を吸引しながら凝結材を酸化させ、酸化時の発熱を利用して鉄鉱石(粉鉱石)を焼結させることが、一般的に行われている。
上記したように、焼結パレットに焼結原料を装入するに際し、装入した焼結原料層の高さ(深さ)方向に均一な粒度分布を持たせた場合、以下の課題があった。
As a method for producing sintered ore using iron ore such as powdered ore, coagulants such as powdered coke, and lime such as quick lime as a sintering material, a part or all of the sintering material is appropriately granulated. After granulating into a granulated product with a diameter and inserting it into a sintering pallet (hereinafter also referred to simply as a pallet), the surface layer of this sintering raw material is ignited and the agglomerated material is sucked down while sucking air toward the bottom of the pallet. It is generally performed to oxidize and sinter iron ore (powder ore) using heat generated during oxidation.
As described above, when the sintering raw material is charged into the sintering pallet, the following problems are encountered when the uniform particle size distribution is given in the height (depth) direction of the charged sintering raw material layer. .

焼結原料層の表層部は、吸引された外気により冷却されて昇温不足になる。また、焼結原料層の下部は、表層部などの上方の焼結原料層よりも高温の気体が通過するため、通気抵抗が上方の焼結原料層よりも増し、吸引される空気量(通気量)が減少する。
従って、上記した昇温不足や通気量の減少によって焼結原料の焼結が進行せず、これが焼結鉱の歩留り低下の原因となったり、また焼結鉱の生産量を低下せざるを得ない原因となったりした。
このため、焼結原料層の表層部では、焼結原料の粒径を小さくし熱を受ける表面積を増加させて焼結を促進し、一方、焼結原料層の下部では、焼結原料の平均粒径を大きくし通気性を向上させることが望ましい。この対策は偏析装入とも呼ばれ、所定の粒度偏析を得るために、従来から種々の技術が提案されている。
The surface layer portion of the sintering raw material layer is cooled by the sucked outside air and the temperature rise is insufficient. In addition, since a gas at a higher temperature passes through the lower part of the sintering raw material layer than the upper sintering raw material layer such as the surface layer part, the airflow resistance is higher than that of the upper sintering raw material layer, and the amount of air sucked (ventilated) Amount) decreases.
Accordingly, sintering of the sintering raw material does not proceed due to the above-described insufficient temperature rise or a decrease in the air flow rate, which may cause a decrease in the yield of the sintered ore or reduce the production of the sintered ore. There was no cause.
For this reason, in the surface layer portion of the sintering material layer, the particle size of the sintering material is reduced to increase the surface area that receives heat, thereby promoting the sintering. It is desirable to increase the particle size and improve air permeability. This countermeasure is also called segregation charging, and various techniques have been proposed in the past in order to obtain a predetermined particle size segregation.

例えば、特許文献1には、焼結原料の装入シュートの下流側に、焼結原料の流下方向に沿って延在する複数のバーを備え、しかも平面視して隣り合うバーの側面視した上下方向の間隔を下流側に行くに従い広くしたバースクリーンを設け、ドラムフィーダーで供給される焼結原料を、装入シュートを介し、バースクリーンで分級しながらパレットへ装入する焼結原料の装入方法が、提案されている。
この方法により、上記した焼結原料の偏析装入を実現でき、その結果、焼結鉱の歩留りを上昇させることができ、この歩留りを略一定とするならば焼成量を増加させることができた。従って、焼成量(トン/日/m)と歩留り(%)との積で得られる焼結鉱の生産性(トン/日/m)の大幅な向上を実現できた。
そこで、焼結鉱の生産性の更なる向上を図るため、上記した特許文献1に記載の方法の改善を図った特許文献2に示す技術が提案された。
For example, Patent Document 1 includes a plurality of bars extending along the flow direction of the sintering raw material on the downstream side of the charging chute of the sintering raw material, and viewed from the side of the adjacent bars in plan view. A bar screen that has a wider vertical space as it goes downstream is provided, and the sintering raw material is charged to the pallet while classifying the sintering raw material supplied by the drum feeder with the bar screen via the charging chute. An entry method has been proposed.
By this method, the above-described segregation charging of the sintered raw material can be realized, and as a result, the yield of the sintered ore can be increased, and if the yield is substantially constant, the amount of firing can be increased. . Therefore, the productivity (ton / day / m 2 ) of the sintered ore obtained by the product of the calcining amount (ton / day / m 2 ) and the yield (%) can be greatly improved.
Therefore, in order to further improve the productivity of sintered ore, a technique shown in Patent Document 2 has been proposed in which the method described in Patent Document 1 is improved.

特許文献2には、パレット幅方向における赤熱帯の下降(焼結の進行)を均一にするため、例えば、パレット幅方向の複数位置で通過風速を測定して通気性を検出し、この検出結果に応じてパレット幅方向の粒度偏析の程度を調整することが記載されている。なお、粒度偏析の程度を調整する方法としては、隣接するバー(条材)の間隔の調整(上下方向の移動距離の調整)やバーの開き角度の調整が記載されている。
この方法により、パレット幅方向の焼結品質を一定とすることができ、パレット幅方向における低歩留り部分の歩留りを改善することができる。
In Patent Document 2, in order to make the descent of the red tropics (sintering progress) uniform in the pallet width direction, for example, the air permeability is detected by measuring the passing wind speed at a plurality of positions in the pallet width direction, and this detection result It is described that the degree of particle size segregation in the pallet width direction is adjusted according to the above. In addition, as a method of adjusting the degree of particle size segregation, adjustment of the interval between adjacent bars (strips) (adjustment of the moving distance in the vertical direction) and adjustment of the opening angle of the bar are described.
By this method, the sintering quality in the pallet width direction can be made constant, and the yield of the low yield portion in the pallet width direction can be improved.

特開昭63−190125号公報Japanese Unexamined Patent Publication No. 63-190125 特開昭64−36731号公報Japanese Patent Laid-Open No. 64-36731

しかしながら、特許文献2に記載の方法は、パレット幅方向の焼結品質を一定にできるか否かの焼結鉱の相対的な歩留り改善であり、より高位な歩留りを実現することができない。また、焼結鉱の歩留りは、焼結原料の配合等の条件が同一でも時系列的に低下していく場合があり、この低下は、上記した方法でパレット幅方向の焼結品質を一定にしても改善することができなかった。 However, the method described in Patent Document 2 is an improvement in the relative yield of sintered ore as to whether or not the sintering quality in the pallet width direction can be made constant, and a higher yield cannot be realized. Also, the yield of sintered ore may decrease in time series even if the conditions such as the composition of the sintering raw material are the same, and this decrease makes the sintering quality in the pallet width direction constant by the method described above. However, it could not be improved.

本発明はかかる事情に鑑みてなされたもので、焼結原料の流下方向に沿って延在する複数のバーを備えたバースクリーンを用い、焼結鉱の歩留りが時系列的に低下していく現象を抑制し、高位な歩留りを実現可能な焼結原料の装入方法を提供することを目的とする。 The present invention has been made in view of such circumstances, and using a bar screen having a plurality of bars extending along the flow direction of the sintering raw material, the yield of the sintered ore decreases in time series. It aims at providing the charging method of the sintering raw material which can suppress a phenomenon and can implement | achieve a high yield.

前記目的に沿う第1の発明に係る焼結原料の装入方法は、焼結原料の装入シュートの下流側に、該装入シュートの幅方向に間隔を有して配置され前記焼結原料の流下方向に沿って延在する複数のバーを備え、しかも側面視して上下方向に隣り合う該バーの下流側の間隔を上流側の間隔よりも広くしたバースクリーンを設け、ドラムフィーダーで供給される前記焼結原料を、前記装入シュートを介し、前記バースクリーンで分級しながらパレットへ装入する焼結原料の装入方法において、
前記パレットの単位幅かつ単位時間当たりに前記パレットへ供給される前記焼結原料の供給量が、予め設定した量以上に増加したことを条件として、前記側面視して上下方向に隣り合うバーの下流側の間隔を、前記焼結原料の供給量が増加する前の間隔よりも広くする。
The method for charging a sintered material according to the first aspect of the present invention comprises the sintering material disposed at a downstream side of the charging chute of the sintering material with an interval in the width direction of the charging chute. A bar screen is provided with a plurality of bars extending along the flow-down direction, and with a downstream space between the bars adjacent to each other in the vertical direction as viewed from the side larger than the upstream space, and is supplied by a drum feeder. In the charging method of the sintered raw material, the sintered raw material is charged into the pallet while being classified by the bar screen via the charging chute.
On the condition that the supply amount of the sintering raw material supplied to the pallet per unit width and unit time of the pallet is increased to a preset amount or more, the bars adjacent to each other in the vertical direction in the side view The interval on the downstream side is made wider than the interval before the supply amount of the sintering raw material is increased.

前記目的に沿う第2の発明に係る焼結原料の装入方法は、焼結原料の装入シュートの下流側に、該装入シュートの幅方向に間隔を有して配置され前記焼結原料の流下方向に沿って延在する複数のバーを備え、しかも側面視して上下方向に隣り合う該バーの下流側の間隔を上流側の間隔よりも広くしたバースクリーンを設け、ドラムフィーダーで供給される前記焼結原料を、前記装入シュートを介し、前記バースクリーンで分級しながらパレットへ装入する焼結原料の装入方法において、
前記パレットの単位幅かつ単位時間当たりに前記パレットへ供給される前記焼結原料の供給量が、予め設定した量以下に減少したことを条件として、前記側面視して上下方向に隣り合うバーの下流側の間隔を、前記焼結原料の供給量が減少する前の間隔よりも狭くする。
The method for charging a sintered material according to the second aspect of the present invention is arranged on the downstream side of the charging chute of the sintered material, and is arranged with an interval in the width direction of the charging chute. A bar screen is provided with a plurality of bars extending along the flow-down direction, and with a downstream space between the bars adjacent to each other in the vertical direction as viewed from the side larger than the upstream space, and is supplied by a drum feeder. In the charging method of the sintered raw material, the sintered raw material is charged into the pallet while being classified by the bar screen via the charging chute.
On the condition that the supply amount of the sintering raw material supplied to the pallet per unit width and unit time of the pallet is reduced to a predetermined amount or less, the bars adjacent to each other in the vertical direction when viewed from the side are used. The interval on the downstream side is made narrower than the interval before the supply amount of the sintering raw material decreases.

第1、第2の発明に係る焼結原料の装入方法において、前記側面視して上下方向に隣り合うバーの下流側の間隔は、該各バーの傾斜角度を調整して行うことが好ましい。 In the method for charging sintered raw materials according to the first and second inventions, it is preferable that the interval between the bars adjacent to each other in the vertical direction when viewed from the side is adjusted by adjusting the inclination angle of each bar. .

第1の発明に係る焼結原料の装入方法は、パレットへ供給される焼結原料の供給量が、予め設定した量以上に増加したことを条件として、側面視して上下方向に隣り合うバーの下流側の間隔を、焼結原料の供給量が増加する前の間隔よりも広くする。これにより、焼結原料の供給量の増加に伴って、バースクリーン上を流下する焼結原料の流下速度が増加しても、バースクリーンで分級されることなくバースクリーンをオーバーランする焼結原料の量を低減でき、パレットへ供給する焼結原料をバースクリーンで適切に分級できる。
また、第2の発明に係る焼結原料の装入方法は、パレットへ供給される焼結原料の供給量が、予め設定した量以下に減少したことを条件として、側面視して上下方向に隣り合うバーの下流側の間隔を、焼結原料の供給量が減少する前の間隔よりも狭くする。これにより、焼結原料の供給量の減少に伴って、バースクリーン上を流下する焼結原料の流下速度が低下しても、パレットへ供給する焼結原料のうち大きな粒径の焼結原料が、小さな粒径の焼結原料と共に、バースクリーンの上流側で隣り合うバーの間を通過することを抑制でき、パレットへ供給する焼結原料をバースクリーンで適切に分級できる。
従って、パレットへ供給される焼結原料の供給量の増減に起因して、焼結鉱の歩留りが時系列的に低下していく現象を抑制でき、高位な歩留りを実現することが可能になる。
The charging method of the sintering raw material according to the first invention is adjacent in the vertical direction as viewed from the side, on the condition that the supply amount of the sintering raw material supplied to the pallet is increased to a predetermined amount or more. The interval on the downstream side of the bar is made wider than the interval before the supply amount of the sintering raw material is increased. As a result, even if the flow rate of the sintering material flowing down on the bar screen increases with an increase in the supply amount of the sintering material, the sintering material overruns the bar screen without being classified by the bar screen. Therefore, the sintering raw material to be supplied to the pallet can be appropriately classified with a bar screen.
Moreover, the charging method of the sintering raw material which concerns on 2nd invention WHEREIN: On the condition that the supply amount of the sintering raw material supplied to a pallet decreased below the preset amount, it was vertical in the side view. The interval on the downstream side of adjacent bars is made narrower than the interval before the supply amount of the sintering raw material is reduced. As a result, even if the flow rate of the sintering raw material flowing down on the bar screen decreases with the decrease in the supply amount of the sintering raw material, the sintering raw material having a large particle size among the sintering raw materials supplied to the pallet is reduced. Further, it is possible to suppress passage between adjacent bars on the upstream side of the bar screen together with the sintered raw material having a small particle diameter, and the sintered raw material supplied to the pallet can be appropriately classified by the bar screen.
Therefore, it is possible to suppress a phenomenon in which the yield of sintered ore is lowered in time series due to increase or decrease in the supply amount of the sintering raw material supplied to the pallet, and it becomes possible to realize a high yield. .

ここで、側面視して上下方向に隣り合うバーの下流側の間隔を、各バーの傾斜角度を調整して行う場合、簡単な方法で、焼結鉱の歩留りが低下する現象を更に抑制できる。 Here, when the interval between the bars adjacent to each other in the vertical direction as viewed from the side is adjusted by adjusting the inclination angle of each bar, the phenomenon that the yield of sintered ore is lowered can be further suppressed by a simple method. .

(A)は本発明の一実施の形態に係る焼結原料の装入方法の説明図、(B)は同焼結原料の装入方法を適用するバースクリーンの斜視図である。(A) is explanatory drawing of the charging method of the sintering raw material which concerns on one embodiment of this invention, (B) is a perspective view of the bar screen which applies the charging method of the sintering raw material. (A)〜(D)はそれぞれ同バースクリーンの側面図、平面図、先端の正面図、基端の背面図である。(A)-(D) are the side view of the same bar screen, a top view, the front view of a front-end | tip, and the rear view of a base end, respectively. パレットへの焼結原料の供給量がパレットに装入された焼結原料層の偏析度に及ぼす影響を示すグラフである。It is a graph which shows the influence which the supply amount of the sintering raw material to a pallet exerts on the segregation degree of the sintering raw material layer inserted into the pallet. パレットに装入された焼結原料層の偏析度が焼結鉱の歩留りに及ぼす影響を示すグラフである。It is a graph which shows the influence which the segregation degree of the sintering raw material layer with which the pallet was charged has on the yield of sintered ore. パレットへの焼結原料の供給量とパレットに装入された焼結原料層の偏析度との関係を示すグラフである。It is a graph which shows the relationship between the supply amount of the sintering raw material to a pallet, and the segregation degree of the sintering raw material layer inserted into the pallet. パレットへの焼結原料の供給量と焼結鉱の歩留りとの関係を示すグラフである。It is a graph which shows the relationship between the supply amount of the sintering raw material to a pallet, and the yield of a sintered ore. パレットへの焼結原料の供給量と焼結鉱の生産性との関係を示すグラフである。It is a graph which shows the relationship between the supply amount of the sintering raw material to a pallet, and the productivity of a sintered ore.

続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態につき説明し、本発明の理解に供する。
まず、図1(A)、(B)、図2(A)〜(D)を参照しながら、本発明の一実施の形態に係る焼結原料の装入方法を適用するドワイトロイド式焼結機の焼結原料の装入装置(以下、単に装入装置ともいう)10について説明する。
焼結原料の装入装置10は、焼結原料11を貯蔵する貯蔵ホッパー12と、焼結原料11を貯蔵ホッパー12から切り出すドラムフィーダー(DF)13と、切り出された焼結原料11を滑走させて下方のパレット(以下、焼結パレットともいう)14へ装入させる装入シュート15とを有している。
Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.
First, with reference to FIGS. 1 (A), 1 (B), and FIGS. 2 (A) to 2 (D), a droidoid-type sintering to which a method for charging a sintered material according to an embodiment of the present invention is applied. A charging apparatus (hereinafter also simply referred to as a charging apparatus) 10 for sintering raw materials of the machine will be described.
The sintered raw material charging apparatus 10 slides the storage hopper 12 that stores the sintered raw material 11, the drum feeder (DF) 13 that cuts the sintered raw material 11 from the storage hopper 12, and the cut sintered raw material 11. And a charging chute 15 for charging into a lower pallet (hereinafter also referred to as a sintering pallet) 14.

装入シュート15の下流側には、装入シュート15の下部から落下する焼結原料11を分級しながらパレット14上に装入するバースクリーン16が設けられている。
このバースクリーン16は、図1(A)、(B)、図2(B)に示すように、装入シュート15の下流側に、平面視してこの装入シュート13の幅方向に間隔dを有して配置され、装入シュート15を滑走する焼結原料11の流下方向に沿って延在する複数のバー17〜19を備えている。各バー17〜19は、金属製(例えば、鉄製等)の棒条材で構成され、焼結原料11の流下方向に沿って下方へ傾斜した状態で、その一端部(上端部)が装入シュート15の裏側に取付けられている。
On the downstream side of the charging chute 15, a bar screen 16 for charging the sintered raw material 11 falling from the lower part of the charging chute 15 onto the pallet 14 while being classified is provided.
As shown in FIGS. 1 (A), 1 (B), and 2 (B), the bar screen 16 has a distance d in the width direction of the charging chute 13 in a plan view on the downstream side of the charging chute 15. And a plurality of bars 17 to 19 extending along the flow-down direction of the sintering raw material 11 sliding on the charging chute 15. Each of the bars 17 to 19 is made of a metal rod (for example, iron or the like), and one end (upper end) of the bar 17 is charged in a state of being inclined downward along the flow direction of the sintering raw material 11. It is attached to the back side of the chute 15.

この各バー17〜19の断面形状は、通常、円形であるが、焼結原料を分級できる形状であれば特に限定されるものではなく、例えば、楕円形や卵形、更には三角形や四角形(矩形)等の多角形でもよい。
また、各バー17〜19の長さは、焼結原料を分級できれば特に限定されるものではないが、世の中にある焼結機での焼結鉱の生産量を考慮すれば、例えば、500〜1000mm程度である。
更に、図2(A)に示すように、各バー17〜19の水平方向に対する下方への傾斜角度α、β、γは、30〜55度の範囲内で調整できる。
The cross-sectional shape of each of the bars 17 to 19 is usually circular, but is not particularly limited as long as the sintering raw material can be classified. For example, an oval shape, an oval shape, a triangular shape or a quadrangular shape ( A polygon such as a rectangle may be used.
Moreover, the length of each bar 17-19 will not be specifically limited if a sintering raw material can be classified, However, if the production amount of the sintered ore with a sintering machine in the world is considered, for example, 500- It is about 1000 mm.
Furthermore, as shown to FIG. 2 (A), downward inclination angle (alpha), (beta), (gamma) with respect to the horizontal direction of each bar 17-19 can be adjusted within the range of 30-55 degree | times.

図2(A)に示すように、各バー17〜19は、側面視して上下方向に、1段目(上段)のバー17、2段目(中段)のバー18、3段目(下段)のバー19というグループに区分されている。このように、各バー17〜19は、側面視して上下方向に隣り合う1段目のバー17と2段目のバー18との下流端(下流側)の間隔a1、及び2段目のバー18と3段目のバー19との下流端(下流側)の間隔a2が、それぞれ上流端(上流側)の間隔b1、b2よりも広くなっている(図2(C)、(D)参照)。これは、1〜3段目の各バー17〜19の傾斜角度α、β、γを、上段側から下段側にかけて大きくしていることによる(α<β<γ)。
ここで、1段目と2段目のバー17、18の傾斜角度の差(β−α)、2段目と3段目のバー18、19の傾斜角度の差(γ−β)は、1〜7度の範囲で調整できる。なお、各バー17〜19の傾斜角度の差は、同一にしているが、異なってもよい。
As shown in FIG. 2A, each of the bars 17 to 19 has a first stage (upper stage) bar 17, a second stage (middle stage) bar 18, and a third stage (lower stage) in the vertical direction when viewed from the side. ) Bar 19. As described above, the bars 17 to 19 have a distance a1 between the downstream end (downstream side) between the first-stage bar 17 and the second-stage bar 18 that are adjacent in the vertical direction when viewed from the side, and the second-stage bar. The distance a2 between the downstream end (downstream side) between the bar 18 and the third-stage bar 19 is wider than the distance b1 and b2 between the upstream ends (upstream side), respectively (FIGS. 2C and 2D). reference). This is because the inclination angles α, β, and γ of the first to third bars 17 to 19 are increased from the upper side to the lower side (α <β <γ).
Here, the difference between the inclination angles of the first and second bars 17 and 18 (β−α), and the difference between the inclination angles of the second and third bars 18 and 19 (γ−β), It can be adjusted within a range of 1 to 7 degrees. In addition, although the difference of the inclination angle of each bar 17-19 is made the same, you may differ.

ここでは、複数のバーを上下方向に3段に分けた場合について説明したが、焼結原料を分級できれば特に限定されるものではなく、上下方向に2段以上の複数段(例えば、4段以上)のグループに分けることもできる。なお、側面視して上下方向に隣り合う1〜3段目の各バー17〜19の鉛直方向の先端間隔は同一にしているが、異なってもよい。
また、各バー17〜19は、図1(B)、図2(C)に示すように、各バー17〜19の先端位置を結ぶ線が、谷、山、谷のW字型(1又は複数の山型)となった場合について説明したが、逆W字型やV字型とすることもでき、更には、V字型や逆V字型を、装入シュートの幅方向にわたって繰り返した形にすることもできる。なお、この形は、図2(D)に示すように、各バー17〜19の基端位置を結ぶ線に適用することも勿論可能であるが、基端位置については、各バーを同一高さ位置にしてもよい。
Here, the case where a plurality of bars are divided into three stages in the vertical direction has been described. However, there is no particular limitation as long as the sintering raw material can be classified, and there are two or more stages in the vertical direction (for example, four or more stages). ). In addition, although the front-end | tip space | interval of the perpendicular direction of each bar | burr 17-19 of the 1st-3rd stage | paragraph adjacent to an up-down direction seeing side is made the same, you may differ.
Moreover, as shown to FIG. 1 (B) and FIG.2 (C), the line which connects each bar | burr 17-19 to the front-end | tip position of each bar | burr 17-19 is a W-shape (1 or In the case of a plurality of mountain-shaped), an inverted W-shape or V-shape can be used, and further, a V-shape or an inverted V-shape is repeated over the width direction of the charging chute. It can also be shaped. It is of course possible to apply this shape to a line connecting the base end positions of the bars 17 to 19 as shown in FIG. 2D. It may be in the position.

更に、バースクリーンは、各バーの先端位置を結ぶ線で形成される山又は谷の斜面を構成するバーの本数を3本とした構成としたが、焼結原料を分級できれば特に限定されるものではなく、2本以上の複数本(例えば、4本以上)で構成することもできる。なお、バースクリーンは、焼結原料を分級できれば、複数のバーのうち一部のバーが部分的に欠落したものでもよい。例えば、図2(C)に示す各バー17〜19の先端位置を結ぶ線で形成される山又は谷の斜面を構成するバーの本数を、3本(同一本数)から2本又は1本(異なる本数)としたものでもよい。
また、図2(B)に示すように、平面視して装入シュート15の幅方向に隣り合うバー17〜19は平行に配置されている(間隔dが同一となっている)が、焼結原料を分級できれば完全に平行となっている必要はなく、例えば、バーの先端にかけてその間隔が広がってもよく、また狭まってもよい。
Furthermore, the bar screen has a configuration in which the number of bars constituting the slopes of the peaks or valleys formed by the lines connecting the tip positions of the bars is three. However, the bar screen is particularly limited as long as the sintering raw material can be classified. Instead, it may be composed of two or more (for example, four or more). The bar screen may be one in which some of the plurality of bars are partially missing as long as the sintered raw material can be classified. For example, the number of bars constituting the slope of a mountain or valley formed by a line connecting the tip positions of the bars 17 to 19 shown in FIG. 2C is changed from three (the same number) to two or one ( Different numbers) may be used.
Further, as shown in FIG. 2B, the bars 17 to 19 adjacent in the width direction of the charging chute 15 in a plan view are arranged in parallel (the interval d is the same). It is not necessary to be completely parallel as long as the raw materials can be classified. For example, the interval may increase or decrease toward the tip of the bar.

次に、本発明に想到した経緯について説明する。
図1(A)、(B)、図2(A)〜(D)に示すバースクリーン16を用いた焼結原料11の偏析装入方法を採用した場合、焼結鉱の歩留り(生産した焼結鉱に対する高炉装入に適した粒径5mm以上の質量割合)を概ね75〜85質量%とすると、配合する鉄鉱石の鉱種変更に伴う造粒物の平均径変動や、降雨による造粒時の添加水の割合変動が、大きな歩留り変動要因となることが一般に知られている(2〜3質量%の歩留り変動)。
Next, the background of the present invention will be described.
When the segregation charging method of the sintered raw material 11 using the bar screen 16 shown in FIGS. 1 (A), 1 (B) and 2 (A) to 2 (D) is adopted, the yield of sintered ore (the produced firing) When the mass ratio of 5 mm or more suitable for blast furnace charging for the ore) is approximately 75 to 85% by mass, the average diameter of the granulated product changes due to the change in the type of iron ore to be blended, or granulation due to rainfall It is generally known that the fluctuation in the ratio of the added water at the time becomes a large yield fluctuation factor (yield fluctuation of 2 to 3% by mass).

これに対し、焼結機による焼結鉱の生産量変動が1割以上となる場合も、焼結鉱の歩留り変動が上記した変動と同程度、更にはそれ以上となる。
このことから、本願発明者らは、焼結鉱の生産量変動が、最も大きな歩留り変動要因の一つであることに新たに着目した。
なお、焼結機の次工程は高炉であるため、焼結機における焼結鉱の単位時間当たりの生産量が常に高位に維持されるものではなく、高炉での溶銑の生産に必要な焼結鉱量の変動に応じて、焼結機で製造する焼結鉱の生産量を変動(上昇又は低下)させる場合がある。
On the other hand, when the production fluctuation of the sintered ore by the sintering machine is 10% or more, the yield fluctuation of the sintered ore is the same as or more than the above fluctuation.
From this, the inventors of the present application newly paid attention to the fact that the fluctuation in the production amount of sintered ore is one of the largest yield fluctuation factors.
Since the next step of the sintering machine is a blast furnace, the production amount of sintered ore per unit time in the sintering machine is not always maintained at a high level, and the sintering required for hot metal production in the blast furnace Depending on the fluctuation of the ore amount, the production amount of the sintered ore manufactured by the sintering machine may be changed (increased or lowered).

焼結機で焼結鉱の生産量を変動させる場合、焼結機に供給する焼結原料量を変動させる必要がある。図1(A)、(B)に示すように、貯蔵ホッパー12に貯蔵された焼結原料11を、ドラムフィーダー13から装入シュート15を経由し、バースクリーン16を経てパレット(以下、焼結パレットともいう)14に流下させて供給するドワイトロイド式焼結機においては、ドラムフィーダー13で切り出される(パレット14に向けて供給される)単位時間当たりの焼結原料11の供給量を増加、即ちバースクリーン16での焼結原料11の流下速度を増加させることで、上記した変動を実現できる。 When changing the production amount of sintered ore with a sintering machine, it is necessary to change the amount of sintering raw material supplied to the sintering machine. As shown in FIGS. 1 (A) and 1 (B), the sintered raw material 11 stored in the storage hopper 12 is transferred from the drum feeder 13 through the charging chute 15 and through the bar screen 16 to the pallet (hereinafter, sintered). In a droidoid sintering machine that flows down and is supplied to 14 (also referred to as a pallet), the supply amount of the sintering raw material 11 per unit time cut out by the drum feeder 13 (supplied toward the pallet 14) is increased. In other words, the above-described fluctuation can be realized by increasing the flow speed of the sintering raw material 11 on the bar screen 16.

ここで、パレットへの焼結原料の供給量がパレットに装入された焼結原料層の偏析度に及ぼす影響を調査した結果について説明する。
図3に示すように、パレットの単位幅かつ単位時間当たりにパレットへ供給される焼結原料の供給量が200(トン/時間/m)から250(トン/時間/m)へ増加すると、パレットに装入された焼結原料層の偏析度が低下することが分かる。
なお、上記した調査で用いたバースクリーンの試験条件の内容を、表1に示す。
Here, the result of investigating the influence of the supply amount of the sintering raw material to the pallet on the segregation degree of the sintering raw material layer charged in the pallet will be described.
As shown in FIG. 3, when the supply amount of the sintering raw material supplied to the pallet per unit width and unit time of the pallet increases from 200 (tons / hour / m) to 250 (tons / hour / m), the pallet It can be seen that the degree of segregation of the sintered raw material layer charged in is reduced.
Table 1 shows the contents of the bar screen test conditions used in the above investigation.

Figure 0005494512
Figure 0005494512

また、パレットに装入された焼結原料層の偏析度が焼結鉱の歩留りに及ぼす影響を調査した結果についても説明する。
図4に示すように、パレットに装入された焼結原料層の偏析度が低下すると、焼結鉱の歩留り(成品(製品)歩留り:質量%)が低下する状況が分かる。
なお、上記した偏析度とは、パレットに装入した焼結原料層(最低でも厚さが500mm程度)の高さ(深さ)方向の粒度分布の指標であり、以下の式により算出した。
(偏析度)={(焼結原料層の下層50mmの平均径)−(焼結原料層の上層50mmの平均径)}/(焼結原料層の全層の平均径)
上記した式から、偏析度が大きいほど、適切な偏析装入が行われていることが分かる。
Moreover, the result of investigating the influence of the segregation degree of the sintering raw material layer charged on the pallet on the yield of the sintered ore will be described.
As shown in FIG. 4, it can be seen that when the segregation degree of the sintered raw material layer charged in the pallet decreases, the yield of the sintered ore (product (product) yield: mass%) decreases.
The degree of segregation described above is an index of the particle size distribution in the height (depth) direction of the sintered raw material layer (at least about 500 mm in thickness) charged in the pallet, and was calculated by the following equation.
(Segregation degree) = {(Average diameter of lower layer 50 mm of sintered raw material layer) − (Average diameter of upper layer of sintered raw material layer 50 mm)} / (Average diameter of all layers of sintered raw material layer)
From the above equation, it can be seen that the larger the degree of segregation, the more appropriate segregation charging is performed.

また、上記した平均径は、以下の方法により算出した。
サンプリングして乾燥した後の焼結原料を、9.5mm、8.0mm、6.7mm、4.75mm、2.8mm、2.0mm、1.0mm、0.5mmの各篩で、記載した順序に順次分級してグループに分け、この各グループについて代表径と質量比(焼結原料全質量に対する当該グループに属する焼結原料の質量)を求めた(JIS Z8801−1「試験用ふるい−第1部:金属製網ふるい」)。そして、グループごとに代表径と質量比との積を算出し、それらの総和を焼結原料の平均径とした。ここで、代表径は、篩い目9.5mmオーバーを12.5mm、篩い目0.5mmアンダーを0.25mm、その他は、篩い目の中心値(例えば、9.5mmアンダーから8.0mmオーバーのグループでは8.75mm)とした。
The above average diameter was calculated by the following method.
The sintered raw material after sampling and drying was described with 9.5 mm, 8.0 mm, 6.7 mm, 4.75 mm, 2.8 mm, 2.0 mm, 1.0 mm, and 0.5 mm sieves. Each group was sequentially classified into groups, and the representative diameter and the mass ratio (the mass of the sintered raw material belonging to the group with respect to the total mass of the sintered raw material) were determined for each group (JIS Z8801-1 “Sieving Test—No. Part 1: Metal mesh sieve "). And the product of the representative diameter and mass ratio was computed for every group, and those sum total was made into the average diameter of a sintering raw material. Here, the representative diameter is 12.5 mm when the sieve mesh is 9.5 mm over, 0.25 mm when the sieve mesh is 0.5 mm under, and other values are the center value of the sieve mesh (for example, 9.5 mm under and 8.0 mm over) 8.75 mm for the group).

以上のことから、本発明者らは、焼結機に供給する焼結原料量を変動させることが、パレットに装入した焼結原料層の上層部から下層部にかけての焼結原料層の偏析度を低下させ、焼結鉱の歩留りに大きな悪影響を及ぼすことに想到した。
上記したパレット14への焼結原料11の供給量は、ドラムフィーダー13のドラムの回転速度、もしくはドラムフィーダー13のゲート高さの変更(焼結原料11の放出口20の面積変更)により、排出される焼結原料11の厚みを変更することで調節(変動)できる。なお、焼結原料11の供給量を上記した方法のいずれで調節したとしても、焼結原料11の供給量(トン/時間/m:パレット14の単位幅当たり、かつ単位時間当たりに供給する焼結原料11の量)に応じて、バースクリーン16での焼結原料11の流下速度が変化する。
From the above, the present inventors can vary the amount of sintering raw material supplied to the sintering machine, and segregate the sintering raw material layer from the upper layer portion to the lower layer portion of the sintering raw material layer charged in the pallet. It was thought that the degree of sinter decreased and the yield of sintered ore was greatly affected.
The supply amount of the sintering raw material 11 to the pallet 14 is discharged by changing the rotation speed of the drum of the drum feeder 13 or the gate height of the drum feeder 13 (changing the area of the discharge port 20 of the sintering raw material 11). It can be adjusted (varied) by changing the thickness of the sintered raw material 11 to be produced. Even if the supply amount of the sintering raw material 11 is adjusted by any of the above-described methods, the supply amount of the sintering raw material 11 (ton / hour / m: the firing supplied per unit width of the pallet 14 and per unit time). The flow rate of the sintered raw material 11 on the bar screen 16 changes according to the amount of the raw material 11).

そこで、本発明では、焼結鉱の歩留りが低下していく現象を抑制し、高位な歩留りを実現する課題を解決するにあたり、焼結工程において焼結原料の供給量が変化した場合でも、パレットに装入した焼結原料層を、その高さ方向の偏析度が最適となる装入状態に調整することで、焼結鉱の歩留り低下を抑制可能とする装入方法を提供することを具体的な課題とした。
以下、本発明の焼結原料の装入方法について、図1(A)、(B)、図2(A)〜(D)を参照しながら説明する。
Therefore, in the present invention, in order to suppress the phenomenon that the yield of sintered ore is reduced and to solve the problem of realizing a high yield, even if the supply amount of the sintering raw material is changed in the sintering process, the pallet Specifically, it is possible to provide a charging method capable of suppressing the yield reduction of the sintered ore by adjusting the sintering raw material layer charged in the state of charging with the optimum segregation degree in the height direction. It was set as a general issue.
Hereinafter, the method for charging the sintered material of the present invention will be described with reference to FIGS. 1 (A), 1 (B), and FIGS. 2 (A) to 2 (D).

本発明の一実施の形態に係る焼結原料の装入方法は、ドラムフィーダー13で供給される焼結原料11を、装入シュート15を介し、バースクリーン16で分級しながらパレット14へ装入する方法であり、パレット14の単位幅かつ単位時間当たりにパレット14へ供給される焼結原料11の供給量が変動したことを条件として、側面視して上下方向に隣り合う1段目のバー17と2段目のバー18の下流側の鉛直方向の間隔a1、及び2段目のバー18と3段目のバー19の下流側の鉛直方向の間隔a2を、焼結原料11の供給量が変動する前の間隔よりも広く又は狭くする方法である。
焼結機(パレット14)の幅が一定の場合、前記したように、焼結鉱の生産量に応じてパレット14への焼結原料11の供給量が変動すると、バースクリーン16での焼結原料11の流下速度が変化する。その結果、焼結原料11層の偏析度が変化し、焼結鉱の歩留りが低下する。
The method for charging a sintered material according to one embodiment of the present invention is to charge the sintered material 11 supplied by the drum feeder 13 into the pallet 14 while classifying it by the bar screen 16 via the charging chute 15. The first-stage bar that is adjacent in the vertical direction as viewed from the side, on condition that the supply amount of the sintering raw material 11 supplied to the pallet 14 per unit time and unit time of the pallet 14 fluctuates. The amount of supply of the sintering raw material 11 is defined as the vertical interval a1 downstream of the 17th and second stage bars 18 and the vertical interval a2 downstream of the second stage bar 18 and third stage bar 19. This is a method of making it wider or narrower than the interval before fluctuating.
When the width of the sintering machine (pallet 14) is constant, as described above, if the supply amount of the sintering raw material 11 to the pallet 14 varies according to the production amount of the sintered ore, the sintering at the bar screen 16 The flow speed of the raw material 11 changes. As a result, the segregation degree of the 11 layers of the sintered raw material changes, and the yield of the sintered ore decreases.

具体的には、焼結原料11の供給量が増加すると、焼結原料11の流下速度の増加につながる。また、パレット14内の焼結原料11層の高さ方向の偏析度が低下するのは、焼結原料11の流下速度が上がるとバースクリーン16を通過して分級されることなくオーバーランする焼結原料11の割合が増加し、バースクリーン16の先端から流れ落ちる焼結原料11の割合が増加することに起因する。
従って、焼結鉱の歩留り低下は、焼結原料11の流下速度の増加により、バースクリーン16で適切に分級されない焼結原料11の量が増えることが原因である。そこで、焼結原料11の供給量が予め設定した量以上に増加したことを条件として、各バー17〜19の下流側の間隔a1、a2を、焼結原料11の供給量が増加する前、即ち供給する焼結原料11の増加量(変動量)が0質量%のときの間隔よりも広くする。
Specifically, when the supply amount of the sintering raw material 11 is increased, the flow rate of the sintering raw material 11 is increased. Moreover, the segregation degree in the height direction of the 11 layers of the sintered raw material in the pallet 14 decreases because the firing speed of the sintered raw material 11 increases as the flow rate of the sintered raw material 11 increases, and overruns without being classified through the bar screen 16. This is because the ratio of the sintering raw material 11 increases and the ratio of the sintering raw material 11 that flows down from the tip of the bar screen 16 increases.
Therefore, the yield reduction of the sintered ore is caused by an increase in the amount of the sintered raw material 11 that is not properly classified by the bar screen 16 due to an increase in the flow rate of the sintered raw material 11. Therefore, on the condition that the supply amount of the sintering raw material 11 is increased to a predetermined amount or more, the intervals a1 and a2 on the downstream side of the bars 17 to 19 are set before the supply amount of the sintering raw material 11 is increased. That is, it is made wider than the interval when the increase amount (variation amount) of the supplied sintering raw material 11 is 0% by mass.

一方、焼結原料11の供給量が減少すると、焼結原料11の流下速度の低下につながる。また、パレット14内の焼結原料11層の高さ方向の偏析度が低下するのは、焼結原料11の流下速度が下がると、パレット14へ供給する焼結原料11のうち大きな粒径の焼結原料11が、小さな粒径の焼結原料11と共に、バースクリーン16の上流側でバー17〜19の間を通過する割合が増加することに起因する。
従って、焼結鉱の歩留りの低下は、焼結原料11の流下速度の低下により、バースクリーン16で適切に分級されない焼結原料11の量が増えることが原因である。そこで、焼結原料11の供給量が予め設定した量以下に減少したことを条件として、各バー17〜19の下流側の間隔a1、a2を、焼結原料11の供給量が減少する前、即ち供給する焼結原料11の減少量(変動量)が0質量%のときの間隔よりも狭くする。
On the other hand, when the supply amount of the sintering raw material 11 decreases, the flow rate of the sintering raw material 11 decreases. In addition, the segregation degree in the height direction of the sintered raw material 11 layer in the pallet 14 is decreased when the flow rate of the sintered raw material 11 is reduced, the larger the particle size of the sintered raw material 11 supplied to the pallet 14. This is because the ratio of the sintered raw material 11 passing between the bars 17 to 19 on the upstream side of the bar screen 16 together with the small raw material 11 is increased.
Therefore, the decrease in the yield of sintered ore is caused by the increase in the amount of the sintered raw material 11 that is not properly classified by the bar screen 16 due to the decrease in the flow rate of the sintered raw material 11. Therefore, on the condition that the supply amount of the sintering raw material 11 has decreased to a predetermined amount or less, the intervals a1 and a2 on the downstream side of the bars 17 to 19 are set before the supply amount of the sintering raw material 11 decreases. That is, it is made narrower than the interval when the decrease amount (variation amount) of the supplied sintering raw material 11 is 0 mass%.

ここで、各バー17〜19の下流側の間隔a1、a2は、以下の2つの方法で調整できる。
1つ目は、各バー17〜19の傾斜角度α、β、γを調整する方法であり、2つ目は、各バー17〜19の傾斜角度α、β、γを一定のままとし、各バー17〜19を高さ方向に平行移動させる方法である。
ここで、1つ目の方法は、例えば、各バー17〜19の一端部(上端部)を、角度調整手段を介して装入シュート15の裏面側に取付け、これを制御部で制御することにより実施できる。
また、2つ目の方法は、例えば、各バー17〜19の一端部を、昇降手段を介して装入シュート15の裏面側に取付け、これを制御部で制御することにより実施できる。
Here, the intervals a1 and a2 on the downstream side of the bars 17 to 19 can be adjusted by the following two methods.
The first is a method of adjusting the inclination angles α, β, γ of the bars 17-19, and the second is that the inclination angles α, β, γ of the bars 17-19 are kept constant, In this method, the bars 17 to 19 are translated in the height direction.
Here, in the first method, for example, one end (upper end) of each of the bars 17 to 19 is attached to the back side of the charging chute 15 via the angle adjusting means, and this is controlled by the control unit. Can be implemented.
Moreover, the 2nd method can be implemented by attaching the one end part of each bar | burr 17-19 to the back surface side of the insertion chute | shooting 15 via an raising / lowering means, and controlling this with a control part, for example.

更に、上記した2つの方法を組み合わせて、各バー17〜19の下流側の間隔a1、a2を調整することもできる。
なお、各段を構成するバー17〜19の傾斜角度α、β、γの調整は、各段ごとに全てのバー17〜19について行うことが好ましいが、焼結原料11の供給量の変動に応じて、全ての段のうちの1段又は2段以上、例えば、3段目のバー19のみ、又は2段目のバー18と3段目のバー19について行うこともできる。
ここで、各段を構成するバー17〜19の傾斜角度α、β、γは、焼結原料11の供給量の変動に応じて、当業者であれば前記した範囲内で適宜調整できる。
Furthermore, the distances a1 and a2 on the downstream side of the respective bars 17 to 19 can be adjusted by combining the two methods described above.
The adjustment of the inclination angles α, β, γ of the bars 17 to 19 constituting each stage is preferably performed for all the bars 17 to 19 for each stage, but the supply amount of the sintering raw material 11 varies. Accordingly, it can be performed for one or more of all the stages, for example, only the third-stage bar 19, or the second-stage bar 18 and the third-stage bar 19.
Here, the inclination angles α, β, and γ of the bars 17 to 19 constituting each stage can be appropriately adjusted within the above-mentioned range by those skilled in the art according to the fluctuation of the supply amount of the sintering raw material 11.

また、各バー17〜19の下流側の間隔a1、a2を調整する基準となる焼結原料11の変動量は、特に限定されるものではなく、例えば、焼結原料11の供給量の変動に応じて、焼結原料11の供給量が増減する前、即ち供給する焼結原料11の変動量が0質量%のときの間隔よりも徐々に広げたり、また狭めたりすることができる。
しかし、焼結原料の供給量が3質量%以上変動(増加又は減少)した場合に、各バー17〜19の下流側の間隔a1、a2を調整することが好ましい。本発明者らの知見では、焼結原料の供給量が一定であっても、偏析度は一定のバラツキを持つが、焼結原料の供給量が3質量%程度変動すると、偏析度の有意な変化(悪化)が生じる。
従って、焼結原料の供給量が少なくとも3質量%以上変化する場合に、各バー17〜19の下流側の間隔a1、a2を変更するとよい。なお、焼結原料の供給量の変動の上限値については特に規定していないが、実際の操業においては50質量%程度である。
Moreover, the fluctuation amount of the sintering raw material 11 used as the reference | standard which adjusts the space | interval a1, a2 of the downstream of each bar 17-19 is not specifically limited, For example, it is to the fluctuation | variation of the supply amount of the sintering raw material 11. Accordingly, before the supply amount of the sintering raw material 11 increases or decreases, that is, the interval when the fluctuation amount of the sintering raw material 11 to be supplied is 0 mass% can be gradually widened or narrowed.
However, when the supply amount of the sintering raw material fluctuates (increases or decreases) by 3% by mass or more, it is preferable to adjust the distances a1 and a2 on the downstream side of the bars 17 to 19. According to the knowledge of the present inventors, even if the supply amount of the sintering raw material is constant, the segregation degree has a certain variation. However, if the supply amount of the sintering raw material varies by about 3% by mass, the segregation degree is significant. Change (deterioration) occurs.
Therefore, when the supply amount of the sintering raw material changes by at least 3% by mass or more, the intervals a1 and a2 on the downstream side of the bars 17 to 19 may be changed. In addition, although the upper limit of the fluctuation | variation of the supply amount of a sintering raw material is not prescribed | regulated, in actual operation, it is about 50 mass%.

次に、本発明の作用効果を確認するために行った実施例について説明する。
ここでは、図1(A)、(B)、図2(A)〜(D)に示す焼結原料の装入装置10を使用して、パレット14への焼結原料11の装入を行った。詳細には、原料を造粒して得た平均径2〜5mmの焼結原料11(擬似粒子)を貯蔵した貯蔵ホッパー12から、ドラムフィーダー13のドラムを回転させ、焼結原料11を、貯蔵ホッパー12から装入シュート15に切り出して滑走させた。そして、焼結原料11を、装入シュート15の下流側に設けられたバースクリーン16上に落下させて分級することにより、パレット14上に、上層が細かく、かつ下層が粗くなるように装入した。
Next, examples carried out for confirming the effects of the present invention will be described.
Here, the sintered raw material 11 is charged into the pallet 14 using the sintered raw material charging device 10 shown in FIGS. 1 (A), 1 (B) and 2 (A) to 2 (D). It was. Specifically, the drum of the drum feeder 13 is rotated from the storage hopper 12 storing the sintered raw material 11 (pseudo particles) having an average diameter of 2 to 5 mm obtained by granulating the raw material, and the sintered raw material 11 is stored. The hopper 12 was cut into the charging chute 15 and slid. Then, by dropping the sintered raw material 11 onto a bar screen 16 provided on the downstream side of the charging chute 15 and classifying it, the charging is performed so that the upper layer is fine and the lower layer is rough on the pallet 14. did.

なお、表2に、パレットへの焼結原料の供給量を200(トン/時間/m)から250(トン/時間/m)へ増加させた場合のバースクリーンの試験条件を、また表3に、試験条件の内容をそれぞれ示す。 Table 2 shows the bar screen test conditions when the supply amount of the sintering raw material to the pallet is increased from 200 (tons / hour / m) to 250 (tons / hour / m). The contents of the test conditions are shown respectively.

Figure 0005494512
Figure 0005494512

Figure 0005494512
Figure 0005494512

表3に示す条件2は、条件1の1段目と2段目のバーの先端間隔a1、及び2段目と3段目のバーの先端間隔a2が、それぞれ5mmずつ広がるように、2段目と3段目のバーをそれぞれ下方へ平行移動させた条件である。また、条件3は、条件1の1段目と2段目のバーの先端間隔a1、及び2段目と3段目のバーの先端間隔a2が、それぞれ5mmずつ広がるように、2段目と3段目のバーの基端を起点として角度変更した条件である。 Condition 2 shown in Table 3 is that the first step and second step bar tip interval a1 of condition 1 and the second step and third step bar tip interval a2 are each increased by 5 mm. This is a condition in which the eyes and the third-stage bar are each translated downward. In condition 3, the first step and second step bar tip intervals a1 and the second step and third step bar tip intervals a2 of condition 1 are increased by 5 mm, respectively. This is a condition in which the angle is changed starting from the base end of the third-stage bar.

まず、パレットへの焼結原料の供給量を200(トン/時間/m)から250(トン/時間/m)へ増加させた場合の焼結原料層の偏析度について、図5を参照しながら説明する。
図5から明らかなように、パレットへの焼結原料の供給量を増加させると、バーの間隔を変更しない比較例(条件1のまま)の偏析度の低下量は大きかった(0.4程度)が、バーの間隔を変更した実施例1、2の偏析度の低下量は、比較例と比較して小さかった(実施例1:0.17程度、実施例2:0.1程度)。特に、バーの間隔をバーの角度調整により変更した実施例2(条件1から条件3)は、バーの間隔をバーの平行移動により変更した実施例1(条件1から条件2)よりも、偏析度の低下量を小さくできた。
First, the segregation degree of the sintering material layer when the supply amount of the sintering material to the pallet is increased from 200 (ton / hour / m) to 250 (ton / hour / m) with reference to FIG. explain.
As is apparent from FIG. 5, when the supply amount of the sintering raw material to the pallet is increased, the amount of decrease in the segregation degree of the comparative example (condition 1 remains unchanged) in which the bar interval is not changed is large (about 0.4). However, the amount of decrease in the degree of segregation in Examples 1 and 2 in which the bar interval was changed was smaller than that in the comparative example (Example 1: about 0.17, Example 2: about 0.1). In particular, Example 2 (condition 1 to condition 3) in which the bar interval was changed by adjusting the angle of the bar is more segregated than Example 1 (condition 1 to condition 2) in which the bar interval was changed by parallel movement of the bar. The amount of decrease in degree could be reduced.

次に、パレットへの焼結原料の供給量を200(トン/時間/m)から250(トン/時間/m)へ増加させた場合の焼結鉱の歩留り(成品歩留り:質量%)について、図6を参照しながら説明する。
図6から明らかなように、パレットへの焼結原料の供給量を増加させると、バーの間隔を変更しない比較例の成品歩留りの低下量は大きかった(5質量%程度)が、バーの間隔を変更した実施例1、2の成品歩留りの低下量は、比較例と比較して小さかった(実施例1:2.5質量%程度、実施例2:1.5質量%程度)。特に、バーの間隔をバーの角度調整により変更した実施例2は、実施例1よりも成品歩留りの低下量を小さくできた。
Next, regarding the yield of sintered ore (product yield: mass%) when the supply amount of the sintering raw material to the pallet is increased from 200 (tons / hour / m) to 250 (tons / hour / m), This will be described with reference to FIG.
As is apparent from FIG. 6, when the supply amount of the sintering raw material to the pallet was increased, the decrease in the product yield of the comparative example in which the bar interval was not changed was large (about 5% by mass). The amount of decrease in the product yield of Examples 1 and 2 in which the above was changed was smaller than that of the comparative example (Example 1: about 2.5% by mass, Example 2: about 1.5% by mass). In particular, Example 2 in which the interval between bars was changed by adjusting the angle of the bar was able to reduce the amount of decrease in product yield compared to Example 1.

最後に、パレットへの焼結原料の供給量を200(トン/時間/m)から250(トン/時間/m)へ増加させた場合の焼結鉱の生産性(トン/日/m)について、図7を参照しながら説明する。
図7から明らかなように、パレットへの焼結原料の供給量を増加させると、バーの間隔を変更した実施例1、2の生産性の増加量を、バーの間隔を変更しない比較例の生産性の増加量よりも高めることができた。特に、バーの間隔をバーの角度調整により変更した実施例2は、実施例1よりも生産性を増加できた。
Finally, the productivity of the sintered ore when the supply amount of the sintering raw material to the pallet is increased from 200 (ton / hour / m) to 250 (ton / hour / m) (ton / day / m 2 ). Will be described with reference to FIG.
As is clear from FIG. 7, when the supply amount of the sintering raw material to the pallet is increased, the increase in productivity of Examples 1 and 2 in which the bar interval is changed is the same as that in the comparative example in which the bar interval is not changed. It was possible to increase more than the increase in productivity. In particular, Example 2 in which the interval between bars was changed by adjusting the angle of the bar was able to increase productivity compared to Example 1.

以上のことから、本発明の焼結原料の装入方法、即ち、パレットへ装入される焼結原料の供給量の変動に応じて、各バーの下流側の間隔を調整することで、焼結鉱の歩留りが時系列的に低下していく現象を抑制し、高位な歩留りを実現できることを確認できた。 From the above, the method of charging the sintered raw material of the present invention, that is, by adjusting the interval on the downstream side of each bar in accordance with the fluctuation of the supply amount of the sintered raw material charged into the pallet, It was confirmed that high yields could be achieved by suppressing the phenomenon of yield reduction in time series.

以上、本発明を、実施の形態を参照して説明してきたが、本発明は何ら上記した実施の形態に記載の構成に限定されるものではなく、特許請求の範囲に記載されている事項の範囲内で考えられるその他の実施の形態や変形例も含むものである。例えば、前記したそれぞれの実施の形態や変形例の一部又は全部を組合せて本発明の焼結原料の装入方法を構成する場合も本発明の権利範囲に含まれる。
また、前記実施の形態においては、パレットへ供給される焼結原料の供給量が増加したときに側面視して上下方向に隣り合うバーの下流側の間隔を広くし、供給量が減少したときに側面視して上下方向に隣り合うバーの下流側の間隔を狭くした場合について説明した。しかし、焼結原料の供給量が減少したときには各バーの下流側の間隔を変更せずに、供給量が増加したときのみ各バーの下流側の間隔を広くし、又は焼結原料の供給量が増加したときには各バーの下流側の間隔を変更せずに、供給量が減少したときのみ各バーの下流側の間隔を狭くすることもできる。
As described above, the present invention has been described with reference to the embodiment. However, the present invention is not limited to the configuration described in the above embodiment, and the matters described in the scope of claims. Other embodiments and modifications conceivable within the scope are also included. For example, a case where the method for charging a sintered raw material of the present invention is configured by combining a part or all of the above-described embodiments and modifications is also included in the scope of the right of the present invention.
Further, in the embodiment, when the supply amount of the sintering raw material supplied to the pallet is increased, the interval between the bars adjacent to each other in the vertical direction is widened in a side view, and the supply amount is decreased. The case where the space | interval of the downstream of the bar | burr adjacent to an up-down direction is narrowed by side view was demonstrated. However, when the supply amount of the sintering raw material decreases, the interval on the downstream side of each bar is not changed, and only when the supply amount increases, the interval on the downstream side of each bar is widened, or the supply amount of the sintering raw material It is also possible to narrow the interval on the downstream side of each bar only when the supply amount is reduced without changing the interval on the downstream side of each bar when the value increases.

10:焼結原料の装入装置、11:焼結原料、12:貯蔵ホッパー、13:ドラムフィーダー、14:パレット、15:装入シュート、16:バースクリーン、17〜19:バー、20:放出口 10: Sintering raw material charging device, 11: Sintering raw material, 12: Storage hopper, 13: Drum feeder, 14: Pallet, 15: Charging chute, 16: Bar screen, 17-19: Bar, 20: Release Exit

Claims (3)

焼結原料の装入シュートの下流側に、該装入シュートの幅方向に間隔を有して配置され前記焼結原料の流下方向に沿って延在する複数のバーを備え、しかも側面視して上下方向に隣り合う該バーの下流側の間隔を上流側の間隔よりも広くしたバースクリーンを設け、ドラムフィーダーで供給される前記焼結原料を、前記装入シュートを介し、前記バースクリーンで分級しながらパレットへ装入する焼結原料の装入方法において、
前記パレットの単位幅かつ単位時間当たりに前記パレットへ供給される前記焼結原料の供給量が、予め設定した量以上に増加したことを条件として、前記側面視して上下方向に隣り合うバーの下流側の間隔を、前記焼結原料の供給量が増加する前の間隔よりも広くすることを特徴とする焼結原料の装入方法。
Provided on the downstream side of the charging chute for the sintering raw material is provided with a plurality of bars arranged in the width direction of the charging chute and extending along the flow-down direction of the sintering raw material. Provided with a bar screen in which the interval on the downstream side of the bars adjacent to each other in the vertical direction is wider than the interval on the upstream side, and the sintered raw material supplied by the drum feeder is passed through the charging chute by the bar screen. In the charging method of the sintering raw material that is charged into the pallet while classifying,
On the condition that the supply amount of the sintering raw material supplied to the pallet per unit width and unit time of the pallet is increased to a preset amount or more, the bars adjacent to each other in the vertical direction in the side view A method for charging a sintered material, characterized in that a downstream space is made wider than a space before the supply amount of the sintered material is increased.
焼結原料の装入シュートの下流側に、該装入シュートの幅方向に間隔を有して配置され前記焼結原料の流下方向に沿って延在する複数のバーを備え、しかも側面視して上下方向に隣り合う該バーの下流側の間隔を上流側の間隔よりも広くしたバースクリーンを設け、ドラムフィーダーで供給される前記焼結原料を、前記装入シュートを介し、前記バースクリーンで分級しながらパレットへ装入する焼結原料の装入方法において、
前記パレットの単位幅かつ単位時間当たりに前記パレットへ供給される前記焼結原料の供給量が、予め設定した量以下に減少したことを条件として、前記側面視して上下方向に隣り合うバーの下流側の間隔を、前記焼結原料の供給量が減少する前の間隔よりも狭くすることを特徴とする焼結原料の装入方法。
Provided on the downstream side of the charging chute for the sintering raw material is provided with a plurality of bars arranged in the width direction of the charging chute and extending along the flow-down direction of the sintering raw material. Provided with a bar screen in which the interval on the downstream side of the bars adjacent to each other in the vertical direction is wider than the interval on the upstream side, and the sintered raw material supplied by the drum feeder is passed through the charging chute by the bar screen. In the charging method of the sintering raw material that is charged into the pallet while classifying,
On the condition that the supply amount of the sintering raw material supplied to the pallet per unit width and unit time of the pallet is reduced to a predetermined amount or less, the bars adjacent to each other in the vertical direction when viewed from the side are used. A method for charging a sintered material, characterized in that an interval on the downstream side is narrower than an interval before the supply amount of the sintered material is reduced.
請求項1又は2記載の焼結原料の装入方法において、前記側面視して上下方向に隣り合うバーの下流側の間隔は、該各バーの傾斜角度を調整して行うことを特徴とする焼結原料の装入方法。 3. The method for charging a sintered material according to claim 1, wherein the interval between the bars adjacent to each other in the vertical direction when viewed from the side is adjusted by adjusting the inclination angle of each bar. A method for charging sintered raw materials.
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JPS6436708A (en) * 1987-07-31 1989-02-07 Nippon Steel Corp Method for charging sintered raw material
JPH03249137A (en) * 1990-02-28 1991-11-07 Nippon Steel Corp Method for charging sintering raw material
JPH07138663A (en) * 1993-11-16 1995-05-30 Nippon Steel Corp Method for charging sintering raw material
JPH07278685A (en) * 1994-04-11 1995-10-24 Nippon Steel Corp Operation method of sintering machine
JPH08127822A (en) * 1994-10-31 1996-05-21 Nippon Steel Corp Operation of sintering

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