JP2001330373A - Cooler for sintered ore - Google Patents

Cooler for sintered ore

Info

Publication number
JP2001330373A
JP2001330373A JP2000147367A JP2000147367A JP2001330373A JP 2001330373 A JP2001330373 A JP 2001330373A JP 2000147367 A JP2000147367 A JP 2000147367A JP 2000147367 A JP2000147367 A JP 2000147367A JP 2001330373 A JP2001330373 A JP 2001330373A
Authority
JP
Japan
Prior art keywords
exhaust heat
sintered ore
hood
heat recovery
pipe
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
Application number
JP2000147367A
Other languages
Japanese (ja)
Inventor
Masayoshi Ishikawa
正芳 石川
Naoki Ishihara
直樹 石原
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2000147367A priority Critical patent/JP2001330373A/en
Publication of JP2001330373A publication Critical patent/JP2001330373A/en
Pending legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Furnace Details (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a cooler which can prevent the trouble in an after process by cooling enough sintered ore even in the case that the quantity of produced sintered ore increases. SOLUTION: This cooler has a hood for covering sintered ore shifting within the cooler itself, a heat exchanger for recovering the exhaust heat of hot blast recovered from the hood, a circulation pipe for circulating the hot blast at a relatively low temperature having its exhaust heat recovered to the downside of sintered ore under the hood, an outside air inlet for sucking outside air into the circulation pipe and mixing it with hot blast at a relatively low temperature, and a damper being arranged in a branch pipe for sending the cooling gas within the circulation pipe to an exhaust cylinder, being branched from the circulation pipe.

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、焼結機から排出さ
れた後、熱間破砕された焼結鉱を冷却する冷却装置に関
し、特に焼結鉱の生産量の変動に対して十分な冷却能力
を維持できる冷却装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling apparatus for cooling a hot-crushed sintered ore after being discharged from a sintering machine, and more particularly to a cooling apparatus which sufficiently cools a fluctuation in the production amount of the ore. The present invention relates to a cooling device capable of maintaining a capacity.

【0002】[0002]

【従来の技術】一般に、焼結機から排出された焼結鉱
は、通常 100〜200mm 程度の大きさに熱間破砕され、熱
間篩にて粉焼結鉱を除去した後、冷却装置にて冷却さ
れ、その後、破砕整粒される。熱間破砕された焼結鉱
は、散水冷却等で急冷すると微細なクラック等が生じて
焼結鉱の強度が低下するため、空冷式の冷却装置を用い
て冷却するのが一般的である。
2. Description of the Related Art Generally, sintered ore discharged from a sintering machine is usually hot crushed to a size of about 100 to 200 mm, and after removing powdered ore with a hot sieve, the sinter is cooled. And then crushed and sized. Hot crushed sintered ore is rapidly cooled by sprinkling cooling or the like, so that fine cracks or the like are generated and the strength of the sintered ore is reduced. Therefore, the ore is generally cooled using an air-cooled cooling device.

【0003】図2は、従来の空冷式の冷却装置の構成を
示す配置図であり、配管系統のブロック図とともに示
す。図2中の矢印は、コンベア上に載置された焼結鉱の
移動方向を示す。焼結機から排出された焼結鉱3は、熱
間破砕された後、シュート1を介してコンベア2上に載
置されて移動する。コンベア2上に載置された焼結鉱3
の上側にはフードが配設され、そのフードは仕切り板6
によって2分割され、上流側のフードが排熱回収ゾーン
フード4、下流側が非排熱回収ゾーンフード5となる。
FIG. 2 is a layout diagram showing a configuration of a conventional air-cooled cooling device, and is shown together with a block diagram of a piping system. The arrow in FIG. 2 indicates the moving direction of the sintered ore placed on the conveyor. The sintered ore 3 discharged from the sintering machine is placed on the conveyor 2 via the chute 1 and moved after being hot-crushed. Sinter 3 placed on conveyor 2
A hood is disposed above the hood, and the hood is provided with a partition plate 6.
The upstream hood becomes the exhaust heat recovery zone hood 4 and the downstream hood becomes the non-exhaust heat recovery zone hood 5.

【0004】熱間破砕された焼結鉱3をシュート1から
コンベア2上に載置するときに粉塵が飛散して、排熱回
収ゾーンフード4から回収された熱風に混入する。した
がって排熱回収ゾーンフード4から回収された熱風は、
集塵機13で粉塵を除去された後、熱交換機7に送給され
て排熱を回収される。排熱を回収された比較的低温の熱
風(以下、排熱回収後の熱風という)は、循環ファン9
を用いて、循環管10を介して排熱回収ゾーンフード4下
を移動する焼結鉱3の下側へ送風される。排熱回収後の
熱風が焼結鉱3を冷却することによって発生する熱風
は、再度、排熱回収ゾーンフード4から回収され、熱交
換機7で排熱を回収されて循環する。
When the hot crushed sintered ore 3 is placed on the conveyor 2 from the chute 1, dust scatters and mixes with the hot air recovered from the exhaust heat recovery zone hood 4. Therefore, the hot air collected from the waste heat recovery zone hood 4 is
After the dust is removed by the dust collector 13, the dust is sent to the heat exchanger 7 and the exhaust heat is collected. The relatively low-temperature hot air from which the exhaust heat has been recovered (hereinafter referred to as “hot air after exhaust heat recovery”) is supplied to the circulation fan 9.
Is blown to the lower side of the sintered ore 3 moving under the exhaust heat recovery zone hood 4 through the circulation pipe 10. The hot air generated by cooling the sintered ore 3 by the hot air after the exhaust heat recovery is recovered from the exhaust heat recovery zone hood 4 again, and the exhaust heat is recovered and circulated by the heat exchanger 7.

【0005】このように空冷式の冷却機を用いて焼結鉱
を冷却すると熱風が発生する。その熱風から排熱を回収
して、種々の装置の熱源として利用すると燃料原単位の
削減に有効である。そこで焼結鉱の冷却機から発生する
熱風の排熱を効率よく回収するために、種々の技術が提
案されている。たとえば特公昭62-17014号公報には、排
熱回収を行なう焼結設備冷却機が開示されている。この
技術は、排熱回収ゾーンフード4をさらに上流側と下流
側に2分割し、上流側の排熱回収ゾーンフードに接続し
た管路のみに集塵機を設けることにより、設備費,運転
費を低減しようとするものである。しかしこの装置で
は、焼結鉱の生産量が増加したときには、排熱回収ゾー
ンフードから回収された熱風の排熱を十分に回収できな
くなる。その結果、排熱回収後の熱風の温度が高くな
り、焼結鉱の冷却が不十分となる。その結果、冷却機か
ら後工程へ焼結鉱を送給する際に、ベルトコンベアのゴ
ムベルトを焼損させるという問題があった。
[0005] When the sintered ore is cooled using the air-cooled cooler, hot air is generated. If the exhaust heat is recovered from the hot air and used as a heat source for various devices, it is effective in reducing the unit fuel consumption. Therefore, various techniques have been proposed in order to efficiently recover the exhaust heat of hot air generated from a sinter cooler. For example, Japanese Patent Publication No. Sho 62-17014 discloses a sintering equipment cooler for recovering exhaust heat. This technology reduces the equipment cost and operating cost by further dividing the exhaust heat recovery zone hood 4 into two parts, the upstream side and the downstream side, and providing a dust collector only in the pipe connected to the upstream side exhaust heat recovery zone hood. What you want to do. However, with this device, when the production amount of the sinter increases, the exhaust heat of the hot air collected from the exhaust heat recovery zone hood cannot be sufficiently recovered. As a result, the temperature of the hot air after exhaust heat recovery becomes high, and the cooling of the sintered ore becomes insufficient. As a result, when the sinter is fed from the cooler to the subsequent process, there is a problem that the rubber belt of the belt conveyor is burned.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記のような
問題を解消し、焼結鉱の生産量が増加した場合でも焼結
鉱を十分に冷却して、後工程のトラブルを防止できる焼
結鉱の冷却装置を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems, and allows the sinter to be sufficiently cooled even if the production amount of the sinter increases, thereby preventing troubles in the post-process. An object of the present invention is to provide a cooling device for condensate.

【0007】[0007]

【課題を解決するための手段】本発明は、焼結機から排
出され、次いで熱間破砕された焼結鉱の冷却装置であっ
て、コンベア上に載置されて移動する焼結鉱を上方から
覆う排熱回収ゾーンフードと、排熱回収ゾーンフードか
ら回収された熱風の排熱を回収する熱交換機と、排熱回
収後の熱風を排熱回収ゾーンフード下の焼結鉱の下側へ
循環させる循環ファンを備えた循環管と、循環管内に外
気を吸入して排熱回収後の熱風と混合する外気吸入口
と、循環管から分岐して循環管内の冷却用ガスを排気筒
ヘ送給する分岐管と、分岐管に配設されたダンパとを有
する焼結鉱の冷却装置である。
SUMMARY OF THE INVENTION The present invention is a cooling device for a sintered ore discharged from a sintering machine and then hot crushed, wherein the ore moving on a conveyor is moved upward. Exhaust heat recovery zone hood to cover from, heat exchanger to recover the exhaust heat of the hot air recovered from the exhaust heat recovery zone hood, and the hot air after the exhaust heat recovery to the lower side of the sintered ore under the exhaust heat recovery zone hood A circulating pipe with a circulating fan to circulate, an outside air suction port that sucks outside air into the circulating pipe and mixes it with the hot air after exhaust heat recovery, and branches from the circulating pipe to send cooling gas in the circulating pipe to the exhaust stack This is a cooling device for sinter having a branch pipe to be supplied and a damper disposed in the branch pipe.

【0008】[0008]

【発明の実施の形態】図1は、本発明の冷却装置の例を
示す配置図であり、配管系統のブロック図とともに示
す。図1中の矢印は、コンベア上に載置された焼結鉱の
移動方向を示す。焼結機から排出された焼結鉱3は、熱
間破砕された後、シュート1を介してコンベア2上に載
置されて移動する。コンベア2上に載置された焼結鉱3
の上側にはフードが配設され、そのフードは仕切り板6
によって2分割され、上流側のフードが排熱回収ゾーン
フード4、下流側のフードが非排熱回収ゾーンフード5
となる。
FIG. 1 is a layout diagram showing an example of a cooling device according to the present invention, which is shown together with a block diagram of a piping system. The arrow in FIG. 1 indicates the moving direction of the sintered ore placed on the conveyor. The sintered ore 3 discharged from the sintering machine is placed on the conveyor 2 via the chute 1 and moved after being hot-crushed. Sinter 3 placed on conveyor 2
A hood is disposed above the hood, and the hood is provided with a partition plate 6.
The hood on the upstream side is an exhaust heat recovery zone hood 4 and the hood on the downstream side is a non-exhaust heat recovery zone hood 5
Becomes

【0009】排熱回収ゾーンフード4から回収された熱
風は熱交換機7に送給され、排熱を回収される。排熱回
収後の熱風と外気とを混合するために、熱交換機7の出
側の循環管10に外気吸入口8を配設して外気を吸入す
る。外気は排熱回収後の熱風より低温であるから、排熱
回収後の熱風と外気とを混合することによって得られる
ガス(以下、冷却用ガスという)の温度は、排熱回収後
の熱風よりさらに低下する。したがって冷却用ガスを用
いると、焼結鉱3の冷却効率が向上する。
The hot air recovered from the waste heat recovery zone hood 4 is sent to a heat exchanger 7 to recover the waste heat. In order to mix the hot air after the recovery of exhaust heat with the outside air, an outside air suction port 8 is provided in the circulation pipe 10 on the outlet side of the heat exchanger 7 to suck the outside air. Since the temperature of the outside air is lower than that of the hot air after the recovery of the exhaust heat, the temperature of the gas obtained by mixing the hot air after the recovery of the exhaust heat and the outside air (hereinafter referred to as cooling gas) is lower than the temperature of the hot air after the recovery of the exhaust heat. Further decline. Therefore, when the cooling gas is used, the cooling efficiency of the sintered ore 3 is improved.

【0010】なお図1中には示されていないが、熱交換
機7の入側に集塵機を配設しても良い。冷却用ガスは、
循環ファン9を用いて、循環管10を介して排熱回収ゾー
ンフード4下を移動する焼結鉱3の下側へ送風される。
冷却用ガスが焼結鉱3を冷却することによって発生する
熱風は、再度、排熱回収ゾーンフード4から回収され、
熱交換機7で排熱を回収されて循環する。
Although not shown in FIG. 1, a dust collector may be provided on the inlet side of the heat exchanger 7. The cooling gas is
Using the circulation fan 9, the air is sent to the lower side of the sintered ore 3 moving under the exhaust heat recovery zone hood 4 through the circulation pipe 10.
The hot air generated by the cooling gas cooling the sinter 3 is recovered from the exhaust heat recovery zone hood 4 again,
Exhaust heat is recovered and circulated by the heat exchanger 7.

【0011】外気吸入口8から外気を過剰に吸入する
と、冷却用ガスの流量も増大する。冷却用ガスの流量が
過剰である場合は、排熱回収ゾーンフード4から回収さ
れる熱風中に粉塵が大量に混入して熱交換機7内の配管
の目詰まりが発生したり、熱交換機7の能力を超える熱
量が発生する等の原因になる。そこで、冷却用ガスの流
量を調整するために、循環管10にはダンパ12を有する分
岐管13を設ける。
If the outside air is excessively sucked from the outside air suction port 8, the flow rate of the cooling gas also increases. When the flow rate of the cooling gas is excessive, a large amount of dust is mixed in the hot air collected from the exhaust heat recovery zone hood 4 to cause clogging of the pipes in the heat exchanger 7, This may cause the generation of heat exceeding the capacity. Therefore, a branch pipe 13 having a damper 12 is provided in the circulation pipe 10 in order to adjust the flow rate of the cooling gas.

【0012】すなわち、循環管10内の冷却用ガスの流量
が過剰である場合は、ダンパ12を開いて、冷却用ガスの
一部を分岐管11へ導入する。こうして分岐管11へ導入さ
れた冷却用ガスは、集塵機13によって粉塵を除去された
後、排気ファン14によって排気筒15から放散される。な
お、熱間破砕された焼結鉱3を、シュート1からコンベ
ア2上に載置するときに粉塵が飛散するが、その粉塵は
排熱回収ゾーンフード4内で冷却用ガスに混入した後、
排気筒15から放散される前に集塵機13で除去される。つ
まり、焼結鉱3が非排熱回収ゾーンフード5下へ移動し
てきたときには、粉塵は発生しない。また焼結鉱3の温
度も低下している。したがって非排熱回収ゾーンフード
5から回収されるガスを排気ファン16によって外気に放
散しても問題はない。
That is, when the flow rate of the cooling gas in the circulation pipe 10 is excessive, the damper 12 is opened and a part of the cooling gas is introduced into the branch pipe 11. The cooling gas introduced into the branch pipe 11 in this manner is dust-removed by the dust collector 13 and then is radiated from the exhaust pipe 15 by the exhaust fan 14. In addition, dust is scattered when the hot crushed sintered ore 3 is placed on the conveyor 2 from the chute 1, and after the dust is mixed with the cooling gas in the exhaust heat recovery zone hood 4,
Before being emitted from the exhaust stack 15, the dust is removed by the dust collector 13. That is, when the sintered ore 3 moves below the non-exhaust heat recovery zone hood 5, no dust is generated. Further, the temperature of the sintered ore 3 is also lowered. Therefore, there is no problem even if the gas collected from the non-exhaust heat recovery zone hood 5 is radiated to the outside air by the exhaust fan 16.

【0013】[0013]

【実施例】有効火格子面積 200m2 の焼結機において、
焼結機の出側に図2に示すような従来の冷却機を配設し
て、焼結機の操業を行なった。これを比較例とする。こ
の比較例では、焼結機の生産性すなわち1hrあたりの生
産量が 460t/hrを越えると、冷却機出側の焼結鉱の温
度が 100℃を越えるため、ベルトコンベアの焼損等の輸
送上の問題が生じた。したがって焼結機の生産性は、最
大 460t/hrであった。
[Example] In a sintering machine with an effective grate area of 200 m 2 ,
A conventional cooling machine as shown in FIG. 2 was disposed on the outlet side of the sintering machine, and the sintering machine was operated. This is a comparative example. In this comparative example, if the productivity of the sintering machine, that is, the production rate per hour exceeds 460 t / hr, the temperature of the sinter ore on the outlet side of the cooling machine exceeds 100 ° C. The problem arose. Therefore, the productivity of the sintering machine was up to 460 t / hr.

【0014】次いで図1に示すように、循環管10に外気
吸入口8を配設し、集塵機13や排気筒15を有する分岐管
11にダンパ12を配設した本発明の冷却装置を用いて、焼
結機の操業を行なった。これを発明例とする。この発明
例では、焼結機の生産性を540t/hrとして操業して
も、冷却機出側の焼結鉱の温度は 100℃以下であり、輸
送上の問題は生じなかった。
Next, as shown in FIG. 1, a branch pipe having a dust collector 13 and an exhaust pipe 15 is provided with an outside air intake port 8 in a circulation pipe 10.
The sintering machine was operated using the cooling device of the present invention in which the damper 12 was provided in 11. This is an example of the invention. In this example of the invention, even when the sintering machine was operated at a productivity of 540 t / hr, the temperature of the sinter on the outlet side of the cooling machine was 100 ° C. or less, and there was no transportation problem.

【0015】したがって発明例と比較例について焼結機
の生産性(t/hr)を比較すると、発明例の方が比較例
より17%増加した。
Therefore, when the productivity (t / hr) of the sintering machine was compared between the invention example and the comparative example, the invention example increased by 17% compared with the comparative example.

【0016】[0016]

【発明の効果】本発明では、焼結鉱の生産量が増加した
場合でも焼結鉱を十分に冷却でき、しかも小規模の設備
改造で対応できるので、経済的に有利である。
According to the present invention, even when the production amount of the sinter is increased, the sinter can be sufficiently cooled and can be dealt with by small-scale equipment modification, which is economically advantageous.

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

【図1】本発明の冷却装置の例を示す配置図であり、配
管系統のブロック図とともに示す。
FIG. 1 is a layout diagram showing an example of a cooling device of the present invention, which is shown together with a block diagram of a piping system.

【図2】従来の冷却装置の例を示す配置図であり、配管
系統のブロック図とともに示す。
FIG. 2 is a layout diagram showing an example of a conventional cooling device, which is shown together with a block diagram of a piping system.

【符号の説明】[Explanation of symbols]

1 シュート 2 コンベア 3 焼結鉱 4 排熱回収ゾーンフード 5 非排熱回収ゾーンフード 6 仕切り板 7 熱交換器 8 外気吸入口 9 循環ファン 10 循環管 11 分岐管 12 ダンパ 13 集塵機 14 排気ファン 15 排気筒 16 排気ファン DESCRIPTION OF SYMBOLS 1 Chute 2 Conveyor 3 Sinter 4 Exhaust heat recovery zone hood 5 Non-exhaust heat recovery zone hood 6 Partition plate 7 Heat exchanger 8 External air intake 9 Circulation fan 10 Circulation pipe 11 Branch pipe 12 Damper 13 Dust collector 14 Exhaust fan 15 Discharge Cylinder 16 exhaust fan

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 焼結機から排出され、次いで熱間破砕さ
れた焼結鉱の冷却装置であって、コンベア上に載置され
て移動する前記焼結鉱を上方から覆う排熱回収ゾーンフ
ードと、前記排熱回収ゾーンフードから回収された熱風
の排熱を回収する熱交換機と、排熱回収後の熱風を前記
排熱回収ゾーンフード下の前記焼結鉱の下側へ循環させ
る循環ファンを備えた循環管と、前記循環管内に外気を
吸入して前記排熱回収後の熱風と混合する外気吸入口
と、前記循環管から分岐して前記循環管内の冷却用ガス
を排気筒ヘ送給する分岐管と、前記分岐管に配設された
ダンパとを有することを特徴とする焼結鉱の冷却装置。
1. A cooling device for a sintered ore discharged from a sintering machine and then hot crushed, wherein the waste heat recovery zone hood covers the sinter ore placed and moving on a conveyor from above. A heat exchanger for collecting the exhaust heat of the hot air collected from the exhaust heat recovery zone hood, and a circulation fan for circulating the hot air after the exhaust heat recovery to the lower side of the sintered ore under the exhaust heat recovery zone hood. A circulating pipe provided with a circulating pipe, an outside air suction port for sucking outside air into the circulating pipe and mixing with the hot air after the exhaust heat recovery, and branching the circulating pipe to send a cooling gas in the circulating pipe to an exhaust pipe. A cooling device for a sintered ore, comprising: a branch pipe to be supplied; and a damper disposed in the branch pipe.
JP2000147367A 2000-05-19 2000-05-19 Cooler for sintered ore Pending JP2001330373A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000147367A JP2001330373A (en) 2000-05-19 2000-05-19 Cooler for sintered ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000147367A JP2001330373A (en) 2000-05-19 2000-05-19 Cooler for sintered ore

Publications (1)

Publication Number Publication Date
JP2001330373A true JP2001330373A (en) 2001-11-30

Family

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010057439A1 (en) * 2008-11-21 2010-05-27 中冶长天国际工程有限责任公司 Method and system for reusing flue gas of circular cooler, and circular cooler
CN104006403A (en) * 2014-05-29 2014-08-27 马钢(集团)控股有限公司 Gas diluting device and gas diluting method
JP2015183875A (en) * 2014-03-20 2015-10-22 株式会社神戸製鋼所 Cooling apparatus cooling sintered ore and pellet and exhaust control method in the cooling apparatus
CN105202918A (en) * 2014-06-29 2015-12-30 上海梅山钢铁股份有限公司 Sintering blowing type annular cooler ore removal temperature control device and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010057439A1 (en) * 2008-11-21 2010-05-27 中冶长天国际工程有限责任公司 Method and system for reusing flue gas of circular cooler, and circular cooler
JP2015183875A (en) * 2014-03-20 2015-10-22 株式会社神戸製鋼所 Cooling apparatus cooling sintered ore and pellet and exhaust control method in the cooling apparatus
CN104006403A (en) * 2014-05-29 2014-08-27 马钢(集团)控股有限公司 Gas diluting device and gas diluting method
CN105202918A (en) * 2014-06-29 2015-12-30 上海梅山钢铁股份有限公司 Sintering blowing type annular cooler ore removal temperature control device and method

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