JPH10330851A - Formation of zinc-removed agglomerate from zinc-containing iron-making dust - Google Patents

Formation of zinc-removed agglomerate from zinc-containing iron-making dust

Info

Publication number
JPH10330851A
JPH10330851A JP16210597A JP16210597A JPH10330851A JP H10330851 A JPH10330851 A JP H10330851A JP 16210597 A JP16210597 A JP 16210597A JP 16210597 A JP16210597 A JP 16210597A JP H10330851 A JPH10330851 A JP H10330851A
Authority
JP
Japan
Prior art keywords
zinc
dust
blast furnace
sintering
containing iron
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP16210597A
Other languages
Japanese (ja)
Other versions
JP3709052B2 (en
Inventor
Masanori Nakano
正則 中野
Michiaki Sakakibara
路晤 榊原
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.)
KIYOUZAI KOGYO KK
Nippon Steel Corp
Original Assignee
KIYOUZAI KOGYO KK
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 KIYOUZAI KOGYO KK, Nippon Steel Corp filed Critical KIYOUZAI KOGYO KK
Priority to JP16210597A priority Critical patent/JP3709052B2/en
Publication of JPH10330851A publication Critical patent/JPH10330851A/en
Application granted granted Critical
Publication of JP3709052B2 publication Critical patent/JP3709052B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain sintered ore having low zinc content at high yield by specifying a packing height of dust and superficial gas flowing speed passed through a packing layer in a sintering machine and sintering zinc-containing iron-making dust. SOLUTION: At the time of producing the sintered ore for blast furnace by executing zinc-removal sintering to the zinc-containing dust produced in iron-making process of secondary ash in the blast furnace, fine granular dust in a converter, dust in an electric furnace, an upward suction type sintering machine is used to sinter these dusts into bulky state. In such a case, the raw material obtd. by mixing the fine grain dust in the converter and the secondary ash in the blast furnace to 1; 1 ratio, is packed to the height of 200-400 mm in the upward suction type sintering machine and the flowing speed of the air passed through the packing layer is regulated to <=0.4 Nm/sec to suck the air upward, and the zinc-removal sintering is executed. The zinc removing ratio of the zinc-containing dust in the raw material is drastically improved and the consumption of the sintered ore as the product in the blast furnace is drastically increased and recycled using ratio of the zinc-containing iron-making dust is improved.

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、高炉2次灰、転炉
微粒ダスト、電気炉ダスト等の製鉄工程で発生する含亜
鉛ダストを焼結機で脱亜鉛塊成化する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dezincifying and agglomerating zinc-containing dust generated in an iron-making process such as secondary ash of a blast furnace, converter dust, and electric furnace dust by a sintering machine.

【0002】[0002]

【従来の技術】従来、含亜鉛製鉄ダストの脱亜鉛処理方
法としては、キルンによる還元揮発法(ウルツ法)が広
く行われている。これに対し、原料ダストの配合方法に
関する特開平7−157829号公報、原料粒度に関す
る特開平7−90395号公報、通風ガス組成および焼
成温度に関する特開平7−188786号公報、粗酸化
亜鉛ダストの捕集方法に関する特開平9−41048号
公報、ならびに焼成の安定化方法に関する特開平7−1
38661号公報、特開平8−127821号公報およ
び特願平7−344379号明細書などに、より簡便か
つ安価で製鉄所構内での立地に適する焼結機による脱亜
鉛塊成化方法が開示されている。
2. Description of the Related Art Hitherto, as a method for dezincing zinc-containing iron dust, a reduction volatilization method using a kiln (Wurtz method) has been widely used. On the other hand, Japanese Patent Application Laid-Open No. 7-157829 concerning the method of blending the raw material dust, Japanese Patent Application Laid-Open No. 7-90395 regarding the particle size of the raw material, Japanese Patent Application Laid-Open No. 7-188786 regarding the ventilation gas composition and the calcination temperature, and the capture of coarse zinc oxide dust JP-A-9-41048 concerning a collecting method and JP-A-7-17-1 concerning a method for stabilizing firing.
No. 38661, JP-A-8-127821 and Japanese Patent Application No. 7-344379 disclose a dezincification agglomeration method using a sintering machine which is simpler, cheaper and more suitable for a location in a steelworks. ing.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記方法にお
いても、脱亜鉛率(原料中亜鉛濃度に対する、原料中亜
鉛と処理後成品塊成鉱中に残留する亜鉛の濃度差の比
率)は5〜7割であり、亜鉛入量制限の厳しい高炉に対
しては、処理後の塊成鉱の完全なリサイクル使用になお
制限が生じる場合があった。
However, even in the above method, the dezincing rate (the ratio of the concentration of zinc in the raw material and the concentration of zinc remaining in the agglomerate after treatment to the zinc concentration in the raw material) is 5 to 5. In the case of a blast furnace with a strict zinc input limit of 70%, there was a case where there was still a restriction on the complete recycling of the agglomerate after treatment.

【0004】そこで本発明は、成品塊成鉱中の亜鉛残留
量をさらに低めて、高炉への使用量を増やし、含亜鉛ダ
ストの製鉄所内リサイクルをさらに推進することを目的
とする。
Therefore, an object of the present invention is to further reduce the residual amount of zinc in the agglomerated ore, increase the amount used in a blast furnace, and further promote the recycling of zinc-containing dust in steelworks.

【0005】[0005]

【課題を解決するための手段】本発明は、上方吸引式焼
結機で含亜鉛製鉄ダストを塊成化する方法において、該
ダストの充填層高さを200〜400mmとし、該充填
層の通過空筒ガス流速を0.4Nm/sec以下として
上方に吸引して焼成することを特徴とする含亜鉛製鉄ダ
ストの脱亜鉛塊成化方法である。
According to the present invention, there is provided a method for agglomerating zinc-containing iron dust using an upward suction type sintering machine, wherein the height of the packed bed of the dust is set to 200 to 400 mm, and the passing of the packed bed is performed. This is a method for dezincification of zinc-containing iron dust, characterized in that the hollow cylinder gas flow rate is 0.4 Nm / sec or less and suction is performed upward for firing.

【0006】本発明は、ダスト中の金属鉄による酸化亜
鉛の還元が進行する1200℃以上の高温保持時間を十
分確保して脱亜鉛反応を促進させるために、最良の焼結
条件、すなわち焼結の通風方法、風速および充填層厚条
件を採用したものである。
According to the present invention, the best sintering conditions, that is, the best sintering conditions, ie, sintering, are used to ensure a sufficient high-temperature holding time of 1200 ° C. or more at which the reduction of zinc oxide by metallic iron in dust proceeds to promote the dezincification reaction. , The wind speed and the packed layer thickness conditions.

【0007】なお、含亜鉛製鉄ダストとは、転炉微粒ダ
スト、高炉2次灰および電気炉ダストならびにそれらの
混合物をいう。そのうち転炉微粒ダストにおいては、脱
亜鉛を促進する観点から、金属鉄分を10%以上含有す
るものとする。また、電気炉ダストを混合する場合の配
合率は、混合物中の還元剤(金属鉄分およびカーボン
分)の量の低下を防ぐ観点から、20%を限度とするの
がよい。
[0007] Zinc-containing iron dust refers to converter dust, blast furnace secondary ash, electric furnace dust, and mixtures thereof. Among them, the converter dust contains 10% or more of metallic iron from the viewpoint of promoting dezincification. In addition, the mixing ratio when mixing the electric furnace dust is preferably limited to 20% from the viewpoint of preventing a reduction in the amount of the reducing agent (metallic iron and carbon) in the mixture.

【0008】[0008]

【発明の実施の形態】まず、上方吸引式送風について説
明する。転炉微粒ダストと高炉2次灰を1:1で配合し
た原料において、鉄鉱石焼結法に一般的に採用される下
方吸引式送風と上方吸引式送風の場合との、塊成化率、
生産速度および脱亜鉛率を比較した結果を表1に示し
た。上方吸引式送風は歩留、生産速度を変えることな
く、脱亜鉛率を20%程度高め得ることが判る。これ
は、図1に両者の焼結進行状況を模式的に比較して示す
ように、溶融ゾーンで生成した融液が、下方吸引式の場
合は下層の冷たい原料層に滴下しつつ急冷されるのに比
較し、上方吸引式の場合は先に生成した下部塊状部上に
滴下して下部からの通風から隔離される形となることで
徐冷されるため、ダスト中の金属鉄による酸化亜鉛の還
元が進行する1200℃以上の高温保持時間が十分確保
されて脱亜鉛反応を促進するためである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, an upward suction type blower will be described. The agglomeration rate of the lower suction type blower and the upper suction type blower generally used in the iron ore sintering method in the raw material in which the converter fine dust and the blast furnace secondary ash are mixed at a ratio of 1: 1,
Table 1 shows the results of comparing the production rate and the dezincification rate. It can be seen that the upward suction type blowing can increase the dezincing rate by about 20% without changing the yield and the production speed. This is because, as shown schematically in FIG. 1, the sintering progress of the two is quenched while the melt generated in the melting zone is dropped onto the lower cold raw material layer in the case of the downward suction type. In contrast, in the case of the upper suction type, zinc oxide is formed by dropping on the previously formed lower lump and isolated from ventilation from the lower part, so that it is gradually cooled. This is because a high-temperature holding time of 1200 ° C. or more in which the reduction proceeds is sufficiently secured to promote the dezincification reaction.

【0009】[0009]

【表1】 〔注〕*1)点火開始時刻から排ガス温度が最高温度を示す時刻までの時間 *2)10cm間隔で焼結充填層内に装入した熱電対がピーク温度を 示す時刻から求めた燃焼進行速度[Table 1] [Note] * 1) The time from the ignition start time to the time when the exhaust gas temperature reaches the maximum temperature. * 2) The burning progress rate calculated from the time when the thermocouple inserted into the sintered packed bed at 10 cm intervals shows the peak temperature.

【0010】なお、上方吸引式送風は下層に大きなシン
ターケーキ塊が形成されるため、その後焼成される上部
の焼結が不安定になりやすく、過大な層厚は上部での未
焼結部の増大を招き、その結果全体としての脱亜鉛率が
低下して行く。従って、良好な脱亜鉛率を維持するに
は、層厚を適正に管理する必要がある。図2は、層厚の
脱亜鉛率に与える影響を示したもので、200〜400
mmが最良であることがわかる。
[0010] In the upper suction type air blowing, since a large sinter cake mass is formed in the lower layer, the sintering of the upper portion to be subsequently fired is likely to be unstable, and the excessive layer thickness is caused by the unsintered portion in the upper portion. The dezincing rate as a whole decreases as a result. Therefore, in order to maintain a good zinc removal rate, it is necessary to properly control the layer thickness. FIG. 2 shows the effect of the layer thickness on the dezincing rate.
It can be seen that mm is the best.

【0011】最後に、通過空筒ガス流速については、通
過空筒ガス流速を低下すると、図3に示すように、FF
S(Flame Front Speed)の低下に比
例する高温保持時間の増加と最高温度上昇により脱亜鉛
率が向上し、0.4Nm/sec以下の流速において高
い脱亜鉛率が達成できる。
Finally, regarding the passing cylinder gas flow velocity, when the passing cylinder gas flow velocity is reduced, as shown in FIG.
The dezincing rate is improved by increasing the high-temperature holding time and increasing the maximum temperature in proportion to the decrease of S (Frame Front Speed), and a high dezincing rate can be achieved at a flow rate of 0.4 Nm / sec or less.

【0012】[0012]

【実施例】転炉ダスト50%、高炉2次灰50%からな
る原料と、円形テーブル式焼結機(有効焼結面積1
2 )を使って、従来法と本発明法を比較した結果を示
す。従来法および本発明法で採用した操業条件と主要な
操業結果を表2に示す。従来法の操業条件としては、鉄
鉱石焼結で通常行われている一般的な条件を採用した。
EXAMPLE A raw material consisting of 50% converter dust and 50% blast furnace secondary ash, and a circular table type sintering machine (effective sintering area 1)
The results of comparing the conventional method and the method of the present invention using m 2 ) are shown. Table 2 shows the operating conditions and main operating results adopted in the conventional method and the method of the present invention. As the operating conditions of the conventional method, general conditions usually performed in iron ore sintering were adopted.

【0013】焼成途中の焼結層内の温度測定の結果、1
200℃以上の高温保持時間が2分以上確保されている
部分は、従来法では全層のうち1/2程度であったが、
本発明法ではほぼ全層にわたることが確認できた。その
結果、従来50〜60%であった塊成鉱の脱亜鉛率が8
0%以上に改善された。なお、風速低下にともない若干
生産性は低下したが、操業上許容できる範囲であった。
As a result of measuring the temperature in the sintered layer during firing, 1
The portion where the high-temperature holding time of 200 ° C. or more is secured for 2 minutes or more is about 1 / of all layers in the conventional method,
It was confirmed that the method of the present invention covers almost all layers. As a result, the dezincing rate of the agglomerate ore, which was conventionally 50 to 60%, is 8
It was improved to 0% or more. Although the productivity slightly decreased with the decrease in the wind speed, the productivity was within an acceptable range.

【0014】[0014]

【表2】 [Table 2]

【0015】[0015]

【発明の効果】本発明により、脱亜鉛率を飛躍的に向上
させることができる。その結果、成品塊成鉱の高炉への
使用量を増加させることができ、含亜鉛ダストの製鉄所
内リサイクルをさらに推進できる。
According to the present invention, the dezincing rate can be drastically improved. As a result, the amount of product agglomerate ore used in the blast furnace can be increased, and the recycling of zinc-containing dust in steel works can be further promoted.

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

【図1】下方吸引式送風と上方吸引式送風の焼結進行状
況を模式的に示す図である。
FIG. 1 is a diagram schematically showing the progress of sintering of a downward suction type blow and an upward suction type blow.

【図2】充填層の層厚による脱亜鉛率の変化を示す図で
ある。
FIG. 2 is a graph showing a change in a dezincing rate depending on the thickness of a filling layer.

【図3】通過空筒ガス流速による脱亜鉛率等の変化を示
す図である。
FIG. 3 is a diagram showing a change in a dezincing ratio and the like depending on a flow velocity of a passing cylinder gas.

【符号の説明】[Explanation of symbols]

1 充填層 1 packed bed

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 上方吸引式焼結機で含亜鉛製鉄ダストを
塊成化する方法において、該ダストの充填層高さを20
0〜400mmとし、該充填層の通過空筒ガス流速を
0.4Nm/sec以下として上方に吸引して焼成する
ことを特徴とする含亜鉛製鉄ダストの脱亜鉛塊成化方
法。
1. A method for agglomerating zinc-containing iron dust with an upward suction type sintering machine, wherein the height of the packed bed of the dust is 20 or less.
A method for dezincification of zinc-containing iron dust, wherein the pressure is 0 to 400 mm, and the gas flow rate of the hollow cylinder passing through the packed bed is 0.4 Nm / sec or less, and the powder is sucked upward and fired.
JP16210597A 1997-06-05 1997-06-05 Dezincification agglomeration method of zinc-containing iron dust Expired - Fee Related JP3709052B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16210597A JP3709052B2 (en) 1997-06-05 1997-06-05 Dezincification agglomeration method of zinc-containing iron dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16210597A JP3709052B2 (en) 1997-06-05 1997-06-05 Dezincification agglomeration method of zinc-containing iron dust

Publications (2)

Publication Number Publication Date
JPH10330851A true JPH10330851A (en) 1998-12-15
JP3709052B2 JP3709052B2 (en) 2005-10-19

Family

ID=15748152

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16210597A Expired - Fee Related JP3709052B2 (en) 1997-06-05 1997-06-05 Dezincification agglomeration method of zinc-containing iron dust

Country Status (1)

Country Link
JP (1) JP3709052B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7875097B2 (en) 2005-12-02 2011-01-25 Kyouzai Kogyo Co., Ltd. Method of granulating raw material for sintering, and method of manufacturing sintered iron ore
US8067188B2 (en) 1999-09-17 2011-11-29 N2Itive1 Innovations Analyte detection

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8067188B2 (en) 1999-09-17 2011-11-29 N2Itive1 Innovations Analyte detection
US7875097B2 (en) 2005-12-02 2011-01-25 Kyouzai Kogyo Co., Ltd. Method of granulating raw material for sintering, and method of manufacturing sintered iron ore

Also Published As

Publication number Publication date
JP3709052B2 (en) 2005-10-19

Similar Documents

Publication Publication Date Title
JPH11310832A (en) Treatement of metal oxide of steel making waste
US20110024681A1 (en) Titanium oxide-containing agglomerate for producing granular metallic iron
JPH11172312A (en) Operation of movable hearth type furnace and movable hearth type furnace
JPH11504985A (en) Method for recovering metals from iron oxide containing materials
JP4470490B2 (en) Method for producing semi-reduced agglomerate
JP4984488B2 (en) Method for producing semi-reduced sintered ore
JPH10330851A (en) Formation of zinc-removed agglomerate from zinc-containing iron-making dust
JPH10147806A (en) Production of high quality reduced iron from ironmaking dust
JP2018178219A (en) Method for smelting oxide ore
JPH0747784B2 (en) Method for recovering zinc and lead from steelmaking dust
JP5892317B2 (en) Production method of raw materials for blast furnace
Nakano et al. Coke breeze-less sintering of BOF dust and its capability of dezincing
US2684296A (en) Reduction of iron ores
JP3797184B2 (en) Method for producing sintered ore
JP3050493B2 (en) Method for producing sintered ore using limonite ore as raw material
JP3020494B2 (en) Method for producing reduced iron agglomerates
US3353953A (en) Process of purifying an anseniccontaining iron ore
JPH10219361A (en) Treatment of sintering raw material
JP2013147718A (en) Method for producing sintered ore
US6863710B1 (en) Sinter mix enhancer
JPH11279668A (en) Production of sintered ore and sintering machine
JPS5920734B2 (en) Treatment method for steelmaking electric furnace dust and mill scale
JP3549918B2 (en) Exhaust gas circulation sintering method
JP2014031528A (en) Method for producing raw material for blast furnace
JP5971482B2 (en) Agglomerate production method

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20040525

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040603

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20040603

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20040525

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20040603

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20040726

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20041027

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050422

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050426

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050712

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050805

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees