JP2003314966A - Pallet truck for sintering machine and its air permeability adjusting method - Google Patents

Pallet truck for sintering machine and its air permeability adjusting method

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Publication number
JP2003314966A
JP2003314966A JP2002122176A JP2002122176A JP2003314966A JP 2003314966 A JP2003314966 A JP 2003314966A JP 2002122176 A JP2002122176 A JP 2002122176A JP 2002122176 A JP2002122176 A JP 2002122176A JP 2003314966 A JP2003314966 A JP 2003314966A
Authority
JP
Japan
Prior art keywords
pallet
pallet truck
breathable
sintering machine
bed
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.)
Withdrawn
Application number
JP2002122176A
Other languages
Japanese (ja)
Inventor
Yohei Ito
洋平 伊藤
Shunji Kasama
俊次 笠間
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2002122176A priority Critical patent/JP2003314966A/en
Publication of JP2003314966A publication Critical patent/JP2003314966A/en
Withdrawn legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pallet truck for a sintering machine and its air permeability adjusting method wherein the permeability in the vicinity of a pallet side wall is reliably suppressed without impairing productivity. <P>SOLUTION: In this lower suction type pallet truck 15 for the sintering machine and its air permeability adjusting method, a non-permeable plate 10 is provided to both side parts of a permeable grate 16 provided at a center part in a width direction of the pallet truck 15 for the sintering machine, a bedding ore is layed over the non-permeable plate 10 and the permeable grate 16, and a sintering raw material is layed over the bedding ore. The pallet truck 15 is provided with a step Y where a top face position of the non-permeable plate 10 is lower than that of the permeable hearth 16 to adjust the permeability at a side of the pallet truck 15. <P>COPYRIGHT: (C)2004,JPO

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、焼結機におけるパ
レット台車とその通気性を調整する方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pallet truck for a sintering machine and a method for adjusting its air permeability.

【0002】[0002]

【従来の技術】高炉に装入する焼結鉱を製造するドワイ
トロイド式(下方吸引式)焼結機では、図2に示すよう
に、先ず、床敷鉱ホッパー1より粒径10〜20mmの
床敷鉱2をパレット台車3上に装入し、更に、その上
に、粒径1〜7mmに擬似造粒した焼結原料4(粉鉄鉱
石、粉石灰石などと粉コークスなどを混合した配合原
料)を原料ホッパー5からドラムフィーダー6、装入装
置7を順次介して装入して焼結原料層8を形成する。そ
して、パレット台車3上方に設けた点火炉9により焼結
原料層8の表面に点火され、さらに、該パレット台車3
下方から吸気される。これにより、表面点火された焼結
原料層8は、パレット台車3の移動に伴って表面から下
向きに通過する空気によって焼結反応を下方に移行さ
せ、排出部に達する間に全層にわたって焼結反応を終了
し、連続的にケーキ状の焼結鉱となって排出される。前
記床敷鉱を装入するのは、焼結原料がパレット台車3の
通気性火床の間からこぼれ落ちるのを防ぐ効果と、熱源
(粉コークス)を含む焼結原料が直接的に通気性火床に
接触し溶着(原料が融けた状態で火床に付いたまま離れ
なくなる現象)することを防ぐためである。
2. Description of the Related Art In a Dwightroid type (downward suction type) sinter machine for producing sinter ore charged into a blast furnace, as shown in FIG. Bedbed ore 2 is loaded on a pallet trolley 3, and a sintering raw material 4 (powdered iron ore, powdered limestone, etc. and powdered coke, etc.) is mixed on the pallet truck 3. (Raw material) is sequentially charged from the raw material hopper 5 through the drum feeder 6 and the charging device 7 to form the sintering raw material layer 8. Then, the surface of the sintering raw material layer 8 is ignited by an ignition furnace 9 provided above the pallet truck 3, and the pallet truck 3 is further ignited.
Inhaled from below. As a result, the surface-ignited sintering raw material layer 8 shifts the sintering reaction downward by the air passing downward from the surface with the movement of the pallet truck 3, and the sintering raw material layer 8 is entirely sintered while reaching the discharge portion. After the reaction is completed, cake-shaped sinter is continuously discharged. The charging of the bed mat ore is effective for preventing the sintering raw material from spilling from between the breathable fire beds of the pallet trolley 3 and the sintering raw material containing the heat source (powder coke) is directly breathable. This is to prevent the material from coming into contact with and welding (a phenomenon in which the raw material melts and remains attached to the fire bed and does not separate).

【0003】このドワイトロイド式焼結機による焼結で
はパレット台車3の側壁(以下パレット側壁と称す)近
傍は壁効果により焼結原料層8の幅方向中央部より通気
性が良好で、過剰に空気が流れる。これは、パレット台
車3の幅方向中央部における焼結原料層8とパレット側
壁近傍における焼結原料層8では空隙率が異なり、原料
粒子同士が十分に充填されている中央部に比べてパレッ
ト側壁近傍で空隙率が大きいからである。更に、焼結原
料層8の焼結が進行するにつれて、焼結原料が焼きしま
るため、側壁近傍に収縮隙間が発生し、空気が過剰に流
れるのを助長するためである。このため、パレット台車
3のパレット側壁近傍では、過剰空気により焼結時間が
短縮され、両端部での必要な焼結反応が行なわれず、ま
た、中央部の空気不足を招き焼結反応に悪影響を及ぼ
し、焼結鉱の歩留まりが悪化する。この問題を解決する
ために、特開平3−211240号公報にはパレット台
車上に装入する床敷鉱を、パレット幅方向で変化させ、
パレット幅方向の通気性を均一にする方法が提案されて
いる。また、特開平5−71879号公報には、パレッ
ト側壁近傍に非通気性板を設置して、パレット側壁近傍
の通気性を抑制して、パレット幅方向における通気性の
均一化を図る方法が提案されている。
In the sintering by the Dwightroid type sintering machine, the vicinity of the side wall of the pallet truck 3 (hereinafter referred to as the pallet side wall) has a better air permeability than the center portion in the width direction of the sintering raw material layer 8 due to the wall effect, and excessively. The air flows. This is because the sintering raw material layer 8 in the central portion in the width direction of the pallet truck 3 and the sintering raw material layer 8 in the vicinity of the pallet side wall have different porosities, and the pallet side wall is larger than the central portion in which the raw material particles are sufficiently filled. This is because the porosity is large in the vicinity. Further, the sintering raw material is burned as the sintering of the sintering raw material layer 8 progresses, so that a shrinkage gap is generated in the vicinity of the side wall, which promotes excessive air flow. Therefore, in the vicinity of the pallet side wall of the pallet truck 3, the sintering time is shortened by the excess air, the necessary sintering reaction is not performed at both ends, and the central portion is deficient in air, which adversely affects the sintering reaction. This will affect the yield of the sintered ore. In order to solve this problem, Japanese Patent Laid-Open No. 3-211240 discloses that the bed ore loaded on the pallet truck is changed in the pallet width direction.
A method of making the air permeability in the pallet width direction uniform has been proposed. Further, Japanese Patent Laid-Open No. 5-71879 proposes a method of installing a non-breathable plate near the side wall of a pallet to suppress air permeability near the side wall of the pallet so as to make the air permeability in the pallet width direction uniform. Has been done.

【0004】[0004]

【発明が解決しようとしている課題】しかし、前記特開
平3−211240号公報の方法は、パレット幅方向中
央部における床敷鉱の層厚を厚くするため、その分、焼
結原料の装入量が低下して生産性が落ちる問題がある。
またパレット側壁近傍から流入した空気量を抑制するよ
りもむしろ、中央部の空気量を増加させ空気流速の均一
化を図る方法なので、基本的に単位原料あたりの風量が
増加し電力原単位が悪化する問題がある。また、特開平
5−71879号公報の方法においては、床敷鉱がパレ
ット幅方向に均等に装入されているため、パレット側壁
近傍から流入した空気が床敷鉱層を通して、パレット幅
方向中央部の通気性火床に流れ込む事から、パレット側
壁近傍に非通気性板を設置しても、パレット側壁近傍の
通気性を大幅に抑制する効果を得る事が不可能であっ
た。本発明は、生産性を阻害する事なく、パレット側壁
近傍の通気性を確実に抑制することを課題とするもので
ある。
However, in the method disclosed in Japanese Patent Laid-Open No. 3-211240, the bed thickness of the bed ore at the center of the pallet in the width direction is increased. However, there is a problem in that the productivity decreases and productivity drops.
Also, rather than suppressing the amount of air that has flowed in from the side wall of the pallet, it is a method of increasing the amount of air in the central part and making the air flow rate uniform, so basically the amount of air per unit raw material increases and the electricity consumption rate deteriorates. I have a problem to do. Further, in the method disclosed in Japanese Patent Laid-Open No. 5-71879, since the bed ore is uniformly loaded in the pallet width direction, the air flowing in from the vicinity of the pallet side wall passes through the bed ore layer and flows through the center of the pallet width direction. Since it flows into the breathable fire bed, even if a non-breathable plate is installed near the side wall of the pallet, it is not possible to obtain the effect of significantly suppressing the breathability near the side wall of the pallet. An object of the present invention is to reliably suppress air permeability near the side wall of a pallet without impeding productivity.

【0005】[0005]

【課題を解決するための手段】本発明は、前記課題を解
決するためになされたものであり、その手段1は、焼結
機のパレット台車の幅方向中央部に設けた通気性火床の
両側部に非通気性板を設け、該非通気性板及び通気性火
床上に床敷鉱を装入し、更に、その上部に焼結原料を装
入する下方吸引式の焼結機のパレット台車において、該
パレット台車には前記非通気性板の上面位置を前記通気
性火床の上面位置の高さよりも低くした段差を設けた焼
結機のパレット台車である。手段2は、前記段差が20
〜30mmである手段1記載の焼結機のパレット台車で
ある。手段3は、前記非通気性板の幅を、前記通気性火
床の幅に対して3〜9%にする前記手段1又は2記載の
焼結機のパレット台車である。手段4は、前記手段1〜
3のいずれか1に記載の構造のパレット台車上に床敷鉱
を装入するに際し、前記通気性火床上に装入する床敷鉱
と前記非通気性板上に装入する床敷鉱のラップ厚さを調
整して、前記パレット台車側部の通気性を調整する焼結
機のパレット台車の通気性調整方法である。手段5は、
前記ラップ厚さを10〜20mmとする手段4記載の焼
結機のパレット台車の通気性調整方法である。
Means for Solving the Problems The present invention has been made to solve the above-mentioned problems, and means 1 thereof is for a breathable fire bed provided in a center portion in the width direction of a pallet truck of a sintering machine. A pallet truck for a downward suction type sintering machine in which a non-breathable plate is provided on both sides, a bed ore is loaded on the non-breathable plate and the breathable fire bed, and a sintering raw material is further loaded on the top. In the pallet truck of the sintering machine, the pallet truck is provided with a step in which the upper surface of the non-breathable plate is lower than the height of the upper surface of the breathable fire bed. The means 2 has the step difference of 20.
The pallet truck of the sintering machine according to means 1, which is ˜30 mm. The means 3 is the pallet truck of the sintering machine according to the means 1 or 2, wherein the width of the non-permeable plate is 3 to 9% of the width of the permeable fire bed. The means 4 is the means 1 to
When loading bedding ore on the pallet trolley having the structure according to any one of 3 above, the bed ore to be loaded on the breathable fire bed and the bed ore to be loaded on the non-permeable plate This is a method for adjusting the air permeability of a pallet truck of a sintering machine, which adjusts the lap thickness to adjust the air permeability of the side portion of the pallet truck. The means 5 is
The method for adjusting the air permeability of a pallet truck of a sintering machine according to means 4, wherein the wrap thickness is 10 to 20 mm.

【0006】[0006]

【発明の実施の形態】以下に、本発明の一実施の形態に
係る焼結機のパレット台車15を図1に基づいて説明す
る。図1に示すように、本発明の一実施の形態に係る焼
結機のパレット台車15は、幅方向中央部を複数のグレ
ートバー(火格子)11を並べて構成した通気性火床1
6と、その両側に非通気性の平板で構成した非通気性板
10を有している。そして、非通気性板10の上面位置
を通気性火床16の上面位置の高さより20〜30mm
低くして段差Yを形成する。そして、この非通気性板1
0と通気性火床16上に床敷鉱をパレット台車15の幅
方向にほぼ均等の層厚(30〜40mm)で装入した
後、焼結原料を装入する。これにより、非通気性板10
と通気性火床16の境界部17には、この段差Yと床敷
鉱層12の層厚に応じたラップ部X(連続した床敷鉱
層)が形成される。
BEST MODE FOR CARRYING OUT THE INVENTION A pallet truck 15 of a sintering machine according to an embodiment of the present invention will be described below with reference to FIG. As shown in FIG. 1, a pallet truck 15 of a sintering machine according to an embodiment of the present invention has a breathable fire bed 1 in which a plurality of great bars (grates) 11 are arranged side by side in the widthwise central portion.
6 and a non-breathable plate 10 composed of a non-breathable flat plate on both sides thereof. And the upper surface position of the non-breathable plate 10 is 20 to 30 mm from the height of the upper surface position of the breathable fire bed 16.
The height is lowered to form the step Y. And this non-breathable plate 1
No. 0 and the breathable fire bed 16 are loaded with bed mat in a width direction of the pallet truck 15 with a substantially uniform layer thickness (30 to 40 mm), and then a sintering raw material is loaded. Thereby, the non-breathable plate 10
At the boundary portion 17 between the and the breathable fire bed 16, the step Y and the lap portion X (continuous bed deposit layer) corresponding to the layer thickness of the bed deposit layer 12 are formed.

【0007】この状態で、パレット台車15下方から吸
気されると、パレット側壁(サイドウォール)13と焼
結原料層18の間に形成された収縮隙間δ(焼結原料の
焼き締りにより形成された隙間)及びパレット側壁13
の近傍の焼結原料層18上面から流入した空気は非通気
性板10を通過出来ずに、床敷鉱層12内を矢印Z方向
に流れ、床敷鉱層12のラップ部Xを通って通気性火床
16から流出する。このように、床敷鉱層12のラップ
部Xは矢印Z方向に流れる吸引空気の通路となることか
ら、このラップ部Xの層厚に応じて、矢印Z方向に流れ
る吸引空気の通気量が変化する。つまり、本実施の形態
は、非通気性板10の上面を通気性火床16の上面より
低くして段差Yを形成する事により、床敷鉱層12のラ
ップ部Xの層厚を薄くする事が可能となり、パレット側
壁13の近傍(収縮隙間δ及びパレット側壁13の焼結
原料層18上面近傍)の通気性を抑制する事が出来る。
そして、段差Yを20〜30mmとする事が好ましい。
これは、床敷鉱層12の層厚が前記したように30〜4
0mmで有り、且つ、床敷鉱の粒径が10〜20mmで
あり、またラップ部Xの層厚は、図3に示すように、1
0mm未満になると通気性が悪化し、パレット側壁の近
傍に風が流れ難くなるため、焼結反応が促進し難くなり
未焼結部分が生じる。従って、ラップ部Xの層厚を10
mm以上にするためには段差Yを30mm以下にする事
が好ましい。また、段差Yを大きくすると焼結鉱の生産
性に影響を与えると共に、ラップ部Xの層厚が20mm
超になると通気性に殆ど変化はなくなる事から、段差Y
を20mm以上にする事が好ましい。
In this state, when air is taken in from below the pallet truck 15, a shrinkage gap δ formed between the pallet side wall (sidewall) 13 and the sintering raw material layer 18 (formed by sintering sintering raw material is formed. Gap) and pallet side wall 13
The air that has flowed in from the upper surface of the sintering raw material layer 18 in the vicinity of does not pass through the non-breathable plate 10, flows in the direction of the arrow Z in the bed ore layer 12, and passes through the lap portion X of the bed ore layer 12 for air permeability. It flows out of the fire bed 16. As described above, since the lap portion X of the bed ore layer 12 serves as a passage for the suction air flowing in the arrow Z direction, the ventilation amount of the suction air flowing in the arrow Z direction changes according to the layer thickness of the lap portion X. To do. That is, in the present embodiment, the upper surface of the non-breathable plate 10 is made lower than the upper surface of the breathable fire bed 16 to form the step Y, so that the layer thickness of the lap portion X of the bed ore layer 12 is reduced. Thus, the air permeability in the vicinity of the pallet side wall 13 (in the vicinity of the shrinkage gap δ and the upper surface of the sintering raw material layer 18 of the pallet side wall 13) can be suppressed.
Then, it is preferable that the step Y is 20 to 30 mm.
This is because the bed ore bed 12 has a layer thickness of 30 to 4 as described above.
0 mm, the particle diameter of the bed ore is 10 to 20 mm, and the layer thickness of the lap portion X is 1 as shown in FIG.
If it is less than 0 mm, the air permeability is deteriorated, and it becomes difficult for the air to flow near the side wall of the pallet, so that the sintering reaction is hard to be promoted and an unsintered portion is generated. Therefore, the layer thickness of the lap portion X is 10
It is preferable that the step Y is 30 mm or less in order to make the thickness more than mm. Further, if the step Y is increased, the productivity of the sintered ore is affected and the layer thickness of the lap portion X is 20 mm.
If it exceeds, there will be almost no change in breathability, so the step Y
Is preferably 20 mm or more.

【0008】また、非通気性板10の幅W10を通気性火
床16の幅W9 に対して3〜9%にする事が好ましい。
これは図4(段差Yが20mmの場合)に示すように3
%未満は、非通気性板の効果が小さく、パレット側壁近
傍からの過剰空気量が段差Yを設けても解消できず歩留
が低下するからである。また9%超では、パレット側壁
近傍に焼成に必要な風量を確保する事が困難となり未焼
原料を生じて歩留が低下する。
The width W 10 of the non-breathable plate 10 is preferably 3 to 9% of the width W 9 of the breathable fire bed 16.
This is 3 as shown in FIG. 4 (when the step Y is 20 mm).
If it is less than%, the effect of the non-breathable plate is small, and the excess air amount from the vicinity of the pallet side wall cannot be eliminated even if the step Y is provided, and the yield is reduced. On the other hand, if it exceeds 9%, it becomes difficult to secure the air volume necessary for firing near the side wall of the pallet, and unburned raw materials are produced to lower the yield.

【0009】更に、パレット台車15上に床敷鉱を装入
するに際して、非通気性板10及び通気性火床16上に
装入する床敷鉱量を調整して、段差部に形成される床敷
鉱層12のラップ部Xの層厚を制御して、パレット台車
15の側部の通気性を調整する。これは、生産性を調整
するために焼結原料層18の層厚を変えた場合に、パレ
ット側壁13の近傍の通気性を調整する必要が生じるか
らである。この際、パレット台車15の幅方向全体の床
敷鉱層12の層厚、又は、非通気性板10上のみの層厚
を調整する事により、ラップ部Xの層厚を制御して、目
標とするパレット側壁13の近傍の通気性を確保するこ
とができる。しかし、ラップ部Xの層厚が20mm超に
なると、この部分における通気が良好になり過ぎて段差
Yの効果(通気抑制効果)がなくなり、また、10mm
未満になると、上記とは逆に、この部分における通気が
低減して、焼成に必要な風量を確保する事が困難となる
ことから、ラップ部Xの層厚は10〜20mmとし、こ
の範囲内で前記層厚を調整する事が好ましい。
Further, when the bed ore is charged on the pallet truck 15, the amount of the bed ore charged on the non-permeable plate 10 and the permeable fire bed 16 is adjusted to form the stepped portion. By controlling the layer thickness of the lap portion X of the floor laid ore layer 12, the air permeability of the side portion of the pallet truck 15 is adjusted. This is because it is necessary to adjust the air permeability in the vicinity of the pallet side wall 13 when the layer thickness of the sintering raw material layer 18 is changed to adjust the productivity. At this time, by adjusting the layer thickness of the floor laying ore layer 12 in the entire width direction of the pallet truck 15 or the layer thickness only on the non-breathable plate 10, the layer thickness of the lap portion X is controlled to achieve the target. The air permeability in the vicinity of the pallet side wall 13 can be ensured. However, when the layer thickness of the lap portion X exceeds 20 mm, ventilation in this portion becomes too good, and the effect of the step Y (ventilation suppression effect) disappears, and 10 mm
If it is less than the above, on the contrary to the above, ventilation in this portion is reduced, and it becomes difficult to secure the air volume necessary for firing, so the layer thickness of the lap portion X is set to 10 to 20 mm, within this range. It is preferable to adjust the layer thickness with.

【0010】[0010]

【実施例】本発明の実施例を、生産能力:16000t
/day、焼結パレット面積:600m2 、パレット台
車幅:5.5m、下方吸引用ブロワー能力2700m3
/minのドワイトロイド式焼結機に適応した場合で説
明する。また、非通気性板10の幅W10を160〜45
0mmとし、通気性火床16の幅W9 を4.6〜5.3
mとした。また、非通気性板10上面と通気性火床16
上面の段差Yを15〜35mmとした。また、パレット
台車15の焼結原料の層厚は600mmで、床敷鉱の粒
度は10〜20mm、ラップ部Xは5〜25mmとし
た。パレット側壁13の近傍及び中央部の通気性を測定
するために、図5に示すように着火後の焼結原料層18
上に直径100mm、長さ500mmの円筒14を設置
し円筒14内を通過する風速を測定して評価した。表1
に本発明例と比較例との操業結果を示す。操業は段差
Y、非通気性板幅、通気性火床幅、床敷鉱層のラップ部
Xをそれぞれ変化させて、パレット側壁部の空気流量と
歩留にて比較評価を行なった。本発明例1〜4は本発明
の範囲内であることから、良好な製品歩留まりを得る事
が出来た。
EXAMPLE An example of the present invention has a production capacity of 16000t.
/ Day, sintering pallet area: 600 m 2 , pallet truck width: 5.5 m, downward suction blower capacity 2700 m 3
The description will be made in the case of being applied to a Dwightroid-type sintering machine of / min. In addition, the width W 10 of the non-breathable plate 10 is set to 160 to 45.
0 mm, and the width W 9 of the breathable fire bed 16 is 4.6 to 5.3.
m. In addition, the upper surface of the non-breathable plate 10 and the breathable fire bed 16
The step Y on the upper surface was set to 15 to 35 mm. Further, the layer thickness of the sintering raw material of the pallet truck 15 was 600 mm, the particle size of the bed ore was 10 to 20 mm, and the lap portion X was 5 to 25 mm. In order to measure the air permeability in the vicinity of the pallet side wall 13 and in the central portion, as shown in FIG. 5, the sintering raw material layer 18 after ignition was used.
A cylinder 14 having a diameter of 100 mm and a length of 500 mm was installed on the top, and the wind speed passing through the cylinder 14 was measured and evaluated. Table 1
The operation results of the example of the present invention and the comparative example are shown in FIG. In the operation, the step Y, the non-breathable plate width, the breathable fire bed width, and the lap portion X of the bedding ore layer were changed, and the air flow rate and the yield of the pallet side wall portion were compared and evaluated. Since the invention examples 1 to 4 were within the scope of the invention, a good product yield could be obtained.

【0011】[0011]

【表1】 [Table 1]

【0012】また、比較例1、2は請求項2における比
較例で、この比較例1は段差Yが15mmで請求項2の
下限を外れた為に、パレット側壁部の風速が高く歩留が
低減した。比較例2は段差が35mmで請求項2の上限
を外れた為に、パレット側壁部の風速が低く歩留が低減
した。比較例3、4は請求項3における比較例で、この
比較例3は非通気性板幅が通気性火床幅の1.9%で請
求項3の下限を外れた為に、パレット側壁部の風速が高
く歩留が低減した。比較例4は非通気性板幅が通気性火
床幅の9.8%で請求項3の上限を外れた為に、パレッ
ト側壁部の風速が低く歩留が低減した。比較例5、6は
請求項5における比較例で、比較例5はラップ部Xのラ
ップ量が5mmで請求項5の下限を外れた為に、パレッ
ト側壁部の風速が低減した。比較例6はラップ量が25
mmで請求項5の上限を外れたために、パレット側壁部
の風速が高く歩留が低減した。
Further, Comparative Examples 1 and 2 are Comparative Examples in Claim 2. In Comparative Example 1, the step Y is 15 mm, which is outside the lower limit of Claim 2, so that the wind speed on the side wall of the pallet is high and the yield is high. Reduced. In Comparative Example 2, the step difference was 35 mm, which was outside the upper limit of claim 2, so that the wind speed on the side wall of the pallet was low and the yield was reduced. Comparative examples 3 and 4 are comparative examples in claim 3, and in this comparative example 3, the non-breathable plate width is 1.9% of the breathable fire bed width, which is outside the lower limit of claim 3, and therefore the pallet side wall portion. The wind speed was high and the yield was reduced. In Comparative Example 4, the non-breathable plate width was 9.8% of the breathable fire bed width, which was outside the upper limit of claim 3, so the wind speed on the side wall of the pallet was low and the yield was reduced. Comparative Examples 5 and 6 are Comparative Examples in Claim 5, and in Comparative Example 5, the lap amount of the lap portion X was 5 mm, which was outside the lower limit of Claim 5, so the wind speed of the pallet side wall portion was reduced. Comparative Example 6 has a lap amount of 25
In mm, the upper limit of claim 5 was exceeded, so the wind velocity on the side wall of the pallet was high and the yield was reduced.

【0013】[0013]

【発明の効果】以上説明したように、本発明により、パ
レット側壁部近傍の通風が大幅に抑制され、パレット上
に装入した焼結原料層の両端部領域と中央部領域の風量
差が少なくなり、焼結鉱の歩留向上させる事が可能とな
り、この分野における効果は大きい。
As described above, according to the present invention, the ventilation near the side wall of the pallet is significantly suppressed, and the difference in air flow between the both end regions and the central region of the sintering raw material layer charged on the pallet is small. Therefore, it becomes possible to improve the yield of the sintered ore, and the effect in this field is great.

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

【図1】本発明の一実施の形態に係る焼結機のパレット
台車の簡略断面図である。
FIG. 1 is a simplified sectional view of a pallet truck of a sintering machine according to an embodiment of the present invention.

【図2】ドワイトロイド(DL)焼結機の全体構成の説
明図である。
FIG. 2 is an explanatory diagram of an overall configuration of a Dwightroid (DL) sintering machine.

【図3】パレット側壁部における平均風速と段差Yの関
係を示す説明図である。
FIG. 3 is an explanatory diagram showing a relationship between an average wind speed and a step Y on a side wall portion of a pallet.

【図4】非通気性板幅と通気性火床幅の比と歩留との関
係を示す説明図である。
FIG. 4 is an explanatory diagram showing a relationship between a ratio of a non-breathable plate width and a breathable fire bed width and a yield.

【図5】パレット側壁部の空気流量を測定する方法の模
式図である。
FIG. 5 is a schematic diagram of a method for measuring the air flow rate on the side wall of the pallet.

【符号の説明】[Explanation of symbols]

1:床敷鉱、2:床敷ホッパー、3:パレット台車、
4:配合原料、5:原料ホッパー、6:ドラムフィーダ
ー、7:装入装置、8:焼結原料層、9:点火炉、1
0:非通気性板、11:グレートバー(火格子)、1
2:床敷鉱層、13:パレット側壁(サイドウォー
ル)、14:円筒、15:パレット台車、16:通気性
火床、17:境界部、18:焼結原料層、X:床敷鉱層
のラップ部、Y:段差、Z:吸引空気の流れる方向
1: bedding mat, 2: bedding hopper, 3: pallet truck,
4: compounded raw material, 5: raw material hopper, 6: drum feeder, 7: charging device, 8: sintered raw material layer, 9: ignition furnace, 1
0: Non-breathable board, 11: Great bar (grate), 1
2: Bedbed ore layer, 13: Pallet side wall (sidewall), 14: Cylinder, 15: Pallet trolley, 16: Breathable fire bed, 17: Boundary part, 18: Sintering raw material layer, X: Wrapped bed orebed layer Part, Y: step, Z: direction of suction air flow

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 焼結機のパレット台車の幅方向中央部に
設けた通気性火床の両側部に非通気性板を設け、該非通
気性板及び通気性火床上に床敷鉱を装入し、更に、その
上部に焼結原料を装入する下方吸引式の焼結機のパレッ
ト台車において、該パレット台車には前記非通気性板の
上面位置を前記通気性火床の上面位置の高さよりも低く
した段差を設けることを特徴とする焼結機のパレット台
車。
1. A non-breathable plate is provided on both sides of a breathable fire bed provided in a center portion in the width direction of a pallet truck of a sintering machine, and a bed ore is loaded on the non-breathable board and the breathable fire bed. Further, in the pallet truck of the downward suction type sintering machine in which the sintering raw material is charged in the upper part, the upper surface position of the non-breathable plate is attached to the pallet carriage by the height of the upper surface position of the breathable fire bed. A pallet trolley for a sintering machine, which is characterized by providing a step lower than the height.
【請求項2】 前記段差が20〜30mmであることを
特徴とする請求項1記載の焼結機のパレット台車。
2. The pallet truck of the sintering machine according to claim 1, wherein the step is 20 to 30 mm.
【請求項3】 前記非通気性板の幅を、前記通気性火床
の幅に対して3〜9%にすることを特徴とする請求項1
又は2記載の焼結機のパレット台車。
3. The width of the non-breathable plate is 3 to 9% of the width of the breathable fire bed.
Alternatively, the pallet truck of the sintering machine described in 2.
【請求項4】 請求項1〜3のいずれか1項に記載のパ
レット台車上に床敷鉱を装入するに際し、前記通気性火
床上に装入する床敷鉱と前記非通気性板上に装入する床
敷鉱のラップ厚さを調整して、前記パレット台車側部の
通気性を調整することを特徴とする焼結機のパレット台
車の通気性調整方法。
4. A bedding ore that is charged on the breathable fire bed and a non-permeable plate when the bedding ore is charged on the pallet trolley according to any one of claims 1 to 3. The air permeability of the pallet truck of the sintering machine is adjusted by adjusting the wrap thickness of the bed ore charged in the pallet to adjust the air permeability of the side portion of the pallet truck.
【請求項5】 前記ラップ厚さを10〜20mmとする
ことを特徴とする請求項4記載の焼結機のパレット台車
の通気性調整方法。
5. The air permeability adjusting method for a pallet truck of a sintering machine according to claim 4, wherein the lap thickness is 10 to 20 mm.
JP2002122176A 2002-04-24 2002-04-24 Pallet truck for sintering machine and its air permeability adjusting method Withdrawn JP2003314966A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002122176A JP2003314966A (en) 2002-04-24 2002-04-24 Pallet truck for sintering machine and its air permeability adjusting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002122176A JP2003314966A (en) 2002-04-24 2002-04-24 Pallet truck for sintering machine and its air permeability adjusting method

Publications (1)

Publication Number Publication Date
JP2003314966A true JP2003314966A (en) 2003-11-06

Family

ID=29537864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002122176A Withdrawn JP2003314966A (en) 2002-04-24 2002-04-24 Pallet truck for sintering machine and its air permeability adjusting method

Country Status (1)

Country Link
JP (1) JP2003314966A (en)

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