JP2004075743A - Cdq gas-circulating method and system therefor - Google Patents

Cdq gas-circulating method and system therefor Download PDF

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Publication number
JP2004075743A
JP2004075743A JP2002234824A JP2002234824A JP2004075743A JP 2004075743 A JP2004075743 A JP 2004075743A JP 2002234824 A JP2002234824 A JP 2002234824A JP 2002234824 A JP2002234824 A JP 2002234824A JP 2004075743 A JP2004075743 A JP 2004075743A
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Japan
Prior art keywords
cdq
steam
inert gas
boiler
main body
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JP3896052B2 (en
Inventor
Yukimasa Tanaka
田中 幸政
Hitoshi Aritaka
有高 均
Naoto Igawa
井川 直人
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Nippon Steel Corp
Nippon Steel Plant Designing Corp
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Nittetsu Plant Designing Corp
Nippon Steel Corp
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Priority to JP2002234824A priority Critical patent/JP3896052B2/en
Priority to AU2003246266A priority patent/AU2003246266A1/en
Priority to PCT/JP2003/008502 priority patent/WO2004016713A1/en
Priority to CN03819273.XA priority patent/CN1675334B/en
Priority to BRPI0313328-1B1A priority patent/BR0313328B1/en
Priority to TW92119043A priority patent/TWI227730B/en
Publication of JP2004075743A publication Critical patent/JP2004075743A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00Cooling or quenching coke
    • C10B39/02Dry cooling outside the oven

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a coke dry quencher (CDQ) gas-circulating method, by which CDQ can be started up with a circulation blower driven with a steam turbine used in a steady-state operation without using an electrically driven small circulation blower, when CDQ is started up, and to provide a gas circulation system having a simplified installation. <P>SOLUTION: This CDQ gas-circulating method comprising subjecting red heat coke charged in a CDQ main body 1 and an inert gas charged from the lower portion of the CDQ main body 1 to a heat exchange treatment, recovering the sensible heat of the inert gas in a boiler 4 after the heat exchange treatment, again charging and circulating the cooled inert gas into the CDQ main body 1 with a circulation blower 5 is characterized by using steam as a driving source for driving the circulation blower 5, introducing the steam from a separately disposed steam supply source 18, when CDQ is started up, and introducing the steam from a bypass pipe 17 branched from a steam pipe 13 from the boiler 4, when the start-up of the CDQ is finished. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明が属する技術分野】
本発明は、コークス乾式消火設備(Coke Dry Quencher 本明細書ではCDQという)の循環ガスの循環システムにおいて、循環ブロワの駆動源として、ボイラにて発生する蒸気と蒸気供給源から供給される蒸気を切り替えて使用する、蒸気駆動によるCDQの循環送風方法およびそのシステムに関する。
【0002】
【従来の技術】
CDQでは、赤熱コークスをCDQ本体のプレチャンバーに装入し冷却室に下降させ、冷却室内へ供給した冷却ガスである不活性ガスを赤熱コークスと熱交換させ、赤熱コークスの熱を回収した高温の不活性ガスをボイラーに導入して熱交換した後、循環ブロワで再度冷却室へ圧送して循環させるようなっている。ボイラーで熱交換により得られた蒸気は発電機に送られ電気エネルギーとして回収される。
【0003】
不活性ガスを圧送する循環ブロワを駆動させるために、例えば、特開昭57−190079号公報に記載されているように、ボイラーで発生する蒸気の一部を利用した蒸気タービンが利用されている。立ち上げ時には、蒸気タービンを駆動する蒸気が得られないので、別途設けた小型モーターで駆動する電気駆動式小型循環ブロワにより送風し、蒸気が所定量発生するようになると循環ブロワを蒸気タービンで駆動して運転する。
【0004】
【発明が解決しようとする課題】
しかしながら、蒸気タービンで駆動する循環ブロワを採用する場合、立ち上げ時に蒸気が所定量発生するまでは、電気駆動式小型循環ブロワで不活性ガスを圧送する設備が必要となり、システムが複雑となる問題があった。
【0005】
そこで、本発明が解決しようとする課題は、立ち上げ時に電気駆動式小型循環ブロワを使用することなく、定常運転で使用する、蒸気タービン駆動の循環ブロワにより立ち上げることができるCDQの循環送風方法及び設備が簡素化された循環送風システムを提供することにある。
【0006】
【課題を解決するための手段】
本発明のCDQの循環送風方法は、CDQ本体に装入された赤熱コークスと前記CDQ本体の下方から導入される不活性ガスとを熱交換して、熱交換後の不活性ガスの顕熱をボイラで回収するとともに、ボイラの顕熱回収により冷却された不活性ガスを循環ブロワにより再度CDQ本体へ導入して循環させるCDQの循環送風方法において、前記循環ブロワを駆動する駆動源を蒸気とし、CDQの立ち上げ時には蒸気を別途設けた蒸気供給源から導入し、CDQの立ち上げ完了後は蒸気をボイラからの蒸気管に設けたバイパス管から導入することを特徴とする。
【0007】
また、本発明のCDQの循環送風システムは、CDQ本体に装入された赤熱コークスと前記CDQ本体の下方から導入される不活性ガスとを熱交換して、熱交換後の不活性ガスの顕熱をボイラで回収するとともに、ボイラの顕熱回収により冷却された不活性ガスを循環ブロワにより再度CDQ本体へ導入して循環させるCDQの循環送風システムにおいて、循環ブロワ駆動用の蒸気タービンに蒸気を供給するバイパス管を前記ボイラからの蒸気管から分岐させ、かつ別途設けた蒸気供給源から蒸気を供給する蒸気供給管を前記蒸気管に接続したことを特徴とする。
【0008】
【発明実施の形態】
図1は本発明のCDQの循環送風システムの一例を示すフロー図である。赤熱コークスを装入して冷却ガスである不活性ガスと熱交換して冷却するCDQ本体1の上部は、除塵器2を備えた排気ダクト3によりボイラ4に接続されている。さらにボイラ4は循環ブロワ5を介して循環ダクト6,7によりCDQ本体1の下部に接続されている。この接続によりCDQ本体1内で赤熱コークスと熱交換された高温の不活性ガスはCDQ本体1から排気され、排気ダクト2を経てボイラ4に導入されて熱交換により冷却されて循環ブロワ5により循環ダクト6,7を経てCDQ本体1に導入される、不活性ガス循環経路が形成される。
【0009】
ボイラ4には伝熱管8が設けられ、伝熱管8にはタンク9に接続された送水管10,11から送水ポンプ12により水が供給される。伝熱管8に流入した水は、CDQ本体1から排出してボイラ4に導入された高温の不活性ガスにより熱交換されて蒸気となり、蒸気は伝熱管8に接続された蒸気管13を経て発電設備14に送られ、発電設備14を出た蒸気は復水器15で復水されてタンク9に流入する。
【0010】
循環ブロワ5は、蒸気タービン16により駆動させる。蒸気タービン16は、蒸気管13から分岐させたバイパス管17を経て供給される蒸気によって駆動させる。
【0011】
蒸気管13には、CDQ本体1の立ち上げ時に循環ブロワ5を駆動させる蒸気タービン16に蒸気を供給するため、別の蒸気供給源18に開閉弁19を備えた蒸気供給管20が接続されている。蒸気供給管20は蒸気供給源18からバイパス管17に蒸気を供給するために、蒸気管13のボイラ4側に設けられた切替弁21と発電設備14側に設けられた遮断弁22との間に接続する。また、蒸気管13には切替弁21とボイラ4側の間に、蒸気を放散するため、放散弁23を備えた放散管24を接続する。
【0012】
循環ブロワ5を駆動する蒸気タービン16を出た低圧の蒸気は、低圧蒸気管25により原料乾燥装置26に送って原料の乾燥に利用され冷却されて水となり、水はタンク9に戻される。
【0013】
次に本発明のCDQの操業について説明する。CDQの立ち上げ時には、蒸気管13の切替弁21と遮断弁22を閉にし、放散弁23を開にする。その後、蒸気供給管20の開閉弁19を開にすると、蒸気供給源18から蒸気が蒸気供給管20、蒸気管13、バイパス管17を通って蒸気タービン16を駆動し、蒸気タービン16を出た低圧の蒸気は冷却されて水となってタンク9に戻され、タンク9から送水管10,11を経て伝熱管8に導入された水は蒸気となって蒸気管13を経て放散管24から放散される。
【0014】
こうして立ち上げ時には、蒸気供給源18からの蒸気の供給により蒸気タービン16を駆動して循環ブロワ5を回転させることにより不活性ガスがCDQ本体1に送り込まれ、赤熱コークスと熱交換された不活性ガスはCDQ本体1から排気され、排気ダクト3を経てボイラ4に導入されて熱交換により冷却されて循環ブロワ5により循環ダクト6,7を経てCDQ本体1に導入される。 図2は蒸気上昇温度と時間の関係を示すグラフである。循環ブロワにより不活性ガスが不活性ガス循環経路の循環を重ねていくにつれて、不活性ガスの温度が上昇し、図2のグラフが示すように、蒸気温度も時間とともに上昇し、不活性ガスの温度が約800℃になると、伝熱管8から発生する蒸気温度が上昇し、蒸気タービン16および発電設備14に必要な蒸気量が発生する。この時点で、蒸気管13の切替弁21と遮断弁22を開にし、放散弁23を閉にし、蒸気供給管20の開閉弁19を閉にすると、伝熱管8の蒸気は、蒸気管13を通って発電設備14に流れ、一部がバイパス管17を通って蒸気タービン16を駆動させ、循環ブロワ5を回転させて不活性ガスを循環させる。
【0015】
【発明の効果】
立ち上げ時と立ち上げ完了後の定常運転時の循環ブロワを1台共用とするので、立ち上げ専用の循環ブロワが不要となり、従来に比べて設備が簡素化される。
【図面の簡単な説明】
【図1】本発明のCDQの循環送風システムの一例を示すフロー図である。
【図2】蒸気上昇温度と時間の関係を示すグラフである。
【符号の説明】
1 CDQ本体
2 除塵器
3 排気ダクト
4 ボイラ
5 循環ブロワ
6,7 循環ダクト
8 伝熱管
9 タンク
10,11 送水管
12 送水ポンプ
13 蒸気管
14 発電設備
15 復水器
16 蒸気タービン
17 バイパス管
18 蒸気供給源
19 開閉弁
20 蒸気供給管
21 切替弁
22 遮断弁
23 放散弁
24 放散管
25 低圧蒸気管
26 原料乾燥装置
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a circulating gas circulation system of a coke dry quencher (herein, referred to as CDQ), which uses steam generated by a boiler and steam supplied from a steam supply source as a driving source of a circulating blower. The present invention relates to a steam-driven CDQ circulating air blowing method and a system thereof that are switched and used.
[0002]
[Prior art]
In the CDQ, red hot coke is charged into the pre-chamber of the CDQ main body, lowered into the cooling chamber, and an inert gas, which is a cooling gas supplied to the cooling chamber, exchanges heat with the red hot coke to recover the heat of the red hot coke. After introducing an inert gas into the boiler and exchanging heat, the circulation gas is sent again to the cooling chamber by a circulation blower and circulated. The steam obtained by heat exchange in the boiler is sent to a generator and collected as electric energy.
[0003]
In order to drive a circulating blower for pumping an inert gas, for example, a steam turbine utilizing a part of steam generated in a boiler is used as described in JP-A-57-190079. . At the time of startup, steam for driving the steam turbine is not obtained, so it is blown by an electrically driven small circulation blower driven by a separately provided small motor, and when a predetermined amount of steam is generated, the circulation blower is driven by the steam turbine And drive.
[0004]
[Problems to be solved by the invention]
However, when a circulation blower driven by a steam turbine is employed, a facility for pumping inert gas with an electrically driven small circulation blower is required until a predetermined amount of steam is generated at startup, which complicates the system. was there.
[0005]
Therefore, the problem to be solved by the present invention is to provide a method for circulating CDQ that can be started by a steam turbine driven circulating blower used in a steady operation without using an electrically driven small circulating blower at startup. Another object of the present invention is to provide a circulation ventilation system with simplified equipment.
[0006]
[Means for Solving the Problems]
The method for circulating and blowing CDQ of the present invention exchanges heat between red hot coke charged in a CDQ main body and an inert gas introduced from below the CDQ main body to reduce the sensible heat of the inert gas after the heat exchange. In the method of circulating the CDQ, in which the inert gas cooled by the sensible heat recovery of the boiler is introduced into the CDQ body again by the circulating blower and circulated, the driving source for driving the circulating blower is steam, When the CDQ is started, steam is introduced from a separately provided steam supply source, and after completion of the CDQ, steam is introduced from a bypass pipe provided in a steam pipe from the boiler.
[0007]
In addition, the CDQ circulation ventilation system of the present invention exchanges heat between the glow coke charged into the CDQ main body and the inert gas introduced from below the CDQ main body, and expresses the inert gas after the heat exchange. In a CDQ circulating air blowing system in which heat is recovered by a boiler and the inert gas cooled by the sensible heat recovery of the boiler is again introduced into the CDQ body by a circulating blower and circulated, steam is supplied to a steam turbine for driving a circulating blower. A bypass pipe to be supplied is branched from a steam pipe from the boiler, and a steam supply pipe to supply steam from a separately provided steam supply source is connected to the steam pipe.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a flow chart showing an example of the CDQ circulation air blowing system of the present invention. The upper part of the CDQ main body 1 which cools by charging red hot coke and exchanging heat with an inert gas as a cooling gas is connected to a boiler 4 by an exhaust duct 3 provided with a dust remover 2. Further, the boiler 4 is connected to a lower portion of the CDQ main body 1 by circulation ducts 6 and 7 via a circulation blower 5. By this connection, the high-temperature inert gas heat-exchanged with the red hot coke in the CDQ main body 1 is exhausted from the CDQ main body 1, introduced into the boiler 4 through the exhaust duct 2, cooled by heat exchange, and circulated by the circulation blower 5. An inert gas circulation path, which is introduced into the CDQ main body 1 through the ducts 6 and 7, is formed.
[0009]
A heat transfer tube 8 is provided in the boiler 4, and water is supplied to the heat transfer tube 8 from water supply tubes 10 and 11 connected to a tank 9 by a water supply pump 12. The water that has flowed into the heat transfer tube 8 is discharged from the CDQ main body 1 and heat-exchanged by the high-temperature inert gas introduced into the boiler 4 to become steam, and the steam is generated through the steam pipe 13 connected to the heat transfer tube 8. The steam sent to the facility 14 and leaving the power generation facility 14 is condensed by the condenser 15 and flows into the tank 9.
[0010]
The circulation blower 5 is driven by a steam turbine 16. The steam turbine 16 is driven by steam supplied through a bypass pipe 17 branched from the steam pipe 13.
[0011]
A steam supply pipe 20 having an on-off valve 19 connected to another steam supply source 18 is connected to the steam pipe 13 to supply steam to a steam turbine 16 that drives the circulation blower 5 when the CDQ main body 1 is started up. I have. The steam supply pipe 20 is provided between a switching valve 21 provided on the boiler 4 side of the steam pipe 13 and a shutoff valve 22 provided on the power generation facility 14 side to supply steam from the steam supply source 18 to the bypass pipe 17. Connect to In addition, a radiation pipe 24 provided with a radiation valve 23 is connected to the steam pipe 13 between the switching valve 21 and the boiler 4 side in order to diffuse steam.
[0012]
The low-pressure steam that has exited the steam turbine 16 that drives the circulation blower 5 is sent to a raw material drying device 26 by a low-pressure steam pipe 25, is used for drying the raw material, is cooled and becomes water, and the water is returned to the tank 9.
[0013]
Next, the operation of the CDQ of the present invention will be described. When the CDQ is started, the switching valve 21 and the shutoff valve 22 of the steam pipe 13 are closed, and the dissipation valve 23 is opened. Thereafter, when the on-off valve 19 of the steam supply pipe 20 is opened, the steam from the steam supply source 18 drives the steam turbine 16 through the steam supply pipe 20, the steam pipe 13, and the bypass pipe 17, and exits the steam turbine 16. The low-pressure steam is cooled and returned to the tank 9 as water, and the water introduced from the tank 9 to the heat transfer tube 8 via the water supply pipes 10 and 11 is converted to steam and diffused from the diffusion pipe 24 via the steam pipe 13. Is done.
[0014]
At the time of startup, the inert gas is sent to the CDQ main body 1 by driving the steam turbine 16 by the supply of steam from the steam supply source 18 and rotating the circulation blower 5, and the inert gas is exchanged with red-hot coke. The gas is exhausted from the CDQ main body 1, introduced into the boiler 4 via the exhaust duct 3, cooled by heat exchange, and introduced into the CDQ main body 1 via the circulation ducts 6 and 7 by the circulation blower 5. FIG. 2 is a graph showing the relationship between the steam rise temperature and time. As the inert gas is circulated in the inert gas circulation path by the circulation blower, the temperature of the inert gas rises, and as shown in the graph of FIG. When the temperature reaches about 800 ° C., the temperature of the steam generated from the heat transfer tube 8 increases, and the amount of steam required for the steam turbine 16 and the power generation equipment 14 is generated. At this time, when the switching valve 21 and the shutoff valve 22 of the steam pipe 13 are opened, the dissipation valve 23 is closed, and the opening / closing valve 19 of the steam supply pipe 20 is closed, the steam of the heat transfer pipe 8 passes through the steam pipe 13. Then, the steam flows through the power generation facility 14, and a part of the steam flows through the bypass pipe 17 to drive the steam turbine 16 and rotate the circulation blower 5 to circulate the inert gas.
[0015]
【The invention's effect】
Since a single circulation blower is used during startup and during normal operation after the startup is completed, a circulation blower dedicated to startup is not required, and the equipment is simplified as compared with the related art.
[Brief description of the drawings]
FIG. 1 is a flow chart showing an example of a CDQ circulation ventilation system of the present invention.
FIG. 2 is a graph showing a relationship between a steam rising temperature and time.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 CDQ main body 2 Dust remover 3 Exhaust duct 4 Boiler 5 Circulating blower 6, 7 Circulating duct 8 Heat transfer pipe 9 Tank 10, 11 Water feed pipe 12 Water feed pump 13 Steam pipe 14 Power generation equipment 15 Condenser 16 Steam turbine 17 Bypass pipe 18 Steam Supply source 19 Open / close valve 20 Steam supply pipe 21 Switching valve 22 Shutoff valve 23 Dissipation valve 24 Dissipation pipe 25 Low-pressure steam pipe 26 Raw material drying device

Claims (2)

CDQ本体に装入された赤熱コークスと前記CDQ本体の下方から導入される不活性ガスとを熱交換して、熱交換後の不活性ガスの顕熱をボイラで回収するとともに、ボイラの顕熱回収により冷却された不活性ガスを循環ブロワにより再度CDQ本体へ導入して循環させるCDQの循環送風方法において、
前記循環ブロワを駆動する駆動源を蒸気とし、CDQの立ち上げ時には蒸気を別途設けた蒸気供給源から導入し、CDQの立ち上げ完了後は蒸気をボイラからの蒸気管から分岐させたバイパス管から導入することを特徴とするCDQの循環送風方法。
The heat exchange is performed between the red hot coke charged into the CDQ main body and the inert gas introduced from below the CDQ main body, and the sensible heat of the inert gas after the heat exchange is recovered by the boiler, and the sensible heat of the boiler is recovered. In the method of circulating and blowing CDQ, the inert gas cooled by the recovery is again introduced into the CDQ body by the circulation blower and circulated,
The drive source for driving the circulating blower is steam, and when the CDQ is started, steam is introduced from a separately provided steam supply source. After the start of the CDQ, the steam is supplied from a bypass pipe branched from a steam pipe from a boiler. A method of circulating CDQ, which is introduced.
CDQ本体に装入された赤熱コークスと前記CDQ本体の下方から導入される不活性ガスとを熱交換して、熱交換後の不活性ガスの顕熱をボイラで回収するとともに、ボイラの顕熱回収により冷却された不活性ガスを循環ブロワにより再度CDQ本体へ導入して循環させるCDQの循環送風システムにおいて、
循環ブロワ駆動用の蒸気タービンに蒸気を供給するバイパス管を前記ボイラからの蒸気管から分岐させ、かつ別途設けた蒸気供給源から蒸気を供給する蒸気供給管を前記蒸気管に接続したことを特徴とするCDQの循環送風システム。
The heat exchange is performed between the red hot coke charged into the CDQ main body and the inert gas introduced from below the CDQ main body, and the sensible heat of the inert gas after the heat exchange is recovered by the boiler, and the sensible heat of the boiler is recovered. In a CDQ circulating air blowing system in which the inert gas cooled by the recovery is introduced again into the CDQ main body by a circulation blower and circulated,
A bypass pipe for supplying steam to a steam turbine for driving a circulation blower is branched from a steam pipe from the boiler, and a steam supply pipe for supplying steam from a separately provided steam supply source is connected to the steam pipe. CDQ circulation ventilation system.
JP2002234824A 2002-08-12 2002-08-12 CDQ circulating air blowing method and system Expired - Fee Related JP3896052B2 (en)

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JP2002234824A JP3896052B2 (en) 2002-08-12 2002-08-12 CDQ circulating air blowing method and system
AU2003246266A AU2003246266A1 (en) 2002-08-12 2003-07-03 Air circulating/supplying method of cdq and its system
PCT/JP2003/008502 WO2004016713A1 (en) 2002-08-12 2003-07-03 Air circulating/supplying method of cdq and its system
CN03819273.XA CN1675334B (en) 2002-08-12 2003-07-03 Air circulating/supplying method of CDQ and its system
BRPI0313328-1B1A BR0313328B1 (en) 2002-08-12 2003-07-03 blow circulation method in a dry coke extinguisher (cdq)
TW92119043A TWI227730B (en) 2002-08-12 2003-07-11 Circularly blowing method of CDQ and system of the same

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013119587A (en) * 2011-12-07 2013-06-17 Jfe Steel Corp Method of recovering sensible heat from scorching coke
CN103696817A (en) * 2013-12-25 2014-04-02 鞍山钢铁集团公司 Power generating device and method using melting slag heat energy

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100547294C (en) * 2007-06-07 2009-10-07 江苏双良锅炉有限公司 The dry coke quenching residual heat boiler of film type wall sealing
ITGE20090060A1 (en) * 2009-07-31 2011-02-01 Martinelli Chiara Ing OVEN FOR COKE WITH DOUBLE ROTATING SOLE
CN102314184B (en) * 2010-07-09 2013-10-30 宝山钢铁股份有限公司 Temperature and pressure control method of dry quenched coke circulating system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57190079A (en) * 1981-05-20 1982-11-22 Ishikawajima Harima Heavy Ind Co Ltd Dry type quenching device for coke
JPH07242878A (en) * 1994-03-07 1995-09-19 Nkk Corp Method for operating coke dry quencher
JPH10237450A (en) * 1997-02-24 1998-09-08 Nippon Steel Corp Heat recovery apparatus of coke dry-quenching apparatus
JP3948115B2 (en) * 1998-04-21 2007-07-25 Jfeスチール株式会社 Steam turbine operation method for coke dry fire extinguishing equipment
TW591101B (en) * 1999-09-20 2004-06-11 Nippon Steel Corp Method and apparatus for dry quenching of coke

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013119587A (en) * 2011-12-07 2013-06-17 Jfe Steel Corp Method of recovering sensible heat from scorching coke
CN103696817A (en) * 2013-12-25 2014-04-02 鞍山钢铁集团公司 Power generating device and method using melting slag heat energy

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AU2003246266A8 (en) 2004-03-03
TWI227730B (en) 2005-02-11
WO2004016713A1 (en) 2004-02-26
AU2003246266A1 (en) 2004-03-03
BR0313328B1 (en) 2013-09-24
CN1675334B (en) 2012-06-27
CN1675334A (en) 2005-09-28
TW200402465A (en) 2004-02-16
JP3896052B2 (en) 2007-03-22
BR0313328A (en) 2005-06-14

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