JPS60248830A - Production of quicklime for binder by sintering machine - Google Patents
Production of quicklime for binder by sintering machineInfo
- Publication number
- JPS60248830A JPS60248830A JP10442284A JP10442284A JPS60248830A JP S60248830 A JPS60248830 A JP S60248830A JP 10442284 A JP10442284 A JP 10442284A JP 10442284 A JP10442284 A JP 10442284A JP S60248830 A JPS60248830 A JP S60248830A
- Authority
- JP
- Japan
- Prior art keywords
- ore
- sintered
- quicklime
- sintering
- limestone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、焼結鉱製造プラントにおいて焼結鉱製造時に
、同時に焼結機によって、焼結原料のバインダである生
石灰を製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing quicklime, which is a binder for sintering raw materials, using a sintering machine at the same time as producing sintered ore in a sintered ore production plant.
焼結操業において、焼結原料中にバインダ(生石灰もし
くは消石灰)を添加すると、焼結の生産率が増し、強度
が増えるので、その分だけ焼結時の所要熱量を減するこ
とができる。特に生石灰は第3図、第4図に例を示すよ
うに、添加による効果が大きい(r鉄と鋼jVo1.6
8゜Mar、、1982) 。In a sintering operation, adding a binder (quicklime or slaked lime) to the sintering raw material increases the sintering production rate and increases the strength, so the amount of heat required during sintering can be reduced accordingly. In particular, quicklime has a large effect when added, as shown in Figures 3 and 4.
8°Mar, 1982).
然るに、生石灰は焼結鉱石灰分の添加物としては非常に
高価で(石灰石の値段の約3〜4倍)、そのために総合
的なコストとして、メリットか減じている。However, quicklime is very expensive as an additive for sintered ore lime (approximately 3 to 4 times the price of limestone), which reduces the overall cost benefit.
生石灰は、従来石灰石をシャフト炉に入れて焼成し、分
解反応を起こさせて製造されていた。しかし、これでは
高価になるため、特開昭52−71306や特開昭58
−31041の如く、焼結の焼成熱を利用して焼結操業
の過程において安価な石灰石から生石灰を製造し、これ
を焼結原料に戻し、石灰石に代えて焼結鉱の製造に供す
ることが提案されている。Quicklime has traditionally been produced by placing limestone in a shaft furnace and firing it to cause a decomposition reaction. However, this would be expensive, so JP-A-52-71306 and JP-A-58
-31041, it is possible to use the firing heat of sintering to produce quicklime from inexpensive limestone in the process of sintering operation, return it to the sintering raw material, and use it to produce sintered ore in place of limestone. Proposed.
特開昭52−71306では、石灰石をパレットに装入
するに際し、床敷鉱の上に層状に装入するので、石灰石
装入用の設備を新たに別に設ける必要があり、特開5B
−31041のように、予め燃料と混合して装入する場
合は、そのための燃料を余分に必要とするという問題が
ある。また、床敷鉱と混合して供給することも提示され
ているが、その場合は粉状のためにパレットのグレート
パーの隙間から風箱側へ吸引されてしまい、その目的を
達成することができない。In JP-A-52-71306, when charging limestone into pallets, it is charged in layers on top of bedding ore, so it is necessary to separately install limestone charging equipment.
-31041, when charging by mixing with fuel in advance, there is a problem in that extra fuel is required. It has also been suggested that the supply be mixed with bedding ore, but in that case, the powder would be sucked into the wind box through the gaps between the pallet grate, making it impossible to achieve the purpose. Can not.
本発明は、上記従来方法の欠点を改善した方法を提供す
ることを目的とし、焼結機で焼結鉱を生産する際、その
廃熱を利用して安価な石灰石から直接生石灰を得てこれ
を返鉱と共に焼結原料にリサイクルするものであるが、
この場合に、焼結機へ石灰石を供給する別途の設備を設
けることなく、既設の設備を利用し、また余分の燃料を
用いることなく効率よ〈実施することのできる方法を提
供するものである。The purpose of the present invention is to provide a method that improves the drawbacks of the above-mentioned conventional methods. When producing sintered ore using a sintering machine, the waste heat is used to directly obtain quicklime from inexpensive limestone. is recycled into raw materials for sintering along with return ore.
In this case, the present invention provides a method that can be carried out efficiently without requiring separate equipment for supplying limestone to the sintering machine, using existing equipment, and without using extra fuel. .
本発明は上記問題点を解決するため、焼結配合原料をバ
レントへ装入するに際し、石灰石を床敷鉱として供給し
、その上に焼結原料を供給して焼結することを特徴とす
る焼結機によるバインダ用生石灰の製造方法を要旨とす
る。In order to solve the above-mentioned problems, the present invention is characterized in that when charging the sintering compound raw material into the balent, limestone is supplied as a bedding ore, and the sintering raw material is supplied on top of it for sintering. The gist of this article is a method for producing quicklime for binder using a sintering machine.
以下図面を参照して本発明を説明する。The present invention will be explained below with reference to the drawings.
本発明における焼結バインダ用生石灰の製造工程を模式
的に第1図、第2図に示す。The manufacturing process of quicklime for sintered binder in the present invention is schematically shown in FIGS. 1 and 2.
5〜10mmに整粒された石灰石りが床敷鉱ホンパ6に
供給される。本発明に用いる石灰石としては、分解反応
後、破砕により粉化しゃすい特性をもつものを用いる。Limestone sized to a size of 5 to 10 mm is supplied to the bedding ore dumper 6. The limestone used in the present invention is one that has the property of being easily pulverized by crushing after a decomposition reaction.
一方、焼結原料槽1a、コークス槽1b、粉石灰石槽1
c、・・・がらそれぞれの原料が供給され、コンベヤ2
を経てドラムミキサ3に投入され、ここで水分添加調整
後、擬似粒子化した焼結原料Rとして給鉱ホッパ4に供
給される。On the other hand, a sintering raw material tank 1a, a coke tank 1b, a powdered limestone tank 1
Each raw material is supplied to conveyor 2.
The sintered raw material R is fed into a drum mixer 3, where water is added and adjusted, and then fed to the feed hopper 4 as a pseudo-particle sintered raw material R.
第2図に示すように、パレット7aを矢印方向に移動さ
せながら、先ず、石灰石りか床敷ホッパ6から供給され
、その上に焼結原料Rが供給される。パレット7a上に
装入された焼結原料は、点火装置5で着火された後、下
向吸引通風により上層部より順次焼結反応を生じっ−っ
移動して焼結機の排鉱部に至る。このようにして全量の
焼結反応か完了し、パレット上の焼結原料は焼結鉱とな
る。風箱で吸引される排風ガス温度は、給鉱側風箱では
常温であるが、焼結原料が順次排鉱側へ移行するに従っ
て上昇し、350°C〜450℃の高温となる。As shown in FIG. 2, while the pallet 7a is being moved in the direction of the arrow, limestone is first supplied from the bedding hopper 6, and the sintering raw material R is supplied thereon. The sintering raw material charged onto the pallet 7a is ignited by the igniter 5, and then moves from the upper layer by downward suction ventilation to cause a sintering reaction and is transferred to the ore discharge section of the sintering machine. reach. In this way, the entire sintering reaction is completed, and the sintered raw material on the pallet becomes sintered ore. The temperature of the exhaust gas sucked in the windbox is at room temperature in the ore supply side windbox, but increases as the sintering raw material sequentially moves to the ore discharge side, reaching a high temperature of 350°C to 450°C.
焼結中の焼結ケーキ内の焼結層断面での温度分布は第5
図に例示するように、最も温度の高い焼結帯で約125
0℃〜1350℃である。The temperature distribution in the cross section of the sintered layer inside the sintered cake during sintering is
As illustrated in the figure, approximately 125
It is 0°C to 1350°C.
床敷鉱として、パレット上の最下部に充填された石灰石
は、焼結パレットの進行と共に、通過排カス温度が上昇
し、焼結ケーキが排鉱部に達する直Witには、第6図
にその温度経過の一例を示したように、真上の焼結ケー
キが赤熱状態を呈して焼結帯として焼結反応を生してい
るため、最高で1000℃〜1100°C程度まで昇温
されることになる。As the sintered pallet progresses, the temperature of the limestone that is filled in the lowest part of the pallet increases, and as the sintered cake reaches the ore discharge area, the temperature rises as shown in Figure 6. As shown in the example of the temperature progression, the sintered cake directly above becomes red hot and a sintering reaction occurs as a sintered zone, so the temperature rises to a maximum of about 1000°C to 1100°C. That will happen.
石灰石の脱炭耐分解反応を考えると、次の分解反応
Ca CO3+ Ca O+ CO2
ΔG’=40250−34.4T
は、標準自由エネルギ変化
ΔG0≦0
より、1170°K(897°C)以−トで起こり得る
。Considering the decarburization and decomposition-resistant reaction of limestone, the following decomposition reaction Ca CO3+ Ca O+ CO2 ΔG'=40250-34.4T is calculated from the standard free energy change ΔG0≦0 at 1170°K (897°C) and above. It can happen in
従って、床敷鉱が石灰石の分解反応に充分な高温域まで
達するような焼結鉱の製造条件の下で、石灰石を生石灰
に分解することができる。生石灰は、破砕機8を経て焼
結鉱と共に冷却機9に移送され、フードlOを介し、上
向吸引通風で冷却機に顕然回収設備を有する場合、集塵
機11、ホイラ12により、その顕熱が蒸気として回収
されると共に、焼結鉱が冷却される。こうして生石灰と
焼結鉱と混在した状態で、次工程の破砕拳篩分は設aL
8に供給され、−5mmは返鉱として、返鉱ホッパに移
送され、他の焼結原料と共に焼結に供される。この返鉱
中には生石灰も混在した状態となっている。Therefore, limestone can be decomposed into quicklime under conditions for producing sintered ore such that the bedding ore reaches a high temperature range sufficient for the decomposition reaction of limestone. The quicklime is transferred to the cooler 9 along with the sintered ore through the crusher 8, and the sensible heat is removed by the dust collector 11 and the wheeler 12 if the cooler has a sensible recovery facility by upward suction ventilation through the hood lO. is recovered as steam, and the sintered ore is cooled. In this way, in a state where quicklime and sintered ore are mixed, the next process of crushing and sifting is carried out at a
-5 mm is transferred to the return ore hopper as return ore, and is subjected to sintering together with other sintering raw materials. Quicklime is also mixed in this return ore.
一方+5 m m中には生石灰は殆ど存在せず、成品焼
結鉱として高炉へ送られる。On the other hand, there is almost no quicklime in +5 mm, and it is sent to the blast furnace as finished sintered ore.
゛また、排ガスダク)14に設けられた集塵機15や破
砕篩分は設備18および排熱回収ダクトlOに設けられ
た集塵機11で他のゲスI・類と共に回収された粉状の
生石灰は、例えば、ニューマローり等の吸引式ダスト回
収車などによって回収され 粉体専用ホッパ21に貯蔵
された後、焼結原料に供される。゛In addition, the powdered quicklime collected together with other gases I and 2 by the dust collector 15 installed in the exhaust gas duct 14 and the crushing sieve equipment 18 and the dust collector 11 installed in the exhaust heat recovery duct 10 is After being collected by a suction-type dust collection vehicle such as a pneumatic dust collector or the like and stored in a hopper 21 exclusively for powder, it is used as a sintering raw material.
こうして、焼結機で製造された生石灰は、返鉱中に混在
した小塊状のものと、ダスト類中に混在した粉状のもの
の2種が、従来、使用されている粉石灰石の代りに使用
される。In this way, the quicklime produced by the sintering machine is of two types: small lumps mixed in the return ore and powdered lime mixed in the dust, which can be used instead of the conventionally used powdered limestone. be done.
5000t/Dの生産量を有するDL式焼結機において
、従来130 k g / t −5inter 使用
していた−3 m mの粉石灰石のうち30kg/1−
sinter に相当する分を、10〜5mmに整流さ
れた石灰石に代えてこれを床敷鉱としてパレ・ントに供
給して操業したところ、従来、焼結成品の中から床敷鉱
として回収していた10〜5mmの焼結鉱がそのまま成
品となったためおよび生石灰の効果により5000t/
Dの生産量か5700t/Dに増加すると共に、焼結原
料中に配合されるコークス原単位が45 k g /
t −5inter か ら43 k g / t−5
interに減少した。In a DL type sintering machine with a production capacity of 5000t/D, 30kg/1 of the 3mm powdered limestone that was conventionally used at 130kg/t-5inter.
The amount equivalent to sinter was replaced with limestone rectified to 10 to 5 mm, and this was supplied to Palento as bedding ore. The sintered ore with a diameter of 10 to 5 mm was turned into a finished product as it was, and due to the effect of quicklime, the production volume was 5000 tons/
The production amount of D increased to 5,700 t/D, and the coke consumption rate added to the sintering raw material increased to 45 kg/D.
43 kg/t-5 from t-5inter
decreased to inter.
このように、本発明によれば、焼結鉱製造過程において
容易に生石灰を製造することか可能になると共に、この
生石灰を使用するので、生産量の増大、燃料費の低減の
外に品質や歩留りの向上、NOx転換率の向上をもたら
し、公害防止の点からも有効であるという種々の効果を
奏する。As described above, according to the present invention, it is possible to easily produce quicklime in the sinter manufacturing process, and since this quicklime is used, it not only increases production volume and reduces fuel costs, but also improves quality. It brings about various effects such as improved yield, improved NOx conversion rate, and is also effective in terms of pollution prevention.
第1図は、本発明の全体工程を示す工程図、第2図は、
その焼結機部分の詳細図、第3図、第4図はそれぞれバ
インダが生産率および落下強度に与える影響を例示した
グラフ、第5図は焼結層内の時間経過によるの温度分布
の例を示すグラフ、第6図は床敷鉱の温度分布を例示し
たグラフである。
■・・・焼結原料槽 2・・・ベルトコンベヤ3・・・
ドラムミキサ 4・・・給鉱ホッパ5・・・点火装置
6・・・床敷ホッパ7・・・焼結機 8・・・破砕機
9・・・冷却機 10・・・フード
11・・・集塵機 12・・・ボイラ
13・・・風箱 14・・・排気ダクト15・・・集塵
機 16・・・排風機
18・・・破砕、篩分は設備
19・・・集塵機 20・・・ブロワ
21・・・粉体専用ホッパ
lJj 願人 川崎製鉄株式会社
代 理 人 弁理士 小 杉 佳 男
升理士 齋藤和則
第3図
〜 第4図
メ
原料水分(%)FIG. 1 is a process diagram showing the overall process of the present invention, and FIG.
A detailed view of the sintering machine part, Figures 3 and 4 are graphs illustrating the influence of binder on production rate and drop strength, respectively, and Figure 5 is an example of temperature distribution over time in the sintered layer. FIG. 6 is a graph illustrating the temperature distribution of bedding ore. ■... Sintering raw material tank 2... Belt conveyor 3...
Drum mixer 4...Ore feeding hopper 5...Ignition device
6...Bedding hopper 7...Sintering machine 8...Crushing machine 9...Cooling machine 10...Hood 11...Dust collector 12...Boiler 13...Wind box 14...・Exhaust duct 15...Dust collector 16...Blower 18...Crushing and sieving equipment 19...Dust collector 20...Blower 21...Powder exclusive hopper lJj Applicant: Kawasaki Steel Co., Ltd. Patent Attorney Kazunori Saito Figures 3 to 4 Material Moisture (%)
Claims (1)
敷鉱として供給し、その上に焼結原料を供給して焼結す
ることを特徴とする焼結機によるバインダ用生石灰の製
造方法。■ A method for producing quicklime for a binder using a sintering machine, which is characterized in that when charging the sintering raw material into a pallet, limestone is supplied as a bedding, and the sintering raw material is supplied on top of it and sintered.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10442284A JPS60248830A (en) | 1984-05-25 | 1984-05-25 | Production of quicklime for binder by sintering machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10442284A JPS60248830A (en) | 1984-05-25 | 1984-05-25 | Production of quicklime for binder by sintering machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60248830A true JPS60248830A (en) | 1985-12-09 |
Family
ID=14380253
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10442284A Pending JPS60248830A (en) | 1984-05-25 | 1984-05-25 | Production of quicklime for binder by sintering machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60248830A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01205038A (en) * | 1988-02-10 | 1989-08-17 | Sumitomo Metal Ind Ltd | Production of sintered ore |
CN100449237C (en) * | 2007-02-13 | 2009-01-07 | 中冶长天国际工程有限责任公司 | Swinging funnel used for paving bottom flavoring of sintering machine |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5482303A (en) * | 1977-12-15 | 1979-06-30 | Sumitomo Heavy Ind Ltd | Manufacture of sintered ore |
JPS58133330A (en) * | 1982-02-03 | 1983-08-09 | Nippon Kokan Kk <Nkk> | Preparation of sintered ore |
-
1984
- 1984-05-25 JP JP10442284A patent/JPS60248830A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5482303A (en) * | 1977-12-15 | 1979-06-30 | Sumitomo Heavy Ind Ltd | Manufacture of sintered ore |
JPS58133330A (en) * | 1982-02-03 | 1983-08-09 | Nippon Kokan Kk <Nkk> | Preparation of sintered ore |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01205038A (en) * | 1988-02-10 | 1989-08-17 | Sumitomo Metal Ind Ltd | Production of sintered ore |
CN100449237C (en) * | 2007-02-13 | 2009-01-07 | 中冶长天国际工程有限责任公司 | Swinging funnel used for paving bottom flavoring of sintering machine |
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