JPH07151472A - Dust collecting method for sintered ore - Google Patents
Dust collecting method for sintered oreInfo
- Publication number
- JPH07151472A JPH07151472A JP29764693A JP29764693A JPH07151472A JP H07151472 A JPH07151472 A JP H07151472A JP 29764693 A JP29764693 A JP 29764693A JP 29764693 A JP29764693 A JP 29764693A JP H07151472 A JPH07151472 A JP H07151472A
- Authority
- JP
- Japan
- Prior art keywords
- dust
- compressed air
- ore
- sintered ore
- sintered
- 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- Withdrawn
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、焼結機で焼結した焼
結鉱の大塊を一次クラッシャーで破砕する際に発生する
粉塵を、集塵する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for collecting dust generated when a large lump of sintered ore sintered by a sintering machine is crushed by a primary crusher.
【0002】[0002]
【従来の技術】焼結機から排鉱された焼結鉱の大塊は、
高温の状態で一次クラッシャーにて破砕された後、焼結
鉱冷却機に給鉱され、冷却された後排鉱される。これら
焼結鉱の排鉱時、破砕時および給鉱時には空気中に粉塵
が発生するが、この粉塵は焼結機排鉱部上方に設けた集
塵機や、焼結鉱冷却機に設けた集塵装置により集塵して
いる。焼結鉱冷却機の集塵装置としては、冷却機の冷却
ゾーンと排気塔との間にルーバー式集塵機を設けたり、
排気塔で散水する方式が採用されている。2. Description of the Related Art Large blocks of sintered ore discharged from a sintering machine are
After being crushed by the primary crusher at high temperature, it is fed to a sinter cooler, cooled, and then discharged. Dust is generated in the air when these sinters are discharged, crushed, and fed, but these dusts are collected in the dust collector installed above the sinter ore cooler of the sinter or the sinter cooler. Dust is collected by the device. As a dust collector for the sinter cooler, a louver dust collector is provided between the cooling zone of the cooler and the exhaust tower,
The method of spraying water in the exhaust tower is adopted.
【0003】しかしながら、焼結鉱冷却後の含塵ガスは
その量が多いため、全排ガス量を集塵するには多大な設
備費がかかるため、特に含塵率の大きい給鉱部付近の排
気塔のみ、前記ルーバー式集塵機のような簡易集塵機を
設けるのが一般的である。However, since the amount of the dust-containing gas after cooling the sinter is large, it takes a great equipment cost to collect the total amount of exhaust gas. Generally, only a tower is provided with a simple dust collector such as the louver type dust collector.
【0004】また、このような問題に対処するため、特
開平5−79770号公報に開示された技術に基づく焼
結鉱冷却機の集塵方法においては、冷却機を冷却前半部
と冷却後半部とに分け、冷却前半部において焼結鉱の冷
却と冷却風による強制発塵を行い、冷却後半部のみのガ
スを集塵機で処理するようにしている。Further, in order to deal with such a problem, in the dust collecting method for a sinter ore cooler based on the technique disclosed in Japanese Patent Laid-Open No. 5-79770, the cooler is cooled in the first half and in the second half. In the first half of cooling, the sinter ore is cooled and forced dust is generated by the cooling air, and the gas in only the second half of cooling is processed by the dust collector.
【0005】また、特開昭60−208428号公報に
開示された技術に基づく焼結鉱冷却機の集塵方法におい
ては、高濃度発塵部を高性能集塵機で、低濃度発塵部を
簡易集塵機で集塵するようにしている。Further, in the dust collecting method of the sinter ore cooler based on the technique disclosed in Japanese Patent Application Laid-Open No. 60-208428, the high-concentration dust generating section is a high-performance dust collecting section, and the low-concentration dust generating section is simple. I try to collect dust with a dust collector.
【0006】[0006]
【発明が解決しようとする課題】しかしながら、上述し
た従来の焼結鉱冷却機の集塵方法には、次のような問題
点があった。 (1)ルーバー式やスプレー式の簡易集塵機による方法 コスト面では有利であるが、粉塵の捕集効率が低く、排
気塔から多量の粉塵が大気中に排出される。 (2)特開平5−79770号公報や特開昭60−20
8428号公報に開示された方法 多大な設備費がかかり、効率的ではあっても経済的では
ない。However, the above-mentioned conventional dust collecting method for the sinter cooler has the following problems. (1) Method using a louver-type or spray-type simple dust collector Although it is advantageous in terms of cost, the dust collection efficiency is low and a large amount of dust is discharged into the atmosphere from the exhaust tower. (2) JP-A-5-79770 and JP-A-60-20
The method disclosed in Japanese Patent No. 8428 has a large equipment cost and is not economical even though it is efficient.
【0007】この発明は従来技術の上述のような問題点
を解消するためになされたものであり、少ない費用で効
率よく集塵することのできる焼結鉱の粉塵集塵方法を提
供することを目的としている。The present invention has been made to solve the above-mentioned problems of the prior art, and it is an object of the present invention to provide a method for collecting dust of sinter that can efficiently collect dust at a low cost. Has an aim.
【0008】[0008]
【課題を解決するための手段】この発明に係る焼結鉱の
粉塵集塵方法は、焼結機で焼結した焼結鉱の大塊を排鉱
部において1次クラッシャーで破砕する際に発生する粉
塵を、1次クラッシャー上方に設けた集塵機で集塵する
方法において、1次クラッシャーの下方に設けた圧縮空
気噴射ノズルから破砕された焼結鉱に向けて圧縮空気を
噴射し、破砕により発生した粉塵を強制浮遊させて集塵
するものである。The method for collecting dust of a sintered ore according to the present invention is generated when a large lump of the sintered ore sintered by a sintering machine is crushed by a primary crusher in an effluent section. Generated by crushing by injecting compressed air toward the crushed sinter from the compressed air injection nozzle provided below the primary crusher in the method of collecting the dust that is generated by the dust collector installed above the primary crusher. The dust is forced to float and collected.
【0009】[0009]
【作用】焼結鉱の破砕時に発生し重力により下方に沈降
しようとする粉塵は、圧縮空気により強制浮遊させられ
て1次クラッシャーの上方に設けられた集塵機により集
塵される。よって、破砕時の集塵効率が高まる。したが
って、破砕に続く焼結鉱の冷却時には、冷却用ガスに含
有される粉塵の濃度は低く、簡易集塵機でも効率よく粉
塵を集塵でき、大気を粉塵で汚染することはない。The dust generated when the sinter ore is crushed and settling downward due to gravity is forcibly suspended by compressed air and collected by the dust collector provided above the primary crusher. Therefore, the dust collection efficiency at the time of crushing is increased. Therefore, when the sinter ore is cooled after crushing, the concentration of the dust contained in the cooling gas is low, the dust can be efficiently collected even by the simple dust collector, and the atmosphere is not polluted with the dust.
【0010】[0010]
【実施例】この発明の実施例の焼結鉱の粉塵集塵方法
を、図1の説明図に基づき説明する。この集塵方法にお
いては、焼結機21により焼結した焼結鉱1を、排鉱部
2において一次クラッシャー3で破砕するときに、一次
クラッシャー3の下方に設けた圧縮空気噴射ノズル4か
ら、圧縮空気を焼結鉱1に向けて噴射する。圧縮空気を
噴射した空間には、焼結鉱1の破砕にともなって発生
し、重力によって沈降しようとしている粉塵5が存在す
るが、これらの粉塵5は圧縮空気により吹き上げられ
る。EXAMPLE A method of collecting dust of sinter according to an example of the present invention will be described with reference to the explanatory view of FIG. In this dust collecting method, when the sintered ore 1 sintered by the sintering machine 21 is crushed by the primary crusher 3 in the discharge ore section 2, from the compressed air injection nozzle 4 provided below the primary crusher 3, Compressed air is jetted toward the sintered ore 1. In the space into which the compressed air is jetted, there are dusts 5 that are generated due to the crushing of the sintered ore 1 and are about to settle due to gravity, but these dusts 5 are blown up by the compressed air.
【0011】このようにして強制的に浮遊させられた粉
塵5は、排鉱部2の上方に設けた集塵機6により集塵さ
れる。この集塵方法においては、従来下方に沈降してし
まう粉塵まで集塵してしまうので、排鉱部2における集
塵効率が上昇する。破砕後の焼結鉱1aは給鉱部22か
ら冷却機23に入り、排鉱部23まで冷却機24を移動
する間に、冷却ブロアー25から送られる冷却用空気に
より冷却される。The dust 5 thus forcibly suspended is collected by a dust collector 6 provided above the mine ore section 2. In this dust collection method, even the dust that has conventionally settled downward is collected, so that the dust collection efficiency in the mine unit 2 is increased. The crushed sinter 1a enters the cooler 23 from the ore feeding section 22 and is cooled by the cooling air sent from the cooling blower 25 while moving the cooler 24 to the discharge ore section 23.
【0012】冷却機23の冷却ゾーン26を通過した含
塵空気は、粉塵が前記排鉱部2で90%以上集塵してあ
るのでその含塵量は少なく、排気塔27から直接排気し
ても、大気を汚染することはない。集塵機6には、電気
集塵機を使用してもよいし、バグフィルター集塵機を使
用してもよい。The dust-containing air that has passed through the cooling zone 26 of the cooler 23 has a small amount of dust because the dust is collected in the exhaust ore section 2 in an amount of 90% or more, and is exhausted directly from the exhaust tower 27. However, it does not pollute the atmosphere. The dust collector 6 may be an electric dust collector or a bag filter dust collector.
【0013】[0013]
【発明の効果】この発明により、焼結鉱の粉塵を安い費
用で効率よく集塵でき、大気汚染も発生しない。According to the present invention, the dust of the sintered ore can be efficiently collected at a low cost and the air pollution does not occur.
【図1】この発明の実施例の焼結鉱の粉塵集塵方法の説
明図である。FIG. 1 is an explanatory view of a method for collecting dust of a sintered ore according to an embodiment of the present invention.
1 焼結鉱 2 排鉱部 3 一次クラッシャー 4 圧縮空気噴射ノズル 5 粉塵 6 集塵機 1 Sintered ore 2 Exhaust ore part 3 Primary crusher 4 Compressed air injection nozzle 5 Dust 6 Dust collector
Claims (1)
において1次クラッシャーで破砕する際に発生する粉塵
を、1次クラッシャー上方に設けた集塵機で集塵する方
法において、1次クラッシャーの下方に設けた圧縮空気
噴射ノズルから破砕された焼結鉱に向けて圧縮空気を噴
射し、破砕により発生した粉塵を強制浮遊させて集塵す
ることを特徴とする焼結鉱の粉塵集塵方法。1. A method of collecting dust generated by crushing a large lump of sinter ore sintered by a sinter with a primary crusher in an effluent section by a dust collector provided above the primary crusher. Sintered ore characterized by injecting compressed air toward a crushed sinter from a compressed air injection nozzle provided below the primary crusher and forcibly suspending the dust generated by the crush and collecting the dust. Dust collection method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29764693A JPH07151472A (en) | 1993-11-29 | 1993-11-29 | Dust collecting method for sintered ore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29764693A JPH07151472A (en) | 1993-11-29 | 1993-11-29 | Dust collecting method for sintered ore |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07151472A true JPH07151472A (en) | 1995-06-16 |
Family
ID=17849285
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29764693A Withdrawn JPH07151472A (en) | 1993-11-29 | 1993-11-29 | Dust collecting method for sintered ore |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07151472A (en) |
-
1993
- 1993-11-29 JP JP29764693A patent/JPH07151472A/en not_active Withdrawn
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20010130 |