JPH0699687B2 - How to enter the boiler section of coke dry fire extinguishing equipment - Google Patents

How to enter the boiler section of coke dry fire extinguishing equipment

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Publication number
JPH0699687B2
JPH0699687B2 JP22721386A JP22721386A JPH0699687B2 JP H0699687 B2 JPH0699687 B2 JP H0699687B2 JP 22721386 A JP22721386 A JP 22721386A JP 22721386 A JP22721386 A JP 22721386A JP H0699687 B2 JPH0699687 B2 JP H0699687B2
Authority
JP
Japan
Prior art keywords
gas
boiler
coke
fire extinguisher
boiler section
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 - Lifetime
Application number
JP22721386A
Other languages
Japanese (ja)
Other versions
JPS6383194A (en
Inventor
裕 桑名
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.)
Nippon Steel Corp
Original Assignee
Nippon 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP22721386A priority Critical patent/JPH0699687B2/en
Publication of JPS6383194A publication Critical patent/JPS6383194A/en
Publication of JPH0699687B2 publication Critical patent/JPH0699687B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、コークス乾式消火設備(以下COQ設備と略
す)のボイラー部立ちり方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for standing a boiler portion of coke dry fire extinguishing equipment (hereinafter abbreviated as COQ equipment).

(従来の技術) 従来、定常操業中のCDQ設備のボイラー部に立ち入って
点検又は修理を行うにはCDQ設備の消火塔内に充填され
ている高温コークスを完全に排出後、循環ガスブロワー
運転状態で冷却ガス循環系内に冷却ガス(循環系内の循
環ガスが高温の時は不活性ガス、例えばN2ガス、循環系
内の循環ガスが低温となった時は空気)を導入し、冷却
ガス循環系内より循環ガスを排出して消火塔及びボイラ
ー部を常温まで冷却する。このような消火塔及びボイラ
ー部の常温までの冷却は、消火塔の内張り耐火物の損傷
を防止するため低冷却速度で冷却しなければならず、冷
却ガス循環系内に冷却ガスを導入後、消火塔及びボイラ
ー部を常温まで冷却するのに3日程度必要である。
(Prior art) Conventionally, in order to enter the boiler section of the CDQ equipment during steady operation for inspection or repair, the hot gas coke filled in the fire extinguisher of the CDQ equipment is completely discharged, and then the circulating gas blower is in operation. Cooling gas is introduced into the cooling gas circulation system (inert gas such as N 2 gas when the circulation gas in the circulation system is high temperature, air when the circulation gas in the circulation system becomes low temperature) and cooled. Circulating gas is discharged from the gas circulation system to cool the fire extinguisher tower and the boiler to room temperature. Such cooling of the fire tower and the boiler part to room temperature must be cooled at a low cooling rate to prevent damage to the refractory lining the fire tower, after introducing the cooling gas into the cooling gas circulation system, It takes about 3 days to cool the fire extinguisher and the boiler to room temperature.

またボイラー部に立ち入って点検又は修理完了後、CDQ
設備を定常操業に復帰させるのにも、消火塔内が常温ま
で冷却されており、しかも消火塔の内張り耐火物の損傷
を防止するため低昇温速度で昇温しなければならず、3
日程度必要である。
Also, after entering the boiler section and completing inspection or repair, CDQ
Even when the equipment is returned to normal operation, the inside of the fire extinguisher must be cooled to room temperature, and the temperature must be raised at a low heating rate in order to prevent damage to the refractory lining the fire extinguisher.
It takes about a day.

(発明が解決しようとする問題点) 本発明は、消火塔内に高温コークスを充填したまま短時
間でボイラー部を冷却でき、消火塔内に高温コークスを
充填したままボイラー部を安全に点検又は修理できると
共にボイラー部の点検又は修理完了後、短時間でCDQ設
備を定常操業に復帰することができるCDQ設備のボイラ
ー部立ち入り方法を提供するものである。
(Problems to be Solved by the Invention) The present invention is capable of cooling a boiler part in a short time while the high-temperature coke is filled in the fire extinguisher, and safely inspecting the boiler part while the high-temperature coke is filled in the fire extinguisher or (EN) A method of entering a boiler section of a CDQ facility that can be repaired and at the same time, after the inspection or repair of the boiler section is completed, the CDQ facility can be returned to normal operation.

(問題点を解決するための手段) 本発明の要旨は次の通りである。(Means for Solving Problems) The gist of the present invention is as follows.

(1) コークス消火設備の消火塔に高温コークスを充
填したまま循環ガスブロワーを停止し、消火塔からボイ
ラー部への循環ガスダクトの除塵器より下流に設けた緊
急ガス放散弁を開くと共に消火塔内及びボイラー部内に
不活性ガスを導入して未燃ガスを上記緊急ガス放散弁を
介して放散し、消火塔からボイラー部への循環ガスダク
トに設置されたダスト切出装置を有する除塵器内へ耐熱
性粉粒体を装入し除塵器内の循環ガス衝突体を埋設して
除塵器の消火塔からボイラー部へのガス通路を遮断し、
消火塔の炉頂ガス放散弁の弁開度を調整して消火塔内圧
を調整しながらボイラー部への不活性ガスの導入を停止
し冷却ガスを導入しボイラー部を冷却してボイラー部に
立ち入ることを特徴とするコークス乾式消火設備のボイ
ラー部立ち入り方法。
(1) Stop the circulating gas blower while the high temperature coke is filled in the fire extinguisher of the coke extinguishing equipment, and open the emergency gas diffusion valve located downstream from the dust remover of the circulating gas duct from the fire extinguisher to the boiler section and also inside the fire extinguisher. Also, an inert gas is introduced into the boiler section to disperse unburned gas through the emergency gas diffusion valve, and heat resistance is applied to the dust remover that has a dust cutting device installed in the circulating gas duct from the fire extinguisher tower to the boiler section. Of the powdery granular material and burying the circulating gas collision body in the dust remover to cut off the gas passage from the fire extinguisher tower of the dust remover to the boiler part,
Adjusting the valve opening of the top gas diffusion valve of the fire extinguisher to adjust the internal pressure of the fire extinguisher while stopping the introduction of the inert gas into the boiler section and introducing the cooling gas to cool the boiler section and enter the boiler section. A method for entering the boiler section of a coke dry fire extinguisher, which is characterized in that

(2) 除塵器内へ投入する耐熱性粉粒体が、コークス
乾式消火設備から回収した粉コークスであることを特徴
とする上記(1)項記載のコークス乾式消火設備のボイラ
ー部立ち入り方法。
(2) The method for entering the boiler part of the coke dry fire extinguisher equipment as described in the above item (1), wherein the heat-resistant powder and granules thrown into the dust remover is powder coke recovered from the coke dry fire extinguishing equipment.

(実施例・作用) 以下本発明について実施例に基づき詳細に説明する。(Examples / Operations) The present invention will be described in detail below based on examples.

第1図に示すように定常操業中の消火塔1内に高温コー
クス2が充填されたまた循環ガスブロワー3を停止する
と共に弁17を全閉する。これに連動して緊急ガス放散弁
4を開き、不活性ガス例えばN2ガスを弁18及び19を介し
て消火塔1内及びボイラー部5内へ導入する。これによ
りガス循環系内の未燃ガスが緊急ガス放散弁4より燃焼
放散される。
As shown in FIG. 1, the high temperature coke 2 is filled in the fire extinguisher 1 during steady operation, the circulating gas blower 3 is stopped, and the valve 17 is fully closed. In conjunction with this, the emergency gas diffusion valve 4 is opened, and an inert gas such as N 2 gas is introduced into the fire extinguishing tower 1 and the boiler section 5 through the valves 18 and 19. As a result, the unburned gas in the gas circulation system is burned and diffused by the emergency gas diffusion valve 4.

緊急ガス放散弁4より放散されるガスの燃焼がおさまる
と、圧力測定孔6,6を開き、そこから1次集塵器7及び
又は2次集塵器8で捕捉されダスト切出装置9及び10で
排出され回収された粉コークスを1次集塵器7内に装入
し、1次集塵器7内の循環ガス衝突板11を、第2図に示
すように例えば30cm程度、粉コークス12で埋設する。
When the combustion of the gas emitted from the emergency gas emission valve 4 has subsided, the pressure measurement holes 6 and 6 are opened, from which the primary dust collector 7 and / or the secondary dust collector 8 captures the dust cutting device 9 and The dust coke discharged and collected at 10 is charged into the primary dust collector 7, and the circulating gas collision plate 11 in the primary dust collector 7 is, for example, about 30 cm as shown in FIG. Buried at 12.

このように1次集塵器7内の循環ガス通路13を粉コーク
ス12で遮断した後、炉頂ガス放散弁14の弁開度を調節し
て消火塔1内圧を0〜5mmAq程度に制御する。
After the circulating gas passage 13 in the primary dust collector 7 is blocked by the powder coke 12 in this way, the valve opening of the furnace top gas diffusion valve 14 is adjusted to control the internal pressure of the fire extinguisher 1 to about 0 to 5 mmAq. .

これにより消火塔1内への空気の侵入が有効に防止され
消火塔1内に充填されている高温コークス2の燃焼によ
るコークス同志の溶着、コークスと消火塔1の内張り耐
火物との溶着を防止される。
This effectively prevents the invasion of air into the fire extinguisher 1 and prevents the welding of the coke and the refractory lining of the fire extinguisher 1 due to the combustion of the high temperature coke 2 filled in the fire extinguisher 1. To be done.

なお未乾留ガスの発生があるため、板に消火塔1内への
N2ガス導入を停止しても炉頂ガス放散弁14の弁開度調節
にて消火塔1内圧を0〜5mmAq程度に制御できる。
In addition, there is the generation of undistilled gas,
Even if the introduction of N 2 gas is stopped, the internal pressure of the fire extinguisher 1 can be controlled to about 0 to 5 mmAq by adjusting the valve opening of the furnace top gas diffusion valve 14.

一方、1次集塵器7内の循環ガス通路13を粉コークス12
で遮断した後、ボイラー部5内へのN2ガス導入を停止
し、ボイラー部5の高さ方向に設けられたマンホール15
群を下から順番に解放して、ボイラー部5内へ空気を導
入しボイラー部5内を冷却した冷却空気を緊急ガス放散
弁4を介して放散してボイラー部5を冷却する。
On the other hand, the circulating gas passage 13 in the primary dust collector 7 is connected to the powder coke 12
After shutting off with N, the introduction of N 2 gas into the boiler part 5 was stopped, and the manhole 15 provided in the height direction of the boiler part 5
The groups are released in order from the bottom, air is introduced into the boiler unit 5, and the cooling air that has cooled the inside of the boiler unit 5 is diffused through the emergency gas diffusion valve 4 to cool the boiler unit 5.

このようにボイラー部5の冷却時、高温コークス2が充
填された消火塔1内圧が正圧に制御され、緊急ガス放散
弁4が開いているが、1次集塵器7内の循環ガス通路13
を粉コークス12で遮断しているので、消火塔1内の高温
ガスのボイラー部5及び1次集塵器7より下流側の循環
ダクト16部への流入並びに緊急ガス放散弁4からの流出
が防止される。このためボイラー部5及び1次集塵器7
より下流側の循環ダクト16部は上記空気導入により速や
かに冷却され、空気導入から1日程度で常温まで冷却で
きる。
In this way, when the boiler part 5 is cooled, the internal pressure of the fire extinguisher 1 filled with the high temperature coke 2 is controlled to be a positive pressure, and the emergency gas diffusion valve 4 is opened, but the circulating gas passage in the primary dust collector 7 is closed. 13
Since the powder coke 12 is shut off, the hot gas in the fire extinguishing tower 1 is prevented from flowing into the circulation duct 16 part on the downstream side of the boiler part 5 and the primary dust collector 7 and the outflow from the emergency gas diffusion valve 4. To be prevented. Therefore, the boiler part 5 and the primary dust collector 7
The circulation duct 16 on the further downstream side is quickly cooled by the air introduction, and can be cooled to room temperature in about one day after the air introduction.

ボイラー部5が常温まで冷却されると、ボイラー部5に
マンホール15より作業者がボイラー部5内に立ち入って
ボイラー部5の炉体煉瓦、ボイラーチューブ等を点検又
は修理する。この時、高温コークス2が充填された消火
塔1内圧が正圧に制御されているが、1次集塵器7内の
循環ガス通路13を粉コークス12で遮断しているので消火
塔1内の高温ガスのボイラー部5への流入が有効に防止
され、安全に点検又は修理を行うことができる。
When the boiler part 5 is cooled to room temperature, an operator enters the boiler part 5 through the manhole 15 and inspects or repairs the furnace bricks, the boiler tubes, etc. of the boiler part 5. At this time, the internal pressure of the fire extinguisher 1 filled with the high temperature coke 2 is controlled to be a positive pressure. However, since the circulating gas passage 13 in the primary dust collector 7 is blocked by the coke 12 of powder, the inside of the fire extinguisher 1 is closed. Inflow of high temperature gas into the boiler section 5 is effectively prevented, and inspection or repair can be performed safely.

ボイラー部5の点検又は修理完了後は、例えばマンホー
ル15群を閉じ、ボイラー部5へN2ガスを導入して緊急ガ
ス放散弁4より排出してボイラー部5内をN2ガスに置換
し、ダスト切出装置9により1次集塵器7内の粉コーク
ス12を排出して1次集塵器7内の循環ガス通路13を開通
し、緊急ガス放散弁4及び炉頂ガス放散弁14を全閉後、
循環ガスブロワー3を起動させて、操業を開始する。
After the inspection or repair of the boiler part 5 is completed, for example, the manhole 15 group is closed, N 2 gas is introduced into the boiler part 5, and the gas is discharged from the emergency gas diffusion valve 4 to replace the inside of the boiler part 5 with N 2 gas, The dust cutting device 9 discharges the powder coke 12 in the primary dust collector 7 to open the circulation gas passage 13 in the primary dust collector 7, and to open the emergency gas diffusion valve 4 and the furnace top gas diffusion valve 14. After fully closed,
The circulating gas blower 3 is activated to start the operation.

なお、未乾留ガスの発生を利用して消火塔1内へのN2
ス導入を停止し、炉頂ガス放散弁14の弁開度調節にて消
火塔1内圧を0〜5mmAq程度に制御している時は、上記
ボイラー部5内へN2ガスを導入と同時に消火塔1内へN2
ガスを導入する。
The introduction of N 2 gas into the fire extinguisher 1 is stopped by utilizing the non-distilled gas, and the internal pressure of the fire extinguisher 1 is controlled to about 0 to 5 mmAq by adjusting the valve opening of the furnace top gas diffusion valve 14. and time and is, N 2 into the boiler section introducing N 2 gas into the 5 same time extinguishing tower 1
Introduce gas.

循環ガスブロワー3の停止からボイラー部5の点検又は
修理完了の循環ガスブロワー3の再起動まで、消火塔1
内に高温コークス2を充填したままであるので消火塔1
の内張り耐火物は高温のままであり、しかも消火塔1内
圧を正圧に制御して、消火塔1内への空気の侵入を有効
に防止し、消火塔1内に充填されている高温コークス2
の燃焼によりコークス同志の溶着、コークスと消火塔1
の内張り耐火物との溶着を防止しているので、循環ブロ
ワー3再起動後、2〜3時間で定常操業に復帰できる。
なおボイラー部5の点検又は修理完了後、定常操業に復
帰するまでの所要時間は、4〜5時間程度である。
From the stop of the circulating gas blower 3 to the restart of the circulating gas blower 3 after the inspection or repair of the boiler section 5 is completed, the fire extinguisher 1
Fire extinguisher 1 because it is still filled with high temperature coke 2
The refractory lined inside the fire extinguishing tower 1 remains at a high temperature, and the internal pressure of the fire extinguishing tower 1 is controlled to be a positive pressure to effectively prevent air from entering the extinguishing tower 1 and the high temperature coke filled in the fire extinguishing tower 1 Two
Burning of coke, welding of cokes, coke and fire extinguisher 1
Since it is prevented from being welded to the refractory lining, it is possible to return to the normal operation in 2 to 3 hours after restarting the circulation blower 3.
After the inspection or repair of the boiler unit 5 is completed, the time required to return to the normal operation is about 4 to 5 hours.

以上の実施例では、耐熱性粉粒体として容易に入手でき
るCDQ設備の1次除塵器7及び又は2次除塵器8で捕捉
され排出され回収された粉コークスを使用しているが、
ボイラー部5下部に堆積した粉コークスを回収したもの
や上記粉コークスと同程度の粒子径を有する耐熱性粉粒
体、例えばセラミックビーズ、石灰粉等を使用すること
ができる。
In the above examples, the powder coke captured and discharged and collected by the primary dust remover 7 and / or the secondary dust remover 8 of the CDQ facility, which is easily available as a heat-resistant powder, is used.
What collect | recovered the powder coke accumulated in the lower part of the boiler part 5, or a heat-resistant powder granular material which has a particle size of the said powder coke, for example, a ceramic bead, a lime powder, etc. can be used.

また板状の循環ガス衝突体、即ち循環ガス衝突板11を内
設した除塵器7を配備したCDQ設備についての説明をし
たが、例えば実開昭59-47637号公報、実開昭59-133644
号公報等に開示される縦スリット状、ハニカム状の循環
ガス衝突体等を内設した除塵器を配備したCDQ設備に対
しても実施できる。
Further, the CDQ equipment provided with the plate-shaped circulating gas collision body, that is, the dust remover 7 having the circulating gas collision plate 11 installed therein has been described, for example, Japanese Utility Model Publication No. 59-47637 and Japanese Utility Model Publication No. 59-133644.
The present invention can also be applied to a CDQ facility equipped with a dust remover having a vertical slit-shaped or honeycomb-shaped circulating gas collision body disclosed therein and the like.

(発明の効果) 以上詳述したように本発明のCDQ設備のボイラー部立ち
入り方法によれば、消火塔内に高温コークスを充填した
まま短時間でボイラー部を冷却でき、消火塔内に高温コ
ークス充填したままボイラー部を安全に点検又は修理で
きると共にボイラー部の点検又は修理完了後、短時間で
CDQ設備を定常操業に復帰することができる。
(Effects of the Invention) As described in detail above, according to the boiler part entry method of the CDQ equipment of the present invention, the boiler part can be cooled in a short time while the high temperature coke is filled in the fire extinguishing tower, and the high temperature coke in the fire extinguishing tower. The boiler section can be safely inspected or repaired while it is filled, and it can be done within a short time after inspection or repair of the boiler section is completed.
CDQ equipment can be returned to normal operation.

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

第1図及び第2図は、本発明のコークス乾式消火設備の
ボイラー部立ち入り方法の説明図である。 1:消火塔、2:高温コークス 3:循環ガスブロワー、4:緊急ガス放散弁 5:ボイラー部、7:集塵器 9:ダスト切出装置、11:循環ガス衝突板 12:粉コークス、13:集塵器のガス通路 14:炉頂ガス放散弁、16:循環ガスダクト
FIG. 1 and FIG. 2 are explanatory views of the method for entering the boiler section of the coke dry fire extinguishing equipment of the present invention. 1: Fire extinguisher, 2: High temperature coke 3: Circulating gas blower, 4: Emergency gas diffusion valve 5: Boiler part, 7: Dust collector 9: Dust cutting device, 11: Circulating gas collision plate 12: Powder coke, 13 : Dust collector gas passage 14: Furnace top gas diffusion valve, 16: Circulating gas duct

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】コークス消火設備の消火塔に高温コークス
を充填したまま循環ガスブロワーを停止し、消火塔から
ボイラー部への循環ガスダクトの除塵器より下流に設け
た緊急ガス放散弁を開くと共に消火塔内及びボイラー部
内に不活性ガスを導入して未燃ガスを上記緊急ガス放散
弁を介して放散し、消火塔からボイラー部への循環ガス
ダクトに設置されたダスト切出装置を有する除塵器内へ
耐熱性粉粒体を装入し除塵器内の循環ガス衝突体を埋設
して除塵器の消火塔からボイラー部へのガス通路を遮断
し、消火塔の炉頂ガス放散弁の弁開度を調整して消火塔
内圧を調整しながらボイラー部への不活性ガスの導入を
停止し冷却ガスを導入しボイラー部を冷却してボイラー
部に立ち入ることを特徴とするコークス乾式消火設備の
ボイラー部立ち入り方法。
1. A fire extinguisher of a coke extinguishing equipment is stopped with a circulating gas blower filled with high temperature coke, and an emergency gas diffusion valve provided downstream from a dust remover of a circulating gas duct from the extinguishing tower to the boiler is opened and the fire is extinguished. In a dust remover with a dust cutting device installed in the circulating gas duct from the fire extinguisher tower to the boiler section by introducing an inert gas into the tower and the boiler section to diffuse unburned gas through the emergency gas diffusion valve. Heat-resistant powder is charged into the dust remover and the circulating gas collision body is embedded in the dust remover to shut off the gas passage from the fire extinguisher tower to the boiler section. By adjusting the internal pressure of the fire extinguisher to stop the introduction of inert gas into the boiler section and introducing cooling gas to cool the boiler section and enter the boiler section. On-site Method.
【請求項2】除塵器内へ投入する耐熱性粉粒体が、コー
クス乾式消火設備から回収した粉コークスであることを
特徴とする特許請求の範囲第1項記載のコークス乾式消
火設備のボイラー部立ち入り方法。
2. The boiler part of the coke dry fire extinguishing equipment according to claim 1, wherein the heat resistant powder and granules to be put into the dust remover is powder coke recovered from the coke dry extinguishing equipment. How to get in.
JP22721386A 1986-09-26 1986-09-26 How to enter the boiler section of coke dry fire extinguishing equipment Expired - Lifetime JPH0699687B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22721386A JPH0699687B2 (en) 1986-09-26 1986-09-26 How to enter the boiler section of coke dry fire extinguishing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22721386A JPH0699687B2 (en) 1986-09-26 1986-09-26 How to enter the boiler section of coke dry fire extinguishing equipment

Publications (2)

Publication Number Publication Date
JPS6383194A JPS6383194A (en) 1988-04-13
JPH0699687B2 true JPH0699687B2 (en) 1994-12-07

Family

ID=16857265

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22721386A Expired - Lifetime JPH0699687B2 (en) 1986-09-26 1986-09-26 How to enter the boiler section of coke dry fire extinguishing equipment

Country Status (1)

Country Link
JP (1) JPH0699687B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108587656B (en) * 2018-07-03 2023-12-22 山东钢铁股份有限公司 Dry quenching circulating system and nitrogen charging replacement process

Also Published As

Publication number Publication date
JPS6383194A (en) 1988-04-13

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