JP2510193B2 - Sinter production method - Google Patents
Sinter production methodInfo
- Publication number
- JP2510193B2 JP2510193B2 JP8126187A JP8126187A JP2510193B2 JP 2510193 B2 JP2510193 B2 JP 2510193B2 JP 8126187 A JP8126187 A JP 8126187A JP 8126187 A JP8126187 A JP 8126187A JP 2510193 B2 JP2510193 B2 JP 2510193B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- layer
- sintered
- sinter
- sintering
- 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.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は焼結鉱の製造方法に関し、さらに詳しくは焼
結原料に用いる生石灰の焼成を併用すると共に、焼結鉱
の顕熱回収の効率化を図る技術に関する。TECHNICAL FIELD The present invention relates to a method for producing a sinter, and more specifically, it uses calcination of quick lime used as a sintering raw material together with the efficiency of sensible heat recovery of the sinter. Related to technology to achieve
連続式焼結機は、第3図に示すように、焼結機1のパ
レット上に床敷鉱ホッパ2から床敷鉱を供給し、原鉱ホ
ッパ3から焼結原料を供給し、この焼結原料層上面に点
火炉4で着火し、焼結機1の終端部で焼結が完了するよ
うに操業される。As shown in FIG. 3, the continuous sintering machine supplies the bed ore from the bed ore hopper 2 and the sintering raw material from the ore hopper 3 on the pallet of the sintering machine 1, and The upper surface of the binder layer is ignited in the ignition furnace 4 and operated at the end of the sintering machine 1 so that the sintering is completed.
このとき焼結原料には、通気性を確保するため造粒剤
として生石灰または消石灰が加えられているが、これら
造粒剤は、別途製造あるいは購入されるため、焼結コス
ト上昇の1原因となっている。At this time, quick lime or slaked lime is added to the sintering raw material as a granulating agent in order to ensure air permeability, but since these granulating agents are manufactured or purchased separately, they are one of the causes of the increase in sintering cost. Has become.
一方、焼結が完了した焼結鉱は図示しない1次クラッ
シャーを経て、冷却機に供給されるが、この焼結鉱は第
4図に示すが如く、温度分布を有しており、焼結層の上
半部は常温付近まで冷却されている。しかしながら従来
の技術では、この低温で粉率の高い焼結鉱も冷却機に供
給するため、その冷却効率が低い。On the other hand, the sintered ore after completion of the sintering is supplied to the cooler through the primary crusher (not shown). This sintered ore has a temperature distribution as shown in FIG. The upper half of the layer is cooled to near room temperature. However, in the conventional technique, since the sinter having a high powder rate at a low temperature is also supplied to the cooler, its cooling efficiency is low.
また、従来の技術としては特開昭58-133330のように
床敷鉱のかわりに石灰石を用い、これを生石灰化して、
回収するものがあるが、この場合には石灰石粒度が大き
いこともあり、そのまま成品系統に混入してしまい、回
収率が低かった。In addition, as a conventional technique, limestone is used instead of bedding as in JP-A-58-133330, and this is quick-calcified,
There is something to be recovered, but in this case, the particle size of limestone is large, so it was mixed into the product line as it was, and the recovery rate was low.
従来の技術では焼結機上で焼成した生石灰を効率良く
回収することは困難であった。また焼結鉱はパレット上
層部の低温で強度が低く粉率の高い部分が高温のパレッ
ト下層部の焼結鉱と共に冷却機に供給されるため、冷却
機における冷却効率が低い。It was difficult to efficiently collect quicklime burned on a sintering machine by the conventional technique. Further, the sinter has a low cooling efficiency in the chiller because the portion of the upper layer of the pallet having a low strength and a high powder ratio is supplied to the cooler together with the sinter of the lower layer of the pallet having a high temperature.
本発明は、連続式焼結機を用いて、焼結原料をパレッ
ト上に供給した後、原料表面に着火させる前の段階で、
パレット上焼結層上層部に粒度5mm〜15mmの石灰石を添
加し、該石灰石を原料焼結層上層部の表面から150mmま
での部分と共に混合し、この後、焼結層上表面に着火
し、焼結原料と共に石灰石を焼成して生石灰化させ、前
記焼結層上層部の表面から150mmまでの部分を除去装置
により連続的に取り出すことを特徴とする焼結鉱製造方
法である。The present invention, using a continuous sintering machine, after supplying the sintering raw material on the pallet, before the stage of igniting the raw material surface,
Limestone having a particle size of 5 mm to 15 mm is added to the upper layer portion of the sinter layer on the pallet, and the limestone is mixed together with a portion up to 150 mm from the surface of the upper layer portion of the raw material sintered layer, and thereafter, the surface of the sintered layer is ignited, A method for producing a sintered ore, characterized in that limestone is sintered together with a sintering raw material to give quick calcification, and a portion up to 150 mm from the surface of the upper portion of the sintered layer is continuously taken out by a removing device.
この場合に、前記除去装置は焼結機上に配置され、該
除去装置により取り出した焼結層上層部を返し鉱に戻
し、生石灰原料として焼結原料にリサイクルすると好適
である。In this case, it is preferable that the removing device is arranged on a sintering machine, the upper part of the sintered layer taken out by the removing device is returned to the return ore, and recycled as a raw material for quick lime into a sintering raw material.
通常の操業の場合、焼結機のパレット進行方向後流側
の部分の焼結層上層部すなわち上面からほぼ150mmまで
は、落下強度が低く、1次クラッシャー以後での粉率が
高い。このパレット上焼結層上層部の表面から150mmま
での部分に粒度5mm〜15mmの石灰石を添加し、焼成し、
次いでこの上層部が常温付近まで冷却され、1次クラッ
シャーに供給される前にこの上層部を除去することによ
って、生石灰化した石灰石は、この上層部と共にほぼ全
量を回収することができる。さらにこのパレット上の原
料層上層部を除去することによって冷却機での処理量が
少なくなり、冷却機での処理鉱石の粉率が低下し、冷却
機に送られる焼結鉱の平均温度が上昇するため、冷却機
の冷却効率が向上し、排熱回収量の増加も可能となる。In normal operation, the drop strength is low and the powder rate after the primary crusher is high up to approximately 150 mm from the upper part of the sintered layer, that is, on the downstream side in the pallet advancing direction of the sintering machine. From the surface of the upper layer of the sintered layer on this pallet, add limestone with a grain size of 5 mm to 15 mm to the part up to 150 mm, and burn,
Then, the upper layer portion is cooled to around room temperature, and the upper layer portion is removed before being supplied to the primary crusher, whereby almost all of the quick-calcified limestone can be recovered together with the upper layer portion. Furthermore, by removing the upper layer of the raw material layer on this pallet, the processing amount in the cooler decreases, the powder rate of the ore processed in the cooler decreases, and the average temperature of the sintered ore sent to the cooler rises. Therefore, the cooling efficiency of the cooler is improved, and the amount of recovered exhaust heat can be increased.
焼結機パレット上のパレット進行方向後流側の部分の
焼結層上層部は、落下強度が低く、下流工程で処理物の
粉率増加の原因となっている。この上層部は、強度が低
く、かつ常温付近まで冷却されているため、焼結機上で
の除去は容易である。The upper part of the sintered layer on the downstream side in the pallet traveling direction on the sinter machine pallet has a low drop strength, which causes an increase in the powder ratio of the processed material in the downstream process. Since this upper layer portion has low strength and is cooled to around room temperature, it is easy to remove it on the sintering machine.
〔実施例〕 本発明の実施例の一例を第1図、第2図、第4図を用
いて説明する。[Embodiment] An embodiment of the present invention will be described with reference to FIGS. 1, 2, and 4.
第1図に示すように、焼結機1のパレット上に床敷鉱
ホッパ2から床敷鉱を供給し、原料ホッパ3から原料を
供給し、この原料上表面に石灰石ホッパ12から石灰石を
供給する。さらにこの石灰石の焼成効率を高めるため、
この石灰石を原料焼結層上層部と共に混合装置13で混合
する。この混合後の原料上面に点火炉4で着火し、大気
を原料層上面から下面へと吸引し、焼結を行う。この焼
結機1のパレット進行方向後流側の部分では原料層上層
部は、焼結が完了しており、石灰石の生石灰化も完了し
ている。また、この部分の原料層上層部は強度、温度共
低いため、除去装置6によって容易に除去することがで
きる。As shown in FIG. 1, the bed mine ore hopper 2 supplies the bed mine ore to the pallet of the sintering machine 1, the raw material hopper 3 supplies the raw material, and the limestone hopper 12 supplies limestone to the upper surface of the raw material. To do. To further increase the firing efficiency of this limestone,
This limestone is mixed with the upper layer part of the raw material sintered layer in the mixing device 13. The upper surface of the mixed raw material is ignited in the ignition furnace 4, and the atmosphere is sucked from the upper surface to the lower surface of the raw material layer to perform sintering. In the portion on the downstream side of the pallet traveling direction of the sintering machine 1, the sintering of the upper layer of the raw material layer is completed and the calcification of limestone is also completed. Further, since the strength and temperature of the upper portion of the raw material layer in this portion are low, it can be easily removed by the removing device 6.
この除去された上層部は除去装置6の後に配置された
ベルトコンベヤ7で系外へ取り出され、返鉱としてリサ
イクルされ、焼結原料の造粒性を向上せしめる。The removed upper layer portion is taken out of the system by a belt conveyor 7 arranged after the removing device 6 and recycled as return ore to improve the granulation property of the sintering raw material.
次にこの除去装置6は、第2図に示すが如く、排土板
9で焼結層5の上層部、すなわち焼結層の表面から深さ
約150mmまでの部分を掘削集鉱する。掘削集鉱された焼
結鉱は、レーキチェーンコンベヤ8によって排土板9に
沿って掻き上げられ、後続のベルトコンベヤ7へ投入さ
れる。ただし、焼結層上層部の強度の低い部分だけを除
去するため、排土板9には図示せぬ掘削抵抗検出装置が
設けられ、その信号によって動作するシリンダ10によっ
て支持部11を支点として傾斜を変更し、これにより掘削
量が適宜制御され、焼結鉱歩止の低下を防止している。Next, as shown in FIG. 2, the removing device 6 excavates and collects the upper layer portion of the sintered layer 5, that is, a portion up to a depth of about 150 mm from the surface of the sintered layer, using the earth discharging plate 9. The sinter that has been excavated and collected is scraped up along the soil discharge plate 9 by the rake chain conveyor 8 and is fed to the subsequent belt conveyor 7. However, in order to remove only the low-strength portion of the upper portion of the sintered layer, the excavation plate 9 is provided with a digging resistance detection device (not shown), and the cylinder 10 operated by the signal tilts the support part 11 as a fulcrum. The amount of excavation is controlled as appropriate to prevent a decrease in the sintered ore retention.
以上の結果、造粒剤としての生石灰を安価に製造提供
することが可能となる。加えて、冷却機へ焼結鉱を供給
する以前に、温度が低くかつ強度が低く粉化し易い焼結
層上層部を取り除くことによって、冷却機の処理量の低
下、通気性の改善によって冷却効率を高めることができ
る。また冷却機へ供給する焼結鉱の平均温度が上昇する
ことによって排熱回収効率が高まり、排熱回収量の増加
が可能となる。As a result, it becomes possible to inexpensively produce and provide quicklime as a granulating agent. In addition, before supplying the sinter to the cooler, by removing the upper layer of the sintered layer, which has low temperature and low strength and is easily pulverized, the throughput of the cooler is reduced and the air permeability is improved to improve the cooling efficiency. Can be increased. In addition, since the average temperature of the sinter supplied to the cooler rises, the exhaust heat recovery efficiency increases and the exhaust heat recovery amount can be increased.
本発明は以上のように構成されているので次の優れた
効果を奏する。Since the present invention is configured as described above, it has the following excellent effects.
(1)焼結機を用いて、造粒剤としての生石灰を安価に
製造、提供することができる。(1) Quick lime as a granulating agent can be manufactured and provided at low cost using a sintering machine.
(2)パレット上の焼結層上層部の粉化し易く、冷却の
必要のない部分を破砕および冷却の前段階で除去するた
め、冷却装置での処理量が減少し、冷却装置での通気抵
抗が改善され、冷却効率の増加、冷却ファンの省電力を
図ることができる。(2) The upper part of the sintered layer on the pallet is easily pulverized, and the part that does not need to be cooled is removed before the crushing and cooling, so the amount of processing in the cooling device is reduced and the ventilation resistance in the cooling device is reduced. Can be improved, cooling efficiency can be increased, and cooling fan power can be saved.
(3)冷却装置へ提供する焼結鉱は、低温部の割合が減
少するため、平均温度が上昇し、排熱回収設備を有する
冷却装置では熱回収効率が上昇し、回収熱量が増加す
る。(3) Since the proportion of the low temperature part of the sinter provided to the cooling device decreases, the average temperature rises, the heat recovery efficiency of the cooling device having the exhaust heat recovery equipment increases, and the amount of recovered heat increases.
【図面の簡単な説明】 第1図は本発明方法の実施に用いる焼結機の模式的側面
図、第2図は本発明方法に用いる焼結鉱除去装置の一例
の模式的側面図、第3図は従来の焼結機の模式側面図、
第4図は焼結機から排出される直前のパレット上焼結鉱
の厚さ方向の温度分布曲線図である。 1……焼結機、2……床敷鉱ホッパ 3……原鉱ホッパ、4……点火炉 5……焼結層、6……除去装置 7……ベルトコンベヤ 8……レーキチェーンコンベヤ 9……排土板、10……シリンダ 11……支持装置、12……石灰石ホッパ 13……混合装置BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic side view of a sintering machine used for carrying out the method of the present invention, and FIG. 2 is a schematic side view of an example of a sintered ore removing device used for the method of the present invention. 3 is a schematic side view of a conventional sintering machine,
FIG. 4 is a temperature distribution curve diagram in the thickness direction of the sinter on the pallet immediately before being discharged from the sintering machine. 1 ... Sintering machine, 2 ... Floor ore hopper 3 ... Raw ore hopper, 4 ... Ignition furnace 5 ... Sintering layer, 6 ... Removal device 7 ... Belt conveyor 8 ... Rake chain conveyor 9 …… Soil dump plate, 10 …… Cylinder 11 …… Supporting device, 12 …… Limestone hopper 13 …… Mixing device
Claims (2)
ト上に供給した後、原料表面に着火させる前の段階で、
パレット上焼結層上層部に粒度5mm〜15mmの石灰石を添
加し、該石灰石を原料焼結層上層部の表面から150mmま
での部分と共に混合し、この後、焼結層上表面に着火
し、焼結原料と共に石灰石を焼成して生石灰化させ、前
記焼結層上層部の表面から150mmまでの部分を除去装置
により連続的に取り出すことを特徴とする焼結鉱製造方
法。1. A continuous sintering machine is used to supply a sintering raw material onto a pallet, and before the surface of the raw material is ignited.
Limestone having a particle size of 5 mm to 15 mm is added to the upper layer portion of the sinter layer on the pallet, and the limestone is mixed together with a portion up to 150 mm from the surface of the upper layer portion of the raw material sintered layer, and thereafter, the surface of the sintered layer is ignited, A method for producing a sintered ore, characterized in that limestone is sintered together with a sintering raw material to give quick calcification, and a portion up to 150 mm from the surface of the upper portion of the sintered layer is continuously taken out by a removing device.
去装置により取り出した焼結層上層部を返し鉱に戻し、
生石灰原料として焼結原料にリサイクルする請求項1記
載の焼結鉱製造方法。2. The removing device is arranged on a sintering machine, and the upper part of the sintered layer taken out by the removing device is returned to the return ore,
The method for producing a sinter according to claim 1, wherein the sinter ore is recycled as a lime raw material into a sinter raw material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8126187A JP2510193B2 (en) | 1987-04-03 | 1987-04-03 | Sinter production method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8126187A JP2510193B2 (en) | 1987-04-03 | 1987-04-03 | Sinter production method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63247315A JPS63247315A (en) | 1988-10-14 |
JP2510193B2 true JP2510193B2 (en) | 1996-06-26 |
Family
ID=13741422
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8126187A Expired - Fee Related JP2510193B2 (en) | 1987-04-03 | 1987-04-03 | Sinter production method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2510193B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0774400B2 (en) * | 1990-07-24 | 1995-08-09 | 川崎製鉄株式会社 | Sintered ore manufacturing method |
US6606202B2 (en) | 2000-09-26 | 2003-08-12 | Canon Kabushiki Kaisha | Zoom lens system and optical apparatus using the same |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58133331A (en) * | 1982-02-03 | 1983-08-09 | Nippon Kokan Kk <Nkk> | Preparation of sintered ore |
-
1987
- 1987-04-03 JP JP8126187A patent/JP2510193B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS63247315A (en) | 1988-10-14 |
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