JPH07286216A - Sintering method by waste gas circulation and waste gas circulation equipment - Google Patents

Sintering method by waste gas circulation and waste gas circulation equipment

Info

Publication number
JPH07286216A
JPH07286216A JP10327994A JP10327994A JPH07286216A JP H07286216 A JPH07286216 A JP H07286216A JP 10327994 A JP10327994 A JP 10327994A JP 10327994 A JP10327994 A JP 10327994A JP H07286216 A JPH07286216 A JP H07286216A
Authority
JP
Japan
Prior art keywords
sintering
exhaust gas
layer
machine
gas circulation
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Withdrawn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
JP10327994A
Other languages
Japanese (ja)
Inventor
Masami Fujimoto
政美 藤本
Yozo Hosoya
陽三 細谷
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 JP10327994A priority Critical patent/JPH07286216A/en
Publication of JPH07286216A publication Critical patent/JPH07286216A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To increase a sintering speed and to improve a sintering yield and productivity by supplying ordinary-temp. air in a range where pressure drop increases according to progression of sintering at the time of sintering by waste gas circulation using a lower suction sintering machine. CONSTITUTION:Raw materials 1 to be sintered are packed into a sintering pallet 8 by a surge hopper 2 and are sintered while this pallet 8 is moved. At this time, the waste gases are sucked into the sintering layer within a range where the progression ratio of sintering in the sintering layer in the pallet 8 in a moving direction is >=0 to <=10% and >=50 to <=100%. Air is sucked into the sintering layer in a range where the progression ratio of the sintering layer is over 10% and below 50%, by which the sintering is executed. A front part circulating gas hood 14a and a rear part circulating gas hood 14b are disposed respectively before and behind the sintering machine exclusive of the rage where the ratio of the machine length in the longitudinal direction of the machine is over 10% and bellow 50%, by which the waste gases from a window box 9 are introduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高炉等で溶銑を製造す
るに際して原料となる焼結鉱を製造する焼結方法および
設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sintering method and equipment for producing a sintered ore which is a raw material for producing hot metal in a blast furnace or the like.

【0002】[0002]

【従来の技術】従来の排ガス循環焼結法の概略工程を図
3に示す。焼結原料1をサージホッパー2に搬送し、シ
ュート3を介して焼結パレット8に装入して原料充填層
6を形成する。この原料充填層6の層厚は600mmで
ある。原料充填層6の表層部分のコークスに点火炉7で
点火する。
2. Description of the Related Art A schematic process of a conventional exhaust gas circulation sintering method is shown in FIG. The sintering raw material 1 is conveyed to the surge hopper 2 and charged into the sintering pallet 8 via the chute 3 to form the raw material filling layer 6. The layer thickness of the raw material filling layer 6 is 600 mm. The coke in the surface layer portion of the raw material packed bed 6 is ignited in the ignition furnace 7.

【0003】ウインドボックス9は供鉱側と排鉱側に分
割し、排鉱側の排ガスあるいは排ガスと空気などを混合
した循環排ガスを供鉱側の焼結層に循環ガスフード14
から吸引して原料充填層6のコークスを燃焼させ、この
燃焼熱で上層から下層にかけて順次原料を焼結する。排
鉱側は空気を吸引しながら原料充填層6のコークスを燃
焼させ、この燃焼熱で上層から下層にかけて順次原料を
焼結する。
The wind box 9 is divided into a mining side and a mine side, and a flue gas on the mine side or a circulating flue gas in which exhaust gas and air are mixed is circulated in a sintering layer on the mine side.
Is sucked in to burn the coke in the raw material-filled layer 6, and the combustion heat sequentially sinters the raw material from the upper layer to the lower layer. The mine ore side burns the coke in the raw material packed bed 6 while sucking air, and the combustion heat sequentially sinters the raw material from the upper layer to the lower layer.

【0004】また、特開昭50−19605号公報に
は、クーラー排出熱風、排鉱部の排出ガスを焼結層に吸
引する排ガス循環焼結法が記載されている。さらに、特
開昭53−58903号公報には、焼結前半部へ排鉱部
の排出ガスを循環する際、焼結後半部にも一部排出ガス
を循環する排ガス循環焼結法が記載されている。
Further, Japanese Patent Laid-Open No. 50-19605 discloses an exhaust gas circulation sintering method in which hot air discharged from a cooler and exhaust gas from an exhaust ore portion are sucked into a sintering layer. Further, JP-A-53-58903 describes an exhaust gas circulation sintering method in which, when the exhaust gas of the exhaust ore part is circulated to the first half of sintering, a part of the exhaust gas is also circulated to the latter half of the sintering. ing.

【0005】[0005]

【発明が解決しようとする課題】従来の焼結法では、図
4に示すように、焼結反応帯6bが下部に移動しながら
シンターケーキー6cが形成されるにしたがって原料層
6aが減少する。単位焼結層当たりの圧力損失は、嵩密
度によりシンターケーキー6c、原料層6a、焼結反応
帯6bの順で大きい値を示す。しかしシンターケーキー
6c、原料層6a、焼結反応帯6bの厚みは焼結の進行
割合によって異なる。したがって、シンターケーキー6
cの圧力損失P1 、焼結反応帯6bの圧力損失P2 、原
料層6aの圧力損失P3 を合計した全圧力損失HPは焼
結の進行の程度によって異なった値を示すことになる。
この全圧力損失HPの推移を図5に示したが、焼結進行
割合が10%から50%の範囲で高くなる傾向を示す。
In the conventional sintering method, as shown in FIG. 4, the raw material layer 6a decreases as the sintering cake 6c is formed while the sintering reaction zone 6b moves downward. The pressure loss per unit sintered layer shows a larger value in the order of the sinter cake 6c, the raw material layer 6a, and the sintering reaction zone 6b depending on the bulk density. However, the thicknesses of the sinter cake 6c, the raw material layer 6a, and the sintering reaction zone 6b differ depending on the progress rate of sintering. Therefore, Sinter Cake-6
pressure loss P 1 of c, the pressure loss P 2 of the sintering reaction zone 6b, the total pressure loss HP which is the sum of the pressure loss P 3 of the raw material layer 6a will show different values depending on the degree of progress of sintering.
The transition of this total pressure loss HP is shown in FIG. 5, but it shows a tendency that the sintering progress ratio increases in the range of 10% to 50%.

【0006】なお、ここで焼結進行割合は点火直後を0
%とし、排鉱部の焼結鉱が焼結パレットの火格子から落
下する地点を100%とする。また、焼結機の長手方向
における機長の割合は、点火直後の地点から排鉱部の焼
結鉱が焼結パレットの火格子より落下する地点までを1
00%とする。
Here, the rate of progress of sintering is 0 immediately after ignition.
%, And the point at which the sinter ore in the slag discharge section falls from the grate of the sinter pallet is 100%. The ratio of the machine length in the longitudinal direction of the sinter machine is 1 from the point immediately after ignition to the point where the sinter in the discharged slag falls from the grate of the sinter pallet.
00%.

【0007】焼結進行割合が10%から50%の範囲で
全圧力損失HPが高い値を示すことにより,当該範囲の
焼結層を通過する排ガス量は低下する。排ガス循環焼結
法においては焼結層に吸引するガスの酸度濃度が低く、
またガスが高温のため空気を吸引する場合よりは更に酸
素供給量が低下する。このため焼結が停滞し、焼結時間
が延長し、生産性が低下する。また、焼結の停滞部では
焼結反応帯6bの維持時間が長くなるため過溶融とな
り、形成されるシンターケーキー6cの嵩密度が高くな
り、シンターケーキー6cの通気性が悪化する。嵩密度
の高いシンターケーキ6cの下層の原料層6aには空気
が到達しにくくなり、コークスの燃焼が妨げられ、さら
なる焼結の停滞と共に、弱いシンターケーキー6cとな
り、歩留(5mm塊以上の製品の収率)が低下する問題
がある。
Since the total pressure loss HP has a high value in the range of 10% to 50% in the progress of sintering, the amount of exhaust gas passing through the sintered layer in the range is reduced. In the exhaust gas circulation sintering method, the acidity concentration of the gas sucked into the sintered layer is low,
Further, since the temperature of the gas is high, the oxygen supply amount is further reduced as compared with the case of sucking air. For this reason, the sintering is delayed, the sintering time is extended, and the productivity is reduced. Further, in the stagnation part of the sintering, the sintering reaction zone 6b is maintained for a long time, so that the sintering reaction zone 6b is excessively melted, the bulk density of the formed sinter cake 6c increases, and the air permeability of the sinter cake 6c deteriorates. Air becomes difficult to reach the lower raw material layer 6a of the sinter cake 6c having a high bulk density, the combustion of coke is hindered, the sintering becomes further stagnant, and the sinter cake 6c becomes weak, and the yield (product of 5 mm lumps or more) is obtained. The yield) is decreased.

【0008】特開昭50−19605号公報あるいは特
開昭53−58903号公報記載の排ガス循環焼結法に
よっても上記問題は解決できない。そこで本発明は、焼
結速度を速め、歩留を向上させ、生産性を向上する排ガ
ス循環焼結方法および排ガス循環設備を提供することを
目的とする。
The above problems cannot be solved even by the exhaust gas circulation sintering method described in JP-A-50-19605 or JP-A-53-58903. Therefore, it is an object of the present invention to provide an exhaust gas circulation sintering method and an exhaust gas circulation facility that accelerate the sintering rate, improve the yield, and improve the productivity.

【0009】[0009]

【課題を解決するための手段】本発明の排ガス循環焼結
方法は、下方吸引焼結機による排ガス循環焼結方法にお
いて、焼結パレット長手方向における焼結層の焼結進行
割合が0%以上10%以下と50%以上100%以下の
範囲内で焼結層へ排ガスを吸引し、焼結層の焼結進行割
合が10%超50%未満の範囲においては焼結層へ空気
を吸引して焼結することを特徴とする排ガス循環焼結方
法である。また、本発明の排ガス循環設備は、下方吸引
焼結機の排ガス循環設備において、焼結機の長手方向に
おける機長の割合が0%以上10%以下と50%以上1
00%以下の範囲内の焼結パレット上部に循環ガスフー
ドを設けたことを特徴とする排ガス循環設備である。
According to the exhaust gas circulation sintering method of the present invention, in the exhaust gas circulation sintering method using a lower suction sintering machine, the sintering progress ratio of the sintered layer in the longitudinal direction of the sintering pallet is 0% or more. Exhaust gas is sucked into the sintered layer within the range of 10% or less and 50% or more and 100% or less, and air is sucked into the sintered layer when the sintering progress ratio of the sintered layer is more than 10% and less than 50%. The exhaust gas circulation sintering method is characterized in that Further, the exhaust gas circulation equipment of the present invention is the exhaust gas circulation equipment of the lower suction sintering machine, wherein the proportion of the machine length in the longitudinal direction of the sintering machine is 0% or more and 10% or less and 50% or more 1.
The exhaust gas circulating equipment is characterized in that a circulating gas hood is provided on the upper portion of the sintering pallet within the range of 00% or less.

【0010】[0010]

【作用】全圧力損失が高くなる焼結進行割合が10%超
50%未満の範囲においては常温空気を吸引するため、
排ガスよりは酸度濃度が低くならず、また空気が常温で
熱風よりは温度が低いため、多くの酸素が焼結層に供給
できるので焼結速度が速くなる。このため焼結の停滞が
防止でき、焼結時間が延長することなく、焼結反応帯6
bの維持時間も長くならず、シンターケーキ6cの嵩密
度も低下せず、歩留の低下も解消される。全圧力損失が
高くなる焼結進行割合が10%超50%未満の範囲の前
後の焼結層には速度の高い排ガスを循環するため、焼結
層へ熱が付加されるため歩留が向上する。
[Function] In the case where the sintering progress ratio in which the total pressure loss is high is more than 10% and less than 50%, room temperature air is sucked,
Since the acidity concentration is not lower than that of the exhaust gas and the temperature of air is lower than that of hot air at room temperature, a large amount of oxygen can be supplied to the sintered layer, which increases the sintering rate. Therefore, the stagnation of the sintering can be prevented, the sintering time does not extend, and the sintering reaction zone 6
The maintenance time of b does not become long, the bulk density of the sinter cake 6c does not decrease, and the decrease in yield is eliminated. Yield is improved because heat is added to the sintered layer because high-speed exhaust gas is circulated in the sintered layer before and after the sintering progress ratio in which the total pressure loss becomes high exceeds 10% and less than 50%. To do.

【0011】なお、焼結機の長手方向における機長の割
合が10超%50%未満の範囲は、焼結進行割合が10
超%50%未満の範囲に相当し、焼結機の長手方向にお
ける機長の割合が10%超50%未満の範囲において全
圧力損失HPが高くなる。
When the ratio of the machine length in the longitudinal direction of the sintering machine is more than 10% and less than 50%, the sintering progress ratio is 10%.
The total pressure loss HP becomes high in the range of more than 10% and less than 50%, which corresponds to the range of more than 50% and less than 50%.

【0012】[0012]

【実施例1】図1に本発明の排ガス循環設備の実施例を
示す。
Embodiment 1 FIG. 1 shows an embodiment of the exhaust gas circulation equipment of the present invention.

【0013】焼結原料1をサージホッパー2に搬送し、
シュート3を介して焼結パレット8に装入して600m
mの原料充填層6を形成した。原料充填層6の表層部分
のコークスに点火炉7で点火した。ウインドボックス9
を、排鉱側の210℃、酸素濃度19.5%の排ガスを
前部循環ガスフード14aと後部循環ガスフード14b
の排ガス導入管13に接続した。
The sintering raw material 1 is conveyed to the surge hopper 2,
600 m after being charged into the sintering pallet 8 through the chute 3
The raw material filling layer 6 of m was formed. The coke in the surface layer portion of the raw material packed bed 6 was ignited in the ignition furnace 7. Wind box 9
The exhaust gas of 210 ° C. and oxygen concentration of 19.5% on the mine side is supplied to the front circulation gas hood 14a and the rear circulation gas hood 14b.
It was connected to the exhaust gas introduction pipe 13 of.

【0014】前部循環ガスフード14aは、点火炉7の
点火直後の地点から焼結機の長手方向における機長の割
合が10%以下の範囲、すなわち、600mmの原料充
填層6の上層60mmの焼結が進行した時点までとし、
後部循環ガスフード14bは、焼結機の長手方向におけ
る機長の割合が50%以上になる範囲、すなわち、60
0mmの原料充填層6の上層から300mm焼結が進行
した時点から、焼結機の長手方向における機長の割合が
85%以下の範囲、すなわち600mmの原料充填層6
の上層から510mm焼結が進行した時点までの範囲と
した。排ガス導入管13には流量調整バルブ21を設置
し、前部循環ガスフード14aと後部循環ガスフード1
4bへの排ガス量を調整した。
The front circulation gas hood 14a has a ratio of the machine length in the longitudinal direction of the sintering machine from the point immediately after ignition of the ignition furnace 7 to 10% or less, that is, the upper layer 60 mm of the raw material filling layer 6 of 600 mm is fired. By the time the knotting progresses,
The rear circulation gas hood 14b has a ratio of the machine length in the longitudinal direction of the sintering machine of 50% or more, that is, 60%.
From the time when 300 mm sintering proceeds from the upper layer of the 0 mm raw material filling layer 6, the ratio of the machine length in the longitudinal direction of the sintering machine is 85% or less, that is, 600 mm of the raw material filling layer 6
The range was from the upper layer to the time when 510 mm of sintering proceeded. A flow rate adjusting valve 21 is installed in the exhaust gas introduction pipe 13, and a front circulation gas hood 14a and a rear circulation gas hood 1 are installed.
The amount of exhaust gas to 4b was adjusted.

【0015】前部循環ガスフード14aと後部循環ガス
フード14bを設置しない全圧力損失が高くなる焼結進
行割合が10%超50%未満の範囲においては空気を吸
引し焼結した。このため焼結の停滞が防止でき、焼結速
度が速くなり、従来の焼結時間35.1分から33.5
分に短縮し、歩留も従来の歩留75.3%から80.7
%に向上した。このため生産性は従来の生産性29.4
T/D/m2 から35.1T/D/m2 に向上した。
When the front circulation gas hood 14a and the rear circulation gas hood 14b were not installed, air was sucked and sintered in a range where the total progress of pressure was high and the sintering progress ratio was more than 10% and less than 50%. Therefore, the stagnation of the sintering can be prevented, the sintering speed can be increased, and the conventional sintering time of 35.1 minutes to 33.5
And the yield is 80.7 from the conventional yield of 75.3%.
Improved to%. Therefore, the productivity is 29.4 of the conventional one.
It was increased from T / D / m 2 to 35.1T / D / m 2.

【0016】[0016]

【実施例2】図2に本発明の排ガス循環設備の他の実施
例を示す。
[Embodiment 2] FIG. 2 shows another embodiment of the exhaust gas circulation equipment of the present invention.

【0017】焼結原料1をサージホッパー2に搬送し、
シュート3を介して焼結パレット8に装入して600m
mの原料充填層6を形成した。原料充填層6の表層部分
のコークスに点火炉7で点火した。排鉱された高温の焼
結鉱を冷却するクーラー22から250℃の熱風を熱風
ブロアー23、熱風管24により前部循環ガスフード1
4aと後部循環ガスフード14bに排ガス導入管13か
ら供給した。
The sintering raw material 1 is conveyed to the surge hopper 2,
600 m after being charged into the sintering pallet 8 through the chute 3
The raw material filling layer 6 of m was formed. The coke in the surface layer portion of the raw material packed bed 6 was ignited in the ignition furnace 7. A hot air blower 23 and a hot air tube 24 are used to supply hot air of 250 ° C. from a cooler 22 for cooling the discharged high temperature sintered ore to the front circulation gas hood 1.
4a and the rear circulation gas hood 14b were supplied from the exhaust gas introducing pipe 13.

【0018】前部循環ガスフード14aは、点火炉7の
点火直後の地点から焼結機の長手方向における機長の割
合が10%以下の範囲、すなわち、600mmの原料充
填層6の上層60mmの焼結が進行した時点までとし、
後部循環ガスフード14bは、焼結機の長手方向におけ
る機長の割合が50%以上になる範囲、すなわち、60
0mmの原料充填層6の上層から300mm焼結が進行
した時点から、焼結機の長手方向における機長の割合が
100%の範囲、すなわち、600mmの原料充填層6
の上層から600mm焼結が進行した時点までの範囲と
した。排ガス導入管13には流量調整バルブ21を設置
し、前部循環ガスフード14aと後部循環ガスフード1
4bへの排ガス量を調整した。
The front circulation gas hood 14a has a ratio of the machine length in the longitudinal direction of the sinter machine of 10% or less from the point immediately after ignition of the ignition furnace 7, that is, the upper layer 60 mm of the raw material filling layer 6 of 600 mm is baked. By the time the knotting progresses,
The rear circulation gas hood 14b has a ratio of the machine length in the longitudinal direction of the sintering machine of 50% or more, that is, 60%.
From the time when 300 mm sintering proceeds from the upper layer of the 0 mm raw material filling layer 6, the ratio of the machine length in the longitudinal direction of the sintering machine is in the range of 100%, that is, 600 mm of the raw material filling layer 6
The range was from the upper layer to the time when 600 mm of sintering proceeded. A flow rate adjusting valve 21 is installed in the exhaust gas introduction pipe 13, and a front circulation gas hood 14a and a rear circulation gas hood 1 are installed.
The amount of exhaust gas to 4b was adjusted.

【0019】前部循環ガスフード14aと後部循環ガス
フード14bを設置しない全圧力損失が高くなる焼結進
行割合が10%超50%未満の範囲においては空気を吸
引し焼結した。このため焼結の停滞が防止でき、焼結速
度が速くなり、従来の焼結時間35.1分から32.7
分に短縮し、歩留も従来の歩留75.3%から81.0
%に向上した。このため生産性は従来の生産性29.4
T/D/m2 から36.8T/D/m2 に向上した。
When the front circulation gas hood 14a and the rear circulation gas hood 14b were not installed, air was sucked and sintered in the range where the progress rate of sintering where the total pressure loss was high was more than 10% and less than 50%. Therefore, the stagnation of sintering can be prevented, the sintering speed can be increased, and the conventional sintering time is 35.1 minutes to 32.7.
The yield is reduced to 81.0 from the conventional yield of 75.3%.
Improved to%. Therefore, the productivity is 29.4 of the conventional one.
It was increased from T / D / m 2 to 36.8T / D / m 2.

【0020】[0020]

【発明の効果】本発明によれば焼結速度が速くなり、ま
た歩留も向上するため、生産性は従来の排ガス循環焼結
法に比較して向上する。
According to the present invention, since the sintering rate is increased and the yield is also improved, the productivity is improved as compared with the conventional exhaust gas circulation sintering method.

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

【図1】本発明の排ガス循環設備の実施例を示す図であ
る。
FIG. 1 is a diagram showing an embodiment of an exhaust gas circulation facility of the present invention.

【図2】本発明の排ガス循環設備の他の実施例を示す図
である。
FIG. 2 is a diagram showing another embodiment of the exhaust gas circulation equipment of the present invention.

【図3】従来の排ガス循環焼結法の工程を示す図であ
る。
FIG. 3 is a diagram showing a process of a conventional exhaust gas circulation sintering method.

【図4】従来の焼結法における焼結進行状況を示す図で
ある。
FIG. 4 is a diagram showing the progress of sintering in a conventional sintering method.

【図5】焼結層の全圧力損失の推移を示す図である。FIG. 5 is a diagram showing changes in total pressure loss of a sintered layer.

【符号の説明】[Explanation of symbols]

1 焼結原料 2 サージホッパー 3 シュート 4 床敷ホッパー 5 床敷 6 原料充填層 6a 原料層 6b 焼結反応帯 6c シンターケーキ 7 点火炉 8 焼結パレット 9 ウインドボックス 10 循環ガス集塵機 11 循環ガスブロアー 12 循環ガス煙道 13 排ガス導入管 14 循環ガスフード 14a 前部循環ガスフード 14b 後部循環ガスフード 15 集塵機 16 脱硫装置 17 ブロアー 18 煙突 21 流量調整バルブ 22 クーラー 23 熱風ブロアー 24 熱風管 1 Sintering Raw Material 2 Surge Hopper 3 Chute 4 Flooring Hopper 5 Flooring 6 Raw Material Packing Layer 6a Raw Material Layer 6b Sintering Reaction Zone 6c Sinter Cake 7 Ignition Furnace 8 Sintering Pallet 9 Windbox 10 Circulating Gas Dust Collector 11 Circulating Gas Blower 12 Circulating gas flue 13 Exhaust gas introducing pipe 14 Circulating gas hood 14a Front circulating gas hood 14b Rear circulating gas hood 15 Dust collector 16 Desulfurization device 17 Blower 18 Chimney 21 Flow rate control valve 22 Cooler 23 Hot air blower 24 Hot air tube

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 下方吸引焼結機による排ガス循環焼結方
法において、焼結パレット長手方向における焼結層の焼
結進行割合が0%以上10%以下と50%以上100%
以下の範囲内で焼結層へ排ガスを吸引し、焼結層の焼結
進行割合が10%超50%未満の範囲においては焼結層
へ空気を吸引して焼結することを特徴とする排ガス循環
焼結方法。
1. In an exhaust gas circulation sintering method using a downward suction sintering machine, a sintering progress rate of a sintered layer in a longitudinal direction of a sintering pallet is 0% to 10% and 50% to 100%.
Exhaust gas is sucked into the sintered layer within the following range, and air is sucked into the sintered layer for sintering in the range where the sintering progress ratio of the sintered layer is more than 10% and less than 50%. Exhaust gas circulation sintering method.
【請求項2】 下方吸引焼結機の排ガス循環設備におい
て、焼結機の長手方向における機長の割合が0%以上1
0%以下と50%以上100%以下の範囲内の焼結パレ
ット上部に循環ガスフードを設けたことを特徴とする排
ガス循環設備。
2. In the exhaust gas circulation equipment of a lower suction sintering machine, the ratio of the machine length in the longitudinal direction of the sintering machine is 0% or more and 1 or more.
An exhaust gas circulation facility, characterized in that a circulating gas hood is provided above the sintering pallet within the range of 0% or less and 50% or more and 100% or less.
JP10327994A 1994-04-19 1994-04-19 Sintering method by waste gas circulation and waste gas circulation equipment Withdrawn JPH07286216A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10327994A JPH07286216A (en) 1994-04-19 1994-04-19 Sintering method by waste gas circulation and waste gas circulation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10327994A JPH07286216A (en) 1994-04-19 1994-04-19 Sintering method by waste gas circulation and waste gas circulation equipment

Publications (1)

Publication Number Publication Date
JPH07286216A true JPH07286216A (en) 1995-10-31

Family

ID=14349915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10327994A Withdrawn JPH07286216A (en) 1994-04-19 1994-04-19 Sintering method by waste gas circulation and waste gas circulation equipment

Country Status (1)

Country Link
JP (1) JPH07286216A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103484661A (en) * 2013-09-13 2014-01-01 中南大学 Method for enhancing sintering of high-proportion limonite by utilization of waste heat of exhaust gas
CN104180658A (en) * 2014-08-08 2014-12-03 天津二十冶建设有限公司 Mounting method for dedusting system of sintering machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103484661A (en) * 2013-09-13 2014-01-01 中南大学 Method for enhancing sintering of high-proportion limonite by utilization of waste heat of exhaust gas
CN104180658A (en) * 2014-08-08 2014-12-03 天津二十冶建设有限公司 Mounting method for dedusting system of sintering machine
CN104180658B (en) * 2014-08-08 2015-12-30 天津二十冶建设有限公司 A kind of installation method of sintering machine dust pelletizing system

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